Effluent Limitations Guidelines and New Source Performance Standards for Synthetic-Based and Other Non-Aqueous Drilling Fluids in the Oil and Gas Extraction Point Source Category
Federal RegisterFeb 3, 1999
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SUMMARY: This proposed rule would amend the technology-based effluent
limitations guidelines for the discharge of certain pollutants into
waters of the United States by existing and new facilities in portions
of the offshore and coastal subcategories of the oil and gas extraction
point source category.
This proposed rule would establish effluent limitations guidelines
and new source performance standards (NSPS) for direct dischargers
based on ``best practicable control technology currently available''
(BPT), ``best conventional pollutant control technology'' (BCT), ``best
available technology economically achievable'' (BAT), and for new
sources ``best available demonstrated control technology'' (BADCT). EPA
is proposing to amend the regulation by providing specific requirements
for the discharge of synthetic-based drilling fluids (SBFs) and other
non-aqueous drilling fluids. The wastestreams that would be limited are
drilling fluids and drill cuttings.
This rule would not amend the current regulations for water-based
drilling fluids. Also, this rule would not amend the zero discharge
requirement for drilling wastes in the coastal subcategory (except Cook
Inlet, Alaska) and in the offshore subcategory within three miles from
shore.
Controlling the discharge of SBFs as proposed today would reduce
the discharge of SBFs by 11.7 million pounds annually. Further,
allowing rather than prohibiting the discharge of SBFs would
substantially reduce non-water quality environmental impacts. Compared
to the zero discharge option, EPA estimates that allowing discharge
will reduce air emissions of the criteria air pollutants by 450 tons
per year, decrease fuel use by 29,000 barrels per year of oil
equivalent, and reduce the generation of oily drill cutting wastes
requiring off-site disposal by 212 million pounds per year.
DATES: Comments on the proposal must be received by May 4, 1999. A
public meeting will be held during the comment period, on Friday, March
5, 1999, from 9:00 a.m. to 12:00 p.m.
ADDRESSES: Send written comments and supporting data on this proposal
to: Mr. Joseph Daly, Office of Water, Engineering and Analysis Division
(4303), U.S. Environmental Protection Agency, 401 M St. SW, Washington,
DC 20460. Please submit any references cited in your comments. EPA
would appreciate an original and two copies of your comments and
enclosures (including references).
The public meeting will be held at the EPA Region 6 Oklahoma Room,
1445 Ross Avenue, Dallas, TX. If you wish to present formal comments at
the public meeting you should have a written copy for submittal. No
meeting materials will be distributed in advance of the public meeting;
all materials will be distributed at the meeting.
The public record is available for review in the EPA Water Docket,
Room EB57, 401 M St. SW, Washington, DC 20460. The public record for
this rulemaking has been established under docket number W-98-26, and
includes supporting documentation, but does not include any information
claimed as Confidential Business Information (CBI). The record is
available for inspection from 9 a.m. to 4 p.m., Monday through Friday,
excluding legal holidays. For access to docket materials, please call
(202) 260-3027 to schedule an appointment.
FOR FURTHER INFORMATION CONTACT: For additional technical information
contact Mr. Joseph Daly at (202) 260-7186. For additional economic
information contact Mr. James Covington at (202) 260-5132.
SUPPLEMENTARY INFORMATION:
Regulated Entities: Entities potentially regulated by this action
include:
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Category Examples of regulated entities
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Industry........................... Facilities engaged in the drilling
of wells in the oil and gas
industry in areas defined as
``coastal'' or ``offshore'' and
discharging in geographic areas
where drilling wastes are allowed
for discharge (offshore waters
beyond 3 miles from the shoreline,
in any Alaska offshore waters with
no 3-mile restriction, and the
coastal waters of Cook Inlet,
Alaska). Includes certain
facilities covered under Standard
Industrial Classification code 13
and North American Classification
System codes 211111 and 213111.
------------------------------------------------------------------------
The preceding 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 EPA is now
aware could potentially be regulated by this action. Other types of
entities not listed in the table could also be regulated. To determine
whether your facility is regulated by this action, you should carefully
examine the applicability criteria in 40 CFR Part 435, Subparts A and
D. If you have questions regarding the applicability of this action to
a particular entity, consult the person listed for technical
information in the preceding FOR FURTHER INFORMATION CONTACT section.
Supporting Documentation
The regulations proposed today are supported by several major
documents:
1. ``Development Document for Proposed Effluent Limitations
Guidelines and Standards for Synthetic-Based Drilling Fluids and other
Non-Aqueous Drilling Fluids in the Oil and Gas Extraction Point Source
Category'' (EPA-821-B-98-021). Hereafter referred to as the SBF
Development Document, the document presents EPA's technical conclusions
concerning the proposal. This document describes, among other things,
the data collection activities in support of the proposal, the
wastewater treatment technology options, effluent characterization,
estimate of costs to the industry, and estimate of effects on non-water
quality environmental impacts.
2. ``Economic Analysis of Proposed Effluent Limitations Guidelines
and Standards for Synthetic-Based Drilling Fluids and other Non-Aqueous
Drilling Fluids in the Oil and Gas Extraction Point Source Category''
(EPA-821-B-98-020). Hereafter referred to as the SBF Economic Analysis,
this document presents the analysis of compliance costs and/or savings;
facility closures; changes in rate of return level. In addition,
impacts on employment and affected communities, foreign trade, specific
demographic groups, and new sources also are considered.
3. ``Environmental Assessment of Proposed Effluent Limitations
Guidelines and Standards for Synthetic-Based Drilling Fluids and other
Non-Aqueous Drilling Fluids in the Oil and Gas Extraction Point Source
Category'' (EPA-821-B-98-019). Hereafter referred to as the SBF
Environmental Assessment, the document presents the analysis of
relative water quality impacts for each regulatory option. EPA
describes the environmental characteristics of SBF drilling wastes,
types of anticipated impacts, and pollutant modeling results for water
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column concentrations, pore water concentrations, and human health
effects via consumption of affected seafood.
All documents are available from the Office of Water Resource
Center, RC-4100, U.S. EPA, 401 M Street SW, Washington, DC 20460;
telephone (202) 260-7786 for the voice mail publication request. The
Development Document can also be obtained through EPA's Home Page on
the Internet, located at WWW.EPA.GOV/OST/GUIDE. The preamble and rule
can also be obtained at this site.
Overview
This preamble includes a description of the legal authority for
these rules; a summary of the proposal; background information on the
industry and its processes; and a description of the technical and
economic methodologies used by EPA to develop these regulations. This
preamble also solicits comment and data on all aspects of this proposed
rule. The definitions, acronyms, and abbreviations used in this notice
are defined in Appendix A to the preamble.
Organization of This Document
I. Legal Authority
II. Purpose and Summary of the Proposed Regulation
A. Purpose of this Rulemaking
B. Summary of the Proposed SBF Regulations
III. Background
A. Clean Water Act
B. Permits
C. Pollution Prevention Act
IV. Description of Well Drilling Process and Activity
A. Well Drilling Process Description
B. Location and Activity
C. Drilling Waste Streams
V. Summary of Data Collection Activities
A. Expedited Guidelines Approach
B. Identification of Information Needs
C. Stakeholder Technical Input
D. EPA Research on Toxicity, Biodegradation, Bioaccumulation
E. EPA Investigation of Solids Control Technologies for Drilling
Fluids
F. Assistance from Other State and Federal Agencies
VI. Development of Effluent Limitations Guidelines and Standards
A. Waste Generation and Characterization
B. Selection of Pollutant Parameters
C. Regulatory Options Considered for SBFs Not Associated with
Drill Cuttings
D. Regulatory Options Considered for SBFs Associated with Drill
Cuttings
E. BPT Technology Options Considered and Selected
F. BCT Technology Options Considered and Selected
G. BAT Technology Options Considered and Selected
H. NSPS Technology Options Considered and Selected
VII. Non-Water Quality Environmental Impacts of Proposed Regulations
A. Introduction and Summary
B. Method Overview
C. Energy Consumption and Air Emissions for Existing Sources
D. Energy Consumption and Air Emissions for New Sources
E. Solid Waste Generation and Management
F. Consumptive Water Use
G. Safety
H. Increased Vessel Traffic
VIII. Water Quality Environmental Impacts of Proposed Regulations
A. Introduction
B. Types of Impacts
C. Water Quality Modeling
D. Human Health Effects Modeling
E. Future Seabed Surveys
IX. Costs and Pollutant Reductions Achieved by Regulatory
Alternatives
A. Introduction
B. Model Wells and Well Counts
C. Method for Estimating Compliance Costs
D. Method for Estimating Pollutant Reductions
E. BCT Cost Test
X. Economic Analysis
A. Introduction and Profile of Affected Industry
B. Costs and Costs Savings of the Regulatory Options
C. Impacts from BAT Options
D. Impacts from NSPS Options
E. Cost Benefit Analysis
F. Small Business Analysis
G. Cost-Effective Analysis
XI. Related Acts of Congress, Executive Orders, and Agency
Initiatives
A. Executive Order 12866: OMB Review
B. Regulatory Flexibility Act and the Small Business Regulatory
Enforcement Fairness Act
C. Unfunded Mandates Reform Act
D. Executive Order 12875: Enhancing Intergovernmental
Partnerships
E. Executive Order 13084: Consultation and Coordination with
Indian Tribal Governments
F. Paperwork Reduction Act
G. National Technology Transfer and Advancement Act
H. Executive Order 13045: Children's Health Protection
XII. Regulatory Implementation
A. Analytical Methods
B. Diesel Prohibition for SBF-Cuttings
C. Monitoring of Stock Base Fluid
D. Upset and Bypass Provisions
E. Variances and Modifications
F. Best Management Practices
G. Sediment Toxicity and Biodegradation Comparative Limitations
XIII. Solicitation of Data and Comments
A. Introduction and General Solicitation
B. Specific Data and Comment Solicitations
Appendix A: Definitions, Acronyms, and Abbreviations Used in This
Notice
I. Legal Authority
These regulations are proposed under the authority of Sections 301,
304, 306, 307, 308, 402, and 501 of the Clean Water Act, 33 U.S.C.
1311, 1314, 1316, 1317, 1318, 1342, and 1361.
II. Purpose and Summary of the Proposed Regulation
A. Purpose of This Rulemaking
The purpose of this rulemaking is to amend the effluent limitations
guidelines and standards for the control of discharges of certain
pollutants associated with the use of synthetic-based drilling fluids
(SBFs) and other non-aqueous drilling fluids in portions of the
Offshore Subcategory and Cook Inlet portion of the Coastal Subcategory
of the Oil and Gas Extraction Point Source Category. The limitations
proposed today apply to wastes generated when oil and gas wells are
drilled using SBFs or other non-aqueous drilling fluids (henceforth
collectively referred to simply as SBFs) in coastal and offshore
regions in locations where drilling wastes may be discharged. The
processes and operations that comprise the offshore and coastal oil and
gas subcategories are currently regulated under 40 CFR Part 435,
Subparts A (offshore) and D (coastal). EPA is proposing these
amendments under the authority of the CWA, as discussed in Section I of
this notice. The regulations are also being proposed pursuant to a
Consent Decree entered in NRDC et al. v. Browner, (D.D.C. No. 89-2980,
January 31, 1992) and are consistent with EPA's latest Effluent
Guidelines Plan under section 304(m) of the CWA. (See 63 FR 47285,
September 4, 1998.) The most recent existing effluent limitations
guidelines were issued on March 4, 1993 (58 FR 12454) for the Offshore
Subcategory and on December 16, 1996 (61 FR 66086) for the Coastal
Subcategory. This proposed rule is referred to as the Synthetic-Based
Drilling Fluids Guidelines, or SBF Guidelines, throughout this
preamble.
Today's proposal presents EPA's preferred technology approach and
several others that are being considered in the regulation development
process. The proposed rule is based on a detailed evaluation of the
available data acquired during the development of the proposed
limitations. EPA welcomes comment on all options and issues and
encourages commenters to submit additional data during the comment
period. Also, EPA is willing to meet with interested parties during the
comment period to ensure that EPA has the views of all parties and the
best possible data upon which to base a decision for the final
regulation. EPA emphasizes that it is soliciting comments on all
options discussed in this proposal and that it may adopt any
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such options or combination of options in the final rule.
B. Summary of Proposed SBF Guidelines
This summary section highlights key aspects of the proposed rule.
The technology descriptions discussed later in this notice are
presented in abbreviated form; more detailed descriptions are included
in the Development Document for Proposed Effluent Limitations
Guidelines and Standards for Synthetic-Based and other Non-Aqueous
Drilling Fluids in the Oil and Gas Extraction Point Source Category,
referred to hereafter as the ``SBF Development Document.''
EPA proposes to establish regulations based on the ``best
practicable control technology currently available'' (BPT), ``best
conventional pollutant control technology'' (BCT), ``best available
technology economically achievable'' (BAT), and the best available
demonstrated control technology (BADCT) for new source performance
standards (NSPS), for the wastestream of synthetic-based drilling
fluids and other non-aqueous drilling fluids, and cuttings contaminated
with these drilling fluids.
For certain drilling situations, such as drilling in reactive
shales, high angle and/or high displacement directional drilling, and
drilling in deep water, progress with water-based drilling fluids
(WBFs) can be slow, costly, or even impossible, and often creates a
large amount of drilling waste. In these situations, the well is
normally drilled with traditional oil-based drilling fluids (OBFs),
which use diesel oil or mineral oil as the base fluid. Because EPA
rules require zero discharge of these wastes, they are either sent to
shore for disposal in non-hazardous oil field waste (NOW) sites or
injected into disposal wells.
Since about 1990, the oil and gas extraction industry has developed
many new oleaginous (oil-like) base materials from which to formulate
high performance drilling fluids. A general class of these are called
the synthetic materials, such as the vegetable esters, poly alpha
olefins, internal olefins, linear alpha olefins, synthetic paraffins,
ethers, linear alkyl benzenes, and others. Other oleaginous materials
have also been developed for this purpose, such as the enhanced mineral
oils and non-synthetic paraffins. Industry developed SBFs with these
synthetic and non-synthetic oleaginous materials as the base fluid to
provide the drilling performance characteristics of traditional OBFs
based on diesel and mineral oil, but with lower environmental impact
and greater worker safety through lower toxicity, elimination of
polynuclear aromatic hydrocarbons (PAHs), faster biodegradability,
lower bioaccumulation potential, and, in some drilling situations, less
drilling waste volume. EPA believes that this product substitution
approach is an excellent example of pollution prevention that can be
accomplished by the oil and gas industry.
EPA intends that these proposed regulations control the discharge
of SBFs in a way that reflects application of appropriate levels of
technology, while also encouraging their use as a replacement to the
traditional mineral oil and diesel oil-based fluids. Based on EPA's
information to date, the record indicates that use of SBFs and
discharge of the cuttings waste with proper controls would overall be
environmentally preferable to the use of OBFs. This is because OBFs are
subject to zero discharge requirements, and thus, must be shipped to
shore for land disposal or injected underground, resulting in higher
air emissions, increased energy use, and increased land disposal of
oily wastes. By contrast, the discharge of cuttings associated with
SBFs would eliminate those impacts. At the same time EPA recognizes
that the discharge of SBFs may have impacts to the receiving water.
Because SBFs are water non-dispersible and sink to the seafloor, the
primary potential environmental impacts are associated with the benthic
community. EPA's information to date, including limited seabed surveys
in the Gulf of Mexico, indicate that the effect zone of the discharge
of certain SBFs is within a few hundred meters of the discharge point
and may be significantly recovered in one to two years. EPA believes
that impacts are primarily due to smothering by the drill cuttings,
changes in sediment grain size and composition (physical alteration of
habitat), and anoxia (absence of oxygen) caused by the decomposition of
the organic base fluid. The benthic smothering and changes in grain
size and composition from the cuttings are effects that are also
associated with the discharge of WBFs and associated cuttings.
Based on the record to date, EPA finds that these impacts, which
are believed to be of limited duration, are less harmful to the
environment than the non-water quality environmental impacts associated
with the zero discharge requirement applicable to OBFs. Compared to the
zero discharge option EPA estimates that allowing discharge will reduce
air emissions of the criteria air pollutants by 450 tons per year,
decrease fuel use by 29,000 barrels per year of oil equivalent, and
reduce the generation of oily drill cutting wastes requiring off-site
disposal by 212 million pounds per year. In addition, EPA estimates
that compliance with these proposed limitations would result in a
yearly decrease in the discharge of 11.7 million pounds of toxic and
nonconventional pollutants in the form of SBFs. These estimates are
based on the current industry practice of discharging SBF-cuttings
outside of 3 miles in the Gulf of Mexico and no discharge of SBFs in
any other areas, including 3 miles offshore of California and in Cook
Inlet, Alaska.
