National Emission Standards for Hazardous Air Pollutants for Source Categories; Wool Fiberglass Manufacturing

Federal RegisterJun 14, 1999

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ENVIRONMENTAL PROTECTION AGENCY

40 CFR Parts 9 and 63

[FRL-6345-3]

RIN 2060-AE75

National Emission Standards for Hazardous Air Pollutants for

Source Categories; Wool Fiberglass Manufacturing

AGENCY: Environmental Protection Agency (EPA).

ACTION: Final rule.

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SUMMARY: This action promulgates national emission standards for

hazardous air pollutants (NESHAP) for new and existing sources in wool

fiberglass manufacturing facilities. This action also adds Method 316

and Method 318 for the measurement of formaldehyde from wool fiberglass

manufacturing lines to appendix A of part 63.

The hazardous air pollutants (HAPs) emitted by the facilities

covered by this rule include compounds of three metals (arsenic,

chromium, lead) and three organic HAPs (formaldehyde, phenol, and

methanol). Exposure to these HAPs can cause reversible or irreversible

health effects including carcinogenic, respiratory, nervous system,

developmental, reproductive, and/or dermal health effects. The EPA

estimates the final rule will reduce nationwide emissions of HAPs from

these facilities by 530 megagrams per year (Mg/yr) (580 tons per year

[ton/yr]), an approximate 30 percent reduction from the current level

of emissions. In addition, the rule will achieve an estimated 760 Mg/yr

(840 ton/yr) of particulate matter (PM) reductions.

These standards implement section 112(d) of the Clean Air Act (CAA)

and are based on the Administrator's determination that wool fiberglass

manufacturing facilities may reasonably be anticipated to emit several

of the 188 HAPs listed in section 112(b) of the CAA from the various

process operations found within the industry. The final rule will

provide protection to the public by requiring all wool

[[Page 31696]]

fiberglass plants that are major sources to meet emission standards

reflecting the application of the maximum achievable control technology

(MACT).

In compliance with the Paperwork Reduction Act (PRA), this action

also amends the table that lists the Office of Management and Budget

(OMB) control numbers issued under the PRA for this rule.

A supplement to the proposed rule was proposed in the Federal

Register on February 12, 1999 (64 FR 7149). The EPA will give careful

consideration to all comments on the supplemental proposal and will

amend this final rule in a future action as appropriate.

EFFECTIVE DATE: June 14, 1999. See the SUPPLEMENTARY INFORMATION

section concerning judicial review.

ADDRESSES: Docket. The docket for this rulemaking containing the

information considered by the EPA in development of the final rule is

Docket No. A-95-24. This docket is available for public inspection

between 8 a.m. and 5:30 p.m., Monday through Friday except for Federal

holidays, at the following address: U.S. Environmental Protection

Agency, Air and Radiation Docket and Information Center (6102), 401 M

Street SW., Washington, DC 20460; telephone: (202) 260-7548. The docket

is located at the above address in Room M-1500, Waterside Mall (ground

floor). A reasonable fee may be charged for copying docket materials.

FOR FURTHER INFORMATION CONTACT: Ms. Mary Johnson, at (919) 541-5025,

Minerals and Inorganic Chemicals Group, Emission Standards Division

(MD-13), U.S. Environmental Protection Agency, Research Triangle Park,

North Carolina 27711. For information regarding Methods 316 and 318,

contact Ms. Rima N. Dishakjian, Emissions, Monitoring, and Analysis

Division, at (919) 541-0443.

SUPPLEMENTARY INFORMATION:

Regulated Entities. Entities potentially regulated by the final

rule are facilities that manufacture wool fiberglass. Regulated

categories and entities are shown in Table 1.

Table 1.--Regulated Categories and Entities

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Entity category Description

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Industrial.......................... Wool Fiberglass Manufacturing Plants (SIC 3296).

Federal Government: Not Affected.

State/Local/Tribal Government: Not

Affected.

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This table is not intended to be exhaustive, but rather provides a

guide for readers regarding entities likely to be regulated by this

action. This table lists the types of entities that the EPA is now

aware could potentially be regulated by this action. To determine

whether your facility is regulated by this action, you should carefully

examine the applicability criteria in Sec. 63.1380 of the final rule.

If you have any questions regarding the applicability of this action to

a particular entity, consult the appropriate regional representative:

Region I--Janet Bowen, Office of Ecosystem Protection, U.S. EPA,

Region I, CAP, JFK Federal Building, Boston, MA 02203, (617) 565-3595.

Region II--Kenneth Eng, Air Compliance Branch Chief, U.S. EPA,

Region II, 290 Broadway, New York, NY 10007-1866, (212) 637-4000.

Region III--Bernard Turlinski, Air Enforcement Branch Chief, U.S.

EPA, Region III, 3AT10, 841 Chestnut Building, Philadelphia, PA 19107,

(215) 566-2110.

Region IV--Lee Page, Air Enforcement Branch, U.S. EPA, Region IV,

Atlanta Federal Center, 61 Forsyth Street, Atlanta, GA 30303-3104,

(404) 562-9131.

Region V--George T. Czerniak, Jr., Air Enforcement Branch Chief,

U.S. EPA, Region V, 5AE-26, 77 West Jackson Street, Chicago, IL 60604,

(312) 353-2088.

Region VI--John R. Hepola, Air Enforcement Branch Chief, U.S. EPA,

Region VI, 1445 Ross Avenue, Suite 1200, Dallas, TX 75202-2733, (214)

665-7220.

Region VII--Donald Toensing, Chief, Air Permitting and Compliance

Branch, U.S. EPA, Region VII, 726 Minnesota Avenue, Kansas City, KS

66101, (913) 551-7446.

Region VIII--Douglas M. Skie, Air and Technical Operations Branch

Chief, U.S. EPA, Region VIII, 999 18th Street, Suite 500, Denver, CO

80202-2466, (303) 312-6432.

Region IX--Barbara Gross, Air Compliance Branch Chief, U.S. EPA,

Region IX, 75 Hawthorne Street, San Francisco, CA 94105, (415) 744-

1138.

Region X--Anita Frankel, Air and Radiation Branch Chief, U.S. EPA,

Region X, AT-092, 1200 Sixth Avenue, Seattle, WA 98101, (206) 553-1757.

Judicial Review. The NESHAP for wool fiberglass manufacturing

plants was proposed on March 31, 1997 (62 FR 15228); this action

announces the EPA's final decisions on the rule. Under section

307(b)(1) of the CAA, judicial review of the NESHAP is available only

by filing a petition for review in the U.S. Court of Appeals for the

District of Columbia Circuit within 60 days of today's publication of

this final rule. Under section 307(b)(2) of the CAA, the requirements

that are the subject of today's notice may not be challenged later in

civil or criminal proceedings brought by the EPA to enforce these

requirements.

Technology Transfer Network. In addition to being available in the

docket, an electronic copy of today's document, which includes the

regulatory text, is available through the Technology Transfer Network

(TTN) at the Unified Air Toxics Website (UATW). Following promulgation,

a copy of the rule will be posted at the TTN's policy and guidance page

for newly proposed or promulgated rules (http://www.epa.gov/ttn/oarpg/

t3pfpr.html). The TTN facilitates the exchange of information in

various areas of air pollution control, such as technology. If more

information on the TTN is needed, call the TTN HELP line at (919) 541-

5384.

Outline. The following outline is provided to aid in reading this

preamble to the final rule.

I. Background

A. Background and Purpose of Standards

B. Technical Basis of Regulation

C. Stakeholder and Public Participation

II. Summary of Final Rule

A. Applicability

B. Emission Standards

C. Compliance and Performance Test Provisions

D. Monitoring and Operating Requirements

E. Notification, Reporting, and Recordkeeping Requirements

III. Summary of Changes Since Proposal

A. Definitions

B. Performance Test Provisions

C. Monitoring Requirements

D. Notification, Reporting, and Recordkeeping Requirements

E. Display of OMB Control Numbers

IV. Summary of Impacts

V. Summary of Responses to Major Comments

A. Selection of Pollutants

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B. Selection of Emission Limits

C. Monitoring

D. Performance Tests

VI. Administrative Requirements

A. Docket

B. Executive Order 12866--Regulatory Planning and Review

C. Executive Order 12875--Enhancing the Intergovernmental

Partnership

D. Unfunded Mandates Reform Act

E. Regulatory Flexibility

F. Submission to Congress and the General Accounting Office

G. Paperwork Reduction Act

H. Pollution Prevention Act

I. National Technology Transfer and Advancement Act

J. Executive Order 13045--Protection of Children from

Environmental Health Risks and Safety Risks

K. Executive Order 13084--Consultation and Coordination With

Indian Tribal Governments

I. Background

A. Background and Purpose of Standards

Section 112 of the CAA requires that the EPA promulgate regulations

for the control of HAP emissions from both new and existing major

sources. The statute requires the regulations to reflect the maximum

degree of reduction in emissions of HAPs that is achievable, taking

into consideration the cost of achieving the emission reduction, any

nonair quality health and environmental impacts, and energy

requirements. This level of control is commonly referred to as MACT.

Section 112 of the CAA requires the EPA to establish national

standards to reduce air emissions from major sources and certain area

sources that emit one or more HAPs. Section 112(b) contains a list of

HAPs to be regulated by NESHAP. Section 112(c) directs the Agency to

use this pollutant list to develop and publish a list of source

categories for which NESHAP will be developed and a schedule for

development of these NESHAP. The Agency must list all known source

categories and subcategories of ``major sources'' that emit one or more

of the listed HAPs. A major source is defined in section 112(a) as any

stationary source or group of stationary sources located within a

contiguous area and under common control that emits or has the

potential to emit in the aggregate, considering controls, 10 tons per

year or more of any one HAP or 25 tons per year or more of any

combination of HAPs. This list of source categories was published in

the Federal Register on July 16, 1992 (57 FR 31576) and includes wool

fiberglass manufacturing.

The control of HAPs is achieved through the promulgation of

technology-based emission standards under section 112 for categories of

sources that emit HAPs. Emission reductions may be accomplished through

the application of measures, processes, methods, systems, or techniques

including, but not limited to: (1) Reducing the volume of, or

eliminating emissions of, such pollutants through process changes,

substitution of materials, or other modifications; (2) enclosing

systems or processes to eliminate emissions; (3) collecting, capturing,

or treating such pollutants when released from a process, stack,

storage or fugitive emissions point; (4) design, equipment, work

practice, or operational standards (including requirements for operator

training or certification) as provided in subsection (h); or (5) a

combination of the above. (See section 112(d)(2).) The EPA may

promulgate more stringent regulations to address residual risk that

remains after the imposition of controls. (See section 112(f)(2).)

Pursuant to section 112(d) of the CAA, on March 31, 1997, the EPA

proposed NESHAP for new and existing major sources in the wool

fiberglass manufacturing source category (62 FR 15228).

B. Technical Basis of Regulation

Since proposal, no changes have been made in the emission standards

or the MACT floor that is the basis for the emission standards. The

rationale for the selection of the standards, including their technical

basis, is discussed in the preamble to the proposed rule (62 FR 15228,

March 31, 1997).

C. Stakeholder and Public Participation

Various stakeholders were involved in the development of these

standards. Individual wool fiberglass companies and the industry

association (the North American Insulation Manufacturers Association)

were consulted throughout the development of these standards.

Representatives from State and Regional enforcement agencies, as well

as representatives from other offices within the EPA, participated in

the regulatory development process by reviewing and commenting on the

standards during development.

The NESHAP for wool fiberglass manufacturing (40 CFR part 63,

subpart NNN) was proposed in the Federal Register on March 31, 1997 (62

FR 15228). The public comment period ended on May 30, 1997. Industry

representatives, regulatory authorities, and environmental groups had

the opportunity to comment on the proposed standard and to provide

additional information during the public comment period. Although the

Agency offered at proposal the opportunity for oral presentation of

data, views, or arguments concerning the proposed rule, no one

requested a hearing and a hearing was not held. The EPA received nine

letters containing comments on the proposed standard from various

groups including associations representing industry, regulatory

agencies, and air pollution control equipment vendors, as well as from

State regulatory agencies and a private citizen. This final rule

reflects the EPA's full consideration of the comments. The major public

comments, along with the EPA's responses to the comments on the

proposed rule, are summarized in this preamble. A more detailed

discussion of public comments and EPA's responses is contained in the

docket (Docket No. A-95-24; Item V-C-2).

II. Summary of Final Rule

A. Applicability

As stated in Sec. 63.1380, the final NESHAP applies to each of the

following existing and newly constructed sources located at a wool

fiberglass manufacturing facility: All glass-melting furnaces, rotary

spin (RS) manufacturing lines that produce bonded building insulation,

and flame attenuation (FA) manufacturing lines producing bonded pipe

insulation. The rule also applies to new FA manufacturing lines

producing bonded heavy-density products. RS and FA manufacturing lines

that produce nonbonded products, where no binder is applied, are not

subject to the standards. A facility emitting less than 10 tons per

year of any HAP or less than 25 tons per year of any combination of

HAPs is an area source and is not subject to this NESHAP. Facilities

that manufacture mineral wool from rock or slag are not subject to this

rule but are subject to a separate NESHAP for mineral wool production.

(See 62 FR 25370 (May 8, 1997), notice of proposed rulemaking.)

B. Emission Standards

No changes were made to the emission limits as proposed. The

emission standards are contained in the final rule in Sec. 63.1382.

C. Compliance and Performance Test Provisions

As stated in Sec. 63.1387, new sources must demonstrate compliance

with the standard at startup. Existing sources must comply within 3

years of the effective date of the final rule but may request an

extension for a fourth year pursuant to the regulatory authority under

section 112(i)(3)(B) of the CAA.

[[Page 31698]]

As required by Sec. 63.1384, owners or operators must, by

conducting a performance test, demonstrate initial compliance with the

PM emission limits for affected glass-melting furnaces and the

formaldehyde emission limits for affected RS and FA manufacturing

lines. During the initial performance test, the owner or operator must

monitor and record the glass pull rate of the furnace and the glass

pull rate of each manufacturing line during each of the three test runs

and determine the emission rate for each run. A determination of

compliance will be based on the average of the three individual test

runs.

In Sec. 63.1384, the owner or operator is required to monitor and

record all parameter values at least every 15 minutes during the

performance test and to calculate an average using all of the parameter

measurements. However, the standard requires that the appropriate

parameters for incinerators and scrubbers be continuously monitored and

recorded.

The owner or operator of an electrostatic precipitator (ESP) that

is used to control PM emissions from a glass-melting furnace must

monitor and record the ESP operating parameter(s) and establish the

parameter limit(s) that will be used to monitor the ESP performance

following the performance test. Where a cold top electric furnace is

operated without the use of an add-on PM control device, the owner or

operator must monitor and record the air temperature above the surface

of the glass melt to ensure that the maximum temperature does not

exceed 120 deg.C (250 deg.F) at a location 46 to 61 centimeters (18

to 24 inches) above the molten glass surface. The owner or operator of

a glass-melting furnace that is not equipped with an add-on PM control

device and that is not a cold top electric furnace must monitor and

record the furnace operating parameter(s) and establish the parameter

limit(s) that will be used to monitor the furnace performance following

the performance test.

To determine compliance with the emission limits for new and

existing RS and FA manufacturing lines subject to the standard, the

owner or operator must measure formaldehyde emissions to the atmosphere

from forming and, when present, curing and cooling processes, and sum

the emissions from these processes. The owner or operator must,

according to Sec. 63.1384, conduct the initial performance test for

each new or existing RS manufacturing line while making the building

insulation product with the highest loss on ignition (LOI) expected to

be produced on that manufacturing line. Initial performance tests are

required for new FA manufacturing lines producing heavy-density

products and on new and existing FA manufacturing lines producing pipe

products. Performance tests for each affected FA manufacturing line

must be conducted while producing the highest LOI heavy-density or pipe

product, as appropriate.

