United States Environmental Protection Agency Industrial Environmental Research Laboratory Research Triangle Park NC 27711 Research and Development EPA-600/S7-83-056 Feb. 1984 Project Summary Analysis of Low NOX Operation of Two Pulverized- Coal-Fired Utility Boilers S.S. Cherry The operation of two pulverized-coal- fired utility boilers subject to the 1971 New Source Performance Standard was reviewed to determine if other boilers could adopt a similar mode of operation to reduce nitrogen oxide (NOx) emissions. These two boilers had been identified, during a previous study, as low NOx emission sources. It was determined that reburnering, burner modification, or optimizing the overt ire air system of existing Foster Wheeler boilers offered the potential to reduce NOX significantly. It was also determined that existing Babcock & Wilcox boilers would probably not respond to further combustion modifica- tions. This Project Summary was developed by EPA's Industrial Environmental Research Laboratory. Research Triangle Park. NC, to announce key findings of the research project that is fully docu- mented in a separate report of the same title (see Project Report ordering information at back). Introduction and Summary It was determined that the N0xemissions from two boilers (Unit 1 of Public Service Co. of New Mexico's San Juan Station, and Unit 3 of Iowa Power and Light's Council Bluffs Station) were lower than other pulverized coal-fired utility boilers analyzed during a previous study. The purpose of the program was to determine if other boilers manufactured by Foster Wheeler (San Juan Unit 1) and Babcock & Wilcox (Council Bluffs Unit 3) could achieve a lower NO emission rate. It was determined that Foster Wheeler boilers with the single-register Intervane burner and operating with overfire air (OFA) could, potentially, reduce emissions by one of the following: 1. Burner modification: including coal splitters in the annular coal nozzle. 2. Burner replacement: substituting the newer dual-register controlled- flow/split-flame variable-velocity (CF/SV) burner for the Intervane burner. 3. Overfire air: increasing the amount of OFA or optimizing the OFA damper settings. The approach selected must be unit- specific. It was determined that the newer Babcock & Wilcox boilers would probably not be able to achieve a significantly lower NOx emission rate using these techniques. All new boilers have dual- register burners and compartmented windboxes (for closer control of burner air flow). Discussion The NOx measured during the perfor- mance test conducted on Foster Wheeler boilers subject to the 1971 New Source Performance Standard (NSPS) is summa- rized in Table 1 .* Note that most of these units have the single-register, high- turbulence Intervance (IV) burner and are operating with OFA. *San Juan Unit 1 was designed to comply with the State of New Mexico NO, limitation of 0.45 lb/108 Btu (194 ng/J) and not the 1971 NSPS. However, it is included in this study of other Foster Wheeler units subject to the 1971 NSPS ------- Table 1. Summary of Foster Wheeler Pulverized-Coal-Fired NSPS Utility Boilers Test 1A. IB. 1C. 2. 3. 4. 5. 6. 7. 8. 9. 10. 11. 12. 13. 14. Utility Public Service Co. New Mexico Omaha Public Power District Proprietary Portland Genera/ Electric Nebraska Public Power District Proprietary Proprietary Northern Indiana Public Service Iowa Public Service Allegheny Power Service Allegheny Power Service Proprietary Proprietary Proprietary Station San Juan Nebraska City - Boardman Gentlemen - - Schahfer Neal Pleasants Pleasants - - Unit 1 1 - 1 7 - -- 15 4 1 2 - — -- Gross MWe 360 575 114 530 650 500 534 511 630 660 660 770 860 736' Firing Mode" 1 2 1 2 2 2 2 2 2 2 2 2 2 2 No. of Burners 16 28 8 32 32 24 24 24 28 24 24 48 32 40 Burner Type" IV IV CF/SV IV IV CF/SV IV IV CF IV IV IV IV IV IV IV Overfrre Air No Yes No Yes" Yes Yes Yes Yes Yes Yes Yes Yes Yes Yes Yes Yes Coal Performance Type* lb/10eBtu Sub. Sub. Sub. Sub. Sub. Sub. Sub. Sub. Sub. Bit. Bit. Bit. Bit. Bit. 1.O5 0.63 0.35 0.479 0.699 0.5T 0.354 0.518 0.465" 0.45 0.345 0.61 0.61 0.63 0.66 0.43 NO, ng/J 452 271 151 206 301 245 152 223 200 194 148 262 262 271 284 185 " 7 = Front-wall 2 = Opposed-wall " IV , Intervane CF/SV = Controlled-flow/'split-flame variable velocity CF = Controlled flow " Sub. = Subbituminous Bit. = Bituminous d Interstage air e Overfire air closed 1 Two boilers supplying one steam turbine. Figure 1 is a plot of these data in terms of the gross MWe per firing wall.