Air pollutants, hazardous; national emission standards: Refractory products manufacturing,

 
CONTENT

[Federal Register: February 13, 2006 (Volume 71, Number 29)]

[Rules and Regulations]

[Page 7415-7441]

From the Federal Register Online via GPO Access [wais.access.gpo.gov]

[DOCID:fr13fe06-9]

ENVIRONMENTAL PROTECTION AGENCY

40 CFR Part 63

[OAR-2002-0088, FRL-8008-2]

RIN 2060-AM90

National Emission Standards for Hazardous Air Pollutants for Refractory Products Manufacturing

AGENCY: Environmental Protection Agency (EPA).

ACTION: Direct final rule; amendments.

SUMMARY: The EPA is taking direct final action on amendments to the national emission standards for hazardous air pollutants (NESHAP) for new and existing refractory products manufacturing facilities, which were promulgated on April 16, 2003, under section 112(d) of the Clean Air Act (CAA). The amendments clarify the testing and monitoring requirements and startup and shutdown requirements for batch processes, make certain technical corrections, and add recent changes to be consistent with the NESHAP General Provisions.

DATES: The direct final rule is effective on April 14, 2006 without further notice, unless adverse comments are received by March 15, 2006 or by March 30, 2006 if a public hearing is requested. If we receive such comment, we will publish a timely withdrawal in the Federal Register indicating which amendments will become effective and which amendments are being withdrawn due to adverse comment.

ADDRESSES: Submit your comments, identified by Docket ID No. OAR-2002- 0088, by one of the following methods:

Federal eRulemaking Portal: http://www.regulations.gov.

Follow the on-line instructions for submitting comments.

Agency Web site: http://www.epa.gov/edocket. EDOCKET,

EPA's electronic public docket and comment

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system, is EPA's preferred method for receiving comments. Follow the on-line instructions for submitting comments.

E-mail: a-and-r-docket@epa.gov and fairchild.susan@epa.gov.

Fax: (202) 566-1741 and (919) 541-5600.

Mail: U.S. Postal Service, send comments to: EPA Docket Center (6102T), Attn: Docket ID No. OAR-2002-0088, 1200 Pennsylvania Ave., NW., Washington, DC 20460. Please include a total of two copies.

Hand Delivery: In person or by courier, deliver comments to: EPA Docket Center (6102T), Attention Docket ID No. OAR-2002-0088, 1301 Constitution Avenue, NW., Room B-108, Washington, DC 20004. Such deliveries are only accepted during the Docket's normal hours of operation, and special arrangements should be made for deliveries of boxed information. Please include a total of two copies.

Instructions: Direct your comments to Docket ID No. OAR-2002-0088. The EPA's policy is that all comments received will be included in the public docket without change and may be made available online at http://www.epa.gov/edkpub/index.jsp , including any personal information

provided, unless the comment includes information claimed to be confidential business information (CBI) or other information whose disclosure is restricted by statute. Do not submit information that you consider to be CBI or otherwise protected through EDOCKET, regulations.gov, or e-mail. Send or deliver information identified as CBI only to the following address: Mr. Roberto Morales, OAQPS Document Control Officer, EPA (C404-02), Attention Docket ID No. OAR-2002-0088, Research Triangle Park, NC 27711. Clearly mark the part or all of the information that you claim to be CBI. The EPA EDOCKET and the Federal regulations.gov websites are ``anonymous access'' systems, which means EPA will not know your identity or contact information unless you provide it in the body of your comment. If you send an e-mail comment directly to EPA without going through EDOCKET or regulations.gov, your e-mail address will be automatically captured and included as part of the comment that is placed in the public docket and made available on the Internet. If you submit an electronic comment, EPA recommends that you include your name and other contact information in the body of your comment and with any disk or CD-ROM you submit. If EPA cannot read your comment due to technical difficulties and cannot contact you for clarification, EPA may not be able to consider your comment. Electronic files should avoid the use of special characters, any form of encryption, and be free of any defects or viruses. For additional information about EPA's public docket visit EDOCKET on-line or see the Federal Register of May 31, 2002 (67 FR 38102).

Docket: All documents in the docket are listed in the EDOCKET index at http://www.epa.gov/edkpub/index.jsp. Although listed in the index,

some information is not publicly available, i.e., CBI or other information whose disclosure is restricted by statute. Certain other material, such as copyrighted material, is not placed on the Internet and will be publicly available only in hard copy form. Publicly available docket materials are available either electronically in EDOCKET or in hard copy form at the EPA Docket Center, Docket ID No. OAR-2002-0088, EPA West Building, Room B-102, 1301 Constitution Ave., NW., Washington, DC. The Public Reading Room is open from 8:30 a.m. to 4:30 p.m., Monday through Friday, excluding legal holidays. The telephone number for the Public Reading Room is (202) 566-1744, and the telephone number for the EPA Docket Center is (202) 566-1742.

FOR FURTHER INFORMATION CONTACT: For further information contact Susan Fairchild, EPA, Office of Air Quality Planning and Standards, Emission Standards Division, Minerals and Inorganic Chemicals Group (C504-05), Research Triangle Park, NC 27711; telephone number (919) 541-5167; fax number (919) 541-5600; e-mail address: fairchild.susan@epa.gov.

SUPPLEMENTARY INFORMATION:

Regulated Entities. Categories and entities potentially regulated by this action include those listed in the following table:

Table 1.--Regulated Entities Table

Category

NAICS*

Examples of regulated entities

Industrial..................... 327124 Clay refractories manufacturing plants. Industrial..................... 327125 Nonclay refractories manufacturing plants.

*North American Industry Classification System

This table is not intended to be exhaustive, but rather provides a guide for readers regarding entities likely to be regulated by this action. To determine whether your facility is regulated by this action, you should examine the applicability criteria in 40 CFR 63.9782 of the Refractory Products Manufacturing NESHAP. If you have any questions regarding the applicability of this action to a particular entity, consult the person listed in the preceding FOR FURTHER INFORMATION CONTACT section.

Worldwide Web (WWW). In addition to being available in the docket, an electronic copy of today's document will also be available on the http://WWW. Following the Administrator's signature, a copy of this action

will be posted at http://www.epa.gov/ttn/oarpg on EPA's Technology

Transfer Network (TTN) policy and guidance page for newly proposed or promulgated rules. The TTN provides information and technology exchange in various areas of air pollution control.

Comments. We are publishing the direct final rule without prior proposal because we view the amendments as noncontroversial and do not anticipate adverse comments because the amendments clarify several of the requirements of the NESHAP, bring the NESHAP into consistency with the General Provisions to 40 CFR part 63, and make technical corrections to the NESHAP. However, in the Proposed Rules section of this Federal Register, we are publishing a separate document that will serve as the proposal to amend the NESHAP for refractory products manufacturing facilities if adverse comments are filed. If we receive adverse comment on one or more distinct amendments, we will publish a timely withdrawal in the Federal Register informing the public which amendments will become effective, and which amendments are being withdrawn due to adverse comment. We will address all public comments on withdrawn amendments in a subsequent final rule. We will not institute a second comment period on this action. Any parties interested in commenting must do so at this time.

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Judicial Review. Under section 307(b)(1) of the CAA, judicial review of the direct final rule amendments is available only by filing a petition for review in the United States Court of Appeals for the District of Columbia Circuit by April 14, 2006. Under section 307(d)(7)(B) of the CAA, only an objection to the direct final rule which was raised with reasonable specificity during the period for public comment can be raised during judicial review. Moreover, under section 307(b)(2) of the CAA, the requirements established by the direct final rule may not be challenged separately in any civil or criminal proceedings brought by EPA to enforce these requirements.

Outline. The information presented in this preamble is organized as follows:

  1. Background II. Amendments to 40 CFR Part 63, Subpart SSSSS

    1. Emission Testing

    2. Control Device Operation

    3. Operating Limits

    4. Monitoring

    5. Other Changes III. Statutory and Executive Order Reviews

    6. Executive Order 12866, Regulatory Planning and Review

    7. Paperwork Reduction Act

    8. Regulatory Flexibility Act

    9. Unfunded Mandates Reform Act

    10. Executive Order 13132, Federalism

    11. Executive Order 13175, Consultation and Coordination With Indian Tribal Governments

    12. Executive Order 13045, Protection of Children From Environmental Health Risks and Safety Risks

    13. Executive Order 13211, Actions That Significantly Affect Energy Supply, Distribution, or Use

  2. National Technology Transfer and Advancement Act

    1. Congressional Review Act

  3. Background

    The EPA promulgated the NESHAP for new and existing refractory products manufacturing facilities on April 16, 2003 (68 FR 18730) as 40 CFR part 63, subpart SSSSS. Shortly after promulgation of the Refractory Products Manufacturing NESHAP, EPA also promulgated amendments to the General Provisions to 40 CFR part 63 (68 FR 32586, May 30, 2003). After reviewing the final amendments to the General Provisions and comparing those to the Refractory Products Manufacturing NESHAP, we discovered discrepancies between sections of the General Provisions as cited in the NESHAP and the newly amended sections of the General Provisions. We also identified minor technical errors and other specific sections of the Refractory Products Manufacturing NESHAP that needed clarification. Today's action includes amendments to the Refractory Products Manufacturing NESHAP that clarify the requirements for testing, control device operation, operating limits, and monitoring.

  4. Amendments to 40 CFR Part 63, Subpart SSSSS

    1. Emission Testing

      The Refractory Products Manufacturing NESHAP specify several requirements that pertain to the testing of batch process sources. Because emissions of hazardous air pollutants (HAP) from a batch process source can vary significantly over the course of a batch cycle, the NESHAP specify emission limits in terms of the peak emissions period. In today's action, we are revising the definition of the peak emissions period in terms of the applicable emission limits to include separate definitions for the 3-hour peak total hydrocarbons (THC) mass emissions period, which applies to batch process sources that comply with the THC percentage reduction limit; the 3-hour peak THC emissions concentration period, which applies to batch sources that satisfy the THC emission concentration limit; and the 3-hour peak hydrogen fluoride (HF) mass emissions period, which pertains to the emission limits for batch process clay refractory products kilns. All references to the peak emissions period in the tables to 40 CFR part 63, subpart SSSSS, have been revised for consistency.

      The NESHAP include provisions to allow the owner or operator of an affected batch process source to develop an emissions profile and use the profile to limit emissions testing to the peak emissions period. In today's action, we are amending 40 CFR 63.9802 to clarify that emissions profiles for sources subject to the THC emission limits must be developed using data collected at the maximum organic HAP processing rate. This amendment also clarifies that a new emissions profile must be developed if a facility wants to use an emissions profile to limit testing to the peak emissions period at a process, but increases its maximum organic HAP processing rate at that process. In addition, we are amending 40 CFR 63.9802 to clarify that emissions profiles for batch process clay refractory kilns must be developed using data from when the kiln is processing the clay refractory product with the highest uncalcined clay processing rate.

      We are amending 40 CRF 63.9798(a) to eliminate the reference to permit renewal, and stating that subsequent performance tests must be conducted at least every 5 years. Item 1(b)(i)(1) of Table 4 to Subpart SSSSS of Part 63 is amended to clarify that a sampling port is also required at the control device inlet if the owner or operator plans to develop an emissions profile or use the provision for reducing the operating temperature of a thermal or catalytic oxidizer on an affected batch process source. In both cases, sampling is required at the control device inlet. Item 8(a)(i)(5) of Table 4 to Subpart SSSSS of Part 63 is amended to specify the THC concentration in terms of the outlet of the control device. We also made other minor changes to this provision in Table 4 to simplify the wording.

