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40 C.F.R. §§ 63.1207–63.1209

3 sections in range

§63.1207. What are the performance testing requirements?

40 C.F.R. § 63.1207

(a)
General. The provisions of § 63.7 apply, except § 63.7(e)(1) and as noted below.
(b)
Types of performance tests—
(1)
Comprehensive performance test. You must conduct comprehensive performance tests to demonstrate compliance with the emission standards provided by this subpart, establish limits for the operating parameters provided by § 63.1209, and demonstrate compliance with the performance specifications for continuous monitoring systems.
(2)
Confirmatory performance test. You must conduct confirmatory performance tests to:
(i)
Demonstrate compliance with the dioxin/furan emission standard when the source operates under normal operating conditions; and
(ii)
Conduct a performance evaluation of continuous monitoring systems required for compliance assurance with the dioxin/furan emission standard under § 63.1209(k).
(3)
One-Time Dioxin/Furan Test for Sources Not Subject to a Numerical Dioxin/Furan Standard. For solid fuel boilers and hydrochloric acid production furnaces, for lightweight aggregate kilns that are not subject to a numerical dioxin/furan emission standard under § 63.1221, and liquid fuel boilers that are not subject to a numerical dioxin/furan emission standard under § 63.1217, you must conduct a one-time emission test for dioxin/furan under feed and operating conditions that are most likely to reflect daily maximum operating variability, similar to a dioxin/furan comprehensive performance test.
(i)
You must conduct the dioxin/furan emissions test no later than the deadline for conducting the initial comprehensive performance test.
(ii)
You may use dioxin/furan emissions data from previous testing to meet this requirement, provided that:
(A)
The testing was conducted under feed and operating conditions that are most likely to reflect daily maximum operating variability, similar to a dioxin/furan compliance test;
(B)
You have not changed the design or operation of the source in a manner that could significantly affect stack gas dioxin/furan emission concentrations; and
(C)
The data meet quality assurance objectives that may be determined on a site-specific basis.
(iii)
You may use dioxin/furan emissions data from a source to represent emissions from another on-site source in lieu of testing (i.e., data in lieu of testing) if the design and operation, including hazardous waste feed and other feedstreams, of the sources are identical.
(iv)
You must include the results of the one-time dioxin/furan emissions test with the results of the initial comprehensive performance test in the Notification of Compliance.
(v)
You must repeat the dioxin/furan emissions test if you change the design or operation of the source in a manner that may increase dioxin/furan emissions.
(vi)
Sources that are required to perform the one-time dioxin/furan test pursuant to paragraph (b)(3) of this section are not required to perform confirmatory performance tests.
(c)
Initial comprehensive performance test—
(1)
Test date. Except as provided by paragraphs (c)(2) and (3) of this section, you must commence the initial comprehensive performance test not later than six months after the compliance date.
(2)
Data in lieu of the initial comprehensive performance test.
(i)
You may request that previous emissions test data serve as documentation of conformance with the emission standards of this subpart provided that the previous testing:
(A)
Was initiated after 54 months prior to the compliance date, except as provided by paragraph (c)(2)(iii) or (iv) of this section;
(B)
Results in data that meet quality assurance objectives (determined on a site-specific basis) such that the results demonstrate compliance with the applicable standards;
(C)
Was in conformance with the requirements of paragraph (g)(1) of this section; and
(D)
Was sufficient to establish the applicable operating parameter limits under § 63.1209.
(ii)
You must submit data in lieu of the initial comprehensive performance test in lieu of (i.e., if the data are in lieu of all performance testing) or with the notification of performance test required under paragraph (e) of this section.
(iii)
The data in lieu test age restriction provided in paragraph (c)(2)(i)(A) of this section does not apply for the duration of the interim standards (i.e., the standards published in the Federal Register on February 13, 2002, 67 FR 6792). See 40 CFR parts 63, 264, 265, 266, 270, and 271 revised as of July 1, 2002. Paragraph (c)(2)(i)(A) of this section does not apply until EPA promulgates permanent replacement standards pursuant to the Settlement Agreement noticed in the Federal Register on November 16, 2001 (66 FR 57715).
(iv)
The data in lieu test age restriction provided in paragraph (c)(2)(i)(A) of this section does not apply to DRE data provided you do not feed hazardous waste at a location in the combustion system other than the normal flame zone.
(3)
For hydrogen fluoride and hydrogen cyanide emission standards, the Notification of Compliance for the initial compliance test must be postmarked no later than the relevant compliance dates in § 63.1206(a). Data in lieu of the initial demonstration of compliance may be submitted in accordance with paragraph (c)(2) of this section. The initial compliance test must follow the notification requirements prescribed for a comprehensive performance test, and may coincide with a comprehensive performance test. After the initial compliance test, compliance with hydrogen fluoride and hydrogen cyanide emission limits must be demonstrated during each subsequent comprehensive performance test.
(d)
Frequency of testing. Except as otherwise specified in paragraph (d)(4) of this section, you must conduct testing periodically as prescribed in paragraphs (d)(1) through (3) of this section. The date of commencement of the initial comprehensive performance test is the basis for establishing the deadline to commence the initial confirmatory performance test and the next comprehensive performance test. You may conduct performance testing at any time prior to the required date. The deadline for commencing subsequent confirmatory and comprehensive performance testing is based on the date of commencement of the previous comprehensive performance test. Unless the Administrator grants a time extension under paragraph (i) of this section, you must conduct testing as follows:
(1)
Comprehensive performance testing. Except as otherwise specified in paragraph (d)(4) of this section, you must commence testing no later than 61 months after the date of commencing the previous comprehensive performance test used to show compliance with § 63.1216, § 63.1217, § 63.1218, § 63.1219, § 63.1220, or § 63.1221. If you submit data in lieu of the initial performance test, you must commence the subsequent comprehensive performance test within 61 months of commencing the test used to provide the data in lieu of the initial performance test.
(2)
Confirmatory performance testing. Except as otherwise specified in paragraph (d)(4) of this section, you must commence confirmatory performance testing no later than 31 months after the date of commencing the previous comprehensive performance test used to show compliance with § 63.1217, § 63.1219, § 63.1220, or § 63.1221. If you submit data in lieu of the initial performance test, you must commence the initial confirmatory performance test within 31 months of the date six months after the compliance date. To ensure that the confirmatory test is conducted approximately midway between comprehensive performance tests, the Administrator will not approve a test plan that schedules testing within 18 months of commencing the previous comprehensive performance test.
(3)
Duration of testing. You must complete performance testing within 60 days after the date of commencement, unless the Administrator determines that a time extension is warranted based on your documentation in writing of factors beyond your control that prevent you from meeting the 60-day deadline.
(4)
Applicable testing requirements under the interim standards—
(i)
Waiver of periodic comprehensive performance tests. Except as provided by paragraph (c)(2) of this section, you must conduct only an initial comprehensive performance test under the interim standards (§§ 63.1203 through 63.1205); all subsequent comprehensive performance testing requirements are waived under the interim standards. The provisions in the introductory text to paragraph (d) and in paragraph (d)(1) of this section apply only to tests used to demonstrate compliance with the standards under §§ 63.1219 through 63.1221.
(ii)
Waiver of confirmatory performance tests. You are not required to conduct a confirmatory test under the interim standards (§§ 63.1203 through 63.1205). The confirmatory testing requirements in the introductory text to paragraph (d) and in paragraph (d)(2) of this section apply only after you have demonstrated compliance with the standards under §§ 63.1219 through 63.1221.
(e)
Notification of performance test and CMS performance evaluation, and approval of test plan and CMS performance evaluation plan.
(1)
The provisions of §§ 63.7(b) and (c) and 63.8(e) apply, except:
(i)
Comprehensive performance test. You must submit to the Administrator a notification of your intention to conduct a comprehensive performance test and CMS performance evaluation and a site-specific test plan and CMS performance evaluation test plan at least one year before the performance test and performance evaluation are scheduled to begin.
(A)
The Administrator will notify you of approval or intent to deny approval of the site-specific test plan and CMS performance evaluation test plan within 9 months after receipt of the original plan.
(B)
You must submit to the Administrator a notification of your intention to conduct the comprehensive performance test at least 60 calendar days before the test is scheduled to begin.
(ii)
Confirmatory performance test. You must submit to the Administrator a notification of your intention to conduct a confirmatory performance test and CMS performance evaluation and a site-specific test plan and CMS performance evaluation test plan for those parameters required under § 63.1207(b)(2)(ii) at least 60 calendar days before the performance test is scheduled to begin. The Administrator will notify you of approval or intent to deny approval of the site-specific test plan and CMS performance evaluation test plan within 30 calendar days after receipt of the original test plans.
(2)
You must make your site-specific test plan and CMS performance evaluation test plan available to the public for review no later than 60 calendar days before initiation of the test. You must issue a public notice to all persons on your facility/public mailing list (developed pursuant to §§ 70.7(h), 71.11(d)(3)(i)(E) and 124.10(c)(1)(ix) of this chapter) announcing the availability of the test plans and the location where the test plans are available for review. The test plans must be accessible to the public for 60 calendar days, beginning on the date that you issue your public notice. The location must be unrestricted and provide access to the public during reasonable hours and provide a means for the public to obtain copies. The notification must include the following information at a minimum:
(i)
The name and telephone number of the source's contact person;
(ii)
The name and telephone number of the regulatory agency's contact person;
(iii)
The location where the test plans and any necessary supporting documentation can be reviewed and copied;
(iv)
The time period for which the test plans will be available for public review; and
(v)
An expected time period for commencement and completion of the performance test and CMS performance evaluation test.
(3)
Petitions for time extension if Administrator fails to approve or deny test plans. You may petition the Administrator under § 63.7(h) to obtain a “waiver” of any performance test—initial or periodic performance test; comprehensive or confirmatory test. The “waiver” would be implemented as an extension of time to conduct the performance test at a later date.
(i)
Qualifications for the waiver.
(A)
You may not petition the Administrator for a waiver under this section if the Administrator has issued a notification of intent to deny your test plan(s) under § 63.7(c)(3)(i)(B);
(B)
You must submit a site-specific emissions testing plan and a continuous monitoring system performance evaluation test plan at least one year before a comprehensive performance test is scheduled to begin as required by paragraph (c)(1) of this section, or at least 60 days before a confirmatory performance test is scheduled to begin as required by paragraph (d) of this section. The test plans must include all required documentation, including the substantive content requirements of paragraph (f) of this section and § 63.8(e); and
(C)
You must make a good faith effort to accommodate the Administrator's comments on the test plans.
(ii)
Procedures for obtaining a waiver and duration of the waiver.
(A)
You must submit to the Administrator a waiver petition or request to renew the petition under § 63.7(h) separately for each source at least 60 days prior to the scheduled date of the performance test;
(B)
The Administrator will approve or deny the petition within 30 days of receipt and notify you promptly of the decision;
(C)
The Administrator will not approve an individual waiver petition for a duration exceeding 6 months;
(D)
The Administrator will include a sunset provision in the waiver ending the waiver within 6 months;
(E)
You may submit a revised petition to renew the waiver under § 63.7(h)(3)(iii) at least 60 days prior to the end date of the most recently approved waiver petition;
(F)
The Administrator may approve a revised petition for a total waiver period up to 12 months.
(iii)
Content of the waiver.
(A)
You must provide documentation to enable the Administrator to determine that the source is meeting the relevant standard(s) on a continuous basis as required by § 63.7(h)(2). For extension requests for the initial comprehensive performance test, you must submit your Documentation of Compliance to assist the Administrator in making this determination.
(B)
You must include in the petition information justifying your request for a waiver, such as the technical or economic infeasibility, or the impracticality, of the affected source performing the required test, as required by § 63.7(h)(3)(iii).
(iv)
Public notice. At the same time that you submit your petition to the Administrator, you must notify the public (e.g., distribute a notice to the facility/public mailing list developed pursuant to §§ 70.7(h), 71.11(d)(3)(i)(E) and 124.10(c)(1)(ix) of this chapter) of your petition to waive a performance test. The notification must include all of the following information at a minimum:
(A)
The name and telephone number of the source's contact person;
(B)
The name and telephone number of the regulatory agency's contact person;
(C)
The date the source submitted its site-specific performance test plan and CMS performance evaluation test plans; and
(D)
The length of time requested for the waiver.
(f)
Content of performance test plan. The provisions of § 63.7(c)(2)(i) through (iii) and (v) regarding the content of the test plan apply. In addition, you must include the following information in the test plan:
(1)
Content of comprehensive performance test plan.
(i)
An analysis of each feedstream, including hazardous waste, other fuels, and industrial furnace feedstocks, as fired, that includes:
(A)
Heating value, levels of ash (for hazardous waste incinerators only), levels of semivolatile metals, low volatile metals, mercury, and total chlorine (organic and inorganic); and
(B)
Viscosity or description of the physical form of the feedstream;
(ii)
For organic hazardous air pollutants established by 42 U.S.C. 7412(b)(1), as amended by subpart C of this part:
(A)
Except as provided by paragraph (f)(1)(ii)(D) of this section, an identification of such organic hazardous air pollutants that are present in each hazardous waste feedstream. You need not analyze for organic hazardous air pollutants that would reasonably not be expected to be found in the feedstream. You must identify any constituents you exclude from analysis and explain the basis for excluding them. You must conduct the feedstream analysis according to § 63.1208(b)(8);
(B)
An approximate quantification of such identified organic hazardous air pollutants in the hazardous waste feedstreams, within the precision produced by analytical procedures of § 63.1208(b)(8); and
(C)
A description of blending procedures, if applicable, prior to firing the hazardous waste feedstream, including a detailed analysis of the materials prior to blending, and blending ratios.
(D)
The Administrator may approve on a case-by-case basis a hazardous waste feedstream analysis for organic hazardous air pollutants in lieu of the analysis required under paragraph (f)(1)(ii)(A) of this section if the reduced analysis is sufficient to ensure that the POHCs used to demonstrate compliance with the applicable DRE standards of this subpart continue to be representative of the most difficult to destroy organic compounds in your hazardous waste feedstreams;
(iii)
A detailed engineering description of the hazardous waste combustor, including—
(A)
Manufacturer's name and model number of the hazardous waste combustor;
(B)
Type of hazardous waste combustor;
(C)
Maximum design capacity in appropriate units;
(D)
Description of the feed system for each feedstream;
(E)
Capacity of each feed system;
(F)
Description of automatic hazardous waste feed cutoff system(s);
(G)
Description of the design, operation, and maintenance practices for any air pollution control system; and
(H)
Description of the design, operation, and maintenance practices of any stack gas monitoring and pollution control monitoring systems;
(iv)
A detailed description of sampling and monitoring procedures including sampling and monitoring locations in the system, the equipment to be used, sampling and monitoring frequency, and planned analytical procedures for sample analysis;
(v)
A detailed test schedule for each hazardous waste for which the performance test is planned, including date(s), duration, quantity of hazardous waste to be burned, and other relevant factors;
(vi)
A detailed test protocol, including, for each hazardous waste identified, the ranges of hazardous waste feedrate for each feed system, and, as appropriate, the feedrates of other fuels and feedstocks, and any other relevant parameters that may affect the ability of the hazardous waste combustor to meet the emission standards;
(vii)
A description of, and planned operating conditions for, any emission control equipment that will be used;
(viii)
Procedures for rapidly stopping the hazardous waste feed and controlling emissions in the event of an equipment malfunction;
(ix)
A determination of the hazardous waste residence time as required by § 63.1206(b)(11);
(x)
If you are requesting to extrapolate metal feedrate limits from comprehensive performance test levels under § 63.1209(l)(1)(v) or (n)(2)(vii):
(A)
A description of the extrapolation methodology and rationale for how the approach ensures compliance with the emission standards;
(B)
Documentation of the historical range of normal (i.e., other than during compliance testing) metals feedrates for each feedstream;
(C)
Documentation that the level of spiking recommended during the performance test will mask sampling and analysis imprecision and inaccuracy to the extent that the extrapolated feedrate limits adequately assure compliance with the emission standards;
(xi)
If you do not continuously monitor regulated constituents in natural gas, process air feedstreams, and feedstreams from vapor recovery systems under § 63.1209(c)(5), you must include documentation of the expected levels of regulated constituents in those feedstreams;
(xii)
Documentation justifying the duration of system conditioning required to ensure the combustor has achieved steady-state operations under performance test operating conditions, as provided by paragraph (g)(1)(iii) of this section;
(xiii)
For cement kilns with in-line raw mills, if you elect to use the emissions averaging provision of this subpart, you must notify the Administrator of your intent in the initial (and subsequent) comprehensive performance test plan, and provide the information required by the emission averaging provision;
(xiv)
For preheater or preheater/precalciner cement kilns with dual stacks, if you elect to use the emissions averaging provision of this subpart, you must notify the Administrator of your intent in the initial (and subsequent) comprehensive performance test plan, and provide the information required by the emission averaging provision;
(xv)
If you are subject to the work practice standard under § 63.1209(s)(1) and are complying under § 63.1209(s)(1)(iii), the demonstration of maximum hydrogen fluoride MTEC and plan for a one-time hydrogen fluoride emissions test if required;
(xvi)
If you are not required to conduct performance testing to document compliance with the mercury, semivolatile metals, low volatile metals, hydrogen fluoride, or hydrogen chloride/chlorine gas emission standards under paragraph (m) of this section, you must include with the comprehensive performance test plan documentation of compliance with the provisions of that section.
(xvii)
If you propose to use a surrogate for measuring or monitoring gas flowrate, you must document in the comprehensive performance test plan that the surrogate adequately correlates with gas flowrate, as required by paragraph (m)(5) of this section, and § 63.1209(j)(2), (k)(3), (m)(2)(i), (n)(5)(i), and (o)(2)(i).
(xviii)
You must submit an application to request alternative monitoring under § 63.1209(g)(1) not later than with the comprehensive performance test plan, as required by § 63.1209(g)(1)(iii)(A).
(xix)
You must document the temperature location measurement in the comprehensive performance test plan, as required by § 63.1209(j)(1)(i) and (k)(2)(i).
(xx)
If your source is equipped with activated carbon injection, you must document in the comprehensive performance test plan:
(A)
The manufacturer specifications for minimum carrier fluid flowrate or pressure drop, as required by § 63.1209(k)(6)(ii); and
(B)
Key parameters that affect carbon adsorption, and the operating limits you establish for those parameters based on the carbon used during the performance test, if you elect not to specify and use the brand and type of carbon used during the comprehensive performance test, as required by § 63.1209(k)(6)(iii).
(xxi)
If your source is equipped with a carbon bed system, and you elect not to specify and use the brand and type of carbon used during the comprehensive performance test, you must include in the comprehensive performance test plan key parameters that affect carbon adsorption, and the operating limits you establish for those parameters based on the carbon used during the performance test, as required by § 63.1209(k)(7)(ii).
(xxii)
If you feed a dioxin/furan inhibitor into the combustion system, you must document in the comprehensive performance test plan key parameters that affect the effectiveness of the inhibitor, and the operating limits you establish for those parameters based on the inhibitor fed during the performance test, if you elect not to specify and use the brand and type of inhibitor used during the comprehensive performance test, as required by § 63.1209(k)(9)(ii).
(xxiii)
If your source is equipped with a wet scrubber and you elect to monitor solids content of the scrubber liquid manually but believe that hourly monitoring of solids content is not warranted, you must support an alternative monitoring frequency in the comprehensive performance test plan, as required by § 63.1209(m)(1)(i)(B)(1)(i).
(xxiv)
If your source is equipped with a particulate matter control device other than a wet scrubber, baghouse, or electrostatic precipitator, you must include in the comprehensive performance test plan:
