Field Evaluation of Low-Emission Coal Burner Technology on Utility Boilers. Volume 3. Field Evaluations

EFA-600/7-89-015c December 1989 FIELD EVALUATION OF LOW-EMISSION COAL BURNER TECHNOLOGY ON UTILITY BOILERS VOLUME III Field Evaluations J. A. Reese, A. R. Abele (Energy and Environmental Research Corporation) and P, W. Waanders Babcock & Wilcox 20, S. Van Buren Avenue Barberton, OH 44203 EPA Contract 68-02-3130 EPA Project Officer: P. Jeff Chappell Air and Energy Engineering Research Laboratory Research Triangle Park, NC 27711 Prepared for; U..S. Environmental Protection Agency Office of Research and Development Washington, DC 20460 ------- 1 TECHNICAL REPORT DATA ' {Please read Instructions on the reverse before completing} t. REPORT NO. EPA-600/7-89-015c 2. 3. RECIPIENT'S ACCESSION NO. 4. TITLE AND SUBTITLE Field Evaluation of Low-Emission Coal Burner Tech" 5. REPORT DATE December 1989 nology on Utility Boilers; uation Volume III. Field Eval- 6. PERFORMING ORGANIZATION CODE 7. AUTHOR(S) J. L. Reese and A. R. Abele (EERC); and P, W, Waanders (Babcock and Wilcox)* 8. PERFORMING ORGANIZATION REPORT NO. 9. PERFORMING ORGANIZATION NAME AND ADDRESS Energy and Environmental Research Corporation 10. PROGRAM ELEMENT NO. 18 Mason Irvine, California 92718 11. CONTRACT/GRANT NO. 68-02-3130* 12. SPONSORING AGENCY NAME AND ADDRESS EPA, Office of Research and Development Air and Energy Engineering Research Laboratory Research Triangle Park, NC 27711 13. TYPE OF REPORT AND PERIOD COVERED' Final; 9/78 - 6/86 14. SPONSORING AGENCY CODE EPA/600/13 15. supplementary notes AEERL pr0ject officer is P. Jeff Ch 3738. () Contract with Babcock and Wilcox, P.O. Box 0351. >1 appell. Mail Drop 63, 919/541- 351, Barberton, OH 44203" is. abstract rep0r£ giveg results of field tests conducted to determine the emission characteristics of a Babcock and Wilcox Circular burner and Dual Register burner (DRB). The field tests were performed at two utility boilers, generally comparable in design and size except for the burner equipment. The Circular burner was eval- uated at Unit 2 of the Colorado Public Services Comanche Generating Station, and the DRB was evaluated at Unit 1 of the Wyodak Generating Station of the Pacific Po- wer and Light Company and the Black Hills Power and Light Company. Of particular interest was the development of NOx amission correlations for the performance of Circular burners and lPRBs /Under boiler conditions which could be used in inter- . preting individual burner! tests in a subscale burner test facility. The field tests were conducted with both boilers operating at nominal.full-load conditions. During each test, boiler performance and operating conditions were monitored using plant equipment, while gaseous emissions of NOx, 02, CO, S02, and C02 were contin- uously monitored using a mobile test trailer .^fT.he nominal NOx emissions with the Circular burner at Comanche were 550 ppm at 0'pb G2. Full-load NOx emissions at Wyodak with all mills in service were 395 ppm at 0% 02.' Operation over a harrow / excess 02 range precluded establishing NOx emission as a function of excess <02. 17, KEY WORDS AND DOCUMENT ANALYSIS a. DESCRIPTORS b.IDENTIFIERS/OPEN ENDED TERMS c. COSATI Field/Gioup Pollution Nitrogen Oxides Coal Electric Utilities Combustion Field Tests Evaluation Burners Pollution Control Stationary Sources Circular Burners Dual Register Burners 13 B 07B 21D 2 IB 14 B 14G 13 A 13. DISTRIBUTION STATEMENT 19. SECURITY CLASS (This Report)' Unclassified 21. NO.„OF.PAGES I 251 j Release to Public 20. SECURITY CLASS (This page) Unclassified 22. PRICE EPA Fsrm 2220-1 (8-731 r I" '. ¦ I i ------- NOTICE This document has been reviewed in accordance with U.S. Environmental Protection Agency policy and approved for publication. Mention of trade names or commercial products does not constitute endorse- ment or recommendation for use. ------- ABSTRACT This report describes the results of field tests conducted to determine the emission characteristics of B&W circular and dual register burners. The field tests were performed at two different utility boilers, generally comparable in design and size except for the burner equipment. The BIW circular burner was evaluated at Unit 2 of the Colorado Public Services Comanche Generating Station and the B&W dual register burner was evaluated at Unit 1 of the Wyodak Generating Station of the Pacific Power and Light Company and the Black Hills Power and Light Company. Of particular interest was the development of N0X emission correlations for the performance of circular and dual register burners under boiler conditions which could be used in interpretation of individual burner tests in a subscale burner test facility. The field tests were conducted with both boilers operating at nominal full-load conditions. During each test, boiler performance and operating conditions were monitored using plant equipment, while gaseous emissions of NQX, O2, CO, SO2, and CO2 were continuously monitored using a mobile test trailer. The nominal N0X emissions with the circular burner at Comanche were 550 ppm at 0 percent O2• Full-load N0X emissions at Wyodak with all mills in service were 395 ppm at 0 percent O2. Since both boilers were operated over a narrow excess O2 range, the data were not sufficient to establish N0X emission as a function of excess 02« However, the data from both boilers do show a strong dependence of N0X on both boiler load and firing configuration. This work was carried out by Energy and Environmental Research Corporation under EPA Contract 68-02-3130, through Babcock and Wilcox Subcontract 940962 NR. ------- TABLE OF CONTENTS Section Page ABSTRACT ii 1.0 INTRODUCTION. 1-1 2.0 SUMMARY 2-1 3.0 BOILER DESCRIPTIONS AND TEST PLAN 3-1 3.1 Description of Comanche Unit 2 .... 3-1 3.2 Description of Wyodak Unit 1 3-5 3.3 Test Plan 3-12 4.0 TEST RESULTS 4-1 4.1 Results at Comanche Unit 2 4-1 4.2 Results at Wyodak 4-8 5.0 REFERENCE 5-1 APPENDICES A. TEST PROCEDURES. A-l B. QUALITY ASSURANCE. B-l C. TEST DATA C-l C—1 Comanche Gaseous Emissions Data ...... C-2 C-2 Comanche Boiler Operating Data C-34 C-3 Wyodak Gaseous Emissions Data C-80 C-4 Wyodak Plant Boiler Logs C-94 C-5 Wyodak Coal and Ash Analysis C-112 C-6 Wyodak Furnace Gas Temperature Data .... C-122 J Preceding Page Blank ^ ------- LIST OF FIGURES Figure Page 2-1 NOx emissions vs. boiler load 2-4 3-1 B&W Circular Burner 3-3 3-2 Comanche Unit 2 burner settings ........... 3-4 3-3 General arrangement of Wyodak Unit 1 ..... 3-6 3-4 Babcock & Wilcox dual register burner 3-8 3-5 Wyodak Unit 1 burner arrangement . 3-10 , 3-6 Field test plan 3-13 4-1 Daily averages of gaseous emissions—Comanche Unit 2 ..... 4-2 4-2 N0X and CO vs. load - Comanche Unit 2 4-4 4-3 Comanche Unit 2 - N0X and CO vs. excess at a load of 253-273 MWe . . 4-6 4-4 Comanche gas stratification test ...... .... 4-7 4-5 Effect of overfire air port damper position on emissions - Comanche 4-9 4-6 Stratification test results at economizer outlet . . 4-11 4-8 Correlation of NQX emissions with load 4-18 4-9 Wyodak furnace gas temperatures 4-22 A-l Air heater inlet continuous monitoring system . A-3 A-2 Internal construction of water-cooled suction pyrometer probes . A-6 A-3 Suction pyrometer tip construction ..... A-7 B-l EPA EMSL coal audit sulfur analysis B-6 B-2 EPA coal audit ash analysis B-7 B-3 EPA EMSL coal audit heating value analysis B-8 ------- LIST OF TABLES Table Page 2-1 Boiler Descriptions . ........ 2-2 2-2 Burner Operating Characteristics. . 2-3 3-1 Comanche Plant Unit 2 Boiler Specifications ..... , 3-2 3-2 Wyodak Plant Unit 1 Boiler Specifications ..... 3-7 3-3 Wyodak Unit 1 Burner Settings 3-11 4-1 Average Emissions at Comanche Unit 2 December 7-12, 1984. .... 4-3 4-2 Summary of Stratification at Economizer Outlet. . 4-12 4-3 Average Emissions at Wyodak Unit 1 January 31 - February 14, 1985 4-14 4-4 Comparison of NO Measured by Continuous Monitoring System and EPA Method 7 Samples at Economizer Outlet .......... 4-16 4-9 Effect of Sootblowing 4-23 A-l Continuous Gas Analyzers—Air Heater Inlet A-4 A-2 Coal and Ash Analyses A-8 B-l Continuous Monitors Relative Accuracy Calculation 12-11-84 Comanche. ............. B-3 B-2 Continuous Monitors Relative Accuracy Calculation Wyodak 2-4-85 ........ . B-4 vn ------- 1.0 INTRODUCTION Field evaluations to determine the emission characteristics of Babcock & Wilcox (B&W) circular and dual register burners were conducted by Energy and Environmental Research {EER) Corporation. These evaluations were part of a burner development program conducted by B&W and EER for the U.S. EPA. This burner development program involved the integration of the EPA distributed mixing burner concept with commercial B&W hardware. The performance and emissions of the distributed mixing burner were evaluated in the Large Watertube Simulator, a full-scale burner test facility. B&W circular and dual register burners were also evaluated in the LWS. The objective of the field evaluation was to develop a correlation between the test results of the circular and dual register burners in the LWS and in the utility boilers. This correlation could then be used to extrapolate the performance and emissions of the di stri buted mixing burner to a 1 arge scale utility application. Field testing was conducted at two boilers, one equipped with the circular burner and one with the dual register burner. The boilers were selected by B&W to be comparable in terms of age, capacity, coal characteristics, and firing configuration. The circular burner was evaluated at the Colorado Public Service Comanche Generating Station, Unit 2 located in Pueblo, Colorado. The dual register burner was tested at the Wyodak Generating Station, Gillette, Wyoming, owned by Pacific Power and Light Company and the Black Hills Power and Light Company. Testing was conducted for one week at Comanche in December 1984 and for two weeks at Wyodak in February 1985. Section 2.0 presents a summary of the field test results. The boilers and test plan are described in Section 3.0. Detailed results are included in Section 4.0. The appendices include test procedures, data, and quality assurance. 1-1 ------- 2.0 , SUMMARY Table 2-1 shows the characteristics of the two boilers tested. Both boilers fire subbi tumi nous coal and use a front and rear wall firing configuration. The front and rear wall burners at the Comanche boiler are directly opposed with four rows of four burners each. The front and rear wall burners at Wyodak are offset to avoid flame interactions and are arranged in five rows of three burners each. The boilers have comparable furnace cross-sectional dimensions, but the Wyodak boiler has a taller furnace to accommodate the five burner rows. Thus, the Wyodak furnace has a lower ratio of firing rate to cooled surface area (HA/SC). During testing, the boilers were generally operated in a normal fashion by the operators without interference from EER. Thus, the burner settings, load, and excess air were controlled by plant personnel. The overfire air N0X ports were closed during the day at the Comanche boiler at the request of EER, and returned to their normal open position of 18 percent at night. Table 2-2 shows the typical burner settings and flame characteristics during the tests. Both the circular and dual register burners operated satisfactorily during the tests. Exact flame lengths could not be determined with the available observation ports. Both burners showed a high combustion efficiency and large imbalances of fuel or air distribution were not observed. Both boilers operated over a narrow excess 02 range, 2.5 to 3.5 percent at Comanche and 3.8 to 4.0 percent at Wyodak. Thus, the data were not sufficient to establish NQX emissions as a function of excess 02- Figure 2-1 shows N0X emissions at the two boilers as a function of load. Both correlations show a similar slope, with lower emissions for the dual register burner at Wyodak. Nominal N0X emissions with the circular burner at Comanche were 550 ppm at 0 percent O2 (0.64 lbs/106 Btu). Full load emissions at Wyodak with all mills in service were 395 ppm at 0 percent 02 (0.46 lbs/10® Btu). More detailed test data are presented in Section 4.0. 2-1 ------- TABLE 2-1. BOILER DESCRIPTIONS 1 UNIT COMANCHE UNIT 2 WYODAK UNIT 1 UTILITY COLORADO PUBLIC SERVICE PACIFIC POWER & LIGHT BLACK HILLS POWER & LIGHT BOILER MANUFACTURER B&W B&W YEAR OF INITIAL OPERATION 1976 1978 GROSS GENERATING CAPACITY 35d MWe 350 MWe TYPE OF BURNER B&W CIRCULAR B&W DUAL REGISTER NO. OF BURNERS 32 30 NO. OF MILLS 5 BURNER ARRANGEMENT W x 4H ON FRONT & REAR WALLS 3W x 5H ON FRONT & REAR WALLS FURNACE DIMENSIONS 43'W x 45'D x 161'H 46'W x 15'D x 180'H COAL TYPE SUB BITUMINOUS SUB BITUMINOUS ADDITIONAL FEATURES 8 NOx PORTS SEALED N0X PORTS OPPOSING BURNERS OFFSET COMPARTMENTED WINDBOXES ------- TABLE 2-2. BURNER OPERATING CHARACTERISTICS UNIT COMANCHE WYODAK BURNER TYPE CIRCULAR DUAL REGISTER TYPICAL BURNER SETTINGS BOTTOM BURNERS-REGISTERS 50% OPEN TOP BURNERS -REGISTERS 100% OPEN OUTER REGISTERS 50% 'OPEN INNER REGISTERS 25-50% OPEN SWIRL VANES 45% OPEN FLAME CHARACTERISTICS LONG AND NARROW 0-2 FT STANDOFF LONG AND NARROW 35 - 44 FT LONG 0.5-3 FT STANDOFF ------- Load MWe Figure 2-1. NO^ emissions vs. boiler load. ------- 3.0 BOILER DESCRIPTIONS AND TEST PLAN Characteristics of the Comanche boiler are included in Section 3.1. The Wyodak boiler is described in Section 3.2. The Test Plan for the evaluation of both boilers is described in Section 3.3. 