As SBFs came into commercial use, EPA determined that the current
discharge monitoring methods, which were developed to control the
discharge of WBFs, did not appropriately control the discharge of these
new drilling fluids. Since WBFs disperse in water, oil contamination of
WBFs with formation oil or other sources can be measured by the static
sheen test, and any toxic components of the WBFs will disperse in the
aqueous phase and be detected by the suspended particulate phase (SPP)
toxicity test. With SBFs, which do not disperse in water but instead
sink as a mass, formation oil contamination has been shown to be less
detectible by the static sheen test. Similarly, the potential toxicity
of the discharge is not apparent in the current SPP toxicity test.
EPA has therefore sought to identify methods to control the
discharge of cuttings associated with SBFs (SBF-cuttings) in a way that
reflects the appropriate level of technology. One way to do this is
through stock limitations on the base fluids from which the drilling
fluids are formulated. This would ensure that substitution of synthetic
and other oleaginous base fluids for traditional mineral oil and diesel
oil reflects the appropriate level of technology. In other words, EPA
wants to ensure that only the SBFs formulated from the ``best'' base
fluids are allowed for discharge. Parameters that distinguish the
various base fluid are the polynuclear aromatic hydrocarbon (PAH)
content, sediment toxicity, rate of biodegradation, and potential for
bioaccumulation.
EPA also thinks that the SBF-cuttings should be controlled with
discharge limitations, such as a limitation on the toxicity of the SBF
at the point of discharge, and a limitation on the mass (as volume) or
concentration of SBFs discharged. The latter type of limitation would
take advantage of the solids separation efficiencies achievable with
SBFs, and consequently minimize the
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discharge of organic and toxic components. EPA believes that SBFs
separated from drill cuttings should meet zero discharge requirements,
as this is the current industry practice due to the value of these
drilling fluids.
Thus, EPA is proposing limits appropriate to SBF-cuttings. EPA is
proposing zero discharge of neat SBFs (not associated with cuttings),
which reflects current practice. The new limitations applicable to
cuttings contaminated with SBFs would be as follows:
Stock Limitations on Base Fluids: (BAT/NSPS).
Maximum PAH content 10 ppm (wt. based on phenanthrene/wt.
base fluid).
Minimum rate of biodegradation (biodegradation equal to or
faster than C16-C18 internal olefin by solid
phase test).
Maximum sediment toxicity (as toxic or less toxic than
C16-C18 internal olefin by 10-day sediment
toxicity test).
Discharge Limitations on Cuttings Contaminated with SBFs:
No free oil by the static sheen test. (BPT/BCT/NSPS).
Maximum formation oil contamination (95 percent of
representative formation oils failing 1 percent by volume in drilling
fluid). (BAT/NSPS).
Maximum well-average retention of SBF on cuttings (percent
base fluid on wet cuttings). (BAT/NSPS).
Discharges remain subject to the following requirements already
applicable to all drilling waste discharges and thus these requirements
are not within the scope of this rulemaking:
Mercury limitation in stock barite of 1 mg/kg. (BAT/NSPS).
Cadmium limitation in stock barite of 3 mg/kg. (BAT/NSPS).
Diesel oil discharge prohibition. (BAT/NSPS).
EPA may require these additional or alternative controls as part of
the discharge option based on method development and data gathering
subsequent to today's notice:
Maximum sediment toxicity of drilling fluid at point of
discharge (minimum LC50, mL drilling fluid/kg dry sediment
by 10-day sediment toxicity test or amended test). (BAT/NSPS).
Maximum aqueous phase toxicity of drilling fluid at point
of discharge (minimum LC50 by SPP test or amended SPP test).
(BAT/NSPS).
Maximum potential for bioaccumulation of stock base fluid
(maximum concentration in sediment-eating organisms). (BAT/NSPS).
EPA is also considering a zero discharge option in the event that
EPA has an insufficient basis upon which to develop appropriate
discharge controls for SBF-cuttings:
Zero discharge of drill cuttings contaminated with SBFs
and other non-aqueous drilling fluids. (BPT/BCT/BAT/NSPS).
While EPA is proposing limitations on these parameters today, many
of the test methods that would be used to demonstrate attainment with
the limitations are still under development at this time, or additional
data needs to be gathered towards validating methods, proving the
variability and appropriateness of the methods, and assessing
appropriate limitations for the parameters. For example, as noted in
the list above, EPA is considering limitations in addition, or as an
alternative, to the limitations in today's proposal. The reason for
this is that EPA has insufficient data at this time to determine how to
best control toxicity and whether a bioaccumulation limitation is
necessary to adequately control the SBF-cuttings wastestream.
EPA would prefer to control sediment toxicity at the point of
discharge. While there is an EPA approved sediment toxicity test to do
this, EPA has concerns about the uniformity of the sediment used in the
toxicity test, the discriminatory power and variability of the test so
applied. Since the test is 10 days long, it poses a practical problem
for operators who would prefer to know immediately whether cuttings may
be discharges. Applying EPA's existing sediment toxicity test to the
base fluid as a stock limitation ameliorates these concerns, such that,
at this stage of the development of the test, EPA thinks that it is
more likely to be practically applied. As this would be the preferred
method of control, EPA intends to continue research into the test as
applied to the drilling fluid at the point of discharge. Industry also
has been conducting research to develop a sediment toxicity test that
may be applied to SBFs at the point of discharge with the cuttings.
Further, EPA intends to perform research into the aquatic toxicity test
to see if it can be used to adequately control the discharge through
modification. EPA may then consider applying an aqueous phase toxicity
test, either alone or in conjunction with a sediment toxicity test of
either the stock base fluid or drilling fluid at the point of
discharge.
In terms of the retention of SBF on cuttings, while EPA has enough
information to propose a limitation, EPA is still evaluating methods to
determine attainment of this limit. For the parameter of
biodegradation, EPA is proposing a numerical limit, but the analytic
method for measuring attainment of the limit has not yet been
validated. EPA wishes to do additional studies to validate the method
and provide public notice of any subsequently developed numerical
limit.
Because EPA plans to gather significant additional information in
support of the final rule, EPA intends to publish a supplemental notice
for public comment providing the proposed limitations and specific test
methods. These data gathering activities are summarized in Section V of
today's notice. Section VI details the information gathered to support
this selection of parameters, and the further information that EPA
intends to gather to support the methods and limitations for the
intended notice and subsequent final rule.
Therefore, the purpose of today's proposal is to request comment on
the candidate requirements listed above, identify the additional work
that EPA intends to perform towards promulgation of the limitations,
and request comments and additional data towards the selection of
parameters, methods and limitations development. EPA also intends that
this proposal serve as guidance to permit writers such that the
proposed methods can be incorporated into permits through best
professional judgement (BPJ). Such permits can be used to gather
supporting information towards selection of parameters, methods
development, and appropriate limitations.
The current regulations establish the geographic areas where
drilling wastes may be discharged: the offshore subcategory waters
beyond 3 miles from the shoreline, and in Alaska offshore waters with
no 3-mile restriction. The only coastal subcategory waters where
drilling wastes may be discharged is in Cook Inlet, Alaska. EPA is
retaining the zero discharge limitations in areas where discharge is
currently prohibited and these requirements are not within the scope of
this rulemaking.
EPA is limiting the scope of today's proposed rulemaking to
locations where drilling wastes may be discharged because these are the
only locations for which EPA has evaluated the non-water quality
environmental impacts of zero discharge versus the environmental
impacts of discharging drill cuttings associated with SBFs. For
example, EPA has only assessed the non-water quality environmental
impacts of zero discharge beyond three miles from shore. EPA expects
these impacts to be less where
[[Page 5492]]
the wastes are generated closer to shore. In addition, EPA has not
assessed the environmental effects of these discharges in coastal
areas. The current zero discharge areas are more likely to be
environmentally sensitive due to the presence of spawning grounds,
wetlands, lower energy (currents), and more likely to be closer to
recreational swimming and fishing areas. Further, dischargers are in
compliance with the zero discharge requirement and have only expressed
an interest in the use of these newer fluids where drilling wastes may
be discharged today.
III. Background
A. Clean Water Act
1. Summary of Effluent Limitations Guidelines and Standards
Congress adopted the Clean Water Act (CWA) to ``restore and
maintain the chemical, physical, and biological integrity of the
Nation's waters'' (Section 101(a), 33 U.S.C. 1251(a)). To achieve this
goal, the CWA prohibits the discharge of pollutants into navigable
waters except in compliance with the statute. The Clean Water Act
confronts the problem of water pollution on a number of different
fronts. Its primary reliance, however, is on establishing restrictions
on the types and amounts of pollutants discharged from various
industrial, commercial, and public sources of wastewater.
Direct dischargers must comply with effluent limitation guidelines
and new source performance standards in National Pollutant Discharge
Elimination System (``NPDES'') permits; indirect dischargers must
comply with pretreatment standards. EPA issues these guidelines and
standards for categories of industrial dischargers based on the degree
of control that can be achieved using various levels of pollution
control technology. The guidelines and standards are summarized below:
a. Best Practicable Control Technology Currently Available (BPT)--
sec. 304(b)(1) of the CWA.--Effluent limitations guidelines based on
BPT apply to discharges of conventional, toxic, and non-conventional
pollutants from existing sources. BPT guidelines are generally based on
the average of the best existing performance by plants in a category or
subcategory. In establishing BPT, EPA considers the cost of achieving
effluent reductions in relation to the effluent reduction benefits, the
age of equipment and facilities, the processes employed, process
changes required, engineering aspects of the control technologies, non-
water quality environmental impacts (including energy requirements),
and other factors the EPA Administrator deems appropriate. CWA
Sec. 304(b)(1)(B). Where existing performance is uniformly inadequate,
BPT may be transferred from a different subcategory or category.
b. Best Conventional Pollutant Control Technology (BCT)--sec.
304(b)(4) of the CWA.--The 1977 amendments to the CWA established BCT
as an additional level of control for discharges of conventional
pollutants from existing industrial point sources. In addition to other
factors specified in section 304(b)(4)(B), the CWA requires that BCT
limitations be established in light of a two part ``cost-
reasonableness'' test. EPA published a methodology for the development
of BCT limitations which became effective August 22, 1986 (51 FR 24974,
July 9, 1986).
Section 304(a)(4) designates the following as conventional
pollutants: biochemical oxygen demanding pollutants (measured as
BOD5), total suspended solids (TSS), fecal coliform, pH, and
any additional pollutants defined by the Administrator as conventional.
The Administrator designated oil and grease as an additional
conventional pollutant on July 30, 1979 (44 FR 44501).
c. Best Available Technology Economically Achievable (BAT)--sec.
304(b)(2) of the CWA.--In general, BAT effluent limitations guidelines
represent the best available economically achievable performance of
plants in the industrial subcategory or category. The CWA establishes
BAT as a principal national means of controlling the direct discharge
of toxic and nonconventional pollutants. The factors considered in
assessing BAT include the age of equipment and facilities involved, the
process employed, potential process changes, non-water quality
environmental impacts, including energy requirements, and such factors
as the Administrator deems appropriate. The Agency retains considerable
discretion in assigning the weight to be accorded these factors. An
additional statutory factor considered in setting BAT is economic
achievability across the subcategory. Generally, the achievability is
determined on the basis of total costs to the industrial subcategory
and their effect on the overall industry (or subcategory) financial
health. As with BPT, where existing performance is uniformly
inadequate, BAT may be transferred from a different subcategory or
category. BAT may be based upon process changes or internal controls,
such as product substitution, even when these technologies are not
common industry practice. The CWA does not require a cost-benefit
comparison in establishing BAT.
d. New Source Performance Standards (NSPS)--section 306 of the
CWA.--NSPS are based on the best available demonstrated control
technology (BADCT) and apply to all pollutants (conventional,
nonconventional, and toxic). NSPS are at least as stringent as BAT. New
plants have the opportunity to install the best and most efficient
production processes and wastewater treatment technologies. Under NSPS,
EPA is to consider the best demonstrated process changes, in-plant
controls, and end-of-process control and treatment technologies that
reduce pollution to the maximum extent feasible. In establishing NSPS,
EPA is directed to take into consideration the cost of achieving the
effluent reduction and any non-water quality environmental impacts and
energy requirements.
e. Pretreatment Standards for Existing Sources (PSES)--sec. 307(b)
of the CWA--and Pretreatment Standards for New Sources (PSNS)--sec.
307(b) of the CWA.--Pretreatment standards are designed to prevent the
discharge of pollutants to a publicly-owned treatment works (POTW)
which pass through, interfere, or are otherwise incompatible with the
operation of the POTW. Since none of the facilities to which this rule
applies discharge to a POTW, pretreatment standards are not being
considered as part of this rulemaking.
f. Best Management Practices (BMPs).--Section 304(e) of the CWA
gives the Administrator the authority to publish regulations, in
addition to the effluent limitations guidelines and standards listed
above, to control plant site runoff, spillage or leaks, sludge or waste
disposal, and drainage from raw material storage which the
Administrator determines may contribute significant amounts of toxic
and hazardous pollutants to navigable waters. Section 402(a)(1) also
authorizes best management practices (BMPs) as necessary to carry out
the purposes and intent of the CWA. See 40 CFR Part 122.44(k).
g. CWA Section 304(m) Requirements.--Section 304(m) of the CWA,
added by the Water Quality Act of 1987, requires EPA to establish
schedules for (i) reviewing and revising existing effluent limitations
guidelines and standards and (ii) promulgating new effluent guidelines.
On January 2, 1990, EPA published an Effluent Guidelines Plan (55 FR
80), in which schedules were established for developing new and revised
effluent guidelines for several industry
[[Page 5493]]
categories, including the oil and gas extraction industry. Natural
Resources Defense Council, Inc., challenged the Effluent Guidelines
Plan in a suit filed in the U.S. District Court for the District of
Columbia, (NRDC et al v. Browner, Civ. No. 89-2980). On January 31,
1992, the Court entered a consent decree (the ``304(m) Decree''), which
establishes schedules for, among other things, EPA's proposal and
promulgation of effluent guidelines for a number of point source
categories. The most recent Effluent Guidelines Plan was published in
the Federal Register on September 4, 1998 (63 FR 47285). This plan
requires, among other things, that EPA propose the Synthetic-Based
Drilling Fluids Guidelines by 1998 and promulgate the Guidelines by
2000.
2. Prior Federal Rulemakings and Other Notices
On March 4, 1993, EPA issued final effluent guidelines for the
Offshore Subcategory of the Oil and Gas Extraction Point Source
Category (58 FR 12454). The data and information gathering phase for
this rulemaking thus corresponded to the introduction of SBFs in the
Gulf of Mexico. Because of this timing, the range of drilling fluids
for which data and information were available to EPA was limited to
water-based drilling fluids (WBFs) and oil-based drilling fluids (OBFs)
using diesel and mineral oil. Industry representatives, however,
submitted information on SBFs during the comment period concerning
environmental benefits of SBFs over OBFs and WBFs, and problems with
false positives of free oil in the static sheen test applied to SBFs.
The requirements in the offshore rule applicable to drilling fluids
and drill cuttings consist of mercury and cadmium limitations on the
stock barite, a diesel oil discharge prohibition, a toxicity limitation
on the suspended particulate phase (SPP) generated when the drilling
fluids or drill cuttings are mixed in seawater, and no discharge of
free oil as determined by the static sheen test.
While the SPP toxicity test and the static sheen test, and their
limitations, were developed for use with WBF, the offshore regulation
does not specify the types of drilling fluids and drill cuttings to
which these limitations apply. Thus, under the rule, any drilling waste
in compliance with the discharge limitations could be discharged. When
the offshore rule was proposed, EPA believed that all drilling fluids,
be they WBFs, OBFs, or SBFs, could be controlled by the SPP toxicity
and static sheen tests. This is because OBFs based on diesel oil or
mineral oil failed one or both of the SPP toxicity test and no free oil
static sheen test. In addition, OBFs based on diesel oil were subject
to the diesel oil discharge prohibition.