(A)
Documentation to support the operating parameter limits you establish for the control device, as required by § 63.1209(m)(1)(iv)(A)(4); and
(B)
Support for the use of manufacturer specifications if you recommend such specifications in lieu of basing operating limits on performance test operating levels, as required by § 63.1209(m)(1)(iv)(D).
(xxv)
If your source is equipped with a dry scrubber to control hydrogen chloride and chlorine gas, you must document in the comprehensive performance test plan key parameters that affect adsorption, and the limits you establish for those parameters based on the sorbent used during the performance test, if you elect not to specify and use the brand and type of sorbent used during the comprehensive performance test, as required by § 63.1209(o)(4)(iii)(A); and
(xxvi)
For purposes of calculating semivolatile metal, low volatile metal, mercury, total fluorine (organic and inorganic), and total chlorine (organic and inorganic), and ash feedrate limits, a description of how you will handle performance test feedstream analytical results that determines these constituents are not present at detectable levels.
(xxvii)
Such other information as the Administrator reasonably finds necessary to determine whether to approve the performance test plan.
(2)
Content of confirmatory test plan.
(i)
A description of your normal hydrocarbon or carbon monoxide operating levels, as specified in paragraph (g)(2)(i) of this section, and an explanation of how these normal levels were determined;
(ii)
A description of your normal applicable operating parameter levels, as specified in paragraph (g)(2)(ii) of this section, and an explanation of how these normal levels were determined;
(iii)
A description of your normal chlorine operating levels, as specified in paragraph (g)(2)(iii) of this section, and an explanation of how these normal levels were determined;
(iv)
If you use carbon injection or a carbon bed, a description of your normal cleaning cycle of the particulate matter control device, as specified in paragraph (g)(2)(iv) of this section, and an explanation of how these normal levels were determined;
(v)
A detailed description of sampling and monitoring procedures including sampling and monitoring locations in the system, the equipment to be used, sampling and monitoring frequency, and planned analytical procedures for sample analysis;
(vi)
A detailed test schedule for each hazardous waste for which the performance test is planned, including date(s), duration, quantity of hazardous waste to be burned, and other relevant factors;
(vii)
A detailed test protocol, including, for each hazardous waste identified, the ranges of hazardous waste feedrate for each feed system, and, as appropriate, the feedrates of other fuels and feedstocks, and any other relevant parameters that may affect the ability of the hazardous waste combustor to meet the dioxin/furan emission standard;
(viii)
A description of, and planned operating conditions for, any emission control equipment that will be used;
(ix)
Procedures for rapidly stopping the hazardous waste feed and controlling emissions in the event of an equipment malfunction; and
(x)
Such other information as the Administrator reasonably finds necessary to determine whether to approve the confirmatory test plan.
(g)
Operating conditions during testing. You must comply with the provisions of § 63.7(e)(2) through (4). The owner or operator may not conduct performance tests during periods of startup, shutdown, or malfunction. The owner or operator must record the process information that is necessary to document operating conditions during the test and include in such record an explanation to support that such conditions represent the entire range of normal operation, including operational conditions for maximum emissions. The owner or operator shall make available to the Administrator such records as may be necessary to determine the conditions of performance tests. Conducting performance testing under operating conditions representative of the extreme range of normal conditions is consistent with the requirements of §§ 63.6(f)(2)(iii)(B) and 63.1207 to conduct performance testing under representative operating conditions.
(1)
Comprehensive performance testing—
(i)
Operations during testing. For the following parameters, you must operate the combustor during the performance test under normal conditions (or conditions that will result in higher than normal emissions):
(A)
Chlorine feedrate. You must feed normal (or higher) levels of chlorine during the dioxin/furan performance test;
(B)
Ash feedrate. For hazardous waste incinerators, you must conduct the following tests when feeding normal (or higher) levels of ash: The semivolatile metal and low volatile metal performance tests; and the dioxin/furan and mercury performance tests if activated carbon injection or a carbon bed is used; and
(C)
Cleaning cycle of the particulate matter control device. You must conduct the following tests when the particulate matter control device undergoes its normal (or more frequent) cleaning cycle: The particulate matter, semivolatile metal, and low volatile metal performance tests; and the dioxin/furan and mercury performance tests if activated carbon injection or a carbon bed is used.
(ii)
Modes of operation. Given that you must establish limits for the applicable operating parameters specified in § 63.1209 based on operations during the comprehensive performance test, you may conduct testing under two or more operating modes to provide operating flexibility.
(iii)
Steady-state conditions.
(A)
Prior to obtaining performance test data, you must operate under performance test conditions until you reach steady-state operations with respect to emissions of pollutants you must measure during the performance test and operating parameters under § 63.1209 for which you must establish limits. During system conditioning, you must ensure that each operating parameter for which you must establish a limit is held at the level planned for the performance test. You must include documentation in the performance test plan under paragraph (f) of this section justifying the duration of system conditioning.
(B)
If you own or operate a hazardous waste cement kiln that recycles collected particulate matter (i.e., cement kiln dust) into the kiln, you must sample and analyze the recycled particulate matter prior to obtaining performance test data for levels of selected metals that must be measured during performance testing to document that the system has reached steady-state conditions (i.e., that metals levels have stabilized). You must document the rationale for selecting metals that are indicative of system equilibrium and include the information in the performance test plan under paragraph (f) of this section. To determine system equilibrium, you must sample and analyze the recycled particulate matter hourly for each selected metal, unless you submit in the performance test plan a justification for reduced sampling and analysis and the Administrator approves in writing a reduced sampling and analysis frequency.
(2)
Confirmatory performance testing. You must conduct confirmatory performance testing for dioxin/furan under normal operating conditions for the following parameters:
(i)
Carbon monoxide (or hydrocarbon) CEMS emissions levels must be below the emission limit established for your hazardous waste combustor;
(ii)
Each operating limit (specified in § 63.1209) established to maintain compliance with the dioxin/furan emission standard must be held within the range of the average value over the previous 12 months and the maximum or minimum, as appropriate, that is allowed, except as provided by paragraph (g)(2)(v) of this section. The average value is defined as the sum of the rolling average values recorded over the previous 12 months, divided by the number of rolling averages recorded during that time. The average value must not include calibration data, startup data, shutdown data, malfunction data, and data obtained when not burning hazardous waste;
(iii)
You must feed chlorine at normal feedrates or greater; and
(iv)
If the combustor is equipped with carbon injection or carbon bed, normal cleaning cycle of the particulate matter control device.
(v)
The Administrator may approve an alternative range to that required by paragraphs (g)(2)(i) and (ii) of this section if you document in the confirmatory performance test plan that it may be problematic to maintain the required range during the test. In addition, when making the finding of compliance, the Administrator may consider test conditions outside of the range specified in the test plan based on a finding that you could not reasonably maintain the range specified in the test plan and considering factors including whether the time duration and level of the parameter when operations were out of the specified range were such that operations during the confirmatory test are determined to be reasonably representative of normal operations. In addition, the Administrator will consider the proximity of the emission test results to the standard.
(h)
Operating conditions during subsequent testing.
(1)
Current operating parameter limits established under § 63.1209 are waived during subsequent comprehensive performance testing.
(2)
Current operating parameter limits are also waived during pretesting prior to comprehensive performance testing for an aggregate time not to exceed 720 hours of operation (renewable at the discretion of the Administrator) under an approved test plan or if the source records the results of the pretesting. Pretesting means:
(i)
Operations when stack emissions testing for dioxin/furan, mercury, semivolatile metals, low volatile metals, particulate matter, or hydrogen chloride/chlorine gas is being performed; and
(ii)
Operations to reach steady-state operating conditions prior to stack emissions testing under paragraph (g)(1)(iii) of this section.
(i)
Time extension for subsequent performance tests. After the initial comprehensive performance test, you may request up to a one-year time extension for conducting a comprehensive or confirmatory performance test to consolidate performance testing with other state or federally required emission testing, or for other reasons deemed acceptable by the Administrator. If the Administrator grants a time extension for a comprehensive performance test, the deadlines for commencing the next comprehensive and confirmatory tests are based on the date that the subject comprehensive performance test commences.
(1)
You must submit in writing to the Administrator any request under this paragraph for a time extension for conducting a performance test.
(2)
You must include in the request for an extension for conducting a performance test the following:
(i)
A description of the reasons for requesting the time extension;
(ii)
The date by which you will commence performance testing.
(3)
The Administrator will notify you in writing of approval or intention to deny approval of your request for an extension for conducting a performance test within 30 calendar days after receipt of sufficient information to evaluate your request. The 30-day approval or denial period will begin after you have been notified in writing that your application is complete. The Administrator will notify you in writing whether the application contains sufficient information to make a determination within 30 calendar days after receipt of the original application and within 30 calendar days after receipt of any supplementary information that you submit.
(4)
When notifying you that your application is not complete, the Administrator will specify the information needed to complete the application. The Administrator will also provide notice of opportunity for you to present, in writing, within 30 calendar days after notification of the incomplete application, additional information or arguments to the Administrator to enable further action on the application.
(5)
Before denying any request for an extension for performance testing, the Administrator will notify you in writing of the Administrator's intention to issue the denial, together with:
(i)
Notice of the information and findings on which the intended denial is based; and
(ii)
Notice of opportunity for you to present in writing, within 15 calendar days after notification of the intended denial, additional information or arguments to the Administrator before further action on the request.
(6)
The Administrator's final determination to deny any request for an extension will be in writing and will set forth specific grounds upon which the denial is based. The final determination will be made within 30 calendar days after the presentation of additional information or argument (if the application is complete), or within 30 calendar days after the final date specified for the presentation if no presentation is made.
(j)
Notification of compliance—
(1)
Comprehensive performance test.
(i)
Except as provided by paragraphs (j)(4) and (5) of this section, within 90 days of completion of a comprehensive performance test, you must postmark a Notification of Compliance documenting compliance with the emission standards and continuous monitoring system requirements, and identifying operating parameter limits under § 63.1209.
(ii)
Upon postmark of the Notification of Compliance, you must comply with all operating requirements specified in the Notification of Compliance in lieu of the limits specified in the Documentation of Compliance required under § 63.1211(c).
(2)
Confirmatory performance test. Except as provided by paragraph (j)(4) of this section, within 90 days of completion of a confirmatory performance test, you must postmark a Notification of Compliance documenting compliance or noncompliance with the applicable dioxin/furan emission standard.
(3)
See §§ 63.7(g), 63.9(h), and 63.1210(d) for additional requirements pertaining to the Notification of Compliance (e.g., you must include results of performance tests in the Notification of Compliance). Beginning November 30, 2026, you must include in the Notification of Compliance a summary of the results of performance test and the performance test report must be submitted according to § 63.1211(f).
(4)
Time extension. You may submit a written request to the Administrator for a time extension documenting that, for reasons beyond your control, you may not be able to meet the 90-day deadline for submitting the Notification of Compliance after completion of testing. The Administrator will determine whether a time extension is warranted.
(5)
Early compliance. If you conduct the initial comprehensive performance test prior to the compliance date, you must postmark the Notification of Compliance within 90 days of completion of the performance test or by the compliance date, whichever is later.
(k)
Failure to submit a timely notification of compliance.
(1)
If you fail to postmark a Notification of Compliance by the specified date, you must cease hazardous waste burning immediately.
(2)
Prior to submitting a revised Notification of Compliance as provided by paragraph (k)(3) of this section, you may burn hazardous waste only for the purpose of pretesting or comprehensive performance testing and only for a maximum of 720 hours (renewable at the discretion of the Administrator).
(3)
You must submit to the Administrator a Notification of Compliance subsequent to a new comprehensive performance test before resuming hazardous waste burning.
(l)
Failure of performance test—
(1)
Comprehensive performance test. The provisions of this paragraph do not apply to the initial comprehensive performance test if you conduct the test prior to your compliance date.
(i)
If you determine (based on CEM recordings, results of analyses of stack samples, or results of CMS performance evaluations) that you have exceeded any emission standard during a comprehensive performance test for a mode of operation, you must cease hazardous waste burning immediately under that mode of operation. You must make this determination within 90 days following completion of the performance test.
(ii)
If you have failed to demonstrate compliance with the emission standards for any mode of operation:
(A)
Prior to submitting a revised Notification of Compliance as provided by paragraph (l)(1)(ii)(C) of this section, you may burn hazardous waste only for the purpose of pretesting or comprehensive performance testing under revised operating conditions, and only for a maximum of 720 hours (renewable at the discretion of the Administrator), except as provided by paragraph (l)(3) of this section;
(B)
You must conduct a comprehensive performance test under revised operating conditions following the requirements for performance testing of this section; and
(C)
You must submit to the Administrator a Notification of Compliance subsequent to the new comprehensive performance test.
(2)
Confirmatory performance test. If you determine (based on CEM recordings, results of analyses of stack samples, or results of CMS performance evaluations) that you have failed the dioxin/furan emission standard during a confirmatory performance test, you must cease burning hazardous waste immediately. You must make this determination within 90 days following completion of the performance test. To burn hazardous waste in the future:
(i)
You must submit to the Administrator for review and approval a test plan to conduct a comprehensive performance test to identify revised limits on the applicable dioxin/furan operating parameters specified in § 63.1209(k);
(ii)
You must submit to the Administrator a Notification of Compliance with the dioxin/furan emission standard under the provisions of paragraphs (j) and (k) of this section and this paragraph (l). You must include in the Notification of Compliance the revised limits on the applicable dioxin/furan operating parameters specified in § 63.1209(k); and
(iii)
Until the Notification of Compliance is submitted, you must not burn hazardous waste except for purposes of pretesting or confirmatory performance testing, and for a maximum of 720 hours (renewable at the discretion of the Administrator), except as provided by paragraph (l)(3) of this section.
(3)
You may petition the Administrator to obtain written approval to burn hazardous waste in the interim prior to submitting a Notification of Compliance for purposes other than testing or pretesting. You must specify operating requirements, including limits on operating parameters, that you determine will ensure compliance with the emission standards of this subpart based on available information including data from the failed performance test. The Administrator will review, modify as necessary, and approve if warranted the interim operating requirements. An approval of interim operating requirements will include a schedule for submitting a Notification of Compliance.
(m)
Waiver of performance test. You are not required to conduct performance tests to document compliance with the mercury, semivolatile metals, low volatile metals, hydrogen fluoride, or hydrogen chloride/chlorine gas emission standards under the conditions specified in paragraph (m)(1) or (2) of this section. The waiver provisions of this paragraph apply in addition to the provisions of § 63.7(h).
(1)
Emission standards based on exhaust gas flow rate.
(i)
You are deemed to be in compliance with an emission standard based on the volumetric flow rate of exhaust gas (i.e., µg/dscm or ppmv) if the maximum theoretical emission concentration (MTEC) does not exceed the emission standard over the relevant averaging period specified under § 63.1209(l), (n), and (o) of this section for the standard:
(A)
Determine the feedrate of mercury, semivolatile metals, low volatile metals, total fluorine or fluoride, or total chlorine and chloride from all feedstreams;
(B)
Determine the stack gas flowrate; and
(C)
Calculate a MTEC for each standard assuming all mercury, semivolatile metals, low volatile metals, total fluorine (organic and inorganic), or total chlorine (organic and inorganic) from all feedstreams is emitted;
(ii)
To document compliance with this provision, you must—
(A)
Monitor and record the feedrate of mercury, semivolatile metals, low volatile metals, total fluorine and fluoride, and total chlorine and chloride from all feedstreams according to § 63.1209(c);
(B)
Monitor with a CMS and record in the operating record the gas flowrate (either directly or by monitoring a surrogate parameter that you have correlated to gas flowrate);
(C)
Continuously calculate and record in the operating record the MTEC under the procedures of paragraph (m)(1)(i) of this section; and
(D)
Interlock the MTEC calculated in paragraph (m)(1)(i)(C) of this section to the AWFCO system to stop hazardous waste burning when the MTEC exceeds the emission standard.
(iii)
In lieu of the requirement in paragraphs (m)(1)(ii)(C) and (D) of this section, you may—
(A)
Identify in the Notification of Compliance a minimum gas flowrate limit and a maximum feedrate limit of mercury, semivolatile metals, low volatile metals, total fluorine and fluoride, and/or total chlorine and chloride from all feedstreams that ensures the MTEC as calculated in paragraph (m)(1)(i)(C) of this section is below the applicable emission standard; and
(B)
Interlock the minimum gas flowrate limit and maximum feedrate limit of paragraph (m)(1)(iii)(A) of this section to the AWFCO system to stop hazardous waste burning when the gas flowrate or mercury, semivolatile metals, low volatile metals, total fluorine and fluoride, and/or total chlorine and chloride feedrate exceeds the limits of paragraph (m)(1)(iii)(A) of this section.
(2)
Emission standards based on hazardous waste thermal concentration.
(i)
You are deemed to be in compliance with an emission standard specified on a hazardous waste thermal concentration basis (i.e., pounds emitted per million Btu of heat input) if the HAP thermal concentration in the waste feed does not exceed the allowable HAP thermal concentration emission rate.
(ii)
To document compliance with this provision, you must—
(A)
Monitor and record the feedrate of mercury, semivolatile metals, low volatile metals, and total chlorine and chloride from all hazardous waste feedstreams in accordance with § 63.1209(c);
(B)
Determine and record the higher heating value of each hazardous waste feed;
(C)
Continuously calculate and record the thermal feed rate of all hazardous waste feedstreams by summing the products of each hazardous waste feed rate multiplied by the higher heating value of that hazardous waste;
(D)
Continuously calculate and record the total HAP thermal feed concentration for each constituent by dividing the HAP feedrate determined in paragraph (m)(2)(ii)(A) of this section by the thermal feed rate determined in paragraph (m)(2)(ii)(C) of this section for all hazardous waste feedstreams;
(E)
Interlock the HAP thermal feed concentration for each constituent with the AWFCO to stop hazardous waste feed when the thermal feed concentration exceeds the applicable thermal emission standard.
(3)
When you determine the feedrate of mercury, semivolatile metals, low volatile metals, or total chlorine and chloride for purposes of this provision, except as provided by paragraph (m)(4) of this section, you must assume that the analyte is present at the full detection limit when the feedstream analysis determines that the analyte in not detected in the feedstream.
(4)
Owners and operators of hazardous waste burning cement kilns and lightweight aggregate kilns may assume that mercury is present in raw material at half the detection limit when the raw material feedstream analysis determines that mercury is not detected.
(5)
You must state in the site-specific test plan that you submit for review and approval under paragraph (e) of this section that you intend to comply with the provisions of this paragraph. You must include in the test plan documentation that any surrogate that is proposed for gas flowrate adequately correlates with the gas flowrate.
Notes, amendments, and revision history