3.1 Description of Comanche Unit 2 Comanche Unit 2 is a horizontally opposed wall fired balanced draft utility boiler manufactured by Babcock & Wilcox. The boiler is located via Pueblo, Colorado and is operated by Public Service Company of Colorado. It has a maximum continuous operating capacity of 350 MWe with a steam flowrate of 2.54 x 10® Ibs/hr at 1005°F and 2500 psig from the superheater. The reheater outlet temperature and pressure are 1005°F and 555 psig. The boiler fi res a subbi tuminous coal with a higher heating value of 8400 Btu/lb and a moi sture content of 31 percent by weight as recei ved. The coal sulfur content is approximately 0.4 percent by weight as received. The characteristics of the boiler are summarized in Table 3-1. The coal for the boiler is ground in four pulverizers designated A, B, C and D. Each mill feeds eight burners. The burners are arranged in four rows of four burners each on two boiler walls. The unit is equipped with eight overfire air ports for N0X control. A single port is located over each of the top row burners. Secondary air is fed through three compartmentalized windboxes. One windbox feeds all the burners located in the lower two rows. Another feeds all burners in the upper two rows and a third windbox feeds all of the overfire air ports. The burners used on the unit are B&W high turbulence circular burners. These are the standard burners used on B&W pre-NSPS (New Source Performance Standards) units. Figure 3-1 shows the circular burner. Coal is supplied through a central coal nozzle. The coal is dispersed into the furnace by an impeller on the end of the coal nozzle. Secondary air flowrate and swirl to each burner are controlled by a single register. Figure 3-2 shows the burner settings during testing. These settings are normally not changed. Burners 3-1 ------- / ;• TABLE 3-1. COMANCHE PLANT UNIT 2 BOILER SPECIFICATIONS I Manufacturer Babcock & Wilcox Year in Commercial Operation 1971 Gross Electrical Capacity 350 MWe Fuel Pulverized Coal Subbituminous Burners Type B&W Circular Number 32 Configuration Horizontal, Opposed-Fired Array 4 Rows of 4 Burners on Front and Rear Walls Number of Pulverizers 4 Furnace Dimensions Width 43 ft Depth 45 ft Height 174 ft Design Efficiency 84.57% at Maximum Continuous Rating Steam F1owrate 2,540,000 Ib/hr at Maximum Continuous Rating Steam Pressure 2500 psig Superheat Temperature 1005°F Reheat Temperature 1005°F HA/SC Design 384 x 103 Btu/hr-ft2 Fiel d i 400 x 103 Btu/hr-ft2 3! -2 ------- ------- s.,-1 % % % Register Setting; 17 17 18 18 0 = Closed 18 = Open fa fa fa 18 % 17 18 ------- on both the front and rear wall are operated with clockwise swirl, as viewed looking at the burners, resulting in opposite rotation. The boiler is normally operated with the N0X ports open 18 percent to provide tempering air in order to prevent superheater fouling. During this test, the ports were closed during the day, but opened during the night. 3.2 Description of Wyodak Unit 1 Wyodak Unit 1 is a radiant reheat boiler manufactured by the Babcock and Wilcox Company (B&W). The plant is located near Gillette, Wyoming, and is owned by Pacific Power & Light Company and Black Hill Power & Light Company. Commercial operation of the plant began in 1978. The plant has a rated capacity of 330 MWe with a steam flowrate of 2,600,000 Ib/hr at 1800 psig and 1000°F. The boiler is equipped with two superheater banks, a pendant reheater, economizer, and regenerative air heater. A diagram of the boiler is shown in Figure 3-3 with key boiler specifications listed in Table 3-2. f The boiler fuel is pulverized subbituminous coal supplied from a mine near the plant. The coal has an average higher heating value of 8000 Btu/lb with 30 percent moisture and 8 percent ash. The sulfur content of the coal is consistently low at about 0.7 percent by weight. The boiler is equipped with B&W's dual register burner compartmentalized windbox firing system. This firing system was developed by B&W to control fuel and air mixing in the burner zone, thus reducing NCX emissions and enhancing complete combustion. The dual register burner (ORB), shown in Figure 3-4, consists of a central coal nozzle surrounded by two concentric secondary air passages. The coal nozzle incorporates a venturi to promote a uniform coal distribution. The venturi plug shown in Figure 3-4, had been f J ~ removed about one year prior to this test program at the Wyodak plant. The absence of this plug has apparently not compromised burner performance. Air flow distribution between the two secondary air passages and swirl generation is controlled by three devices: outer secondary air register, inner secondary air register, and inner secondary air axial spin vanes. The multiple air passages and the associated controls allow variation in the rate 3-5 ------- A> A uttit} rim Figure 3-3. General arrangement of Wyodak Unit 1. 3-6 ------- TABLE 3-2. WYODAK PLANT UNIT 1 BOILER SPECIFICATIONS r • Manufacturer Babcock & Wilcox Year in Commercial Operation 1978 Gross Electrical Capacity 350 MWe Fuel Pulverized Coal, Wyoming Sub- bituminous Burners Type B&W Dual Register Number 30 Configuration Horizontal, Opposed-Fired Array 5 Rows of 3 Burners on Front and Rear Walls Number of Pulverizers 5 Furnace Dimensions . Width 46 ft Depth 45 ft Height 180 ft Design Efficiency 83.921 at Maximum Continuous Rating Steam Flowrate 2,600,000 lb/hr at Maximum Continuous Rating Steam Pressure 1800 psig Superheat Temperature 1000°F Reheat Temperature 1Q00OF HA/SC Design (5 mills) 387 x 103 Btu/hr-ft2 j Field 330 x 103 Btu/hr-ft2 j 3' '1 -7 ------- Figure 3-4. Babcock & Wilcox dual register burner. ------- of fuel and air mixing, thereby controlling N0X emissions. The compartmented windbox separately controls the combustion air flow for the group of burners associated with each pulverizer. The compartmented windbox thus permits balancing the secondary air to each burner group in operation. Wyodak Unit 1 has 30 dual register, burners arranged in a horizontally opposed firing configuration, as shown in Figure 3-5. The 30 burners are arranged in five rows of three burners on both the front and rear walls. Opposing burners are offset avoiding direct flame tail interaction and promoting uniform heat release across the lower furnace. In addition, the top row of burners on both walls, supplied by D mill, is spaced 12 feet above the lower four rows of burners. During this two-week test period, no adjustments were made to the burner controls. The settings for each burner maintained during this test period are listed in Table 3-3. Each register control had 18 divisions, with notch 1 representing closed and notch 19 representing open. Thus, each division for the registers represents approximately five degrees of motion. The spin controls also have 18 notches, but there is a 2:1 gear ratio that permits 180° of travel; i.e., 0 to 90°CW and 0 to 90°CCW. It is general practice on this unit to have the spin vanes always in the same direction as the outer register. The predominant firing configuration for full load operation at Wyodak during this test was with D mill and the associated top row of burners out of service and all the other mills and burners in service. When a mill is taken out of service, the air flow to the idle burners is reduced to provide only flow to cool the burner components. With D mill out of service, the windbox compartment for burners D1-D6 is closed so that only about 10 percent of the total secondary air is supplied for cooling. The other additional configuration had C mill, which supplies burners C1-C6, out of service. These three cases allowed evaluation of the effect of firing pattern on boiler performance and emissions. ------- -/) -7 - - %, . 0 7e$\ ' io; K?s 0 -c^ Figure 3-5. Wyodak Unit 1 burner arrangement, ,3-10 ------- TABLE. 3-!3> WYODAK UNIT 1 BURNER SETTINGS Front-Wall Rear Wall Burner Outer Register Inner Register Spin Vanes* Burner Outer . Regi ster Inner Register* Spin, Vanes'* B1 7 B2 9 B3 7 B4 7 B5 8 B6 7 €1 9 C2 8 C3 9 C4 5 C5 5 C6 9 D1 10 02 9 D3 9 6 10 10 9 10 11 10 .10 10 10 10 11 2 4 3 3 3 3 ,A1 A2 A3 A4 A5 A6 El E2 E3 E4 E5 E6 : 04 D5 D6 9 10 9 9 9 8 9 10 10 10 10 11 10 10 10 9 10 10 9 10 10 3. 7 ' 5 4 4 ; 4 4 4 5 3 5 ^Notches Open--: ------- 3.3 Test Plan The field evaluations consisted of monitoring boiler performance for one week at the Comanche boiler and for two weeks at the Wyodak boiler. Testing at Comanche was reduced because additional data was available from previous testing by Exxon (Reference 1) for the EPA in 1977. During tests at both boilers, boiler operating conditions were established by the boiler operators. Figure 3-6 shows the field test plan for both boilers. Boiler operating condi tions and performance were monitored using plant instrumentation. Gaseous emissions of N0X> Og, CO, SO2, and CO2 were continuously monitored using a mobile test trailer. Sampling was performed at both boilers using an array of probes located at the air heater inlet. Coal and ash samples were collected from selected points throughout the boiler for analysis. Burner performance was assessed using observations of flame characteristics and evaluation of combustion efficiency as determined from ash analyses and CO emissions. The relative fuel/air balance to the burners was assessed by gas stratification measurements obtained at the air heater inlet. In addition, furnace gas temperatures were measured at Wyodak using a water-cooled suction pyrometer. Detailed descriptions of the test procedures are included in Appendix A. 3-12 ------- 1.0 BOILER DATA FROM PLANT INSTRUMENTATION • FUEL FLOWRATE • STEAM QUALITY AND FLOWRATE • WATER/STEAM TEMPERATURES AND PRESSURES • AIR/FLUE GAS TEMPERATURES AND PRESSURES • BOILER LOAD CYCLE • RANGE OF BURNER OPERATING CONDITIONS 2.0 EXHAUST GAS MEASUREMENTS BY EER • CONTINUOUS MONITORING OF NO. CO, C0?, 0?, SO2 AT AIR HEATER INLET X L c • PERIODIC ANALYSIS OF COAL AND ASH COMPOSITION COAL FEED FLY ASH AT AIR HEATER INLET BOTTOM ASH PARTICULATE COLLECTOR HOPPER 3.0 BURNER/BOILER PERFORMANCE • FLAME OBSERVATIONS • COMBUSTION EFFICIENCY FROM COAL AND FLUE GAS MEASUREMENTS • FURNACE GAS TEMPERATURE WITH WATER-COOLED PROBE AT WYODAK Figure 3-6. Field test plan. 3-13' ------- 4.0 TEST RESULTS 4.1 Results at Comanche Unit 2 Emissions testing of the B&W circular burner was conducted by EER at Comanche Unit 2 from December 7 through December 12, 1984. Gaseous emissions of N0X, 02» CO, SO2, and CO2 were continuously monitored during this period. The plant was operated in response to system demand. The N0X overfire air ports are normally partially open. At the request of EER, the ports were closed during the day, but opened at night. Otherwise the boiler operating condi tions were established by the plant operators. Emissions were measured at this unit by Exxon in 1977 as part of another EPA program. Exxon's results are compared to the results of the current test program. During the week of testing, boiler load varied from 150 to 360 MW. The trends for the daily averages of gaseous emissions and boiler load are shown ^ in Figure 4-1. The overall averages are summarized in Table 4-1. During a i portion of the testing the boiler was operated with mill A out of service. The A mill supplies coal to the upper two burner rows on the front wall. Excess O2 varied from only 2.5 to 3.5 percent Og. A brief series of tests was performed at 300 MW to assess the impact of the N0X overfire air ports on N0X emissions. N0X and CO emissions as a function of boiler load are presented in Figure 4-2. N0X emissions wi th all mills on and the overfire air ports ' closed showed the following correlation: N0X (ppm @ Q% 02) = (1.136)(Load, MW) + 1487? Nominal N0X emissions at full load of 360 MW were 550 ppm § 0 percent O2. corresponding to 0.64 lbs/10® Btu. These emissions are substantially lower than the N0X measured by Exxon of 847 ppm @ 0 percent O2 (0.99 lbs/106 Btu). The Exxon data were obtained at a higher excess O2 level, 5.2 percent compared to 2.7 percent, however. Operation with the A mill out of service resulted in a slight decrease in N0X emissions. This result could be due to 4-1 ------- j DUU i 400 : 300 i 200 ; 100 i 0 500 400 300 4 3 2 400 350 300; 250 200 l \ = J L. 10 11 12 AVG SD 368 51.73 AVG SD 19.32 0.16 233/2 89.8 385.5 44.4 3.15 0.27 \|AVG ;=.-275.2 , ! SD T 32^7, " DEC 4-1. Daily averages of gaseous emissions--Cornanche Unit 2. ~4-2~ ------- TABLE 4-1. AVERAGE EMISSIONS AT COMANCHE UNIT 2 DECEMBER 7-12, 1984 Species Average Concentration Measured 0 0% 02 lb/106 Btu °2 3.15% __ — NOx 328 ppm 386 ppm 0.45 so2 313 ppm 368 ppm — CO 198 ppm 233 ppm — C02 16,4%, 19.3% — — i 4-3 ------- ——I 1 1 1 r ~ Mill 2A OOS ON, OFA CLOSED 3.1 - 3.4%0 800 700 600 O All Mills ON, OFA CLOSED 2.5 - 2.7% 0; O All Mills ON, OFA CLOSED 3.2-3.4%^ u2 "A Exxon-NO OFA 5.2%02 5.6%02 ~ All Mills ON, OFA CLOSED 3.5-4.0% 0 E CL CL 500 i "i >> i- o CM O O 400 300 200 100 _L I ± ± 60 120 180 240 Load MW Figure 4-2. 