During performance tests on affected RS and FA manufacturing lines,

the owner or operator must record, as specified in Sec. 63.1384, the

LOI and density of each product for each line tested, the free

formaldehyde content of the resin(s) used during the tests, and the

binder formulation(s) used during the tests. The performance tests must

be conducted using the resin having the highest free formaldehyde

content that the owner or operator expects to use on that line. If the

owner or operator uses process modifications to comply with the

emission limits for affected RS or FA manufacturing lines, the owner or

operator must monitor and record the process parameter(s) and establish

the process parameter limit(s) that will be used to monitor the

performance of the process modifications following the performance

tests. If a wet scrubbing control device is used to control

formaldehyde emissions from affected RS or FA manufacturing lines, the

owner or operator must continuously monitor and record the scrubber

parameters and establish the operating limits of the pressure drop

across each scrubber, the scrubbing liquid flow rate to each scrubber,

and the identity and feed rate of any chemical additive. Where a

thermal incinerator is used to comply with the emission limit for

formaldehyde, the owner or operator is required to continuously measure

and record the incinerator operating temperature during the performance

test and determine the average temperature during each 1-hour test run.

The average of the three test runs will be used to monitor compliance.

Under Sec. 63.1384, the owner or operator may seek to broaden or

extend the operating limits established during the performance tests

for affected control devices and processes by conducting additional

performance tests to demonstrate compliance at the new limits.

Under Sec. 63.1384, the owner or operator of RS and FA

manufacturing lines may conduct short-term experimental production runs

without conducting additional performance tests. The final rule

requires the owner or operator to notify the Administrator at least 15

days in advance of an experimental production run. The experimental

runs must not exceed 1 week in duration unless a longer period is

approved by the Administrator. The owner or operator may conduct the

experimental production run unless notified of a decision to disapprove

the run or unless notified of a request for additional information

prior to the date of the run.

D. Monitoring and Operating Requirements

Owners or operators of affected sources must submit, under

Sec. 63.1383, an operations, maintenance, and monitoring plan as part

of their application for a part 70 permit. The plan must include

procedures for the proper operation and maintenance of processes and

control devices used to comply with the emission limits as well as the

corrective actions to be taken when control devices or process

parameters deviate from allowable levels established during performance

testing. The plan also must identify the procedures for the proper

operation and maintenance of monitoring devices including periodic

calibration and verification of accuracy.

Section 63.1383 requires that each baghouse used on a glass-melting

furnace be equipped with a bag leak detection system having an audible

alarm that automatically sounds when an increase in particulate

emissions above a predetermined level is detected. Such a device

monitors the performance of the baghouse, detects an increase in PM

emissions, and indicates that maintenance of the baghouse is needed.

The operating limits of Sec. 63.1382 require the owner or operator to

initiate corrective action within 1 hour of the alarm sounding

according to the operations, maintenance, and monitoring plan. If the

alarm is activated for more than 5 percent of the total operating time

during the 6-month block reporting period, the owner or operator must

develop and implement a Quality Improvement Plan (QIP). The QIP must be

consistent with the compliance assurance monitoring rule, 40 CFR part

64 subpart D (62 FR 54900, October 22, 1997).

The monitoring requirements of Sec. 63.1383 require the owner or

operator of each ESP used to control an affected glass-melting furnace

to monitor and record the established ESP parameter(s) according to the

procedures in the operations, maintenance, and monitoring plan. The

final rule requires the owner or operator to initiate corrective action

within 1 hour, according to the procedures in the facility's

operations, maintenance, and monitoring plan, if the monitored

[[Page 31699]]

parameter(s) deviates from the limit(s) established during performance

tests. If the monitored parameter(s) is outside the established

limit(s) for more than 5 percent of the total operating time in a 6-

month block reporting period, the owner or operator must develop and

implement a QIP. The owner or operator must operate the ESP such that

the monitored parameter(s) does not deviate from the established

limit(s) for more than 10 percent of the total operating time in a 6-

month block reporting period.

Under Sec. 63.1383 of the final rule, the owner or operator of a

cold top electric furnace, who complies with the PM emission limit

without the use of an air pollution control device, must monitor and

record the air temperature above the glass melt to monitor when the

temperature exceeds the maximum temperature of 120 deg.C (250 deg.F)

measured at a location 46 to 61 centimeters (18 to 24 inches) above the

molten glass surface. The owner or operator must initiate corrective

action within 1 hour according to Sec. 63.1382 if the average air

temperature exceeds the maximum. If the air temperature as measured

above the molten glass exceeds the maximum for more than 5 percent of

the total operating time in a 6-month block reporting period, the owner

or operator is required to develop and implement a QIP. The rule also

requires that the owner or operator operate the cold top electric

furnace so that the maximum temperature is not exceeded for more than

10 percent of the total operating time in a 6-month block reporting

period.

The final rule (Sec. 63.1383) requires the owner or operator of a

glass-melting furnace, which is not equipped with an air pollution

control device for PM control and which is not a cold top electric

furnace, to monitor the glass-melting furnace according to the

procedures in the operation, maintenance, and monitoring plan. The plan

must include the furnace operating parameter(s) and parameter limit(s)

to be monitored to identify any operational problems, a monitoring

schedule, and recordkeeping procedures. As required by Sec. 63.1382,

the owner or operator must initiate corrective action within 1 hour if

the monitored operating parameter(s) deviates from the limits

established during the initial performance. The rule also requires the

owner or operator to develop and implement a QIP if the monitored

furnace operating parameter value(s) is outside the established

limit(s) for more than 5 percent of the total operating time in a 6-

month block reporting period. The owner or operator must operate the

affected glass-melting furnace so that the monitored furnace parameter

value(s) is not outside the established limit(s) for more than 10

percent of the total operating time in a 6-month block reporting

period.

The final rule, under Sec. 63.1383, requires the owner or operator

to monitor and record the glass pull rate on all existing and new

glass-melting furnaces. If the monitored pull rate exceeds by more than

20 percent the average glass pull rate measured during the performance

test, the owner or operator must initiate corrective action within 1

hour as required by Sec. 63.1383. If the glass pull rate exceeds (by

more than 20 percent) the average established during the performance

test for more than 5 percent of the total operating time in a 6-month

block reporting period, the owner or operator must develop and

implement a QIP. The final rule requires the owner or operator to

operate the glass-melting furnace so that the glass pull rate does not

exceed (by more than 20 percent) the average established during the

performance test for more than 10 percent of the total operating time

in a 6-month block reporting period.

If an incinerator is used to control formaldehyde emissions,

Sec. 63.1383 requires that the owner or operator continuously monitor

and record the operating temperature. Following the initial performance

test, the operating limits of Sec. 63.1382 require that the owner or

operator maintain the temperature so that the temperature, averaged

over any 3-hour block period, does not fall below the average

temperature established during the initial performance test. As

required in Sec. 63.1383, the owner or operator must also annually

inspect each incinerator to ensure its proper operation and

maintenance. The rule specifies that, at a minimum, the following be

included in the inspection:

(1) Burners, pilot assemblies, and pilot sensing devices;

(2) Adjustment of combustion air;

(3) Internal structures, such as baffles;

(4) Dampers, fans, and blowers;

(5) Proper sealing;

(6) Motors;

(7) Refractory lining; and (8) Incinerator shell.

Section 63.1383 of the final rule requires that the owner or

operator, who uses a wet scrubbing control device to control

formaldehyde emissions from affected RS or FA manufacturing lines,

continuously monitor and record the gas pressure drop across each

scrubber, the scrubbing liquid flow rate to each scrubber, and the

identity and feed rate of any chemical added to the scrubbing liquid.

As required in Sec. 63.1382, the owner or operator must initiate

corrective action according to the procedures in the facility's

operations, maintenance, and monitoring plan within 1 hour if the

average scrubber parameter for any 3-hour block period deviates from

the limit(s) established during the initial performance test. If any

scrubber parameter is outside an established limit(s) for more than 5

percent of the total operating time in a 6-month block reporting

period, the owner or operator must develop and implement a QIP. The

owner or operator must operate each affected scrubber such that none of

the monitored parameters deviate from the established limits for more

than 10 percent of the total operating time in a 6-month block

reporting period.

As required in Sec. 63.1383, the owner or operator who uses process

modifications to comply with the emission limits for RS or FA

manufacturing lines must establish a correlation between the

parameter(s) to be monitored and formaldehyde emissions. The owner or

operator must also include as part of the operations, maintenance, and

monitoring plan information on how the process will be operated and

maintained, the process parameter(s) to be monitored including the

correlation between the parameter(s) and formaldehyde emissions, a

monitoring schedule, and recordkeeping procedures to document proper

operation of the process modifications. Section 63.1382 of the final

rule requires the owner or operator to initiate corrective action

within 1 hour of a deviation of a process parameter from the

established limits and to develop and implement a QIP if the process

parameter(s) is outside the established limit(s) for more than 5

percent of the total operating time in a 6-month block reporting

period. The owner or operator must operate the process so that the

process modification parameters do not deviate from the established

limits for more than 10 percent of the total operating time in a 6-

month block reporting period.

Under Sec. 63.1383 of the final rule, the owner or operator must

monitor and record the free formaldehyde content of each resin

shipment, the formulation of each batch of binder used, and, every 8

hours, product LOI and product density. Following the performance test,

Sec. 63.1382 requires that the owner or operator must formulate binders

using resins having a free formaldehyde content that does not exceed

the free formaldehyde content range contained in the resin

specification established and used during the performance test.

[[Page 31700]]

The final rule also requires that the owner or operator use a binder

formulation that does not vary from the specification and operating

range established during the performance test. For purposes of this

rule, the addition of urea and lignin to the binder formulation is not

considered changes in the formulation.

Failure to operate all affected processes and control devices

according to the operating limits of Sec. 63.1382, for example, failure

to initiate corrective actions or failure to develop and implement a

QIP, is considered a violation of the operating requirements.

Under Sec. 63.1383 of this rule, the owner or operator may modify

any of the control device or process parameter limits established

during the initial performance tests provided that the owner or

operator conducts additional emission testing to verify compliance at

the new parameter levels.

E. Notification, Reporting, and Recordkeeping Requirements

Notification, reporting, and recordkeeping requirements for MACT

standards are included in the NESHAP general provisions (40 CFR part

63, subpart A). The general provisions require: (1) Initial

notification(s) of applicability, notification of performance test, and

notification of compliance status; (2) a report of performance test

results; (3) a startup, shutdown, and malfunction plan with semiannual

reports of any reportable events; and (4) semiannual reports of

deviations from established parameters. When deviations in operating

parameters established during performance testing are reported, the

owner or operator must report quarterly until a request to return to

semiannual reporting is approved by the Administrator.

In addition to the requirements of the general provisions,

Sec. 63.1386 of the final rule specifies additional records to be kept

by the owner or operator. The final rule requires the owner or operator

to maintain records of the following, as applicable:

(1) Bag leak detection system alarms, including the date and time

of the alarm, when corrective actions were initiated, the cause of the

alarm, an explanation of the corrective actions taken, and when the

cause of the alarm was corrected;

(2) ESP parameter value(s) used to monitor ESP performance,

including any period when the value(s) deviates from the established

limit(s), the date and time of the deviation, when corrective actions

were initiated, the cause of the deviation, an explanation of the

corrective actions taken, and when the cause of the deviation was

corrected;

(3) Air temperature above the molten glass in an uncontrolled cold

top electric furnace, including any period when the temperature exceeds

120 deg.C (250 deg.F) at a location 46 to 61 centimeters (18 to 24

inches) above the molten glass surface, the date and time of the

exceedance, when corrective actions were initiated, the cause of the

exceedance, an explanation of the corrective actions taken, and when

the cause of the exceedance was corrected;

(4) Uncontrolled glass-melting furnace (that is not a cold top

electric furnace) parameter value(s) used to monitor furnace

performance, including any period when the value(s) exceeds the

established limit(s), the date and time of the exceedance, when

corrective actions were initiated, the cause of the exceedance, an

explanation of the corrective actions taken, and when the cause of the

exceedance was corrected;

(5) The LOI and product density for each bonded product

manufactured on a RS or FA manufacturing line, the free formaldehyde

content of each resin shipment received and used in binder formulation,

and the binder formulation of each batch;

(6) Process parameter level(s) for RS and FA manufacturing lines

that use process modifications to comply with the emission standards,

including any period when the parameter level(s) deviates from the

established limit(s), the date and time of the deviation, when

corrective actions were initiated, the cause of the deviation, an

explanation of the corrective actions taken, and when the cause of the

deviation was corrected;

(7) Scrubber pressure drop, scrubbing liquid flow rate, and any

chemical additive (including chemical feed rate to the scrubber),

including any period when a parameter level(s) deviates from the

established limit(s), the date and time of the deviation, when

corrective actions were initiated, the cause of the deviation, an

explanation of the corrective actions taken, and when the cause of the

deviation was corrected;

(8) Incinerator operating temperature and results of periodic

inspection of incinerator components, including any period when the

temperature falls below the established average or the inspection

identifies problems with the incinerator, the date and time of the

problem, when corrective actions were initiated, the cause of the

problem, an explanation of the corrective actions taken, and when the

cause of the problem was corrected;

(9) Glass pull rate, including any period when the pull rate

exceeds the average pull rate established during the performance test

by more than 20 percent, the date and time of the exceedance, when

corrective actions were initiated, the cause of the exceedance, an

explanation of the corrective actions taken, and when the cause of the

exceedance was corrected.

The NESHAP general provisions (40 CFR part 63, subpart A) require

that records be maintained for at least 5 years from the date of each

record. The owner or operator must retain the records onsite for at

least 2 years but may retain the records offsite the remaining 3 years.

The files may be retained on microfilm, on microfiche, on a computer,

on computer disks, or on magnetic tape disks. Reports may be made on

paper or on a labeled computer disk using commonly available and EPA-

compatible computer software.

III. Summary of Changes Since Proposal

Changes have been incorporated into the final NESHAP for wool

fiberglass manufacturing plants in response to comments on the proposed

rule. The principal changes made since proposal are summarized below.

Additional discussion of changes and the rationale for these changes is

presented in section V of this preamble.

A. Definitions

In response to public comments, minor clarifying changes were made

in Sec. 63.1381 to the definitions of building insulation, glass pull

rate, manufacturing line, and wool fiberglass. For purposes of

clarifying the applicability of the rule and because of changes in the

monitoring requirements for certain glass-melting furnaces, definitions

were added for cold top electric furnace, new source, and wool

fiberglass manufacturing facility.

B. Performance Test Provisions

In response to public comments, the EPA revised the proposed

provision that would allow the owner or operator of RS and FA

manufacturing lines subject to the NESHAP to conduct short-term

experimental production runs without conducting additional performance

tests. Section 63.1384 of the final rule requires that the owner or

operator notify the Administrator at least 15 days in advance of an

experimental production run. The duration of the test run may not

exceed 1 week unless the Administrator approves a longer period. The

Administrator may disapprove the experimental production run or request

additional information but such disapproval or request for additional

information must be made prior to the date of the experimental

production run.

[[Page 31701]]

Other revisions clarify the proposed requirements for performance

testing by specifying the frequency for monitoring and recording

process and/or control device parameters during performance tests. The

requirements to establish process and control device parameter limits

for compliance monitoring are more appropriately a part of the

requirements for performance testing and, thus, were moved from the

monitoring requirements section to the performance test requirements

section. The requirement for RS manufacturing lines to use the most

frequently manufactured building insulation when conducting performance

tests was deleted from the proposed definition of building insulation.

A requirement was added to the performance testing provisions

(Sec. 63.1384) for affected RS and FA manufacturing lines to conduct

performance test while manufacturing the product having the highest LOI

expected to be produced on the affected line. Because a glass-melting

furnace may supply more than one manufacturing line, the final rule

clarifies that, in addition to the furnace glass pull rate, the glass

pull rate for the manufacturing line must also be monitored during the

performance test.

Methods for measuring formaldehyde emissions from RS and FA

manufacturing lines were contained in the proposed rule. Because the

Agency now has an FTIR method (Method 320) that can be used at other

sources, a self-validating method is no longer necessary. Method 318

was modified by removing the spiking procedures, which simplifies use

of the method. The EPA has also clarified that this method is only

applicable at mineral wool and wool fiberglass manufacturing sources.