Amendments

[91 FR 33532, June 3, 2026]

Source

Source: 64 FR 53038, Sept. 30, 1999, unless otherwise noted.

Authority

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

Source

Source: 57 FR 61992, Dec. 29, 1992, unless otherwise noted.

Amendments

[91 FR 33532, June 3, 2026]

§63.1208. What are the test methods?

40 C.F.R. § 63.1208

(a)
[Reserved]
(b)
Test methods. You must use the following test methods to determine compliance with the emissions standards of this subpart:
(1)
Dioxins and furans.
(i)
To determine compliance with the emission standard for dioxins and furans, you must use:
(A)
Before June 3, 2029, EPA Method 0023A, Sampling Method for Polychlorinated Dibenzo-p-Dioxins and Polychlorinated Dibenzofurans emissions from Stationary Sources, EPA Publication SW-846 (incorporated by reference—see § 63.14). After June 3, 2029, EPA Method 0023A is no longer allowed; or
(B)
EPA Method 23 of appendix A-7 to part 60 of this chapter.
(ii)
You must sample for a minimum of three hours, and you must collect a minimum sample volume of 2.5 dscm;
(iii)
You may assume that nondetects are present at zero concentration.
(2)
Mercury. You must use EPA Method 29 of appendix A-8 to part 60 of this chapter to demonstrate compliance with emission standard for mercury.
(3)
Cadmium and lead. You must use EPA Method 29 of appendix A-8 to part 60 of this chapter to determine compliance with the emission standard for cadmium and lead (combined).
(4)
Arsenic, beryllium, and chromium. You must use EPA Method 29 of appendix A-8 to part 60 of this chapter to determine compliance with the emission standard for arsenic, beryllium, and chromium (combined).
(5)
Hydrogen chloride and chlorine gas—
(i)
Compliance with MACT standards— . To determine compliance with the emission standard for hydrogen chloride and chlorine gas (combined), you must use:
(A)
EPA Method 26 or 26A of appendix A-8 to part 60 of this chapter; or
(B)
EPA Method 320 or 321 of appendix A to this part for hydrogen chloride and the back-half, caustic impingers of EPA Method 26 or 26A of appendix A-8 to part 60 of this chapter to measure chlorine gas.
(C)
[Reserved]
(ii)
Compliance with risk-based limits under § 63.1215. To demonstrate compliance with emission limits established under § 63.1215, you must use EPA Method 26 or 26A of appendix A-8 to part 60 of this chapter, EPA Method 320 of appendix A to this part, or EPA Method 321 of appendix A to this part.
(A)
For cement kilns and sources equipped with a dry acid gas scrubber, you must use EPA Method 320 or 321 of appendix A to this part to measure hydrogen chloride, and the back-half, caustic impingers of EPA Method 26 or 26A of appendix A-8 to part 60 of this chapter to measure chlorine gas; and
(B)
For incinerators, boilers, and lightweight aggregate kilns, you must use EPA Method 320 or 321 of appendix A to this part to measure hydrogen chloride, and EPA Method 26 or 26A of appendix A-8 to part 60 of this chapter to measure total chlorine, and calculate chlorine gas by difference if:

(1) The bromine/chlorine ratio in feedstreams is greater than 5 percent; or

(2) The sulfur/chlorine ratio in feedstreams is greater than 50 percent.

