State of the Art (SOTA) Manual for Boilers and Process Heaters



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State of the Art (SOTA) Manual for Boilers and Process Heaters Original Date: July 1997 Revision Date: February 22, 2004 State of New Jersey Department of Environmental Protection Air Quality Permitting Element

Section State of the Art (SOTA) Manual for Boilers and Process Heaters Section 3.12 Table of Contents Page Number 3.12.i: Tables... 3.12-3 3.12.ii: Abbreviations... 3.12-4 3.12: SOTA Manual for Boilers and Process Heaters... 3.12-5 3.12.1: Scope... 3.12-5 3.12.2: SOTA Performance Levels... 3.12-5 3.12.2.1: SOTA Emission Levels for -Fired Boilers and Process Heaters 3.12-5 3.12.2.2: SOTA Emission Levels for Fuel Oil-Fired Boilers and Process Heaters... 3.12-6 3.12.3: Technical Basis... 3.12-7 3.12.3.1: Basis for Recommended Guidance... 3.12-7 3.12.3.2: Control Technologies for -Fired Boilers and Process Heaters 3.12-7 3.12.3.3: Control Technologies for Fuel Oil-Fired Boilers and Process Heaters 3.12-8 3.12.3.4: Control Technologies for Coal and Other Solid Fuel Fired Boilers... 3.12-9 3.12.4: Energy Efficiency Considerations... 3.12 9 3.12-2

3.12.i TABLES Table Page Number SOTA Emission Level Tables: Table 1a. -Fired Boilers and Process Heaters 10 to <50 MMBTU/hr... 3.12-5 Table 1b. -Fired Boilers and Process Heaters 50 to <75 MMBTU/hr... 3.12-5 Table 1c. -Fired Boilers and Process Heaters 75 MMBTU/hr... 3.12-6 Table 2a. Distillate Fuel Oil-Fired Boilers and Process Heaters 10 to <75 MMBTU/hr... 3.12-6 Table 2b. Distillate Fuel Oil-Fired Boilers and Process Heaters 75 MMBTU/hr... 3.12 6 SOTA Control Technology Tables: Table 3a. -Fired Boilers and Process Heaters 10 to <50 MMBTU/hr... 3.12-7 Table 3b. -Fired Boilers and Process Heaters 50 to <75 MMBTU/hr... 3.12 8 Table 3c. -Fired Boilers and Process Heaters 75 MMBTU/hr... 3.12-8 Table 4. Fuel Oil-Fired Boilers and Process Heaters, 10 to < 75 MMBTU/hr... 3.12-9 Table 5. Fuel Oil-Fired Boilers and Process Heaters, 75 MMBTU/hr... 3.12-9 3.12-3

3.12.ii ABBREVIATIONS BACT CFR EPA ESP FGD FGR LAER LNB MMBTU N.J.A.C. NO x NSPS PM 10 PSD SCR SNCR SOTA SO 2 TSP Best Achievable Control Technology Code of Federal Regulations Carbon Monoxide United States Environmental Protection Agency Electrostatic Precipitator Flue Gas Desulfurization Flue Gas Recirculation Lowest Achievable Emission Rate Low NO x Burner Million British Thermal Units New Jersey Administrative Code Nitrogen Oxides New Source Performance Standards Particulate Matter Equal to or Smaller Than 10 Microns in Diameter Prevention of Significant Deterioration Selective Catalytic Reduction Selective Non-Catalytic Reduction State of the Art Sulfur Dioxide Total Suspended Particulate Matter Volatile Organic Compounds 3.12-4

3.12 STATE OF THE ART MANUAL FOR BOILERS AND PROCESS HEATERS 3.12.1 Scope The state of the art (SOTA) performance levels outlined below apply to newly constructed, reconstructed, and modified industrial and utility boilers and process heaters subject to the SOTA provisions of N.J.A.C. 7:27-8 and N.J.A.C. 7:27-22. 3.12.2 SOTA Performance Levels The following tables present state of the art one hour average emission levels for criteria pollutants and control technologies for each category of boilers and process heaters. Where no emission levels for SO 2 and TSP are specified, the emissions of these pollutants would be dependent on fuel composition. Coal and other solid fuel fired boilers will address SOTA levels on a case-by-case basis. 3.12.2.1 State of the Art Emission Levels for -Fired Boilers and Process Heaters Table 1a -Fired Boilers and Process Heaters Emission Level (LB/MMBTU) 10 to <50 MMBTU/hr NO x 0.0350 0.0500 0.00500 Table 1b -Fired Boilers and Process Heaters Emission Level (LB/MMBTU) 50 to < 75 MMBTU/hr NO x 0.0200 0.0500 0.00500 3.12-5

Table 1c -Fired Boilers and Process Heaters Emission Level (LB/MMBTU) 75 MMBTU/hr NO x 0.010 0.0390 0.00500 3.12.2.2 State of the Art Emission Levels for Distillate Fuel Oil-Fired Boilers and Process Heaters Table 2a Distillate Fuel Oil-Fired Boilers and Process Heaters Emission Level (LB/MMBTU) 10 and <75 MBTU/hr NOx 0.0600 0.0390 0.0100 Table 2b Distillate Fuel Oil-Fired Boilers and Process Heaters Emission Level (LB/MMBTU) 75 MMBTU/hr NOx 0.0300 0.0390 0.0100 NOTE: SOTA performance levels for boilers and process heaters combusting fuel oils other than distillate oil will be addressed on a case-by-case basis. SOTA performance levels for natural draft process heaters and air pre-heaters will be addressed on a case-by-case basis. 3.12-6