300 360 NO and CO vs X 350 - 300 - S 250 >> j- ™ 200 x o S 150 100 - 50 - 60 120 180 240 Load MW 300 360 load - Comanche Unit 2. ------- a decrease in the ratio of firing rate to cooled surface area or to a degree of combustion staging. Here, combustion staging refers to operation with the burner zone at a lower stoichiometry and with the addition of combustion air above the burner zone. The latter conclusion is supported by the measured CO emissions and by the operating excess air level. With all coal mills (and burners) in service, combustion efficiency was typical ly high, as indicated by low CO emissions in the range of 50 to 60 ppm. However, operation with the A mill out of service resulted in increased CO emissions of up to 500 ppm. Increased CO emissions would be consistent with a decrease in combustion efficiency due to relatively poor fuel /air mixing that could be associated with a degree of combustion staging occurring with the A mil 1 off. In addition, the boiler operating excess air level was generally not increased when the A mill was taken out of service. Since the idle burners would need to be supplied with cooling air, operation at a constant excess air level would result in a lower burner zone stoichiometry with the A mill out of service, resulting in a degree of combustion staging. Figure 4-3 shows N0X and CO emissions vs. excess 02 at a constant load of 253 to 273 MW. In' general , the data taken during the current test do not have enough variation in O2 level to indicate a trend. However, comparing the current data with the previous Exxon data would suggest a strong dependence of N0X on excess O2 • This is typically the case with subbituminous coals as indicated in LWS tests. Exhaust gas composition was measured using an array of 12 probes in the two exhaust ducts upstream of the air heater. "Hie gas compositions at each sampling location were measured on December 10 and 11, 1984 to determine gas stratification. In wall-fired boilers, gas stratification measurements upstream of the air heater can typically be used to evaluate the side to side balance of fuel and air to the burners. Figure 4-4 shows the results of the stratification measurements at Comanche. Although some variation in O2 and CO levels is evident, no consistent imbalance between the two ducts or within each duct can be seen from these data. Thus, adjustment of the burners to improve the air/fuel, balance would be expected to result in only a minor improvement in combustion performance. ------- I CTl 800 700 600 — 500 £? ¦o O Mi Tl 2A 00S" - 261-273 MW-OFA" Open 1 . Q Mill 2A 00S - 257-267 MW-OFA Closed O All Mills On - 252-269 MW-OFA Closed A Exxon Data - All Mills On, OFA Closed 275MW A 400 o S 300 200 100 Q CP excess 0,,,% -S Figure 4T3?r Comanche Unit 2 - NO and CO vs. excess 09 at a load of 253-273 MW A L C ------- 12-10-84 A of b 'ppm ppm- 3.29 4.59 2.89 5.24 4.74 2.49 504 480 350 379 400 306 36 77 186 94 129 - 2.99 3.26 3.74 ^ ¦ 4 3:74" 478 420 335 iff- '? 1340 :• 35 59 416 187;! ( > 228? ?./. '122] ; / Avg 02 3.46 ri Avg 02 3.61% 12-11 < 00 1 B 3.73 2.67 4.72 2.00 1.92 2.52 517 476 451 475 473 426 84 91 102 43 43 56 4.12 2.57 3.55 4.02 2.17 2.87 454 479 457 483 446 417 49 45 42 48 145 57 Avg 02 3.561 i i \| I Avg 02 2.58% Figure 4-4. Comanche gas stratification test. ------- Figure 4-5 shows the effect of opening the overfire air ports on N0X and CO emissions. Opening the ports resulted in a substantial decrease in N0X emissions. This trend is similar to that seen during the Exxon testing, except that no decrease in N0X was observed until the ports were opened more than 30 percent. Evidently the back lash in the mechanical linkage resulted in the ports not actually opening until the indicator was past 30 percent. Thus, although the plant normally operates with the ports 18 percent open, they may actually be closed. Unlike the results seen during the Exxon tests, however, opening the overfi re air ports resulted in a large increase in CO emissions, to over 800 ppm at the maximum opening, indicating a substantial decrease in combustion efficiency. 4.2 Results at Wyodak Emissions and boiler performance were monitored at the Wyodak plant from January 31 to February 14, 1985. During this test period, the unit was operated based on normal practice following system demand. The boiler was essentially base loaded through the test program with only brief load variations. A short boiler outage occurred between February 7 and 10, for necessary boiler repairs. The primary objective of the test program was to characterize the performance of B&W Dual Register Burners in a typical utility boiler. The burner performance was determined based on CO emissions, flame character!"sties, and efficiency. Emissions measured included continuous moni toring of N0X, CO, O2, CO2 and SO2* Visual observations were made through available inspection ports to determine flame characteristics to the extent possible. Combustion efficiency was determined by analysis of unburned carbon content in fly ash samples and measurement of CO emissions. In addition, the overall boiler efficiency was determined based on calculation of the heat rate during the test period. ------- OFA Ports (% Open) (OFA Ports (% Open) Figure 4-'5. Effect of overfire air port damper position on" emissions- Comanche. ------- 4.2.1 Emissions Emissions were monitored at the economizer outlet of Wyodak Unit 1. The gaseous species monitored included O2, CO, COg. N0X and SO2. A continuous emissions monitoring system was used to measure the gaseous species with an array of eight probes. Four probes were placed in each of the two ducts leading from the economizer to the air heater to ensure a representative sample. The gas sample flow rate was balanced to provide an equal sampling rate through each of the eight probes. In addition, each of the probes was monitored individually at a typical operating condition during the test period to determine the presence and extent of stratification of the gas stream. The gas stratification test was conducted on February 6 between 9:30 to 11:00 AM with the unit running at 360 MWe gross output and with D mill out of service. The results of this test are shown in Figure 4-6 and summarized in Table 4-6. The concentration profiles of 0?, N0X, and CO shown in Figure 4-5, indicate that the gas concentrations are slightly higher in the west duct. Previous tests at other boilers have shown that burner-to- burner imbalances in fuel or air flow result in non-uniform gas concentrations across the width of the boiler. Thus, slight burner-to-burner flow imbalances may account for the differences measured during the stratification test. Averaged concentrations for the two ducts are compared with gas concentrations from balanced sampling with all . probes before and after the individual probe stratification test in Table 4-2. Again, the O2 concentration in the west duct was siightly higher than measured in the east duct. Associated with the higher oxygen concentration in the west duct are higher N0X emissions. This is an indication that careful control of excess air and proper balances of fuel and air, from burner to burner is beneficial in reducing overall N0X emissions. Differences between averaged concentrations from the two ducts and balanced probe sampling are about 5 percent, which is within the fluctuations typical of normal boil er operation. ; 4-10: ------- West Duct East Duct o2 <) N0X (ppm) Measured -• (0 0% o2l— 271 263 (344) (333) 267 279 (335) (365) 4.48 4.43 4.28 4.97 271 254 (334) (300) 267 244 (342) (300) 3.98 3.23 4.64 3.96 CO (ppm) Measured 33 35 {% 0% o2) — (41) (45) 58 40 (73) (52) 35 34 (43) (40) 29 31 (37) (38) Figure 4-6. Stratification test results at economizer outlet. f 4-11 ------- TABLE 4-2. SUMMARY OF STRATIFICATION AT ECONOMIZER OUTLET Sample ?2. >) NOx (ppm ® Of O2 3 CO [ppm 0 0% O2) Average West Duct Average East Duct Average Both Ducts All Probes Balanced 4.54 3.95 '4.24 4.03 344 319 331 318 53 40 46 51 ------- Hourly averages of the gaseous emissions were calculated from the continuous monitoring data. These hourly averages are tabulated in Appendix C-3. The hourly averages were used to calculate daily and overall averages for the test period. The overall averages of measured gas concentration for the test period are summarized in Table 4-3. These values represent essentially base-loaded operation, with only about four hours of reduced load operation during the test period. The N0X emission rate of 0.40 lb/10® Btu is below the Federal New Source Performance Standard of 0.5 lb/106 Btu for subbituminous coal-fired boilers. The trends for the daily averages of gaseous emissions and boiler load are shown in Figure 4-7. A short boiler outage occurred between February 7 and 10 during which time no emissions data was collected. The plant load it" averaged 358 MWe during the test period when in operation, with only 1 J- 1 percent relative deviation. Close control was maintained on the operating excess air level, indicated by 2.5 percent deviation from the average of 4.03 percent O2 measured in the flue gas. CO emissions were low throughout the test period and averaged about 51 ppm. The variations in CO measured at this low level are generally considered to be insignificant. The CO2 and SO2 emissions, which are directly related to the coal composition, also showed variations that were generally small. Gaseous emissions, including N0X emissions, were monitored primarily with continuous analyzers. In addition, N0X emissions were measured following ERA Method 7 procedures on one day during the test period to verify the accuracy of the continuous monitors. The results of the EPA Method 7 sampling are summarized in Table 4-4 with details included in Appendix B: Quality Assurance. The discrete Method 7 samples are compared with the continuous monitor responses in the table. Each Method 7 value represents a set of three discrete samples while the continuous monitor value is time averaged during the Method 7 sampling period. The agreement between the two measurement techniques is good. The continuous monitors were within about 13.7 percent, including 95 percent confidence interval, of the EPA standard method. 4—13 ------- TABLE 4-;3^ AVERAGE EMISSIONS AT WYODAK UNIT 1 v' JANUARY 31 - FEBRUARY 14, 1985 ' Average Concentration Species Measured @ 01 02 lb/10® Btu °2 4,03% __ — NOx 278 ppm 344 ppm 0.40 SO 2 584 ppm 723 ppm 1.17 CO 42 ppm 52 ppm 0.03 C02 15.7% ' 19.4% 216.7 4-14 ------- Boiler Outage so2 5 0% 02 (ppm) CO2 0 0% 0^ (ppm) CO 9 0% 0- (ppm) N0X @ OS 0, (ppm) (2i Boiler 'Load; (MWe) 1200 1100 900 700 500 300 20 19 18 100 80 60 40 20 0 400 300 200 5 —1 1— T —1 1 n 1 1— —1 T —r T t AVG = 723 •rr - SD = 153 1 i 1 _i 1 1 1 1 1 1 JL. 1 1 ¦ 400 380 360 340 320 300 1 r t Jk T wMm i ) 1 1 1 r IJSLSLJSiiiiSS^ JL _1_ _1_ _1_ 31 JAN 6 FEB AVG = 19.35 SD = 0.12 AVG = 51.5 SD = 13.3 AVG SD 344.5 22.6 AVG SD 4.03 0.10 AVG SD 358.1 5.3 10 11 12 13 14 Figure 4-7. Daily averages of gaseous emissions. ;4-^5, ------- TABLE 4-4:. COMPARISON OF NOx MEASURED BY CONTINUOUS MONITORING SYSTEM AND EPA METHOD 7 SAMPLES AT ECONOMIZER OUTLET Date Time / NOv @ 0% 02, dry * Method 7 CMS 2-4-85 1603 358 395 2-4-85 1612 368 397 2-4-85 1616 368 400 2-4-85 1623 357 405 ------- N0X emissions at Wyodak were sensitive to burner firing arrangement and boiler Toad. These effects are shown in Figure 4-8. The data are averages of hourly emissions for three firing configurations. The primary " configuration at Wyodak has the D mill out of service. The D mill supplies the top row of burners on both the front and rear walls. The two other firing configurations were: (1) all mil 1s and burners in service and (2) "C" mill out of service. The burners supplied by C mill are the second and third rows from the top on the front wall. Operation with the D mill out of service resulted in the lowest average N0X emissions {344 ppm at nominal full-load operation), while operation with all mills and burners in service resulted in the highest N0X emissions (395 ppm at nominal full-load operation). An intermediate level, of NOx emissions was produced with the C mill out of service. These results are somewhat surprising since operation with the D mill out of service produces the highest HA/SC ratio. In general, the effects of the boiler firing configuration on N0X emissions could be due to slight variations in the burner operating stoichiometry (combustion staging) or to changes in the burner flame length and, consequently, changes in the degree of flame confinement and flame-to-flame interactions. Since the excess air level was similar for operation with all mills in service and for operation with the C mill out of service, the burners in the latter case could have been operating at a slightly lower stoichiometry, resulting in a decrease in burner N0X emissions. However, when the D mill was taken out of service, the boiler was operated at a higher excess air level. This result is consistent with the standard B&W practice of increasing the operating excess air level as a result of supplying additional air to cool the idle burners. Therefore, it is likely that the burners were operating at the design stoichiometry. Since operation with the D mill out of service would have required the burner throughput to increase, it is possible that the flame length could have changed. As indicated by the results of the LWS burner studies, N0X production from the dual register burners correlates directly with flame length. In addition, variations in the boiler firing configuration and burner flame length would be expected to influence the boiler flow patterns and flame-to-flame interactions and could possibly account for the variations S4-T7 i ------- ~ ALL MILLS IN SERVICE A C MILL OUT OF SERVICE O D MILL OUT OF SERVICE ERROR BARS SHOW 95% CONFIDENCE INTERNAL 0.50 0.45 0.40 NOx = 1.043(Load)-29. 0.35 Figure 4-'8. Correlation of N0X emissions with load. 0.30 0.25 200 250 300 Boiler Load (MW , Gross) e 350 400 ------- i n N0X emissions. Although thi s analysis is simplistic, these results do indicate the importance of burner arrangement and firing configuration on burner performance. Limited data were obtained at reduced loads with D mill out of service. For typical coal-fired boilers, N0X increases with load due to increasing combustion intensity and fuel/air mixing rates. As shown in Figure 4-8, N0X emissions correlate essentially linearly with boiler load. Least square linear regression yields the following correlation for operation with the D mill out of service: N0X (ppm @ 01 02) = 1.043 x Load (MWe) - 29.6, while the correlation obtained for all data taken during the field test was: N0X (ppm 0 0% 02) = 1.25 x Load {MWe) - 77. These relationships only apply over the small range of excess air levels at which the boiler operated during this field test. 4.2.2 Boiler Performance Boiler performance during the field evaluation was monitored using the plant instrumentation and measurements performed by EER. Boiler performance parameters of interest included: 1. Coal characteristics 2. Mill performance 3. Burner performance • Air/fuel mixing • Flame characteristics • Combustion efficiency • Burner pressure drop 4. Boiler heat rate 5. Furnace gas temperatures The Wyodak plant is typically base loaded and operates almost continuously at full load of about 360 MW gross. During the two week test period, the plant 4-19 ------- experienced no significant operating problems and operated at full load with the following brief exceptions; 1. Two day outage on February 8 and 9, 1985. 