(6)
Hydrogen fluoride. To determine compliance with the emission standard for hydrogen fluoride gas, you must use:
(A)
EPA Method 26 or 26A of appendix A-8 to part 60 of this chapter; or
(B)
EPA Method 320 of appendix A to this part.
(7)
Hydrogen cyanide. To determine compliance with the emission standard for hydrogen cyanide gas, you must use:
(A)
EPA Method 320 of appendix A to this part; or
(B)
If there are entrained water droplet conduct the performance test according to the site-specific test plan submitted according to § 63.1207(e)(1)(i) . Any performance test, from a site with enclosed water droplets, which measures HCN concentrations, must be submitted for the Administrator's approval prior to testing according to § 63.7(f).
(8)
Particulate matter. You must use EPA Method 5 or 5I of appendix A-3 to part 60 of this chapter to demonstrate compliance with the emission standard for particulate matter.
(9)
DRE. The test method selected by the facility for volatile and/or semivolatile organic compounds must be approved in the comprehensive performance test plan.
(10)
Feedstream analytical methods. You may use any reliable analytical method to determine feedstream concentrations of metals, chlorine, fluorine, and other constituents. It is your responsibility to ensure that the sampling and analysis procedures are unbiased, precise, and that the results are representative of the feedstream.
(11)
Opacity. If you determine compliance with the opacity standard under the monitoring requirements of § 63.1209(a)(1)(iv) and (v), you must use EPA Method 9 of appendix A-4 to part 60 of this chapter.
Notes, amendments, and revision history

Amendments

[91 FR 33539, June 3, 2026]

Source

Source: 64 FR 53038, Sept. 30, 1999, unless otherwise noted.

Authority

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

Source

Source: 57 FR 61992, Dec. 29, 1992, unless otherwise noted.

Amendments

[91 FR 33539, June 3, 2026]

§63.1209. What are the monitoring requirements?

40 C.F.R. § 63.1209

(a)
Continuous emissions monitoring systems (CEMS) and continuous opacity monitoring systems (COMS).
(1)
(i)
You must use either a carbon monoxide or hydrocarbon CEMS to demonstrate and monitor compliance with the carbon monoxide and hydrocarbon standard under this subpart. You must also use an oxygen CEMS to continuously correct the carbon monoxide or hydrocarbon level to 7 percent oxygen.
(ii)
(A)
Cement kilns under— § 63.1204. Except as provided by paragraphs (a)(1)(iv) and (v) of the section, you must use a COMS to demonstrate and monitor compliance with the opacity standard under § 63.1204(a)(7) and (b)(7) at each point where emissions are vented from these affected sources including the bypass stack of a preheater or preheater/precalciner kiln with dual stacks.
(B)
Cement kilns under— § 63.1220. Except as provided by paragraphs (a)(1)(iv) and (v) of the section and unless your source is equipped with a bag leak detection system under § 63.1206(c)(8) or a particulate matter detection system under § 63.1206(c)(9), you must use a COMS to demonstrate and monitor compliance with the opacity standard under § 63.1220(a)(7) and (b)(7) at each point where emissions are vented from these affected sources including the bypass stack of a preheater or preheater/precalciner kiln with dual stacks.
(C)
You must maintain and operate each COMS in accordance with the requirements of § 63.8(c) except for the requirements under § 63.8(c)(3). The requirements of § 63.1211(c) shall be complied with instead of § 63.8(c)(3); and
(D)
Compliance is based on a six-minute block average.
(iii)
[Reserved]
(iv)
If you operate a cement kiln subject to the provisions of this subpart and use a fabric filter with multiple stacks or an electrostatic precipitator with multiple stacks, you may, in lieu of installing the COMS required by paragraph (a)(1)(ii) of this section, comply with the opacity standard in accordance with the procedures of EPA Method 9 of appendix A-4 to part 60 of this chapter:
(A)
You must conduct the EPA Method 9 of appendix A-4 to part 60 of this chapter test while the affected source is operating at the highest load or capacity level reasonably expected to occur within the day;
(B)
The duration of the EPA Method 9 of appendix A-4 to part 60 of this chapter test shall be at least 30 minutes each day;
(C)
You must use EPA Method 9 of appendix A-4 to part 60 of this chapter procedures to monitor and record the average opacity for each six-minute block period during the test; and
(D)
To remain in compliance, all six-minute block averages must not exceed the opacity standard.
(v)
If you operate a cement kiln subject to the provisions of this subpart and use a particulate matter control device that exhausts through a monovent, or if the use of a COMS in accordance with the installation specification of Performance Specification 1 (PS-1) of appendix B to part 60 of this chapter is not feasible, you may, in lieu of installing the COMS required by paragraph (a)(1)(ii) of this section, comply with the opacity standard in accordance with the procedures of EPA Method 9 of appendix A-4 to part 60 of this chapter:
(A)
You must conduct the EPA Method 9 of appendix A-4 to part 60 of this chapter test while the affected source is operating at the highest load or capacity level reasonably expected to occur within the day;
(B)
The duration of the EPA Method 9 of appendix A-4 to part 60 of this chapter test shall be at least 30 minutes each day;
(C)
You must use EPA Method 9 of appendix A-4 to part 60 of this chapter procedures to monitor and record the average opacity for each six-minute block period during the test; and
(D)
To remain in compliance, all six-minute block averages must not exceed the opacity standard.
(2)
Performance specifications. You must install, calibrate, maintain, and continuously operate the CEMS and COMS in compliance with the quality assurance procedures provided in the appendix to this subpart and Performance Specifications 1 (opacity), 4B (carbon monoxide and oxygen), and 8A (hydrocarbons) of appendix B to part 60 of this chapter.
(3)
Carbon monoxide readings exceeding the span.
(i)
Except as provided by paragraph (a)(3)(ii) of this section, if a carbon monoxide CEMS detects a response that results in a one-minute average at or above the 3,000 ppmv span level required by Performance Specification 4B of appendix B to part 60 of this chapter, the one-minute average must be recorded as 10,000 ppmv. The one-minute 10,000 ppmv value must be used for calculating the hourly rolling average carbon monoxide level.
(ii)
Carbon monoxide CEMS that use a span value of 10,000 ppmv when one-minute carbon monoxide levels are equal to or exceed 3,000 ppmv are not subject to paragraph (a)(3)(i) of this section. Carbon monoxide CEMS that use a span value of 10,000 are subject to the same CEMS performance and equipment specifications when operating in the range of 3,000 ppmv to 10,000 ppmv that are provided by Performance Specification 4B of appendix B to part 60 of this chapter for other carbon monoxide CEMS, except:
(A)
Calibration drift must be less than 300 ppmv; and
(B)
Calibration error must be less than 500 ppmv.
(4)
Hydrocarbon readings exceeding the span.
(i)
Except as provided by paragraph (a)(4)(ii) of this section, if a hydrocarbon CEMS detects a response that results in a one-minute average at or above the 100 ppmv span level required by Performance Specification 8A of appendix B to part 60 of this chapter, the one-minute average must be recorded as 500 ppmv. The one-minute 500 ppmv value must be used for calculating the hourly rolling average HC level.
(ii)
Hydrocarbon CEMS that use a span value of 500 ppmv when one-minute hydrocarbon levels are equal to or exceed 100 ppmv are not subject to paragraph (a)(4)(i) of this section. Hydrocarbon CEMS that use a span value of 500 ppmv are subject to the same CEMS performance and equipment specifications when operating in the range of 100 ppmv to 500 ppmv that are provided by Performance Specification 8A of appendix B to part 60 of this chapter, for other hydrocarbon CEMS, except:
(A)
The zero and high-level calibration gas must have a hydrocarbon level of between 0 and 100 ppmv, and between 250 and 450 ppmv, respectively;
(B)
The strip chart recorder, computer, or digital recorder must be capable of recording all readings within the CEM measurement range and must have a resolution of 2.5 ppmv;
(C)
The CEMS calibration must not differ by more than ±15 ppmv after each 24-hour period of the seven day test at both zero and high levels;
(D)
The calibration error must be no greater than 25 ppmv; and
(E)
The zero level, mid-level, and high level calibration gas used to determine calibration error must have a hydrocarbon level of 0-200 ppmv, 150-200 ppmv, and 350-400 ppmv, respectively.
(5)
Petitions to use CEMS for other standards. You may petition the Administrator to use CEMS for compliance monitoring for particulate matter, mercury, semivolatile metals, low volatile metals, and hydrogen chloride and chlorine gas under § 63.8(f) in lieu of compliance with the corresponding operating parameter limits under this section.
(6)
Calculation of rolling averages—
(i)
Calculation of rolling averages initially. The carbon monoxide or hydrocarbon CEMS must begin recording one-minute average values by 12:01 a.m. and hourly rolling average values by 1:01 a.m., when 60 one-minute values will be available for calculating the initial hourly rolling average for those sources that come into compliance on the regulatory compliance date. Sources that elect to come into compliance before the regulatory compliance date must begin recording one-minute and hourly rolling average values within 60 seconds and 60 minutes (when 60 one-minute values will be available for calculating the initial hourly rolling average), respectively, from the time at which compliance begins.
(ii)
Calculation of rolling averages upon intermittent operations. You must ignore periods of time when one-minute values are not available for calculating the hourly rolling average. When one-minute values become available again, the first one-minute value is added to the previous 59 values to calculate the hourly rolling average.
(iii)
Calculation of rolling averages when the hazardous waste feed is cutoff.
(A)
Except as provided by paragraph (a)(6)(iii)(B) of this section, you must continue monitoring carbon monoxide and hydrocarbons when the hazardous waste feed is cutoff if the source is operating. You must not resume feeding hazardous waste if the emission levels exceed the standard.
(B)
You are not subject to the CEMS requirements of this subpart during periods of time you meet the requirements of § 63.1206(b)(1)(ii) (compliance with emissions standards for nonhazardous waste burning sources when you are not burning hazardous waste).
(7)
Operating parameter limits for hydrocarbons. If you elect to comply with the carbon monoxide and hydrocarbon emission standard by continuously monitoring carbon monoxide with a CEMS, you must demonstrate that hydrocarbon emissions during the comprehensive performance test do not exceed the hydrocarbon emissions standard. In addition, the limits you establish on the destruction and removal efficiency (DRE) operating parameters required under paragraph (j) of this section also ensure that you maintain compliance with the hydrocarbon emission standard. If you do not conduct the hydrocarbon demonstration and DRE tests concurrently, you must establish separate operating parameter limits under paragraph (j) of this section based on each test and the more restrictive of the operating parameter limits applies.
(b)
Other continuous monitoring systems (CMS).
(1)
You must use CMS (e.g., thermocouples, pressure transducers, flow meters) to document compliance with the applicable operating parameter limits under this section.
(2)
Except as specified in paragraphs (b)(2)(i) and (ii) of this section, you must install and operate continuous monitoring systems other than CEMS in conformance with § 63.8(c)(3) that requires you, at a minimum, to comply with the manufacturer's written specifications or recommendations for installation, operation, and calibration of the system:
(i)
Calibration of thermocouples and pyrometers. The calibration of thermocouples must be verified at a frequency and in a manner consistent with manufacturer specifications, but no less frequent than once per year. You must operate and maintain optical pyrometers in accordance with manufacturer specifications unless otherwise approved by the Administrator. You must calibrate optical pyrometers in accordance with the frequency and procedures recommended by the manufacturer, but no less frequent than once per year, unless otherwise approved by the Administrator. And,
(ii)
Accuracy and calibration of weight measurement devices for activated carbon injection systems— . If you operate a carbon injection system, the accuracy of the weight measurement device must be ±1 percent of the weight being measured. The calibration of the device must be verified at least once each calendar quarter at a frequency of approximately 120 days.
(3)
CMS must sample the regulated parameter without interruption, and evaluate the detector response at least once each 15 seconds, and compute and record the average values at least every 60 seconds.
(4)
The span of the non-CEMS CMS detector must not be exceeded. You must interlock the span limits into the automatic waste feed cutoff system required by § 63.1206(c)(3).
(5)
Calculation of rolling averages—
(i)
Calculation of rolling averages initially. Continuous monitoring systems must begin recording one-minute average values by 12:01 a.m., hourly rolling average values by 1:01 a.m. (e.g., when 60 one-minute values will be available for calculating the initial hourly rolling average), and twelve-hour rolling averages by 12:01 p.m. (e.g., when 720 one-minute averages are available to calculate a 12-hour rolling average), for those sources that come into compliance on the regulatory compliance date. Sources that elect to come into compliance before the regulatory compliance date must begin recording one-minute, hourly rolling average, and 12-hour rolling average values within 60 seconds, 60 minutes (when 60 one-minute values will be available for calculating the initial hourly rolling average), and 720 minutes (when 720 one-minute values will be available for calculating the initial 12-hour hourly rolling average) respectively, from the time at which compliance begins.
(ii)
Calculation of rolling averages upon intermittent operations. You must ignore periods of time when one-minute values are not available for calculating rolling averages. When one-minute values become available again, the first one-minute value is added to the previous one-minute values to calculate rolling averages.
(iii)
Calculation of rolling averages when the hazardous waste feed is cutoff.
(A)
Except as provided by paragraph (b)(5)(iii)(B) of this section, you must continue monitoring operating parameter limits with a CMS when the hazardous waste feed is cutoff if the source is operating. You must not resume feeding hazardous waste if an operating parameter exceeds its limit.
(B)
You are not subject to the CMS requirements of this subpart during periods of time you meet the requirements of § 63.1206(b)(1)(ii) (compliance with emissions standards for nonhazardous waste burning sources when you are not burning hazardous waste).
(c)
Analysis of feedstreams—
(1)
General. Prior to feeding the material, you must obtain an analysis of each feedstream that is sufficient to document compliance with the applicable feedrate limits provided by this section.
(2)
Feedstream analysis plan. You must develop and implement a feedstream analysis plan and record it in the operating record. The plan must specify at a minimum:
(i)
The parameters for which you will analyze each feedstream to ensure compliance with the operating parameter limits of this section;
(ii)
Whether you will obtain the analysis by performing sampling and analysis or by other methods, such as using analytical information obtained from others or using other published or documented data or information;
(iii)
How you will use the analysis to document compliance with applicable feedrate limits (e.g., if you blend hazardous wastes and obtain analyses of the wastes prior to blending but not of the blended, as-fired, waste, the plan must describe how you will determine the pertinent parameters of the blended waste);
(iv)
The test methods which you will use to obtain the analyses;
(v)
The sampling method which you will use to obtain a representative sample of each feedstream to be analyzed using sampling methods described in appendix IX to part 266 of this chapter, or an equivalent method; and
(vi)
The frequency with which you will review or repeat the initial analysis of the feedstream to ensure that the analysis is accurate and up to date.
(3)
Review and approval of analysis plan. You must submit the feedstream analysis plan to the Administrator for review and approval, if requested.
(4)
Compliance with feedrate limits. To comply with the applicable feedrate limits of this section, you must monitor and record feedrates as follows:
(i)
Determine and record the value of the parameter for each feedstream by sampling and analysis or other method;
(ii)
Determine and record the mass or volume flowrate of each feedstream by a CMS. If you determine flowrate of a feedstream by volume, you must determine and record the density of the feedstream by sampling and analysis (unless you report the constituent concentration in units of weight per unit volume (e.g., mg/l)); and
(iii)
Calculate and record the mass feedrate of the parameter per unit time.
(5)
Waiver of monitoring of constituents in certain feedstreams. You are not required to monitor levels of metals, chlorine, or fluorine in the following feedstreams to document compliance with the feedrate limits or work practice standards under this section provided that you document in the comprehensive performance test plan the expected levels of the constituent in the feedstream and account for those assumed feedrate levels in documenting compliance with feedrate limits or work practice standards: natural gas, process air, and feedstreams from vapor recovery systems.
(d)
Performance evaluations.
(1)
The requirements of § 63.8(d) (Quality control program) and (e) (Performance evaluation of continuous monitoring systems) apply, except that you must conduct performance evaluations of components of the CMS under the frequency and procedures (for example, submittal of performance evaluation test plan for review and approval) applicable to performance tests as provided by § 63.1207.
(2)
You must comply with the quality assurance procedures for CEMS prescribed in appendix A to this subpart.
(e)
Conduct of monitoring. The provisions of § 63.8(b) apply.
(f)
Operation and maintenance of continuous monitoring systems. The provisions of § 63.8(c) apply except:
(1)
Section 63.8(c)(3). The requirements of § 63.1211(c), that require CMS to be installed, calibrated, and operational on the compliance date, shall be complied with instead of § 63.8(c)(3);
(2)
Section 63.8(c)(4)(ii). The performance specifications for carbon monoxide, hydrocarbon, and oxygen CEMS in appendix B to part 60 of this chapter that require detectors to measure the sample concentration at least once every 15 seconds for calculating an average emission rate once every 60 seconds shall be complied with instead of § 63.8(c)(4)(ii); and
(3)
Section 63.8(c)(4)(i), (c)(5), and (c)(7)(i)(C) pertaining to COMS apply only to owners and operators of hazardous waste burning cement kilns.
(g)
Alternative monitoring requirements other than continuous emissions monitoring systems (CEMS)—
(1)
Requests to use alternatives to operating parameter monitoring requirements.
(i)
You may submit an application to the Administrator under this paragraph for approval of alternative operating parameter monitoring requirements to document compliance with the emission standards of this subpart. For requests to use additional CEMS, however, you must use paragraph (a)(5) of this section and § 63.8(f). Alternative requests to operating parameter monitoring requirements that include unproven monitoring methods may not be made under this paragraph and must be made under § 63.8(f).
(ii)
You may submit an application to waive an operating parameter limit specified in this section based on documentation that neither that operating parameter limit nor an alternative operating parameter limit is needed to ensure compliance with the emission standards of this subpart.
(iii)
You must comply with the following procedures for applications submitted under paragraphs (g)(1)(i) and (ii) of this section:
(A)
Timing of the application. You must submit the application to the Administrator not later than with the comprehensive performance test plan.
(B)
Content of the application. You must include in the application:

(1) Data or information justifying your request for an alternative monitoring requirement (or for a waiver of an operating parameter limit), such as the technical or economic infeasibility or the impracticality of using the required approach;

(2) A description of the proposed alternative monitoring requirement, including the operating parameter to be monitored, the monitoring approach/technique (e.g., type of detector, monitoring location), the averaging period for the limit, and how the limit is to be calculated; and

(3) Data or information documenting that the alternative monitoring requirement would provide equivalent or better assurance of compliance with the relevant emission standard, or that it is the monitoring requirement that best assures compliance with the standard and that is technically and economically practicable.

(C)
Approval of request to use an alternative monitoring requirement or waive an operating parameter limit. The Administrator will notify you of approval or intention to deny approval of the request within 90 calendar days after receipt of the original request and within 60 calendar days after receipt of any supplementary information that you submit. The Administrator will not approve an alternative monitoring request unless the alternative monitoring requirement provides equivalent or better assurance of compliance with the relevant emission standard, or is the monitoring requirement that best assures compliance with the standard and that is technically and economically practicable. Before disapproving any request, the Administrator will notify you of the Administrator's intention to disapprove the request together with:

(1) Notice of the information and findings on which the intended disapproval is based; and

(2) Notice of opportunity for you to present additional information to the Administrator before final action on the request. At the time the Administrator notifies you of intention to disapprove the request, the Administrator will specify how much time you will have after being notified of the intended disapproval to submit the additional information.

(D)
Responsibility of owners and operators. You are responsible for ensuring that you submit any supplementary and additional information supporting your application in a timely manner to enable the Administrator to consider your application during review of the comprehensive performance test plan. Neither your submittal of an application, nor the Administrator's failure to approve or disapprove the application, relieves you of the responsibility to comply with the provisions of this subpart.
(iv)
Dual standards that incorporate the interim standards for HAP metals—
(A)
Semivolatile and low volatile metals. You may petition the Administrator to waive a feedrate operating parameter limit under paragraph (n)(2) of this section for either the emission standards expressed in a thermal emissions format or the interim standards based on documentation that the feedrate operating parameter limit is not needed to ensure compliance with the relevant standard on a continuous basis.
(B)
Mercury. You may petition the Administrator to waive a feedrate operating parameter limit under paragraph (l)(1) of this section for either the feed concentration standard under § 63.1220(a)(2)(i) and (b)(2)(i) or the interim standards based on documentation that the feedrate operating parameter limit is not needed to ensure compliance with the relevant standard on a continuous basis.
(2)
Administrator's discretion to specify additional or alternative requirements. The Administrator may determine on a case-by-case basis at any time (e.g., during review of the comprehensive performance test plan, during compliance certification review) that you may need to limit additional or alternative operating parameters (e.g., opacity in addition to or in lieu of operating parameter limits on the particulate matter control device) or that alternative approaches to establish limits on operating parameters may be necessary to document compliance with the emission standards of this subpart.
(h)
Reduction of monitoring data. The provisions of § 63.8(g) apply.
(i)
When an operating parameter is applicable to multiple standards. Paragraphs (j) through (p) of this section require you to establish limits on operating parameters based on comprehensive performance testing to ensure you maintain compliance with the emission standards of this subpart. For several parameters, you must establish a limit for the parameter to ensure compliance with more than one emission standard. An example is a limit on minimum combustion chamber temperature to ensure compliance with both the DRE standard of paragraph (j) of this section and the dioxin/furan standard of paragraph (k) of this section. If the performance tests for such standards are not performed simultaneously, the most stringent limit for a parameter derived from independent performance tests applies.
(j)
DRE. To remain in compliance with the destruction and removal efficiency (DRE) standard, you must establish operating limits during the comprehensive performance test (or during a previous DRE test under provisions of § 63.1206(b)(7)) for the following parameters, unless the limits are based on manufacturer specifications. You must comply with those limits at all times that hazardous waste remains in the combustion chamber (i.e., the hazardous waste residence time has not transpired since the hazardous waste feed cutoff system was activated). When hazardous waste does not remain in the combustion chamber, you are not required to comply with the operating limits pursuant to paragraph (j) of this section:
(1)
Minimum combustion chamber temperature.
(i)
You must measure the temperature of each combustion chamber at a location that best represents, as practicable, the bulk gas temperature in the combustion zone. You must document the temperature measurement location in the test plan you submit under § 63.1207(e);
(ii)
You must establish a minimum hourly rolling average limit as the average of the test run averages;
(2)
Maximum flue gas flowrate or production rate.
(i)
As an indicator of gas residence time in the control device, you must establish and comply with a limit on the maximum flue gas flowrate, the maximum production rate, or another parameter that you document in the site-specific test plan as an appropriate surrogate for gas residence time, as the average of the maximum hourly rolling averages for each run.
(ii)
You must comply with this limit on a hourly rolling average basis;
(3)
Maximum hazardous waste feedrate.
(i)
You must establish limits on the maximum pumpable and total (i.e., pumpable and nonpumpable) hazardous waste feedrate for each location where hazardous waste is fed.
(ii)
You must establish the limits as the average of the maximum hourly rolling averages for each run.
(iii)
You must comply with the feedrate limit(s) on a hourly rolling average basis;
(4)
Operation of waste firing system. You must specify operating parameters and limits to ensure that good operation of each hazardous waste firing system is maintained.
(k)
Dioxins and furans. You must comply with the dioxin and furans emission standard by establishing and complying with the following operating parameter limits. You must base the limits on operations during the comprehensive performance test, unless the limits are based on manufacturer specifications.
(1)
Gas temperature at the inlet to a dry particulate matter control device.
(i)
For sources other than a lightweight aggregate kiln, if the combustor is equipped with an electrostatic precipitator, baghouse (fabric filter), or other dry emissions control device where particulate matter is suspended in contact with combustion gas, you must establish a limit on the maximum temperature of the gas at the inlet to the device on an hourly rolling average. You must establish the hourly rolling average limit as the average of the test run averages.
(ii)
For hazardous waste burning lightweight aggregate kilns, you must establish a limit on the maximum temperature of the gas at the exit of the (last) combustion chamber (or exit of any waste heat recovery system) on an hourly rolling average. The limit must be established as the average of the test run averages;
(2)
Minimum combustion chamber temperature.
(i)
For sources other than cement kilns, you must measure the temperature of each combustion chamber at a location that best represents, as practicable, the bulk gas temperature in the combustion zone. You must document the temperature measurement location in the test plan you submit under § 63.1207(e) and (f);
(ii)
You must establish a minimum hourly rolling average limit as the average of the test run averages.
(3)
Maximum flue gas flowrate or production rate.
(i)
As an indicator of gas residence time in the control device, you must establish and comply with a limit on the maximum flue gas flowrate, the maximum production rate, or another parameter that you document in the site-specific test plan as an appropriate surrogate for gas residence time, as the average of the maximum hourly rolling averages for each run.
(ii)
You must comply with this limit on a hourly rolling average basis;
(4)
Maximum hazardous waste feedrate.
(i)
You must establish limits on the maximum pumpable and total (pumpable and nonpumpable) hazardous waste feedrate for each location where waste is fed.
(ii)
You must establish the limits as the average of the maximum hourly rolling averages for each run.
(iii)
You must comply with the feedrate limit(s) on a hourly rolling average basis;
(5)
Particulate matter operating limit. If your combustor is equipped with an activated carbon injection system, you must establish operating parameter limits on the particulate matter control device as specified by paragraph (m)(1) of this section;
(6)
Activated carbon injection parameter limits. If your combustor is equipped with an activated carbon injection system:
(i)
Carbon feedrate. You must establish a limit on minimum carbon injection rate on an hourly rolling average calculated as the average of the test run averages. If your carbon injection system injects carbon at more than one location, you must establish a carbon feedrate limit for each location.
(ii)
Carrier fluid. You must establish a limit on minimum carrier fluid (gas or liquid) flowrate or pressure drop as an hourly rolling average based on the manufacturer's specifications. You must document the specifications in the test plan you submit under § 63.1207(e) and (f);
(iii)
Carbon specification.
(A)
You must specify and use the brand (i.e., manufacturer) and type of carbon used during the comprehensive performance test until a subsequent comprehensive performance test is conducted, unless you document in the site-specific performance test plan required under § 63.1207(e) and (f) key parameters that affect adsorption and establish limits on those parameters based on the carbon used in the performance test.
(B)
You may substitute at any time a different brand or type of carbon provided that the replacement has equivalent or improved properties compared to the carbon used in the performance test and conforms to the key sorbent parameters you identify under paragraph (k)(6)(iii)(A) of this section. You must include in the operating record documentation that the substitute carbon will provide the same level of control as the original carbon.
(7)
Carbon bed parameter limits. If your combustor is equipped with a carbon bed system:
(i)
Monitoring bed life. You must:
(A)
Monitor performance of the carbon bed consistent with manufacturer's specifications and recommendations to ensure the carbon bed (or bed segment for sources with multiple segments) has not reached the end of its useful life to minimize dioxin/furan and mercury emissions at least to the levels required by the emission standards;
(B)
Document the monitoring procedures in the operation and maintenance plan;
(C)
Record results of the performance monitoring in the operating record; and
(D)
Replace the bed or bed segment before it has reached the end of its useful life to minimize dioxin/furan and mercury emissions at least to the levels required by the emission standards.
(ii)
Carbon specification.
(A)
You must specify and use the brand (i.e., manufacturer) and type of carbon used during the comprehensive performance test until a subsequent comprehensive performance test is conducted, unless you document in the site-specific performance test plan required under § 63.1207(e) and (f) key parameters that affect adsorption and establish limits on those parameters based on the carbon used in the performance test.
(B)
You may substitute at any time a different brand or type of carbon provided that the replacement has equivalent or improved properties compared to the carbon used in the performance test. You must include in the operating record documentation that the substitute carbon will provide an equivalent or improved level of control as the original carbon.
(iii)
Maximum temperature. You must measure the temperature of the carbon bed at either the bed inlet or exit and you must establish a maximum temperature limit on an hourly rolling average as the average of the test run averages.
(8)
Catalytic oxidizer parameter limits. If your combustor is equipped with a catalytic oxidizer, you must establish limits on the following parameters:
(i)
Minimum flue gas temperature at the entrance of the catalyst. You must establish a limit on minimum flue gas temperature at the entrance of the catalyst on an hourly rolling average as the average of the test run averages.
(ii)
Maximum time in-use. You must replace a catalytic oxidizer with a new catalytic oxidizer when it has reached the maximum service time specified by the manufacturer.
(iii)
Catalyst replacement specifications. When you replace a catalyst with a new one, the new catalyst must be equivalent to or better than the one used during the previous comprehensive test, as measured by:
(A)
Catalytic metal loading for each metal;
(B)
Space time, expressed in the units s−1, the maximum rated volumetric flow of combustion gas through the catalyst divided by the volume of the catalyst; and
(C)
Substrate construction, including materials of construction, washcoat type, and pore density.
(iv)
Maximum flue gas temperature. You must establish a maximum flue gas temperature limit at the entrance of the catalyst as an hourly rolling average, based on manufacturer's specifications.
(9)
Inhibitor feedrate parameter limits. If you feed a dioxin/furan inhibitor into the combustion system, you must establish limits for the following parameters:
(i)
Minimum inhibitor feedrate. You must establish a limit on minimum inhibitor feedrate on an hourly rolling average as the average of the test run averages.
(ii)
Inhibitor specifications.
(A)
You must specify and use the brand (i.e., manufacturer) and type of inhibitor used during the comprehensive performance test until a subsequent comprehensive performance test is conducted, unless you document in the site-specific performance test plan required under § 63.1207(e) and (f) key parameters that affect the effectiveness of the inhibitor and establish limits on those parameters based on the inhibitor used in the performance test.
(B)
You may substitute at any time a different brand or type of inhibitor provided that the replacement has equivalent or improved properties compared to the inhibitor used in the performance test and conforms to the key parameters you identify under paragraph (k)(9)(ii)(A) of this section. You must include in the operating record documentation that the substitute inhibitor will provide the same level of control as the original inhibitor.
(l)
Mercury. You must comply with the mercury emission standard by establishing and complying with the following operating parameter limits. You must base the limits on operations during the comprehensive performance test, unless the limits are based on manufacturer specifications.
(1)
Feedrate of mercury.
(i)
For incinerators and solid fuel boilers, when complying with the mercury emission standards under §§ 63.1203, 63.1216 and 63.1219, you must establish a 12-hour rolling average limit for the total feedrate of mercury in all feedstreams as the average of the test run averages.
(ii)
For liquid fuel boilers, when complying with the mercury emission standards of § 63.1217, you must establish a rolling average limit for the mercury feedrate as follows on an averaging period not to exceed an annual rolling average:
(A)
You must calculate a mercury system removal efficiency for each test run and calculate the average system removal efficiency of the test run averages. If emissions exceed the mercury emission standard during the comprehensive performance test, it is not a violation because the averaging period for the mercury emission standard is (not-to-exceed) one year and compliance is based on compliance with the mercury feedrate limit with an averaging period not-to-exceed one year.
(B)
If you burn hazardous waste with a heating value of 10,000 Btu/lb or greater, you must calculate the mercury feedrate limit as follows:

(1) The mercury feedrate limit is the emission standard divided by [1−system removal efficiency].

(2) The mercury feedrate limit is a hazardous waste thermal concentration limit expressed as pounds of mercury in hazardous waste feedstreams per million Btu of hazardous waste fired.

(3) You must comply with the hazardous waste mercury thermal concentration limit by determining the feedrate of mercury in all hazardous waste feedstreams (lb/hr) at least once a minute and the hazardous waste thermal feedrate (MM Btu/hr) at least once a minute to calculate a 60-minute average thermal emission concentration as [hazardous waste mercury feedrate (lb/hr)/hazardous waste thermal feedrate (MM Btu/hr)].

(4) You must calculate a rolling average hazardous waste mercury thermal concentration that is updated each hour.

(5) If you select an averaging period for the feedrate limit that is greater than a 12-hour rolling average, you must calculate the initial rolling average as though you had selected a 12-hour rolling average, as provided by paragraph (b)(5)(i) of this section. Thereafter, you must calculate rolling averages using either one-minute or one-hour updates. Hourly updates shall be calculated using the average of the one-minute average data for the preceding hour. For the period beginning with initial operation under this standard until the source has operated for the full averaging period that you select, the average feedrate shall be based only on actual operation under this standard.

(C)
If you burn hazardous waste with a heating value of less than 10,000 Btu/lb, you must calculate the mercury feedrate limit as follows:

(1) You must calculate the mercury feedrate limit as the mercury emission standard divided by [1−System Removal Efficiency].

(2) The feedrate limit is expressed as a mass concentration per unit volume of stack gas (µg/dscm) and is converted to a mass feedrate (lb/hr) by multiplying it by the average stack gas flowrate of the test run averages.

(3) You must comply with the feedrate limit by determining the mercury feedrate (lb/hr) at least once a minute to calculate a 60-minute average feedrate.

(4) You must update the rolling average feedrate each hour with this 60-minute feedrate measurement.

(5) If you select an averaging period for the feedrate limit that is greater than a 12-hour rolling average, you must calculate the initial rolling average as though you had selected a 12-hour rolling average, as provided by paragraph (b)(5)(i) of this section. Thereafter, you must calculate rolling averages using either one-minute or one-hour updates. Hourly updates shall be calculated using the average of the one-minute average data for the preceding hour. For the period beginning with initial operation under this standard until the source has operated for the full averaging period that you select, the average feedrate shall be based only on actual operation under this standard.

(D)
If your boiler is equipped with a wet scrubber, you must comply with the following unless you document in the performance test plan that you do not feed chlorine at rates that may substantially affect the system removal efficiency of mercury for purposes of establishing a mercury feedrate limit based on the system removal efficiency during the test:

(1) Scrubber blowdown must be minimized during a pretest conditioning period and during the performance test:

(2) Scrubber water must be preconditioned so that mercury in the water is at equilibrium with stack gas at the mercury feedrate level of the performance test; and

(3) You must establish an operating limit on minimum pH of scrubber water as the average of the test run averages and comply with the limit on an hourly rolling average.

(iii)
For cement kilns—
(A)
When complying with the emission standards under § 63.1220(a)(2)(i) and (b)(2)(i), you must:

(1) Comply with the mercury hazardous waste feed concentration operating requirement on a twelve-hour rolling average;

(2) Monitor and record in the operating record the as-fired mercury concentration in the hazardous waste (or the weighted-average mercury concentration for multiple hazardous waste feedstreams);

(3) Initiate an automatic waste feed cutoff that immediately and automatically cuts off the hazardous waste feed when the as-fired mercury concentration operating requirement is exceeded;

(B)
When complying with the emission standards under §§ 63.1204 and 63.1220(a)(2)(ii)(A) and (b)(2)(ii)(A), you must establish a 12-hour rolling average limit for the feedrate of mercury in all feedstreams as the average of the test run averages;
(C)
Except as provided by paragraph (l)(1)(iii)(D) of this section, when complying with the hazardous waste maximum theoretical emission concentration (MTEC) under § 63.1220(a)(2)(ii)(B) and (b)(2)(ii)(B), you must:

(1) Comply with the MTEC operating requirement on a twelve-hour rolling average;

(2) Monitor and record the feedrate of mercury for each hazardous waste feedstream according to § 63.1209(c);

(3) Monitor with a CMS and record in the operating record the gas flowrate (either directly or by monitoring a surrogate parameter that you have correlated to gas flowrate);

(4) Continuously calculate and record in the operating record a MTEC assuming mercury from all hazardous waste feedstreams is emitted;

(5) Initiate an automatic waste feed cutoff that immediately and automatically cuts off the hazardous waste feed when the MTEC operating requirement is exceeded;

(D)
In lieu of complying with paragraph (l)(1)(iii)(C) of this section, you may— (1) Identify in the Notification of Compliance a minimum gas flowrate limit and a maximum feedrate limit of mercury from all hazardous waste feedstreams that ensures the MTEC calculated in paragraph (l)(1)(iii)(C)(4) of this section is below the operating requirement under paragraphs § 63.1220(a)(2)(ii)(B) and (b)(2)(ii)(B); and

(2) Initiate an automatic waste feed cutoff that immediately and automatically cuts off the hazardous waste feed when either the gas flowrate or mercury feedrate exceeds the limits identified in paragraph (l)(1)(iii)(D)(1) of this section.

(iv)
For lightweight aggregate kilns—
(A)
When complying with the emission standards under §§ 63.1205, 63.1221(a)(2)(i) and (b)(2)(i), you must establish a 12-hour rolling average limit for the total feedrate of mercury in all feedstreams as the average of the test run averages;
(B)
Except as provided by paragraph (l)(1)(iv)(C) of this section, when complying with the hazardous waste feedrate corresponding to a maximum theoretical emission concentration (MTEC) under § 63.1221(a)(2)(ii) and (b)(2)(ii), you must:

(1) Comply with the MTEC operating requirement on a twelve-hour rolling average;

(2) Monitor and record the feedrate of mercury for each hazardous waste feedstream according to § 63.1209(c);

(3) Monitor with a CMS and record in the operating record the gas flowrate (either directly or by monitoring a surrogate parameter that you have correlated to gas flowrate);

(4) Continuously calculate and record in the operating record a MTEC assuming mercury from all hazardous waste feedstreams is emitted;

(5) Initiate an automatic waste feed cutoff that immediately and automatically cuts off the hazardous waste feed when the MTEC operating requirement is exceeded;

(C)
In lieu of complying with paragraph (l)(1)(iv)(B) of this section, you may— (1) Identify in the Notification of Compliance a minimum gas flowrate limit and a maximum feedrate limit of mercury from all hazardous waste feedstreams that ensures the MTEC calculated in paragraph (l)(1)(iv)(B)(4) of this section is below the operating requirement under paragraphs § 63.1221(a)(2)(ii) and (b)(2)(ii); and

(2) Initiate an automatic waste feed cutoff that immediately and automatically cuts off the hazardous waste feed when either the gas flowrate or mercury feedrate exceeds the limits identified in paragraph (l)(1)(iv)(C)(1) of this section.