In response to comments, the final rule also contains editorial and

clarifying changes in Method 318.

C. Monitoring Requirements

The monitoring requirements section in the proposed rule specified,

for each control device and process, the parameter that was to be

monitored. In the final rule, the section on monitoring requirements

was revised. In the final rule, the monitoring requirements section

(Sec. 63.1383) specifies that process or control device parameters must

be monitored as well as monitoring frequency. The final rule recognizes

that a deviation of a process or control device parameter from a level

established during a performance test is more appropriately a violation

of an operating limit rather than a violation of an emission limit. The

operating limits are part of the standard and are specified in

Sec. 63.1382.

The proposed rule stated that the owner or operator of each

affected source had to submit an operations, maintenance, and

monitoring plan containing information on the proper operation and

maintenance of process modifications and control devices, the

parameter(s) to be monitored that would be used to determine

compliance, and corrective actions to be taken when monitoring

indicated a deviation from the limit(s) established during the

performance tests. The final rule (Sec. 63.1383) clarifies that the

operations, maintenance, and monitoring plan must also include

procedures for the proper operation and maintenance of all monitoring

devices. As proposed, each baghouse used on a glass-melting furnace

must be equipped with a bag leak detection system having an audible

alarm that automatically sounds when an increase in particulate

emissions above a predetermined level is detected. In response to

comments and for consistency with other regulations, Sec. 63.1383 of

the final standard requires that the monitor be capable of detecting PM

emissions at concentrations of 10 milligrams per actual cubic meter

(0.0044 grains per actual cubic foot). Also, because guidelines for the

operation and maintenance of triboelectric bag leak detection systems

have become available since proposal, these guidelines are specifically

cited in the rule. The EPA's ``Fabric Filter Bag Leak Detection

Guidance'' (EPA-454/R-98-015, September 1997) is available on the TTN

under Emission Measurement Center (EMC), Continuous Emission

Monitoring. To maintain consistency with bag leak detection system

requirements in other regulations and to allow owners and operators

flexibility to make necessary bag leak detection system adjustments,

the final rule specifies that following initial adjustment, the owner

or operator may adjust the range, averaging period, alarm set points,

or alarm delay time as specified in the approved operations,

maintenance, and monitoring plan. The final rule further specifies that

in no event may the range be increased by more than 100 percent or

decreased by more than 50 percent over a 365 day period unless a

responsible official, as defined in Sec. 63.2 of the general provisions

in subpart A of 40 CFR part 63, certifies in writing to the

Administrator that the fabric filter has been inspected and found to be

in good operating condition. The final rule clarifies that the alarm

must be located in an area where appropriate plant personnel will be

able to hear it and that in response to the sounding of an alarm, the

owner or operator must complete corrective actions in a timely manner.

The final rule also specifies some example corrective actions for bag

leak detection system alarms that may be included in the operations,

maintenance, and monitoring plan.

Under the proposed rule, the owner or operator would continuously

monitor and record the glass pull rate on all existing and new glass-

melting furnaces. As a result of comments, Sec. 63.1383 of the final

rule clarifies what is meant by continuous monitoring of the glass pull

rate. Similar revisions were made to the monitoring requirements for

other control devices and process parameters to clarify the

requirements for monitoring frequency. Revisions were made to the

proposed rule to clarify when corrective actions are required in

response to monitored levels that are outside the limits established

during performance tests.

Under the proposed NESHAP, the owner or operator would be in

violation of the standard if the binder formulation deviated from the

formulation specifications used during the performance test. In

response to comments, the final rule states that the addition of urea

and lignin to the binder formulation does not constitute a change in

binder formulation, and the operating limits in Sec. 63.1382 for the

binder formulation and the use of resins were clarified to incorporate

this change.

In response to comments, clarifying changes were made throughout

the monitoring and operating requirements to indicate that because some

control device or process parameters used for monitoring purposes may

be established as minimum and/or maximum values, it is not always

appropriate to have requirements that are in terms of exceeding control

device or process parameter values. Other minor editorial changes were

made throughout the monitoring and operating requirements to improve

clarity.

Consistent with the general provision requirements to operate and

maintain air pollution equipment in a manner consistent with good air

pollution control practices, the final rule contains specific

provisions for the annual inspection of incinerators to ensure that

they maintain their performance in reducing formaldehyde emissions.

The proposed rule allowed the owner or operator of a glass-melting

furnace that complies with the PM emission limit without the use of

add-on control devices to determine the appropriate process parameter

or control device parameter to monitor to determine compliance. Section

63.1383 of the final

[[Page 31702]]

rule specifies that the owner or operator of a cold top electric

furnace is required to monitor the air temperature above the molten

glass surface. Section 63.1382 requires the owner or operator of a cold

top electric furnace to operate the furnace such that the air

temperature above the molten glass does not exceed 120 deg.C (250

deg.F) more than 10 percent of total operating time in a 6-month block

reporting period.

D. Notification, Reporting, and Recordkeeping Requirements

The proposed rule specified additional records to be kept by the

owner or operator in addition to the requirements of the general

provisions. Editorial and clarifying revisions were made to the final

notification, reporting, and recordkeeping requirements (Sec. 63.1386).

The final rule specifies that the time that corrective action is

initiated, as well as when the cause of the alarm, deviation, or

exceedance was corrected, must be recorded. In addition, product

density and glass pull rate were added to the list for which records

are required to be kept, consistent with the monitoring provisions in

Sec. 63.1383. Other revisions were made to the recordkeeping provisions

consistent with changes made in the monitoring and operating

provisions.

E. Display of OMB Control Numbers

The EPA is today amending the table of currently approved

information collection request (ICR) control numbers issued by OMB for

various regulations. Today's amendment updates the table to list the

information requirements contained in this final rule. The EPA will

continue to present OMB control numbers in a consolidated table format

to be codified in 40 CFR part 9 of the Agency's regulations, and in

each CFR volume containing EPA regulations. The table lists the section

numbers with reporting and recordkeeping requirements, and the current

OMB control numbers. This listing of the OMB control numbers and its

subsequent codification in the CFR satisfy the requirements of the

Paperwork Reduction Act (PRA) (44 U.S.C. 3501 et seq.) and OMB's

implementing regulations at 5 CFR part 1320.

The ICR was previously subject to public notice and comment prior

to OMB approval. As a result, EPA finds there is ``good cause'' under

section 553(b)(B) of the Administrative Procedure Act (5 U.S.C.

553(b)(B)) to amend this table without prior notice and comment. Due to

the technical nature of the table, further notice and comment would be

unnecessary.

IV. Summary of Impacts

The impacts estimated to be attributable to the final rule are the

same as those estimated to be attributable to the proposed rule (62 FR

15228, March 31, 1997). Nationwide emissions of formaldehyde from

existing RS and FA manufacturing lines are estimated to be 1,770 Mg/yr

(1,950 ton/yr) at the current level of control. Implementation of the

final rule will reduce nationwide formaldehyde emissions from existing

sources by 410 Mg/yr (450 ton/yr). Emission reductions from RS

manufacturing lines producing building insulation constitute the entire

reduction; there are no emission reductions from FA manufacturing

lines. Reduction in formaldehyde emissions from new RS manufacturing

lines is estimated to be 120 Mg/yr (130 ton/yr) in the fifth year of

the standard. Total reductions in formaldehyde emissions from both

existing and new RS manufacturing lines, therefore will be 530 Mg/yr

(580 ton/yr). Nationwide PM emissions from existing glass-melting

furnaces at the current level of control, are about 750 Mg/yr (830 ton/

yr). Under this rule, PM emissions from existing furnaces will be

reduced by about 600 Mg/yr (660 ton/yr), of which 40 Mg/yr (50 ton/yr)

is particulate matter less than 10 microns (m) in diameter

(PM-10). The PM emission reduction from new glass-melting furnaces

resulting from this rule is estimated to be 160 Mg/yr (180 ton/yr) in

the fifth year of the standard. Under the final rule, PM emissions from

existing and new furnaces will be reduced by a total of 760 Mg/yr (840

ton/yr). Current nationwide emissions of metal HAPs from existing

furnaces is 270 kg/yr (600 lb/yr). Under the final rule, metal HAP

emissions from existing furnaces and new furnaces will be reduced by 9

kg/yr (20 lb/yr) and 2 kg/yr (5 lb/yr), respectively.

The EPA expects no water or solid waste impacts from the final

rule. Because this standard is based on the use of baghouses, dry

ESP's, thermal incinerators, and process modifications, there are no

water pollution impacts. One existing RS manufacturing line uses

scrubbers to control HAP emissions from forming. This rule will not

affect the water pollution impact of the scrubbers. No additional

sources are expected to add wet scrubbers for the control of HAP

emissions. The PM captured by the baghouses added to existing

uncontrolled electric furnaces will be recycled back to the furnace and

no solid or hazardous waste is generated by the use of thermal

incinerators. The EPA estimates that the rule will have a minor impact

on energy consumption.

The total nationwide capital cost for existing glass-melting

furnaces under the final rule is $3.2 million; the total annual cost is

$1.5 million. These costs result from the expected addition of

baghouses to seven electric glass-melting furnaces as well as the

monitoring costs of bag leak detection systems installed on baghouses

and temperature monitors installed on cold top electric furnaces.

The EPA estimates the nationwide capital costs of upgrading process

modifications on 30 RS manufacturing lines to be $16.3 million, with

annual costs of $4.8 million. None of the existing curing ovens that

are uncontrolled for HAPs will have to add an incinerator. None of the

FA manufacturing lines subject to the rule will require additional

controls to comply with the emission standards. Therefore, no control

costs are associated with complying with the final rule for FA

manufacturing lines. For all RS and FA manufacturing lines subject to

the standard, there is a one-time cost of $15,000 per line to establish

the process parameter values for compliance monitoring. Because the

parameters that the owner or operator is required to monitor on RS and

FA manufacturing lines are currently monitored by the industry, no

additional costs will be incurred for monitoring beyond the one-time

cost of $15,000 per line.

Total nationwide capital cost for the standard is estimated to be

$19.5 million and annual nationwide cost is estimated to be $6.3

million/yr, including installation, operation, and maintenance of

emission control and monitoring systems.

The economic analysis of the rule finds impacts at the facility and

market-level to be modest. The average market price increases for both

structural and nonstructural wool fiberglass are expected to be less

than 0.5 percent. The resultant decreases in quantity demanded range

from 0.17 percent for structural insulation markets to 0.22 percent for

nonstructural insulation markets. None of the affected firms are

classified as small businesses and no closures are predicted.

V. Summary of Responses to Major Comments

The EPA received nine comment letters on the proposed NESHAP for

wool fiberglass manufacturing. A copy of each comment letter is

available for public inspection in the docket for the rulemaking

(Docket No. A-95-24; see

[[Page 31703]]

the ADDRESSES section of this preamble for information on inspecting

the docket). The EPA has had follow-up discussions with commenters

regarding specific issues initially raised in their written comments.

Copies of correspondence and other information exchanged between the

EPA and the commenters during the post-comment period are available for

public inspection in the docket for the rulemaking.

All comments received by EPA were reviewed and carefully considered

by the Agency. The EPA made changes to the rule where appropriate. A

summary of responses to major comments received on the proposed rule is

presented below. Additional discussion of the EPA's responses to public

comments is presented in the document ``Summary of Public Comments and

Responses on Wool Fiberglass Manufacturing NESHAP'' (Docket A-95-24,

Item V-C-2).

A. Selection of Pollutants

Comment: Two commenters stated that the issues of fine mineral

fibers as HAP and the health effects of wool fiberglass particles

greater than 1 micron in diameter should be addressed. One commenter

stated that because the definition of fine mineral fibers is under

review in response to new data on health effects and respirability, the

EPA should address in the final preamble the possibility of a new

definition for fine mineral fibers and its effects on the NESHAP.

Response: The rule does not include emission limits for fine

mineral fibers at wool fiberglass manufacturing facilities because EPA

determined that the affected sources do not emit ``fine mineral

fibers,'' as presently defined by the CAA. Fiberglass emissions from

the affected manufacturing lines at wool fiberglass manufacturing

facilities consist of clumps of fibers that are much larger than 10

micrometers in diameter. The CAA, by contrast, defines ``fine mineral

fibers'' to include mineral fiber emissions from facilities

manufacturing or processing glass, rock, or slag fibers (or other

mineral derived fibers) of average diameter 1 micrometer or less. (See

section 112(b)(1)n.3.)

B. Selection of Emission Limits

Comment: One commenter stated that the EPA determined the MACT

floor for glass-melting furnaces inappropriately by establishing

equipment standards as the MACT floor rather than a straightforward

determination of numerical MACT floors as specified in section

112(d)(3) of the CAA. Such an approach, according to the commenter, has

allowed the EPA to use emissions data from the worst performing units

to set emission limits that are no more stringent than the nearly 20-

year-old NSPS for glass-melting furnaces. The commenter believes that

new baghouses and precipitators, and low-cost upgrades of existing

ones, would allow much more stringent emission limits. The commenter

stated that the EPA should base the MACT floors on the numerical

emissions of the best performing 12 percent for existing sources and

the best performing source for new sources and revise the emission

limits to be consistent with the more stringent floors.

Response: In determining the MACT floor, the EPA is not limited

merely to examining emissions test data from the best performing

sources and calculating the numeric mean of such sources' emission

rates, because the test data may not translate directly to truly

achievable standards. Rather, the Agency has taken alternative

approaches to establishing MACT floors in the past, depending on the

type, quality, and applicability of available emissions information.

(See 62 FR 49051, 49060 (September 18, 1997) (describing various

alternatives)).

Among the standard options the EPA may follow is to establish the

floor in consideration of the emissions control technology used by the

best performing sources. Specifically, the Agency could establish the

new source MACT floor based on the technology employed by the best-

controlled similar source and the existing source MACT floor based on

the technology used by the average of the best-performing 12 percent of

sources (or, in the case of categories with fewer than 30 sources, the

average of the best-performing five sources). The EPA would then

calculate a numeric MACT emission limit that is achievable in practice

by sources employing that technology, in view of process and air

pollution control device variability.

The EPA followed this technology-driven approach in the present

rulemaking. Available emissions information indicates that both

baghouses and ESP's are equally effective in controlling PM emissions

from glass-melting furnaces, and that the best performing sources in

the wool fiberglass source category employ such technology.

Accordingly, the Agency determined that either of these technologies,

when well-designed and well-operated, would form the basis of the MACT

floor for controlling emissions from glass-melting furnaces in this

source category. The EPA then sought, consistent with the CAA, to

express the MACT floor in terms of a numeric emissions limit. To do so,

it evaluated existing test data from wool fiberglass facilities

controlling glass-melting furnace emissions with baghouses and ESP's.

Because the measured emission rates varied, even though each of the

sources had well-operated and maintained air pollution control

equipment, the Agency concluded that the measured rates were indicative

of equipment and process variability. The EPA therefore established the

MACT floor at an emission level achievable by the best performing

technology, after accounting for normal operating variability.

The Agency's approach in this rulemaking to determine the

applicable MACT floors is consistent with the CAA. The CAA requires a

standard that is ``achievable'' (42 U.S.C. 112(d)(2) (``Emission

standards * * * shall require the maximum degree of reductions in

emissions * * * that the Administrator * * * determines is achievable *

* * '')). However, the commenter's insistence on setting the MACT floor

based solely on a numeric average would require the Agency to establish

a standard that, in light of normal and unavoidable control equipment

and process variability, would not be achievable consistently by the

best performing sources in the category. The EPA's method in the

present rulemaking, by contrast, heeds Congress's attention to

achievability and is a prudent exercise of the discretion the CAA

grants the Agency ``to use its best engineering judgment in collecting

and analyzing the (available emissions) data, and in assessing the

data's comprehensiveness, accuracy, and variability, in order to

determine which sources achieve the best emission reductions.'' (59 FR

29196, 29199 (June 6, 1994)) (emphasis added). See also National Lime

Association v. E.P.A., 627 F.2d 416, 431 n. 46 (D.C. Cir. 1980) (``to

be achievable, we think a uniform standard must be capable of being met

under most adverse conditions which can reasonably be expected to

recur'').