3.12.3 Technical Basis 3.12.3.1 Basis for Recommended Guidance The recommended standards are based on the following: - Permits issued by the New Jersey Department of Environmental Protection and other states in United States; - State and federal regulations; - BACT data from the Bay Area Air Quality Management District; - BACT data from the California Air Resource Board; and - Data from the United States Environmental Protection Agency s RACT/BACT/LAER Information Systems. 3.12.3.2 Control Technologies for Fired Boilers and Process Heaters The state of the art NO x emission levels listed for natural gas-fired boilers and process heaters for the size ranges 10 to 50 MMBTU/hr heat input rate have been achieved with the use of Low NO x Burners (LNBs) with Flue Gas Recirculation (FGR) or ultra LNBs (ULNB). The state of the art NO x emission levels listed for natural gas-fired boilers and process heaters for the size ranges 50 to 75 MMBTU/hr heat input rate have been achieved with LNBs with FGR or ULNB. The state of the art NO x emission levels listed for natural gas-fired boilers and process heaters for the size ranges equal to and greater than 75 MMBTU/hr heat input rate have been achieved with or without Selective Catalytic Reduction System (SCR). The state of the art and emission levels listed for natural gas-fired boilers and process heaters for the size ranges greater than 10 MMBTU/hr heat input rate have been achieved with combustion controls. Oxidation catalysts also reduce emissions of and. Natural gas is considered a clean fuel due to its low sulfur and particulate content. Table 3a -Fired Boilers and Process Heaters, 10 and <50 MBTU/hr NOx Control Technology LNB with FGR or ULNB 3.12-7

SO 2 TSP/PM10 Table 3b -Fired Boilers and Process Heaters, 50 to 75 MMBTU/hr NOx SO 2 TSP/PM10 Control Technology LNB with FGR or ULNB Table 3c -Fired Boilers and Process Heaters, 75 MMBTU/hr NOx SO 2 TSP/PM10 Control Technology LNB with FGR and/or SCR 3.12.3.3 Control Technologies for Fuel Oil-Fired Boilers and Process Heaters The state of the art NO x emission levels listed for distillate fuel oil-fired boilers and process heaters for the size ranges 10 to 75 MMBTU/hr heat input rate have been achieved with the use of LNBs with FGR. The state of the art NO x emission levels listed for distillate fuel oil-fired boilers and process heaters for the size ranges greater than 75 MMBTU/hr heat input rate have been achieved with the use of LNBs with FGR and SCR. The state of the art and emission levels listed for distillate fuel oil-fired boilers and process heaters for the sizes greater than 10 MMBTU/hr heat input rate can be achieved by combustion controls. SO 2 emissions are controlled on fuel oil-fired boilers and process heaters by using low sulfur fuel. Distillate oil (No. 1 or No. 2) contains less sulfur than residual oil (No. 5 or No. 6), and thus use of distillate oil is considered a control strategy. Ultra low sulfur fuel oil shall be evaluated as a back up 3.12-8

fuel instead of conventional low sulfur fuel because Ultra low S has less than 50 ppm sulfur and will result in very low SO 2 emissions. This fuel will have very low TSP and PM-10 emissions. Methods for controlling particulate emissions from fuel oil-fired boilers and process heaters include fuel specification (clean burning distillate fuels) and mechanical methods (multi cyclones). Table 4 Fuel Oil-Fired Boilers and process heaters, 10 and <75 MMBTU/hr NOx SO 2 Control Technology LNB with FGR Fuel Specification (Low Sulfur Fuel) Table 5 Fuel Oil-Fired Boilers and process heaters, 75 MMBTU/hr NOx SO 2 TSP/PM10 Control Technology LNB with FGR and SCR Fuel Specification (Low Sulfur Fuel) Multi cyclones 3.12.3.4 Control Technologies for Coal and Other Solid Fuel Fired Boilers and Process Heaters Coal fired boilers would be large enough to be subject to 40 CFR 52.21 Best Available Control Technology (BACT) requirements, and N.J.A.C. 7:27-18.1 et. seq. Lowest Achievable Emission rate (LAER) requirements. Both BACT and LAER requirements are determined on a case by case. Other solid fuel-fired boilers and process heaters may also be subject to the same requirements. The control technology currently available for coal fired boilers is SCR and/or SNCR for NO x, scrubbers for SO 2, carbon injection for mercury and baghouses for particulate matter emissions. These air pollution control technologies are also applicable to other solid fuel fired boilers. 3.12-9

EMISSIONS REDUCTION WITH INCREASED ENERGY EFFICIENCY- POLLUTION PREVENTION The New Jersey Air Pollution Control Code, N.J.A.C. 7:27-8.4(k)1 and N.J.A.C. 7:27-22, require inclusion of greenhouse gases resulting from fuel combustion in boilers and process heaters in air pollution control permits. Greenhouse gases include carbon dioxide, methane and nitrous oxide. Emissions of carbon dioxide can be reduced by favoring higher efficiency processes such as boilers and process heaters which are inherently more efficient. The energy efficiency of the boilers and process heaters expressed in terms of fuel to steam efficiency must be reported in the application. The SOTA level will be determined at the time of the application on a case by case basis. DEP is not setting a specific energy level requirement at this time as a SOTA level. Improving the energy efficiency of the system used is the best pollution prevention method. Higher efficiency systems require less fuel to produce the needed power. Improving energy efficiency also results in boilers and process heaters which emit lesser amounts of the criteria and hazardous air pollutants on an output basis. 3.12-10