      Item 13 of Table 4 to Subpart SSSSS of Part 63 is amended to eliminate the reference to the THC percentage reduction limit. We have clarified that regardless of which THC emission limit applies to a specific source, the owner or operator of the source must measure not only the THC concentration, but also the oxygen concentration at the control device inlet for at least the 1-hour period that immediately follows the temperature reduction. This measurement is necessary for demonstrating that the source is meeting the limit of 20 parts per million dry volume (ppmvd) THC, corrected to 18 percent oxygen, after the oxidizer temperature has been reduced.

      Item 13.a.5 of Table 4 to Subpart SSSSS of Part 63 is amended to clarify that only the THC emissions concentration limit applies following any reduction in the oxidizer temperature. We received comment on the proposed rule (67 FR 42108, June 20, 2002) requesting a second emission limit be allowed for sources wanting to meet a percentage reduction limit rather than an emission concentration limit. The commenter believed that since EPA had promulgated percentage reduction limits for other MACT standards to reduce emissions of THC, and since air pollution control devices are usually rated and installed with a minimum percent reduction achieved by the devices, that emission limit would be simpler to meet. At promulgation of the final rule (68 FR 18730, April 16, 2003), we changed the rule to allow regulated sources to meet either the percentage reduction limit or the concentration limit.

      In the final rule, we allowed the choice between either the percentage reduction limit or the concentration limit, but required owners and operators to meet the selected emission limit during all times of operation. We also allowed owners and operators the option to turn off the control device when it was no longer needed. However, for those owners or operators

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      meeting the percentage reduction compliance option, it is not possible to meet that limit if the control device is not in operation. We believe that conserving energy is a beneficial option for all owners and operators, and regardless of the compliance option selected, all should have the opportunity to benefit from turning off the control device when it is no longer needed. Thus, we are clarifying that whether an owner or operator shows compliance with the percentage reduction limit or the concentration limit, compliance with the rule for a unit with a control device no longer in operation may only be demonstrated by meeting the concentration limit; that is, when the THC emissions are below 20 ppmvd corrected to 18 percent oxygen from the heated process unit. Owners and operators in this case may choose to meet the percentage reduction limit before turning off the control device and may show compliance with the concentration limit after turning off the control device.

      Item 14(a)(i)(1) of Table 4 to Subpart SSSSS of Part 63 is amended to specify that the performance tests must be performed while processing the clay refractory product with the highest uncalcined clay processing rate.

    2. Control Device Operation

      Refractory products manufacturing plants typically produce a wide range of products, some of which may contain organic HAP binders or additives, while other products may contain only inorganic binders or additives that do not contain or form HAP. Many plants do not have dedicated thermal process units (e.g., dryers and kilns) for each type of product they manufacture and instead, use the same process units to manufacture products that emit HAP and products that do not contain or emit HAP. Recognizing this situation, we are amending 40 CFR 63.9792 of the NESHAP to clarify that control devices used to comply with the emission limits established by 40 CFR part 63, subpart SSSSS, do not have to be operated when an otherwise affected process unit is processing products that do not contain or release HAP. This amendment applies to sources subject to the THC emission limits as well as the emission limits for HF and hydrogen chloride (also known as hydrochloric acid).

      Table 3 to Subpart SSSSS of Part 63, which specifies work practice standards, includes several options for controlling emissions of polycyclic organic matter from shape preheaters and pitch working tanks used in the manufacture of pitch-impregnated refractory products. Options include exhausting the affected source to a thermal or catalytic oxidizer that is comparable to a thermal or catalytic oxidizer that is used to meet the emission limits for an affected defumer or coking oven. To clarify what is meant by a ``comparable'' thermal or catalytic oxidizer, we are amending 40 CFR 63.9824 to include a definition of ``comparable control device.''

    3. Operating Limits

      The Refractory Products Manufacturing NESHAP refer to the operating limit as the ``maximum allowable organic HAP processing rate.'' We are amending the definition of maximum organic HAP processing rate in 40 CFR 63.9824 to distinguish between the operating limit and the actual processing rate measured during the performance test.

      The Refractory Products Manufacturing NESHAP include several operating limits for clay refractory products kilns that are controlled by dry limestone adsorbers (DLA). We are amending the NESHAP to eliminate the operating limits of maintaining free-flowing limestone throughout the DLA because the term ``free-flowing'' may not be appropriate for the grade of limestone used in DLA. The remaining operating limits specified for DLA in the NESHAP are adequate for ensuring compliance with the emission limits for clay refractory products kilns.

      As specified in Table 2 (Requirements for Establishing Operating Limits) of the rule, Subpart SSSSS of Part 63, owners and operators of certain thermal process sources of organic HAP are required to establish an operating limit for the maximum organic HAP processing rate. The organic HAP processing rate is a function of the amount of organic HAP in the raw materials and the amounts of those raw materials in the refractory product formulation. Because there are minor variations in the content of organic HAP in a specific binder or additive, the operating limit for the maximum organic HAP processing rate can inadvertently be exceeded without changing the product formulation. In today's action, we are amending the procedure for establishing the operating limit and clarifying that minor exceedances of the maximum organic HAP processing rate established during the performance test are not violations of the operating limit. Specifically, we are amending items 3(b) and 8(b) of Table 4 (Requirements for Performance Tests) to Subpart SSSSS of Part 63 to be consistent with the requirements in Table 2 that reflect a 10 percent allowance when calculating the operating limit.

      Today's action amends the procedures for determining minimum temperature operating limits for thermal and catalytic oxidizers that are used to control emissions from certain batch process sources of organic HAP as they pertain to sources that comply with the provisions for reducing the operating temperature of a thermal or catalytic oxidizer.

      We are also amending subpart SSSSS to clarify that owners or operators of batch process sources controlled with thermal or catalytic oxidizers must measure the oxidizer operating temperature throughout each entire test run.

    4. Monitoring

      The Refractory Products Manufacturing NESHAP require THC continuous emission monitoring systems on thermal process sources of organic HAP that use process changes or control devices other than thermal or catalytic oxidizers to meet the THC emission limits. We are amending 40 CFR 63.9800(i)(1) by adding a reference to sources that use process changes to meet the emission limits.

      We are also amending 40 CFR 63.9800(i) to state that such sources must maintain the 3-hour block average THC concentration at or below 20 ppmvd, corrected to 18 percent oxygen.

      Today's action amends the definition of ``deviation'' in 40 CFR 63.9824 to include failure to provide adequate continuous monitoring systems (CMS) data for demonstrating compliance with any emission limit or other requirement. In addition, we are amending the requirement that the owner or operator of an affected source that is required to use a CMS to meet an operating limit must report any deviations from those operating limits.

    5. Other Changes

      We are amending the Refractory Products Manufacturing NESHAP to include definitions for Shutdown and Startup to preclude unnecessary reporting of batch process source operation.

  5. Statutory and Executive Order Reviews

    1. Executive Order 12866, Regulatory Planning and Review

      Under Executive Order 12866 (58 FR 51735, October 4, 1993), EPA must determine whether the regulatory action is ``significant'' and, therefore, subject to review by the Office of Management and Budget (OMB) and the requirements of the Executive Order. The Executive Order defines ``significant regulatory

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      action'' as one that is likely to result in a rule that may:

      (1) Have an annual effect on the economy of $100 million or more or adversely affect in a material way the economy, a sector of the economy, productivity, competition, jobs, the environment, public health or safety, or State, local, or tribal governments or communities;

      (2) Create a serious inconsistency or otherwise interfere with an action taken or planned by another agency;

      (3) Materially alter the budgetary impact of entitlements, grants, user fees, or loan programs, or the rights and obligation of recipients thereof; or

      (4) Raise novel legal or policy issues arising out of legal mandates, the President's priorities, or the principles set forth in the Executive Order.

      Pursuant to the terms of Executive Order 12866, it has been determined that this rule is a ``significant regulatory action'' because it raises novel legal or policy issues arising out of legal mandates. As such, this action was submitted to OMB for review. Changes made in response to OMB suggestions or recommendations will be documented in the public record.

    2. Paperwork Reduction Act

      This action does not impose an information collection burden under the provisions of the Paperwork Reduction Act, 44 U.S.C. 3501, et seq. The OMB approved the information collection requests for the NESHAP for refractory products manufacturing pursuant to the provisions of the Paperwork Reduction Act, 44 U.S.C. 3501, et seq. The OMB assigned OMB control number 2060-0515 (EPA ICR No. 2040.02) to these information collection requests (ICR). A copy of the ICR may be obtained from Susan Auby by mail at the Office of Environmental Information, Collection Strategies Division (2822T), EPA, 1200 Pennsylvania Ave., NW, Washington, DC 20460; by e-mail at auby.susan@epa.gov; or by calling (202) 566-1672. You may also download a copy off the Internet at http://www.epa.gov/icr .

      Today's action makes clarifying changes to the NESHAP for refractory products manufacturing and imposes no new information collection requirements on the industry. Because there is no additional burden on the industry as a result of the direct final rule amendments, the ICR has not been revised.

      Burden means the total time, effort, or financial resources expended by persons to generate, maintain, retain, or disclose or provide information to or for a Federal agency. This includes the time needed to review instructions; develop, acquire, install, and utilize technology and systems for the purposes of collecting, validating, and verifying information, processing and maintaining information, and disclosing and providing information; adjust the existing ways to comply with any previously applicable instructions and requirements; train personnel to be able to respond to a collection of information; search data sources; complete and review the collection of information; and transmit or otherwise disclose the information.

      An agency may not conduct or sponsor, and a person is not required to respond to, a collection of information unless it displays a current valid OMB control number. The OMB control numbers for EPA's regulations are listed in 40 CFR part 9.

    3. Regulatory Flexibility Act

      EPA has determined that it is not necessary to prepare a regulatory flexibility analysis in connection with this final rule.

      For purposes of assessing the impacts of today's rule on small entities, small entity is defined as: (1) A small business as defined by the Small Business Administrations' regulations at 13 CFR 121.201; (2) a small governmental jurisdiction that is a government of a city, county, town, school district or special district with a population of less than 50,000; and (3) a small organization that is any not-for- profit enterprise which is independently owned and operated and is not dominant in its field.

      After considering the economic impacts of today's direct final rule amendments on small entities, EPA has concluded that this action will not have a significant economic impact on a substantial number of small entities. This action includes minor corrections and clarifications to the Refractory Products Manufacturing NESHAP that do not add any additional requirements.

      Although the direct final rule amendments will not have a significant economic impact on a substantial number of small entities, EPA nonetheless has tried to reduce the impact of the direct final rule amendments on small entities. The EPA has limited the amendments to changes that clarify ambiguities of the Refractory Products Manufacturing NESHAP, correct citations to the General Provisions, and clarify the complex batch testing requirements of the Refractory Products Manufacturing NESHAP. The EPA believes that the amendments will simplify the NESHAP and will not add additional burden to regulated entities.

    4. Unfunded Mandates Reform Act

      Title II of the Unfunded Mandates Reform Act of 1995 (UMRA), Public Law No. 104-4, establishes requirements for Federal agencies to assess the effects of their regulatory actions on State, local, and tribal governments and the private sector. Under section 202 of the UMRA, EPA generally must prepare a written statement, including a cost-benefit analysis, for proposed and final rules with ``Federal mandates'' that may result in expenditures by State, local, and tribal governments, in the aggregate, or by the private sector, of $100 million or more in any 1 year. Before promulgating an EPA rule for which a written statement is needed, section 205 of the UMRA generally requires EPA to identify and consider a reasonable number of regulatory alternatives and adopt the least costly, most cost-effective, or least burdensome alternative that achieves the objectives of the rule. The provisions of section 205 do not apply when they are inconsistent with applicable law. Moreover, section 205 allows EPA to adopt an alternative other than the least costly, most cost-effective, or least burdensome alternative if the Administrator publishes with the final rule an explanation why that alternative was not adopted. Before EPA establishes any regulatory requirements that may significantly or uniquely affect small governments, including tribal governments, it must have developed under section 203 of the UMRA a small government agency plan. The plan must provide for notifying potentially affected small governments, enabling officials of affected small governments to have meaningful and timely input in the development of EPA's regulatory proposals with significant Federal intergovernmental mandates, and informing, educating, and advising small governments on compliance with the regulatory requirements.