2. Three hour outage on February 12, 1985 caused by an electrical disturbance in the power distribution system unrelated to station operation. 3. Five hours of low load operation at 275 MW on February 13, 1985 at the request of EER. 4. Two hours of operation at 325 MW on February 14, 1985 at the request of EER. Wyodak uses Powder River Basin coal , which is mined locally. The coal has a low sulfur content with approximately 30 percent moisture and a higher heating value of 8000 Btu/lb. Coal moisture, ash, sulfur and heating value are monitored daily by the station. These results and coal analyses by EER are presented in Appendix C. With the exception, of sulfur content, coal properties did not vary substantially during the test period. Coal sulfur varied from about 0.3 to 0.7 percent, as received. The boiler is equipped with five mills, but can operate at full load with only four mills in operation. During the majority of the test period, the plant operated with the D mill out of service. The D mil 1 supplies coal to the top row of burners on both the front and rear walls. The boiler operated with the C mill out of service during February 4 and 5, 1985 to allow repairs on the C mill. The boiler also operated will all mills in service during the brief periods while the C mill was taken offline and brought back online. Mill performance was satisfactory during the test period. Coal fineness test results provided by the station showed fineness to vary from 68 to 85 percent less than 200 mesh. Detailed fineness results are included in Appendix C. ------- Burner performance with the dual register burners was satisfactory throughout the test program. Air/fuel distribution between burners was relatively uniform, as shown by flame observations and by variations in excess O2 concentrations in the exhaust duct prior to the air heater. Flame observations showed the flame shapes to be uniform and stable for all burners. Exact flame length was difficult to evaluate due to the lack of observation ports in the middle of the furnace side walls. Flame lengths appeared to be relatively long, however, extending from 1/2 to 3/4 of the distance across the furnace. The burners on the front and rear walls are offset to minimize flame interactions. Combustion efficiency was very high, as measured by carbon in the fly ash and CO emissions. Carbon in the ash averaged 0.16 percent, corresponding to a carbon utilization of 99.98 percent. Ash analyses are included in Appendix C. Carbon monoxide emissions were stable, averaging less than 60 ppm. Overall boiler performance and electrical generation efficiency were measured in terms of the gross plant heat rate, the ratio of fuel heat input to gross electrical production {Btu/kw hr). The average heat rate during the test period was 10,236 Btu/kw hr compared to the design heat rate of 10,177 Btu/kw hr. Thus, overall boiler performance was satisfactory, with efficiency very near to design conditions. Upper furnace gas temperatures were measured during full load operation using a water-cooled suction pyrometer. Figure 4-9 shows the range of temperatures measured. The furnace exit temperature at the inlet to the superheater pendants varied from 1120 to 1359°C. The temperatures at the bottom portion of the superheater are above the ash fusion temperature of about 1200°C, and thus some buildup of ash/slag deposits could be expected in this region. However, fouling of the superheater tubes was not observed to be a significant operational problem during testing. The impact of sootblowing on furnace gas temperatures was evaluated during testing. The results shown in Table 4-9 show sootblowing to have very little effect on gas temperatures. 4-21 ------- Figure 4-9. Wyodak furnace gas temperatures. ; 4-\|2 ------- TABLE 4-9. EFFECT OF SOOTBLOWING Port Distance Into Furnace Temp.oc Before Blowlng Temp.°C After Blowing Sootblowing Location 10W 9-1/2W 9-1/2W 9-1/2W 9-1/2W 9-1/2W 12' 16' 20' 12' 16' 20' 1120 1416 1384 1377 1324 1383 13541 ¦ 1345 • 1402' 1120 1370 1351-62 1315-32 1370 1351-62 1315-32 Furnace Front of Superheater Front of Superheater Front of Superheater Air Heater i 4-2 3 ------- 5.0 REFERENCE 1. Manny, E, H. and A. R. Crawford. Control of Utility Boiler and Gas Turbine Pollutant Emissions by Combustion Modification - Phase II. EPA-600/7-81-039 (NTIS PB 81-222267), March 1981. 5-1 ------- APPENDIX A TEST PROCEDURES A-1 ------- Measurements performed by EER included the following; Flue gas composition of N0X > Og, CO, SO2» and CO2 by continuous monitors • Coal and ash composition • Furnace gas temperatures by suction pyrometer Flue Gas Composition The flue gas composition (N0X, CO, CO2, O2, and SO?) was monitored with continuous analyzers at the inlet of the air heater. Figure A-l shows a /v /. schematic diagram of the monitoring system at the air heater inlet. The gas sample was obtained with eight sample probes. The gas sample flow rate from each probe is controlled with a glass rotameter to ensure equal flows through each probe. In addition, sampling can be conducted through one probe at a time to determine stratification of the gas concentrations. All components of the sample system upstream of the moisture condenser are heated. A separate sample stream for the SO2 analyzer is dried with a Perma Pure drier. Moisture is removed from the condenser frequently using solenoid valves and a timer to minimize contact of moisture and the sample. All components of the system are stainless steel, Teflon, or glass to minimize possible reactions with the sample. The continuous monitoring instrumentation is listed in Table A-l. ^ ^ / Furnace Gas Temperature Furnace gas temperatures were measured using a water-cooled suction pyrometer. A suction pyrometer was used due to the inaccuracies in high- temperature measurements caused by radiation loss from standard thermocouples. The suction pyrometer consists of a high-temperature thermocouple in a ceramic shield. A high flow rate of furnace gas is withdrawn through the shield and over the thermocouple so that convective heat transfer dominates, reducing the errors caused by radiation losses to an insignificant level. An air ejector is used to aspirate furnace gas. The ¦ A-2 • ------- Figure A-1. Air heater inlet continuous monitoring system. ' IX-3 ------- TABLE A-1. CONTINUOUS GAS ANALYZERS — AIR HEATER INLET GdS Mea- sured Detection Principle Manufacturer Model No. Range Nominal Calibra- tion Gas Level 02 Paramagnetic Taylor 0A570 10% 8% S02 Pulsed Fluorescence A J TECO _ 40 1000 ppm 800 ppm N0X Chemiluminescent TECO 10AR 1000 ppm 800 ppm CO Nondispersi ve Infrared ANARAD AR500R 500 ppm 400 ppm C02 Nondi spersi ve Infrared ANARAD AR500R 25% 22.5% ------- gas flow rate is monitored with a calibrated orifice to ensure an adequate gas velocity over the thermocouple. Temperatures are measured with K or S type thermocouples. Figure A-2 shows the design of the suction pyrometer probe. Figure A-3 shows the construction of the pyrometer tip. Coal and Ash Characteristics Samples of coal and ash were collected throughout the test program to determine chemical composition and physical characteristics. Coal samples were collected on a daily basis. Ash samples were obtained from the bottom hopper of the boiler, the precipitator hopper, and the high volume particulate sampler during the field tests. Solids analytical procedures are listed in Table A-2. A-5 ------- Water Out Thermocouple Pressure Taps Swagelock fitting Suction Pipe Tubes of same length with Identical bends Expansfon Joint Figure A-2. Internal construction of water-cooled suction pyrometer probes. ------- Inner Ceramic Shield Figure A-3. Suction pyrometer tip construction. r ------- TABLE A-2. COAL AND ASH ANALYSES Parameter Analytical Procedure -Samples - • tdi'b'e,- Analyzed Coal Ash Proximate Analysis Volatiles, Fixed C, Ash ASTM D 317 2 X Heating Value ASTM D2015 X Ultimate Analysis C, H, N» Ash, S ASTM D3176 X Ultimate Analysis C, H, N, Ash Perkin Elmer 240b Analyzer X X Sulfur Leco SC 32 Sulfur Analyzer X X Ash ASTM 03174 X X A-8 ------- APPENDIX B QUALITY ASSURANCE ------- Exhaust gas composi tion was measured using continuous monitors at the air heater gas inlet. This location was selected to allow flue gas stratification to be measured prior to dilution and mixing by the air heater. Routine quality control procedures included daily leak checks of the sampling system and calibration of the analyzers using standard compressed gas certified by the manufacturer to have an accuracy within 2 percent of the stated value. Replicate calibrations were monitored as a measure of instrument precision. Precision was generally less than 2 percent. Data were corrected for instrument drift for the few occasions that precision exceeded 2 percent. The relative accuracy of N0X. 02 and CO2 was evaluated using wet chemical analyses using EPA Reference Methods. NQX concentrations were determined using grab samples collected in glass sample flasks in accordance with Method 7. Sampling was performed by EER and the analysis was performed by Truesdail Laboratories. Truesdail also analyzed the grab samples for CO2 and Og using Method 3. Results of the relative accuracy measurement are shown in Tables B-l and B-2. Relative accuracy of the N0X emission rate in terms of lbs/106 Btu were well within the EPA performance specifications for continuous monitors of 20 percent. Some of the data for N0X, Oj, and CO? on an as measured basis showed substantial differences compared to the continuous monitors. Those differences are due to gas stratification in the exhaust ducts. The Method 7 flasks obtain a grab sample at a single location over a period of a few seconds. Each of the twelve flasks collected at each boiler were obtained at different points in an attempt to obtain a representative sample. As can be seen in Table B-l, flasks collected in the west duct showed an Og concentration very close to the monitors, while the east duct samples showed a large difference, apparently due to variations in O2 concentration between the two ducts. This variation was the cause of the apparent poor relative accuracy for O2- Similar results were seen in Table B-2. Although the overall N0X emission rate showed good instrument accuracy, the N0X and O2 concentrations showed poor accuracy apparently due to gas stratification at the sample points. B-'2! ------- TABLE B-1. CONTINUOUS MONITORS RELATIVE ACCURACY CALCULATION 12-11-84 COMANCHE Time N0X (ppm) °2 (%) C02 U) N0X (lbs/106 Btu) RM AVG RM M DIFF RM M DIFF RM M DIFF RM M DIFF 0902 — 4 2 2.2 2- 65 0.45 16.7 17 .02 0.32 X 0904 366 \ 420 2 3.6 0.95 16.3 0.72 I 0.567 0.564 0.003 0907 473 ) 2.7 0.05 16.4 0.62 ) 0912 431 \ 2.3 0.35 16.6 0.42 \ 0915 456 I 410 12 2.1 0.55 17.0 0.02 > 0.540 0.564 0.024 0923 342 ) ' 2.8 0.15 16.2 t 0.82 ) 1003 411 ) 3? )4 5.7 2. 62 3.08 14.6 16 .53 1.93 ) 1006 410 > 407 13 3.9 1.28 15.3 1.23 i 0.614 0.525 0.089 1008 399 ) 4.7 2.08 14.8 1.73 ) 1012 337 \ 4.2 1.58 14.9 1.63 ) 1021 411 > 377 17 4.3 1.68 14.9 1.63 \ 0.562 0.525 0.037 1023 384 ) - ' 5.2 r 2.58 14.9 1.63 ) Avg 404 11 3-6 1.23 15.7 1.06 0.571 0.038 Confidence Coefficient 10 0.63 0.41 0.058 Relative Accuracy 5.2 51.7 9.4 16.8 Grab Samples From West Duct Grab Samples From East Duct ------- TABLE B-2. CONTINUOUS MONITORS RELATIVE ACCURACY CALCULATION WYODAK 2-4-85 NOx (ppm) 02 (%) C02 (%) N0X (lbs/10® Btu) Time RM Avg RM M DIFF RM M DIFF RM M DIFF RM M DIFF 1603 287 ) 5.3 3. 78 1.52 14.8 15. 58 0.78 ) 0.461 > 283 324 41 > 0.415 0.046 1609 279 ) 3.3 0.48 15.8 0.22 ) 1614 290 ) 5.5 1.72 15.6 0.02 \ 1616 283 > 292 32 3.6 0.18 14.0 1.58 > 0.431 0.030 1617 304 J 4.1 0.32 14.9 0.68 ) 1620 279 ) ' 4.6 0.82 15.3 0.28 ) > 292 32 > 0.430 0.031 1620 304 ) 4.1 0.32 14.9 0.68 ) 1623 261 ) 5.5 1.72 14.7 0.88 ) 1625 279 > 275 49 5.3 1.52 14.9 0.68 > 0.417 0.044 1626 284 ) 3.7 r 0.08 15.3 f 0.28 ) Avg 285.5 38.5 4.5 0.87 15.0 0.61 0.423 0.038 Confi dence Coefficient 13.0 0.49 0.32 0.013 Relative Accuracy 18.0 30.2 6.2 12.1 ------- Quality assurance of the solids analysis by EER and Hagen includes analyses of audit samples provided by the EPA EMSL for coal. Figures B-l, B-2, and B-3 show the results of these analyses in terms of quality control charts. ";t-S ------- ACCURACY QUALITY CONTROL CHART A QA Goal O EER A Hazen Results for samples with lower sulfur content are shaded Median of A11 Labs High Sulfur Concentration Low Sulfur Concentration J i i I I I I—i Date 3/^ 9/g2 3/83 9/83 3/84 %4 3/85 9/85 3/86 Figure B-1. EPA EMSL coal audit sulfur analysis. ------- i—i—i—I—i—i—i—i—r O ACCURACY QUALITY CONTROL CHART 15 10 -5 10 o J I I L J I —I L A hazen O eer MEDIAN ALL PARTICIPANTS RESULTS FOR SAMPLES WITH LOWER ASH CONTENT SHADED qA GOAL o & 9 — QA GOAL 3/82 9/82 3/83 9/83 3/84 9/84 3/85 9/85 3/86 DATE Figure B-2. EPA coal audit ash analysis. ------- ACCURACY QUALITY CONTROL CHART 1 1 1 1 1 1 1 1 1 O 1st Sample (~1 2nd Sample Analysis by Hazen Research, Inc. i 5 - — 4 - - 3 0 - QA Goal - >> (J n) J- 1 n - o n n o - u u c -1 - ~ o B ~ g Q - 4-» n) 0) ct -2 -3 R QA Goal -4 1 LJ -5 I ¦ ~ 1 1 1 1 l I l 3/82 9/82 3/83 9/83 3/84 9/s4 3/85 9/85 3/86 Figure B-3. EPA EMSL coal audit heating value analysis. ------- REPORT Truesdail Laboratories, Inc. CHEMISTS - MICROBIOLOGISTS R C9 EAM C » CLIENT SAMPLE DEVELOPMENT ENGINEERS - tCITINS Energy and Environmental Research 8001 Irvine Blvd. Santa Ana, GA 92705 Attention: Jim Reese Preparation and shipment of N0X Flasks to Pueblo, Co. 14.201 FRANKLIN AVENUE TUSTIN, CALIFORNIA 9Z6B0 AREA CODE 714 • 733 • 4239 AREA CODE 213 ¦ SZ9 * 1S«4 CABLE: TRJELABS date _ • , • December 21, 1984 RECEIVED November 16, 1984 LABORATORY NO. 00358 P.O. No. 28219 INVESTIGATION Nitrogen Oxides RESULTS _ The submitted samples were analyzed for carbon dioxide (CO?) and Oxygen (02) by Orsat and for nitrogen oxides (N0X) by phenol disulfonic acid (PDSA) method. The results were as follows: Sample I.D. C0?, % • ¦ Qg» % ¦ Sftu ppm dry. 3606 14.9 4.3 411 1439 14.9 4.2 337 1090 •14.9 5.2 384 13S7 16.3 3.6 366 1377 14.6 5.7 411 1328 14.8 4.7 399 1437 15.3 3.9 410 612 17.0 2.1 456 611 16.6 ¦ 2.3 431 1193 16.2 2.8 342 3330 . 