EPA thought SBFs could also be adequately controlled by the
regulation based on comments received from industry. After the offshore
rule was proposed, EPA received several industry comments which focused
on the fact that the static sheen test could often be interpreted as
giving a false positive for the presence of diesel oil, mineral oil, or
formation hydrocarbons. For this reason, the industry commenters
contended that SBFs should be exempt from compliance with the no free
oil limitation required by the proposed offshore effluent guidelines.
In the final rulemaking in 1993, EPA's response to these comments
was that the prohibition on discharges of free oil was an appropriate
limitation for discharge of drill fluids and drill cuttings, including
SBFs. While EPA agreed that some of the newer SBFs may be less toxic
and more readily biodegradable than many of the OBFs, EPA was concerned
that no alternative method was offered for determining compliance with
the no free oil standard to replace the static sheen test. In other
words, if EPA were to exclude certain fluids from the requirement,
there would be no way to determine if at that particular facility,
diesel oil, mineral oil or formation hydrocarbons were also being
discharged.
Also in the final offshore rule, EPA encouraged the use of drilling
fluids that were less toxic and biodegraded faster. EPA solicited data
on alternative ways of monitoring for the no free oil discharge
requirement, such as gas chromatography or other analytical methods.
EPA also solicited information on technology issues related to the use
of SBFs, any toxicity data or biodegradation data on these newer
fluids, and cost information.
By focusing on the issue of false positives with the static sheen
test, EPA interpreted the offshore effluent guidelines to mean that
SBFs could be discharged provided they complied with the current
discharge requirements. EPA did not think, however, that many, if any,
SBFs would be able to meet the no free oil requirement.
In the final coastal effluent guidelines, EPA raised the issue of
false negatives with the static sheen test as opposed to the issue of
false positives raised during the offshore rulemaking. EPA had
information indicating that the static sheen test does not adequately
detect the presence of diesel, mineral, or formation oil in SBFs. In
addition, EPA raised other concerns regarding the inadequacy of the
current effluent guidelines to control of SBF wastestreams. Thus the
final coastal effluent guidelines, published on December 16, 1996 (61
FR 66086), constitute the first time EPA identified, as part of a
rulemaking, the inadequacies of the current regulations and the need
for new BPT, BAT, BCT, and NSPS controls for discharges associated with
SBFs.
The coastal rule adopted the offshore discharge requirements to
allow discharge of drilling wastes in one geographic area of the
coastal subcategory; Cook Inlet, Alaska, and prohibited the discharge
of drilling wastes in all other coastal areas.
Due to the lack of information concerning appropriate controls, EPA
could not provide controls specific to SBFs as a part of the coastal
rule. However, the coastal rulemaking solicited comments on SBFs. In
responding to these comments, EPA again identified certain
environmental benefits of using SBFs, and stated that allowing the
controlled discharge of SBF-cuttings would encourage their use in place
of OBFs. EPA also raised the inadequacies of the current effluent
guidelines to control the SBF wastestreams, and provided an outline of
the parameters which EPA saw as important for adequate control. The
inadequacies cited include the inability of the static sheen test to
detect formation oil or other oil contamination in SBFs and the
inability of the SPP toxicity test to adequately measure the toxicity
of SBFs. EPA offered alternative tests of gas chromatography (GC) and a
benthic toxicity test to verify the results of the static sheen and the
suspended particulate phase (SPP) toxicity testing currently required.
EPA also mentioned the potential need for controls on the base fluid
used to formulate the SBF, based on one or more of the following
parameters: PAH content, toxicity (preferably sediment toxicity), rate
of biodegradation, and bioaccumulation potential.
The final coastal rule also incorporated clarifying definitions of
drilling fluids for both the offshore and coastal subcategories to
better differentiate between the types of drilling fluids. The rule
provided guidance to permit writers needing to write limits for SBFs on
a best professional judgement (BPJ) basis as using GC as a confirmation
tool to assure the absence of free oil in addition to meeting the
current no free oil (static sheen), toxicity, and barite limits on
mercury and cadmium. EPA
[[Page 5494]]
recommended Method 1663 as described in EPA 821-R-92-008 as a gas
chromatograph with flame ionization detection (GC/FID) method to
identify an increase in n-alkanes due to crude oil contamination of the
synthetic materials coating the drill cuttings. Additional tests, such
as benthic toxicity conducted on the synthetic material prior to use or
whole SBF prior to discharge, were also suggested for controlling the
discharge of cuttings contaminated with drilling fluid.
EPA stated intentions to evaluate further the test methods for
benthic toxicity and determine an appropriate limitation if this
additional test is warranted. In addition, test methods and results for
bioaccumulation and biodegradation, as indications of the rate of
recovery of the cuttings piles on the sea floor, were to be evaluated.
EPA recognized that evaluations of such new testing protocols may be
beyond the technical expertise of individual permit writers, and so
stated that these efforts would be coordinated as a continuing effluent
guidelines effort. Today's proposal is a result of these efforts.
B. Permits
Four EPA Regions currently issue or review permits for offshore and
coastal oil and gas well drilling activities in areas where drilling
wastes may be discharged: Region 4 in the Eastern Gulf of Mexico (GOM),
Region 6 in the Central and Western GOM, Region 9 in offshore
California, and Region 10 in offshore and Cook Inlet, Alaska. Permits
in Regions 4, 9 and 10 never allowed the discharge of SBFs, and those
three Regions are currently preparing final general permits that either
specifically disallow SBF discharges until adequate discharge controls
are available to control the SBF wastestreams, or allow a limited use
of SBF to facilitate information gathering.
Discharge of drill cuttings contaminated with SBF (SBF-cuttings)
has occurred under the Region 6 offshore continental shelf (OCS)
general permit issued in 1993 (58 FR 63964), and the general permit
reissued on November 2, 1998 (63 FR 58722) again does not specifically
disallow the continued discharge of SBF-cuttings. The reason for these
differences between Region 6 and the other EPA Regions relates to the
timing of the 1993 Region 6 general permit and the issues raised in
comments during the issuance of that permit.
The previous individual and general permits of Regions 4, 9 and 10
were issued long before SBFs were developed and used. In Region 6,
however, the first SBF well was drilled in June of 1992 and the
development of the Region 6 OCS general permit, published December 3,
1993 (58 FR 63964), thus corresponded to the introduction of SBF use in
the GOM. After proposal of this permit, industry representatives
commented that the no free oil limitation as measured by the static
sheen test should be waived for SBFs, due to the occurrence of false
positives. They contended that a sheen was sometimes perceived when the
SBF was known to be free of diesel oil, mineral oil or formation oil.
These comments were basically the same as those submitted as part of
the offshore rulemaking, which occurred in the same time frame. EPA
responded as it had in the offshore rulemaking, maintaining the static
sheen test until there existed a replacement test to determine the
presence of free oil. EPA stated that if the current discharge
requirements could be met then the drilling fluid and associated wastes
could be discharged. This response indicated EPA's position that SBF
drilling wastes could be discharged as long as the discharge met permit
requirements. But again, in the context of these comments, EPA did not
expect that many, if any SBFs, would be able to meet the static sheen
requirements.
In addition to the requirements of the offshore guidelines, the
Region 6 OCS general permit also prohibited the discharge of oil-based
and inverse emulsion drilling fluids. Although SBFs are, in chemistry
terms, inverse emulsion drilling fluids, the definition in the permit
limited the term ``inverse emulsion drilling fluids'' to mean ``an oil-
based drilling fluid which also contains a large amount of water.''
Further, the permit provides a definition for oil-based drilling fluid
as having ``diesel oil, mineral oil, or some other oil as its
continuous phase with water as the dispersed phase.'' Since the SBFs
clearly do not have diesel or mineral oil as the continuous phase,
there was a question of whether synthetic base fluids (and more
broadly, other oleaginous base fluids) used to formulate the SBFs are
``some other oil.'' With consideration of the intent of the inverse
emulsion discharge prohibition, and the known differences in
polynuclear aromatic hydrocarbon content, toxicity, and biodegradation
between diesel and mineral oil versus the synthetics, EPA determined
that SBFs were not inverse emulsion drilling fluids as defined in the
Region 6 general permit. This determination is exemplified by the
separate definitions for OBFs and SBFs introduced with the Coastal
Effluent Guidelines (see 61 FR 66086, December 16, 1996).
In late 1998 and early 1999, all four Regions are (re)issuing their
general permits for offshore (Regions 4, 6 and 9) and coastal (Region
10) oil and gas wells. Once the effluent guidelines or guidance becomes
available, EPA intends to reopen the permits to add requirements that
adequately control SBF drilling wastes.
EPA intends for today's proposal to act as guidance such that the
Regions do not have to wait until issuance of a final rule planned for
December 2000, but may propose to add the appropriate discharge
controls through best professional judgement (BPJ). In this manner, the
controlled discharge of SBF may be used to further aid EPA in gathering
information subsequent to today's proposal.
C. Pollution Prevention Act
The Pollution Prevention Act of 1990 (PPA) (42 U.S.C. 13101 et
seq., Pub. L. 101-508, November 5, 1990) ``declares it to be the
national policy of the United States that pollution should be prevented
or reduced whenever feasible; pollution that cannot be prevented should
be recycled in an environmentally safe manner, whenever feasible;
pollution that cannot be prevented or recycled should be treated in an
environmentally safe manner whenever feasible; and disposal or release
into the environment should be employed only as a last resort * * *''
(Sec. 6602; 42 U.S.C. 13101 (b)). In short, preventing pollution before
it is created is preferable to trying to manage, treat or dispose of it
after it is created. The PPA directs the Agency to, among other things,
``review regulations of the Agency prior and subsequent to their
proposal to determine their effect on source reduction'' (Sec. 6604; 42
U.S.C. 13103(b)(2)). EPA reviewed this effluent guideline for its
incorporation of pollution prevention.
According to the PPA, source reduction reduces the generation and
release of hazardous substances, pollutants, wastes, contaminants, or
residuals at the source, usually within a process. The term source
reduction ``include[s] equipment or technology modifications, process
or procedure modifications, reformulation or redesign of products,
substitution of raw materials, and improvements in housekeeping,
maintenance, training or inventory control. The term `source
reduction.' does not include any practice which alters the physical,
chemical, or biological characteristics or the volume of a hazardous
substance, pollutant, or contaminant through a
[[Page 5495]]
process or activity which itself is not integral to or necessary for
the production of a product or the providing of a service.'' 42 U.S.C.
13102(5). In effect, source reduction means reducing the amount of a
pollutant that enters a waste stream or that is otherwise released into
the environment prior to out-of-process recycling, treatment, or
disposal.
In this proposed rule, EPA supports pollution prevention technology
by encouraging the use of SBFs based on certain synthetic materials and
other similarly performing materials in place of traditional oil-based
drilling fluids based on diesel oil and mineral oil. The waste
generated from SBFs is anticipated to have lower toxicity, lower
bioaccumulation potential, faster biodegradation, and elimination of
polynuclear aromatic hydrocarbons, including those which are priority
pollutants. With these improved characteristics, and to encourage their
use in place of OBFs, EPA is proposing to allow the controlled on-site
discharge of the cuttings associated with SBF. Use of SBF in place of
OBF will eliminate the need to barge to shore or inject oily waste
cuttings, reducing fuel use, air emissions, and land disposal. It also
eliminates the risk of OBF and OBF-cuttings spills. In addition, the
proposed regulatory option includes efficient closed-loop recycling
systems to reduce the quantity of SBF discharged with the drill
cuttings. A discussion of this pollution prevention technology is
contained in Section VI of this notice and in the Development Document.
IV. Description of Process and Well Drilling Activities
A. Well Drilling Process Description
Drilling occurs in two phases: exploration and development.
Exploration activities are those operations involving the drilling of
wells to locate hydrocarbon bearing formations and to determine the
size and production potential of hydrocarbon reserves. Development
activities involve the drilling of production wells once a hydrocarbon
reserve has been discovered and delineated.
Drilling for oil and gas is generally performed by rotary drilling
methods which use a circularly rotating drill bit that grinds through
the earth's crust as it descends. Drilling fluids are pumped down
through the drill bit via a pipe that is connected to the bit, and
serve to cool and lubricate the bit during drilling. The rock chips
that are generated as the bit drills through the earth are termed drill
cuttings. The drilling fluid also serves to transport the drill
cuttings back up to the surface through the space between the drill
pipe and the well wall (this space is termed the annulus), in addition
to controlling downhole pressure and stabilizing the well bore.
As drilling progresses, large pipes called ``casing'' are inserted
into the well to line the well wall. Drilling continues until the
hydrocarbon bearing formations are encountered. In areas where drilling
fluids and drill cuttings are allowed to be discharged under the
current regulations, well depths range from approximately 4,000 to
12,000 feet deep, and it takes approximately 20 to 60 days to complete
drilling.
On the surface, the drilling fluid and drill cuttings undergo an
extensive separation process to remove as much fluid from the cuttings
as possible. The fluid is then recycled into the system, and the
cuttings become a waste product. The drill cuttings retain a certain
amount of the drilling fluid that are discharged or disposed with the
cuttings. Drill cuttings are discharged by the shale shakers and other
solids separation equipment. Drill cuttings are also cleaned out of the
mud pits and from the solid separation equipment during displacement of
the drilling fluid system. Intermittently during drilling, and at the
end of the drilling process, drilling fluids may become wastes if they
can no longer be reused or recycled.
In the relatively new area of deepwater drilling, generally greater
than 3000' water depth, new drilling methods are evolving which can
significantly improve drilling efficiencies and thereby reduce the
volume of drilling fluid discharges as well as reduce non-water quality
effects of fuel and steel consumption and air emissions. Subsea
drilling fluid boosting, referred to as ``subsea pumping'', is one such
technology. Rotary drilling methods are generally performed as
described with the exception that the drilling fluid is energized or
boosted by use of a pump at or near the seafloor. By boosting the
drilling fluid, the adverse effect on the wellbore caused by the
drilling fluid pressure from the seafloor to the surface is eliminated,
thereby allowing wells to be drilled with as much as a 50% reduction in
the number of casing strings generally required to line the well wall.
Wells are drilled in less time, including less trouble time. To enable
the pumping of drilling fluids and cuttings to the surface, some drill
cuttings, larger than approximately one-fourth of an inch, are
separated from the drilling fluid at the seafloor since these cuttings
cannot reliably be pumped to the surface. The drill cuttings which are
separated at the seafloor are discharged through an eductor hose at the
seafloor within a 300' radius of the well site. For purposes of
monitoring, representative samples of drill cuttings discharged at the
seafloor can be transported to the surface and separated from the
drilling fluid in a manner similar to that employed at the seafloor.
The drilling fluid, which is boosted at the seafloor and transports
most of the drill cuttings back to the surface, is processed as
described in the general rotary drilling methods described above in
this section.
Once the target formations have been reached, and a determination
made as to which have commercial potential, the well is made ready for
production by a process termed ``completion.'' Completion involves
cleaning the well to remove drilling fluids and debris, perforating the
casing that lines the producing formation, inserting production tubing
to transport the hydrocarbon fluids to the surface, and installing the
surface wellhead. The well is then ready for production, or actual
extraction of hydrocarbons.
B. Location and Activity
This proposed regulation would establish discharge limitations for
SBFs in areas where drilling fluids and drill cuttings are allowed for
discharge. These discharge areas are the offshore waters beyond 3 miles
from shore except the offshore waters of Alaska which has no 3 mile
discharge restriction, and the coastal waters of Cook Inlet, Alaska.
Drilling is currently active in three regions in these discharge areas:
(i) the offshore waters beyond three miles from shore in the Gulf of
Mexico (GOM), (ii) offshore waters beyond three miles from shore in
California, and (iii) the coastal waters of Cook Inlet, Alaska.
Offshore Alaska is the only other area where drilling is active and
effluent guidelines allows discharge. However, drilling wastes are not
currently discharged in the Alaska offshore waters.
Among these three areas, most drilling activity occurs in the GOM,
where 1,302 wells were drilled in 1997, compared to 28 wells drilled in
California and 7 wells drilled in Cook Inlet. In the GOM, over the last
few years, there has been high growth in the number of wells drilled in
the deepwater, defined as water greater than 1,000 feet deep. For
example, in 1995, 84 wells were drilled in the deepwater, comprising
8.6 percent of all GOM wells drilled that year. By 1997, that number
increased to 173 wells drilled and comprised over 13 percent of all GOM
[[Page 5496]]
wells drilled. The increased activity in the deepwater increases the
usefulness of SBFs. Operators drilling in the deepwater cite the
potential for riser disconnect in floating drill ships, which favors
SBF over OBF; higher daily drilling cost which more easily justifies
use of more expensive SBFs over WBFs; and greater distance to barge
drilling wastes that may not be discharged (i.e., OBFs).