Comment: Two commenters stated that the EPA is not limited to

setting emission limits at the MACT floors and thermal and catalytic

incinerators could provide cost-effective 98 to 99 percent emission

reductions on RS forming, curing, and cooling and FA forming and

curing. According to one commenter, the emission limits for flame

attenuation manufacturing lines are much too high; more appropriate

formaldehyde emission limits are 0.068-0.078 lb/ton. Another commenter

stated that emissions as low as 0.02 kg/Mg for RS manufacturing, 0.13

kg/Mg for heavy-density flame attenuation

[[Page 31704]]

manufacturing, and 0.11 kg/Mg for pipe flame attenuation manufacturing

could be achieved if catalytic oxidation were used to control forming,

curing, and cooling processes. According to one commenter, the EPA

should also consider other creative control technology applications,

for example, ducting multiple sources, such as forming and curing, to a

single control unit at a much lower cost than separate controls on

individual process units while achieving 98-99 percent reduction in

forming and curing oven emissions. One commenter also stated that the

EPA has ignored the use of carbon-and zeolite-based concentrators,

which can reduce exhaust volumes thereby reducing the size and cost of

required control devices. According to this commenter, such

concentrators can reduce exhaust volumes to be treated at least tenfold

and sometimes much greater allowing the use of small control devices

after forming and curing. Alternatively, the concentrated exhaust could

be ducted to the curing oven or curing oven control device, thus

allowing for low-cost control of emissions from the entire wool

fiberglass manufacturing line.

Response: Even though incineration is demonstrated on rotary spin

curing ovens and is the MACT floor for new and existing rotary spin

curing ovens, incineration is not demonstrated for rotary spin forming

or for flame attenuation forming or flame attenuation curing. Further,

concentrators are not demonstrated in this industry for any process.

Although not demonstrated, the EPA considered the beyond-the-floor

control option of incineration for both rotary spin forming and flame

attenuation forming and curing processes. According to an analysis of

the cost effectiveness of beyond-the-floor controls for RS

manufacturing lines, the cost effectiveness of controlling formaldehyde

emissions from forming using incineration is $183,000 per ton of

formaldehyde reduction. On FA manufacturing lines producing heavy-

density products, the cost effectiveness of controlling formaldehyde

emissions using incineration is $1.95 million per ton of formaldehyde

reduction for forming processes and $13.5 million per ton of

formaldehyde reduction for curing processes. On FA manufacturing lines

producing pipe products, the cost effectiveness of controlling

formaldehyde emissions using incineration is $2.7 million per ton of

formaldehyde reduction for forming processes and $42.3 million per ton

of formaldehyde reduction for curing processes. At this time, the EPA

considers that the cost effectiveness of these beyond-the-floor

controls are not reasonable. Therefore, the EPA rejected beyond-the-

floor controls and set emission standards at the MACT floor level.

Comment: A commenter stated that, in light of formaldehyde

classification as a Class B1, probable human carcinogen, the EPA should

reconsider its use of the largest emission rates as the emission limits

for the flame attenuation lines producing pipe products and heavy-

density products. According to one commenter, the emission limits for

flame attenuation manufacturing lines are much too high with more

appropriate formaldehyde emission limits being 0.068-0.078 lb/ton.

Another commenter stated that emissions as low as 0.13 kg/Mg for heavy-

density flame attenuation manufacturing, and 0.11 kg/Mg for pipe flame

attenuation manufacturing could be achieved if catalytic oxidation were

used to control forming, curing, and cooling processes.

Response: In establishing emission limits for affected FA

manufacturing lines, the EPA followed the approach used for glass-

melting furnaces. Process modifications constitute the pollution

control technology used by the best performing sources, and each of the

facilities currently producing pipe insulation and heavy density

products employ an identical level of process modifications on their FA

manufacturing lines. Nevertheless, the measured emission rates of

formaldehyde from these sources varied. Because the same degree of

pollution control had different emission rates, the Agency concluded

that operational variability accounted for the differences and factored

such variability into the promulgated emission standard by setting the

MACT floor at a level achievable in practice by sources using the

identified technology.

Comment: Because the EPA is allowing averaging of emissions across

the various units making up the manufacturing line, one commenter

stated that this tends to increase emissions above those associated

with emission limits on separate process units and that EPA should set

emission limits more stringent than the sum of the floor limits rather

than allow averaging.

Response: In setting emission limits for rotary spin and flame

attenuation manufacturing lines, the EPA used available emissions data

for each process unit (forming, curing, and cooling for rotary spin

lines, and forming and curing for flame attenuation lines) to determine

the appropriate MACT floor for each process unit in the line. The

Agency then summed emissions from the MACT floors to create a resultant

line-based MACT floor emission limit. Therefore, the EPA disagrees that

these ``line'' limits are less stringent than the limits that would

have been established for individual process units if the source

subject to MACT had been defined more narrowly. For instance, because

the MACT floor for cooling on rotary spin lines and for curing on flame

attenuation lines is no control, the EPA may not have set emission

limits for these sources if limits were set on a unit-by-unit basis.

Thus, potentially higher emissions would have been allowed than are

currently being allowed under this rule.

C. Monitoring

Comment: Several comments were received concerning the use of bag

leak detectors for monitoring baghouses used to control emissions from

glass-melting furnaces. One commenter stated that because the industry

standard for sensitivity of bag leak detectors is 0.0005 gr/dscf, the

sensitivity cited in the rule should be changed from 0.0004 gr/dscf to

0.0005 gr/dscf.

According to another commenter, the requirements to install and

operate bag leak detectors according to EPA guidance

(Sec. 63.1384(b)(5)) will be difficult to enforce. The commenter

further stated that if EPA wants the guidance to be followed, it should

be contained in a rule; if not, it should be in the preamble as

recommended practice.

Another commenter asked if a source would be in violation of the

standard if the alarm on the bag leak detector is activated more than

10 percent of the total operating time during a 6-month block reporting

period.

Response: After reviewing technical data from a supplier of dust

detection equipment and reviewing other EPA standards that require bag

leak detectors for consistency, EPA has modified the required

sensitivity level to ``0.0044 gr/dscf or less.'' This change does not

alter the intended function of the bag leak detector, and is consistent

with the industry standard for sensitivity and other EPA standards.

Although EPA understands, as the one commenter indicated, that

enforcement may be more difficult, there are currently no performance

specifications available for bag leak detectors. EPA guidance on the

use of triboelectric bag leak detectors has been developed and is cited

in the rule along with information on its availability.

[[Page 31705]]

In the proposed and final rules, the source would not be in

violation of the standard if the alarm on the bag leak detector is

activated more than 10 percent of the total operating time during a 6-

month block reporting period. The EPA issued a supplemental proposal

(64 FR 7149, February 12, 1999) for wool fiberglass and other source

categories which, along with other compliance issues, deals with the

question as to the existence of a violation when the bag leak detector

alarm is activated and how it is enforced. The EPA will consider all

comments on the supplemental proposal and will amend this final rule in

a future action as appropriate.

Comment: For clarity with State agencies, one commenter recommended

that the requirement in Sec. 63.1386(e) to ``continuously monitor and

record'' as it applies to glass pull rate be defined to mean to

install, operate and maintain pull rate monitoring and recording

equipment per the written operations, maintenance, and monitoring plan.

Response: Based on additional information provided by the

commenter, EPA learned that the commenter would like the rule to

clarify the monitoring and recording frequency associated with

continuous monitors for glass pull rate. According to the commenter,

the process is very steady and there is not a need for minute-by-minute

monitoring and recordkeeping. EPA has revised the rule to require that

on existing glass-melting furnaces with continuous monitors and on all

new glass-melting furnaces, the glass pull rate must be monitored and

recorded on an hourly basis and every 4 hours an average is to be

calculated for purposes of determining compliance. At any time that a

4-hour average pull rate exceeds the average pull rate established

during the performance test by greater than 20 percent, corrective

action must be initiated within 1 hour. If a 20 percent or more

exceedance of the pull rate occurs for more than 5 percent of the total

operating time in the 6-month block reporting period, a QIP is

required. The final rule requires the owner operate the glass-melting

furnace so that the glass pull rate does not exceed, by more than 20

percent, the established maximum glass pull rate for more than 10

percent of the total operating time in the 6-month block reporting

period.

As a result of this comment, the EPA examined the other monitoring

provisions and made similar clarifying changes throughout the

monitoring section as they pertain to monitoring frequency and

averaging period.

D. Performance Tests

Comment: One commenter recommended revisions to the monitoring

requirements of Sec. 63.1386(g)(2) to clarify that if changes are made

in the binder formulation that would not result in an increase in HAP

emissions, such as the use of resin extenders, additional emissions

testing is not required. The commenter explained that binder

formulations are developed and controlled centrally by technical

experts at each company and are not subject to modification at each

plant. According to this commenter, normal practice is for any new

binder formulation to be supported by additional emission tests. For

reasons of material availability and cost reduction, the commenter

explained that the binder formulation specification allows some

flexibility for substituting resin extenders. During subsequent

discussions with the commenter, it was explained that extenders replace

components of the binder and that urea and lignin are used as extenders

and replace some of the formaldehyde and phenol in the binder. The

extenders act to dilute the binder and because the rate of application

of the extended binder does not change, the emissions of formaldehyde

and phenol are decreased.

Response: Based on this comment as well as additional information

supplied by the commenter on the use of extenders and their effects on

formaldehyde emissions, the EPA has revised the rule to permit the

addition of the extenders urea and lignin in the binder formulations

without the need to perform additional emission testing.

During discussions to obtain additional information from the

commenter on this issue, the commenter was also concerned that the

occasional switching of resin suppliers where the resins are made to

the same specifications, may be interpreted by enforcement agencies as

a change in resin and require additional emissions testing. The EPA

does not intend for additional emission testing to be performed where a

facility switches resin suppliers as long as the resin from the new

supplier is made to the same product specifications as that used during

the performance test.

VI. Administrative Requirements

A. Docket

The docket is intended to be an organized file of the

administrative records compiled by EPA. The docket is a dynamic file

because information is added throughout the rulemaking development. The

docketing system is intended to allow members of the public and

industries involved to readily identify and locate documents so that

they can effectively participate in the rulemaking process. Along with

the proposed and promulgated standards and their preambles, the docket

will contain the record in case of judicial review. (See section

307(d)(7)(A) of the CAA.) The location of the official rulemaking

record, including all public comments received on the proposed rule, is

in the ADDRESSES section at the beginning of this preamble.

B. Executive Order 12866--Regulatory Planning and Review

Under Executive Order 12866 (58 FR 51735, October 4, 1993), the EPA

must determine if a regulatory action is ``significant,'' and therefore

subject to review by OMB and the requirements of the Executive Order.

The Executive Order defines ``significant regulatory action'' as one

that is likely to result in a rule that may:

(1) Have an annual effect on the economy of $100 million or more or

adversely affect in a material way the economy, a sector of the

economy, productivity, competition, jobs, the environment, public

health or safety, or State, local, or tribal governments or

communities;

(2) Create a serious inconsistency or otherwise interfere with an

action taken or planned by another agency;

(3) Materially alter the budgetary impact of entitlements, grants,

user fees, or loan programs, or the rights and obligation of recipients

thereof; or

(4) Raise novel legal or policy issues arising out of legal

mandates, the President's priorities, or the principles set forth in

the Executive Order.

It has been determined that this final rule is not a ``significant

regulatory action'' under the terms of the Executive Order and is

therefore not subject to OMB review.

C. Executive Order 12875--Enhancing the Intergovernmental Partnership

Under Executive Order 12875, the EPA may not issue a regulation

that is not required by statute and that creates a mandate upon a

State, local or tribal government, unless the Federal government

provides the funds necessary to pay the direct compliance costs

incurred by those governments, or the EPA consults with those

governments. If the EPA complies by consulting, Executive Order 12875

requires the EPA to provide to the OMB a description of the extent of

the EPA's prior consultation with representatives of affected State,

local and tribal governments, the nature of their concerns, copies of

any written

[[Page 31706]]

communications from the governments, and a statement supporting the

need to issue the regulation. In addition, Executive Order 12875

requires the EPA to develop an effective process permitting elected

officials and other representatives of State, local and tribal

governments ``to provide meaningful and timely input in the development

of regulatory proposals containing significant unfunded mandates.''

Today's rule does not create a mandate on State, local or tribal

governments. The rule does not impose any enforceable duties on State,

local or tribal governments, because they do not own or operate any

sources that would be subject to this rule. Accordingly, the

requirements of section 1(a) of Executive Order 12875 do not apply to

this rule.

D. Unfunded Mandates Reform Act

Title II of the Unfunded Mandates Reform Act of 1995 (UMRA), Pub.

L. 104-4, establishes requirements for Federal agencies to assess the

effects of their regulatory actions on State, local, and tribal

governments and the private sector. Under section 202 of the UMRA, the

EPA generally must prepare a written statement, including a cost-

benefit analysis, for proposed and final rules with ``Federal

mandates'' that may result in expenditures by State, local, and tribal

governments, in the aggregate, or by the private sector, of $100

million or more in any one year. Before promulgating an EPA rule for

which a written statement is needed, section 205 of the UMRA generally

requires the EPA to identify and consider a reasonable number of

regulatory alternatives and adopt the least costly, most cost-effective

or least burdensome alternative that achieves the objectives of the

rule. The provisions of section 205 do not apply when they are

inconsistent with applicable law. Moreover, section 205 allows the EPA

to adopt an alternative other than the least costly, most cost-

effective or least burdensome alternative if the Administrator

publishes with the final rule an explanation why that alternative was

not adopted. Before the EPA establishes any regulatory requirements

that may significantly or uniquely affect small governments, it must

have developed under section 203 of the UMRA a small government agency

plan. The plan must provide for notifying potentially affected small

governments, enabling officials of affected small governments to have

meaningful and timely input in the development of EPA regulatory

proposals with significant Federal intergovernmental mandates, and

informing, educating, and advising small governments on compliance with

the regulatory requirements.

The EPA has determined that this rule does not contain a Federal

mandate that may result in expenditures of $100 million or more for

State, local, and tribal governments, in the aggregate, or the private

sector in any one year. The EPA has determined that the total

nationwide capital cost for the standard is approximately $19.5 million

and the annual nationwide cost is approximately $6.3 million/yr. This

rule is based partially on pollution prevention alternatives and on a

manufacturing line approach. It is the least costly and burdensome

approach for industry since the purchase of add-on control devices will

be avoided by most of the industry. The only costs to State and local

governments are those associated with implementing this standard

through the permitting process, and these costs are recouped through

permit fees. Thus, today's rule is not subject to the requirements of

sections 202 and 205 of the UMRA. In addition, the EPA has determined

that this rule contains no regulatory requirements that might

significantly or uniquely affect small governments because it does not

impose any enforceable duties on small governments; such governments

own or operate no sources subject to these rules and therefore would

not be required to purchase control systems to meet the requirements of

the rule.

E. Regulatory Flexibility

The Regulatory Flexibility Act (RFA) generally requires an agency

to conduct a regulatory flexibility analysis of any rule subject to

notice and comment rulemaking requirements unless the agency certifies

that the rule will not have a significant economic impact on a

substantial number of small entities. Small entities include small

businesses, small not-for-profit enterprises, and small governmental

jurisdictions.

EPA has determined that it is not necessary to prepare a regulatory

flexibility analysis in connection with this final rule. EPA has also

determined that this rule will not have a significant impact on a

substantial number of small entities because no company that owns

sources in the source category meets the criteria for small business.

The Small Business Administration defines ``small business,'' as the

term applies to SIC 3296, as a firm with fewer than 750 employees. None

of the firms in the industry have fewer than 750 employees and, thus,

are not small businesses by this criterion.