16.7 2.2 * 1183 16.4 2.7 473 * Sample lost during analysis r ! s-i Respectfully submitted, TRUESDAIL LABORATORIES, INC. O. JSmmk- S. Hugh "Brawki Supervisor Air Pollution Testing TWi report applies oaly totfcw ample; or samples. iarestigttedl ii col Mceutrilr iwiicad-ws oi dae qutlit? c cecdituro of ipjamidy icUctiaki ox similar products. As ¦ mutual protection to dieats> tbe public aad these Latara tenia* tbis report is fobttitted tad tcccpwu for the exdusive use of the client to whom it is addressed ttfid iqxn die eomiitioo that ii is act to be usea, itt whele or io part, in ftn? uhcftUiQi or pufeliciiy natter without prior writtea imfeorfrarwm torn diese Laboratories. ;b-\| j ------- N0X SAMPLING DATA AND RESULTS / Sample No. Date n 5i" Time Flask Vol Vf (ml) Initial Ba rom. Press ''bar j (in Hg) Initial Man Vacuum M/j (Cm Hg) Initial Flask Press PI (mm Hg) Initial Flask Temp TI (°C) Final Barom. Press ^barp (in Hg) Final Man Vacuum MF (Cm Hg) Final Flask Press PF (mm Hg) Final Flask Temp TF (°C) Corr. Sample Vol Vsc (ml) no2 in Sample (ng) N0x cone as no2, C (lbs/scf N0x cone, C (ppm) / u 333 O i^/n/py olol A.OV3 5-/. 75' Lo\'T /ZSy O9o fe,// O</a. V 3 y kJ!-\ 6~-u 3-D 5-5- vr& KjOf!--" 1113 efjO io/fc W "t '-€¦ \T>7? /003, H/l k)o^i-£ IH37 / vote a.o9o 'it 0 A>ot3£ /JA,p 100 $ 3.0 70 -y-17 idotv-e / ------- REPORT CLIENT SAMPLE ENERGY AND ENVIRONMENTAL RESEARCH 8001 Irvine Blvd. Santa Ana, CA 92705 ATTENTION: Jim Reese 14301 FRANKLIN AVENUE TUSTIN. CALIFORNIA 92489 AREA CODE 714 • 730-6239 AREA CODE 213 • 885 • 1S64 CABLE: TRUELABS DATE February 22, 1985 RECEIVED February 6, 1985 LABORATORY NO. 05516 Preparation of 12 PDSA-Flasks-Shipment to Pacific Power and Light Plant in Wyoming P.O. Number: 28976 INVESTIGATION Nitrogen Oxides RESULTS The submitted samples were analyzed for nitrogen oxides (N0X) by the phenoldisulfonic acid (PDSA) method, and for carbon dioxide (CO2) and oxygen (O2) by Orsat. The results were as, follows: No sample. Sample I.D* CQp, % 0?, % NO,, ppm dry 1i)60 15-3 H.6- 279 3473 14.9 4.1 304 1360 15.6 3-8 302 968 14.7 5.5 261 1413 15.8 3.3 279 1474 14.8 5.3 267 3253 ' . 14.2 ' 12.1 250 610 ' 14.0 3.6 283 619 15.3 3.7 284 626 14.9 ' 5-3 279 • 613 1442 15.6 5.5 290 Respectfully submitted, TRUESDAIL LABORATORIES, INC. /? 0JWKJ O ^ X S. Hugh Brt>wn, Supervisor Air Pollution Testing This report applies oaly to the ample, of samples, investigated audi is sot necessarily indicative of the quality or coaditica ol apparently identical of similaf products, As a mutual protect: oa to clients, the public tad these Laboratories, this report is submitted and accepted foj die exdusrre use of the client to whom it is addressed tad upon the condition that it Is oot to be usea. in whole Of Iq part, in say advertising or publicity matter without prior written guihonzadcn from these Ddxmtsrica. B-11 ------- N0X SAMPLING DATA AND RESULTS ffl. oj . ^/ fc "3° Pi-AnsT : W y o O f- Citj<- &iLLfrr£ ^ <• Sample No. Date Time To Tot. -XS~I Flask Vol Vf (ml) Initial Barom. Press ^bar^ (in Hg) Initial Man Vacuum M/, (Cm Hg) Initial Flask Press PI (mm Hg) Initial Flask Temp TI (°C) Final Barom. Press ''barp (in Hg) Final Man Vacuum MF (Cm Hg) Final Flask Press PF (mm Hg) Final Flask Temp tf (°c) Corr. Sample Vol Vsc (ml) no2 in Sample tug) N°x cone as no2, c (lbs/scf N0X cone, C (ppm) /A /iTi xjt/s-s- !(/.o3 a_A 3XS"J> /Co', ol IPOS' no i tS.tt 3A IHl$ 7/4/<* IM X.OS-J I& £> 13 z/ykC IL'./3 2.o3y W h >5S MIX. ll'/q X077 a& (c to ixh< !G'(b Z£>l$ / <- mco \(o'VM" /t Aoo t ------- GAS COMCFNTPAIION P^LCI'lAHON Date Test 1-31-"gS^ No. /-31-/4 -? 1-31 Operator Avg Gas Response, Davg Actual Gas Concentration, Ga (°avg~Zavg) x Gs/(savg zavg^ Gas Concentration-0 0%, Ga@0% = (G^ x 21)/(21-XO^) i ^ ! -i? : J 8 n . CO I - # Co j ~ TIME LOCATION N0X \| CO \| C02 02 S02 Davg ga G/\@Oi \| DaVg ga G/\@0% \| Davg GA Ga@0% Davg Gd Ga@0% Davg ga gago* /ty 3 A 3i-/y 33 hi 33.3 34 1 3'SV i-< 3 /U 3?J3^ 37, w !<- ¦ US tf.iJ' f!-\l t3 . 3.^" 5o.b /urr 'nt> n ¦ )3li4o 11 w & xu ; }•% jfe a 7 6-0 fi.V ' ' yy/ =r^ - Il«® _anil_ flfa Vo^luu/ -IfiiB 3^ am [ if* ,1.l> H 3,.W ¦ 48-0 Y3' fTZ-f \%oo tv n 9jCtTH_0 Ol/t 31-5 -2/T7 /r s~i Icjr 4AS ?.?r 47 52-3 tfoD /-VI0 V) TP- n 5^ (s> l?2> \Sn 40 35® 4\ 3<°1 Htn lr° to ll 32.3 m / lL> rf.T? firs' tf.f 4or 3H Y 2^ V no ZZ ¦tf.to be* j 7^ / if) /£ 4p I i/7 /f.a iH-rt HI* 11 3M- 451 /' OD /- 3/- -Z-U & l# 3^ /2 3' 3^ L 11.P- hH 4-. 30 vy 2sOO i -I'i tMj ^ 1' Ui M.f Y-?5 I ii.f v I ~~~ ?d"- y trW a~ ------- GA: CONCFUTDATION CA'.CTATICM Date Operator Q Avg Gas Response, Dayg Test No. . Actual Gas Concentration, Ga = (Dflvg-Zavg) x Gs/(Savg-Zavg) Gas Concentration-0 0%, Ga@0% = (G x 21)/(21-XO ) A 2 ECOfiJ ¦ OUT' N0X fO 1 I co2 o2 - so2 TIME LOCATION "avg Ga Ga0O% \| °avg GA ga@o% °avg GA Gam Davg Ga Ga@0% Davq ga Ga0OX OZrlO 3--1 ~ 1 jj.f 5^4 ll>0 35 44 (,s~r /s.i«r n:iH ¦m /3 8 VLd H'T 5^7 x~\ -r 33-r 3«rv. ll.0 3^ 4 4 (({,,0 i5.u> rf.-LO hi It.d TO 553 c^— 1110 M'.-l 3 »'£- >> 3 8S llU'f Z% (p7iK ¦ /%£! ri-14 %:< ^/* ItpOD tZhhT OfJiy, Z'l —- /o.D 3/ ~ —- —¦ 4 sr v ®?2^ 3i-z- "2_l ¦Z. ------- C\S fOWCEMTPATIOM CAL"ULATIOfl Date 2' I 2-'2-- ^ Operator Avg Gas Response, Dayg Test No. Z-Z~ 7 Actual Gas Concentration, Ga = (Davg-Zavg) x Gs/(savg~zavg) Gas Concentration-0 0%, Ga@0% = (G. x 21)/(21-%0 ) " 2 TIME t-USAa 0^ LOCATION N0X bl>/ CO ^ CO2 >~ O2 bl- SO2 w/». Davg ga GA0O% Davg gA GA0OX Davg GA GaPOl °avg Ga Ga@0% Davq gA gapos a-;-/e> 3^ ll.T- -iO 3C» ^.r /?-33 / W "#3 4.0 /? Oi 1-/- a- 7 lf-V 1S\ 3 5 \|&Vi I1.VO 3.l • 5V-o ^£? boz- Z JBo i-\- n 3^f 33 ,/D 11 3 5 6-lf, 0 y5.?o /?¦ . rt.n 3-^z toOt- ^00 2'/- /f 2/y 329 11^ ¦30 37 lelP /Oo rf-yv- ys.r y.ot. S5.0 5'DC? 6l£ >3 ft) 3t-i 1 l-b 35 Ul-V / 5^5 /f.3& VXiT A.ot, - 50 52o v- /' 2?7 3U1 11° iJj 3r Gt<> /5"-70 ft. 9^ 4-®z- 5^- ^ (&L>) loo l-Z'i #•1 3/k 3ff 11.0 -2A b%.<> /£7> /.# ff.r ^y.i72- 7 3^ 2 2,-v7- 3t 47.7 /££?> if. i-7 Yp 3.f7 bH'O ~fW ff?0- 72-7 3 3«K 2?7 370 //•' 3 (0 b1-< /r.si t9.fl yvjr HO y >> ^7 ¦36, V //.p Vi ? iT" 1p% /r.70 tq.vt* 1st ko.r (V 3°^ 3fr° /1.0 } i-D > uo 55c? isi Z'2- & 3tt 3^ /i.s' 31 3 * M* w 3.?7 Si r.00 1-2-7 3f0 1+0 m ^ \,%n ll-U 14b 4,1 3-37 57,$ ^ £43 ------- GAS r.ONrFMT"ATION r/>Lv"l/TION Date Test No. -rf Operator j) ,(t Avg Gas Response, Davg Actual Gas Concentration, Ga = (Davg-Zavg) x Gs/(Savg-Zavg) Gas Concentration-0 OS, Ga@0Z = (G^ x 21)/(21-560^) TIME n.L ^ 17, J /5Y /f 2/ a«r ^5? / -713 nio 0 V.d - 3^z- n.f 5^ on v/y '3.y^ , s?i TP/ w S0U t (. J-t-ll Uf Zt 3 fi /if Ho Gr.o ./?-/ YU 5.8^- 6/,r •5a w /i2i J -3- ~l ^ zi1 nS 3f 4t . 15-51 >9-/7 HU 3% /i 5 • 5 7^3 i S°x, 7 i-x-n Hk i°l\ 375_ 3b5^ (1.5 - vy 1 Ul-f (oi kzr tf* 7 A-H /V? n.i° VI4 VJ.O J. ">4 3. ^ >r £?,r bf) t& 7 N J Ikl {J&j j-i-if 3s",d 367 H.Y y S (pfi-d /»? rt.il V1.0 3^° 6 7,J" ' (oil 772 /vr/ s«i. et f 7.J7 (p 37V n r £T^> Q } K K ------- GAS CONCENTRATION CALCULATION Date / - ^ f S Operator f) Avg Gas Response, Davg Test No. Actual Gas Concentration, Ga = (DaVg-ZaVg) x Gs/(SaVg-ZaVg) Gas Concentration-@ 0%, Ga@0l = (G^ x 21)/(21-%02) TIME gr(0AJ. 0 u 1 LOCATION N0X \| CO C02 o2 S02 "avg GA GA@0% \| Davg ga Ga@0% Davg GA GaGOX Davg Ga GaPOX Davq ga GA0OX wq ~ f (# 13.^ ,z?^ 3&°l fi.O v/ r/ /V^f , 5?2- Iff.T IpL") •gi u 21V 3^2- ii >r z? 3S" (et.f rf.V0o /?. Qt-0 1&fc nsi~- nr 2?2- 3^ iur Jo 3^ C/1z 373 /7.0 ao /5".£D /?.27 if.o ^00 5"?,r Wi 21S jy.r Z°l1 3^ /y-fl ^ ( s'° 61,1 /?./? VZr 3-yr n.a 5^7 u° liri- tfG- 3/0 H 3#3 \| a% 1^3! nr 3."?^ $Z>r WH &>')- j-x-xi :af 35^ \| •' - v_ (e°liO iS.uo rf-ZZ- iu oo.r oofX ^3-t 2U Z ------- GAS CONCENTRATION CALCULATION Date Test No. Operator J), Avg Gas Response, Dayg Actual Gas Concentration, Ga = (Davg-Zavg) x Gs/(Savg-Zavg) Gas Concentration-@ 0%, Ga@0% = (Q^ x 21)/(21-%0^) TIME LOCATION N0X CO I coz o2 S02 °avg ga ga@ox Davg GA Ga@0% Davg GA Ga@0% °avg Ga Ga@0% Davg ga gaw oyjr- a-vr 33-3 2. 7 35 7 MO tAjtC - — 67.0 /5-££> fi.Hl %-JL rr.r '^H"u (/H o2 31.? 213 3^o II — (if') IS "7-3 11.11 yy.o 3.?« 65V <4 ~1 3U 2-7 33fc (\ Mi /5".7° Ml yrd> ^ r 5M1 no (57^ .27? 3V'Z- ll ¦— - jo.o ^V5 /?. 5' 2- W "?-?r fal'O I \| i ------- GAS CONCENTRATION CALCULATION Date -f i Operator f]) •.O Avg Gas Response, Dayg Test No. Actual Gas Concentration, Ga = (Davg-Zavg) x G^/fSayg-Zgyg) Gas Concentration-0 0%, Ga@0l ' = (G^ x 21)/(21-^0^) ¦ N0X CO C02 °2 S02 TIME LOCATION Davg Ga Ga@0% Davg Ga GAP0X 1 Davg GA Ga@0% Davg Ga Ga@0% Davg GA ga@oi (oft 71-t 7 fr7,r rj-01 3.2^° (g^.O 711" tIK l-l- 10 )t1 Ztl 3<-7 ifS (el.O i$SD v^r (o^A Mb gft1) /Xrj^ I -J -ll 3J.0 no W lH-d 4-7 50 GU 16. It jf.il V4-Q 418 7l>0 1^ 11 J--} Ho Zp !((.o 6"7 no (,U /5M 5.12 /f.37 Vi~)' ' 7 7CS nZ w Z-I-I'-I 3i rfc? 35? I 110 4"2- 51 \an i^.m /?.3? VV'f 3^1 77.0 . IV ^00 V /cr3- ixs 2-76 341 j/7,0 4^ r/ ur iS.lo11 /f.^3 .44 no 1^o & ;->/(, m zsx l/^O 11 fT7 (£•0 /5.7«/ /f.4/ m 3 b? 15-17. /f-44 .0° 1?' ittt- j-l-ir n'i 2 V /v." 41 k. ' \Uo /5.l4 tf.m Hir ?7 pr. 0 j'l-n Mrs m 3^3 i Y.o 4"7 ao \ti-vi- /? 77 Hf.o >{.0Z- IK °n\ ¦ d )l!?X ^3^0 #<7 in /s~ o ^1- 67, f 5.11 /?. yj7v 4.°7 f-y.o ^ol T?,r l%h 35^ 6> 1 O.ir /¦# yfsf 'f.£>7 ------- GAS CONCENTRATION CALCULATION Date pL - 3 - f Operator . Avg Gas Response, Davg Test No. ' Actual Gas Concentration, Ga = (taVg-Zavg) x Gs/^avg"zavg) Gas Concentration-P OX, Ga@0% = (G^ x 21)/(21-%0 ) TIME LOCATION N0X CO co2 °2 S02 °avg ga GflpOl Davg Ga GA0Oi Davg GA Ga&Ol Davg Gd Ga@0% Dayg Ga ga@o% 32.r m 347 'M u iS-toZ rf. V? 7&>Z- 8?- in 131- 3(rf /f.o /5.L1- it-x t). $$<° HI IPI1 o.X s> 31.0 1% H'O ^7 \Q1J iS.fr W ^i) tA/lC ^4 ?Y,r SOL . \|002_ e3y^ X-H-H 37-6 $o ^<6 /v.r kl 1^,2- 6. iT \wi- tl f.r VI ovrl j-H-r 31.3 Z>3 5>1 /t.(? 57 "•1 QX 15.17- n-Hi 1 1 >< orru h.i< lib /t.r 5? 73 as !$.& \|W1 1' rio OGD- l-Lh~l y/r 115 /7.r >/ I5S1) Y\M K 1 1 \V i ^ o f-4 0>i_ ------- •c o IB Psf 1 OJ > tf CO CSJ N. cs l/i M X t\J S^. <»¦«. •s^ Ol M—Mt, > 0mm IB cy KJ i X B) > < m r- it it « © W s IB « o i- ®» • 4p m c c 0> a* o CA u ¦p* c o 4-1 fl3 a. (J L. Cfl > O lA •C EC to CS u (A to i « m U s Ol > ifi > < s m & Q D J> to L. Ol & O i i o s a 4 CSI o to g < CD .JS C" VN S> c£^ OCS ^¦J o e~i r- ^jr dikS"'' i i < tf "3— «r~ 1 «J- V> r_ C" r-^ C"" T" r- CVO _s> ^o" £ ^ rJ kT( _£» I 1 1 > «? 5^ <© k> & <3 & o fx. L vi r^i •o VI r>. V rs. O L «H >A ( i cv o art O «e O 1 IC 19 N o 5 -JK (K r-> • ;> Oh Cr- r^ v> rA >- Ci - ? . 1 1 m > R3 o » SI ¦o Or w 5S" v»> V >- U _ i p- 5" \_ Ln zr S O » re 19 o 3** K v. •X 'H "< Sf" H >- s r/ >• «S^ 1 ^ 1 1 ^ o u c is u c "'1 ^ Q v"^ u 5> X» r» \J^ r^ U I 1 \ • "v. 1 § '-.s > ie O ¦ vi, r< vs S_V r<- r< O1 /< v3 \ ¦"S K ;,VS- ii• v> "5- > t ¦o c K > V> j-A < a r-* v» r< 0» f >¦ t v\ H « ir% H U r< - ^ ? > r>A irt [*i o > #o a o o rK r-i \ •o \ »r> •«& «o —Jiio i "Z> W X Nil r-» Ci o r • ^r> * ^ * o 2 »* o & < C3 p. r-i vj 3~ r-s r-N. r-% •U r-t u 2k r^. f-> <3- < r-> <2s rx v> firi p-s <« 'J $< ' 5 '''K > O r** r~\ 'jrj ro r-s r-> \ ^s. f-^ ci ro t V >o XwTS ^-r> (—> i>«i « LOCATION t^o ; "3" i n. o / 3- 1 ns 1 > ! •o tA T 3"~ t i •^r # ri (A rv * i T 3" j -H u J > r 1 sS> J T~ ( rfr r- j ¦j- i ~tj T 1 L&J s H* <>» c~ u o o ¦o <"C >S. c* r ~xr r4 o< n-St . m r A *i r\ §,> "X J Vo S-21 ------- Dor Date ^ — y — f- 3 Test No. GAS CONCENTRATION CALCULATION Operator J), f , Avg Gas Response, Dayg Actual Gas Concentration, Ga = (Davg-Zavg) x Gs/(Savg-Zavg) Gas Concentration-P 0%, Ga@0fc = (Gfl x 21)/(Z1-%0Z) TIME LOCATION N0X \| CO co2 °2 so2 Davg ga GffiOl \| Dayg GA gapo% Davg GA Gam Oavg Gd Ga@0% Oavg ga ga@o% a/ofSBjr " 17S 39 « 30 67, r H3-0 im Cel-f "5^ 711 fO/^ Sett d 3Z.o 2>%°[ //?.r lA 3f 195 /fz-T HiX 31.V w.r LOT Ibl ton i' H s^r c V.°! 2>U //.^ 31 3€> /5.?o /?. Ha- fl.JL 3.vo CZ'd 511 7of KtXl Sfe-r D 3t,3- 11.0 3o 37 67.7 /5:t3 3.^ G!>f '57^ 7t>) I I ^. • 1 \| v-v-ji 00 I no PO /f NOy ferf-s ------- r . GAS CONCENTRATION CALCULATION Date Q ~L/ - T > Test No. Operator x>. c Avg Gas Response, Davg Actual Gas Concentration, Ga = (Davg-Zavg) x Gs/(Savg-Zavg) Gas Concentration-0 0%, Ga@0l = (G^ x 21)/(21-%02) TIME LOCATION N0X CO \| co2 o2 so2 Davg ga ga@o% Davg ga G/\@0% \| Davg ga Ga@0% Davg Ga Ga@0% °avq ga Ga0O% I /M3, uoy sar VV w lo.fr 67>r /r.rr l°\.Oo i%6 Gl-C liv /(,IK JOy>C&T- •' g.~q-xd ir-o in 3?7 (6.$~ JY /f.?r n.xr y/.z GKt mi : IU17 Atoy S~eT "C" v.i If Y oo l/.l ¦3/ J r cr-r tr.lo yy.t 3.f» (,2>0 fn 7 of W>y fer "t> " r Y ~ 2 T- ir-'t ni H«r II.0 1,0. ¦ 31 (el.7 n~(,3 /?'/'! ft.? 3.^ (ef»f 511 Jo, ¦ ((<%< i-'i-fi 37.X vr~ 3V7 /jL 6 77 VT ir-3 rf.iZ /9.3/ 3^ co.r Mo rjoo i7xo i-y-j-i n.% ' "in, 31 (& m ?>n 1 1,0 \fld 5<> 3fc Hi i?> . hlA. i? ,(t /j.i'i 15. LI rviu / ' \Q7.o IS.1L, 3-&7 fxr lofV l-H-3-7 Xs 3/7 1 t~o (ir 7^ K \|Ur Vi.d s-%0 506 1.13 Xifd x-H-xi W [f.D 7* ll~ 'it.Yf 7.77 sv-o 661 J-h.-;i 3G.fr 3 vi (I, d ¦J / IV Gl.o T.?f vxr y/,« f>>0 00 V no ------- GAS CONCENTRATION CALCULATION Date Operator Avg Gas Response, Dayg Test No. Actual Gas Concentration, Ga = (0avg-Zavg) x Gs/(Savg-Zavg) Gas Concentration-!? OX, Ga@0S = (G^ x 21)/(21 -^KO^) TIME LOCATION N0X CO co2 °2 so2 Davg Ga gagoi Davg Ga GA0O% Davg GA GaGOl Davg Ga Gam Davg Ga gaqo% Of SO Z-jT-3- 3^7 r lo 3 /c wflf HU Sib oord JL-f-7 !(.< 3/3 h -—¦ — Ifc.o! t%H0 11 iM nr.y ¦ i 1 Vfr'&y fj)>~ ------- GAS CONCENTRATION CALCULATION Date jT~ —zf S Operator J) « C_ Avg Gas Response, Dayg Test No. ¦ Actual Gas Concentration, Ga = (DaVg-Zavg) x Gs/(Savg-Zavg) Gas Concentration-0 0%> Ga@01 = (G. x 21)/(21-%0 ) A 2 TIME LOCATION N0X CO 1 co2 o2 so2 Davg ga Ga0OZ Davg ga ga@o% Dayg GA GaPOl Davg Ga GaPOX Dayq ga GA0OX 38 Td JL-r-V 7b~d 76 1 11.2- !^>(f C It -?y.r ?7 340 f/.r !