      The EPA has determined that today's direct final rule amendments do not contain a Federal mandate that may result in expenditures of $100 million or more for State, local, and tribal governments, in the aggregate, or the private sector in any 1 year, nor do the direct final rule amendments significantly or uniquely impact small governments because there are no requirements that apply to such governments or impose obligations upon them. Thus, today's direct final rule amendments are not subject to the

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      requirements of sections 202 and 205 of the UMRA.

    5. Executive Order 13132, Federalism

      Executive Order 13132, entitled ``Federalism'' (64 FR 43255, August 10, 1999), requires EPA to develop an accountable process to ensure ``meaningful and timely input by State and local officials in the development of regulatory policies that have federalism implications.'' ``Policies that have federalism implications'' is defined in the Executive Order to include regulations that have ``substantial direct effects on the States, on the relationship between the national government and the States, or on the distribution of power and responsibilities among the various levels of government.''

      The direct final rule amendments do not have federalism implications. They will not have substantial direct effects on the States, on the relationship between the national government and the States, or on the distribution of power and responsibilities among the various levels of government, as specified in Executive Order 13132. None of the affected facilities are owned or operated by State or local governments, and the direct final rule amendments will not supercede State regulations that are more stringent. Thus, Executive Order 13132 does not apply to the direct final rule amendments.

    6. Executive Order 13175, Consultation and Coordination With Indian Tribal Governments

      Executive Order 13175, entitled ``Consultation and Coordination with Indian Tribal Governments'' (65 FR 67249, November 9, 2000), requires EPA to develop an accountable process to ensure ``meaningful and timely input by tribal officials in the development of regulatory policies that have tribal implications.'' The direct final rule amendments do not have tribal implications, as specified in Executive Order 13175. They will not have substantial direct effects on tribal governments, on the relationship between the Federal government and Indian tribes, or on the distribution of power and responsibilities between the Federal government and Indian tribes, as specified in Executive Order 13175. No tribal governments own or operate refractory products manufacturing facilities. Thus, Executive Order 13175 does not apply to the direct final rule amendments.

    7. Executive Order 13045, Protection of Children From Environmental Health Risks and Safety Risks

      Executive Order 13045 (62 FR 19885, April 23, 1997) applies to any rule that: (1) Is determined to be ``economically significant'' as defined under Executive Order 12866 and (2) concerns an environmental health or safety risk that EPA has reason to believe may have a disproportionate effect on children. If the regulatory action meets both criteria, the Agency must evaluate the environmental health or safety effects of the planned rule on children, and explain why the planned rule is preferable to other potentially effective and reasonably feasible alternatives considered by the Agency.

      The EPA interprets Executive Order 13045 as applying only to those regulatory actions that are based on health or safety risks, such that the analysis required under section 5-501 of the Executive Order has the potential to influence the regulation. Today's direct final rule amendments are not subject to Executive Order 13045 because they are based on technology performance and not on health or safety risks. In addition, the direct final rule amendments have been determined not to be ``economically significant'' as defined under Executive Order 12866.

    8. Executive Order 13211, Actions Concerning Regulations That Significantly Affect Energy Supply, Distribution, or Use

      This rule is not a ``significant regulatory action'' as defined in Executive Order 13211 (66 FR 28355, May 22, 2001) because it is not likely to have a significant adverse effect on the supply, distribution, or use of energy. We have concluded that the direct final rule amendments are not likely to have any adverse energy effects.

  6. National Technology Transfer and Advancement Act

    Section 12(d) of the National Technology Transfer and Advancement Act (NTTAA) of 1995, Public Law No. 104-113; 12(d) (15 U.S.C. 272 note) directs EPA to use voluntary consensus standards (VCS) in its regulatory activities unless to do so would be inconsistent with applicable law or otherwise impractical. The VCS are technical standards (e.g., materials specifications, test methods, sampling procedures, and business practices) that are developed or adopted by VCS bodies. The NTTAA directs EPA to provide Congress, through the OMB, explanations when the Agency decides not to use available and applicable VCS.

    The direct final rule amendments implement clarifications and corrections to the NESHAP for refractory product manufacturing, but do not change any technical standards. Therefore, EPA did not consider the use of any VCS.

    1. Congressional Review Act

    The Congressional Review Act, 5 U.S.C. 801, et seq., as added by the Small Business Regulatory Enforcement Fairness Act of 1996, generally provides that before a rule may take effect, the agency promulgating the rule must submit a rule report, which includes a copy of the rule, to each House of the Congress and to the Comptroller General of the United States. The EPA will submit a report containing the direct final rule amendments and other required information to the United States Senate, the United States House of Representatives, and the Comptroller General of the United States prior to publication of the direct final rule amendments in the Federal Register. A major rule cannot take effect until 60 days after it is published in the Federal Register. This action is not a ``major rule'' as defined by 5 U.S.C. 804(2). The direct final rule amendments are effective on April 14, 2006.

    List of Subjects in 40 CFR Part 63

    Environmental protection, Administrative practice and procedure, Air pollution control, Hazardous substances, Intergovernmental relations, Reporting and recordkeeping requirements.

    Dated: December 7, 2005. Stephen L. Johnson, Administrator.

    0 For the reasons stated in the preamble, title 40, chapter I, part 63 of the Code of Federal Regulations is amended as follows:

    PART 63--[AMENDED]

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

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

    Subpart SSSSS--[Amended]

    0 2. Section 63.9792 is amended as follows: 0 a. Revising paragraph (b); 0 b. Redesignating paragraph (f) as paragraph (g); and 0 c. Adding a new paragraph (f).

    Sec. 63.9792 What are my general requirements for complying with this subpart?

    * * * * *

    (b) Except as specified in paragraphs (e) and (f) of this section, you must

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    always operate and maintain your affected source, including air pollution control and monitoring equipment, according to the provisions in Sec. 63.6(e)(1)(i). During the period between the compliance date specified for your affected source in Sec. 63.9786 and the date upon which continuous monitoring systems have been installed and validated and any applicable operating limits have been established, you must maintain a log detailing the operation and maintenance of the process and emissions control equipment. * * * * *

    (f) For any affected source that is subject to any of the emission limits specified in Table 1 to this subpart, you do not have to operate the control device on that affected source under the conditions specified in paragraphs (f)(1) and (2) of this section.

    (1) For any source that is subject to the THC emissions concentration limit or the THC percentage reduction limit, you do not have to operate the control device on that source when none of the refractory products that are being processed by that source contain or form an organic HAP.

    (2) For any new clay refractory products kiln that is subject to the production-based mass emission limits or the percentage reduction limits for hydrogen flouride (HF) and hydrogen chloride (HCl), you do not have to operate the control device on that kiln when none of the refractory products that are being processed by that kiln are clay refractory products, as defined in Sec. 63.9824. * * * * *

    0 3. Section 63.9798 is amended as follows: 0 a. Revising paragraph (a); 0 b. Revising paragraph (c) introductory text; and 0 c. Revising paragraphs (c)(2) and (d).

    Sec. 63.9798 When must I conduct subsequent performance tests?

    (a) You must conduct a performance test at least every 5 years following the initial performance test. * * * * *

    (c) If you own or operate a source that is subject to the emission limits specified in items 2 through 9 of Table 1 to this subpart, you must conduct a performance test on the source(s) listed in paragraphs (c)(1) and (2) of this section before you start production of any refractory product for which the organic HAP processing rate is likely to exceed the maximum allowable organic HAP processing rate, as defined in items 3(b) and 8(b) of Table 4 to this subpart, established during the most recent performance test on that same source. * * * * *

    (2) Each affected kiln that follows an affected shape dryer or curing oven in the same process line and is used to process the refractory product with the higher organic HAP processing rate.

    (d) If you own or operate a kiln that is subject to the emission limits specified in item 5 or 9 of Table 1 to this subpart, you must conduct a performance test on the affected kiln following any process changes that are likely to increase organic HAP emissions from the kiln (e.g., a decrease in the curing cycle time for a curing oven that precedes the affected kiln in the same process line). * * * * *

    0 4. Section 63.9800 is amended as follows: 0 a. Revising paragraph (g)(1); 0 b. Revising paragraph (g)(3); 0 c. Revising paragraph (i)(1) introductory text; and 0 d. Adding paragraphs (i)(1)(iv) to (vi).

    Sec. 63.9800 How do I conduct performance tests and establish operating limits?

    * * * * *

    (g) * * *

    (1) To determine compliance with the total hydrocarbon (THC) emission concentration limit listed in Table 1 to this subpart, you must calculate your emission concentration corrected to 18 percent oxygen for each test run using Equation 1 of this section:

    [GRAPHIC] [TIFF OMITTED] TR13FE06.000

    Where:

    CTHCC = THC concentration, corrected to 18 percent oxygen, parts per million by volume, dry basis (ppmvd) CTHC= THC concentration (uncorrected), ppmvd CO2 = Oxygen concentration, percent * * * * *

    (3) To determine compliance with production-based HF and HCl emission limits in Table 1 to this subpart, you must calculate your mass emissions per unit of uncalcined clay processed for each test run using Equation 3 of this section:

    [GRAPHIC] [TIFF OMITTED] TR13FE06.001

    Where:

    MP = mass emissions of specific HAP (HF or HCl) per unit of production, kilograms of pollutant per megagram (pounds per ton) of uncalcined clay processed ER = mass emissions rate of specific HAP (HF or HCl) during each performance test run, kilograms (pounds) per hour P = average uncalcined clay processing rate for the performance test, megagrams (tons) of uncalcined clay processed per hour * * * * *

    (i) * * *

    (1) For sources subject to the THC concentration limit specified in item 3, 4, 7, or 8 of Table 1 to this subpart, you must satisfy the requirements specified in paragraphs (i)(1)(i) through (vi) of this section. * * * * *

    (iv) You must meet the data reduction requirements specified in Sec. 63.8(g).

    (v) You must maintain the 3-hour block average THC concentration at or below 20 ppmvd, corrected to 18 percent oxygen.

    (vi) To calculate the oxygen correction specified in paragraph (i)(1)(v) of this section, you may use oxygen concentration measurements concurrent with THC concentration measurements, the average oxygen concentration measured during the most recent performance test on the affected source, or other oxygen concentration measurements that are representative of normal operation for the affected source. * * * * *

    0 5. Section 63.9802 is revised to read as follows:

    Sec. 63.9802 How do I develop an emissions profile?

    (a) If you decide to develop an emissions profile for an affected batch process source, as indicated in item 8(a)(i)(4) or 17(b)(i)(4) of Table 4 to this subpart, you must measure and record mass emissions of the applicable pollutant throughout a complete batch cycle of the affected batch process source according to the procedures described in paragraph (a)(1) or (2) of this section.

    (1) If your affected batch process source is subject to the THC concentration limit specified in item 6(a), 7(a), 8, or 9 of Table 1 to this subpart or the THC percentage reduction limit specified in item 6(b) or 7(b) of Table 1 to this subpart, you must measure and record the THC mass emissions rate at the inlet to the control device using the test methods, averaging periods, and procedures specified in items 10(a) and (b) of Table 4 to this subpart for each complete hour of the batch process cycle and while the source is processing the product with the maximum organic HAP processing rate.

    [[Page 7422]]

    (2) If your affected batch process source is subject to the HF and HCl percentage reduction emission limits in item 11 of Table 1 to this subpart, you must measure and record the HF mass emissions rate at the inlet to the control device through a series of 1-hour test runs using one of the test methods specified in item 14(a) of Table 4 to this subpart for each complete hour of the batch process cycle and while the source is processing the product with the highest uncalcined clay processing rate.