F. Submission to Congress and the General Accounting Office

The Congressional Review Act, 5 U.S.C. 801 et seq., as added by the

Small Business Regulatory Enforcement Fairness Act of 1996, generally

provides that before a rule may take effect, the agency promulgating

the rule must submit a rule report, which includes a copy of the rule,

to each House of the Congress and to the Comptroller General of the

United States. EPA will submit a report containing this rule and other

required information to the U.S. Senate, the U.S. House of

Representatives, and the Comptroller General of the United States prior

to publication of the rule in the Federal Register. This action is not

a ``major rule'' as defined by 5 U.S.C. 804(2). This rule will be

effective June 14, 1999.

G. Paperwork Reduction Act

The OMB has approved the information collection requirements

contained in this rule under the provisions of the PRA, 44 U.S.C. 3501

et seq. and has assigned OMB control number 2060-0359.

The information collection requirements include the notification,

reporting, and recordkeeping requirements of the NESHAP general

provisions, authorized under section 114 of the CAA, which are

mandatory for all owners or operators subject to national emission

standards. All information submitted to the EPA for which a claim of

confidentiality is made is safeguarded according to Agency policies in

40 CFR part 2, subpart B. This rule does not require any notifications

or reports beyond those required by the general provisions. Subpart NNN

does require additional records of specific information needed to

determine compliance with the rule. These include records of: (1) Any

bag leak detection system alarm, including the date and time, with a

brief explanation of the cause of the alarm and the corrective action

taken; (2) ESP parameter values, such as secondary voltage for each

electrical field including any deviation outside the limits established

during the performance test and a brief explanation of the cause of the

deviation and the corrective action taken; (3) air temperature above

the surface of the molten glass of a cold top electric furnace that

does not use an add-on control device for PM emission control,

including any air temperature above 120 deg.C (250 deg.F) with a

brief explanation of the cause and the corrective action taken; (4)

operating parameter(s) for uncontrolled glass melting furnace (that

[[Page 31707]]

is not a cold top electric furnace) that does not use an add-on control

device for the control of PM emissions including any exceedance of the

level established during the performance test and a brief explanation

of the cause of the exceedance and the corrective action taken; (5) the

free-formaldehyde content of the resin being used; (6) the formulation

of the binder being used; (7) the product LOI and product density for

each 8-hour period on a RS or FA manufacturing line subject to the

NESHAP; (8) forming process modification parameter(s), including any

period when the parameter level(s) deviate from the level(s)

established during the performance test and a brief explanation of the

cause of the deviation and the corrective action taken; (9) pressure

drop, liquid flow rate, and information on chemical additives to the

scrubbing liquid, including any period when there is a deviation from

the levels established during the performance tests and a brief

explanation of the cause and the corrective action taken; (10)

incinerator operating temperature, including any 3-hour block period

when the temperature falls below the level established during the

performance test, and the results of the annual inspection, including

any problems discovered during the inspection, with a brief explanation

of the cause and, the corrective action taken; and (11) glass pull

rate, including any period when the pull rate exceeds the average pull

rate established during the performance test by more than 20 percent,

with a brief explanation of the cause of the exceedance, the corrective

action taken, and the time the corrective action was initiated. All

records documenting corrective actions must include the time of the

alarm, deviation, or exceedance and the time that the corrective action

is initiated as well as when the cause of the alarm, deviation, or

exceedance is corrected. Each of these information requirements is

needed to determine compliance with the standards.

The annual public reporting and recordkeeping burden to industry

for this collection is estimated at 17,100 labor hours per year at an

annual cost of $548,000. This estimate includes a one-time performance

test and report (with repeat tests where needed); one-time preparation

of a startup, shutdown, and malfunction plan with semiannual reports of

any event in which the procedures in the plan were not followed;

semiannual excess emissions reports; notifications; and recordkeeping.

The annualized capital cost associated with monitoring requirements is

estimated at $41,000. The operation and maintenance cost is estimated

at $3,000/yr.

Burden means the total time, effort, or financial resources

expended by persons to generate, maintain, retain, or disclose or

provide information to or for a Federal agency. This includes the time

needed to review instructions; develop, acquire, install, and utilize

technology and systems for the purpose of collecting, validating, and

verifying information, processing and maintaining information, and

disclosing and providing information; adjust the existing ways to

comply with any previously applicable instructions and requirements;

train personnel to be able to respond to a collection of information;

search data sources; complete and review the collection of information;

and transmit or otherwise disclose the information.

An Agency may not conduct or sponsor, and a person is not required

to respond to, a collection of information unless it displays a

currently valid OMB control number. The OMB control numbers for EPA's

regulations are listed in 40 CFR part 9 and 48 CFR chapter 15. The EPA

is amending the table in 40 CFR part 9 of currently approved ICR

control numbers issued by OMB for various regulations to list the

information requirements contained in this final rule.

H. Pollution Prevention Act

The Pollution Prevention Act of 1990 states that pollution should

be prevented or reduced at the source whenever feasible. The emission

standards for RS and FA manufacturing lines subject to the standard are

formulated as line standards, i.e., the sum of the individual forming,

curing, and cooling MACT floor emission levels for RS manufacturing

lines and forming and curing MACT floor emission levels for certain FA

manufacturing lines. By formulating the standard as a line standard,

tradeoffs are allowed for existing facilities that will accomplish the

same environmental results at lower costs and will encourage process

modifications and pollution prevention alternatives. According to the

industry, new RS manufacturing lines may be able to meet the line

standard without the use of costly incinerators with their energy and

other environmental impacts, such as increased nitrogen oxides

(NOX) and sulfur oxides (SOX) emissions, by

incorporating pollution prevention measures, such as binder

reformulation and improved binder application efficiency. Pollution

prevention alternatives will also increase binder utilization

efficiency and reduce production costs for industry. In selecting the

format of the emission standard for emissions from manufacturing lines,

the EPA considered various alternatives such as setting separate

emission limits for each process, i.e., forming, curing, and cooling. A

line standard gives the industry greater flexibility in complying with

the emission limits and is the least costly because industry can avoid

the capital and annual operating and maintenance costs associated with

the purchase of add-on control equipment by using pollution prevention

measures.

I. National Technology Transfer and Advancement Act

Section 12(d) of the National Technology Transfer and Advancement

Act (NTTAA), Pub. L. 104-113 (March 7, 1996), directs the EPA to use

voluntary consensus standards in regulatory and procurement activities

unless to do so would be inconsistent with applicable law or otherwise

impractical. Voluntary consensus standards are technical standards

(such as materials specifications, test methods, sampling procedures,

and business practices) which are developed or adopted by voluntary

consensus standard bodies. Where available and potentially applicable

voluntary consensus standards are not used by EPA, the Act requires the

Agency to provide Congress, through the OMB, an explanation for not

using such standards. This section summarizes the EPA's response to the

requirements of the NTTAA for the analytical test methods promulgated

as part of this final rule.

Consistent with the NTTAA, the EPA conducted searches to identify

voluntary consensus standards for the EPA's emissions sampling and

analysis reference methods and industry recommended materials analysis

procedures cited in this rule. Candidate voluntary consensus standards

for materials analysis were identified for product loss on ignition

(LOI), product density, and free formaldehyde content. Consensus

comments provided by industry experts were that the candidate standards

did not meet industry materials analysis requirements. Therefore, EPA

has determined these voluntary consensus standards were impractical for

the wool fiberglass manufacturing NESHAP. The EPA, in consultation with

the North American Insulation Manufacturers Association (NAIMA), has

formulated industry-specific materials analysis, consensus standards

which are promulgated in this rule.

[[Page 31708]]

The EPA search to identify voluntary consensus standards for the

EPA's emissions sampling and analysis reference methods cited in this

rule identified 17 candidate standards that appeared to have possible

use in lieu of EPA standard reference methods. However, after reviewing

available standards, EPA determined that 12 of the candidate consensus

standards identified for measuring emissions of the HAPs or surrogates

subject to emission standards in the rule would be not be practical due

to lack of equivalency, documentation, validation data and other

important technical and policy considerations. Five of the remaining

candidate consensus standards are new standards under development that

EPA plans to follow, review and consider adopting at a later date. This

rule requires standard EPA emission test methods known to the industry

and States. Approved alternative methods also may be used with prior

EPA approval.

J. Executive Order 13045--Protection of Children From Environmental

Health Risks and Safety Risks

Executive Order 13045 (62 FR 19885, April 23, 1997) applies to any

rule that(1) is determined to be ``economically significant'' as

defined under Executive Order 12866, and (2) concerns the environmental

health or safety risk that the EPA has reason to believe may have a

disproportionate effect on children. If the regulatory action meets

both criteria, the Agency must evaluate the environmental health or

safety effects of the planned rule on children and explain why the

planned regulation is preferable to other potentially effective and

reasonably feasible alternatives considered by the Agency.

The EPA interprets Executive Order 13045 as applying only to those

regulatory actions that are based on health or safety risks, such that

the analysis required under section 5-501 of the Order has the

potential to influence the regulation. This final rule is not subject

to Executive Order 13045 because it is not an economically significant

regulatory action as defined by Executive Order 12866, and it is based

on technology performance and not on health or safety risks.

K. Executive Order 13084--Consultation and Coordination With Indian

Tribal Governments

Under Executive Order 13084, the EPA may not issue a regulation

that is not required by statue, that significantly or uniquely affects

the communities of Indian tribal governments, and that imposes

substantial direct compliance costs on those communities, unless the

Federal government provides the funds necessary to pay the direct

compliance costs incurred by the tribal governments, or the EPA

consults with those governments. If the EPA complies by consulting,

Executive Order 13084 requires the EPA to provide to the OMB, in a

separately identified section of the preamble to the rule, a

description of the extent of EPA's prior consultation with

representatives of affected tribal governments, a summary of the nature

of their concerns, and a statement supporting the need to issue the

regulation. In addition, Executive Order 13084 requires the EPA to

develop an effective process permitting elected officials and other

representatives of Indian tribal governments ``to provide meaningful

and timely input in the development of regulatory policies on matters

that significantly or uniquely affect their communities.''

Today's rule does not significantly or uniquely affect the

communities of Indian tribal governments. No wool fiberglass

manufacturing facilities are owned or operated by Indian tribal

governments. Accordingly, the requirements of section 3(b) of Executive

Order 13084 do not apply to this rule.

List of Subjects

40 CFR Part 9

Environmental protection, Reporting and recordkeeping requirement

40 CFR Part 63

Environmental protection, Air pollution control, Hazardous

substances, Reporting and recordkeeping requirements, Wool fiberglass

manufacturing.

Dated: May 13, 1999.

Carol M. Browner,

Administrator.

For the reasons set out in the preamble, parts 9 and 63 of title

40, chapter I of the Code of Federal Regulations are amended as

follows:

PART 9--OMB APPROVALS UNDER THE PAPERWORK REDUCTION ACT

1. The authority citation for part 9 continues to read as follows:

Authority: 7 U.S.C. 135 et seq., 136-136y; 15 U.S.C. 2001, 2003,

2005, 2006, 2601-2671; 21 U.S.C. 331j, 346a, 348; 31 U.S.C. 9701; 33

U.S.C. 1251 et. seq., 1311, 1313d, 1314, 1318, 1321, 1326, 1330,

1342, 1344, 1345 (d) and (e), 1361; E.O. 11735, 38 FR 21243, 3 CFR,

1971-1975 Comp. p. 973; 42 U.S.C. 241, 242b, 243, 246, 300f, 300g,

300g-1, 300g-2, 300g-3, 300g-4, 300g-5, 300g-6, 300j-1, 300j-2,

300j-3, 300j-4, 300j-9, 1857 et seq., 6901-6992k, 7401-7671q, 7542,

9601-9657, 11023, 11048.

2. In Sec. 9.1, the table is amended by adding new entries in

numerical order under the indicated heading to read as follows:

Sec. 9.1 OMB approvals under the Paperwork Reduction Act.

* * * * *

------------------------------------------------------------------------

OMB control

40 CFR citation No.

------------------------------------------------------------------------

* * * * *

National Emission Standards for Hazardous Air Pollutants for Source

Categories \3\

* * * * *

63.1383.................................................... 2060-0359

63.1386.................................................... 2060-0359

63.1387.................................................... 2060-0359

* * * * *

------------------------------------------------------------------------

\3\ The ICRs referenced in this section of the table encompass the

applicable general provisions contained in 40 CFR part 63, subpart A,

which are not independent information collection requirements.

* * * * *

PART 63--NATIONAL EMISSION STANDARDS FOR HAZARDOUS AIR POLLUTANTS

FOR SOURCE CATEGORIES

3. The authority citation for part 63 continues to read as follows:

Authority: 42 U.S.C. 7401 et seq.

4. Part 63 is amended by adding subpart NNN consisting of

Secs. 63.1380 through 63.1399 to read as follows:

Subpart NNN--National Emission Standards for Hazardous Air Pollutants

for Wool Fiberglass Manufacturing

Sec.

63.1380 Applicability.

63.1381 Definitions.

63.1382 Emission standards.

63.1383 Monitoring requirements.

63.1384 Performance test requirements.

63.1385 Test methods and procedures.

63.1386 Notification, recordkeeping, and reporting requirements.

63.1387 Compliance dates.

63.1388--63.1399 [Reserved]

Table 1 to Subpart NNN of part 63--Applicability of general

provisions (40 CFR part 63, subpart A) to subpart NNN.

Appendix A to Subpart NNN of part 63--Method for the determination

of LOI

Appendix B to Subpart NNN of part 63--Free formaldehyde analysis of

insulation resins by hydroxylamine hydrochloride

Appendix C to Subpart NNN of part 63--Method for the determination

of product density

[[Page 31709]]

Subpart NNN--National Emission Standards for Hazardous Air

Pollutants for Wool Fiberglass Manufacturing

Sec. 63.1380 Applicability.

(a) Except as provided in paragraphs (b) and (c) of this section,

the requirements of this subpart apply to the owner or operator of each

wool fiberglass manufacturing facility that is a major source or is

located at a facility that is a major source.

(b) The requirements of this subpart apply to emissions of

hazardous air pollutants (HAPs), as measured according to the methods

and procedures in this subpart, emitted from the following new and

existing sources at a wool fiberglass manufacturing facility subject to

this subpart:

(1) Each new and existing glass-melting furnace located at a wool

fiberglass manufacturing facility;

(2) Each new and existing rotary spin wool fiberglass manufacturing

line producing a bonded wool fiberglass building insulation product;

and

(3) Each new and existing flame attenuation wool fiberglass

manufacturing line producing a bonded pipe product and each new flame

attenuation wool fiberglass manufacturing line producing a bonded

heavy-density product.

(c) The requirements of this subpart do not apply to a wool

fiberglass manufacturing facility that the owner or operator

demonstrates to the Administrator is not a major source as defined in

Sec. 63.2.

(d) The provisions of this part 63, subpart A that apply and those

that do not apply to this subpart are specified in Table 1 of this

subpart.

Sec. 63.1381 Definitions.

Terms used in this subpart are defined in the Clean Air Act, in

Sec. 63.2, or in this section as follows:

Bag leak detection system means systems that include, but are not

limited to, devices using triboelectric, light scattering, and other

effects to monitor relative or absolute particulate matter (PM)

emissions.

Bonded means wool fiberglass to which a phenol-formaldehyde binder

has been applied.

Building insulation means bonded wool fiberglass insulation, having

a loss on ignition of less than 8 percent and a density of less than 32

kilograms per cubic meter (kg/m3) (2 pounds per cubic foot

[lb/ft3]).

Cold top electric furnace means an all-electric glass-melting

furnace that operates with a temperature of 120 deg.C (250 deg.F) or

less as measured at a location 46 to 61 centimeters (18 to 24 inches)

above the molten glass surface.

Flame attenuation means a process used to produce wool fiberglass

where molten glass flows by gravity from melting furnaces, or pots, to

form filaments that are drawn down and attenuated by passing in front

of a high-velocity gas burner flame.

Glass-melting furnace means a unit comprising a refractory vessel

in which raw materials are charged, melted at high temperature,

refined, and conditioned to produce molten glass. The unit includes

foundations, superstructure and retaining walls, raw material charger

systems, heat exchangers, melter cooling system, exhaust system,

refractory brick work, fuel supply and electrical boosting equipment,

integral control systems and instrumentation, and appendages for

conditioning and distributing molten glass to forming processes. The

forming apparatus, including flow channels, is not considered part of

the glass-melting furnace.