(, c/ .r tiro J~s~~ II 3 c.j 7/X 77^ If.t 31 3 r (^¦C10 n.J>a ?ld vr.a 5'5? a & m vr 7") 1 16.0 IV 3 r fC°!S rtVi Ui \7T £Lf Hit fyi- rtro i-r-i 3 0 V7 i?r ?-7 xy 3 70 X /f J/f %p x^> Vjf.o i\ 7 si lU? Arrd ?~r-n 37.7 2X°j Y0 ^J//.r lo 1 7 7 O.o /rsu (1.17 VU (,1S 37.»" IK 3 ? 7 l/l.7 31 7 K 70-2-- tf-n i%y\ 7^0 7.7/ / . Gfr.6 b^i M) s~d j-r-n 3r,7y n.31 iU' 111 ?r.d VI obis- D tr ^5b~y^ ------- CTi > (Q rsj 'oi > «U * o ID V\ wa <3- csft r>- £3 7^- r qO «— s~ «c> -T~ ¦<.0 o "5- 0O o \r> N oCi 4 r^ •D& O <3- oO ffs r0> C~ C/") —"* w C\J ^ o ** C5 I CVJ o to < C9 -3 c-» r- VT" -~S- V> «» V> C— "5- «-» (—• _ tJ C\J M a > to o -ss rs. /\ L r< rs K % . V5, IS. u K , r> ¦O IN' o r^, rv «a f^> r>- r\ <1 1 s: rs ¦3 i; rs u si r^ 1 X o> > < ro CT O w II li o & fO- CD • CD o ©> O CSJ o ro CD r—> . r-^ o- l^-\ bv (S r-s r-^ r-^ CN r^v r^\ •»- > «c o o/ \ U \N /¦ & i k' ^=, >« L 0) (A c o Q. U) e a> u c o o c o w ¦C i. 4-> ** o C' re O >. r< vj. tf <3~~ ss> (\ si u C^» Q£ (/> C3 (9 C3 ro O) u c o o o o < CP s> * ^r o>. si "3- tt- C - < w u < > IQ Q fc-i 01— o-c Ci <5i Im£r, r» rs J f\ S5 K si S3 fc>5 A s> o e> < 19 ( "¦O r—i > V" "ir o ( —> > / >• rs > <5. <^s C, PA u o u O o o < C3 > >- r-> u > r> >- >¦' r^ >- >- r^\ zr- U :r- l. o CD > ID O «=3 ( • 1 S, r- v= >¦ o r^i v-, r—'i o r-i C5 u eo r>^ c^s <« t- 0> & o «rQ O <£• < Cfl >" \4 (s-> \y rr r-> r> r rr C- 3- r-> ri O r~\ f~N r-i •ri u s o r-"> V, X o < o ' O c- "V r^ ^y- r* <-< r- . rS <3^ -s fs 0^ v=i v> Z' r r- <y /> as > e? si n r-> < ^ >- <-s r^> r^ A "3- r~> r--> -n V ¦o r^ Vo r^> i z o ri , 1 1 r^ o~- i T~ - ~— < o 1 u / vS i o \y o O o j o S3 sir \ I ss o _J n> ¦^w i 1 -s. 1 -i 1 I. «~t> Date 4-J CO a> k- LU s p 75 —i <~"< e, r-~i ¦<~i 5 o o § 0 e <-< o a c> 1 o z lo O z o- C^i cj^ S5 •^5 ¦^O u 1 «-t! o ^ III B-26 ------- D GAS CONCENTRATION CALCULATION Date £ -6 ~~IT$ Operator > C ¦ Avg Gas Response, Dayg Test No. Actual Gas Concentration, Ga = (DaVg-ZaVg) x Gs/(Savg-ZaVg) f-r/l/hrt Pcc/f w r~ Gas Concehtratlon-0 0%, Ga@0 = (Ga X 21)/(21-j;o2) N0X CO co2 o2 S02 TIME LOCATION Davg Ga GA0O% Davg ga ga@o% J Davg GA GaPOl Davg Gd Ga@0% Davq ga GfipOl 0?7f A 3'.f fro IX ( ar HO ro a. 6 tW IMC, Hs, 1 LfiOO 1(0 i> yfy ton L~!i PRjoner i ~io 0 (0.(<, 31 ir ay tf.61 if.n nr h% 7frd ^II ' V (o to P/L0JIF * 2_ 30-j" trU 3 oa U.'L Ho 70.0 /r,n it.rJL 37 r 1X2 h- f to ii Ji 7J.r titl 7 y,n /f. C3-p7.fr V.CH \|? Y.o b% CD 1 ro I0%( ii" ^/)£T t/ Mifr ;7/ //-r /sap ?r V 3 Gn /X36 it.^r \lr 79. r 'I9f fto NnJi * toXr W lL p/uflir ^ ------- GAS CONCENTRATION CALCULATION Date 3- ~(g T & Opera tor T) ' C. > Avg Gas Response, Davg Test No. ' Actual Gas Concentration, Ga = ("aVg-?aVg) * ®OX tjoo M 33o «.r ic HI t,1s ;r,ir \%ol no i,y? 2%r ^55- wHc] (Ho$ / - (p -l~3 3J," p-l 737 ~ Ho pd a.i yW/ It.V V.o hio toil ' W ».0 ,1 31/ a. s' Ho &> hrs /rJ/ itM Hf 3JC 93. r '%%' Hoi iLod j/.r W u.< ir « i V%x /Wi ll.oy m i,n ru 311 io% I$o0 JY.o ir? f?X $~r a h.t w ir.fr nr.? i w IUQ %J i.t\ U-f Tot %l M 00 3A-d Ml 3ir fro £1 (.7.0 o.i- mr y.fj tUl HH, 2s~o 'oH \o!5 -M 3a.jr 711 inr /u rr l?.U %s %t\ tt-r iti- 18\| J--G -311 3/.ST &1 31X rf i?.)' tt.yf %c V./3 fzo "\0't ItfJ n< ZHoO 33.0 ;?? ry 6 r «r ff.o? //.?? %f %/' y,o? ?U 1P) VI ------- I GAS CONCENTRATION CALCULATION Date ^ —7 Operator /) >C « Avg Gas Response, Dayg Test No. Actual Gas Concentration, Ga = (Davg-ZaVg) x Gs/(Savg-Zavg) Gas Concetitratlon-8 OX, Ga@0% = (G^ x 21)/(21 ) TIME LOCATION N0X CO co2 °2 S02 Davg ga ga»oi Davg Ga gapoi Davg GA GaGOt Davg Ga Ga@0i Davg GA GAP0X 03J(r ir--d 7° \UY /ay /?.1 ¦ ' i ------- GAS CONCENTRATION CALCULATION Date / - 7-f S Operator J) . C i Avg Gas Response, Davg Test No. . Actual Gas Concentration, Ga = (Davg-Zavg) x Gs/(SaVg"Zavg) Gas Concentration-0 0%, Ga@0% = (G^ x 21)/(21-^02) TIME LOCATION N0X CO I C02 o2 S02 Davg ga ga@o% Davg gA G/\@0t \| Davg GA Ga@0% Davg Gd Ga@0% Dayg ga GA@0X l/9° /loo y-i-r 30.-5 w 7 III loX. M /fo ~\|V 1 "/ £7,5" (ef-C 16.41 Kp.oC, (%b 75 yj.r l.fl hi 7T.o 111 m 911 fWD IHoo ^0-1 11J ir°i yzo /o.r (0.0 10 x-r }"V G~lt0 /r.c,r tf.ir V57-0 y.ii l-tr !> 7i7z> in Ml %$< KjA0 X-l-it) yi'f I4/.« Ho ro 67,0 tr,/\ VY.i l.?S' — fab \oq iiM 1-7- II 310 xn 32.7 />" 3f HC /r,Y? IfrV HXr 7>rr rtd ¦ M15 IY00 110 w 111 /If 7f tQ\ ££r tr.?j Itlo %r m.o \n-5 ft 00 x-7-n ii.r r?r 33 (e fl.c ?P7~ 70.0 ir.H t?J 7 92J MbV J-00O ftr 31>1 n Cl.f /r,7i 19. Jo HW Xw 9f.o 1 \l^ Moo }¦-!-/i~ 317- tii 33 * /ir yj r;L (tf If,71 !%Jo Hl.f ~7.tr ?7d ^\n \u^ jtfoo lo.y Irl 3/1> /y.(? (r^ tr.Yi 19.2 r 1M y./r- a/o ~~1 /"'C -— r — lloo 4-7-17 Jtf.o ni .?Fr~ /i.r y? $~r.o ti.fl 7o.7 no 7.?f A/O IA/KL —-. ¦ 1 fL&Ar'r 6-01 & D 0^ ------- liAS CQiMrFMTR^T" on calculaYioi: Date t')Q- V-S~ Operator Avg Gas Response, Davg Test Mo. Actual Gas Concentration, Ga = (Oavg-ZaVg) x Gs/(Savg-Zgvg) Gas Concentration-@ 0%, GapOX = (G. x 21)/(21-^0 ) " 2 TIME 4tai LOCATION MO JjU \| CO oiO^ C02 Utv\ °2 bl^k S02 \jfold~ Davg ga 1 GA@0% Davg ga G^POl J Davg GA Ga@0% Davg Ga Gam Davq ga GA0O% //'» y* 'm ix(p //1> 3r V 3 /r>L\ yys- 3,?/ li < b-\< fyo /ZK> Z'to-n 110 73 "> ,®.3 3 1 7^ 1^7 ° /T-W 19,0 r •ii.o !•?(„ ¦ v(< \<\4 '3 Go I'10 -K us 17 f 73? jo, "5 ii 3 1 h~Gf if,? ? 11 7 :?y (el% Wfo l1 00 2 -P-if 3io tfD 7rr 7 (. 471? If-Lf 11 H.O i>% 47 V !¥> 'lit /{ Oo Z-iO'"T 17 r iv; ?.o £7.z tf~.ro 11.1) y,/y L ~).D !L W 2.10-1 (, 33.v t.r 7% tftsr /s~n 19. r 7 KS H'O! I (°~1' Z Itl 17 Co I'Jo- 11 32.< 737 "7- "2- lis ^ o tfiff /?.?7- $ IjVt 1^ fl 00 -3I-T Ar 77 Xo zr ir?r tu ? i.?r klr-Q (#1$ 1lH CO 2--I0 - /f 33-V irr 7 fyJ ?;D 2-S~ 16 lUir \%t.r $•< l.Y! L?Cv 20 VD l-IO - ID jrr 7TY £.i 11 )7 ityr i9,7Y fi-o y 1< to1/ yi< 11 OV 2-lt>, l- 3^ wr 76 5" 7-'o /r '? . \| \bfh in?y 1%IY 47.0 H'lC ll< 73 W 110-it 23/ Xr~ 7 n tH /? (? /si 10 1S I inn IpD^ 4,1 ------- GA^ CONCENTRATION CALCIT/TIOM Date 2-"y\|"^S Operator Avg Gas Response, Oavg Test No. Actual Gas Concentration, Ga = (Davg-Zavg) x Gs/(savg_zavg) Gas Concentration-@ 0%, Ga@0% = (n x 21)/(2'\-%0 ) " 2 TIME £ur*r~ LOCATION N0X CO \| co2 o2 S02 Davg ga GAm Davg ga GA@0% \| Dgvg GA Gam °avg Ga GaPOi Davg ga Ga0OX Ql'00 2--IM P xro 7V f 1-< 17 a ^ f mo nn 4l>-< v.// ¦W) \ol< 2- Co Z-lf- 2- 32- w 1-^ 17 A a. F" nlrr 11)7 H,a 5^. W l ^Cb 7-11-3 3ll wi "K i 7-« if -W /rcr : tf'U i'H tot ¦1 CO Z-W-i m W lo W-% tr.tr i?70 i%n €.7- H.or " 4.r UM^ 9i°0 (p'.O 33.0 w 7Y? -?> A1 7 [r %0 If. to fl.rc 1^-? V./y in .9 5V/ Z-—1( - "7 * ;r 7r7 9-2- (, is: if nc i m y^y vyr n ¦ \ - ------- § rRfrTl F (CATiO GAS CONCENTRATION CALCULATION Date Test No. c^~~ ( ( Operator Q'C< Avg Gas Response, Davg Actual Gas Concentration, Ga = (Davg-Zavg) x Gs/(Savg-Zavg) Gas Concehtratlon-0 0%, Ga@0% = (G^ x 21)/(21-%0 ) U3 CO CO Oi,01 TIME LOCATION N0X \ CO coz o2 so? Davg ga GA0O% \| ^avg Ga GA0OX Davg GA Ga@0% °avg Ga Ga@0% DaVq Ga GffiOl tfod exod. o e- IT} /r,d Hi, rv 7/.0 /£,n itri 77. r i,zr — fS3-X PRotjit J li.< &r u.f \(fl.n IHlOI 17,17 (ll.f r.cr HV.f W tot (ru rn-or> Id ((,.01 /ftvy Hi 1,16 Mr 57 kit mo Pno De~ e~ " ¦— I — I— — (W Aufl/iona 33-f 'W II'V 17 nr G>C >o n:n %Jr H.ir SV.f m i - ------- GAS CONCENTRATION CALCULATION Date Test No. Operator d Avg Gas Response, Davg Actual Gas Concentration, Ga = (Davg-ZaVg) x Gs/(savg~zavg) Gas Concentration-0 0%, Ga@0% = (G^ x 21)/ V CO! TIME LOCATION N0X CO C02 o2 so2 Davg Ga GflQOl DaVg ga ga@oz Davg GA Ga»0X Davg Ga GaPOl Davq ga Ga®0% 09 (ri &Corf-orf~ x-u~r 3VuO U 1 \|/'W J? 3~. (f 7' i /JT£ «j /£ S\h noo j-u-ii J2.0 M }3C ?3 r? pf ir.rr If'YJ %u h.k, %,0 hm 5ib }ooo ;-n ~ (V &r 33n %s "wn 5"l.J ho d '/ri 7rv //,.r 3 y/ Gt-o irne nrr %r ft/3 ynd vpy 5-P3 noo j-i i 3?^ 2H lr? \|/U lo 3 r &7< i /cry tin v-r %Hr. HZS Heol ------- o I— < ra 'CD > * cs 1 ac CSJ w -X, > pmm C rxi i X Os > IB CP O OW II n m © CJ >«—• > o A3 IB O - U & , * e e 0) a; © Irt u ¦P" c c -> o o 10 fit o im 4> tn € a: « & C5 V (/) C «5 «¦» o * u 3 o* +-> > U w < < C? * £3 1-3 IS 3J Q, o I t 0> w AS <1* o ~—• CSJ o - to »c o < X3 V* r: c^l V- €~ T" rn \A 3~" Vrs "3" r-w i- ¦T a— Vk tr w> V c a? § ^J oO 3 4-r 3 fW~ o" rx >• ^5. £ 1 ^T" o >- >¦ u 0- 1 ~> ^-ra. g <& 5^- rs -+m \f Q> > re O V C>o vi >• t3- w Q> K. ^"S •si- vh si cr- CM O W o & <0 CS (J-, > •~A r_ Cp* > Q"" > L 5k CK ri oC p-k > 3- s5 b < £5 v_ £ . ¦ fc fc i - U \ «-«» "t <_ V. c r^. v3 K. S3 >- \_ r< VI U N. s,} r< c rC •y • k. K V9 o U) &« o ©I 1? i3 >- r- r-> b- 5s* >- vJ~" <3~ r% s> >- A 5s" < n r n r> U r\ u U r-% H rs rs n >- f^S > CO o u (Q> \ ¦o y <3 t-i —•^ rs rn X o gg> s o < a m r- o— ri r^ rl >- c ts "3" r^- ,-v '•=>- H rx "3" r- «r- <3- -H. ; "X Of w. r~ OS » .J® Q r* rs^ I - i \ r-4 —. J S Or ; US 'i rs. ) T"<» T --t TINE r~i «=> O 1- «-t I (O j Ss I »w 1 O- S r-> ¦ca T5 O rz >o ¦o o o o o r^ ------- GAS CONCENTRATION CALCULATION Date 7_- \ Operator Avg Gas Response, Davg Test No. ^ ^ Actual Gas Concentration, Ga = (DaVg-Zavg) x Gs/(SaVg-Zavg) Gas Concentration-@ 0%, Ga@0% = (G^ x 21)/(Zl-XO^) ------- GAS CONCENTRATION CALCULATION Date .£"'2-' a o Operator Avg Gas Response, Davg Test No. MyoXcJk. Actual Gas Concentration, Ga = (Davg-Zavg) x Gs^Savg"Zavg) Gas Concentration-<® Ofc, Ga@0X = x 21)/(21 ) TIME Ou'V" LOCATION N0X CO I co2 °2 SO2 Davg Ga GAm Davg GA GA0O% Davg GA Ga@0l DaVg Go Ga@0l Davg Ga Ga0OX i u> Z-lz-ff 2-« 5^7 '1 4Cp- 57 u.< /£ It titl V-0& jjl.€ ^1 cj :qo Z-il- °( 3Z-° r/c 333 41 lio (Lt is.-y> /t)n Yf.o <{3.0 W M70 /O 00 z-\l- /o 33.3 m 3^ /b Slo \o°i QS /$n /toj fls ^?_3 0-) Vol llo I f it> Z-ii- k 3 H-i Vb°\ 5"M !~LQd z-u- il 5z-^ >7- 33/ SI, bX bio /f.LO trw 3-76 &.0 t/l 11 CD 1.11- H 31-8 2U 101 as /9rOC HID (¦5.0 llo ,(f CD z-ii- n 32.0 £70 3P.-7 2.-7 m n-b? ls% i«r 'f 0 z-/V 'f 32.° 17b v* /X .w 8o (b.vj V3.P S/T IDS \s% •o0L /£ Z-C* L-H' 11° JJ-* 711 32C Lit V u.c /yn p.6 jg 11 31-b" it W /? (,<* ?( /STy? far 43.5 s.rz. I1} of) "/2- '1 - i '? on L-ll- 'f cM '1AaS\ — < t-)L- 10 JA %iA '/tM i ------- GAS CONCENTRATION CALCULATION Date ^„/3 - Operator Avg Gas Response, Davg Test No. - Actual Gas Concentration, Ga = (DaVg~ZaVg) Gs/(savg"^avg^ Gas Concentration-9 0%, Ga@0l = (G^ x 21)/(zl-%0 ) TIME boat LOCATION N0X CO C0Z o2 SO2 Davg Ga GAm Davg GA gago* Davg GA GaPO?, Davg Ga Ga90% Davq Ga Ga0OX ?.'£»> Z-ivf 25( Z30 -z^r /3 V V2- rV /S^ /f.?3 y.fc/ (.07 115 /o:od Z'fyro lC-1^ 22- 2,rv /f-3 3i vo £3.3 / y.76 $7- v-if tl'l'. 12>1 1* //>60 2-' ?'Y 7-0 "L 2X>0 y0.8 21 ?>7 ./V-17 /?Z3 52-£> y.A6 II1/ voO irrt "4 " n«i Z'W-IZ- m 7-T(° p. r 3r /v.jry /f./f 5&0 <{.% t,f.D •ST) m- >2oo 2-13-13 U>o fl-3 30 38 L.> /ViL A? fj.CLe 5o. ZlU Z(>1 /3.r !T' p'f.° /i': 3 ^ /?. Z-2- 47-P £/.ZO . 3^ iCOo l-l3' if 25^ 3/1 /?.p £«f TS~" /5T-7Z /f-Yl 4Co y.oo iio il 2-n-^ 3/fe /£ 6~4 IS71 /tvr tyfo /) ,t>u &CST isi 11 to l-U -'i 31:4 3" l/.tffl Y4/ ry" Lir /f. 71/ rw t/S.D if.ISO W-7 (0/ w fa 1-/3.- it- 3 <-f it A7-° 72 '^jry- /f vy.'fi 3-e7<> 6S~.D IHl 7J> 00 Z--/3- ZP 3i-3 ul 327? //.r •/if 3.1 < ti-r G"bo 11^ 2( Of Z.-'3- 2/ i)'-3 lb 4 \| /I " 11 7? /? f! vV r 3.<7 ------- GAS CONCENTRATION CALCULATION Date 7^1 3 - Operator ¦ Avg Gas Response, Dayg Test No. Z'Cf - Actual Gas Concentration, Ga = (Davg-Zavg) x Gs/(Savg-Zavg) Gas Concentration-0 OX, Ga@0l = (G^ x Z\)/ TIME LOCATION N0X CO co2 o2 S02 Davg ga GAm Davg GA gapo% Davg GA Ga@0% Davg Gd Ga@0% Davg ga Ga0OX 2'l 3-2^- 32^ 2^ 3^ 3 /ft. 5"Z) £>/ /f^ W Hf Ti #z /i"t7 /f-VZ- y .«r fro wtf 111 ¦10 Z'l1)-! 2k 3 tf-S" 4 r si 6f.o /s\£z tf-Ht y> 1M' 2 Od z-W'Z 32-^ Z"W 3 vo Af,x ro t/ ^ 1? /T./z. tUi yrv V-03 le> 5. 2- Lot) 153 3 ct> J(.^ 20 3zf vv sty. 67-2 /r-7 /<;. i y K2 y.°7 fcV) 1l»t y o° 2-/4- f 3zs" 3 VV lc Yf <£> / tf.o /5~>L /?./> in y./g PS 1H f 00 2-/4 - "T 3l-S 1 fl.teO M. v/e (olO Do 2-/4- U 3/>o 2-5"/ ~?l£ ns i< 5~2- (p%.~L ^-VZ -tWL it* 6,1.0 Vh< $00 7 ft 7rH- 7 Zf.o 2J/7 303 H rs- b%.S / S". ------- INSTRUMENT CALIBRATION DATE /- 3 !-f . Plant Yo DAK TEST NO. Operator p^C, TIME OF INITAL CALIBRATION /q ft ¦ TIME OF FINAL CALIBRATION / ? / 3 - NOx CO co2 o2 . so2 Span Gas Concentration, Gs f/2. y' Hffi.f 11,HI ?.0 -PXe? Initial Zero Response, (01v) i"< 0 J~ 0. S~^ 0 5"vd Final Zero Response, Zf (D1v) c< o 5" 1 v-r 51 Li ^ cf. y f5" r f (Sf-Zf MS1-Z1) -WZ 0, "f D, 1 I. o -o.Z ------- INSTRUMENT CALIBRATION DATE- I - 1! ~ f SPlant uy-fg Q TEST MO. - Operator Qt , TIME OF INITAL CALIBRATION fl "Xl TIME OF FINAL CALIBRATION 0 lH\ NOx CO C02 °2 S02 Span Gas Concentration, Ss t I t'xo Initial Zero Response, Z,- (Div) TO r 0 5 0 S"'0 Final Zero Response, Zf (Dfv) r.>~ r, 3 S * Initial Span Response, Sf (Dfv) S-G, 1 ?r, i f°f<0 0 '?7>o Fina-'l Span Response, Sf (Div) ey. t tfr^o Avg. Zero Response, Zavg (Div) - (Zt + Zf)/2 S-) S,1b' 5: [ . Avg. Span Response, Savg (Dfv) 3 + Sf)/2 Hit* nf & fLo Zero Drift, (S) = \|Zf-Zi) t>. z i.f o. 3 . -O./ z Span Drift, {%) * (Sf-Zf MS-j-Zf) -l.i* -0J -t.-b O. I© -2.2- ------- INSTRUMENT CALIBRATION DATE S--( - FJ . Plant M/y^? O&K TEST NO.- Operator f) ,f, TIME OF INITAL CALIBRATION TIME OF FINAL CALIBRATION iff TC NOx CO C02 °2 so2 Span Gas Concentration, Ss 1 To Initial Zero Response, Zj (D1v) J- 0 r. o S~t a Final Zero Response, Zf (Oiv) 0 r^d s. t M Initial Span Response, S-j (D1v) SO J fi.i- ?r.f ?s.o ?1,0 Final Span Response, Sf (Dlv) ll-t ?u- nnX gr-o %r0. Avg. Zero Response, Zavg (Div) - (Z-j + 2f)/Z £ • D 6 S.o^ f.f ( Avg. Span Response, Savg (D1v} - (Si + Sf)/2 ^¦26 ' ?6.0 Zero Drift, (} - (Zf-Zf) o' o 0 Of 1 -0,1 Span Drift, (%) - (Sf-ZfMSfZt 3 /.r t 0.1 -p'j -I.J ------- INSTRUMENT CALIBRATION DATE J~~l TEST NO. ' TIME OF INITAL CALIBRATION TIME OF FINAL CALIBRATION NOx ¦ CO C02 02 S02 Span Sas Concentration, 6s Hof^ xl'Hl ftO f'^-0 Initial Zero Response, Z-j (D1 v) & 0 S i 0 0 r, i <> 9f. C $S,3 Avg. Zero Response, Zavg \|D1v) - (Zt + Zf}/2 f-'K S", 2— 5- ! - Avg. Span Response, Savg (D1v) ¦¦ (S-j + Sf)/2 U'p ef^f.o s $ ------- INSTRUMENT CALIBRATION DATE • ;u/ ~t Plant ,uyX£iM_ TEST NO. - Operator* ¦ V < NOx CO C02 02 S02 Span Sas Concentration, Gs Hon ¦? r.t. Initial Zero Response, Z-j (D1 v) $ > o S^d 2- Final Zero Response, Zf (01v) r.o S~,f r. d d Avg. Zero Response, Zavg (D1v) -» (Zf + Zf5/2 3 5"" £.0. c^ 1 Avg. Span Response, Savg (Div) a (Sf + Sf)/2 i K ------- INSTRUMENT CALIBRATION date x ~ % - Ps^ TEST NO. , TIME OF INITAL CALIBRATION / Q { (p TIME OF FINAL CALIBRATION X. N0X CO C02 o2 so2 Span Gas Concentration, 6s //-W tof, f 70 Initial Zero Response, Z\ {D1v) S~ Q T, 0 s\a r. a Final Zero Response, Zf (D1 v) ¦ r.2- 1,0 S~i 0 i. Z "f.O 0 -o.z- ro.