    (b) You must develop a new emissions profile if you meet all of the conditions specified in paragraphs (b)(1) through (3) of this section.

    (1) You own or operate a batch process source that is subject to the emission limits specified in item 6(a), 6(b), 7(a), 7(b), 8, or 9 of Table 1 to this subpart.

    (2) You use an emissions profile to limit emission testing to the 3-hour peak emissions period.

    (3) You begin manufacturing a new refractory product for which the organic HAP processing rate is likely to exceed the maximum allowable organic HAP processing rate established during the most recent performance test on that same source.

    0 6. Section 63.9812 is amended by revising paragraphs (b) and (c) to read as follows:

    Sec. 63.9812 What notifications must I submit and when?

    * * * * *

    (b) As specified in Sec. 63.9(b)(2), if you start up your affected source before April 16, 2003, you must submit an Initial Notification not later than 120 calendar days after April 16, 2003.

    (c) As specified in Sec. 63.9(b)(2), if you start up your new or reconstructed affected source on or after April 16, 2003, you must submit an Initial Notification not later than 120 calendar days after you become subject to this subpart. * * * * *

    0 7. Section 63.9816 is amended by revising paragraph (c)(9) to read as follows:

    Sec. 63.9816 What records must I keep?

    * * * * *

    (c) * * *

    (9) If you operate a source that is subject to the THC emission limits specified in item 2 or 6 of Table 1 to this subpart and is controlled with a catalytic oxidizer, records of annual checks of catalyst activity levels and subsequent corrective actions. * * * * *

    0 8. Section 63.9824 is amended as follows: 0 a. Revising paragraph (3) and adding paragraph (4) to the definition of Deviation; 0 b. Revising the definitions of Maximum organic HAP processing rate and Peak emissions period; and 0 c. Adding the definitions of Comparable control device, Shutdown, and Startup.

    Sec. 63.9824 What definitions apply to this subpart?

    * * * * *

    Comparable control device means, subject to paragraphs (1), (2), and (3) of this definition, a control device with design and operating parameters that are comparable to the reference control device.

    (1) For a thermal oxidizer, a comparable control device is either:

    (i) A thermal oxidizer with a residence time at least as long as, and a combustion chamber operating temperature at least as high as the reference thermal oxidizer; or

    (ii) A control device that has been demonstrated to control emissions to a level that is comparable to or better than the level of emissions control achieved by the reference thermal oxidizer.

    (2) For a catalytic oxidizer, a comparable control device is either:

    (i) A catalytic oxidizer with a space velocity no greater than, and a catalyst bed inlet temperature at least as high as the reference catalytic oxidizer; or

    (ii) A control device that has been demonstrated to control emissions to a level that is comparable to or better than the level of emissions control achieved by the reference catalytic oxidizer.

    (3) For other control devices, a comparable control device is one that has been demonstrated either through engineering calculations or emission testing to control emissions to a level that is comparable to or better than the level of control achieved by the reference control device. * * * * *

    Deviation * * *.

    (3) Fails to meet any emission limitation (emission limit, operating limit, or work practice standard) in this subpart during startup, shutdown, or malfunction, regardless of whether or not such failure is permitted by this subpart; or

    (4) Fails to provide adequate monitoring data for demonstrating compliance with any emission limitation (emission limit, operating limit, or work practice standard) or other applicable requirement established by this subpart due to a malfunction or failure of any CMS required by this subpart. * * * * *

    Maximum organic HAP processing rate means the maximum rate at which the mass of organic HAP materials in refractory shapes are processed in an affected process unit. (See also the definition of organic HAP processing rate.) * * * * *

    Peak emissions period means the period of consecutive hourly average emissions of the applicable pollutant that is greater than any other period of consecutive hourly average emissions for the same pollutant over the course of a specified batch process cycle, as defined in paragraphs (1) through (3) of this definition. The peak emissions period is a function of the rate at which the temperature of the refractory shapes is increased, the mass and loading configuration of the shapes in the process unit, the constituents of the refractory mix, and the type of pollutants emitted.

    (1) The 3-hour peak THC mass emissions period is the period of 3 consecutive hours over which the sum of the uncontrolled hourly THC mass emissions rates is greater than the sum of the uncontrolled hourly THC mass emissions rates for any other period of 3 consecutive hours during the same batch process cycle.

    (2) The 3-hour peak THC emissions concentration period is the period of 3 consecutive hours over which the sum of the THC concentrations, corrected to 18 percent oxygen, is greater than the sum of the THC concentrations at the same sampling location, corrected to 18 percent oxygen, for any other period of 3 consecutive hours during the same batch process cycle.

    (3) The 3-hour peak HF mass emissions period is the period of 3 consecutive hours over which the sum of the uncontrolled hourly HF mass emissions rates is greater than the sum of the uncontrolled hourly HF mass emissions rates for any other period of 3 consecutive hours during the same batch process cycle. * * * * *

    Shutdown means the cessation of operation of an affected source. For an affected batch process source, shutdown means the cessation of operation during a batch cycle. Shutdown does not include normal periods between batch cycles when the batch process source is not in operation.

    Startup means the setting into operation of an affected source. For an affected batch process source, startup means the initial startup of the source

    [[Page 7423]]

    or the startup of the source following maintenance, replacement of equipment, or equipment repairs. Startup does not include routine recharging of a batch process source at the start of a batch cycle. * * * * *

    0 9. Table 1 to subpart SSSSS is amended as follows: 0 a. Revising items 6.a and b; 0 b. Revising items 7.a and b; 0 c. Revising item 8; 0 d. Redesignating items 9, 10, and 11 as items 10, 11, and 12; 0 e. Adding a new clarification as item 9; 0 f. Revising newly redesignated items 11.a and b; and

    Table 1 to Subpart SSSSS of Part 63.--Emission Limits [As stated in Sec. 63.9788, you must comply with the emission limits for affected sources in the following table:]

    You must meet the following For . . .

    emission limits . . .

    * * * * * * * 6. Batch process units that are

    a. The 2-run block average THC controlled with a thermal or catalytic concentration for the 3-hour oxidizer.

    peak THC emissions concentration period must not exceed 20 ppmvd, corrected to 18 percent oxygen, at the outlet of the control device; or b. The 2-run block average THC mass emissions rate for the 3- hour peak THC mass emissions period must be reduced by at least 95 percent. 7. Batch process units that are

    a. The 2-run block average THC equipped with a control device other concentration for the 3-hour than a thermal or catalytic oxidizer. peak THC emissions concentration period must not exceed 20 ppmvd, corrected to 18 percent oxygen, at the outlet of the control device; or b. The 2-run block average THC mass emissions rate for the 3- hour peak THC mass emissions period must be reduced by at least 95 percent. 8. Batch process units that use process The 2-run block average THC changes to reduce organic HAP

    concentration for the 3-hour emissions.

    peak THC emissions concentration period must not exceed 20 ppmvd, corrected to 18 percent oxygen, at the outlet of the process gas stream. 9. Batch process units that have turned The 2-run block average THC off the control device or are not

    concentration for the 3-hour equipped with a control device.

    peak THC emissions concentration period must not exceed 20 ppmvd, corrected to 18 percent oxygen, at the outlet of the process gas stream. 10. Batch process kilns that are not The 2-run block average THC equipped with a control device.

    concentration for the 3-hour peak THC emissions concentration period must not exceed 20 ppmvd, corrected to 18 percent oxygen, at the outlet of the process gas stream. 11. Each new continuous kiln that is a. The 3-hour block average HF used to produce clay refractory

    emissions must not exceed products.

    0.019 kilograms per megagram (kg/Mg) (0.038 pounds per ton kiln that is (lb/ton)) of uncalcined clay processed, OR the 3-hour block average HF mass emissions rate must be reduced by at least 90 percent; and b. The 3-hour block average HCl emissions must not exceed 0.091 kg/Mg (0.18 lb/ton) of uncalcined clay processed, OR the 3-hour block average HCl mass emissions rate must be reduced by at least 30 percent.

    * * * * * * *

    [[Page 7424]]

    0 10. Table 2 to subpart SSSSS is amended as follows: 0 a. Revising item 1.c; 0 b. Revising item 4; 0 c. Revising 7; 0 d. Revising items 8.a and b and adding items 8.c through e; 0 e. Revising items 9.a and b, and adding new items 9.d through f; and 0 f. Removing item 11.b and redesignating items 11.c and d as items 11.b and c, respectively.

    Table 2 to Subpart SSSSS of Part 63.--Operating Limits [As stated in Sec. 63.9788, you must comply with the operating limits for affected sources in the following table]

    For . . .

    You must . . .

    1. Each affected source listed in Table 1 to this

    * * * subpart.

    b. Capture emissions and vent them through a closed system; and c. Operate each control device that is required to comply with this subpart on each affected source during all periods that the source is operating, except where specified in Sec. 63.9792(e) and (f), item 2 of this table, and item 13 of Table 4 to this subpart; and * * *

    * * * * * * * 4. Each affected continuous process unit............... Maintain the 3-hour block average organic HAP processing rate (pounds per hour) at or below the maximum allowable organic HAP processing rate established during the most recent performance test.

    * * * * * * * 7. Each affected batch process unit.................... For each batch cycle, maintain the organic HAP processing rate (pounds per batch) at or below the maximum allowable organic HAP processing rate established during the most recent performance test. 8. Batch process units that are equipped with a thermal a. Except as specified in item 8.b. of this table, oxidizer.

    maintain throughout the entire batch cycle the hourly average operating temperature in the thermal oxidizer combustion chamber at or above the minimum allowable operating temperature established during the most recent performance test, as determined according to item 11 of Table 4 to this subpart; and b. If complying with the provisions for reducing the thermal oxidizer operating temperature, as specified in item 13 of Table 4 to this subpart, satisfy the requirements of items 8.c. through 8.e. of this table; c. From the start of the batch cycle until the batch process unit reaches its maximum temperature, maintain the thermal oxidizer combustion chamber temperature at or above the minimum allowable temperature established during the most recent performance test, as determined according to item 11 of Table 4 to this subpart; d. From the time when the batch process unit reaches its maximum temperature, maintain the thermal oxidizer combustion chamber temperature at or above the minimum allowable temperature established during the most recent performance test, as determined according to item 11 of Table 4 to this subpart, for a length of time that equals or exceeds the length of time between the process unit reaching its maximum temperature and the start of the thermal oxidizer temperature reduction during the most recent performance test; e. For the remainder of the batch process cycle, maintain the thermal oxidizer combustion chamber temperature at or above the reduced thermal oxidizer temperature established during the most recent performance test, as specified in item 13 of Table 4 to this subpart.

    [[Page 7425]]

    9. Batch process units that are equipped with a

    a. Except as specified in item 9.b. of this table, catalytic oxidizer.

    maintain throughout the entire batch cycle the hourly average operating temperature at the inlet of the catalyst bed at or above the minimum allowable operating temperature established during the most recent performance test, as determined according to item 12 of Table 4 to this subpart; and b. If complying with the provisions for reducing the catalytic oxidizer operating temperature, as specified in item 13 of Table 4 to this subpart, satisfy the requirements of items 9.d through 9.f of this table; and c. Check the activity level of the catalyst at least every 12 months. d. From the start of the batch cycle until the batch process unit reaches its maximum temperature, maintain the temperature at the inlet of the catalyst bed at or above the minimum allowable temperature established during the most recent performance test, as determined according to item 12 of Table 4 to this subpart; e. From the time when the batch process unit reaches its maximum temperature, maintain the temperature at the inlet of the catalyst bed at or above the minimum allowable temperature established during the most recent performance test, as determined according to item 12 of Table 4 to this subpart, for a length of time that equals or exceeds the length of time between the process unit reaching its maximum temperature and the start of the catalytic oxidizer temperature reduction during the most recent performance test; f. For the remainder of the batch process cycle, maintain the temperature at the inlet of the catalyst bed at or above the reduced catalyst bed inlet temperature established during the most recent performance test, as specified in item 13 of Table 4 to this subpart.