Glass pull rate means the mass of molten glass that is produced by

a single glass-melting furnace or that is used in the manufacture of

wool fiberglass at a single manufacturing line in a specified time

period.

Hazardous Air Pollutant (HAP) means any air pollutant listed in or

pursuant to section 112(b) of the Clean Air Act.

Heavy-density product means bonded wool fiberglass insulation

manufactured on a flame attenuation manufacturing line and having a

loss on ignition of 11 to 25 percent and a density of 8 to 48 kg/m\3\

(0.5 to 3 lb/ft \3\).

Incinerator means an enclosed air pollution control device that

uses controlled flame combustion to convert combustible materials to

noncombustible gases.

Loss on ignition (LOI) means the percent decrease in weight of wool

fiberglass after it has been ignited. The LOI is used to monitor the

weight percent of binder in wool fiberglass.

Manufacturing line means the manufacturing equipment for the

production of wool fiberglass that consists of a forming section where

molten glass is fiberized and a fiberglass mat is formed and which may

include a curing section where binder resin in the mat is thermally set

and a cooling section where the mat is cooled.

New source means any affected source the construction or

reconstruction of which is commenced after March 31, 1997.

Pipe product means bonded wool fiberglass insulation manufactured

on a flame attenuation manufacturing line and having a loss on ignition

of 8 to 14 percent and a density of 48 to 96 kg/m \3\ (3 to 6 lb/

ft\3\).

Rotary spin means a process used to produce wool fiberglass

building insulation by forcing molten glass through numerous small

orifices in the side wall of a spinner to form continuous glass fibers

that are then broken into discrete lengths by high-velocity air flow.

Any process used to produce bonded wool fiberglass building insulation

by a process other than flame attenuation is considered rotary spin.

Wool fiberglass means insulation materials composed of glass fibers

made from glass produced or melted at the same facility where the

manufacturing line is located.

Wool fiberglass manufacturing facility means any facility

manufacturing wool fiberglass on a rotary spin manufacturing line or on

a flame attenuation manufacturing line.

Sec. 63.1382 Emission standards

(a) Emission limits--(1) Glass-melting furnaces. On and after the

date the initial performance test is completed or required to be

completed under Sec. 63.7 of this part, whichever date is earlier, the

owner or operator shall not discharge or cause to be discharged into

the atmosphere in excess of 0.25 kilogram (kg) of particulate matter

(PM) per megagram (Mg) (0.5 pound [lb] of PM per ton) of glass pulled

for each new or existing glass-melting furnace.

(2) Rotary spin manufacturing lines. On and after the date the

initial performance test is completed or required to be completed under

Sec. 63.7 of this part, whichever date is earlier, the owner or

operator shall not discharge or cause to be discharged into the

atmosphere in excess of:

(i) 0.6 kg of formaldehyde per megagram (1.2 lb of formaldehyde per

ton) of glass pulled for each existing rotary spin manufacturing line;

and

(ii) 0.4 kg of formaldehyde per megagram (0.8 lb of formaldehyde

per ton) of glass pulled for each new rotary spin manufacturing line.

(3) Flame attenuation manufacturing lines. On and after the date

the initial performance test is completed or required to be completed

under Sec. 63.7 of this part, whichever date is earlier, the owner or

operator shall not discharge or cause to be discharged into the

atmosphere in excess of:

(i) 3.9 kg of formaldehyde per megagram (7.8 lb of formaldehyde per

ton) of glass pulled for each new flame attenuation manufacturing line

that produces heavy-density wool fiberglass; and

(ii) 3.4 kg of formaldehyde per megagram (6.8 lb of formaldehyde

per ton) of glass pulled from each existing

[[Page 31710]]

or new flame attenuation manufacturing line that produces pipe product

wool fiberglass.

(b) Operating limits. On and after the date on which the

performance test required to be conducted by Secs. 63.7 and 63.1384 is

completed, the owner or operator must operate all affected control

equipment and processes according to the following requirements.

(1)(i) The owner or operator must initiate corrective action within

1 hour of an alarm from a bag leak detection system and complete

corrective actions in a timely manner according to the procedures in

the operations, maintenance, and monitoring plan.

(ii) The owner or operator must implement a Quality Improvement

Plan (QIP) consistent with the compliance assurance monitoring

provisions of 40 CFR part 64, subpart D when the bag leak detection

system alarm is sounded for more than 5 percent of the total operating

time in a 6-month block reporting period.

(2)(i) The owner or operator must initiate corrective action within

1 hour when any 3-hour block average of the monitored electrostatic

precipitator (ESP) parameter is outside the limit(s) established during

the performance test as specified in Sec. 63.1384 and complete

corrective actions in a timely manner according to the procedures in

the operations, maintenance, and monitoring plan.

(ii) The owner or operator must implement a QIP consistent with the

compliance assurance monitoring provisions of 40 CFR part 64 subpart D

when the monitored ESP parameter is outside the limit(s) established

during the performance test as specified in Sec. 63.1384 for more than

5 percent of the total operating time in a 6-month block reporting

period.

(iii) The owner or operator must operate the ESP such that the

monitored ESP parameter is not outside the limit(s) established during

the performance test as specified in Sec. 63.1384 for more than 10

percent of the total operating time in a 6-month block reporting

period.

(3)(i) The owner or operator must initiate corrective action within

1 hour when any 3-hour block average temperature of a cold top electric

furnace as measured at a location 46 to 61 centimeters (18 to 24

inches) above the molten glass surface, exceeds 120 deg.C (250 deg.F)

and complete corrective actions in a timely manner according to the

procedures in the operations, maintenance, and monitoring plan.

(ii) The owner or operator of a cold top electric furnace must

implement a QIP consistent with the compliance assurance monitoring

provisions of 40 CFR part 64, subpart D when the temperature, as

measured at a location 46 to 61 centimeters (18 to 24 inches) above the

molten glass surface, exceeds 120 deg.C (250 deg.F) for more than 5

percent of the total operating time in a 6-month block reporting

period.

(iii) The owner or operator must operate the cold top electric

furnace such that the temperature does not exceed 120 deg.C (250

deg.F) as measured at a location 46 to 61 centimeters (18 to 24 inches)

above the molten glass surface, for more than 10 percent of the total

operating time in a 6-month reporting period.

(4)(i) The owner or operator must initiate corrective action within

1 hour when any 3-hour block average value for the monitored

parameter(s) for a glass-melting furnace, which uses no add-on controls

and which is not a cold top electric furnace, is outside the limit(s)

established during the performance test as specified in Sec. 63.1384

and complete corrective actions in a timely manner according to the

procedures in the operations, maintenance, and monitoring plan.

(ii) The owner or operator must implement a QIP consistent with the

compliance assurance monitoring provisions of 40 CFR Part 64 subpart D

when the monitored parameter(s) is outside the limit(s) established

during the performance test as specified in Sec. 63.1384 for more than

5 percent of the total operating time in a 6-month block reporting

period.

(iii) The owner or operator must operate a glass-melting furnace,

which uses no add-on controls and which is not a cold top electric

furnace, such that the monitored parameter(s) is not outside the

limit(s) established during the performance test as specified in

Sec. 63.1384 for more than 10 percent of the total operating time in a

6-month block reporting period.

(5)(i) The owner or operator must initiate corrective action within

1 hour when the average glass pull rate of any 4-hour block period for

glass melting furnaces equipped with continuous glass pull rate

monitors, or daily glass pull rate for glass melting furnaces not so

equipped, exceeds the average glass pull rate established during the

performance test as specified in Sec. 63.1384, by greater than 20

percent and complete corrective actions in a timely manner according to

the procedures in the operations, maintenance, and monitoring plan.

(ii) The owner or operator must implement a QIP consistent with the

compliance assurance monitoring provisions of 40 CFR part 64, subpart D

when the glass pull rate exceeds, by more than 20 percent, the average

glass pull rate established during the performance test as specified in

Sec. 63.1384 for more than 5 percent of the total operating time in a

6-month block reporting period.

(iii) The owner or operator must operate each glass-melting furnace

such that the glass pull rate does not exceed, by more than 20 percent,

the average glass pull rate established during the performance test as

specified in Sec. 63.1384 for more than 10 percent of the total

operating time in a 6-month block reporting period.

(6) The owner or operator must operate each incinerator used to

control formaldehyde emissions from forming or curing such that any 3-

hour block average temperature in the firebox does not fall below the

average established during the performance test as specified in

Sec. 63.1384.

(7)(i) The owner or operator must initiate corrective action within

1 hour when the average pressure drop, liquid flow rate, or chemical

feed rate for any 3-hour block period is outside the limits established

during the performance tests as specified in Sec. 63.1384 for each wet

scrubbing control device and complete corrective actions in a timely

manner according to the procedures in the operations, maintenance, and

monitoring plan.

(ii) The owner or operator must implement a QIP consistent with the

compliance assurance monitoring provisions of 40 CFR part 64, subpart D

when any scrubber parameter is outside the limit(s) established during

the performance test as specified in Sec. 63.1384 for more than 5

percent of the total operating time in a 6-month block reporting

period.

(iii) The owner or operator must operate each scrubber such that

each monitored parameter is not outside the limit(s) established during

the performance test as specified in Sec. 63.1384 for more than 10

percent of the total operating time in a 6-month block reporting

period.

(8)(i) The owner or operator must initiate corrective action within

1 hour when the monitored process parameter level(s) is outside the

limit(s) established during the performance test as specified in

Sec. 63.1384 for the process modification(s) used to control

formaldehyde emissions and complete corrective actions in a timely

manner according to the procedures in the operations, maintenance, and

monitoring plan.

(ii) The owner or operator must implement a QIP consistent with the

compliance assurance monitoring provisions of 40 CFR part 64, subpart D

[[Page 31711]]

when the process parameter(s) is outside the limit(s) established

during the performance test as specified in Sec. 63.1384 for more than

5 percent of the total operating time in a 6-month block reporting

period.

(iii) The owner or operator must operate the process modifications

such that the monitored process parameter(s) is not outside the

limit(s) established during the performance test as specified in

Sec. 63.1384 for more than 10 percent of the total operating time in a

6-month block reporting period.

(9) The owner or operator must use a resin in the formulation of

binder such that the free-formaldehyde content of the resin used does

not exceed the free-formaldehyde range contained in the specification

for the resin used during the performance test as specified in

Sec. 63.1384.

(10) The owner or operator must use a binder formulation that does

not vary from the specification and operating range established and

used during the performance test as specified in Sec. 63.1384. For the

purposes of this standard, adding or increasing the quantity of urea

and/or lignin in the binder formulation does not constitute a change in

the binder formulation.

Sec. 63.1383 Monitoring requirements.

On and after the date on which the performance test required to be

conducted by Secs. 63.7 and 63.1384 is completed, the owner or operator

must monitor all affected control equipment and processes according to

the following requirements.

(a) The owner or operator of each wool fiberglass manufacturing

facility must prepare for each glass-melting furnace, rotary spin

manufacturing line, and flame attenuation manufacturing line subject to

the provisions of this subpart, a written operations, maintenance, and

monitoring plan. The plan must be submitted to the Administrator for

review and approval as part of the application for a part 70 permit.

The plan must include the following information:

(1) Procedures for the proper operation and maintenance of process

modifications and add-on control devices used to meet the emission

limits in Sec. 63.1382;

(2) Procedures for the proper operation and maintenance of

monitoring devices used to determine compliance, including quarterly

calibration and certification of accuracy of each monitoring device

according to the manufacturers's instructions; and

(3) Corrective actions to be taken when process parameters or add-

on control device parameters deviate from the limit(s) established

during initial performance tests.

(b)(1) Where a baghouse is used to control PM emissions from a

glass-melting furnace, the owner or operator shall install, calibrate,

maintain, and continuously operate a bag leak detection system.

(i) The bag leak detection system must be certified by the

manufacturer to be capable of detecting PM emissions at concentrations

of 10 milligrams per actual cubic meter (0.0044 grains per actual cubic

foot) or less.

(ii) The bag leak detection system sensor must produce output of

relative PM emissions.

(iii) The bag leak detection system must be equipped with an alarm

system that will sound automatically when an increase in relative PM

emissions over a preset level is detected and the alarm must be located

such that it can be heard by the appropriate plant personnel.

(iv) For positive pressure fabric filter systems, a bag leak

detection system must be installed in each baghouse compartment or

cell. If a negative pressure or induced air baghouse is used, the bag

leak detection system must be installed downstream of the baghouse.

Where multiple bag leak detection systems are required (for either type

of baghouse), the system instrumentation and alarm may be shared among

the monitors.

(v) A triboelectric bag leak detection system shall be installed,

operated, adjusted, and maintained in a manner consistent with the U.S.

Environmental Protection Agency guidance, ``Fabric Filter Bag Leak

Detection Guidance'' (EPA-454/R-98-015, September 1997). Other bag leak

detection systems shall be installed, operated, adjusted, and

maintained in a manner consistent with the manufacturer's written

specifications and recommendations.

(vi) Initial adjustment of the system shall, at a minimum, consist

of establishing the baseline output by adjusting the range and the

averaging period of the device and establishing the alarm set points

and the alarm delay time.

(vii) Following the initial adjustment, the owner or operator shall

not adjust the range, averaging period, alarm setpoints, or alarm delay

time except as detailed in the approved operations, maintenance, and

monitoring plan required under paragraph (a) of this section. In no

event shall the range be increased by more than 100 percent or

decreased more than 50 percent over a 365-day period unless a

responsible official as defined in Sec. 63.2 of the general provisions

in subpart A of this part certifies that the baghouse has been

inspected and found to be in good operating condition.

(2) The operations, maintenance, and monitoring plan required by

paragraph (a) of this section must specify corrective actions to be

followed in the event of a bag leak detection system alarm. Example

corrective actions that may be included in the plan include the

following:

(i) Inspecting the baghouse for air leaks, torn or broken bags or

filter media, or any other conditions that may cause an increase in

emissions.

(ii) Sealing off defective bags or filter media.

(iii) Replacing defective bags or filter media, or otherwise

repairing the control device.

(iv) Sealing off a defective baghouse compartment.

(v) Cleaning the bag leak detection system probe, or otherwise

repairing the bag leak detection system.

(vi) Shutting down the process producing the particulate emissions.

(c)(1) Where an ESP is used to control PM emissions from a glass-

melting furnace, the owner or operator must monitor the ESP according

to the procedures in the operations, maintenance, and monitoring plan.

(2)The operations, maintenance, and monitoring plan for the ESP must

contain the following information:

(i) The ESP operating parameter(s), such as secondary voltage of

each electrical field, to be monitored and the minimum and/or maximum

value(s) that will be used to identify any operational problems;

(ii) A schedule for monitoring the ESP operating parameter(s);

(iii) Recordkeeping procedures, consistent with the recordkeeping

requirements of Sec. 63.1386, to show that the ESP operating

parameter(s) is within the limit(s) established during the performance

test; and

(iv) Procedures for the proper operation and maintenance of the

ESP.

(d) The owner or operator must measure and record at least once per

shift the temperature 46 to 61 centimeters (18 to 24 inches) above the

surface of the molten glass in a cold top electric furnace that does

not use any add-on controls to control PM emissions.

(e)(1) Where a glass-melting furnace is operated without an add-on

control device to control PM emissions, the owner or operator must

monitor the glass-melting furnace according to the procedures in the

operations, maintenance, and monitoring plan.

(2) The operations, maintenance, and monitoring plan for the glass-

melting

[[Page 31712]]

furnace must contain the following information:

(i) The operating parameter(s) to be monitored and the minimum and/

or maximum value(s) that will be used to identify any operational

problems;

(ii) A schedule for monitoring the operating parameter(s) of the

glass-melting furnace;

(iii) Recordkeeping procedures, consistent with the recordkeeping

requirements of Sec. 63.1386, to show that the glass-melting furnace

parameter(s) is within the limit(s) established during the performance

test; and

(iv) Procedures for the proper operation and maintenance of the

glass-melting furnace.