< Span Drift, (%) • (Sf-Zf) O'i -/-3 Or! 0-5kO Wro QfrK Operator Q ------- INSTRUMENT CALIBRATION DA^ £ > Plant u/Y/j p/f-fc TEST MO. ' Operator f)< C , TIME OF INITAL CALIBRATION /T 3> ^ , TIME OF FINAL CALIBRATION N0X CO co2 °2 so2 Span Gas Concentration, Gs : t tfhH ' H0(. 1 f'O rto Initial Zero Response, Zj (Div) i--o r 7 Initial Span Response, Si (D1v) S-Q.'i FH i (? ?%1 fr.o 27,0 Fina-1 Span Response, Sf [D1v) TH>d ?7r0 tow tr, 3 ts~<0 Avg. Zero Response, Zavg (Div) - {Z^ + Zf)/2 5M 4-f Avg. Span Response, Savg (Div) 85 i$i + Sf)/Z ;; ycyo §6- ° Zero Drift, (l) - (Zf-Z-j) o t-y .2- ¦ -0,1 Span Drift, (I) - (Sf-Zf )-(S1-Z,-) "23 , v 3.1 o.f -1.7 B-46 ------- INSTRUMENT CALIBRATION DATE 2- — 1 -I i T- Plant yui Q pftK TEST NO. Operator Q - C , TIME Of INITAL CALIBRATION [Q0 £ TIME OF FINAL CALIBRATION Oiq 0 / T ^ N0X CO - C02 02 SO2 Span Gas Concentration, Gs ?#> 1 ' y?/, 0 f, a r. 0 s~ 0 n 0 Final Zero Response, Zf (Dlv) r.i y,r Initial Span Response, Si (D1v) 19,6 fr>o F1na-1 Span Response, Sf (Dlv) sr>6 tH'f ft.r ?r,3 ti(Q Avg. Zero Response, Zavg (Dlv) - o 0, ir Span Drift, (S) - (Sf-Zf)-(S1-Zf) ~oP\ o.h -Q,f -i\| B-47 ------- INSTRUMENT CALIBRATION DATE i"Y—f S"~ Plant UjY(7 D A-1 TEST NO, Operator P < C . TIME OF INITAL CALIBRATION 0fOf TIME OF FINAL CALIBRATION NOx CO C02 °2 so2 Span Sas Concentration, Gs i pz-H' Yf/.? t<0 $Za Initial Zero Response, Zn- (D1v) fr Zero Drift, {%) = (Zf-Zj) (M 0. H Span Drift, (%) • (Sf-Zf)-(S1-Z1) V-'h '0.1- 0.3 B-48 ------- INSTRUMENT CALIBRATION DATE S ¦ Plant TEST NO.' Operator p <-C. > TIME OF INITAL CALIBRATION //~3f TIME OF FINAL CALIBRATION /Cd % Initial Zero Response, Zf (D1v) ru ire r. ' M 5,0 . Avg. Span Response, Savg (01v) 3 (Si + Sf)/2 £x> ST2- ^\|(b tO Zero Drift, (%) = (Zf-Z,) o -0' l c> £>.f 0 ------- INSTRUMENT CALIBRATION DATE ^ - Y - Plant W/tf dK TEST NO. Operator p <-C < TIME OF INITAL CALIBRATION f/„ .C& TIME OF FINAL CALIBRATION a 1^1 NOx CO co2 °2 S02 Span Sas Concentration, Gs t-12-V ' Hof^ iy.t/3 fXd Initial Zero Response, Zj (01v) S l P O O r.y r. a, Final Zero Response, Zf (01 v) r. i Initial Span Response, Si (Dlv) is"' 0 f r- o Flna-1 Span Response, Sf (01 v) ti.r ir.d f3,r Avg. Zero Response, Zavg (D1v) - i2\ + Zf)/2 4-fr S\oO S'. ¥€> 5,0 Avg. Span Response, Savg (D1v) • (Si ~ Sf)/2 % i^-1 Hi< It if Zero Drift, {%) - (Zf-Zt) . o ¦ . L o o 0,0 Span Drift, (S) ¦ {Sf-Zf)-(St-Z1) D > (p ~ i - PA -\.L ------- INSTRUMENT CALIBRATION DATE ' JX --(S-f-Zt) 0 ' (f ! on 0>(f 0'H ~J.o B-51 ------- INSTRUMENT CALIBRATION DATE ,4-5 -f j"~~ ¦ Plant \aj^(7QAK TEST NO. ¦ Operator P«Q TIME Of IN1TAL CALIBRATION f(m P i~ TIME OF FINAL CALIBRATION ------- INSTRUMENT CALIBRATION DATE J-G > Plant u/V 0 D4k TEST NO. Operator P > C . TIME OF INITAL CALIBRATION O ?OQ TIME OF FINAL , CALIBRATION (Q 1 NOx .CO co2 02 so2 Span Gas Concentration, Gs $tl, «-/ jj.ii ?.o' Initial Zero Response,. Zf C01 v} & l d S t 3 S~~i 0 r, 0 ritf Final Zero Response, Zf (D1v> CT 3,r s~. iT3 .Initial Span Response, S-f (D1 v J ft, A tr-i °t%d Final Span Response, Sf (01v) tt.r w.r o tf'i fno Avg. Zero Response, ZdVg (01v) 3 (Z< + Zf)/2 S~,/f i0 Avg, Span Response, Sgyg (D1v) - (Si + Sf)/2 • HO fj.fr loX.e ffor \|t.o Zero On'ft, (%) 3 !Zf-Zi) e-l -/..r o. ? o.z Span Drift, (%) « (Sf-Zf l-tS-j-Zf 3 O.I ~/.v T.T o. f -l.-b 8-5.3 ------- INSTRUMENT CALIBRATION Plant ^Y(JOA-£ Operator D r C ' ¦ o?s~& NQX CO cog 02 S02 Span Gas Concentration, Gs in. y Vol, ? wjj }r< 0 fl-O Initial Zero Response, Zi (D1v) r;o S'o 5-J 5~ d Final Zero Response, Zf (01v) AO r.c r<. 0 d Initial Span Response, S-j (D1v) ?r°i 91. f 97.0 ?Ur K.'o Zero Drift, (%) (Zf-Zj) 0-6 0.0 Span Drift, (%) » (Sf-Z'f)-(-Zf) /, i" 0>1 -n DATE ' J ~ ------- INSTRUMENT CALIBRATION DATE 1~1~H Plant Wjq Q TEST NO. • Operator j)i C~ i ( TIME OF IMITAL CALIBRATION lQ 0 3 Avg. Zero Response, ZaVg (Oiv) ¦ {Z-J + Zf)/2 J i J i.r r, o S" x> Avg. Span Response, Savg (01v) (Si + Sf)/2 HJr .97.tr ff.ff $5i <5 Zero Orift, (?) ¦ (Zf-Z-f) -/,o 0. f o.y o.v Span Orift, {%) s (SfZf )-(S-j-Zj) -0.1 'O.l -2-1 -o.t -VI,I B-55 ------- INSTRUMENT CALIBRATION DATE 2 -~7-jr f~ Plant vyVtf D 4 K 4MnMHVaaaa\|aaaaaaaaaaaaaaaaaaaaaaawaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaft TEST NO, Operator Q < , TIME OF IMITAL CALIBRATION /$~^> 3 TIME OF FINAL CALIBRATION GlHjb M0X CO COg 02 S02 Span Gas Concentration, as ft! 1.7 Wj fro Initial Zero Response,. Zi (01 v) r, ^ 1 J r. d s~ 0 s~. Final Zero Response, Zf (D1vl r- 7 7« o r,i~ U SI 1— Initial Span Response, S-) (Olv) rc.l gr.X 7h0- ?l,d Final Span Response, Sf CDiv) n,i. n.r 103,0 fysl m Avg. Zero Response, Zavg (Div) - (Zt + Zf5/2 r. i r C-s r. i i Q'l -on 3.P ~o,r - }(0 B-56 ------- INSTRUMENT CALIBRATION DATE rt~L0-F C Plant VKjj Q DAK TEST NO. Operator p . C. TIME OF INITAL CALIBRATION crf/C TIME OF FINAL CALIBRATION Q 1 H 0 N0X CO CO 2 O2 so2 Span Sas Concentration, Gs Htl. 1 J j y? f.tf Initial Zero Response,. Zi (D1 v) Tt o rj r.a Si Slo Final Zero Response, Zf (D1v) S\d Z.o r-1> Initial Span Response, $¦) (Div) ff.Q 9% d J>fT£ Final Span Response, Sf (01 v) %•* ti>o ??<> ry.r Avg. Zero Response, Z4vg (Dlv) - Uj + Zf)/2 ' S.o ¦ 4.t> So 5> f.o Avg. Span Response, Savg (D1v) 3 (Si +¦ Sf )/2 IL.Z n 3C?A O /-r -VT B-57 ------- INSTRUMENT CALIBRATION DATE ^-1 I —' Plant yyf Q Q&K TEST MO. Operator Q-C . TIME OF INITAL CALIBRATION g7ff ' TIME QF FINAL CALIBRATION [(,11 NO CO' . ¦ coj 02 SO 2 Span Gas Concentration, Ss H fot> ? f-.o Initial Zero Response, Zi (01 v) Tu? r.o Sid Final Zero Response, Zf (Div) i.r Q.f V, e 57 c? 0 Initial Span Response, Si COiv) %(.r no ?7cO Final Span Response, Sf (01v) n.? ??• HS.X 0-6 C"9 Span Drift, {%) - (Sf-Zf)-(St-Zt) 0 . ff M "s. y 0, 0 B-58 ------- INSTRUMENT CALIBRATION DATE ^ ~!(Plant wy 0 QA-K TEST NO. Operator 9 , f . . TIME OF INITAL CALIBRATION [(„ Cd . ...... TIME OF FINAL CALIBRATION ol^H NOx CO C02 02 SO 2 Span Gas Concentration, Gs 1 ' Hob 1 ti.ii ro Initial Zero Response, l\ (D1v) r-d fl a ------- INSTRUMENT CALIBRATION DATE . / - Jf~ t S~~- Plant U/y.f j) TEST MO. Operator J) t C , TIME OF INITAl CALIBRATION Q ?Cl TIME OF FINAL CALIBRATION IC y Xh v? (7 Initial Zero Response,. Z-f (01 v) 3^ 0 5^ 0 S-^0 £\o Final Zero Response, Zf (Div) s~< o i.r 5~ 0 $". 1 Initial Span Response, S-j (01 v) ?r.d H%d fn d 81,o Final Span Response, Sf (Div) ft {09-1 %.l Avg. Zero Response, Zavg (01v) ¦ (Z, + Zf)/2 f-o Coo 5.1 Avg. Span Response, Savg (Div) • (Si m Sf)/2 ux Uls 0.3 Zero Orift, [%) ¦ (Zf-ZO 0 -Q45& D <0,3 0 (V Span Drift, (2) =» (Sf-Zf)-(S1-Z1) -0. 1 }¦€ h 3 £>,3 - D.°l B-.6.0J. ------- INSTRUMENT CALIBRATION DATE fSL-r .P Plant Ws j$ j) & £ TEST NO. " - Operator- p, Q TIME OF INITAL CALIBRATION /£ TIME OF FINAL CALIBRATION Gl 0 &0 Initial Zero Response,. Zi (013 S~ o 5"' 0 r. d Final Zero Response, Zf (D1v) . >\o (f t s jrvtK S, 5 n d Initial Span Response, Sf (01 v) tco Final Span Response, Sf (D1v) 5%.S~ tu Pe-» Srvt )C ff'l Avg. Zero Response, Zavg (01v) - {Zf + Zf)/Z 5"-° s:o 0 4.0 Avg. Span Response, S8Vg (01vI » (Si * Sf)/2 ¦ JPt.if eft 0 Zero Drift, il) * (Zf-Zi! o >r 0 a 6.0 . Span Drift, (5) » (Sf-Zf)-(S-j-Zi) O I • 1 ISO 0,0 !¦'2- ¦i.l B-61 ------- INSTRUMENT CALIBRATION WTE 3 ~t 7 Plant UjY(7i)^/C TEST NO. Operator 0 ?( , TIME OF IMITAL CALIBRATION /? foC TIME OF FINAL CALIBRATION -\\fi mx CO * CO 2 °2 SO£ Span Sas Concentration, Ss tn, i let. f nn t-o Initial Zero Response,. Zt (D1v) 5~7 0 - S~< o P< 0 tC . zc ?r-/r %c^ Vj,0 Zero Drift, {%) - (Zf-Zt} t> 9 o °<7 0<0, Span Drift, (%) » (Sf-Zf)-CS-j-Z-j 5 -O, I -0,7- -1-7 o. 3 B-62 ------- INSTRUMENT CALIBRATION DATE c* ~ I 3 \ Plant U/NL'¦'] D 4 O -o.l 0.0 Span Drift,. (I) '¦ (Sf-ZfMS-j-Zf) ~o. 5" i.0 D, I . "1-t B-63 ------- APPENDIX C TEST DATA C-1 ------- C-1 COMANCHE GASEOUS EMISSIONS DATA C-2 ------- Comanche Instantaneous readings N0X vs OFAf open © constant 02 -12/12 Test Dates 12/7/84 1345-1615; 209-265 MWe; 3.2-3.4% 02; OFA-Closed; "2A" MOOS 12/8/84 930-1130; "2A" MOOS; 152-286 MWe; 3.2-3.4% O2; OFA-Closed 1300-1600; 252-269 MWe; 3.2-3.41 02; OFA-Closed; all mills 12/10/84 830- 930; 334-360 MWe; 3.95-4.05% 02 OFA-Open; all mills on 1000-1330; 296-345 MWe; 2.7-3.95% 02; OFA-Closed; all mills on 1500-1600; 261-273 MWe; 2.75-2.9% 02; "2A" MOOS, OFA-Closed 1630 ; 281 MWe; 3.0% 02; OFA-Open; all mills on 12/11/84 1100-1430; 257-263 MWe; 2.5-2.7% 02; OFA-Closed; all mills on except 1300 12/12/84 800-1430; 290-321 MW; 2.5-2.75% 02; OFA-Closed, all mills on OFA - normally open 18% C-3 ------- Comanche Overfire Air 12/8/84 9:10 N0X ports closed 12/10/84 9:40 OFA ports closed 16:15 OFA ports opened 12/11/84 16:15 OFA ports opened 12/12/84 OFA Test 750 OFA Closed lOpen . Time Load 10 1445 270 MW 20 1455 295 30 1505 291 avg. load = 298 MW + 8.7 40 1515 285 t . 50 1525 294 1 60 1535 302 + 2.9% 70 1545 315 rel std 80 1555 305 dev 90 1610 295 100 1620 293 Normal 1628 305 MW tf/out 315 MW avg load = 296 + 6.7 = 2.2% C-4 ------- k -J \ V !4j < * VI * * * Ss 'y V ill ¦> ¦c ^>— -"4 V. i, O )mm < -J CJ —i <' CJ 2 O < cc UJ o z o U5 c/> < er> > n3 M 'OS > 4) fc"> TS W eg *¦ O 1/1 « C3 i X" CM > r—'' «3 \|\j (sj I X cr> > J re C u li s* m o UJ ®> « J» CJ? . o ' » cn a* > ¦» o tA y c c o o a. W1 u to a ^ as o £ 4-» c - V u e o u a> +J t > U IQ «C « 55 k. O 01 Ok o >- r\ i i-4 r % Q % 5 ' o 3K W> ITS ^r- / > u >- r> 3- > > • Ch > > <>, 5- L fx fx \ • tv--V cs iv^ _£^ O crt < a . r-s s4 u Ci<2> r"N • ( ti IX f"N ^5> fx C^i ^ " f-A L, L r> r"> u L ¦ l""'. > to a OC. (Vk v. t4 t-^ > I "1 Cs $5 " ^3 [ws u &< -D 5 6 fO o CNJ o CD £ s~ r< rN r< K ?A r~\ rv >" r^, rv > r-i U r-> rs > r4 > {^\ f\ r\ ¦ r- rv f-^v pw r^x C7> > its a i »iO rs - r> tj . 'N (vo •-. rr\ jy\ I —» - 3r r-\ % r—k on C\J o o M O ® UJ V Oko r< -> > • ^ >- ps r4 >- QT" iri ', vV r\ r4. • - « €5 r^- o» C; x< s/1 rs si r~\ C""* •<5r K, s> - ^ xi -««3 Sjr ^5s t "¦ av > s va V-o <55 A \=» K s3 s c? O S D; <3 r-\ " c^i Jw • Jb ' ^. • ri si r4 v5 r\ 0>o n r-\ ts %3- . vS r^» L On. P-\ o < o > ' >• i5k» H > 4 , C^=> r< y~ e-t ^4f r^% ¦ k r^. Xi Oq> L>» n pi t4 fA «» n T< rv r-% —> B) > >9 a - rx. X y. i ^ o "3s- rx o «5> Cs \ » ~ L s o \> u N^s .<3 r" r» ifco r^ ¦%!S* » »«» «-L ai > <0 a $ c< I-4 V, •f^ u >• r—\ f^-s u !—> «a> V- U- dsk ¦"4 r-v LOCATION ] 1 i U «> 1 5^ 3- 3" 1 vi r4 y * I ± t * I? f* "• r o 'O r-» f 5r* sW — t " Til 'x ] C-5 ------- I' I > H3 M I > (/> CM O (0 CsJ M 1 X o> > <5 ro C5 O -aw (1 II a* \|Q o C5 <2/ o £ < o < Q£ u 2 O o oO < CS — o » CT5 fr* > w o <0 O u e> c c V 0) o u e c o o CO & o u to OJ VI c OS « a> CJ3 L) tfl c o O <0 u a O* v to > u 4-> l/> re 0) O H- « O ©> < <5 4 i^a Qb > \ <> r-A \ cs 1 u 1^ C-- ¦Ci rv CSJ O l/> < C5 u >- c\ V- r-» ¦TX r-^ U f-\ N-\ I -^s r-.^ I ( vr ' s> r v. © > (0 o CN ,v/"» M Qi cr- j rs n I <> Mi I ~5 I • -n \ -n ' ¦ &Q N.'-\ rv rc IQ CD CM o rQ 43 :> ri < r> >- (vA n n- P r - rv r-v ri r\ u C^x CD > (9 O CK. M fi"^ f^\ o K r- K r> ' r^ r—' v. r^N K r-%. CM © d« o & re O V- Or tr- L tj- c-\ Sh Cj~- <—\ Cn r-\ c^ /-- < CD rJ « Z^ u 4 - r^- <5> r-. o > si >- o> > a V -I r< f< vs r< ' v* o ^S< \^ vj \ ¦sn 3- n cr- I (5^ io r^ . 4 i^ O- r^ o o < CD pi r- rl r r4 o 3- A o r>i. i_ rl >- 'C* / <5» t sS 1~ > ro O T5>- o o U «» i^a V S T t. U rC v^- K' 6o o Or >¦. «• o ¦ o <-> r-^ L 3~ ri >- r° J 0-c r> r^A rrs . r-~» . 3r >- 3^ "3^ .T~ T^ r-* 3- W. r-^ r-A Cr- X o z < o I ' c "7- . O IT- r- sS« ts •\> Oo r-^ PS 1—N P-- . sS > f^N r^ Oi > ro a ti Ci '--S «-< o ¦ n: ts^ ^-o u rx 51- o V-> LOCATION - 1 ( UJ £ h- i o Q <-» M T < o 1 ® • r u 3" » q o r- o c ; d A ^ o o Ci r- r-~» 0" s c> r» C) \ * 1 fi => m r-^> «. - 5 o T n ^ r ir r-> >^"» T ^ 1 5 ^•. OJ n U c r-^\ .— ; ¦£ h • r-C c4- \ >. r-C •>• r<. >• C-6 ------- GAS CONCENTRATION CALCULATION Date /7- 7 j-10 ~ . Operator Avg Gas Response, Davg Test No. Actual Gas Concentration, Ga = (Davg-ZaVg) x Gs/(Savg-Zavg) /// Gas Concentration-® Q%, Ga@0% = (G^ x 21)/(21- ) NOx CO co2 °2 so2 TIME LOCATION Davg gA GA0Oi Davg Ga GAeo% Davg GA Gam Davg Gd Gam Davq Ga Ga0O% ll-q [(tt>0 - (700 3HT l7,o fj 7o. 0 l(fJ9 /?J7 0 7.o J.M J ho ??* 7 f 1 i;-°" \loo - itfod %i Hi 7 \1,0 ^L/ 76,r Hf.tl "3//T H.r 'yr 3 7 / ifoo- llto "io- o JJTH 'ii&r. •?(r\| 3fr 70.r It.TA. If, Hi 37, ^ 3/ to lof :s£ 6? ivi llii- ¦ Load Iti.f 1's^f ir-t «?G- 1 70. Z I(p i (p 0 ft.rc. JC.f ~i,!Y hj,r "/j(p ao - Jit & 117 ^/l if.o ^ 1 ?3 1 70 >f /L '>~X 19,y? it,r 'JJS~ p^.(? no 3^ 5' j.ioe - 4.10 o 3S"-o W f(,.o 21 \ ytf-o TO.f /t-f in. HI \u.f 1,/T \si.t 'no •ioO - Zlot> ir.r lol 30 4. i~i IC.i" 7J>~ 3F, o ~}> 0 o 7f3 ir" ol.M~ n. O / 01 oo- o lob 13,6 jn irr 0.0 / "J 7 ^ LU /f.f/ mr w lo.o '} f"'l c J in i?1' OH0°- op>o n,r ^7 f 1 3s"f ($ n~fi m' v r,o L(i 3 0 12S nf wc ------- GAS CONCENTRATION CALCULATION Date {¦% - /(J-fr- y Operator Avg Gas Response, Davg Test No. Actual Gas Concentration, Ga = (Davg"zavg) x. Gs/(savg~zavg) t+t PP/o,'> Gas Concentration-0 Ofc, Ga@0% = (G^ x 21)/(21-%02) N0X CO co2 02 so2 TIME LOCATION °avg GA GA@0% I Davg gA ga0oxJ Davg GA Ga@0% Davg Gd Ga@0% Oavq ga Ga0O% OTOO- OGOO yr.v loH 7 rA ; ?i irU £6.r ir.r i if, ra V,fV %Zo Zf.s" ^vr '1jO .r'° o(,oO- 0 700 3C.r lit HO t n,o Wx - rro- H. o ir.sr Hjr 7 t.o %10 7o>s~ ;;r -ill ,fS e n y- tln' Htf n Y 7.r ¦rc, 7 5 u.r n~ s 'Y r 3-f' 0 i id H M (,1,0 <1.ZV n. 3.s-f 11. - 3 t.o in y £ ( tK CUT &?c 0 (0)2.1 \l\0 / 0 ^ yu s-rv- i) UtoO .0 l»J l iu- iY%o 1U l,Y 17r "130 /?-'• - i(r i Vb-J"- 3rr L( oCf />¦» tllo- J-ou 110 172 Lnr f.r 13 W nr 17,/i 19.