    * * * * * * *

    0 11. Table 4 to subpart SSSSS is revised to read as follows:

    Table 4 to Subpart SSSSS to Part 63.--Requirements for Performance Tests [As stated in Sec. 63.9800, you must comply with the requirements for performance tests for affected sources in the following table:]

    According to the following For . . .

    You must . . .

    Using . . .

    requirements . . .

    1. Each affected source listed in a. Conduct performance i. The requirements of (1) Record the date of the Table 1 to this subpart.

    tests.

    the General

    test; and Provisions in subpart (2) Identify the emission A of this part and source that is tested; and the requirements to (3) Collect and record the this subpart.

    corresponding operating parameter and emission test data listed in this table for each run of the performance test; and (4) Repeat the performance test at least every 5 years; and (5) Repeat the performance test before changing the parameter value for any operating limit specified in your OM&M plan; and (6) If complying with the THC concentration or THC percentage reduction limits specified in items 2 through 9 of Table 1 to this subpart, repeat the performance test under the conditions specified in items 2.a.2 and 2.a.3. of this table; and (7) If complying with the emission limits for new clay refractory products kilns specified in items 10 and 11 of Table 1 to this subpart, repeat the performance test under the conditions specified in items 14.a.i.4. and 17.a.i.4. of this table.

    [[Page 7426]]

    b. Select the

    i. Method 1 or 1A of (1) To demonstrate locations of sampling 40 CFR, part 60,

    compliance with the ports and the number appendix A.

    percentage reduction of traverse points.

    limits specified in items 2.b., 3.b., 6.b., 7.b., 10, and 11 of Table 1 to this subpart, OR to develop an emissions profile, OR to satisfy the requirements of item 13.a. of this table, locate sampling sites at the inlet of the control device and at either the outlet of the control device or at the stack prior to any releases to the atmosphere; AND (2) To demonstrate compliance with any other emission limit specified in Table 1 to this subpart, locate all sampling sites at the outlet of the control device or at the stack prior to any releases to the atmosphere. c. Determine gas

    Method 2, 2A, 2C, 2D, Measure gas velocities and velocity and

    2F, or 2G of 40 CFR volumetric flow rates at 1- volumetric flow rate. part 60, appendix A. hr intervals throughout each test run. d. Conduct gas

    (i) Method 3, 3A, or As specified in the molecular weight

    3B of 40 CFR part 60, applicable test method. analysis.

    appendix A; or (ii) ASME PTC 19.10- You may use ASME PTC 19.10- 1981--Part 10.

    1981--Part 10 (available for purchase from Three Park Avenue, New York, NY 10016-5990) as an alternative to EPA Method 3B. e. Measure gas

    Method 4 of 40 CFR As specified in the moisture content. part 60, appendix A. applicable test Method. 2. Each new or existing curing a. Conduct performance ...................... (1) Conduct the performance oven, shape dryer, and kiln that tests.

    test while the source is is used to process refractory b. Satisfy the

    operating at the maximum products that use organic HAP; applicable

    organic HAP processing each new or existing coking oven requirements listed

    rate, as defined in Sec. and defumer that is used to

    in items 3 through 13

    63.9824, reasonably produce pitch-impregnated

    of this table.

    expected to occur; and refractory products; each new

    (2) Repeat the performance shape preheater that is used to

    test before starting produce pitch-impregnated

    production of any product refractory products; AND each new

    for which the organic HAP or existing process unit that is

    processing rate is likely exhausted to a thermal or

    to exceed the maximum catalytic oxidizer that also

    allowable organic HAP controls emissions from an

    processing rate affected shape preheater or pitch

    established during the working tank.

    most recent performance test, as specified in Sec. 63.9798(c); and (3) Repeat the performance test on any affected uncontrolled kiln following process changes (e.g., shorter curing oven cycle time) that could increase organic HAP emissions from the affected kiln, as specified in Sec. 63.9798(d). 3. Each affected continuous process a. Perform a minimum The appropriate test Each test run must be at unit.

    of 3 test runs.

    methods specified in least 1 hour in duration. items 1, 4, and 5 of this table. b. Establish the

    i. Method 311 of 40 (1) Calculate and record operating limit for CFR part 63, appendix the organic HAP content of the maximum organic A, OR material safety all refractory shapes that HAP processing rate. data sheets (MSDS), are processed during the OR product labels to performance test, based on determine the mass the mass fraction of fraction of organic organic HAP in the resins, HAP in each resin, binders, or additives; the binder, or additive; mass fraction of each and

    binder, or additive, in ii. Product

    the product; and the formulation data that process feed rate; and specify the mass (2) Calculate and record fraction of each

    the organic HAP processing resin, binder, and rate (pounds per hour) for additive in the

    each test run; and products that are (3) Calculate and record processed during the the maximum allowable performance test; and. organic HAP processing iii. Process feed rate rate as 110 percent of the data (tons per hour). average of the processing rates for the three test runs.

    [[Page 7427]]

    c. Record the

    Process data.......... During each test run and at operating temperature

    least once per hour, of the affected

    record the operating source.

    temperature in the highest temperature zone of the affected source. 4. Each continuous process unit a. Measure THC

    i. Method 25A of 40 (1) Each minute, measure that is subject to the THC

    concentrations at the CFR Part 60, appendix and record the emission limit listed in item

    outlet of the control A.

    concentrations of THC in 2.a., 3.a., 4, or 5 of Table 1 to device or in the

    the exhaust stream; and this subpart.

    stack.

    (2) Provide at least 50 1- minute measurements for each valid hourly average THC concentration. b. Measure oxygen i. Method 3A of 40 CFR (1) Each minute, measure concentrations at the Part 60, appendix A. and record the outlet of the control

    concentrations of oxygen device or in the

    in the exhaust stream; and stack.

    (2) Provide at least 50 1- minute measurements for each valid hourly average oxygen concentration. c. Determine the

    i. Equation 1 of Sec. (1) Calculate the hourly hourly average THC 63,9800(g)(1); and average THC concentration concentration,

    ii. The 1-minute THC for each hour of the corrected to 18

    and oxygen

    performance test as the percent oxygen.

    concentration data. average of the 1-minute THC measurements; and (2) Calculate the hourly average oxygen concentration for each hour of the performance test as the average of the 1-minute oxygen measurements; and (3) Correct the hourly average THC concentrations to 18 percent oxygen using Equation 1 of Sec. 63.9800(g)(1). d. Determine the 3- The hourly average Calculate the 3-hour block hour block average concentrati on of average THC emission THC emission

    THC, corrected to 18 concentration, corrected concentration,

    percent oxygen, for to 18 percent oxygen, as corrected to 18

    each test run.

    the average of the hourly percent oxygen.

    average THC emission concentrations, corrected to 18 percent oxygen. 5. Each continuous process unit a. Measure THC

    i. Method 25A of 40 (1) Each minute, measure that is subject to the THC

    concentrations at the CFR part 60, appendix and record the percentage reduction limit listed inlet and outlet of A.

    concentrations of THC at in item 2.b. or 3.b. of Table 1 to the control device.

    the inlet and outlet of this subpart.

    the control device; and (2) Provide at least 50 1- minute measurements for each valid hourly average THC at the control device inlet and outlet. b. Determine the

    i. The 1-minute THC Calculate the hourly THC hourly THC mass

    concentration data at mass emissions rates at emissions rates at the control device the control device inlet the inlet and outlet inlet and outlet; and and outlet for each hour of the control device. ii. The volumetric of the performance test. flow rates at the control device inlet and outlet. c. Determine the 3- i. The hourly THC mass (1) Calculate the hourly hour block average emissions rates at THC for each hour of the THC percentage

    the inlet and outlet performance test using reduction.

    of the control device. Equation 2 of Sec. 63.9800(g)(1); and (2) Calculate the 3-hour block average THC percentage reduction. 6. Each continuous process unit a. Establish the

    i. Continuous

    (1) At least every 15 that is equipped with a thermal operating limit for recording of the

    minutes, measure and oxidizer.

    the minimum allowable output of the

    record the thermal thermal oxidizer

    combustion chamber oxidizer combustion combustion chamber temperature

    temperature; and temperature.

    measurement device. (2) Provide at least one measurement during at least three 15-minute periods per hour of testing; and (3) Calculate the hourly average thermal oxidizer combustion chamber temperature for each hour of the performance test; and (4) Calculate the minimum allowable combustion chamber temperature as the average of the combustion chamber temperatures for the three test runs, minus 14 [deg]C (25 [deg]F). 7. Each continuous process unit a. Establish the

    i. Continuous

    (1) At least every the 15 that is equipped with a catalytic operating limit for recording of the

    minutes, measure and oxidizer.

    the minimum allowable output of the

    record the temperature at temperature at the temperature

    the inlet of the catalyst inlet of the catalyst measurement device. bed; and bed.

    (2) Provide at least one catalyst bed inlet temperature measurement during at least three 15- minute periods per hour of testing; and (3) Calculate the hourly average catalyst bed inlet temperature for each hour of the performance test; and (4) Calculate the minimum allowable catalyst bed inlet temperature as the average of the catalyst bed inlet temperatures for the three test runs, minus 14 [deg]C (25 [deg]F).

    [[Page 7428]]

    8. Each affected batch process unit a. Perform a minimum i. The appropriate (1) Each test run must be of 2 test runs.

    test methods

    conducted over a separate specified in items 1, batch cycle unless you 9, and 10 of this satisfy the requirements table.

    of Sec. 63.9800(f)(3) and (4); and (2) Each test run must begin with the start of a batch cycle, except as specified in item 8.a.i.4. of this table; and (3) Each test run must continue until the end of the batch cycle, except as specified in items 8.a.i.4. and 8.a.i.5. of this table; and (4) If you develop an emissions profile, as described in Sec. 63.9802(a)(1), you can limit each test run to the 3-hour peak THC mass emissions period; and (5) If you do not develop an emissions profile, a test run can be stopped, and the results of that run considered complete, if either of the following provisions are met: (i) you measure emissions continuously until at least 3 hours after the affected process unit has reached maximum temperature, AND the hourly average THC mass emissions rate at the outlet of the control device or in the stack has not increased during the 3- hour period since maximum process temperature was reached, AND the applicable emission limit specified in items 6 through 9 of Table 1 to this subpart was met during each of the 3 hours since maximum process temperature was reached, OR, (ii) for sources equipped with a thermal or catalytic oxidizer, at least 1 hour has passed since any reduction in the operating temperature of the oxidizer, as specified in item 13 of this table. b. Establish the

    i. Method 311 of 40 (1) Calculate and record operating limit for CFR part 63, appendix the organic HAP content of the maximum organic A, OR MSDS, OR

    all refractory shapes that HAP processing rate. product labels to are processed during the determine the mass performance test, based on fraction of organic the mass fraction of HAP in each resin, organic HAP in the resins, binder, or additive; binders, or additives; the and

    mass fraction of each ii. Product

    resin, binder, or formulation data that additive, in the product, specify the mass

    and the batch weight prior fraction of each (2) Calculate and record resin, binder, and the organic HAP processing additive in the

    rate (pounds per batch) products that are for each test run; and processed during the (3) Calculate and record performance test; and. the maximum allowable iii. Batch weight

    organic HAP processing as (tons).

    110 percent of the average of the organic HAP processing rates for the two test runs. c. Record the batch Process data.......... Record the total elapsed cycle time.

    time from the start to the completion of the batch cycle. d. Record the

    Process data.......... Record the operating operating temperature

    temperature of the of the affected

    affected source at least source.

    once every hour from the start to the completion of the batch cycle. 9. Each batch process unit that is a. Measure THC

    i. Method 25A of 40 (1) Each minute, measure subject to the THC emission limit concentrations at the CFR part 60, appendix and record concentrations listed in item 6.a., 7.a., 8, or 9 outlet of the control A.

    of THC in the exhaust of Table 1 to this subpart.

    device or in the

    stream; and stack.