(v)
Extrapolation of feedrate levels. In lieu of establishing mercury feedrate limits as specified in paragraphs (l)(1)(i) through (iv) of this section, you may request as part of the performance test plan under §§ 63.7(b) and (c) and 63.1207(e) and (f) to use the mercury feedrates and associated emission rates during the comprehensive performance test to extrapolate to higher allowable feedrate limits and emission rates. The extrapolation methodology will be reviewed and approved, as warranted, by the Administrator. The review will consider in particular whether:
(A)
Performance test metal feedrates are appropriate (i.e., whether feedrates are at least at normal levels; depending on the heterogeneity of the waste, whether some level of spiking would be appropriate; and whether the physical form and species of spiked material is appropriate); and
(B)
Whether the extrapolated feedrates you request are warranted considering historical metal feedrate data.
(2)
Wet scrubber. If your combustor is equipped with a wet scrubber, you must establish operating parameter limits prescribed by paragraph (o)(3) of this section, except for paragraph (o)(3)(iv).
(3)
Activated carbon injection. If your combustor is equipped with an activated carbon injection system, you must establish operating parameter limits prescribed by paragraphs (k)(5) and (6) of this section.
(4)
Activated carbon bed. If your combustor is equipped with an activated carbon bed system, you must comply with the requirements of paragraph (k)(7) of this section to assure compliance with the mercury emission standard.
(m)
Particulate matter. You must comply with the particulate matter emission standard by establishing and complying with the following operating parameter limits. You must base the limits on operations during the comprehensive performance test, unless the limits are based on manufacturer specifications.
(1)
Control device operating parameter limits (OPLs)—
(i)
Wet scrubbers. For sources equipped with wet scrubbers, including ionizing wet scrubbers, high energy wet scrubbers such as venturi, hydrosonic, collision, or free jet wet scrubbers, and low energy wet scrubbers such as spray towers, packed beds, or tray towers, you must establish limits on the following parameters:
(A)
For high energy scrubbers only, minimum pressure drop across the wet scrubber on an hourly rolling average, established as the average of the test run averages;
(B)
For all wet scrubbers— (1) To ensure that the solids content of the scrubber liquid does not exceed levels during the performance test, you must either:

(i) Establish a limit on solids content of the scrubber liquid using a CMS or by manual sampling and analysis. If you elect to monitor solids content manually, you must sample and analyze the scrubber liquid hourly unless you support an alternative monitoring frequency in the performance test plan that you submit for review and approval; or

(ii) Establish a minimum blowdown rate using a CMS and either a minimum scrubber tank volume or liquid level using a CMS.

(2) For maximum solids content monitored with a CMS, you must establish a limit on a twelve-hour rolling average as the average of the test run averages.

(3) For maximum solids content measured manually, you must establish an hourly limit, as measured at least once per hour, unless you support an alternative monitoring frequency in the performance test plan that you submit for review and approval. You must establish the maximum hourly limit as the average of the manual measurement averages for each run.

(4) For minimum blowdown rate and either a minimum scrubber tank volume or liquid level using a CMS, you must establish a limit on an hourly rolling average as the average of the test run averages.

(C)
For high energy wet scrubbers only, you must establish limits on either the minimum liquid to gas ratio or the minimum scrubber water flowrate and maximum flue gas flowrate on an hourly rolling average. If you establish limits on maximum flue gas flowrate under this paragraph, you need not establish a limit on maximum flue gas flowrate under paragraph (m)(2) of this section. You must establish these hourly rolling average limits as the average of the test run averages; and
(ii)
-(iii) [Reserved]
(iv)
Other particulate matter control devices. For each particulate matter control device that is not a fabric filter or high energy wet scrubber, or is not an electrostatic precipitator or ionizing wet scrubber for which you elect to monitor particulate matter loadings under § 63.1206(c)(9) for process control, you must ensure that the control device is properly operated and maintained as required by § 63.1206(c)(7) and by monitoring the operation of the control device as follows:
(A)
During each comprehensive performance test conducted to demonstrate compliance with the particulate matter emissions standard, you must establish a range of operating values for the control device that is a representative and reliable indicator that the control device is operating within the same range of conditions as during the performance test. You must establish this range of operating values as follows:

(1) You must select a set of operating parameters appropriate for the control device design that you determine to be a representative and reliable indicator of the control device performance.

(2) You must measure and record values for each of the selected operating parameters during each test run of the performance test. A value for each selected parameter must be recorded using a continuous monitor.

(3) For each selected operating parameter measured in accordance with the requirements of paragraph (m)(1)(iv)(A)(1) of this section, you must establish a minimum operating parameter limit or a maximum operating parameter limit, as appropriate for the parameter, to define the operating limits within which the control device can operate and still continuously achieve the same operating conditions as during the performance test.

(4) You must prepare written documentation to support the operating parameter limits established for the control device and you must include this documentation in the performance test plan that you submit for review and approval. This documentation must include a description for each selected parameter and the operating range and monitoring frequency required to ensure the control device is being properly operated and maintained.

(B)
You must install, calibrate, operate, and maintain a monitoring device equipped with a recorder to measure the values for each operating parameter selected in accordance with the requirements of paragraph (m)(1)(iv)(A)(1) of this section. You must install, calibrate, and maintain the monitoring equipment in accordance with the equipment manufacturer's specifications. The recorder must record the detector responses at least every 60 seconds, as required in the definition of continuous monitor.
(C)
You must regularly inspect the data recorded by the operating parameter monitoring system at a sufficient frequency to ensure the control device is operating properly. An excursion is determined to have occurred any time that the actual value of a selected operating parameter is less than the minimum operating limit (or, if applicable, greater than the maximum operating limit) established for the parameter in accordance with the requirements of paragraph (m)(1)(iv)(A)(3) of this section.
(D)
Operating parameters selected in accordance with paragraph (m)(1)(iv) of this section may be based on manufacturer specifications provided you support the use of manufacturer specifications in the performance test plan that you submit for review and approval.
(2)
Maximum flue gas flowrate or production rate.
(i)
As an indicator of gas residence time in the control device, you must establish a limit on the maximum flue gas flowrate, the maximum production rate, or another parameter that you document in the site-specific test plan as an appropriate surrogate for gas residence time, as the average of the maximum hourly rolling averages for each run.
(ii)
You must comply with this limit on a hourly rolling average basis;
(3)
Maximum ash feedrate. Owners and operators of hazardous waste incinerators, solid fuel boilers, and liquid fuel boilers must establish a maximum ash feedrate limit as a 12-hour rolling average based on the average of the test run averages. This requirement is waived, however, if you comply with the particulate matter detection system requirements under § 63.1206(c)(9).
(n)
Semivolatile metals and low volatility metals. You must comply with the semivolatile metal (cadmium and lead) and low volatile metal (arsenic, beryllium, and chromium) emission standards by establishing and complying with the following operating parameter limits. You must base the limits on operations during the comprehensive performance test, unless the limits are based on manufacturer specifications.
(1)
Maximum inlet temperature to dry particulate matter air pollution control device. You must establish a limit on the maximum inlet temperature to the primary dry metals emissions control device (e.g., electrostatic precipitator, baghouse) on an hourly rolling average basis as the average of the test run averages.
(2)
Maximum feedrate of semivolatile and low volatile metals—
(i)
General. You must establish feedrate limits for semivolatile metals (cadmium and lead) and low volatile metals (arsenic, beryllium, and chromium) as follows, except as provided by paragraph (n)(2)(vii) of this section.
(ii)
For incinerators, cement kilns, and lightweight aggregate kilns, when complying with the emission standards under §§ 63.1203 through 63.1205 and 63.1219, and for solid fuel boilers when complying with the emission standards under § 63.1216, you must establish 12-hour rolling average limits for the total feedrate of semivolatile and low volatile metals in all feedstreams as the average of the test run averages.
(iii)
Cement kilns under— § 63.1220. (A) When complying with the emission standards under § 63.1220(a)(3)(i), (a)(4)(i), (b)(3)(i), and (b)(4)(i), you must establish 12-hour rolling average feedrate limits for semivolatile and low volatile metals as the thermal concentration of semivolatile metals or low volatile metals in all hazardous waste feedstreams. You must calculate hazardous waste thermal concentrations for semivolatile metals and low volatile metals for each run as the total mass feedrate of semivolatile metals or low volatile metals for all hazardous waste feedstreams divided by the total heat input rate for all hazardous waste feedstreams. The 12-hour rolling average feedrate limits for semivolatile metals and low volatile metals are the average of the test run averages, calculated on a thermal concentration basis, for all hazardous waste feeds.
(B)
When complying with the emission standards under § 63.1220(a)(3)(ii), (a)(4)(ii), (b)(3)(ii), and (b)(4)(ii), you must establish 12-hour rolling average limits for the total feedrate of semivolatile and low volatile metals in all feedstreams as the average of the test run averages.
(iv)
Lightweight aggregate kilns under— § 63.1221. (A) When complying with the emission standards under § 63.1221(a)(3)(i), (a)(4)(i), (b)(3)(i), and (b)(4)(i), you must establish 12-hour rolling average feedrate limits for semivolatile and low volatile metals as the thermal concentration of semivolatile metals or low volatile metals in all hazardous waste feedstreams as specified in paragraphs (n)(2)(iii)(A) of this section.
(B)
When complying with the emission standards under § 63.1221(a)(3)(ii), (a)(4)(ii), (b)(3)(ii), and (b)(4)(ii), you must establish 12-hour rolling average limits for the total feedrate of semivolatile and low volatile metals in all feedstreams as the average of the test run averages.
(v)
Liquid fuel boilers under— § 63.1217—(A) Semivolatile metals. You must establish a rolling average limit for the semivolatile metal feedrate as follows on an averaging period not to exceed an annual rolling average.

(1) System removal efficiency. You must calculate a semivolatile metal system removal efficiency for each test run and calculate the average system removal efficiency of the test run averages. If emissions exceed the semivolatile metal emission standard during the comprehensive performance test, it is not a violation because the averaging period for the semivolatile metal emission standard is one year and compliance is based on compliance with the semivolatile metal feedrate limit that has an averaging period not to exceed an annual rolling average.

(2) Boilers that feed hazardous waste with a heating value of 10,000 Btu/lb or greater. You must calculate the semivolatile metal feedrate limit as the semivolatile metal emission standard divided by [1−System Removal Efficiency].

(i) The feedrate limit is a hazardous waste thermal concentration limit expressed as pounds of semivolatile metals in all hazardous waste feedstreams per million Btu of hazardous waste fed to the boiler.

(ii) You must comply with the hazardous waste semivolatile metal thermal concentration limit by determining the feedrate of semivolatile metal in all hazardous waste feedstreams (lb/hr) and the hazardous waste thermal feedrate (MM Btu/hr) at least once a minute to calculate a 60-minute average thermal emission concentration as [hazardous waste semivolatile metal feedrate (lb/hr)/hazardous waste thermal feedrate (MM Btu/hr)].

(iii) You must calculate a rolling average hazardous waste semivolatile metal thermal concentration that is updated each hour.

(iv) If you select an averaging period for the feedrate limit that is greater than a 12-hour rolling average, you must calculate the initial rolling average as though you had selected a 12-hour rolling average, as provided by paragraph (b)(5)(i) of this section. Thereafter, you must calculate rolling averages using either one-minute or one-hour updates. Hourly updates shall be calculated using the average of the one-minute average data for the preceding hour. For the period beginning with initial operation under this standard until the source has operated for the full averaging period that you select, the average feedrate shall be based only on actual operation under this standard.

(3) Boilers that feed hazardous waste with a heating value less than 10,000 Btu/lb. (i) You must calculate the semivolatile metal feedrate limit as the semivolatile metal emission standard divided by [1−System Removal Efficiency].

(ii) The feedrate limit is expressed as a mass concentration per unit volume of stack gas (µg/dscm) and is converted to a mass feedrate (lb/hr) by multiplying it by the average stack gas flowrate (dscm/hr) of the test run averages.

(iii) You must comply with the feedrate limit by determining the semivolatile metal feedrate (lb/hr) at least once a minute to calculate a 60-minute average feedrate.

(iv) You must update the rolling average feedrate each hour with this 60-minute feedrate measurement.

(v) If you select an averaging period for the feedrate limit that is greater than a 12-hour rolling average, you must calculate the initial rolling average as though you had selected a 12-hour rolling average, as provided by paragraph (b)(5)(i) of this section. Thereafter, you must calculate rolling averages using either one-minute or one-hour updates. Hourly updates shall be calculated using the average of the one-minute average data for the preceding hour. For the period beginning with initial operation under this standard until the source has operated for the full averaging period that you select, the average feedrate shall be based only on actual operation under this standard.

(B)
Chromium—
(1)
Boilers that feed hazardous waste with a heating value of 10,000 Btu/lb or greater. (i) The 12-hour rolling average feedrate limit is a hazardous waste thermal concentration limit expressed as pounds of chromium in all hazardous waste feedstreams per million Btu of hazardous waste fed to the boiler. You must establish the 12-hour rolling average feedrate limit as the average of the test run averages.

(ii) You must comply with the hazardous waste chromium thermal concentration limit by determining the feedrate of chromium in all hazardous waste feedstreams (lb/hr) and the hazardous waste thermal feedrate (MMBtu/hr) at least once each minute as [hazardous waste chromium feedrate (lb/hr)/hazardous waste thermal feedrate (MMBtu/hr)].

(2) Boilers that feed hazardous waste with a heating value less than 10,000 Btu/lb. You must establish a 12-hour rolling average limit for the total feedrate (lb/hr) of chromium in all feedstreams as the average of the test run averages.