C. Drilling Wastestreams
Drilling fluids and drill cuttings are the most significant
wastestreams from exploratory and development well drilling operations.
This rule proposes limitations for the drilling fluid and cuttings
wastestream resulting when SBFs or other non-aqueous drilling fluids
are used. All other wastestreams and drilling fluids have current
applicable limitations which are outside the scope of this rulemaking.
A summary of the characteristics of these wastes is presented in
Section VI of this notice. A more detailed discussion of the origins
and characteristics of these wastes is included in the Development
Document.
V. Summary of Data Gathering Efforts
A. Expedited Guidelines Approach
This regulation is being developed using an expedited rulemaking
process. This process relies on stakeholder support to develop the
initial technology and regulatory options. At various stages of
information gathering, industry, EPA and other stakeholders present and
discuss their preferred options and identify differences in opinion.
This proposal, as part of the expedited process, is being presented
today in a shorter developmental time period, and with less information
than a typical effluent guidelines proposal. The proposed rule is then
a tool to identify the candidate requirements, and request comments and
additional data. EPA plans to continue this expedited rulemaking
process of relying on industry, environmental groups, and other
stakeholder support for the further regulatory development after
proposal.
EPA encourages full public participation in developing the final
SBF Guidelines. This expedited rulemaking process succeeds with more
open communication between EPA, the regulated community, and other
stakeholders, and relies less on formal data and information gathering
mechanisms. The expedited guidelines approach is suitable when EPA,
industry, and other stakeholders have a common goal on the structure of
the limitations and standards. EPA believes this is the case with the
SBF rulemaking; EPA is proposing to allow the controlled discharge of
the SBF-cuttings wastestream to encourage the use and further
development of this pollution prevention technology. Based on
information to date, EPA believes that this option has better
environmental results than the current use and subsequent land disposal
or injection of OBFs. Through the exchange of information among the
stakeholders, EPA understands the industry's interest in discharging
the SBF-cuttings wastestream because discharge of SBFs is more likely
to be cost effective as a replacement to the diesel and mineral oil
based OBFs. EPA was able to accommodate both environmental benefits and
business interests in today's proposal.
Throughout regulatory development, EPA has worked with
representatives from the oil and gas industry and several trade
associations, including the National Ocean Industries Association
(NOIA) and the American Petroleum Institute (API), SBF vendors, solids
control equipment vendors, the U.S. Department of Energy, the U.S.
Department of Interior Minerals Management Service, the Texas Railroad
Commission, and research and regulatory bodies of the United Kingdom
and Norway, to develop effluent limitations guidelines and standards
that represent the appropriate level of technology (e.g., BAT). The
Agency also discussed the progress of the rulemaking with the Natural
Resources Defense Council (NRDC) and invited its participation. The
Cook Inlet Keepers are participating in the rulemaking as well.
As part of the expedited approach to this rulemaking, EPA has
chosen not to gather data using the time consuming approach of a Clean
Water Act section 308 questionnaire, but rather by using data submitted
by industry, vendors, academia, and others, along with data EPA can
develop in a limited period of time. Because all of the facilities
affected by this proposal are direct dischargers, the Agency did not
conduct an outreach survey to POTWs.
Subsequent to today's proposal, EPA intends to continue its data
gathering efforts for support of the final rule. These continuing
efforts are discussed below in conjunction with the information already
gathered. Because of these continuing information gathering activities,
EPA expects that it will publish a subsequent notice of any data either
generated by EPA or submitted after this proposal that will be used to
develop the final rule.
B. Identification of Information Needs
As part of the final coastal effluent guidelines, published on
December 16, 1996 (61 FR 66086), EPA stated that appropriate and
adequate discharge controls would be necessary to allow the discharge
of SBF-cuttings under BPT, BAT, BCT, and NSPS in NPDES permits. As
detailed in Section III of today's notice, in the final coastal
effluent guidelines EPA recommended gas chromatography (GC) as a test
for formation oil contamination, and a sediment toxicity test as a
replacement for the suspended particulate phase (SPP) toxicity testing
currently required. EPA also mentioned the potential need for controls
on the base fluid used to formulate the SBF, controlling one or more of
the following parameters: PAH content, toxicity (preferably sediment
toxicity), rate of biodegradation, and bioaccumulation potential. EPA
summarized the information available from seabed surveys at SBF-
cuttings discharge sites.
Subsequent to the publication of the final coastal effluent
guidelines, EPA continued research into the appropriate controls for
the SBF-cuttings wastestream, and presented its findings to
stakeholders at meetings held in Dallas, Texas, on February 19, 1998,
and in Houston on May 8 and 9, 1997. EPA also presented data and
information requirements to develop adequate and appropriate controls
for the SBF-cuttings wastestream at four conferences, in Aberdeen,
Scotland, on June 23 and 24, 1997, in Houston, Texas on February 9,
1998, again in Aberdeen Scotland on June 18 and 19, 1998, and at the
Minerals Management Service Information Transfer Meeting held in New
Orleans, Louisiana on December 18, 1997. The conferences in Scotland
were germane because of the work that the Scottish Office Agriculture,
Environment and Fisheries Department had performed on sediment toxicity
testing, biodegradability testing, and seabed surveys at SBF-cuttings
and OBF-cuttings discharge sites. This detailed level of work has not
been performed in the United States.
EPA conducted literature reviews and in September 1997 published
documents entitled ``Bioaccumulation of Synthetic-Based Drilling
Fluids,'' ``Biodegradation of Synthetic-Based Drilling Fluids,''
``Assessment and Comparison of Available Drilling Waste Data from Wells
Drilled Using Water Based Fluids and Synthetic Based Fluids,'' and
``Seabed Survey Review and Summary.'' The purpose of these documents
was to help direct EPA's and other stakeholder's research efforts in
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defining BPT, BAT, BCT, and NSPS, and address CWA 403(c) requirements
for SBFs.
Industry stakeholders, with the motivation of having SBFs addressed
in NPDES permits that allow the discharge of SBF-cuttings, assisted EPA
in the development of methods and data gathering to describe currently
available technologies. Thus, by means of meetings, conferences, and
other stakeholder meetings, EPA detailed the methods and/or types of
information required in order to support BPT, BCT, BAT, and NSPS
controls in NPDES permits. The past and anticipated future efforts by
various stakeholder groups and the EPA are presented below.
C. Stakeholder Technical Work Groups
In order to concentrate efforts on certain technical issues, in May
of 1997 industry prepared studies on the following subjects: (a) the
determination of formation oil contamination in SBFs, (b) toxicity
testing of SBFs and base fluids, (c) quantity of SBF discharged
(retention of base fluid on cuttings), and (d) seabed surveys at SBF-
cuttings discharge sites. Industry representatives formed work groups
to address these issues. The sections below describe their work.
1. Formation Oil Contamination Determination (Analytical)
The goal of this work group was to define the monitoring and
compliance method to determine crude oil (or other oil) contamination
of SBF-cuttings. The work group has issued several reports concerning
the static sheen test, and developed two replacement tests for
formation oil contamination, one based on fluorescence and the other on
gas chromatography with mass spectroscopy detection (GC/MS).
On September 28, 1998, the workgroup published the final draft of
the Phase I report entitled ``Evaluation of Static Sheen Test for
Water-based Muds, Synthetic-based Muds and Enhanced Mineral Oils. The
conclusions of the report are that the static sheen test is not a good
indicator of oil contamination in SBFs, and that in WBFs formation oil
contamination is often detected at 1.0 percent and sometimes as low as
0.5 percent.
On October 21, 1998, the work group published its final draft to
the Phase II report entitled ``Survey of Monitoring Approaches for the
Detection of Oil Contamination in Synthetic-based Drilling Muds.'' This
document lists thirteen methods that the work group considered as a
replacement to the static sheen test. From these thirteen, EPA selected
the reverse phase extraction method to be used on offshore drilling
sites, and the GC/MS method for onshore baseline measurements.
On November 16, 1998, the work group published its final draft of
the Phase III report entitled ``Laboratory Evaluation of Static Sheen
Replacements: RPE Method and GC/MS Method.'' This report provides the
methods. The future work of the Analytical Work Group is to validate
these methods.
2. Retention on Cuttings
The goals of this work group were to determine the SBF retention on
cuttings using the equipment currently used in the Gulf of Mexico
(GOM), and investigate ways of determining the total quantity of SBF
discharged when drilling a well. To address the first goal, API
reported data from GOM wells on the amount of SBF base fluid retained
on drill cuttings. The results were published on August 29, 1997, in a
report entitled ``Retention of Synthetic-Based Drilling Material on
Cuttings Discharged to the Gulf of Mexico.''
To address the second goal of determining the total quantity of SBF
discharged, the work group has created a spreadsheet which records
information allowing two independent analyses of the SBF quantity
discharged. One method is based on a mass balance of the SBF, and the
other is based on retort measurements of the cuttings wastestream. Both
methods of analyses carry certain benefits and drawbacks. By comparing
the results from the two analyses, EPA intends to select one method as
preferred for the final rule. The work group is currently gathering
these comparative data. The preferred method will then be validated for
inclusion in the final rule. At this time, EPA thinks that the retort
measurement is preferable to implement, and therefore it is the method
proposed today. As further information is gathered, however, EPA may
decide that attainment of the limit in the final rule is to be
determined by the mass balance method.
3. Toxicity Testing
The goal of this work group was to define the toxicity test for
monitoring and compliance of SBF-cuttings. EPA has indicated that the
test could be performed on either the stock base fluid, or the SBF
separated from the cuttings at the point of discharge.
Through data generated by members of the work group, the work group
has shown that SBF and synthetic base fluid toxicity are mainly evident
in the sedimentary phase. When measured in the suspended particulate
phase (SPP) in the current Mysid shrimp toxicity test, the toxicity is
not evident and the results are highly variable, and are easily
affected by the intensity of stirring and emulsifier content of the
SBF.
Having shown that an aqueous phase test is unlikely to yield
satisfactory results with SBFs and associated base fluids, the work
group has been investigating sediment toxicity tests, mainly the 10-day
sediment toxicity test with amphipods (ASTM E1367-92). To effect this
work, API funded a currently ongoing contract to evaluate four test
methods: 10-day acute sediment toxicity test with (a) Ampelisca abdita,
(b) Leptocheirus plumulosus, and (c) Mysidopsis bahia, and (d) microtox
tests. Main issues that the work group hopes to resolve are
discriminatory power of the method and variability in results. Since
the API contract work began, the work group has considered many
variables to the sediment toxicity test to ameliorate these problems.
The work group is investigating: organisms other than amphipods, such
as Mysid shrimp and polychaetes; shortening the length of the test,
i.e. from 10 days to 4 days; and the use of formulated sediments in
place of natural sediments. Work continues to determine the most
appropriate method to evaluate the toxic effect of the SBF discharged
with drill cuttings.
4. Environmental Effects/Seabed Surveys
The goal of this work group was to determine the spacial and
temporal recovery of the seafloor at sites where SBF-cuttings had been
discharged, and compare these effects with effects caused by the
discharge of WBF and WBF-cuttings discharge.
The work group performed a five-day screening cruise at three
offshore oil platforms where SBFs has been used and SBF-cuttings
discharged for the purpose of gathering preliminary environmental
effects information. This screening cruise, and its planning, was
performed in collaboration with EPA and with the use of the EPA Ocean
Survey Vessel Peter W. Anderson. The study conducted a preliminary
evaluation of offshore discharge locations and determine the areal
extent of observable physical, chemical, and biological impact. EPA
intended that this base information would provide (1) information
relative to the immediate concerns on impacts, and (2) valuable
preliminary information for designing future offshore assessments.
The study provided preliminary information on cuttings deposition,
SBF content of nearfield marine sediments,
[[Page 5498]]
anoxia in nearfield sediments, qualitative information on biological
communities in the area, and toxicity of field collected sediments. The
results of this survey were published on October 21, 1998, in a report
entitled ``Joint EPA/Industry Screening Survey to Assess the Deposition
of Drill Cuttings and Associated Synthetic Based Mud on the Seabed of
the Louisiana Continental Shelf, Gulf of Mexico.''
The ongoing effort of the work group is to address CWA 403(c)
permit requirements for seabed surveys by organizing collaborative
industry seabed surveys at selected SBF-discharge sites.
D. EPA Research on Toxicity, Biodegradation, Bioaccumulation
Subsequent to today's proposal, EPA plans to compare the relative
environmental effects of SBFs and OBFs in terms of (i) sediment and
aquatic toxicity, (ii) biodegradation, and (iii) bioaccumulation. The
methods development to occur as part of this research, and the
resulting data, are intended to be used towards the final stock base
fluid limitations and SBF discharge limitations proposed today.
The base fluids to consider in the sediment toxicity,
biodegradation, and bioaccumulation tests are the full range of
synthetic and oleaginous base fluids. These include the synthetic oils
such as vegetable esters, linear alpha olefins, internal olefins and
poly alpha olefins, the traditional base oils of mineral oil and diesel
oil, and the newer more refined and treated oils such as enhanced
mineral oil and paraffinic oils. These oily base fluids are common in
that they are immiscible (do not mix) with water, and form drilling
fluids that do not disperse in water.
The outline of this research plan in terms of goals and
considerations is as follows:
For sediment toxicity, this plan intends to investigate
the effects of base fluid, whole mud formulation, and crude oil
contamination on sediment toxicity as measured by the 10-day acute
sediment toxicity test performed in natural sediment with Ampelisca
abdita and Leptocheirus plumulosus. The goals of this research are
threefold:
Amend the EPA 10-day acute sediment toxicity test for
application to SBFs and base fluids.
Determine the LC50 values for the base fluids
by this method, potentially for determination of stock limitations
values.
Determine the effects of mud formulation and crude oil
contamination on sediment toxicity by maintaining the base fluid
constant. The purpose is to investigate the parameters which affect
toxicity in SBFs.
For aqueous phase toxicity, this plan intends to
investigate if any correlation exists between aqueous phase toxicity to
Mysid shrimp and sediment toxicity.
For biodegradation, this plan intends to perform the solid
phase test or modified solid phase test as developed by the Scottish
Office Agriculture, Environment and Fisheries Department for a range of
oily base fluids, and environments of the Gulf of Mexico, Offshore
California, Cook Inlet Alaska, and Offshore Alaska.
For bioaccumulation, this plan intends to test
bioconcentration in Macoma nasuta and Nereis virens.
The research concerning sediment toxicity testing that API supports
is seen as complementary to, and not overlapping with, this EPA plan.
API's goal is to identify a bioassay test organism and protocol to
accurately and reliably evaluate the toxicity of SBF and OBF in
sediments. The API research is concentrating efforts on using both
formulated and natural sediments, and possibly a test period shorter
than the standard 10-day EPA method. Thus, while EPA is focusing on
investigating the parameters that affect toxicity of SBFs, the API
research is looking ahead to discharge monitoring requirements with the
goal of identifying an appropriate and reliable test method.
E. EPA Investigation of Solids Control Technologies for Drilling Fluids
EPA has contacted numerous vendors of solids control equipment and
requested information on performance and cost of the various solids
separation units available. EPA has also received information from
operators data showing the performance of the vibrating centrifuge
technology. As part of its investigation of solids control equipment
used on offshore drilling platforms, EPA visited Amoco's Marlin
deepwater drilling project aboard the Amirante semi-submersible
drilling platform located in Viosca Knoll Block 915 approximately 100
miles south of Mobile, Alabama. The primary purpose of this site visit
was to observe the demonstration of the vibrating centrifuge drilling
fluid recovery device heretofore used only on North Sea drilling
projects. The device reportedly can produce drill cuttings containing
less than 6 percent by volume synthetic drilling fluid on wet cuttings
when well operated and maintained and used in conjunction with shale
shakers that are well operated and maintained. The information gathered
by the EPA during this trip is described in a report dated August 7,
1998, entitled ``Demonstration of the `Mud 10' Drilling Fluid Recovery
Device at the Amoco Marlin Deepwater Drill Site.''