(f)(1) The owner or operator of an existing glass-melting furnace

equipped with continuous glass pull rate monitors must monitor and

record the glass pull rate on an hourly basis. For glass-melting

furnaces that are not equipped with continuous glass pull rate

monitors, the glass pull rate must be monitored and recorded once per

day.

(2) On any new glass-melting furnace, the owner or operator must

install, calibrate, and maintain a continuous glass pull rate monitor

that monitors and records on an hourly basis the glass pull rate.

(g)(1) The owner or operator who uses an incinerator to control

formaldehyde emissions from forming or curing shall install, calibrate,

maintain, and operate a monitoring device that continuously measures

and records the operating temperature in the firebox of each

incinerator.

(2) The owner or operator must inspect each incinerator at least

once per year according to the procedures in the operations,

maintenance, and monitoring plan. At a minimum, an inspection must

include the following:

(i) Inspect all burners, pilot assemblies, and pilot sensing

devices for proper operation and clean pilot sensor, as necessary;

(ii) Ensure proper adjustment of combustion air and adjust, as

necessary;

(iii) Inspect, when possible, internal structures, for example,

baffles, to ensure structural integrity per the design specifications;

(iv) Inspect dampers, fans, and blowers for proper operation;

(v) Inspect for proper sealing;

(vi) Inspect motors for proper operation;

(vii) Inspect combustion chamber refractory lining and clean and

repair/replace lining, as necessary;

(viii) Inspect incinerator shell for corrosion and/or hot spots;

(ix) For the burn cycle that follows the inspection, document that

the incinerator is operating properly and make any necessary

adjustments; and

(x) Generally observe that the equipment is maintained in good

operating condition.

(xi) Complete all necessary repairs as soon as practicable.

(h) The owner or operator who uses a wet scrubbing control device

to control formaldehyde emissions must install, calibrate, maintain,

and operate monitoring devices that continuously monitor and record the

gas pressure drop across each scrubber and scrubbing liquid flow rate

to each scrubber according to the procedures in the operations,

maintenance, and monitoring plan. The pressure drop monitor is to be

certified by its manufacturer to be accurate within 250

pascals (1 inch water gauge) over its operating range, and

the flow rate monitor is to be certified by its manufacturer to be

accurate within 5 percent over its operating range. The

owner or operator must also continuously monitor and record the feed

rate of any chemical(s) added to the scrubbing liquid.

(i)(1) The owner or operator who uses process modifications to

control formaldehyde emissions must establish a correlation between

formaldehyde emissions and a process parameter(s) to be monitored.

(2) The owner or operator must monitor the established parameter(s)

according to the procedures in the operations, maintenance, and

monitoring plan.

(3)The owner or operator must include as part of their operations,

maintenance, and monitoring plan the following information:

(i) Procedures for the proper operation and maintenance of the

process;

(ii) Process parameter(s) to be monitored to demonstrate compliance

with the applicable emission limits in Sec. 63.1382. Examples of

process parameters include LOI, binder solids content, and binder

application rate;

(iii) Correlation(s) between process parameter(s) to be monitored

and formaldehyde emissions;

(iv) A schedule for monitoring the process parameter(s); and

(v) Recordkeeping procedures, consistent with the recordkeeping

requirements of Sec. 63.1386, to show that the process parameter

value(s) established during the performance test is not exceeded.

(j) The owner or operator must monitor and record the free-

formaldehyde content of each resin shipment received and used in the

formulation of binder.

(k) The owner or operator must monitor and record the formulation

of each batch of binder used.

(l) The owner or operator must monitor and record at least once

every 8 hours, the product LOI and product density of each bonded wool

fiberglass product manufactured.

(m) For all control device and process operating parameters

measured during the initial performance tests, the owners or operators

of glass-melting furnaces, rotary spin manufacturing lines or flame

attenuation manufacturing lines subject to this subpart may change the

limits established during the initial performance tests if additional

performance testing is conducted to verify that, at the new control

device or process parameter levels, they comply with the applicable

emission limits in Sec. 63.1382. The owner or operator shall conduct

all additional performance tests according to the procedures in this

part 63, subpart A and in Sec. 63.1384.

Sec. 63.1384 Performance test requirements.

(a) The owner or operator subject to the provisions of this subpart

shall conduct a performance test to demonstrate compliance with the

applicable emission limits in Sec. 63.1382. Compliance is demonstrated

when the emission rate of the pollutant is equal to or less than each

of the applicable emission limits in Sec. 63.1382. The owner or

operator shall conduct the performance test according to the procedures

in 40 CFR part 63, subpart A and in this section.

(1) All monitoring systems and equipment must be installed,

operational, and calibrated prior to the performance test.

(2) Unless a different frequency is specified in this section, the

owner or operator must monitor and record process and/or add-on control

device parameters at least every 15 minutes during the performance

tests. The arithmetic average for each parameter must be calculated

using all of the recorded measurements for the parameter.

(3) During each performance test, the owner or operator must

monitor and record the glass pull rate for each glass-melting furnace

and, if different, the glass pull rate for each rotary spin

manufacturing line and flame attenuation manufacturing line. Record the

glass pull rate every 15 minutes during any performance test required

by this subpart and determine the arithmetic average of the recorded

measurements for each test run and calculate the average of the three

test runs.

[[Page 31713]]

(4) The owner or operator shall conduct a performance test for each

existing and new glass-melting furnace.

(5) During the performance test, the owner or operator of a glass-

melting furnace controlled by an ESP shall monitor and record the ESP

parameter level(s), as specified in the operations, maintenance, and

monitoring plan, and establish the minimum and/or maximum value(s) that

will be used to demonstrate compliance after the initial performance

test.

(6) During the performance test, the owner or operator of a cold

top electric furnace that is not equipped with an add-on control device

for PM emissions control, must monitor and record the temperature 46 to

61 centimeters (18 to 24 inches) above the molten glass surface to

ensure that the maximum temperature does not exceed 120 deg.C (250

deg.F).

(7) During the performance test, the owner or operator of a glass

melting furnace (other than a cold top electric furnace) that is not

equipped with an add-on control device for PM emissions control, must

monitor and record the furnace parameter level, and establish the

minimum and/or maximum value(s) that will be used to demonstrate

compliance after the initial performance test.

(8) The owner or operator must conduct a performance test for each

rotary spin manufacturing line, subject to this subpart, while

producing the building insulation with the highest LOI expected to be

produced on that line; and for each flame attenuation manufacturing

line, subject to this subpart, while producing the heavy-density

product or pipe product with the highest LOI expected to be produced on

the affected line.

(9) The owner or operator of each rotary spin manufacturing line

and flame attenuation manufacturing line regulated by this subpart must

conduct performance tests using the resin with the highest free-

formaldehyde content. During the performance test of each rotary spin

manufacturing line and flame attenuation manufacturing line regulated

by this subpart, the owner or operator shall monitor and record the

free-formaldehyde content of the resin, the binder formulation used,

and the product LOI and density.

(10) During the performance test, the owner or operator of a rotary

spin manufacturing line or flame attenuation manufacturing line who

plans to use process modifications to comply with the emission limits

in Sec. 63.1382 must monitor and record the process parameter level(s),

as specified in the operations, maintenance, and monitoring plan, which

will be used to demonstrate compliance after the initial performance

test.

(11) During the performance test, the owner or operator of a rotary

spin manufacturing line or flame attenuation manufacturing line who

plans to use a wet scrubbing control device to comply with the emission

limits in Sec. 63.1382 must continuously monitor and record the

pressure drop across the scrubber, the scrubbing liquid flow rate, and

addition of any chemical to the scrubber, including the chemical feed

rate, and establish the minimum and/or maximum value(s) that will be

used to determine compliance after the initial performance test.

(12) During the performance test, the owner or operator of a rotary

spin manufacturing line or affected flame attenuation manufacturing

line shall continuously record the operating temperature of each

incinerator and record the average during each 1-hour test; the average

operating temperature of the three 1-hour tests shall be used to

monitor compliance.

(13) Unless disapproved by the Administrator, an owner or operator

of a rotary spin or flame attenuation manufacturing line regulated by

this subpart may conduct short-term experimental production runs using

binder formulations or other process modifications where the process

parameter values would be outside those established during performance

tests without first conducting performance tests. Such runs must not

exceed 1 week in duration unless the Administrator approves a longer

period. The owner or operator must notify the Administrator and

postmark or deliver the notification at least 15 days prior to

commencement of the short-term experimental production runs. The

Administrator must inform the owner or operator of a decision to

disapprove or must request additional information prior to the date of

the short-term experimental production runs. Notification of intent to

perform an experimental short-term production run shall include the

following information:

(i) The purpose of the experimental production run;

(ii) The affected line;

(iii) How the established process parameters will deviate from

previously approved levels;

(iv) The duration of the experimental production run;

(v) The date and time of the experimental production run; and

(vi) A description of any emission testing to be performed during

the experimental production run.

(b) To determine compliance with the PM emission limit for glass-

melting furnaces, use the following equation:

[GRAPHIC] [TIFF OMITTED] TR14JN99.040

Where:

E = Emission rate of PM, kg/Mg (lb/ton) of glass pulled;

C = Concentration of PM, g/dscm

(gr/dscf);

Q = Volumetric flow rate of exhaust gases, dscm/h (dscf/h);

K1 = Conversion factor, 1 kg/1,000 g (1 lb/7,000 gr); and

P = Average glass pull rate, Mg/h (tons/h).

(c) To determine compliance with the emission limit for

formaldehyde for rotary spin manufacturing lines and flame attenuation

forming processes, use the following equation:

[GRAPHIC] [TIFF OMITTED] TR14JN99.041

Where:

E = Emission rate of formaldehyde, kg/Mg (lb/ton) of glass pulled;

C = Measured volume fraction of formaldehyde, ppm;

MW = Molecular weight of formaldehyde, 30.03 g/g-mol;

Q = Volumetric flow rate of exhaust gases, dscm/h (dscf/h);

K1 = Conversion factor, 1 kg/1,000 g (1 lb/453.6 g);

K2 = Conversion factor, 1,000 L/m3 (28.3 L/

ft3);

K3 = Conversion factor, 24.45 L/g-mol; and

P = Average glass pull rate, Mg/h (tons/h).

Sec. 63.1385 Test methods and procedures.

(a) The owner or operator shall use the following methods to

determine compliance with the applicable emission limits:

(1) Method 1 (40 CFR part 60, appendix A) for the selection of the

sampling port location and number of sampling ports;

(2) Method 2 (40 CFR part 60, appendix A) for volumetric flow rate;

(3) Method 3 or 3A (40 CFR part 60, appendix A) for O2

and CO2 for diluent measurements needed to correct the

concentration measurements to a standard basis;

(4) Method 4 (40 CFR part 60, appendix A) for moisture content of

the stack gas;

(5) Method 5 (40 CFR part 60, appendix A) for the concentration of

PM. Each run shall consist of a minimum run time of 2 hours and a

minimum sample volume of 60 dry standard cubic feet (dscf). The probe

[[Page 31714]]

and filter holder heating system may be set to provide a gas

temperature no greater than 177 14 deg.C (350

25 deg.F);

(6) Method 316 or Method 318 (appendix A of this part) for the

concentration of formaldehyde. Each run shall consist of a minimum run

time of 1 hour;

(7) Method contained in appendix A of this subpart for the

determination of product LOI;

(8) Method contained in appendix B of this subpart for the

determination of the free-formaldehyde content of resin;

(9) Method contained in appendix C of this subpart for the

determination of product density;

(10) An alternative method, subject to approval by the

Administrator.

(b) Each performance test shall consist of 3 runs. The owner or

operator shall use the average of the three runs in the applicable

equation for determining compliance.

Sec. 63.1386 Notification, recordkeeping, and reporting requirements.

(a) Notifications. As required by Sec. 63.9(b) through (h) of this

part, the owner or operator shall submit the following written initial

notifications to the Administrator:

(1) Notification for an area source that subsequently increases its

emissions such that the source is a major source subject to the

standard;

(2) Notification that a source is subject to the standard, where

the initial startup is before June 14, 2002.

(3) Notification that a source is subject to the standard, where

the source is new or has been reconstructed, the initial startup is

after June 14, 2002, and for which an application for approval of

construction or reconstruction is not required;

(4) Notification of intention to construct a new major source or

reconstruct a major source; of the date construction or reconstruction

commenced; of the anticipated date of startup; of the actual date of

startup, where the initial startup of a new or reconstructed source

occurs after June 14, 2002, and for which an application for approval

or construction or reconstruction is required (See Sec. 63.9(b)(4) and

(5) of this part);

(5) Notification of special compliance obligations;

(6) Notification of performance test; and (7) Notification of

compliance status.

(b) Performance test report. As required by Sec. 63.10(d)(2) of the

general provisions, the owner or operator shall report the results of

the initial performance test as part of the notification of compliance

status required in paragraph (a)(7) of this section.

(c) Startup, shutdown, and malfunction plan and reports. (1) The

owner or operator shall develop and implement a written plan as

described in Sec. 63.6(e)(3) of this part that contains specific

procedures to be followed for operating the source and maintaining the

source during periods of startup, shutdown, and malfunction and a

program of corrective action for malfunctioning process modifications

and control systems used to comply with the standard. In addition to

the information required in Sec. 63.6(e)(3), the plan shall include:

(i) Procedures to determine and record the cause of the malfunction

and the time the malfunction began and ended;

(ii) Corrective actions to be taken in the event of a malfunction

of a control device or process modification, including procedures for

recording the actions taken to correct the malfunction or minimize

emissions; and

(iii) A maintenance schedule for each control device and process

modification that is consistent with the manufacturer's instructions

and recommendations for routine and long-term maintenance.

(2) The owner or operator shall also keep records of each event as

required by Sec. 63.10(b) of this part and record and report if an

action taken during a startup, shutdown, or malfunction is not

consistent with the procedures in the plan as described in

Sec. 63.10(e)(3)(iv) of this part.

(d) Recordkeeping. (1) As required by Sec. 63.10(b) of this part,

the owner or operator shall maintain files of all information

(including all reports and notifications) required by the general

provisions and this subpart:

(i) The owner or operator must retain each record for at least 5

years following the date of each occurrence, measurement, maintenance,

corrective action, report, or record. The most recent 2 years of

records must be retained at the facility. The remaining 3 years of

records may be retained off site;

(ii) The owner or operator may retain records on microfilm, on a

computer, on computer disks, on magnetic tape, or on microfiche; and

(iii) The owner or operator may report required information on

paper or on a labeled computer disk using commonly available and EPA-

compatible computer software.