* Also shown in this figure is a linear regression of these data (except Tests 3,5, and 9) which shows a high degree of correlation (r2 = 0.80) of NO, in terms of MWe/wall. Linear regressions of data obtained on pre-NSPS boilers are also highly cor- related in terms of this parameter (r2 — 0.81 for baseline, r2 = 0.85 for staged combustion). Results from San Juan Unit 1 with the dual-register controlled-flow/split-flame variable-velocity burner (Figure 2) indicate a NOX reduction of 32 to 44 percent with respect to the IV burner operating with OFA. However, results from Boardman Unit 1 (Test 4, Table 1) are not consistent with San Juan Unit 1; i.e., it was anticipated that the emissions for the CF/SV burner-equipped Boardman Unit 1 should have been lower. Adding coal splitters to the IV burner (operating without OFA has been demon- strated to significantly reduce NO* emissions from pre-NSPS units. However, these results have also been shown to be highly unit-specific. It was determined that the low emissions for Tests 5 and 9 (Table 1) were due to a modification of the OFA system to increase OFA flow. These modifications 'The performance NO, is that measured during the performance test required by the 1971 NSPS using EPA Method 7 700 600 •^500 el O *300 i I §200 700 Pre-1971 NSPS Units Baseline Staged Combustion 400 300 (13) 2OO c i (1C) O Front-Wall, Subbituminous CD Opposed-Wall. Subbituminous • Opposed-Wall, Bituminous O CF/SV Burner, without OFA 100 0. O 100 200 300 400 System Load/Firing Wall, Gross MWe 500 Figure 1. Foster Wheeler NSPS units, Intervane burners with OFA. were apparently responsible for achieving a NOx level lower than the correlation based on other Foster Wheeler boilers (Figure 1). An analysis of Babcock & Wilcox NSPS boilers operating with Subbituminous coal (Figure 3) indicated that Council Bluffs Unit 3 was not a particularly low NOx emission source when compared with other B&W 1971 NSPS units. These data demonstrate that the performance test NOx for Council Bluffs Unit 3 is no different than the sample mean. This result implies that B&W NSPS units operating with Subbituminous coal would probably not be able to achieve ------- 1.2 1.0 0.8 0.6 =8 O 0.4 0.2 IV IV = Intervene Burner CF/SV = Controlled-Flow/ Split-Flame Variable- Velocity Burner IV CF/SV 500 400 300 1 i 200 100 Figure 2. Closed Open Overfire Air Ports Low NO* burner comparison. Closed Open (Not Yet Tested) flame variable velocity configuration) offers the potential to reduce NOX emission on Foster Wheeler 1971 NSPS boilers. Quantification of the effectiveness of these approaches is uncertain due to an apparent unit specific nature of the results. The effectiveness of burner replacement should become more firmly established as new units with the CF/SV burner are performance tested. Optimizing the OFA system would probably be most applicable to units with a low windbox-to- furnace pressure differential. significantly lower NOx. (All such units have dual-register burners and compart- mented windboxes.) Conclusions (Note: The objective of this effort was to assess the potential NO* reduction for 1971 NSPS boilers manufactured by Babcock & Wilcox and Foster Wheeler, based on the operation of Council Bluffs Unit 3 (B&W) and San Juan Unit 1 (F.W.).) It was concluded that: 1. B&W 1971 NSPS units would not significantly benefit from the adop- tion of Council Bluffs Unit 3's mode of operation. 2. Foster Wheeler 1971 NSPS units would benefit from a burner modifi- cation, burner replacement, or optimization of the overfire air system. The degree of potential NO* reduction is uncertain. The first conclusion is based on a comparison between Council Bluffs Unit 3 and other subbituminous-coal-fired B&W boilers, which showed no statistical difference in NOx emission levels mea- sured during the performance test. Thus, the initial perception that Council Bluffs Unit 3 was a significantly low NOX source is not warranted when compared to other B&W 1971 NSPS units. Burner modification (adding primary air/coal stream splitters to single register burners) or burner replacement (replacing Intervane burner with controlled flow/split ------- auu 400 £ d 3? 300 <*> ^200 O 100 0 I I I I I I I Subbituminous Coal Dual-Register Burners f~\ _ Compartmented Windbox 9 Council Bluffs Unit 3 + Mean _ - I _ o o o o+°o o* - o ° o - I I 1 1 1 1 250 200 -J 150 % i 100 50 O 700 200 300 System Load/Firing Wall, Gross MWe 400 Figure 3. Babcock & Wilcox 1971 NSPS boilers. S. S. Cherry is with KVB. Inc., Irvine. CA 92714. Michael C. Osborne is the EPA Project Officer (see below). The complete report, entitled "Analysis of Low NO* Operation of Two Pulverized- Coal-Fired Utility Boilers," (Order No. PB84-118918; Cost: $8.50, subject to change) will be available only from: National Technical Information Service 5285 Port Royal Road Springfield. VA 22161 Telephone: 703-487-4650 The EPA Project Officer can be contacted at: Industrial Environmental Research Laboratory U.S. Environmental Protection Agency Research Triangle Park, NC 27711 ADS GOVERNMENT PRINTING OfFICE 1984-759-015/7306 United States Environmental Protection Agency Center for Environmental Research Information Cincinnati OH 45268 BULK RATE POSTAGE & FEES P/> EPA PERMIT No. G-35 Official Business Penalty for Private Use $300 ------- |