F. Assistance From Other State and Federal Agencies
The United States Department of Interior Minerals Management
Service (MMS) maintains data of the number of wells drilled in offshore
waters under MMS jurisdiction, i.e., those that are not territorial
seas. In general, this covers the offshore waters beyond 3 miles from
the shoreline, which corresponds with the area were drilling wastes are
currently allowed for discharge and so is the same area affected by
this rule. MMS supplied data for years 1995, 1996, and 1997 of the
number of wells drilled in the GOM and offshore California according to
depth (less than or greater than 1000 feet water depth) and type of
well (exploratory or development). Since Texas jurisdiction over oil
and gas leases extends out to 10 miles, information was requested and
received from the Texas Railroad Commission regarding the number of
wells drilled in Texas territorial seas from 3 miles to 10 miles from
shore. This is the area in the GOM that is affected by this proposed
rule, but not included in the MMS data.
Information concerning the number of wells drilled in the state
waters of Upper Cook Inlet, Alaska, was gathered from the Alaska Oil
and Gas Commission. The Alaska Oil and Gas Commission provided
information of the number of wells drilled in Upper Cook Inlet for the
years 1995, 1996, and 1997, according to type of well as exploratory or
development.
MMS also assisted in developing the cruise plan of the screening
seabed survey mentioned in section V.C.4 above.
The United States Department of Energy (DOE) has been active in
assisting EPA to gather information concerning drilling waste disposal
methods and costs, and type of fuel used on offshore platforms. In
November 1998 Argonne National Laboratory, under contract with DOE,
published the results of this information gathering effort in a report
entitled ``Data Summary of Offshore Drilling Waste Disposal
Practices.''
Also under contract with DOE, Brookhaven National Laboratory
developed a comparative risk assessment for the discharge of SBFs. The
risk assessment, published November 1998, is entitled ``Framework for a
Comparative Environmental Assessment of Drilling Fluids.''
[[Page 5499]]
VI. Development of Effluent Limitations Guidelines and Standards
A. Waste Generation and Characterization
Drill cuttings are produced continuously at the bottom of the hole
at a rate proportionate to the advancement of the drill bit. These
drill cuttings are carried to the surface by the drilling fluid, where
the cuttings are separated from the drilling fluid by the solids
control system. The drilling fluid is then sent back down hole,
provided it still has characteristics to meet technical requirements.
Various sizes of drill cuttings are separated by the solids separations
equipment, and it is necessary to remove the fines (small sized
cuttings) as well as the large cuttings from the drilling fluid to
maintain the required flow properties.
SBFs, used or unused, are considered a valuable commodity and not a
waste. It is industry practice to continuously reuse the SBF while
drilling a well interval, and at the end of the well, to ship the
remaining SBF back to shore for refurbishment and reuse. Compared to
WBFs, SBFs are relatively easy to separate from the drill cuttings
because the drill cuttings do not disperse in the drilling fluid to the
same extent. With WBF, due to dispersion of the drill cuttings,
drilling fluid components often need to be added to maintain the
required drilling fluid properties. These additions are often in excess
of what the drilling system can accommodate. The excess ``dilution
volume'' of WBF is a resultant waste. This dilution volume waste does
not occur with SBF. For these reasons, SBF is only discharged as a
contaminant of the drill cuttings wastestream. It is not discharged as
neat drilling fluid (drilling fluid not associated with cuttings).
The top of the well is normally drilled with a WBF. As the well
becomes deeper, the performance requirements of the drilling fluid
increase, and the operator may, at some point, decide that the drilling
fluid system should be changed to either a traditional OBF based on
diesel oil or mineral oil, or an SBF. The system, including the drill
string and the solids separation equipment, must be changed entirely
from the WBF to the SBF (or OBF) system, and the two do not function as
a blended system. The entire system is either (a) a water dispersible
drilling fluid such as a WBF, or (b) a water non-dispersible drilling
fluid such as an SBF. The decision to change the system from a WBF
water dispersible system to an OBF or SBF water non-dispersible system
depends on many factors including:
The operational considerations, i.e. rig type (risk of
riser disconnects with floating drilling rigs), rig equipment, distance
from support facilities,
The relative drilling performance of one type fluid
compared to another, e.g., rate of penetration, well angle, hole size/
casing program options, horizontal deviation,
The presence of geologic conditions that favor a
particular fluid type or performance characteristic, e.g., formation
stability/sensitivity, formation pore pressure vs. fracture gradient,
potential for gas hydrate formation,
Drilling fluid cost--base cost plus daily operating cost,
Drilling operation cost--rig cost plus logistic and
operation support,
Drilling waste disposal cost.
Industry has commented that while the right combination of factors that
favor the use of SBF can occur in any area, they most frequently occur
with ``deep water'' operations. This is due to the fact that these
operations are higher cost and can therefore better justify the higher
initial cost of SBF use.
The volume of cuttings generated while drilling the SBF intervals
of a well depends on the type of well, development or production, and
the water depth. According to analyses of the model wells provided by
industry representatives, wells drilled in less than 1,000 feet of
water are estimated to generate 565 barrels for a development well and
1,184 barrels for an exploratory well. Wells drilled in water greater
than 1,000 feet deep are estimated to generate 855 barrels for a
development well, and 1,901 for an exploratory well. These values
assume 7.5 percent washout, based on the rule of thumb reported by
industry representatives of 5 to 10 percent washout when drilling with
SBF. Washout is caving in or sluffing off of the well bore. Washout,
therefore, increases hole volume and increases the amount of cuttings
generated when drilling a well. Assuming no washout, the values above
become, respectively, 526, 1,101, 795, and 1,768, barrels.
The drill cuttings range in size from large particles on the order
of a centimeter in size to small particles a fraction of a millimeter
in size, called fines. As the drilling fluid returns from downhole
laden with drill cuttings, it normally is first passed through primary
shale shakers which remove the largest cuttings, ranging in size of
approximately 1 to 5 millimeters. The drilling fluid may then be passed
over secondary shale shakers to remove smaller drill cuttings. Finally,
a portion or all of the drilling fluid may be passed through a
centrifuge or other shale shaker with a very fine mesh screen, for the
purpose of removing the fines. It is important to remove fines from the
drilling fluid in order to maintain the desired flow properties of the
active drilling fluid system. Thus, the cuttings wastestream normally
consists of larger cuttings from the primary shale shakers and fines
from a fine mesh shaker or centrifuge, and may also consist of smaller
cuttings from a secondary shale shaker. Before being discharged, the
larger cuttings are sometimes sent through another separation device in
order to recover additional drilling fluid.
The recovery of SBF from the cuttings serves two purposes. The
first is to deliver drilling fluid for reintroduction to the active
drilling fluid system, and the second is to minimize the discharge of
SBF. The recovery of drilling fluid from the cuttings is a conflicting
concern, because as more aggressive methods are used to recover the
drilling fluid from the cuttings, the cuttings tend to break down and
become fines. The fines are not only more difficult to separate from
the drilling fluid, but as stated above they also deteriorate the
properties of the drilling fluid. Increased recovery from the cuttings
is more problematic for WBF than with SBF because the WBF water-wets
the cuttings which encourages the cuttings to disperse and spoil the
drilling fluid properties. Therefore, compared to WBF, more aggressive
methods of recovering SBF from the cuttings wastestream are practical.
These more aggressive methods may be justified for cuttings associated
with SBF so as to reduce the discharge of SBF. This, consequently, will
reduce the potential to cause anoxia (lack of oxygen) in the receiving
sediment as well as reduce the quantity of toxic organic and metallic
components of the drilling fluid discharged.
Drill cuttings are typically discharged continuously as they are
separated from the drilling fluid in the solids separation equipment.
The drill cuttings will also carry a residual amount of adhered
drilling fluid. TSS makes up the bulk of the pollutant loadings, and is
comprised of two components: the drill cuttings themselves, and the
solids in the adhered drilling fluid. The drill cuttings are primarily
small bits of stone, clay, shale, and sand. The source of the solids in
the drilling fluid is primarily the barite weighting agent, and clays
which are added to modify the viscosity. Because the quantity of TSS is
so high and consists of mainly large particles which settle quickly,
discharge of SBF drill cuttings can cause benthic
[[Page 5500]]
smothering and/or sediment grain size alteration resulting in potential
damage to invertebrate populations and alterations in benthic community
structure.
Additionally, environmental impacts can be caused by toxic,
conventional, and nonconventional pollutants adhering to the solids.
The adhered SBF drilling fluid is mainly composed, on a volumetric
basis, of the synthetic material, or more broadly speaking, oleaginous
material. The oleaginous material may also be toxic or bioaccumulate,
and it may contain priority pollutants such as polynuclear aromatic
hydrocarbons (PAHs). This oleaginous material may cause hypoxia
(reduction in oxygen) or anoxia in the immediate sediment, depending on
bottom currents, temperature, and rate of biodegradation. Oleaginous
materials which biodegrade quickly will deplete oxygen more rapidly
than more slowly degrading materials. EPA, however, thinks that fast
biodegradation is environmentally preferable to persistence despite the
increased risk of anoxia which accompanies fast biodegradation. This is
because recolonization of the area impacted by the discharge of SBF-
cuttings or OBF-cuttings has been correlated with the disappearance of
the base fluid in the sediment, and does not seem to be correlated with
anoxic effects that may result while the base fluid is disappearing. In
studies conducted in the North Sea, base fluids that biodegrade faster
have been found to disappear more quickly, and recolonization at these
sites has been more rapid.
As a component of the drilling fluid, the barite weighting agent is
also discharged as a contaminant of the drill cuttings. Barite is a
mineral principally composed of barium sulfate, and it is known to
generally have trace contaminants of several toxic heavy metals such as
mercury, cadmium, arsenic, chromium, copper, lead, nickel, and zinc.
B. Selection of Pollutant Parameters
1. Stock Limitations of Base Fluids
a. General.--EPA is proposing to establish BAT and NSPS that would
require the synthetic materials and other oleaginous materials which
form the base fluid of the SBFs and other non-aqueous drilling fluids
to meet limitations on PAH content, sediment toxicity and
biodegradation. The technology basis for meeting these limits would be
product substitution, or zero discharge based on land disposal or
injection if these limits are not met. These parameters are being
regulated to control the discharge of certain toxic and nonconventional
pollutants. A large range of synthetic, oleaginous, and water miscible
materials have been developed for use as base fluids. These stock
limitations on the base fluid are intended to encourage product
substitution reflecting best available technology wherein only those
synthetic materials and other base fluids which minimize potential
loadings and toxicity may be discharged.
b. PAH Content.--EPA proposes to regulate PAH content of base
fluids because PAHs are comprised of toxic priority pollutants. SBF
base fluids typically do not contain PAHs, whereas the traditional OBF
base fluids of diesel and mineral oil typically contain on the order of
5 to 10 percent PAH in diesel oil and 0.35 percent PAH in mineral oil.
The PAHs typically found in diesel and mineral oil include the toxic
priority pollutants fluorene, naphthalene, phenanthrene, and others,
and nonconventional pollutants such as alkylated benzenes and
biphenyls. Thus, this stock limitation would be one component of a rule
reflecting the use of the best available technology.
c. Sediment Toxicity.--EPA proposes to regulate sediment toxicity
in base fluids and SBFs as a nonconventional pollutant parameter, as an
indicator for toxic components of base fluids or drilling fluid. Some
of the toxic components of the base fluids may include enhanced mineral
oils, internal olefins, linear alpha olefins, paraffinic oils,
vegetable esters of 2-hexanol and palm kernel oil, and other oleaginous
materials. Some of the possible toxic components of drilling fluids may
include the same components as the base fluid, and in addition mercury,
cadmium, arsenic, chromium, copper, lead, nickel, and zinc, formation
oil contaminants, and other intended or unintended components of the
drilling fluid. It has been shown, during EPA's development of the
Offshore Guidelines, that establishing limits on toxicity encourages
the use of less toxic drilling fluids and additives. Many of the
synthetic base fluids have been shown to have lower toxicity than
diesel and mineral oil, but among the synthetic and other oleaginous
base fluids some are more toxic than others. Today's proposed discharge
option includes a sediment toxicity limitation of the SBF's base fluid
stock material, as measured by the 10-day sediment toxicity test (ASTM
E1367-92) using a natural sediment and Leptocheirus plumulosus as the
test organism.
Subsequent to this proposal and before the final rule, EPA intends
to gather information to determine how to most appropriately control
toxicity and solicit comment on these findings. The sediment toxicity
test may be altered, for instance, in terms of test organism (other
amphipods or possibly a polychaete), sediment type (formulated in place
of natural), or length of test (to shorten the 10-day test period).
Further, while today's proposal includes a sediment toxicity limitation
of the base fluid stock material, the final discharge option to control
toxicity might consist of a different option.
EPA would prefer to control sediment toxicity at the point of
discharge as opposed to controlling the base fluid. EPA realizes,
however, that the sediment toxicity test may be impractical to
implement as a discharge requirement due to potential problems in the
availability of uniform sediment and other factors affecting test
variability. If EPA finds, through subsequent research, that the
sediment toxicity test at the point of discharge is both practical and
superior to the base fluid toxicity as an indicator of the toxicity of
the SBF at the point of discharge, EPA might apply the sediment
toxicity test to the SBF at the point of discharge in place of today's
proposed method of the sediment toxicity test to the base fluid.
If the sediment toxicity test of neither the SBF at point of
discharge nor synthetic base fluid as a stock limitation is found to be
practical due to variability, lack of discriminatory power, or other
problems, EPA will search for an alternative toxicity test. One
candidate is modification to the current SPP toxicity test, or aquatic
phase toxicity test. EPA has several concerns with applying the current
SPP test to SBFs. EPA has received information from industry sources
and testing laboratories that the results from the SPP test applied to
SBFs are highly dependent on both the agitation when mixing the
seawater with the SBF and the amount and type of emulsifiers in the SBF
formulation. Further, results to date show that, compared to the
aquatic toxicity test, the sediment toxicity test provides a better
correlation with known toxicity effects of the various synthetic and
oleaginous base fluids, and the experimental situation more closely
mimics the actual fate of the drilling fluid. While EPA does not think
that the current SPP test is useful for application to SBFs,
modifications to either the method or limitation may render it
functional. Thus, EPA intends to investigate the aquatic phase toxicity
test as a possible control in the event that the sediment toxicity test
of the drilling fluid is impractical and the
[[Page 5501]]
sediment toxicity test of the base fluid is either impractical or
inadequate to control the toxicity of the SBF at the point of
discharge.
EPA intends, therefore, to investigate further the most appropriate
test method for controlling toxicity of SBF discharges, and to validate
this method. EPA intends to publish any additional data concerning this
limitation in a notice prior to publication of the final rule.
d. Biodegradation.--EPA proposes to limit biodegradation as an
indicator of the extent, in level and duration, of the toxic effect of
toxic components of nonconventional pollutants present in the base
fluids, e.g., poly alpha olefins, enhanced mineral oils, internal
olefins, linear alpha olefins, paraffinic oils, and vegetable ester of
2-hexanol and palm kernel oil. The various SBF base fluids vary widely
in biodegradation rate, as measured by the solid phase test and
simulated seabed tests. Based on results from seabed surveys at sites
where various base fluids have been discharged with drill cuttings, EPA
believes that the results from both measurement methods are indicative
of the relative rates of biodegradation in the marine environment. In
addition, EPA thinks this parameter correlates strongly with the rate
of recovery of the seabed where SBF-cuttings have been discharged.
While EPA is proposing to use the solid phase test to measure
compliance with the biodegradation limitation, this test is not yet an
EPA validated method. In addition to validating the method for the
final rule, EPA intends to gather additional data in support of the
biodegradation rate limitation. EPA plans to present any additional
data it collects towards this limitation in a notice subsequent to
today's proposed rule and before the final rule.
e. Bioaccumulation.--While not a part of today's proposal, EPA is
also considering establishing BAT and NSPS that would require the
synthetic materials and other base fluids used in non-aqueous drilling
fluids to meet limitations on bioaccumulation potential. The regulated
parameters would be the nonconventional and toxic priority pollutants
that bioaccumulate. Based on current information, EPA believes that the
base fluid controls on PAH content, sediment toxicity, and
biodegradation rate being proposed today are sufficient to control
bioaccumulation. EPA intends, however, to study the bioaccumulation
potential of the various synthetic base fluids for comparison, and
subsequently solicit comments on the results if EPA thinks that some
measure of bioaccumulation potential is needed to control adequately
the SBF-cuttings wastestream.
2. Discharge Limitations
a. Free Oil.--Under BPT and BCT limitations for SBF-cuttings, EPA
would retain the prohibition on the discharge of free oil as determined
by the static sheen test. Under this prohibition, drill cuttings may
not be discharged when the associated drilling fluid would fail the
static sheen test defined in Appendix 1 to 40 CFR Part 435, Subpart A.