(2) In addition to the general records required by Sec. 63.10(b)(2)

of this part, the owner or operator shall maintain records of the

following information:

(i) Any bag leak detection system alarms, including the date and

time of the alarm, when corrective actions were initiated, the cause of

the alarm, an explanation of the corrective actions taken, and when the

cause of the alarm was corrected;

(ii) ESP parameter value(s) used to monitor ESP performance,

including any period when the value(s) deviated from the established

limit(s), the date and time of the deviation, when corrective actions

were initiated, the cause of the deviation, an explanation of the

corrective actions taken, and when the cause of the deviation was

corrected;

(iii) Air temperature above the molten glass in an uncontrolled

cold top electric furnace, including any period when the temperature

exceeded 120 deg.C (250 deg.F) at a location 46 to 61 centimeters (18

to 24 inches) above the molten glass surface, the date and time of the

exceedance, when corrective actions were initiated, the cause of the

exceedance, an explanation of the corrective actions taken, and when

the cause of the exceedance was corrected;

(iv) Uncontrolled glass-melting furnace (that is not a cold top

electric furnace) parameter value(s) used to monitor furnace

performance, including any period when the value(s) exceeded the

established limit(s), the date and time of the exceedance, when

corrective actions were initiated, the cause of the exceedance, an

explanation of the corrective actions taken, and when the cause of the

exceedance was corrected;

(v) The formulation of each binder batch and the LOI and density

for each product manufactured on a rotary spin manufacturing line or

flame attenuation manufacturing line subject to the provisions of this

subpart, and the free formaldehyde content of each resin shipment

received and used in the binder formulation;

(vi) Process parameter level(s) for RS and FA manufacturing lines

that use process modifications to comply with the emission limits,

including any period when the parameter level(s) deviated from the

established limit(s), the date and time of the deviation, when

corrective actions were initiated, the cause of the deviation, an

explanation of the corrective actions taken, and when the cause of the

deviation was corrected;

(vii) Scrubber pressure drop, scrubbing liquid flow rate, and any

chemical additive (including chemical feed rate to the scrubber),

including any period when a parameter level(s) deviated from the

established limit(s), the date and time of the deviation, when

corrective actions were initiated, the cause of the deviation, an

explanation of

[[Page 31715]]

the corrective actions taken, and when the cause of the deviation was

corrected;

(viii) Incinerator operating temperature and results of periodic

inspection of incinerator components, including any period when the

temperature fell below the established average or the inspection

identified problems with the incinerator, the date and time of the

problem, when corrective actions were initiated, the cause of the

problem, an explanation of the corrective actions taken, and when the

cause of the problem was corrected;

(ix) Glass pull rate, including any period when the pull rate

exceeded the average pull rate established during the performance test

by more than 20 percent, the date and time of the exceedance, when

corrective actions were initiated, the cause of the exceedance, an

explanation of the corrective actions taken, and when the cause of the

exceedance was corrected.

(e) Excess emissions report. As required by Sec. 63.10(e)(3)(v) of

this part, the owner or operator shall report semiannually if measured

emissions are in excess of the applicable standard or a monitored

parameter deviates from the levels established during the performance

test. The report shall contain the information specified in

Sec. 63.10(c) of this part as well as the additional records required

by the recordkeeping requirements of paragraph (d) of this section.

When no deviations have occurred, the owner or operator shall submit a

report stating that no excess emissions occurred during the reporting

period.

Sec. 63.1387 Compliance dates.

(a) Compliance dates. The owner or operator subject to the

provisions of this subpart shall demonstrate compliance with the

requirements of this subpart by no later than:

(1) June 14, 2002, for an existing glass-melting furnace, rotary

spin manufacturing line, or flame attenuation manufacturing line; or

(2) Upon startup for a new glass-melting furnace, rotary spin

manufacturing line, or flame attenuation manufacturing line.

(b) Compliance extension. The owner or operator of an existing

source subject to this subpart may request from the Administrator an

extension of the compliance date for the emission standards for one

additional year if such additional period is necessary for the

installation of controls. The owner or operator shall submit a request

for an extension according to the procedures in Sec. 63.6(i)(3) of this

part.

Secs. 63.1388--63.1399 [Reserved]

Table 1 to Subpart NNN of Part 63.--Applicability of General Provisions (40 CFR Part 63, Subpart A) to Subpart NNN

--------------------------------------------------------------------------------------------------------------------------------------------------------

Applies to subpart

General provisions citation Requirement NNN Explanation

--------------------------------------------------------------------------------------------------------------------------------------------------------

63.1(a)(1)-(a)(4)............... Applicability........... Yes.

63.1(a)(5)...................... ........................ No.................. [Reserved].

63.1(a)(6)-(a)(8)............... ........................ Yes.

63.1(a)(9)...................... ........................ No.................. [Reserved].

63.1(a)(10)-(a)(14)............. ........................ Yes.

63.1(b)(1)-(b)(3)............... Initial Applicability Yes.

Determination.

63.1(c)(1)-(c)(2)............... Applicability After Yes.

Standard Established.

63.1(c)(3)...................... ........................ No.................. [Reserved].

63.1(c)(4)-(c)(5)............... ........................ Yes.

63.1(d)......................... ........................ No.................. [Reserved].

63.1(e)......................... Applicability of Permit Yes.

Program.

63.2............................ Definitions............. Yes................. Additional definitions in Sec. 63.1381.

63.3(a)-(c)..................... Units and Abbreviations. Yes.

63.4(a)(1)-(a)(3)............... Prohibited Activities... Yes.

63.4(a)(4)...................... ........................ No.................. [Reserved].

63.4(a)(5)...................... ........................ Yes.

63.4(b)-(c)..................... ........................ Yes.

63.5(a)(1)-(a)(2)............... Construction/ Yes.

Reconstruction.

63.5(b)(1)...................... Existing, New, Yes.

Reconstructed.

63.5(b)(2)...................... ........................ No.................. [Reserved].

63.5(b)(3)-(b)(6)............... ........................ Yes.

63.5(c)......................... ........................ No.................. [Reserved].

63.5(d)......................... Approval of Construction/ Yes.

Reconstruction.

63.5(e)......................... ........................ Yes.

63.5(f)......................... ........................ Yes.

63.6(a)......................... Compliance with Yes.

Standards and

Maintenance

Requirements.

63.6(b)(1)-(b)(5)............... ........................ Yes.

63.6(b)(6)...................... ........................ No.................. [Reserved].

63.6(b)(7)...................... ........................ Yes.

63.6(c)(1)...................... Compliance Date for Yes................. Sec. 63.1387 specifies compliance dates.

Existing Sources.

63.6(c)(2)...................... ........................ Yes.

63.6(c)(3)-(c)(4)............... ........................ No.................. [Reserved].

63.6(c)(5)...................... ........................ Yes.

63.6(d)......................... ........................ No.................. [Reserved].

63.6(e)(1)-(e)(2)............... Operation & Maintenance. Yes................. Sec. 63.1383 specifies operations/maintenance plan.

63.6(e)(3)...................... Startup, Shutdown Yes.

Malfunction Plan.

63.6(f)(1)-(f)(3)............... Compliance with Yes.

Nonopacity Emission

Standards.

[[Page 31716]]

63.6(g)(1)-(g)(3)............... Alternative Nonopacity Yes.

Standard.

63.6(h)......................... Opacity/VE Standards.... No.................. Subpart NNN-no COMS, VE or opacity standards.

63.6(i)(1)-(i)(14).............. Extension of Compliance. Yes.

63.6(i)(15)..................... ........................ No.................. [Reserved].

63.6(i)(16)..................... ........................ Yes.

63.6(j)......................... Exemption from Yes.

Compliance.

63.7(a)......................... Performance Testing Yes Sec. 63.1384 has specific requirements.

Requirements.

63.7(b)......................... Notification............ Yes.

63.7(c)......................... Quality Assurance Yes.

Program/Test Plan.

63.7(d)......................... Performance Testing Yes.

Facilities.

63.7(e)(1)-(e)(4)............... Conduct of Performance Yes.

Tests.

63.7(f)......................... Alternative Test Method. Yes.

63.7(g)......................... Data Analysis........... Yes.

63.7(h)......................... Waiver of Performance Yes.

Tests.

63.8(a)(1)-(a)(2)............... Monitoring Requirements. Yes.

63.8(a)(3)...................... ........................ No.................. [Reserved].

63.8(a)(4)...................... ........................ Yes.

63.8(b)......................... Conduct of Monitoring... Yes.

63.8(c)......................... CMS Operation/ Yes.

Maintenance.

63.8(d)......................... Quality Control Program. Yes.

63.8(e)......................... Performance Evaluation Yes.

for CMS.

63.8(f)......................... Alternative Monitoring Yes.

Method.

63.8(g)......................... Reduction of Monitoring Yes.

Data.

63.9(a)......................... Notification Yes.

Requirements.

63.9(b)......................... Initial Notifications... Yes.

63.9(c)......................... Request for Compliance Yes.

Extension.

63.9(d)......................... New Source Notification Yes.

for Special Compliance

Requirements.

63.9(e)......................... Notification of Yes.

Performance Test.

63.9(f)......................... Notification of VE/ No.................. Opacity/VE tests not required.

Opacity Test.

63.9(g)......................... Additional CMS Yes.

Notifications.

63.9(h)(1)-(h)(3)............... Notification of Yes.

Compliance Status.

63.9(h)(4)...................... ........................ No.................. [Reserved].

63.9(h)(5)-(h)(6)............... ........................ Yes.

63.9(i)......................... Adjustment of Deadlines. Yes.

63.9(j)......................... Change in Previous Yes.

Information.

63.10(a)........................ Recordkeeping/Reporting. Yes.

63.10(b)........................ General Requirements.... Yes.

63.10(c)(1)..................... Additional CMS Yes.

Recordkeeping.

63.10(c)(2)-(c)(4).............. ........................ No.................. [Reserved].

63.10(c)(5)-(c)(8).............. ........................ Yes.

63.10(c)(9)..................... ........................ No.................. [Reserved].

63.10(c)(10)-(15)............... ........................ Yes.

63.10(d)(1)..................... General Reporting Yes.

Requirements.

63.10(d)(2)..................... Performance Test Results Yes.

63.10(d)(3)..................... Opacity or VE No.................. No limits for VE/opacity.

Observations.

63.10(d)(4)..................... Progress Reports........ Yes.

63.10(d)(5)..................... Startup, Shutdown, Yes.

Malfunction Reports.

63.10(e)(1)-(e)(3).............. Additional CMS Reports.. Yes.

63.10(e)(4)..................... Reporting COM Data...... No.................. COM not required.

63.10(f)........................ Waiver of Recordkeeping/ Yes.

Reporting.

63.11(a)........................ Control Device Yes.

Requirements.

63.11(b)........................ Flares.................. No.................. Flares not applicable.

63.12........................... State Authority and Yes.

Delegations.

63.13........................... State/Regional Addresses Yes.

63.14........................... Incorporation by No..................

Reference.

63.15........................... Availability of Yes.

Information.

--------------------------------------------------------------------------------------------------------------------------------------------------------

[[Page 31717]]

Appendix A to Subpart NNN of Part 63--Method for the Determination of

LOI

1. Purpose

The purpose of this test is to determine the LOI of cured

blanket insulation. The method is applicable to all cured board and

blanket products.

2. Equipment

2.1 Scale sensitive to 0.1 gram.

2.2 Furnace designed to heat to at least 540 deg.C (1,000

deg.F) and controllable to 10 deg.C (50 deg.F).

2.3 Wire tray for holding specimen while in furnace.

3. Procedure

3.1 Cut a strip along the entire width of the product that will

weigh at least 10.0 grams. Sample should be free of dirt or foreign

matter.

Note: Remove all facing from sample.

3.2 Cut the sample into pieces approximately 12 inches long,

weigh to the nearest 0.1 gram and record. Place in wire tray. Sample

should not be compressed or overhang on tray edges.

Note: On air duct products, remove shiplaps and overspray.

3.3 Place specimen in furnace at 540 deg.C (1,000 deg.F),

10 deg.C (50 deg.F) for 15 to 20 minutes to insure

complete oxidation. After ignition, fibers should be white and

should not be fused together.

3.4 Remove specimen from the furnace and cool to room

temperature.

3.5 Weigh cooled specimen and wire tray to the nearest 0.1

gram. Deduct the weight of the wire tray and then calculate the loss

in weight as a percent of the original specimen weight.

Appendix B to Subpart NNN of Part 63--Free Formaldehyde Analysis of

Insulation Resins by Hydroxylamine Hydrochloride

1. Scope

This method was specifically developed for water-soluble

phenolic resins that have a relatively high free-formaldehyde (FF)

content such as insulation resins. It may also be suitable for other

phenolic resins, especially those with a high FF content.

2. Principle

2.1 a. The basis for this method is the titration of the

hydrochloric acid that is liberated when hydroxylamine hydrochloride

reacts with formaldehyde to form formaldoxine:

HCHO + NH2OH:HCl CH2:NOH + H2O + HCl

b. Free formaldehyde in phenolic resins is present as monomeric

formaldehyde, hemiformals, polyoxymethylene hemiformals, and

polyoxymethylene glycols. Monomeric formaldehyde and hemiformals

react rapidly with hydroxylamine hydrochloride, but the polymeric

forms of formaldehyde must hydrolyze to the monomeric state before

they can react. The greater the concentration of free formaldehyde

in a resin, the more of that formaldehyde will be in the polymeric

form. The hydrolysis of these polymers is catalyzed by hydrogen

ions.

2.2 The resin sample being analyzed must contain enough free

formaldehyde so that the initial reaction with hydroxylamine

hydrochloride will produce sufficient hydrogen ions to catalyze the

depolymerization of the polymeric formaldehyde within the time

limits of the test method. The sample should contain approximately

0.3 grams free formaldehyde to ensure complete reaction within 5

minutes.

3. Apparatus

3.1 Balance, readable to 0.01 g or better.

3.2 pH meter, standardized to pH 4.0 with pH 4.0 buffer and pH

7 with pH 7.0 buffer.

3.3 50-mL burette for 1.0 N sodium hydroxide.

3.4 Magnetic stirrer and stir bars.

3.5 250-mL beaker.

3.6 50-mL graduated cylinder.

3.7 100-mL graduated cylinder.

3.8 Timer.

4. Reagents

4.1 Standardized 1.0 N sodium hydroxide solution.

4.2 Hydroxylamine hydrochloride solution, 100 grams per liter,

pH adjusted to 4.00.

4.3 Hydrochloric acid solution, 1.0 N and 0.1 N.

4.4 Sodium hydroxide solution, 0.1 N.

4.5 50/50 v/v mixture of distilled water and methyl alcohol.

5. Procedure

5.1 Determine the sample size as follows:

a. If the expected FF is greater than 2 percent, go to Part A to

determine sample size.

b. If the expected FF is less than 2 percent, go to Part B to

determine sample size.

c. Part A: Expected FF 2 percent.

Grams resin = 60/expected percent FF

i. The following table shows example levels:

------------------------------------------------------------------------

Sample

Expected % free formaldehyde size, grams

------------------------------------------------------------------------

2.......................................................... 30.0

5.......................................................... 12.0

8.......................................................... 7.5

10......................................................... 6.0

12......................................................... 5.0

15......................................................... 4.0

------------------------------------------------------------------------

ii. It is very important to the accuracy of the results that the

sample size be chosen correctly. If the milliliters of titrant are

less than 15 mL or greater than 30 mL, reestimate the needed sample

size and repeat the tests.

d. Part B: Expected FF 2).

3.4 Measure sample thickness.

3.5 Calculate the product density:

Density (lb/ft3) = area weight (lb/ft2)/

thickness (ft)

5. Appendix A to part 63 is amended by adding in numerical order

methods 316 and 318 to read as follows:

Appendix A To Part 63--Test Methods

* * * * *

Method 316--Sampling and Analysis for Formaldehyde Emissions From

Stationary Sources in the Mineral Wool and Wool Fiberglass Industries

1.0 Introduction

This method is applicable to the determination of formaldehyde,

CAS Registry number 50-00-0, from stationary sources in the mineral

wool and wool fiber glass industries. High purity water is used to

collect the formaldehyde. The formaldehyde concentrations in the

stack samples are determined using the modified pararosaniline

method. Formaldehyde can be detected as low as 8.8 x

1010 lbs/cu ft (11.3 ppbv) or as high as 1.8 x

103 lbs/cu ft (23,000,000 ppbv), at standard conditions

over a 1 hour sampling period, sampling approximately 30 cu ft.

2.0 Summary of Method

Gaseous and particulate pollutants are withdrawn isokinetically

from an emission source and are collected in high purity water.

Formaldehyde present in the emissions is highly soluble in high

purity water. The high purity water containing formaldehyde is then

analyzed using the modified pararosaniline method. Formaldehyde in

the sample reacts with acidic pararosaniline, and the sodium

sulfite, forming a purple chromophore. The intensity of the purple

color, measured spectrophotometrically, provides an accurate and

precise measure of the formaldehyde concentration in the sample.

3.0 Definitions

See the definitions in the General Provisions of this Subpart.

4.0 Interferences

Sulfite and cyanide in solution interfere with the

pararosaniline method. A procedure to overcome the interference by

each compound has been described by Miksch, et al.

5.0 Safety. (Reserved)

6.0 Apparatus and Materials

6.1 A schematic of the sampling train is shown in Figure 1.

This sampling train configuration is adapted from

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