    (2) Provide at least 50 1- minute measurements for each valid hourly average THC concentration. b. Measure oxygen i. Method 3A of 40 CFR (1) Each minute, measure concentrations at the part 60, appendix A. and record concentrations outlet of the control

    of oxygen in the exhaust device or in the

    stream; and stack.

    (2) Provide at least 50 1- minute measurements for each valid hourly average oxygen concentration. c. Determine the

    i. Equation 1 of Sec. (1) Calculate the hourly hourly average THC 63.9800(g)(1); and average THC concentration concentration,

    ii. The 1-minute THC for each hour of the corrected to 18

    and oxygen

    performance test as the percent oxygen.

    concentration data. average of the 1-minute THC measurements; and (2) Calculate the hourly average oxygen concentration for each hour of the performance test as the average of the 1-minute oxygen measurement; and (3) Correct the hourly average THC concentrations to 18 percent oxygen using Equation 1 of Sec. 63.9800(g)(1).

    [[Page 7429]]

    d. Determine the 3- The hourly average THC Select the period of 3 hour peak THC

    concentrations,

    consecutive hours over emissions

    corrected to 18

    which the sum of the concentration period percent oxygen.

    hourly average THC for each test run.

    concentrations, corrected to 18 percent oxygen, at the control device outlet or in the stack is greater than the sum of the hourly average THC emission concentrations, corrected to 18 percent oxygen, at the control device outlet or in the stack for any other period of 3 consecutive hours during the test run. e. Determine the

    The hourly average THC Calculate the average of average THC

    emission

    the hourly average THC concentration,

    concentrations,

    concentrations, corrected corrected to 18

    corrected to 18

    to 18 percent oxygen, for percent oxygen, for percent oxygen, for the 3 hours of the peak each test run.

    the 3-hour peak THC THC emissions emissions

    concentration period for concentration period. each test run. f. Determine the 2-run The average THC

    Calculate the average of block average THC concentration,

    the average THC concentration,

    corrected to 18

    concentrations, corrected corrected to 18

    percent oxygen, for to 18 percent oxygen, for percent oxygen, for each test run.

    the two test runs. the emission test. 10. Each batch process unit that is a. Measure THC

    i. Method 25A of 40 (1) Each minute, measure subject to the THC percentage

    concentrations at the CFR part 60, appendix and record the reduction limit listed in item inlet and outlet of A.

    concentrations of THC at 6.b. or 7.b. of Table 1 to this the control device.

    the control device inlet subpart.

    and outlet; and (2) Provide at least 50 1- minute measurements for each valid hourly average THC concentration at the control device inlet and outlet. b. Determine the

    i. The 1-minute THC Calculate the hourly THC hourly THC mass

    concentration data at mass emissions rates at emissions rates at the control device the control device inlet the control device inlet and outlet; and and outlet for each hour inlet and outlet. ii. The volumetric of the performance test. flow rates at the control device inlet and outlet. c. Determine the 3- The hourly THC mass Select the period of 3 hour peak THC mass emissions rates at consecutive hours over emissions period for the control device which the sum of the each test run.

    inlet.

    hourly THC mass emissions rates at the control device inlet is greater than the sum of the hourly THC mass emissions rates at the control device inlet for any other period of 3 consecutive hours during the test run. d. Determine the

    i. Equation 2 of Sec. Calculate the average THC average THC

    63.9800(g)(2); and percentage reduction for percentage reduction ii. The hourly THC each test run using for each test run. mass emissions rates Equation 2 of Sec. at the control device 63.9800(g)(2). inlet and outlet for the 3-hour peak THC mass emissions period. e. Determine the 2-run The average THC

    Calculate the average of block average THC percentage reduction the average THC percentage percentage reduction for each test run. reductions for the two for the emission

    test runs. test. f. If complying with i. Method 3A of 40 CFR (1) Each minute, measure the provisions for part 60, appendix A. and record the reducing the thermal

    concentrations of oxygen oxidizer operating

    in the exhaust stream; and temperature, as

    (2) Calculate each hourly specified in item 13

    average oxygen of Table 4 to this

    concentration using at subpart, measure the

    least 50 1-minute oxygen concentration

    measurements for each at the inlet to the

    valid hourly average control device.

    oxygen concentration.

    [[Page 7430]]

    11. Each batch process unit that is a. Establish the

    i. Continuous

    (1) At least every 15 equipped with a thermal oxidizer. operating limit for recording of the

    minutes of each entire the minimum thermal output of the

    test run, measure and oxidizer combustion combustion chamber record the thermal chamber temperature. temperature

    oxidizer combustion measurement device. chamber temperature; and (2) Provide at least one temperature measurement during at least three 15- minute periods per hour of testing; and (3) For each test run, calculate the hourly average combustion chamber temperature for each hour of the 3-hour peak THC emissions concentration period or the 3-hour peak THC mass emissions period, as defined in Sec. 63.9824, whichever applies; and (4) Calculate the average combustion chamber temperature for the applicable 3-hour peak emissions period for each test run using the average hourly combustion chamber temperatures for the applicable 3-hour peak emissions period; and (5) Calculate the minimum allowable thermal oxidizer combustion chamber operating temperature as the average of the average combustion chamber temperatures for the applicable 3-hour peak emissions period for the two test runs, minus 14 [deg]C (25 [deg]F). 12. Each batch process unit that is a. Establish the

    i. Continuous

    (1) At least every 15 equipped with a catalytic oxidizer. operating limit for recording of the

    minutes of each entire the minimum allowable output of the

    test run, measure and temperature at the temperature

    record the temperature at inlet of the catalyst measurement device. the inlet of the catalyst bed.

    bed; and (2) Provide at least one catalyst bed inlet temperature measurement during at least three 15- minute periods per hour of testing; and (3) For each test run, calculate the hourly average catalyst bed inlet temperature for each hour of the 3-hour peak THC emissions concentration period or the 3-hour peak THC mass emissions period, as defined in Sec. 63.9824, whichever applies; and (4) Calculate the average catalyst bed inlet temperature for the applicable 3-hour peak emissions period for each test run using the average hourly catalyst bed inlet temperatures for the applicable 3-hour peak emissions period; and (5) Calculate the minimum allowable catalyst bed inlet operating temperature as the average of the average catalyst bed inlet temperatures for the applicable 3-hour peak emissions period for the two test runs, minus 14 [deg]C (25 [deg]F).

    [[Page 7431]]

    13. Each batch process unit that is a. During each test ...................... (1) The oxidizer can be equipped with a thermal or

    run, maintain the

    shut off or the oxidizer catalytic oxidizer.

    applicable operating

    operating temperature can temperature of the

    be reduced if you do not oxidizer until

    use an emissions profile emission levels allow

    to limit testing to the 3- the oxidizer to be

    hour peak THC mass shut off or the

    emissions period, as operating temperature

    specified in item 8.a.i.4. of the oxidizer to be

    of this table; reduced.

    (2) At least 3 hours have passed since the affected process unit reached maximum temperature; and (3) The applicable emission limit specified in item 6.a. or 6.b. of Table 1 to this subpart was met during each of the previous three 3-hour periods; and (4) The hourly average THC mass emissions rate at the control device inlet did not increase during the 3- hour period that immediately preceded the oxidizer temperature reduction; and (5) The THC concentration at the oxidizer inlet did not exceed 20 ppmvd, corrected to 18 percent oxygen, during each of the four 15-minute periods immediately following the oxidizer temperature reduction; and (6) If the THC concentration exceeded 20 ppmvd, corrected to 18 percent oxygen, during any of the four 15-minute periods immediately following the oxidizer temperature reduction, you must return the oxidizer to its normal operating temperature as soon as possible and maintain that temperature for at least 1 hour; and (7) Continue the test run until the THC concentration at the oxidizer inlet is no more than 20 ppmvd, corrected to 18 percent oxygen, for at least four consecutive 15-minute periods that immediately follow the oxidizer temperature reduction. 14. Each new continuous kiln that a. Measure emissions i. Method 26A of 40 (1) Conduct the test while is used to process clay refractory of HF and HCL.

    CFR part 60, appendix the kiln is operating at products.

    A; or 60, appendix A; the maximum production or

    level and is processing ii. Method 26 of 40 the refractory product CFR part 60, appendix with the highest A; or.

    uncalcined clay processing iii. Method 320 of 40 rate, as specified in item CFR part 63, appendix 15.a. of this table; and A.

    (2) You may use Method 26 of 40 CFR part 60, appendix A, only if no acid PM (e.g., HF or HCL dissolved in water droplets emitted by sources controlled by a wet scrubber) is present; and (3) If you use Method 320 of 40 CFR part 63, appendix A, you must follow the analyte spiking procedures of Section 13 of Method 320 unless you can demonstrate that the complete spiking procedure has been conducted at a similar source; and (4) Repeat the performance test if the affected source is controlled with a DLA and you change the source of the limestone used in the DLA. b. Perform a minimum The appropriate test Each test run must be at of 3 test runs.

    methods specified in least 1 hour in duration. items 1 and 14.a. of this table. 15. Each new continuous kiln that a. Record the

    i. Production data; (1) Record the production is subject to the production-based uncalcined clay

    and

    rate (tons per hour of HF and HCL emission limits

    processing rate. ii. Product

    fired product); and specified in items 10.a. and 10.b.

    formulation data that (2) Calculate and record of Table 1 to this subpart.

    specify the mass

    the average rate at which fraction of

    uncalcined clay is uncalcined clay in processed (tons per hour) the products that are for each test run. processed during the performance test. b. Determine the HF i. Method 26A of 40 Calculate the HF mass mass emissions rate CFR part 60, appendix emissions rate for each at the outlet of the A; or

    test run. control device or in ii. Method 26 of 40 the stack.

    CFR part 60, appendix A; or. iii. Method 320 of 40 CFR part 63, appendix A..

    [[Page 7432]]

    c. Determine the 3- i. The HF mass

    (1) Calculate the hourly hour block average emissions rate for production-based HF production-based HF each test run; and emissions rate for each emissions rate.

    ii. The average

    test run using Equation 3 uncalcined clay

    of Sec. 63.9800(g)(3); processing rate.

    and (2) Calculate the 3-hour block average production- based HF emissions rate as the average of the hourly production-based HF emissions rates for each test run. d. Determine the HCL i. Method 26A of 40 Calculate the HCl mass mass emissions rate CFR part 60, appendix emissions rate for each at the outlet of the A; or

    test run. control device or in ii. Method 26 of 40 the stack.

    CFR part 60, appendix A; or. iii. Method 320 of 40 CFR part 63, appendix A. e. Determine the 3- i. The HCl mass

    (1) Calculate the hourly hour block average emissions rate for production-based HCl production-based HCL each test run; and emissions rate for each emissions rate.

    ii. The average

    test run using Equation 3 uncalcined clay

    of Sec. 63.9800(g)(3); processing rate.

    and (2) Calculate the 3-hour block average production- based HCl rate as the average of the production- based HCl emissions rates for each test run. 16. Each new continuous kiln that a. Measure the HF mass i. Method 26A of 40 Calculate the HF mass is subject to the HF and HCL

    emissions rates at CFR part 60, appendix emissions rates at the percentage reduction limits

    the inlet and outlet A; or

    control device inlet and specified in items 10.a. and 10.b. of the control device. ii. Method 26 of 40 outlet for each test run. of Table 1 to this subpart.