The prohibition on the discharge of free oil is intended to minimize
the formation of sheens on the surface of the receiving water. The
regulated parameter of the no free oil limitation would be the
conventional pollutants oil and grease which separate from the SBF and
cause a sheen on the surface of the receiving water.
The free oil discharge prohibition does not control the discharge
of oil and grease and crude oil contamination in SBFs as it would in
WBFs. With WBFs, oils which may be present (such as diesel oil, mineral
oil, formation oil, or other oleaginous materials) are present as the
discontinuous phase. As such these oils are free to rise to the surface
of the receiving water where they may appear as a film or sheen upon or
discoloration of the surface. By contrast, the oleaginous matrices of
SBFs do not disperse in water. In addition they are weighted with
barite, which causes them to sink as a mass without releasing either
the oleaginous materials which comprise the SBF or any contaminant
formation oil. Thus, the test would not identify these pollutants.
However, a portion of the synthetic material comprising the SBF may
rise to the surface to cause a sheen. These components that rise to the
surface fall under the general category of oil and grease and are
considered conventional pollutants. Therefore, the purpose of the no
free oil limitation of today's proposal is to control the discharge of
conventional pollutants which separate from the SBF and cause a sheen
on the surface of the receiving water. The limitation, however, is not
intended to control formation oil contamination nor the total quantity
of conventional pollutants discharged.
b. Formation Oil Contamination.--Formation oil contamination of the
SBF associated with the cuttings would be limited under BAT and NSPS.
Formation oil is an ``indicator'' pollutant for the many toxic and
priority pollutant components present in formation (crude) oil, such as
aromatic and polynuclear aromatic hydrocarbons. These pollutants
include benzene, toluene, ethylbenzene, naphthalene, phenanthrene, and
phenol. (See Development Document Chapter VII). The primary limitation
is based on a fluorescence test. This test is considered an
appropriately ``weighted'' test because crude oils containing more
toxic aromatic and PAH components tend to show brighter fluorescence
and hence noncompliance at a lower level of contamination. Since
fluorescence is a relative brightness test, gas chromatography with
mass spectroscopy detection (GC/MS) is provided as a baseline method
before the drilling fluid is delivered for use, and is also available
as an assurance method when the results from the fluorescence
compliance method are in doubt.
c. Retention of SBF on Cuttings.--The retention of SBF on drill
cuttings would be limited under BAT and NSPS. This limitation controls
the quantity of SBF discharged with the drill cuttings. Both
nonconventional and priority toxic pollutants would be controlled by
this limitation. Nonconventionals include the SBF base fluids, such as
vegetable esters, internal olefins, linear alpha olefins, paraffinic
oils, mineral oils, and others. This limitation would also limit the
toxic effect of the drilling fluid and the persistence or
biodegradation of the base fluid. Several toxic and priority pollutant
metals are present in the barite weighting agent, including arsenic,
chromium, copper, lead, mercury, nickel, and zinc, and nonconventional
pollutants such as aluminum and tin.
The emulsifying and wetting agents of the SBF would also be
controlled by limiting the amount of SBF discharged. EPA solicits
information concerning the composition of the wetting and emulsifying
agents so that they can be classified as conventional, nonconventional,
or toxic pollutants.
Today's proposed rule uses the retort method to determine
compliance with the limit. The limit is expressed as percentage base
fluid on wet cuttings (weight/weight), averaged over the well sections
drilled with SBF. This method has not yet been validated by EPA.
Further, EPA is currently researching a mass balance method as an
alternative method to determine the quantity of SBF discharged. After
EPA has gathered sufficient data using the two methods in a comparative
analysis, EPA intends to validate the preferred method and solicit
comment concerning the method to be applied for the final rule.
3. Maintenance of Current Requirements
EPA would retain the existing BAT and NSPS limitations on the stock
barite of 1 mg/kg mercury and 3 mg/kg
[[Page 5502]]
cadmium. These limitations would control the levels of toxic pollutant
metals because cleaner barite that meets the mercury and cadmium limits
is also likely to have reduced concentrations of other metals.
Evaluation of the relationship between cadmium and mercury and the
trace metals in barite shows a correlation between the concentration of
mercury with the concentration of arsenic, chromium, copper, lead,
molybdenum, sodium, tin, titanium and zinc. (See the Offshore
Development Document in Section VI).
EPA also would retain the BAT and NSPS limitations prohibiting the
discharge of drilling wastes containing diesel oil in any amount.
Diesel oil is considered an ``indicator'' for the control of specific
toxic pollutants. These pollutants include benzene, toluene,
ethylbenzene, naphthalene, phenanthrene, and phenol. Diesel oil may
contain from 3 to 10 percent by volume PAHs, which constitute the more
toxic components of petroleum products.
C. Regulatory Options Considered for SBFs Not Associated With Drill
Cuttings
Today EPA proposes, under BPT, BCT, BAT, and NSPS, zero discharge
for SBFs not associated with drill cuttings. This option is technically
available and economically achievable with equipment commonly used. It
is also current industry practice due to the value of SBFs recovered
and reused. Since this option reflects current industry practice, it
has no non-water quality environmental impacts.
Industry sources have indicated that at times, there may be minor
drips or spills of SBFs that occur on the platform. EPA is considering
whether these discharges should be governed by the zero discharge
requirement, or whether to view the zero discharge requirements as
being limited to discharge of whole drilling fluids, and allowing
unintentional drips and spills to be treated as miscellaneous wastes.
EPA solicits comment on this approach. EPA thinks that the best way to
control these discharges would be through the use of BMPs and solicits
comment on what types of BMPs would be effective for controlling these
discharges and whether such BMPs should be part of this effluent
guideline or be applied by the permit authority.
D. Regulatory Options Considered for SBFs Associated With Drill
Cuttings
EPA considered two options for today's proposed rule for SBFs
associated with drill cuttings, or SBF-cuttings: a discharge option and
a zero discharge option. EPA has selected the discharge option as the
basis for today's proposal. As detailed above, this discharge option
controls under BAT and NSPS the stock base fluid through limitations on
PAH content, sediment toxicity, and biodegradation rate, and controls
at the point of discharge under BPT and BCT sheen formation and under
BAT and NSPS formation oil content and quantity of SBF discharged. The
discharge option maintains current requirements of stock limitations on
barite of mercury and cadmium, and the diesel oil discharge
prohibition. EPA at this time thinks that all of these components are
essential for appropriate control of the SBF cuttings wastestream.
Although not the basis for today's proposal, EPA considered zero
discharge as an option for BPT, BCT, BAT, and NSPS. Under zero
discharge all pollutants would be controlled in SBF discharges. This
option was clearly technically feasible and economically achievable
because in the past SBFs did not exist, and industry was able to
operate using only the traditional non-dischargeable OBFs based on
diesel oil and mineral oil.
EPA presently rejects zero discharge as the preferred option
because it would result in unacceptable non-water quality environmental
impacts. If EPA were to choose zero discharge for SBF-cuttings,
operators would not have an incentive to use SBFs since they are more
expensive than OBFs. Thus, if EPA requires zero discharge, OBF-cuttings
would continue to be injected or shipped to shore for land disposal.
EPA's analysis shows that under this option as compared to the
discharge option, for existing and new sources combined, there would be
172 million pounds annually of OBF-cuttings shipped to shore for
disposal in non-hazardous oilfield waste sites and 40 million pounds
annually injected, with associated fuel use of 29,000 BOE and annual
air emissions of 450 tons. EPA believes these impacts far outweigh the
water impacts associated with these discharges detailed in Section VIII
of this preamble. EPA's current analysis shows that the impacts of
these discharges to water are of limited scope and duration,
particularly if EPA controls the discharges of SBFs to the best
environmental performers that also meet the technical requirements
needed to drill. By contrast, the landfilling of OBF-cuttings is of a
longer term duration and associated pollutants may effect ambient air,
soil, and groundwater quality. For these reasons, under EPA's authority
to consider the non-water quality environmental impacts of its rule,
EPA rejects zero discharge of SBF-cuttings.
Nonetheless, while discharge with adequate controls is preferred
over zero discharge, discharge with inadequate controls is not
preferred over zero discharge. EPA believes that to allow discharge of
SBF-cuttings, there must be appropriate controls to ensure that EPA's
discharge limitations reflect the ``best available technology'' or
other appropriate level of technology. EPA has worked with industry to
address the determination of PAH content, sediment toxicity,
biodegradation, bioaccumulation, the quantity of SBF discharged, and
formation oil contamination. The successful completion of these efforts
is necessary for EPA to continue to reject zero discharge.
E. BPT Technology Options Considered and Selected
As previously discussed, Section 304(b)(1)(A) of the CWA requires
EPA to identify effluent reductions attainable through the application
of ``best practicable control technology currently available for
classes and categories of point sources.'' Generally, EPA determines
BPT effluent levels based upon the average of the best existing
performances by plants of various sizes, ages, and unit processes
within each industrial category or subcategory. In industrial
categories where present practices are uniformly inadequate, however,
EPA may determine that BPT requires higher levels of control than any
currently in place if the technology to achieve those levels can be
practicably applied. See A Legislative History of the Federal Water
Pollution Control Act Amendments of 1972, U.S. Senate Committee of
Public Works, Serial No. 93-1, January 1973, p. 1468.
In addition, CWA Section 304(b)(1)(B) requires a cost assessment
for BPT limitations. In determining the BPT limits, EPA must consider
the total cost of treatment technologies in relation to the effluent
reduction benefits achieved. This inquiry does not limit EPA's broad
discretion to adopt BPT limitations that are achievable with available
technology unless the required additional reductions are ``wholly out
of proportion to the costs of achieving such marginal level of
reduction.'' See Legislative History, op. cit. p. 170. Moreover, the
inquiry does not require the Agency to quantify benefits in monetary
terms. See e.g. American Iron and Steel Institute v. EPA, 526 F. 2d
1027 (3rd Cir., 1975).
In balancing costs against the benefits of effluent reduction, EPA
considers the volume and nature of expected
[[Page 5503]]
discharges after application of BPT, the general environmental effects
of pollutants, and the cost and economic impacts of the required level
of pollution control. In developing guidelines, the Act does not
require consideration of water quality problems attributable to
particular point sources, or water quality improvements in particular
bodies of water. Therefore, EPA has not considered these factors in
developing the limitations being proposed today. See Weyerhaeuser
Company v. Costle, 590 F. 2d 1011 (D.C. Cir. 1978).
EPA today proposes BPT effluent limitations for the cuttings
contaminated with SBF and other non-aqueous drilling fluids. The BPT
effluent limitations proposed today would control free oil as a
conventional pollutant. The limitation is no free oil as measured by
the static sheen test, performed on SBF separated from the cuttings.
In setting the no free oil limitation, EPA considered the sheen
characteristics of currently available SBFs. Since this requirement is
currently met by dischargers in the Gulf of Mexico, EPA anticipates no
additional costs to the industry to comply with this limitation.
EPA also considered a BPT level of control for the quantity of SBF
discharged with the cuttings consisting of improved use of currently
existing shale shaker equipment. However, EPA did not have enough
information to establish BPT beyond current performance. Further, EPA
is not setting a BPT limit based on current performance because
operators already have incentive to recover as much SBFs as possible
through the optimization of existing equipment due to the value of the
SBFs. Therefore, a BPT limitation based on the current equipment, and
as it is currently used, would not have any practical effect on the
quantity of SBF discharged with the cuttings. Further, given that the
BAT and NSPS limitations would be more stringent and control the
conventional pollutants in addition to the non-conventional and toxic
pollutants, EPA saw no reason to expend time and resources to develop a
different, less restrictive BPT limit.
F. BCT Technology Options Considered and Selected
In July 1986, EPA promulgated a methodology for establishing BCT
effluent limitations. EPA evaluates the reasonableness of BCT candidate
technologies--those that are technologically feasible--by applying a
two-part cost test: (1) a POTW test; and (2) an industry cost-
effectiveness test.
EPA first calculates the cost per pound of conventional pollutant
removed by industrial dischargers in upgrading from BPT to a BCT
candidate technology and then compares this cost to the cost per pound
of conventional pollutants removed in upgrading POTWs from secondary
treatment. The upgrade cost to industry must be less than the POTW
benchmark of $0.25 per pound (in 1976 dollars).
In the industry cost-effectiveness test, the ratio of the
incremental BPT to BCT cost divided by the BPT cost for the industry
must be less than 1.29 (i.e., the cost increase must be less than 29
percent).
In today's proposal, EPA is proposing to establish a BCT limitation
of no free oil equivalent to the BPT limitation of no free oil as
determined by the static sheen test. In developing BCT limits, EPA
considered whether there are technologies (including drilling fluid
formulations) that achieve greater removals of conventional pollutants
than proposed for BPT, and whether those technologies are cost-
reasonable according to the BCT Cost Test. EPA identified no
technologies that can achieve greater removals of conventional
pollutants than proposed for BPT that are also cost-reasonable under
the BCT Cost Test, and accordingly EPA proposes BCT effluent
limitations equal to the proposed BPT effluent limitations guidelines.
G. BAT Technology Options Considered and Selected
EPA today proposes BAT effluent limitations for the cuttings
contaminated with SBFs. The BAT effluent limitations proposed today
would control the stock base fluids in terms of PAH content, sediment
toxicity, and biodegradation. Controls at the point of discharge
include formation oil contamination and the quantity of SBF discharged.
This level of control has been developed taking into consideration the
availability and cost of oleaginous (SBF) base fluids in terms of PAH
content, sediment toxicity, and biodegradation rate; the frequency of
formation oil contamination at the control level; the performance and
cost of equipment to recover SBF from the drill cuttings. The technical
availability and economic achievability of today's proposed limitations
is discussed below by regulated parameter.
1. Stock Base Fluid Technical Availability and Economic Achievability
a. Introduction.--As SBFs have developed over the past few years,
the industry has come to use mainly a few primary base fluids. These
include the vegetable esters, internal olefins, linear alpha olefins,
and poly alpha olefins. Thus, these are the base fluids for which EPA
has data and costs to develop the effluent limitations of today's
proposed rule. In this document, vegetable ester means a monoester of
2-ethylhexanol and saturated fatty acids with chain lengths in the
range C8-C16, internal olefin means a series of
isomeric forms of C16 and C18 alkenes, linear
alpha olefin means a series of isomeric forms of C14 and
C16 monoenes, and poly alpha olefins means a mix mainly
comprised of a hydrogenated decene dimer C20H62
(95%), with lesser amounts of C30H62 (4.8%) and
C10H22 (0.2%). EPA also has data on other
oleaginous base fluids, such as enhanced mineral oil, paraffinic oils,
and the traditional OBF base fluids mineral oil and diesel oil.
The stock base fluid limitations presented below are based on
currently available base fluids, and the limitations would be
achievable through product substitution. EPA anticipates that the
currently available and economically achievable base fluids meeting all
requirements would include vegetable esters and internal olefins. EPA
also solicits data on linear alpha olefins and certain paraffinic oils
to determine whether these base fluids are comparable in terms of
sediment toxicity, biodegradation, and bioaccumulation.
b. PAH Content Technical Availability.--Today's proposed limitation
of PAH content is 0.001 percent, or 10 parts per million (ppm), weight
percent PAH expressed as phenanthrene. This limitation is based on the
availability of base fluids that are free of PAHs and the detection of
the PAHs by EPA Method 1654A. EPA's proposed PAH content limitation is
technically available. Producers of several SBF base fluids have
reported to EPA that their base fluids are free of PAHs. The base
fluids which suppliers have reported are free of PAHs include linear
alpha olefins, internal olefins, vegetable esters, certain enhanced
mineral oils, synthetic paraffins, certain non-synthetic paraffins, and
others. See the Development Document, Chapter VII. Compliance with the
BAT and NSPS stock limitations on PAH content may be achieved by
product substitution.
c. Sediment Toxicity Technical Availability.--EPA is today
proposing a sediment toxicity stock base fluid limitation that would
allow only the discharge of SBF-cuttings using base fluids as toxic or
less toxic, but not more toxic, than C16-C18
internal olefin.
[[Page 5504]]
Alternatively, this limitation could be expressed as the
LC50 of the base fluid minus the LC50 of the
C16-C18 internal olefin shall not be less than
zero. Based on information available to EPA at this time, the only base
fluids which would attain this limitation are the internal olefins and
vegetable esters.