(vi)
LVM limits for pumpable wastes. You must establish separate feedrate limits for low volatile metals in pumpable feedstreams using the procedures prescribed above for total low volatile metals. Dual feedrate limits for both pumpable and total feedstreams are not required, however, if you base the total feedrate limit solely on the feedrate of pumpable feedstreams.
(vii)
Extrapolation of feedrate levels. In lieu of establishing feedrate limits as specified in paragraphs (n)(2)(ii) through (vi) of this section, you may request as part of the performance test plan under §§ 63.7(b) and (c) and 63.1207(e) and (f) to use the semivolatile metal and low volatile metal feedrates and associated emission rates during the comprehensive performance test to extrapolate to higher allowable feedrate limits and emission rates. The extrapolation methodology will be reviewed and approved, as warranted, by the Administrator. The review will consider in particular whether:
(A)
Performance test metal feedrates are appropriate (i.e., whether feedrates are at least at normal levels; depending on the heterogeneity of the waste, whether some level of spiking would be appropriate; and whether the physical form and species of spiked material is appropriate); and
(B)
Whether the extrapolated feedrates you request are warranted considering historical metal feedrate data.
(3)
Control device operating parameter limits (OPLs). You must establish operating parameter limits on the particulate matter control device as specified by paragraph (m)(1) of this section;
(4)
Maximum total chlorine and chloride feedrate. You must establish a 12-hour rolling average limit for the feedrate of total chlorine and chloride in all feedstreams as the average of the test run averages.
(5)
Maximum flue gas flowrate or production rate.
(i)
As an indicator of gas residence time in the control device, you must establish a limit on the maximum flue gas flowrate, the maximum production rate, or another parameter that you document in the site-specific test plan as an appropriate surrogate for gas residence time, as the average of the maximum hourly rolling averages for each run.
(ii)
You must comply with this limit on a hourly rolling average basis.
(o)
Hydrogen chloride and chlorine gas. You must comply with the hydrogen chloride and chlorine gas emission standard by establishing and complying with the following operating parameter limits. You must base the limits on operations during the comprehensive performance test, unless the limits are based on manufacturer specifications.
(1)
Feedrate of total chlorine and chloride—
(i)
Incinerators, cement kilns, lightweight aggregate kilns, solid fuel boilers, and hydrochloric acid production furnaces. You must establish a 12-hour rolling average limit for the total feedrate of chlorine (organic and inorganic) in all feedstreams as the average of the test run averages.
(ii)
Liquid fuel boilers—
(A)
Boilers that feed hazardous waste with a heating value not less than 10,000 Btu/lb. (1) The feedrate limit is a hazardous waste thermal concentration limit expressed as pounds of chlorine (organic and inorganic) in all hazardous waste feedstreams per million Btu of hazardous waste fed to the boiler.

(2) You must establish a 12-hour rolling average feedrate limit as the average of the test run averages.

(3) You must comply with the feedrate limit by determining the mass feedrate of hazardous waste feedstreams (lb/hr) at least once a minute and by knowing the chlorine content (organic and inorganic, lb of chlorine/lb of hazardous waste) and heating value (Btu/lb) of hazardous waste feedstreams at all times to calculate a 1-minute average feedrate measurement as [hazardous waste chlorine content (lb of chlorine/lb of hazardous waste feed)/hazardous waste heating value (Btu/lb of hazardous waste)]. You must update the rolling average feedrate each hour with this 60-minute average feedrate measurement.

(B)
Boilers that feed hazardous waste with a heating value less than 10,000 Btu/lb. You must establish a 12-hour rolling average limit for the total feedrate of chlorine (organic and inorganic) in all feedstreams as the average of the test run averages. You must update the rolling average feedrate each hour with a 60-minute average feedrate measurement.
(2)
Maximum flue gas flowrate or production rate.
(i)
As an indicator of gas residence time in the control device, you must establish a limit on the maximum flue gas flowrate, the maximum production rate, or another parameter that you document in the site-specific test plan as an appropriate surrogate for gas residence time, as the average of the maximum hourly rolling averages for each run.
(ii)
You must comply with this limit on a hourly rolling average basis;
(3)
Wet scrubber. If your combustor is equipped with a wet scrubber:
(i)
If your source is equipped with a high energy wet scrubber such as a venturi, hydrosonic, collision, or free jet wet scrubber, you must establish a limit on minimum pressure drop across the wet scrubber on an hourly rolling average as the average of the test run averages;
(ii)
If your source is equipped with a low energy wet scrubber such as a spray tower, packed bed, or tray tower, you must establish a minimum pressure drop across the wet scrubber based on manufacturer's specifications. You must comply with the limit on an hourly rolling average;
(iii)
If your source is equipped with a low energy wet scrubber, you must establish a limit on minimum liquid feed pressure to the wet scrubber based on manufacturer's specifications. You must comply with the limit on an hourly rolling average;
(iv)
You must establish a limit on minimum pH on an hourly rolling average as the average of the test run averages;
(v)
You must establish limits on either the minimum liquid to gas ratio or the minimum scrubber water flowrate and maximum flue gas flowrate on an hourly rolling average as the average of the test run averages. If you establish limits on maximum flue gas flowrate under this paragraph, you need not establish a limit on maximum flue gas flowrate under paragraph (o)(2) of this section; and
(4)
Dry scrubber. If your combustor is equipped with a dry scrubber, you must establish the following operating parameter limits:
(i)
Minimum sorbent feedrate. You must establish a limit on minimum sorbent feedrate on an hourly rolling average as the average of the test run averages.
(ii)
Minimum carrier fluid flowrate or nozzle pressure drop. You must establish a limit on minimum carrier fluid (gas or liquid) flowrate or nozzle pressure drop based on manufacturer's specifications.
(iii)
Sorbent specifications.
(A)
You must specify and use the brand (i.e., manufacturer) and type of sorbent used during the comprehensive performance test until a subsequent comprehensive performance test is conducted, unless you document in the site-specific performance test plan required under § 63.1207(e) and (f) key parameters that affect adsorption and establish limits on those parameters based on the sorbent used in the performance test.
(B)
You may substitute at any time a different brand or type of sorbent provided that the replacement has equivalent or improved properties compared to the sorbent used in the performance test and conforms to the key sorbent parameters you identify under paragraph (o)(4)(iii)(A) of this section. You must record in the operating record documentation that the substitute sorbent will provide the same level of control as the original sorbent.
(p)
Maximum combustion chamber pressure. If you comply with the requirements for combustion system leaks under § 63.1206(c)(5) by maintaining the maximum combustion chamber zone pressure lower than ambient pressure to prevent combustion systems leaks from hazardous waste combustion, you must perform instantaneous monitoring of pressure and the automatic waste feed cutoff system must be engaged when negative pressure is not adequately maintained.
(q)
Operating under different modes of operation. If you operate under different modes of operation, you must establish operating parameter limits for each mode. You must document in the operating record when you change a mode of operation and begin complying with the operating limits for an alternative mode of operation.
(1)
Operating under otherwise applicable standards after the hazardous waste residence time has transpired. As provided by § 63.1206(b)(1)(ii), you may operate under otherwise applicable requirements promulgated under Clean Air Act sections 112 and 129 in lieu of the substantive requirements of this subpart.
(i)
The otherwise applicable requirements promulgated under Clean Air Act sections 112 and 129 are applicable requirements under this subpart.
(ii)
You must specify (e.g., by reference) the otherwise applicable requirements as a mode of operation in your Documentation of Compliance under § 63.1211(c), your Notification of Compliance under § 63.1207(j), and your title V or other air permit application. These requirements include the otherwise applicable requirements governing emission standards, monitoring and compliance, and notification, reporting, and recordkeeping.
(2)
Calculating rolling averages under different modes of operation— . When you transition to a different mode of operation, you must calculate rolling averages as follows:
(i)
Retrieval approach— . Calculate rolling averages anew using the continuous monitoring system values previously recorded for that mode of operation (i.e., you ignore continuous monitoring system values subsequently recorded under other modes of operation when you transition back to a mode of operation); or
(ii)
Start anew— . Calculate rolling averages anew without considering previous recordings.
(A)
Rolling averages must be calculated as the average of the available one-minute values for the parameter until enough one-minute values are available to calculate hourly or 12-hour rolling averages, whichever is applicable to the parameter.
(B)
You may not transition to a new mode of operation using this approach if the most recent operation in that mode resulted in an exceedance of an applicable emission standard measured with a CEMS or operating parameter limit prior to the hazardous waste residence time expiring; or
(iii)
Seamless transition— . Continue calculating rolling averages using data from the previous operating mode provided that both the operating limit and the averaging period for the parameter are the same for both modes of operation.
(r)
Averaging periods. The averaging periods specified in this section for operating parameters are not-to-exceed averaging periods. You may elect to use shorter averaging periods. For example, you may elect to use a 1-hour rolling average rather than the 12-hour rolling average specified in paragraph (l)(1)(i) of this section for mercury.
(s)
Hydrogen fluoride— . You must comply with the hydrogen fluoride gas emission standard either by complying with the following work practice standard in paragraph (s)(1) of this section or by establishing and complying with the operating parameter limits in paragraph (s)(2) of this section, as directed by §§ 63.1216 through 63.1221.
(1)
Work practice standard for emissions of hydrogen fluoride— . You must comply with one of the following provisions:
(i)
If your hazardous waste combustor actively controls emissions of hydrogen chloride (e.g. using an air pollution control device) and has at least one AWFCO-interlocked operating parameter limit as specified in § 63.1209(o)(2) through (o)(4), then comply with the operating parameter limits specified for hydrogen chloride and chlorine gas under § 63.1209(o). Indicate in your comprehensive performance test report and notification of compliance that compliance with the hydrogen fluoride gas work practice standard is demonstrated by complying with the hydrogen chloride and chlorine gas operating parameter limits;
(ii)
If you do not feed any material with detectable levels of fluorine to your hazardous waste combustor, then certify that no fluorine is fed to your hazardous waste combustor in the comprehensive test report. Indicate in your comprehensive performance test report and notification of compliance that compliance with the hydrogen fluoride gas work practice standard is demonstrated by certifying that no fluorine is fed to the combustor; or
(iii)
Monitor and record in the operating record the total feedrate of fluorine (organic and inorganic) in all feedstreams as a 12-hour rolling average. Monitor with a CMS and record in the operating record the gas flowrate (either directly or by monitoring a surrogate parameter that you have correlated to gas flowrate). In every comprehensive performance test plan, calculate the maximum MTEC of hydrogen fluoride since the previous comprehensive performance test. If the maximum MTEC is greater than the existing source solid fuel boiler hydrogen fluoride emission limit in § 63.1216(a)(8), then conduct a one-time emissions test for hydrogen fluoride gas during the comprehensive performance test. The one-time test does not need to be repeated at any subsequent comprehensive performance test, regardless of the calculated maximum MTEC value.
(2)
Operating parameter limits for hydrogen fluoride— . You must comply with the hydrogen fluoride emission standard by establishing and complying with the following operating parameter limits. You must base the limits on operations during the comprehensive performance test, unless the limits are based on manufacturer specifications.
(i)
Feedrate of total fluorine and fluoride— . You must establish a 12-hour rolling average limit for the total feedrate of fluorine (organic and inorganic) in all feedstreams as the average of the test run averages.
(ii)
Maximum flue gas flowrate or production rate— . (A) As an indicator of gas residence time in the control device, you must establish a limit on the maximum flue gas flowrate, the maximum production rate, or another parameter that you document in the site-specific test plan as an appropriate surrogate for gas residence time, as the average of the maximum hourly rolling averages for each run.
(B)
You must comply with this limit on an hourly rolling average basis;
(iii)
Wet scrubber— . If your combustor is equipped with a wet scrubber:
(A)
If your source is equipped with a high energy wet scrubber such as a venturi, hydrosonic, collision, or free jet wet scrubber, you must establish a limit on minimum pressure drop across the wet scrubber on an hourly rolling average as the average of the test run averages;
(B)
If your source is equipped with a low energy wet scrubber such as a spray tower, packed bed, or tray tower, you must establish a minimum pressure drop across the wet scrubber based on manufacturer's specifications. You must comply with the limit on an hourly rolling average;
(C)
If your source is equipped with a low energy wet scrubber, you must establish a limit on minimum liquid feed pressure to the wet scrubber based on manufacturer's specifications. You must comply with the limit on an hourly rolling average;
(D)
You must establish a limit on minimum pH on an hourly rolling average as the average of the test run averages;
(E)
You must establish limits on either the minimum liquid to gas ratio or the minimum scrubber water flowrate and maximum flue gas flowrate on an hourly rolling average as the average of the test run averages. If you establish limits on maximum flue gas flowrate under this paragraph, you need not establish a limit on maximum flue gas flowrate under paragraph (s)(2)(ii) of this section; and
(iv)
Dry scrubber— . If your combustor is equipped with a dry scrubber, you must establish the following operating parameter limits:
(A)
Minimum sorbent feedrate— . You must establish a limit on minimum sorbent feedrate on an hourly rolling average as the average of the test run averages.
(B)
Minimum carrier fluid flowrate or nozzle pressure drop— . You must establish a limit on minimum carrier fluid (gas or liquid) flowrate or nozzle pressure drop based on manufacturer's specifications.
(C)
Sorbent specifications— . (1) You must specify and use the brand (i.e., manufacturer) and type of sorbent used during the comprehensive performance test until a subsequent comprehensive performance test is conducted, unless you document in the site-specific performance test plan required under § 63.1207(e) and (f) key parameters that affect adsorption and establish limits on those parameters based on the sorbent used in the performance test.
(2)
You may substitute at any time a different brand or type of sorbent provided that the replacement has equivalent or improved properties compared to the sorbent used in the performance test and conforms to the key sorbent parameters you identify under paragraph (s)(2)(iv)(C)(1) of this section. You must record in the operating record documentation that the substitute sorbent will provide the same level of control as the original sorbent.
Notes, amendments, and revision history

Amendments

[91 FR 33540, June 3, 2026]

Source

Source: 64 FR 53038, Sept. 30, 1999, unless otherwise noted.

Authority

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

Source

Source: 57 FR 61992, Dec. 29, 1992, unless otherwise noted.

Amendments

[91 FR 33540, June 3, 2026]