    CFR part 60, appendix A; or. iii. Method 320 of 40 CFR part 63, appendix A. b. Determine the 3- i. The HF mass

    (1) Calculate the hourly HF hour block average HF emissions rates at percentage reduction using percentage reduction. the inlet and outlet Equation 2 of Sec. of the control device 63.9800(g)(2); and for each test run. (2) Calculate the 3-hour block average HF percentage reduction as the average of the HF percentage reductions for each test run. c. Measure the HCL i. Method 26A of 40 Calculate the HCl mass mass emissions rates CFR part 60, appendix emissions rates at the at the inlet and

    A; or

    control device inlet and outlet control device. ii. Method 26 of 40 outlet for each test run. CFR part 60, appendix A; or. iii. Method 320 of 40 CFR part 63, appendix A. d. Determine the 3- i. The HCl mass

    (1) Calculate the hourly hour block average emissions rates at HCl percentage reduction HCL percentage

    the inlet and outlet using Equation 2 of Sec. reduction.

    of the control device 63.9800(g)(2); and for each test run. (2) Calculate the 3-hour block average HCl percentage reduction as the average of HCl percentage reductions for each test run. 17. Each new batch process kiln a. Measure emissions i. Method 26A of 40 (1) Conduct the test while that is used to process clay

    of HF and HCL at the CFR part 60, appendix the kiln is operating at refractory products.

    inlet and outlet of A; or

    the maximum production the control device. ii. Method 26 of 40 level and is processing CFR part 60, appendix the refractory product A; or.

    with the highest iii. Method 320 of 40 uncalcined clay processing CFR part 63, appendix rate, as specified in item A.

    15.a. of this table; and (2) You may use Method 26 of 40 CFR part 60, appendix A, only if no acid PM (e.g., HF or HCl dissolved in water droplets emitted by sources controlled by a wet scrubber) is present; and (3) If you use Method 320 of 40 CFR part 63, appendix A, you must follow the analyte spiking procedures of Section 13 of Method 320 unless you can demonstrate that the complete spiking procedure has been conducted at a similar source; and (4) Repeat the performance test if the affected source is controlled with a DLA and you change the source of the limestone used in the DLA.

    [[Page 7433]]

    b. Perform a minimum i. The appropriate (1) Each test run must be of 2 test runs.

    test methods

    conducted over a separate specified in items 1 batch cycle unless you and 17.a. of this satisfy the requirements table.

    of Sec. 63.9800(f)(3) and (4); and (2) Each test run must consist of a series of 1- hour runs at the inlet and outlet of the control device, beginning with the start of a batch cycle, except as specified in item 17.b.i.4. of this table; and (3) Each test run must continue until the end of the batch cycle, except as specified in item 17.b.i.4. of this table; and (4) If you develop an emissions profile, as described in Sec. 63.9802(a)(2), you can limit each test run to the 3-hour peak HF mass emissions period. c. Determine the

    i. The appropriate Determine the hourly mass hourly HF and HCl test methods

    HF and HCl emissions rates mass emissions rates specified in items 1 at the inlet and outlet of at the inlet and

    and 71.a. of this the control device for outlet of the control table.

    each hour of each test device.

    run. d. Determine the 3- The hourly HF mass Select the period of 3 hour peak HF mass emissions rates at consecutive hours over emissions period. the inlet of the

    which the sum of the control device.

    hourly HF mass emissions rates at the control device inlet is greater than the sum of the hourly HF mass emissions rates at the control device inlet for any other period of 3 consecutive hours during the test run. e. Determine the 2-run i. The hourly average (1) Calculate the HF block average HF

    HF emissions rates at percentage reduction for percentage reduction the inlet and outlet each hour of the 3-hour for the emissions of the control

    peak HF mass emissions test.

    device.

    period using Equation 2 of Sec. 63.9800(g)(2); AND (2) Calculate the average HF percentage reduction for each test run as the average of the hourly HF percentage reductions for the 3-hour peak HF mass emissions period for that run; and (3) Calculate the 2-run block average HF percentage reduction for the emission test as the average of the average HF percentage reductions for the two test runs. f. Determine the 2-run i. The hourly average (1) Calculate the HCl block average HCl HCl emissions rates percentage reduction for percentage reduction at the inlet and

    each hour of the 3-hour for the emission test. outlet of the control peak HF mass emissions device.

    period using Equation 2 of Sec. 63.9800(g)(2); and (2) Calculate the average HCl percentage reduction for each test run as the average of the hourly HCl percentage reductions for the 3-hour peak HF mass emissions period for that run; and (3) Calculate the 2-run block average HCl percentage reduction for the emission test as the average of the average HCl percentage reductions for the two test runs. 18. Each new kiln that is used to a. Establish the

    i. Data from the

    (1) At least every 15 process clay refractory products operating limit for pressure drop

    minutes, measure the and is equipped with a DLA.

    the minimum pressure measurement device pressure drop across the drop across the DLA. during the

    DLA; and performance test. (2) Provide at least one pressure drop measurement during at least three 15- minute periods per hour of testing; and (3) Calculate the hourly average pressure drop across the DLA for each hour of the performance test; and (4) Calculate and record the minimum pressure drop as the average of the hourly average pressure drops across the DLA for the two or three test runs, whichever applies. b. Establish the

    i. Data from the

    (1) Establish the limestone operating limit for limestone feeder

    feeder setting 1 week the limestone feeder during the

    prior to the performance setting.

    performance test. test; and (2) Record and maintain the feeder setting for the 1- week period that precedes the performance test and during the performance test.

    [[Page 7434]]

    19. Each new kiln that is used to a. Document

    Data from the

    Submit analyses and process clay refractory products conformance with

    installation and

    supporting documentation and is equipped with a DIFF or DLS/ specifications and calibration of the demonstrating conformance FF.

    requirements of the bag leak detection with EPA guidance and bag leak detection system.

    specifications for bag system.

    i. Data from the lime leak detection systems as b. Establish the

    feeder during the part of the Notification operating limit for performance test. of Compliance Status. the lime feeder

    (1) For continuous lime setting.

    injection systems, ensure that lime in the feed hopper or silo is free- flowing at all times during the performance test; and (2) Record the feeder setting for the two or three runs, whichever applies. (3) If the feed rate setting varies during the three test runs, calculate and record the average feed rate for the two or three test runs, whichever applies. 20. Each new kiln that is used to a. Establish the

    i. Data from the

    (1) At least every 15 process clay refractory products operating limit for pressure drop

    minutes, measure the and is equipped with a wet

    the minimum scrubber measurement device pressure drop across the scrubber.

    pressure drop.

    during the

    scrubber; and performance test. (2) Provide at least one pressure drop measurement during at least three 15- minute periods per hour of testing; and (3) Calculate the hourly average pressure drop across the scrubber for each hour of the performance test; and (4) Calculate and record the minimum pressure drop as the average of the hourly average pressure drops across the scrubber for the two or three test runs, whichever applies. b. Establish the

    i. Data from the pH (1) At least every 15 operating limit for measurement device minutes, measure scrubber the minimum scrubber during the

    liquid pH; and liquid pH.

    performance test. (2) Provide at least one pH measurement during at least three 15-minute periods per hour of testing; and (3) Calculate the hourly average pH values for each hour of the performance test; and (4) Calculate and record the minimum liquid pH as the average of the hourly average pH measurements for the two or three test runs, whichever applies. c. Establish the

    i. Data from the flow (1) At least every 15 operating limit for rate measurement

    minutes, measure the the minimum scrubber device during the scrubber liquid flow rate; liquid flow rate. performance test. and (2) Provide at least one flow rate measurement during at least three 15- minute periods per hour of testing; and (3) Calculate the hourly average liquid flow rate for each hour of the performance test; and (4) Calculate and record the minimum liquid flow rate as the average of the hourly average liquid flow rates for the two or three test runs, whichever applies. d. If chemicals are i. Data from the

    (1) At least every 15 added to the scrubber chemical feed rate minutes, measure the liquid, establish the measurement device scrubber chemical feed operating limit for during the

    rate; and the minimum scrubber performance test. (2) Provide at least one chemical feed rate.

    chemical feed rate measurement during at least three 15-minute periods per hour of testing; and (3) Calculate the hourly average chemical feed rate for each hour of the performance test; and (4) Calculate and record the minimum chemical feed rate as the average of the hourly average chemical feed rates for the two or three test runs, whichever applies.

    0 12. Table 5 to subpart SSSSS is amended as follows: 0 a. Revising items 5 and 6; and 0 b. Revising items 10.a and b.

    [[Page 7435]]

    Table 5 to Subpart SSSSS of Part 63.--Initial Compliance with Emission Limits [As stated in Sec. 63.9806, you must show initial compliance with the emission limits for affected sources according to the following table:]

    You have For . . .

    For the following demonstrated initial emission limit . . . compliance if . . .

    * * * * * * * 5. Each affected batch

    The average THC The 2-run block process unit that is

    concentration must average THC subject to the THC emission not exceed 20

    emission concentration limit listed ppmvd, corrected to concentration for in item 6.a., 7.a., 8, or 9 18 percent oxygen. the 3-hour peak THC of Table 1 to this subpart.

    emissions concentration period measured during the performance test using Methods 25A and 3A is equal to or less than 20 ppmvd, corrected to 18 percent oxygen. 6. Each affected batch

    The average THC The 2-run block process unit that is

    percentage

    average THC subject to the THC

    reduction must

    percentage percentage reduction limit equal or exceed 95 reduction for the 3- listed in item 6.b. or 7.b. percent.

    hour peak THC mass of Table 1 to this subpart.

    emissions period measured during the performance test using Method 25A is equal to or greater than 95 percent.

    * * * * * * * 10. Each new batch process a. The average

    The 2-run block kiln that is used to

    uncontrolled HF average HF emission process clay refractory emissions must be reduction for the 3- products.

    reduced by at least hour peak HF mass 90 percent.

    emissions period measured during the performance test is equal to or greater than 90 percent. b. The average

    The 2-run block uncontrolled HCl average HCl emissions must be emissions reduction reduced by at least for the 3-hour peak 30 percent.

    HF mass emissions period measured during the performance test is equal to or greater than 30 percent.

    * * * * * * *

    0 13. Table 7 to subpart SSSSS is amended as follows: 0 a. Revising item 2; 0 b. Revising item 4 by designating the entry in column 3 as item i and adding item 4.ii; 0 c. Revising item 5 by designating the entry in column 3 as item i and adding item 5.ii; and 0 d. Removing item 9.a.ii and redesignating items 9.a.iii and iv as items 9.a.ii and iii, respectively.

    Table 7 to Subpart SSSSS to Part 63.--Continuous Compliance with Emission Limits [As stated in Sec. 63.9810, you must show continuous compliance with the emission limits for affected sources according to the following table:]

    You have For . . .

    For the following demonstrated initial emission limit . . . compliance if . . .

    * * * * * * * 2. Each new or existing As specified in Satisfying the curing oven, shape dryer, items 3 through 7 applicable and kiln that is used to of this table.

    requirements process refractory products

    specified in items that use organic HAP; each

    3 through 7 of this new or existing coking oven

    table. and defumer that is used to produce pitch-impregnated refractory products; each new shape preheater that is used to produce pitch- impregnated refractory products; AND each new or existing process unit that is exhausted to a thermal or catalytic oxidizer that also controls emissions from an affected shape preheater or pitch working tank.

    * * * * * * * 4. Each affected process The average THC i. Operating and unit that is equipped with concentration must maintaining a THC a control device other than not exceed 20

    CEMS at the outlet a thermal or catalytic

    ppmvd, corrected to of the control oxidizer.

    18 percent oxygen; device or in the OR the average THC stack of the percentage

    affected source, reduction must

    according to the equal or exceed 95 requirements of percent.

    Procedure 1 of 40 CFR part 60, appendix F; and ii. Maintaining the 3-hour block average THC concentration at or below 20 ppmvd, corrected to 18 percent oxygen.