EPA finds this limit to be technically available because
information in the rulemaking record supports that internal olefin SBFs
and vegetable ester SBFs together have performance characteristics
enabling them to be used in a wide variety of drilling situations
offshore. Marketing data given to the EPA shows that, at least for
certain of the major drilling fluid suppliers, internal olefin SBFs are
currently the most popular SBFs used in the Gulf of Mexico.
Various researchers have performed toxicity testing of the
synthetic base fluids with the 10-day sediment toxicity test (EPA/600/
R-94/025) using a natural sediment and Leptocheirus plumulosus as the
test organism. The synthetic base fluids have been shown to have lower
toxicity than diesel and mineral oil, and among the synthetic and other
oleaginous base fluids some are more toxic than others. For example,
Still et al. reported the following 10-day LC50 results,
expressed as mg base fluid/Kg dry sediment: diesel LC50 of
850, enhanced mineral oil LC50 of 251, internal olefin
LC50 of 2,944, and poly alpha olefin LC50 of
9,636. A higher LC50 value means the material is less toxic.
Similar results, with the same trend in toxicity in the base fluids
above, have been reported by Hood et al. Candler et al. performed the
10-day sediment toxicity test with the amphipod Ampelicsa abdita in
place of Leptocheirus plumulosus, and again obtained very similar
results as follows: diesel LC50 of 879, enhanced mineral oil
LC50 of 557, internal olefin LC50 of 3,121, and
PAO LC50 of 10,680.
None of these researchers reported sediment toxicity values for
vegetable esters. Recently, industry has evaluated a number of base
fluids including vegetable esters. While the absolute values are not
comparable because the tests were performed on the drilling fluid and
not just the base fluid, the results showed the vegetable ester to be
less toxic than the internal olefin.
Researchers in the United Kingdom and Norway investigating effects
in the North Sea have conducted sediment toxicity tests on other
organisms, namely Corophium volutator and Abra alba. Similar trends
were seen in the measured toxicity, with vegetable ester having very
low sediment toxicity (very high LC50), poly alpha olefin
having a mid range toxicity, and internal olefin having a higher
toxicity, in this comparison.
While the poly alpha olefins were found to have the lowest toxicity
of the measured base fluids (excludes vegetable esters), EPA did not
base the toxicity limitation on poly alpha olefins because, as
presented below, they biodegrade much more slowly and so are unlikely
to pass the biodegradation limitation. EPA intends to generate and
gather additional data comparing the toxicity of the various base
fluids, especially to compare the vegetable ester toxicity with that of
the olefins since, at this time, directly comparable data is not
available. If vegetable esters are found to have significant reduced
toxicity compared to the other base fluids, EPA may choose to base the
toxicity limitation on vegetable esters. EPA has concerns, however,
over the technical performance and possible non-water quality
implications with the use of vegetable ester as the only technology
available to meet the stock base fluid limitations, as discussed below
under biodegradation.
As an alternative, EPA solicits comment on a numeric limitation of
a minimum LC50 of 2,600 mg base fluid/Kg dry sediment as an
appropriate level of control, based on the toxicity of
C16-C18 internal olefins as determined by the 10-
day sediment toxicity test using Leptocheirus plumulosus as the test
organism. If EPA pursues this approach, EPA expects that it may need to
revise this numeric limitations due to the variability currently
experienced with this test.
d. Biodegradation Rate Technical Availability.--Today's proposed
limitation of biodegradation rate for the base fluid, as determined by
the solid phase test, is equal to or faster than the rate of a
C16-C18 internal olefin. Alternatively, this
limitation could be expressed as the percent of the base fluid degraded
at 120 days minus the percent of C16-C18 internal
olefin degraded at 120 days shall not be less than zero. With this
limitation the base fluids currently available for use include
vegetable ester, linear alpha olefin, internal olefins, and possibly
certain linear paraffins. Combined with the other stock base fluid
limitations of PAH content and sediment toxicity, the base fluids for
which EPA has data that would attain all three limitations are internal
olefins and vegetable esters.
EPA finds this limit to be technically available because
information in the rulemaking record supports that internal olefin SBFs
and vegetable ester SBFs together have performance characteristics to
address the broad variety of drilling situations found offshore.
As an alternative to today's proposal, EPA solicits comment on a
numeric limitation of a minimum biodegradation rate of 68 percent base
fluid dissipation at 120 days for the standardized solid phase test. If
EPA pursues this approach, EPA expects that it may need to revise this
numeric limitations as additional test results are generated.
As with the sediment toxicity test presented above, due to the lack
of data from the biodegradation test EPA again intends to propose a
limitation based on comparative testing rather than propose a numerical
limitation. Therefore, if SBFs based on fluids other than internal
olefins and vegetable esters are to be discharged with drill cuttings,
data showing the biodegradation of the base fluid should be presented
with data, generated in the same series of tests, showing the
biodegradation of the internal olefin as a standard. EPA prefers this
approach rather than set a numerical limitation at this time because of
the small amount of data available to EPA upon which to base a
numerical limitation. EPA sees this as an interim solution to the
problem of having insufficient information at the time of this proposal
to provide a numerical limitation, in that it still provides a
limitation based on the performance of available technologies.
Rates of biodegradation for synthetic and mineral oil base fluids
have been determined by both the solid phase and the simulated seabed
test, and the relative rates of biodegradation among these two tests
agree. These tests have found that, the order of degradation, from
fastest to slowest, is as follows: vegetable ester > linear alpha
olefin > internal olefin > linear paraffin > mineral oil > poly alpha
olefin.
EPA has selected the internal olefin as the basis for the
biodegradation rate limitation instead of the vegetable ester for two
reasons: technical performance and non-water quality environmental
impacts. Industry representatives have reported that SBFs using esters
currently on the market today are not adequate choices for most
deepwater drilling applications. Reportedly, the available esters
thicken considerably at the cold temperatures encountered in the riser
in deep water. This thickening can cause excessive pressure surges when
attempting to re-initiate circulation. These pressure surges can result
in breakdown of exposed formations resulting in severe SBF losses to
the destabilized formations. In addition to SBF losses, pressure surges
can destabilize the formation to the extent of hole collapse and loss
of any
[[Page 5505]]
drilling tools downhole. EPA solicits comment concerning the maximum
depth at which vegetable ester SBFs are practical, the development on
new esters with lower viscosity, and if special systems, such as subsea
pumping systems, ameliorate the pumping difficulties.
Cost is a factor in encouraging the use of SBFs in place of OBFs.
Industry representatives have told EPA that vegetable ester SBF costs
about twice as much as internal olefin SBF. EPA believes that if the
lower cost internal olefin SBFs can be discharged, then more wells
currently drilled with OBF would be encouraged to convert to SBF than
if only the more expensive vegetable ester SBFs were available for
discharge. This conversion is preferable for the improvements in non-
water quality environmental impacts (see section VII below). If future
research shows that vegetable esters have a significantly reduced
toxicity in addition to the proven faster rate of biodegradation, EPA
may consider more stringent stock base fluid limitations to favor the
use of vegetable ester SBFs for the final rule.
e. Economic Achievability of Stock Base Fluid Controls.--EPA finds
that the proposed stock base fluid controls are economically
achievable. Industry representatives have told EPA that while the
synthetic base fluids are more expensive than diesel and mineral oil
base fluids, the savings in discharging the SBF-cuttings versus land
disposal or reinjection of OBF-cuttings more than offsets the increased
cost of SBFs. Thus, it reportedly costs less for operators to invest in
the more expensive SBF provided it can be discharged. The stock base
fluid limitations proposed above allow use of the currently popular
SBFs based on internal olefins ($195/bbl) and vegetable esters ($380/
bbl). For comparison, diesel oil-based drilling fluid costs about $65/
bbl, and mineral oil-based drilling fluid costs about $75/bbl.
According to industry sources, currently in the Gulf of Mexico the most
widely used and discharged SBFs are, in order of use, based on internal
olefins, linear alpha olefins, and vegetable esters. Since the stock
limitations allow the continued use of the preferred internal olefin
and vegetable ester SBFs, EPA attributes no additional cost due to the
stock base fluid requirements other than monitoring (testing and
certification) costs. EPA expects that these monitoring costs will fall
upon the base fluid suppliers as a marketing cost. As further described
in Section XII, EPA anticipates that PAH monitoring would occur
batchwise, and sediment toxicity and biodegradation monitoring would
occur once annually per synthetic base fluid per supplier.
Pursuant to EPA's further research into sediment toxicity and
biodegradation, EPA may propose limits for the final rule that are
different than the limits proposed today. If the limits were to allow
only more expensive SBFs, such as the vegetable ester, EPA would likely
estimate a cost to comply with the stock base fluid limits for those
operators who currently use and discharge the less expensive SBFs, for
instance those based on internal olefins.
2. Discharge Limitations Technical Availability and Economic
Achievability
a. Formation Oil Contamination of SBF-Cuttings.--Today's proposed
formation oil contamination limitation of the SBF adhered to the drill
cuttings is ``weighted'' to detect contamination by highly aromatic
formation oils at lower concentrations than formation oils with lower
aromatic contents. Under the proposed limitation approximately 5
percent of all (all meaning a large representative sampling) formation
oils would fail (not comply) at 0.1 percent contamination and 95
percent of all formation oils will fail at 1.0 percent contamination.
The majority of formation oils would cause failure when present in SBFs
at a concentration of about 0.5 percent (vol/vol).
EPA is proposing two methods for the determination of formation oil
in SBFs. Analysis by gas chromatography with mass spectroscopy
detection (GC/MS) would apply to any SBF being shipped offshore for
drilling to allow discharge of the associated cuttings. During
drilling, the SBF would be required to comply with the limitation of
formation oil contamination as determined by the reverse phase
extraction (RPE) method. SBFs found to be non-compliant by the RPE
method could, at the operators discretion, be confirmed by testing with
the GC/MS method. Results from the GC/MS method would supersede those
of the RPE method.
EPA intends that the limitation proposed on formation (crude) oil
contamination in SBF is no less stringent that the limitation imposed
on WBF through the static sheen test. A study concerning this issue
found that in WBF, the static sheen test detected formation oil
contamination in WBF down to 1 percent in most cases, and down to 0.5
percent in some cases.
Currently, only a very small percent of WBF cannot be discharged
due to presence of formation oil as determined by the static sheen
test. EPA solicits information regarding the frequency of formation oil
contamination at this level of control. EPA has received some anecdotal
information to the effect that far less than one percent of SBF
cuttings would not be discharged due to formation oil contamination at
this level of control. Based on the available information, EPA believes
that only a very minimal amount of SBF will be non-compliant with this
limitation and therefore be required to dispose of SBF-cutting onshore
or by injection. EPA thus finds that this limitation is technically
available. EPA also finds this option to be economically achievable
because there is no reason why formation oil contamination would occur
more frequently under this rule than under the current rules which
industry can economically afford. For calculation purposes, EPA has
determined that no costs are associated with this requirement other
than monitoring and reporting costs, which are minimal costs for this
test for this industry.
b. Retention of SBF on Cuttings.--This limitation considers the
technical availability of methods to recover SBF from the cuttings
wastestream. EPA evaluated the performance of several technologies to
recover SBF from the cuttings wastestream and their costs, as detailed
in the Development Document. EPA also considered fuel use, safety, and
other considerations.
The solids control system typically consists of, at a minimum, a
primary shale shaker to remove the larger cuttings. Typically, all or a
portion of the drilling fluid is then passed through a secondary shale
shaker or ``mud cleaner'' to remove the small particle cuttings, or
``fines,'' before being recirculated to the active mud system. Greater
efficiencies in the use of these currently used technologies through
reduced loadings and more even flow across the screens, better
maintenance of the screens, and better integration of the solids
control system would help operators achieve these proposed discharge
limitations. An ancillary or alternative method to reduce SBF
discharges is to retain the fines for on shore disposal. Because of
their small size and large surface area, the fines retain more drilling
fluid than an equal amount of larger cuttings coming off the shale
shakers. Therefore, while the bulk of the cuttings may be discharged,
retaining the fines for on shore disposal can be used to
disproportionately reduce the overall discharges of SBF.
The American Petroleum Institute (API) performed a study in 1997
which gathered data on SBF retention on drill cuttings. Data gathered
in the study show the long term average retention
[[Page 5506]]
rate of SBF on cuttings, weighted by hole volume, is 10.6 percent from
the primary shale shaker and 15.0 percent from the secondary shale
shaker, expressed as weight synthetic base fluid per weight of wet
cuttings. Industry representatives further estimated that the cuttings
from the primary shale shaker comprise 80 percent of the total cuttings
wastestream, and the remaining 20 percent is removed by either the
secondary shale shaker or other devices to remove very small cuttings,
or fines. EPA used this information to calculate a long term average
weighted retention of 11.5 percent base fluid on wet cuttings using the
current technologies employed in the Gulf of Mexico.
Recently, in the wake of the development of SBFs and discharge
limitations in the North Sea, new cuttings cleaning devices have been
developed which reduce SBF retained on the cuttings. An effective
device consists of a conically shaped vibrating centrifuge, which
removes recycle-grade SBF from the cuttings coming off the primary
shale shakers. EPA selected this conical vibrating centrifuge as the
model technology on which to base its performance and cost
calculations. The manufacturer of the device has supplied EPA with
detailed performance data and some cost information of this device. The
performance has been confirmed by one operator, showing retention data
for twelve wells and comparing the vibrating centrifuge with shale
shaker technology. In addition, EPA was invited by an operator in the
Gulf of Mexico to observe the operation of the vibrating centrifuge.
EPA has learned that the operator has written a report concerning the
operation of this SBF recovery device, but this report has not been
made available to EPA. The operator has informed EPA as to the cost of
implementing the vibrating centrifuge, and EPA used this cost
information in determining the total cost of implementation. EPA is
aware of at least one other company that makes a similar centrifugal
device to recover SBFs from drill cuttings, although EPA has not
received performance or costs for this machine.
The limitation proposed today for retention of SBF is 10.2 percent
base fluid on wet cuttings (weight/weight), averaged by hole volume
over the well sections drilled with SBF. Those portions of the cuttings
wastestream that are retained for no discharge are factored into the
weighted average with a retention value of zero. The limit assumes that
SBF-cuttings processed by the vibrating centrifuge technology comprise
80 percent of the wastestream while the remaining 20 percent is
comprised of SBF-cuttings from the secondary shale shaker. Thus, from
the available data EPA determined that the retention attained for 95
percent of volume-weighted well averages was 7.22 for the vibrating
centrifuge and 22.0 for the secondary shale shakers. Applying the
assumption of an 80/20 split between the two wastestreams, EPA
determined the weighted average retention regulatory limit of 10.2
percent.
Based on current performance of the vibrating centrifuge
technology, 95 percent of all volume-weighted average values for
retention of drilling fluids over the course of drilling a well are
expected to be less than the proposed limit. Some, but not all, of the
variability between wells is due to factors under the control of the
operators. EPA believes that the proposed limit can be met at all times
by providing better attention to the operation of the technology and by
keeping track of the weighted average for retention as the well is
being drilled. If the trend in weighted average retention appears to
the operator as if the average retention for a particular well will
exceed the limitation prior to completion of the well then EPA
recommends that the operator retain some or all of the remaining
cuttings for no discharge. This is feasible because retention of SBF on
drill cuttings is generally low in the early stages of drilling a well
and it increases as the well goes deeper.
EPA used the same statistical analysis to determine the long term
average retention values. These values were used for cost and loadings
calculations. For the vibrating centrifuge and the secondary shale
shaker, respectively, EPA determined that the long term between-well
average percent retention of SBF on cuttings was 5.14 and 15.00.
Applying the assumption of an 80/20 split between the two wastestreams,
the long term average value for cost and loading calculations is 7.11
percent SBF retained on wet cuttings. Cost and loadings calculations
also assumed 7.5 percent washout of the well bore.
EPA finds that a well-average limit of 10.2 percent base fluid on
wet cuttings is economically achievable. According to EPA's analysis,
in addition to reducing the discharge of SBFs associated with the
cuttings, EPA estimates that this control will result in a net savings
of $5.0 MM. This savings results because the value of the SBF recovered
is greater than the cost of implementation of the technology. This
analysis is presented in Section IX of today's notice, and in greater
detail in the Development Document.
EPA thinks that this regulatory limitation is necessary to both
hasten and broaden the use of improved SBF recovery devices, even
though industry may be inclined to implement the SBF recovery
technology to save valuable SBF irrespective of the limitation. There
could be several reasons why industry does not already use the model
SBF recovery technology even though, in EPA's assessment, it saves the
operator money. For one, market acceptance and market penetration of
the vibrating centrifuge could be a reason. The vibrating centrifuge
recovery technology is a new technology that was developed in the North
Sea and has only been demonstrated a few times in the United States.
Secondly, the cost and resources devoted to retrofitting might only
benefit a small portion of the wells drilled by an operator. This is
because only a small fraction of wells, about 13 percent in EPA's
analysis, are drilled with SBFs. To counter this, however, is the fact
that most SBF wells are concentrated in the deep water. EPA projects
that 75 percent of all wells drilled in the deepwater would use SBFs.
In addition, retrofitting costs and market forces would encourage the
dedication of drill platforms equipped with improved SBF recovery
technology to the drilling of SBF wells. The use of improved SBF
recovery devices in the North Sea is a case in point. Operators have
reported to EPA that in the North Sea they were reluctant to use
improved SBF recovery devices, and eventually did so only in response
to more stringent regulatory requirements. These operators report that
their total cost to drill an SBF well actually went down as they
implemented the improved SBF recovery devices because of the value of
the SBF recovered.
H. NSPS Technology Options Considered and Selected
The general approach followed by EPA for developing NSPS options
was to evaluate the best demonstrated SBFs and processes for control of
priority toxic, nonconventional, and conventional pollutants.
Specifically, EPA evaluated the technologies used as the basis for BPT,
BCT and BAT. The Agency considered these options as a starting point
when developing NSPS options because the technologies used to control
pollutants at existing facilities are fully applicable to new
facilities.
EPA has not identified any more stringent treatment technology
option which it considered to represent NSPS level of control
applicable to the SBF-cuttings wastestream. Further, EPA has made a
finding of no barrier to entry based upon the establishment of this
[[Page 5507]]
level of control for new sources. See section X, Economic Analysis.
Therefore, EPA is proposing that NSPS be established equivalent to BPT
and BAT for conventional, priority, and nonconventional pollutants.
VII. Non-Water Quality Environmental Impacts of Proposed
Regulations
A. Introduction and Summary
The elimination or reduction of one form of pollution has the
potential to aggravate other environmental problems. Under sections
304(b) and 306 of the CWA, EPA is required to consider these non-water
quality environmental impacts (including energy requirements) in
developing effluent limitations guidelines and NSPS. In compliance with
these provisions, EPA has evaluated the effect of this proposed
regulation on air pollution, energy consumption, solid waste generation
and management, consumptive water use, safety, and vessel traffic.
Based on this evaluation, EPA currently prefers the discharge
option over the zero discharge option because of the non-water quality
environmental impacts that would occur with zero discharge, compared to
the water quality impacts that would occur with discharge as controlled
by this proposed rule. Thus, non-water quality environmental impacts
are a major consideration for this rule because of the nature of the
wastes and where the wastes are generated and disposed.
If SBF-cuttings cannot be discharged, cuttings from SBF wells would
have to be transported to shore for treatment and disposal, or made
into a slurry and injected on-site. In this case, EPA assumes that most
operators will not use SBF in place of OBF, because SBFs cost more than
OBFs. On the other hand, if SBF-cuttings can be discharged, not only
are non-water quality environmental impacts from current SBF wells
drastically reduced, but EPA also estimates that some OBF wells would
convert to SBF, further decreasing these impacts. EPA estimates that in
the Gulf of Mexico (GOM) 20 percent of OBF wells will convert to SBF
wells. EPA also estimates that these GOM OBF wells are in shallow water
(less than 1000 feet). In deep water, EPA assumes that those wanting to
use SBFs are already doing so and therefore these facilities are not
considered to yield non-water quality environmental impacts reductions.
In offshore California and Cook Inlet, Alaska, EPA assumes that all OBF
wells will convert, because of the greater expense of OBF-cuttings
discharge and an ever greater concern for non-water quality
environmental impacts in these areas as compared to the GOM. For
example, disposal of OBF-cuttings in Cook Inlet, Alaska, would likely
require the barging of the waste to the lower 48 States. Air quality in
California is a continuing concern and therefore there is pressure to
keep air emissions from oil and gas drilling activities in the
neighboring offshore waters at a minimum.
In total, for existing and new sources under the discharge option,
EPA estimates that air emissions would be reduced by 72 tons per year,
based on OBF facilities switching to SBF. If the zero discharge option
was selected, however, air emissions would increase by 378 tons per
year, based on SBF to OBF conversion. Therefore, in moving from the
zero discharge option to the discharge option, air emissions would be
reduced by 450 tons per year. In addition, EPA estimates than 29,359
BOE less fuel would be used.
Other favorable non-water quality environmental impacts occur with
the elimination of the long term disposal of OBF-cuttings on shore,
because the pollutants present in OBF-cuttings may affect ambient air,
soil, and groundwater quality. EPA estimates that allowing discharge of
SBF-cuttings compared to zero discharge would decrease the amount of
OBF-cuttings disposed at land based facilities by 172 MM pounds
annually, and the amount injected by 40 MM pounds. The methodology used
to arrive at these numbers is described in the sections which follow,
and the results are discussed in more detail.
In consideration of the many non-water quality benefits with SBF-
discharge, EPA currently prefers to allow the controlled discharge of
SBF-cuttings despite some additional SBF-cuttings discharges that may
occur as a result of this rule. EPA's authority to consider the non-
water quality environmental impacts of its rule, therefore, forms the
primary basis in EPA's rejection of zero discharge of SBF-cuttings.
B. Method Overview
EPA estimated annual energy consumption (i.e., fuel usage), air
emissions, and solid waste generation rates from information on model
well characteristics and current drilling activity gathered from
industry, State, and Federal agency sources. This framework is based
upon the model well, well count, and control technology data that is
detailed in the compliance cost and pollutant reductions discussions of
today's notice (Section IX). EPA's calculations are based on the
following projections: wells drilled with SBF in the Gulf of Mexico
currently discharge SBF-cuttings containing an average 11 percent by
weight synthetic base fluid; under the discharge option SBF-cuttings
would retain an average 7 percent base fluid on cuttings; and of the
wells drilled with OBF 80 percent practice zero discharge by hauling
OBF-cuttings to shore for land-based disposal, and the remaining 20
percent inject on-site. In the context of the non-water quality
environmental impacts analysis, SBF wells using standard solids control
equipment and discharging SBF-cuttings at 11 percent retention are
defined as the baseline. Increases or decreases in non-water quality
environmental impacts are compared to this baseline. For example,
current OBF wells that EPA projects would convert to SBF in the
discharge option are assigned baseline impacts because these wells use
energy consuming technologies (i.e., transportation for disposal or
injection) beyond standard solids control equipment.
After establishing baseline impacts, EPA calculated impacts
resulting from compliance with the proposed discharge and zero
discharge options, details of which are given in the following
discussions. EPA then calculated the incremental impacts by subtracting
the compliance impacts from the baseline impacts.
The discussions below adopt the following acronyms for the four
model well types developed for well-specific analyses: DWD (deep-water
development), DWE (deep-water exploratory), SWD (shallow-water
development), and SWE (shallow-water exploratory).
C. Energy Consumption and Air Emissions for Existing Sources
1. Energy Consumption
a. Baseline Energy Consumption.--EPA's estimated non-water quality
environmental impacts for the discharge and zero discharge options, for
existing sources, are presented in Table VII-1. EPA set baseline energy
consumption according to SBF wells discharging SBF-cuttings at 11
percent retention of base fluid on wet cuttings. Table VII-1 shows,
therefore, that the baseline energy consumption (i.e., fuel usage) is
zero for existing Gulf of Mexico SBF wells, because increases or
decreases in fuel use and air emissions are compared to this level.
[[Page 5508]]
Table VII-1.--Summary Annual Baseline, Compliance, and Incremental Compliance, Non-Water Quality Environmental Impacts of SBF Cuttings Management from
Existing Sources
--------------------------------------------------------------------------------------------------------------------------------------------------------
Gulf of Mexico Offshore California Cook Inlet, Alaska Total
-----------------------------------------------------------------------------------------------------------------
Technology basis Air Air Air Air
emissions Fuel usage emissions Fuel usage emissions Fuel usage emissions Fuel usage
(tons/yr) (BOE/yr) a (tons/yr) (BOE/yr) a (tons/yr) (BOE/yr) a (tons/yr) (BOE/yr) a
--------------------------------------------------------------------------------------------------------------------------------------------------------
Baseline Non-Water Quality
Environmental Impacts:
Currently SBF Discharge (11%
reten.).......................... 0 0 NA NA NA NA 0 0
Currently OBF Zero Discharge b.... 47.92 3,433 36.61 2,121 2.08 285 86.61 5,839
Compliance Non-Water Quality
Environmental Impacts:
Discharge Option (7% reten.)...... 12.54 3,035 0.76 187 0.01 4 13.30 3,226
Zero Discharge Option............. 338.55 24,125 NA NA NA NA 338.55 24,125
Incremental Non-Water Quality
Environmental Impacts Reductions
(Increases):
Discharge Option (7% reten.)...... 35.38 398 35.86 1,934 2.07 281 73.31 2,613
Zero Discharge Option............. (338.55) (24,125) 0 0 0 0 (338.55) (24,125)
--------------------------------------------------------------------------------------------------------------------------------------------------------
a BOE (barrels of oil equivalent) is the total diesel volume required converted to equivalent oil volume (by the factor 1 BOE = 42 gal. diesel) and the
volume of natural gas required converted to equivalent oil volume (by the factor 1,000 scf = 0.178 BOE).
b Baseline non-water quality environmental impacts from the 23 (20 percent) OBF wells that convert to SBF upon promulgation of today's proposed rule.
Baseline fuel usage rates for OBF wells in offshore California and
coastal Cook Inlet, Alaska derive from activities associated with
transporting waste drill cuttings to shore and land-disposing the
cuttings. For this analysis, EPA used the method developed to estimate
zero discharge impacts under the Offshore and Coastal Oil and Gas
Rulemakings. EPA used the volumes of drilling waste requiring onshore
disposal to estimate the number of supply boat trips necessary to haul
the waste to shore. Projections made regarding boat use included types
of boats used for waste transport, the distance traveled by the boats,
allowances for maneuvering, idling and loading operations at the drill
site, and in-port activities at the dock. EPA estimated fuel required
to operate the cranes at the drill site and in-port based on
projections of crane usage. EPA determined crane usage by considering
the drilling waste volumes to be handled and estimates of crane
handling capacity. EPA also used drilling waste volumes to determine
the number of truck trips required. The number of truck trips, in
conjunction with the distance traveled between the port and the
disposal site, enabled an estimate of fuel usage. The use of land-
spreading equipment at the disposal site was based on the drilling
waste volumes and the projected capacity of the equipment. The annual
baseline fuel usage in barrels of oil equivalents (BOE) is 2,121 BOE
for offshore California, and 285 BOE for coastal Cook Inlet.
In the Gulf of Mexico analysis, EPA projected that 20 percent of
OBF wells in shallow water would become SBF wells as a result of this
rule, and therefore they are included in the zero discharge analysis.
Baseline fuel usage rates (and all other impacts) for OBF wells in the
Gulf of Mexico are based on the assumption that 80 percent of these
wells use land-disposal for zero discharge and the remaining 20 percent
use on-site injection to dispose of OBF-cuttings. This assumption is
discussed further in Section IX of this Preamble, and in the
Development Document. Baseline fuel usage rates for zero discharge via
land-disposal were calculated using the same analysis used in the
offshore rule for California wells and coastal rule for Cook Inlet
wells. Baseline fuel usage rates for Gulf of Mexico wells that inject
waste cuttings onsite were calculated as the sum of the fuel usage for
the model turnkey injection system considered for the zero discharge
option, which consists of transfer equipment for moving cuttings,
grinding and processing equipment, and injection equipment. The per-
well fuel usage rates for wells that use on-site injection are weighted
averages of diesel usage rates and natural gas usage rates, according
to the estimate that 85 percent use diesel and 15 percent use natural
gas as primary power sources in the Gulf of Mexico. By multiplying the
average per-well baseline fuel usage rates by the projected annual
drilling activity for the four model wells in the Gulf of Mexico, EPA
calculated an annual baseline fuel usage of 3,433 BOE for the Gulf of
Mexico, and 5,839 BOE for all wells in the baseline.
b. Compliance Energy Consumption.--Energy consumption for the
discharge option was calculated by identifying the equipment and
activities associated with the operation of a vibrating centrifuge to
reduce the retention of the synthetic base fluid on drill cuttings from
an average 11 percent to seven percent, measured on a wet-weight basis.
Details regarding the technology basis for this option are presented in
Section VI of this Preamble, and in the Development Document. Using the
characteristics of the four model wells (see Section IX.B), EPA
calculated per-well energy consumption based on the horsepower demand
specified for the vibrating centrifuge by its manufacturer. The
horsepower demand was multiplied by the fuel usage rate and the hours
of operation required to drill the SBF section of the well, specific to
each model well type.
Since they are based on the same technology, the discharge option
per-well energy consumption rates are the same for the three geographic
areas, but vary based on the fuel source employed in each area. In the
Gulf of Mexico, industry sources recently estimated that approximately
85 percent of drilling operations use diesel oil as the primary fuel
source, and the remaining 15 percent use natural gas. Information
regarding fuel sources for the offshore California area indicates a
variety of sources, including diesel, natural gas, and for some
platforms, submerged electrical cables connected to shore-based power
supplies. For this analysis, it was determined that deep water wells in
offshore California use diesel as the primary fuel source, and shallow
water wells use natural gas. For coastal Cook Inlet wells, natural gas
was determined to be the primary fuel source, based on information
supplied by the industry both recently and submitted in the Coastal Oil
and Gas Rulemaking effort. Based on these determinations and projected
drilling activity estimates, EPA calculated the following annual
[[Page 5509]]
discharge option fuel usage rates for the three geographic areas: 3,035
BOE for the Gulf of Mexico, 187 BOE for offshore California, and 4 BOE
for Cook Inlet, for a total annual fuel usage rate of 3,226 BOE for
existing sources in the discharge option.
EPA calculated energy consumption for compliance with the zero
discharge option for the Gulf of Mexico wells that EPA estimates
currently discharge SBF cuttings, since these wells would need to
convert from discharge to zero discharge under this option. EPA
estimated fuel usage rates were estimated by identifying the equipment
and activities associated with two zero discharge technologies
currently in use in the Gulf of Mexico: 1) transporting waste cuttings
to shore-based land disposal sites; and 2) on-site injection. The
methods developed for calculating fuel usage for both these zero
discharge technologies are described above for baseline OBF wells.
While the same line-items were used to estimate impacts for the
transport and land-disposal technology scenario in all three geographic
areas, the per-well fuel usage rates vary between the three geographic
areas due to the various distances traveled by and trip frequencies of
boats and trucks in these areas. By multiplying the weighted average
per-well fuel usage rates by the projected annual drilling activity for
the four model wells in the Gulf of Mexico, EPA calculated a total
annual fuel usage rate of 24,125 BOE for existing sources in the zero
discharge option.
c. Incremental Compliance Energy Consumption. Incremental
compliance impacts are the difference between the baseline and the
compliance impacts, and indicate the amount by which baseline impacts
would be reduced with implementation of the compliance technologies
considered. Table VII-1 lists the total annual incremental fuel usage
rates for each geographic area for both the discharge and zero
discharge options. With the implementation of the discharge option,
there would be a reduction in fuel use of 2,613 BOE annually for
existing sources. This reduction is due to the elimination of transport
and land disposal equipment used to manage waste cuttings from baseline
OBF wells that switch to SBFs. Under zero discharge, there would be an
increase in fuel use of 24,125 BOE per year for existing sources. This
increase is due to the addition of transport and land disposal
equipment to manage waste cuttings from baseline SBF wells that
currently discharge cuttings.
2. Air Emissions
EPA estimated air emissions resulting from the operation of boats,
cranes, trucks, and earth-moving equipment necessary to dispose of
waste cuttings onshore, or the operation of on-site grinding and
injection equipment, by using emission factors relating the production
of air pollutants to time of equipment operation and amount of fuel
consumed. The baseline emissions, emissions reductions under the
discharge option, and emissions increases under the zero discharge
option are presented in Table VII-1.
D. Energy Consumption and Air Emissions for New Sources
Based on curr
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