    [[Page 7436]]

    5. Each affected process The average THC i. Operating and unit that uses process

    concentration must maintaining a THC changes to meet the

    not exceed 20

    CEMS at the outlet applicable emission limit. ppmvd, corrected to of the control 18 percent oxygen. device or in the stack of the affected source, according to the requirements of Procedure 1 of 40 CFR part 60, appendix F; and ii. Maintaining the 3-hour block average THC concentration at or below 20 ppmvd, corrected to 18 percent oxygen.

    * * * * * * *

    0 14. Table 8 to subpart SSSSS is amended as follows: 0 a. Revising item 4.iii and adding item 4.iv; 0 b. Revising item 7.iv and adding item 7.v; 0 c. Revising items 8 and 8.i through v and adding items 8.vi through viii; 0 d. Revising items 9 and 9.i through iv, redesignating items 9.v and vi as items 9.viii and ix, respectively, and adding items 9.v. through vii; 0 e. Revising items 11.a.ii and iii, adding item 11.a.iv, removing item 11.b, and redesignating items 11.c and d as items 11.b and c, respectively; and 0 f. Revising items 13.a.ii and iii, 13.b.ii and iii, 13.c.ii and iii, and 13.d.ii and iii, and adding items 13.a.iv, 13.b.iv, 13.c.iv, and 13.d.iv.

    Table 8 to Subpart SSSSS of Part 63.--Continuous Compliance With Operating Limits [As stated in Sec. 63.9810, you must show continuous compliance with the operating limits for affected sources according to the following table:]

    You must demonstrate For the following

    continuous For . . .

    operating limit . . compliance by . . . .

    * * * * * * * 4. Each affected continuous a. Maintain process * * * process unit.

    operating

    iii. Maintaining the parameters within 3-hour block the limits

    average organic HAP established during processing rate at the most recent or below the performance test. maximum allowable organic HAP processing rate established during the most recent performance test; and iv. Reporting, in accordance with Sec. 63.9814(e), any 3-hour block average organic HAP processing rate that exceeds the maximum allowable organic HAP processing rate established during the most recent performance test

    * * * * * * * 7. Each affected batch

    a. Maintain process * * * process unit.

    operating

    iv. Maintaining the parameters within organic HAP the limits

    processing rate at established during or below the the most recent maximum allowable performance test. organic HAP processing rate established during the most recent performance test; and v. Reporting, in accordance with Sec. 63.9814(e), any organic HAP processing rate that exceeds the maximum allowable organic HAP processing rate established during the most recent performance test.

    [[Page 7437]]

    8. Batch process units that Maintain the hourly i. Measuring and are equipped with a thermal average temperature recording the oxidizer.

    in the thermal

    thermal oxidizer oxidizer combustion combustion chamber chamber at or above temperature at the minimum

    least every 15 allowable operating minutes throughout temperature

    any period during established during which the thermal the most recent oxidizer is performance test. required to be in operation; and ii. Calculating the hourly average thermal oxidizer combustion chamber temperature for any period during which the thermal oxidizer is required to be in operation; and iii. Except as permitted by item 8.iv of this table, maintaining throughout the entire batch cycle the hourly average operating temperature in the thermal oxidizer combustion chamber at or above the minimum allowable operating temperature established during the most recent performance test; and iv. If complying with the provisions for reducing the thermal oxidizer operating temperature, as specified in item 13 of Table 4 to this subpart, satisfying the requirements of items 8.vi. through 8.viii. of this table; and v. Reporting, in accordance with Sec. 63.9814(e), any temperature measurements below the minimum allowable thermal oxidizer combustion chamber temperature established during the most recent performance test. vi. From the start of the batch cycle until the batch process unit reaches its maximum temperature, maintaining the thermal oxidizer combustion chamber temperature at or above the minimum allowable temperature established during the most recent performance test, as determined according to item 11 of Table 4 to this subpart; vii. From the time when the batch process unit reaches its maximum temperature, maintaining the thermal oxidizer combustion chamber temperature at or above the minimum allowable temperature established during the most recent performance test, as determined according to item 11 of Table 4 to this subpart, for a length of time that equals or exceeds the length of time between the process unit reaching its maximum temperature and the start of the thermal oxidizer temperature reduction during the most recent performance test; viii. For the remainder of the batch process cycle, maintaining the thermal oxidizer combustion chamber temperature at or above the reduced thermal oxidizer temperature established during the most recent performance test, as specified in item 13 of Table 4 to this subpart.

    [[Page 7438]]

    9. Batch process units that Maintain the hourly i. Measuring and are equipped with a

    average temperature recording the catalytic oxidizer.

    at the inlet of the temperature at the catalyst bed at or inlet of the above the minimum catalyst bed at allowable operating least every 15 temperature

    minutes throughout established during any period during the most recent which the catalytic performance test. oxidizer is required to be in operation; and ii. Calculating the hourly average temperature at the catalyst bed inlet for any period during which the catalytic oxidizer is required to be in operation; and iii. Except as specified in items 9.a.iv through 9.a.vii of this table, maintaining throughout the entire batch cycle the hourly average operating temperature at the catalyst bed inlet at or above the minimum allowable performance allowable operating temperature established during the most recent performance test; and iv. If complying with the provisions for reducing the catalytic oxidizer operating temperature, as specified in item 13 of Table 4 to this subpart, satisfying the requirements of items 9.a.v. through 9.a.vii. of this table; and v. From the start of the batch cycle until the batch process unit reaches its maximum temperature, maintaining the temperature at the inlet of the catalyst bed at or above the minimum allowable temperature established during the most recent performance test, as determined according to item 12 of Table 4 to this subpart; and vi. From the time when the batch process unit reaches its maximum temperature, maintaining the temperature at the inlet of the catalyst bed at or above the minimum allowable temperature established during the most recent performance test, as determined according to item 12 of Table 4 to this subpart, for a length of time that equals or exceeds the length of time between the process unit reaching its maximum temperature and the start of the catalytic oxidizer temperature reduction during the most recent performance test; and vii. For the remainder of the batch process cycle, maintaining the temperature at the inlet of the catalyst bed at or above the reduced catalyst bed inlet temperature established during the most recent performance test, as specified in item 13 of Table 4 to this subpart; and viii. Reporting, in accordance with Sec. 63.9814(e), any catalyst bed inlet temperature measurements below the minimum allowable bed inlet temperature measured during the most recent performance test; and ix. Checking the activity level of the catalyst at least every 12 months and taking any necessary corrective action, such as replacing the catalyst, to ensure that the catalyst is performing as designed.

    [[Page 7439]]

    * * * * * * * 11. Each new kiln that is a. Maintain the * * * equipped with a DLA.

    average pressure ii. Calculating the drop the DLA for hourly average each 3-hour block pressure drop period at or above across the DLA; and the mininum

    iii. Maintaining the pressure drop

    3-hour block established during average pressure the most recent drop across the DLA performance test. at or above the minimum pressure drop established during the most recent performance test; and iv. Reporting, in accordance with Sec. 63.9814(e), any 3-hour block average pressure drop across the DLA below the minimum pressure drop established during the most recent performance test.

    * * * * * * * 13. Each new kiln that is a. Maintain the * * * used to process clay

    average pressure ii. Calculating the refractory products and is drop across the hourly average equipped with a wet

    scrubber for each 3- pressure drop scrubber.

    hour block period across the at or above the scrubber; and minimum pressure iii. Maintaining the drop established 3-hour block during the most average scrubber recent performance pressure drop at or test.

    above the minimum pressure drop established during the most recent performance test; and iv. Reporting, in accordance with during the Sec. 63.9814(e), any 3- hour block average most recent pressure drop across the scrubber below the minimum pressure drop established during the most recent performance test. b. Maintain the * * * average average ii. Calculating the scrubber liquid pH hourly average for each 3-hour scrubber liquid pH; block period at or and above the minimum iii. Maintaining the scrubber liquid pH 3-hour block established during average scrubber the most recent liquid pH at or performance test. above the minimum scrubber liquid pH estalbished during the most recent perforamnce test; and iv. Reporting, in accordance with Sec. 63.9814(e), any 3-hour block average scrubber liquid pH below the minimum liquid pH established during the most recent performance test. c. Maintain the * * * average scrubber ii. Calculating the liquid flow rate hourly average for each 3-hour scrubber liquid block period at or flow rate; and above the minimum iii. Maintaining the scrubber liquid 3-hour block flow rate

    average scrubber established during liquid flow rate at the most recent or above the performance test. minimum scrubber liquid flow rate established during the most recent performance test; and iv. Reporting, in accordance with Sec. 63.9814(e), any 3-hour block average established scrubber liquid flow rate below the minimum liquid flow rate established during the most most recent performance test.

    [[Page 7440]]

    d. If chemicals are * * * added to the

    ii. Calculating the scrubber liquid, hourly average maintain the

    scrubber chemical average scrubber feed rate; and chemical feed rate iii. Maintaining the for each 3-hour 3-hour block block period at or average scrubber above the minimum chemical feed rate scrubber chemical at or above the feed rate

    scrubber minimum established during scrubber chemical the most recent feed rate performance test. established during the most recent rate for each performance test; and iv. Reporting, in accordance with Sec. 63.9814(e), any 3-hour block average scrubber chemical feed rate below the minimum chemical feed rate established during the most recent performance test

    * * * * * * *

    0 15. Table 10 to subpart SSSSS is amended by revising item 1 to read as follows:

    Table 10 to Subpart SSSSS of Part 63.--Requirements for Reports [As stated in Sec. 63.9814, you must comply with the requirements for reports in the following table:]

    The report must You must submit the You must submit a(n) . . . contain . . .

    report . . .

    1. Compliance report........ The information in Semiannually Sec. 63.9814(a) according to the through (f).

    requirements in Sec. 63.9814(b)

    * * * * * * *

    0 16. Table 11 to subpart SSSSS is amended as follows: 0 a. Revising citation Sec. 63.4; 0 b. Adding citations Sec. 63.6(i)(15) and (16); 0 c. Revising citation Sec. 63.7(b)(2); 0 d. Revising citation Sec. 63.7(e)(3); and 0 e. Revising citations Sec. 63.8(c)(1)(i), (ii), and (iii).

    Table 11 to Subpart SSSSS of Part 63.--Applicability of General Provisions to Subpart SSSSS [As stated in Sec. 63.9820, you must comply with the applicable General Provisions requirements according to the following table:]

    Applies to subpart SSSSS Citation

    Subject

    Brief description

    * * * * * * * Sec. 63.4.................. Prohibited Activities... Compliance date;

    Yes. circumvention; fragmentation.

    * * * * * * * Sec. 63.6(i)(15)........... [Reserved].............. Sec. 63.6(i)(16)........... Administrator's

    Granting extension does not Yes. authority.

    abrogate Administrator's authority.

    * * * * * * * Sec. 63.7(b)(2)............ Notification of

    Must notify Administrator as Yes. Rescheduling.

    soon as is practicable and provide rescheduled date.

    * * * * * * * Sec. 63.7(e)(3)............ Test Run Duration....... Must have three test runs for Yes; Yes, except where at least the time specified specified in Sec. in the relevant standard; 63.9800 for batch compliance is based on

    process sources; Yes. arithmetic mean of three runs; specifies conditions when data from an additional test run can be used. Sec. 63.8(c)(1)(i)......... Operation and

    Must maintain CMS in

    Yes. Maintenance of CMS. accordance with Sec. 63.6(e)(1). Sec. 63.8(c)(1)(ii)........ Spare Parts for CMS..... Must maintain spare parts for Yes. routine CMS repairs. Sec. 63.8(c)(1)(iii)....... SSMP for CMS............ Must develop and implement Yes. SSMP for CMS. * * * * * * *

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    [FR Doc. 06-1218 Filed 2-10-06; 8:45 am]

    BILLING CODE 6560-50-P