^ 3/,r 2 i(> i hSr.o ^ i ? r - JL / 3-0 Yv.r W yr-i $,r~ 71 8-7 7%r O'tH I %f(f 3/.o ?,Co r J 13 r 7 FA * HW- 3L>0 iir ->77 nz. r>r 71. M 7 i.r /7,W tf.L 7 Mo JOO \l7.o ? Xlio io.r 3r7 r-r 7 ^ Fll li.f 7 ?./«/ J/,r ic.r :/r . ;• o 'J 13X>~ ooto HbC t-f 71. W no i ho x p z;o ino Y/. i" Y n ------- GAS CONCENTRATION CALCULATION Date j£~l j — Y y Operator ' • - Avg Gas Response, Dayg Test No. Actual Gas Concentration, Ga = {Oa¥g~ZaVg) X Gs/(SaVg-Zavg) t+1 j-ttfiHfpw Gas Concentration-0 0%, 6a@Q* - (r,^ * 21)/(2l-%02) N0X CO co2 02 SOz TIME LOCATION Davg Ga ga®q* Davg Ga Ga§0% Davg GA Ga@0i Davg Ga Gam Dava 1 gA ga»oi 0OlO~ 01 la • hi.r Jt 1 Lf^ t\| ¦ll> 9 H no !?.rA t?.n 32.. 0 Od 'is, i" 3?r Y3r? tijX 9110- fffZ-P yj.r ni H- to O 73 ?y.o )7,o^ it, n 31. o X(7o Y/,r yf H if I %A\ 0H)-O - aS~L0 v«.r 10 mi r-f 7 "i 7%o !7\0X /¦M v ihr H. o Kd H/2. . \lAl oy}#- OblO if-o H6l HQ I !?, r s~> Cci 7i.o r sl.o ?i~?0 ^O'T jrr H o'l l^ll OtW " olio „ no t>o C3 7 Z 70 0,f 1 /0 no 3fc( yrfl 7'X t\tl i/.r ICril y/'O 242- 31 'J. s>7 tloo- Hl.f W ¦ 7,r H hn 3(r<\ 'yr .'b.' ia"1 i Tft- iftti CO'9 m' 11,0 IV i°t b.r %,lt 11,) 2. it,r i<(e y %r 7 (r r 3 f 3' \yi{ \i~ee - if/V Lli) H71 11,0 Gf id wr }i,M \%T>C. l!(, 7 iLr " '! / r- ¦ •' j 7f y iyA tSai if. r W /•?.(? it f 7 1 \n ------- GAS CONCENTRATION CALCULATION Date /1 -/ / - Sr V Test No. Operator i Avg Gas Response, DaVg .Actual Gas Concentration, Ga - (DaVg~avg) * Gs/^savg'zavg^ Gas Concentration-0 01, Ga@0X = (G x 21)/(21-%0 ) A 2 TIME LOCATION NO* CO "avg gA Ga0O% Javg ga co2 °2 GftBQl \| Dayg GA GaQOl Davg Ga Ga901 ^avq G^ G^fiOl SO? l^-11 a.l\ 1 r1' t-aOO - t IffO J-X06- nod 1^9 a -11 WO- XHod »'>V W - 0100 010»' oloo Oi-oo- oi>ao 0100- o-iio prod )V' OSTJ0- 00 cd StQO- OlOQ \>- Ay a too - 10 00 Ioto- 110 0 vy. I 7Aj 1H Xi'O lt'0 t,o 3ho 37.0 ir-o H 3.o ^7 iri \19.0 H7 yi l UM v°-a /'6r<"'o ll» X 0 I I tetCBO 111 lo I Ifirttoo ?oc 1 ? 1 ^ I Xlr\ 12 \~10'° 3^ lot 1H'( Ilk 7 3 7l n { J H' lo.o lO'O 7fo 7-r ¦¦Mt ni IT'O 6 °\ 77 9* !l^\ Ml Ul V70 H)ro 3U 1, t I T7 (f (,? (For data on CO2, 02> and S02, see page C-ll) ------- GAS CONCENTRATION CALCULATION Date ll-ll-f Test No. Operator Avg Gas Response, Davg ¦ Actual Gas Concentration, Ga = (Davg-Zavg) x Gs/(Savg-Zavg) Gas Concentration-0 OS, Ga@01 » (G4 x 21)/(21-10 ) A 2 TIME LOCATION N0„ CO uavg Ga G^BOl I Dgvg G^ G^0O% I Davg I co2 o2 so2 [ Davg GA GaGOl Davg Ga Ga601 °avq gA GAeoi bv,r Z7./3 11,% 7 o.X 3j~>~ 3(7 3' 7r lli~Z 3o.r j>n IJ'O 3d c) 1YZ^ 71? i ?,r/ ?2.f Ml 33. r X if Wlf /UV / W i 0 ( jz-r Mr 333 7 h? /CW7 it,)' }'/«¦/ 7J.C? 12.0 f&vrA WW? J?,t? 3-/9 72'/- x/ r n •) i) iz r (7,30 11 <5 13rr pi.i- /d 140 3V3 ii-r 17,/) / f.rr 3l>0 7S9 x?r 33? fS-'d p?}¦ lato - } IfiO a ,ii /iff- ttoo it- ,ii Q a -ii V'o- iHot ,%+ i1 ir1 17-/^ »-'v - oioo O)0Q- oleo ot-oo o^oo tiao- o^ioo ocvc/ lV oroo- o(td tiQO' 070X> ,K Av ^ loo - \Q 00 torn- IIQQ (For data on NOx and CO, see page C-10) ------- GAS CONCENTRATION CALCULATION Oate li—(-fr/ Operator Avg Gas Response, Davg Test No. ¦ Actual Gas Concentration, Ga «. (Oavg-ZaVg) x Gs/(SaVg-ZaVg) Gas Concentration-0 OS, Ga§QX = 21)/{Zl-XOg) NO* CO : C02 °2 so2 TIME LOCATION °avq gA GA0OX °avg fiA ga§gs 0aVg GA GaBOf Davg Ga Ga0OS Davq GA GAeo* 1UH • tj-oa HtS Hit PO i Sr, e Co ft f ' 1/.0 ICS* ¦J/, r ur xr.% 2JZ K,(< i- i'SOd lu HHl sv? 7>r ro r) ! i io, r /tf '12 f 3- r? tvu UM- ma Hk* w Y'O %o (, \ l/.o iC aa z&r Ifjo- mc III mr sr.o ('<0 1 7 /c,fy !% ilf /r>o }oo 7%v Wl tUr jr,p f h0 ? r 7 I too - ifed / it'f H7 1 n,o /i-6 73- o tcxr /f-n jr-o 7-ft jf. r $6 f 2'SI Woo- Med v7,r "ill ao 2^1 29o 7 j.r /(,.)& If,<(7 lf'0 xnf J 31 f-Ot) 0- hW v.r 12i n,e 2 4 1 If 1 [73-3- /C'GJ jr,r l<0>-{ 3.r itr r7 H sY? Moa j/,r hi 3) 1 lil.o Ijro ;yy \(t%0 tl.Lt, yf.r l 3.'0 HO ?. y \Vp Jiiea- xyeo lu- jfi i n IhO i2(T 7fQ p,J" If>21 itt? f n>f H,n ru i i-o J'St •»> 01 BO ll >r Hi l?r. T.r Id /XI 1%7<, >f-r r.?3 i7 r i ~j r ------- GAS CONCENTRATION CALCULATION Date !%-! 3 - Operator Avg Gas Response, Davg Test No. Actual Gas Concentration, Ga = (Davg-Zavg) x Gs/(Savg-Zavg) Gas Concentration-0 01, Ga@0i = (G^ x 21)/(21-%02) TIME LOCATION N0X CO I C02 °2 so2 Davg GA GAm Davg ga G^@0Z \| Dayg GA Gam Davg Gd Ga0O% Davq gA GA0O% vioo - ¦>7-r m lit y r 10 t7 oiiO r-M /W 01. o 0 lUt G7'0 6-/? A/O / A/ K 01 »0- vioo n.r iki ii. r K-d If ^ Gi-r (/GO Co ii ------- INSTRUMENT CALIBRATION / 2 ~7 — ' Plant C,o/^i4~/vc/~i£T TEST NO. / Operator 0 , C > TIME OF INITAL CALIBRATION f 3 HO . , TIME OF FINAL CALIBRATION /£ ^ (Z>s6tr # -2oo o 1 NOx CO co2 02 S02 Span Gas Concentration, Gs s fo-i' W. f /3. yi Mo Initial Zero Response, Zj (Div) jT <£5 S-'d . ¦ 5- d V $ Final Zero Response, Zf (Div) 5". (7 r.i y* r ^3- Initial Span Response, S-j (Div) f&, y f. d ff.j f f '6 f r< o Fina-1 Span Response, Sf (Div) rr. i Jl^'O ff.l $T< Q /y,r Avg. Zero Response, Zavg (Div) - (Zf + Zf)/2 ¦?<&' r./r 5- /$"" Avg. Span Response, Savg (D1v) = (Sf + Sf)/Z ?ST'6>r ff'O £ ------- INSTRUMENT CALIBRATION Plant Co/H&fcHer Operator Q, c . til RktJgg~ 0 -2st a / NO* CO C02 °z S02 Span Gas Concentration, Gs rtj-i Ho i, f f, <3 Mo Initial Zero Response, 1\ £01v) S~ a S"-d s" <3. C-6 S". a Final Zero Response, Zf (D1v) r.> y. r 3 initial Span Response, S^ (Div) f Ci>4 ) ' 2 n 4 4 ?-> >d f b~> o Final Span Response, Sf (Div) fT. 1 A?>o £f> o ry.r Avg. Zero Response, ZaVg (Div) * di + if)/2 ¦ 5 id r>/r sr-'~ Avg. Span Response, Savg (oiv) a (S-f + Sf)/2 h~' Zf'O 9 ir- & f ff'O >7f Zero Drift, (i) (Zf-Zf) $-0 0.(3 01 - ------- INSTRUMENT CALIBRATION DATE / 7 - ? - , Plant Ctf/tj /yg. # £T TEST NO. I Operator D. $ ,.C TIME OF INITAL CALIBRATION \~?6 i <7'Of. 1 /JYr" ¥' Initial Zero Response, Zt (Div) &~'d ro 9f'? £f7o $s- Zero Drift, {%) = Uf-Z\) <£>./ -AZ- 0 'O -£>. 5 -0.2- Span Drift, (I) ¦ (Sf-Zf J-CSfZt) 0.2— .a, t -2. .3- C—16 i ------- INSTRUMENT CALIBRATION DATE • / 2 -- S" -ST Y • Plant rj)^JtA/Cl-f-tr TEST' NO. """ ~~~ Operator f), g,c - TIME OF INITAL CALIBRATION .J 9 ${j TIME OF FINAL , CALIBRATION jjlf N0X co co2 02 S02 Span Gas Concentration, Gs ftf.Y' Hdt. ? 90 ?d Initial Zero Response, Z-j {Div5 f.d 9-d 5" d 3"- d Final Zero Response, Zf (01v) r,: d jr. o 6 r, j~ r. a Initial Span Response, Sf (D1v) Af.d ?9 F1 na-l Span Response, Sf (D1v) ?%/ 9f' Q 7/r - 4%-o>S~ sr. 3 $8-o Zero Drift, {%) - (Zf-Z,) , o. ° Q.O o.o 0-£— £).C.3 Span Orlft, (%) = {Sf-Zf)-{Si ) £>. 7- o.o D-1 OA -H-O C-17 ------- INSTRUMENT CALIBRATION J DATE TEST NO. TIME OF INITAl CALIBRATION TIME OF FINAL CALIBRATION Plant CaMfr/VC/f£T~ Operator ft 0 ~7"Xi N0X- CO CQz 02 so2 Span Gas Concentration, Gs ¦i' frf.9 ja'93 ?. C fgd Initial Zero Response, Z-j (Div) r.d s • & ^¦o !T, & Final Zero Response, Zf (D1v) o $< c) Initial Span Response, Sj (Div) ^0 ff. r TT-0 ff'O Final Span Response, Sf (Div) •? V.d f S~ 0 . $ Avg. Zero Response, Zavg (Div) ¦ (Zt + Zf)/Z Gd $<0 r. o CO f.O . Avg. Span Response, SaVg (D1v) - (St + Sf)/2 K'Or n°i ?f>0 Zero Drift, {%) = (Zf-Z,) 00 O-o 0 . 0 o. a a. o Span Drift,. (J) - (Sf-Zf)-(Sf-Zi) -0 ------- INSTRUMENT CALIBRATION Plant /-/ /t Operator • p O 7 9 .... tt.ro MOx CO C02 02 $02 Span Gas Concentration, Gs n-j\ r-d /& Initial Zero Response, 1\ (D1v) f' d a 5" O Final Zero Response, Zf (D1v) ro ¦s\ a T-c? r. 3 s r. o r./r M.I Avg. Span Response, SaVg (01v) s (St + Sf)/Z ?G'l ------- INSTRUMENT CALIBRATION DATE ! X ~10 -f ¥ ¦ Plant C.0MA-/rcH6T TEST NO. V' . Operator V (Td TIME OP INITAL CALIBRATION ( 10 f TIME OF FINAL CALIBRATION o 73C NOx CO co2 02 S02 Span Gas Concentration, Gs iO. f • a Final Zero Response, If (Div) 5"-C7 y>* Jt t i~ o r- 0 Initial Span Response, S-,- (D1v) fc.r f% 0 rr< o 17,d Final Span Response, Sf (Div) rc.Y iw / 0 1,0 m Avg. Zero Response, Zavg (Div) « (Zt + Zf)/2 'hs\ fr'd fro S~> 0. Avg. Span Response, Savg (Div) - (Si -i- Sf)/2 $-(,£> r (o a ?Y ------- INSTRUMENT CALIBRATION DATE . Plant Lf' TEST NO. ' Operator Q u c TIME OF INITAL CALIBRATION Q 7 5"~d .... TIME OF FINAL CALIBRATION / C. / f NOx CO C02 Og S02 Span Gas Concentration, Ss 8fP. Y vw. i J7-¥J P-<7 Initial Zero Response, Zf (D1v) 5" a fio ro P' Final Zero Response, Zf (Div) f< o ¦C, I i Fi.f Avg. Zero Response, Zavg (Div) - Hi + Zf)/2 <^TuO ¦5" Of r<3f tj.Yf /"id ; Avg, Span Response, SaVg (Div) - (Si + Sf)/2 ti-7f K-7~ Zero Drift, (%) » (Zf-Zj) O'O 0. t o.7 --0 -3 0-0 Span Drift, (%) (Sf-Zf)-(S1-Zt) -c -X~ 0>O -0-r -o-% - /.r C-21 ------- INSTRUMENT CALIBRATION DATE }7~f f~ fry Plant r.J mam c iter TEST MO. Operator p u~c_ * TIME OF IMITAL CALIBRATION ; (c£ 7 - - ,, , TIME OF FINAL CALIBRATION o 7Z 5" NOx CO C02 02 . so2 Span Gas Concentration, Gs r vj.'h ' Hot, f x y;? 0 Initial Zero Response, Zj CD1v) r. 0 r.o Final Zero Response, Zf (Div) S~ & "iA 5~ > X. jHC y, x_. Initial Span Response, $1 (D1v) H,o n,o gr.o ??, a Final Sp^n Response, Sf (Div) fcf io/,0 Fr.t n.i' Avg. Zero Response, ZaVg (Div) - (Zi + Zf)/2 H$r r > i it < 0 r, i Avg. Span Response, SaVg (Div) » (St + Sf)/2 ?t.r H'lr la O'O #,?r Zero Drift, {%} = (Zf-Z,) 0,0 —Q • f 0' 0.6 a-X Span Drift, (%) = (Sf-Zf)-(S7-Zj) <7.7 (? " (# hf ' O'Q -O : ? C-22 ------- n-'-f. •4-% 1 ! 0 INSTRUMENT CALIBRATION Plant CdA^A-^C/fE Operator 0 c<- N0X. CO CO2 °2 S02 Span Gas Concentration, Gs S7y ' W, f . 7T.O£~ fl.o gr.o 8L>. ^ Zero Drift, (%) - (Zf-Zi) 0.0 0.0 -6.2- o( Q'O Span Drift, (%) »• (Sf-Zf)-(S1-Zi) <5-0 ©J -3,8 -0, ( -L. ------- INSTRUMENT CALIBRATION DATE / 2 -/X - $¦ Y ;x/;i/gf Plant C&M A TEST NO. cV Operator 0(T C. TIME OF INiTAL CALIBRATION / G J~ 1 .... TIME OF FINAL CALIBRATION 01. NOx CO C02 °2 so2 Span Gas Concentration, Gs "T ¥' Ho t, <=f % Zo Initial Zero Response, Z< (Div) r.0 r. 5T<7 -ssBuy ( ' r- o Final Zero Response, Zf (Div) r- <=> r:c>' r.? Initial Span Response, S-f (01 v) A? ??.¦0. Avg. Zero Response, Zavg (Div) • (Zf + Zf)/2 z.o Co r. 2- "ctr Avg. Span Response, Savg (D1v) a (S-j + Sf)/2 &-3 fof.o £.s~ 3r 8c?r ¦ Zero Drift, (?) - (Zf-Zii O ¦ o o ¦ o 0-"4- O .o Span Drift, {%) * (Sf-Zf5-(SfZt) Q.o £>•! 3.6 £>.y '7f " '.I C-24 ------- COMMANCHE DATA SUMMARY WITH POINTS TAKEN OFF STRIP CHART TO CORRESPOND TO INSTANTANEOUS CONTROL ROOM READINGS C-25 ------- f#sl\| -'' r!4 J)aia. •SuM.iM.&ry > •5 ! 1 A'y m°A po/tJT j jJWBER loa-d mk Wfti- FiOW '$tr MILL OUT OF sew ice • % M0X PfO^Dt CO PpM&JCV i /VjT ~Z7o— Tcn:rz ' • 5 f - --¦/•>— /vn" - , /ror J-ff — 'X.GT H^U ?0 " /r^r- inr ±°ll ' 1 q 1, r 1~ ,—„ . p?,jT 1 >xr 1' 3^, /?tr - /r;L r~ 3- if / 2- —. 1 U (f A 'ff /rAf- /j 3 i r r1 2 r? r \ 3 0 y' 9% 7 y'S-jr- /rir 10X i <¦/ r, ? 2- — j,t~r \ ;?i ' i l $ Z. 1; £?0 /rv ~- } ~rr -. ——- - '• l J'. ftf- J -2& ' H ¦jJ C-26 ------- oio f 5uwr r 2 - y s 441 57 ¦ • wi ' /S<>0 no y ITff.t ? 7 f. r 2-Lf ¦ S£>3 ~ 57 5T?3 . 51 ! il J a . /a ~ Z-u< i 45^ 57 nC ' ^ ' 1^9 0 /£? '«u 10 7 >P> i 4zt > ¥ 3 (9 fa f / 1 fljHgS> : . 1Z t no 442- -2/t/V /30 O lb? / 131 — 3- 2> 4r 7 /3f — 3.7, / y o 0 _/0 25 2- }31 : 3-40 430 7^- \ / 33C ; 5M' yi t0r$ ;• ¦;9>i> 334 H i [; — '.5"23' k>2- / , _ 4 1 D 3Ioq mir - 5 J4 ¦" b 1/ > L loop $+£ HZ . - 3, jo Sjo - 'W ' /0 30 32f ' ¦ ft it. • - 3.jf 5fZ ff It C>L> ¦ 333 tit - 3- tS 533 tf ¦ f^OO 30/ ¦" til - z- 70 4f 3 # / 3 30 /j"9 _~ 2 ¦ 7f ns Hi# V C-27 ------- c O - Hi &«*¦ kt \| Cj II IP/ ' Le ; (jmlkpflfk -SomrA&v-y ll~)0 sss 'ft! j -— pottJT A/UWZt? LOAD MlAfe. CO^L. fu>uJ "Ar MILL OUT OF- SEin/ice ot Z N Ox^ SfitriteSfafiNr" + • " I" 4h> CO -£yaaiJfe£M^ q)b t?-l— , _. .-j (TO e^o,. (7 9-ja 7 1 } 1V,< ' . 4 ^, i mC ?- r St? (1 ¦ £'lie %0.. ¦" iyi'0 7 _ 3.^ j tT* I f 3 s 7 r . — ¦£"0 Cs» LI-. lie 0 i<-/<-f.fr? £/ l U '? _£,}£> i li^D W / 6 jo 1 H.r r w 1 — !• 3< I Ml? 7 y ^ 4Li - ll ff 0 3 73 .'¦ ~ny.fi- \ H1 ¦ I H t j" ' \| 3-U 'C i 7 Uo 5"3^ ^ - !-3o o ; 7 Uo 4^5 4'L. tfv 0 ^">.3 1 V?,<7 V ! "7 H : T £ ' 1 X ; %A 0 \ 7s ^ — — ff30 J'i!: ¦ / 4 f • ? f~ I A- 'U \ 1 r \ ?oo . — 34^ — lit o c ;?7 / V/"- ^ Kb 7 2 1 f _? >* ¦ 2W ¦ 3bV — «?f/, '. ihY.c 9 -j 7 r J-At ! 3 9 ?f 3OO — , r.' — ' - \ C-28 ------- ^rDeck. ¦5uiv\M&ry poi/JT fijtitjBER LOAD mk CCftL- ' FLOW '^r MILL OUT OF SEJWlce Ot % hlOx CO TV xfh to il 90 «s'? ' , 3( %&t> 3-?r 7 40 qiA 1u , /l 3 0 xn lfQ.O% ,— . 2. L f HI 1 qyo ?, j— fly2> / 37 a 2&1L ' <-< ?, i C ¦.— i Z-1' b . <-t j i 3&o ~7, 5t> 41 ¦ iHo o JG Z I'-tf, y 7 ! 7 0 i ?.& . ¦ L " 2.: i~~ I 37 H 3 0 f i h y, to 7 2. > H i,s~- Z -70 j J ^ 3 >j£> ifV i( / 1 - 1 ! ; i •' j i ? i i i 1 . ! ! i i i r 1 ¦ t . . ¦ 1 1 1 C-29 ------- r /7-tl r Ma- SuMPA&ry PO//JT tfWBZR LOAD MV4 C6WJ- ¦ FldW '^r MiLt OUT OP sew ice 0 L % MO* CO W'tc&Gi P°f 0O0 6® %o u ?!£>¦;; ' y . 9^0 ^ s-/ i «& _ 1! 2 k>& i . i V5V 7 fo :f/f ^4. x / 30 3ol /$! ~~ 7 5 ! Vf. ~ i-so \ r~ st> 57 . /0 & 0 j/0 >YZ . — J) ' -f 7 2.L»o • [ ^0 s > >~~ -JO 5'c? t go .• /o3° J/ £ 1 y 3 — • 2-")o ' r 0 t+S"E> 7 / j™~ i?D $(& ^7./ // 0/J 2j2> — 1 1 ¦' i-(j H %o r £>l? n/ "7o //?( >47 — ' 5 /-r. ;• ^r-O ! f3S ? HO m J types ii v til — ? 2- ; " ,". r 11 i vy-' - , /}¦ - /i7 ~ v 7 2,;~ V ? ¦ j H?0 ? tp$ • _/-— —trf- ' r- Ji ^ * /jlU-A J-U j p fH }>)Ci $1^ \o~a. C-30 ------- POl/JT /JWBER JJ~-7 /~ ¥f ¦H ¦) o SHU i'i } o '-iH, >ro o in i /r i o >rif f-t, < r o-ii o ! 0 0 0 io j. s & \fiOQ II-JO 'N.59 ! '4 JO 0 /ri o H S 0 LOAD r? J !- w^.t\^£)&ja. 5um,MAVy * a i: COfti- flomJ '&r /]%?i i ii.(,i nrr f 1 1 %atf Jt J } 0 310- / 1 c-J. 7^ i {f- ' f, f Z- iir.ii I37,t? /??«/? /? r-"?5 /•; >. > / no, >3i /7d,7G / ?/>JM /I hi I WLl. OUT OF s£Wice / ^ -4 Ot % MO* 1 > • r 1, ^ r ^ 4~ 17.5 J ' '2- ' ^ ¦ ! ^ r" CO ¦ppiftft3r fi® Y i. 7- r i s A j r-; S, 3 A A tf • j" 1' 'f 1 s, r - 7' f -7T 4" 7. r 6 ; 1 r-r ¦ ¦ 4 ! nr / -/ / r0 ¦? 0 ?~A ??¦ j- ?,?- f Vj~ 5 7 r-' '} I r C' J ' /, 1 5=' I .4 7 ?, S3 !< ' % ' 0 X A i r>; 7,3 r l A 1'H ^ .4 (t //¦ A < ¦ r 7.3 r :• f - j l ?' 5""" /¦7 0 > v / f r /3M'/ J ;¦ 4 l- 7 7 3 7. 11 . > /. J", j. 3-if" h Ho 10 U< ~ a ¦ 5'^ -1 31 < 41 a «jj TT- V ' %o H I ^ r ' ioc 2-qO -j—p co "J. i 5'C 3^ to O^P'-L i 3 <- ^ 37 : 332 329 3^ r ¦ f; ¥ 2^ r i'"!? 3a j sb i 1°l Z? 'S 22-5" ^2- / .3^ 3^ vv 247 3 'C 24") 2P 51 51 ?. j- t,"P 7. r <0 •>¦ r so r to ?- j €£? "T 6^ 437 1 < Q 4ST> H lo 5"? ^ . fc. 7/ J? 5°!: "7 2- C-31 ------- r (_S^c^-Ckx D '33* /yee LOPc D mk. 3 3«/ 3/9 3 / 3d /4) 3 / 3>$ 2j$ p r 7^1 / 3t>l? COftt- FU)\fJ ?:_poo '^kr / 3L? /3i ) VP WZ l V3 'ii / ^ b MILL OUT Or sewice Ot % lo, ( z.fC 1/ 760 MO, 1 o I S"P It 2.L>o y 5u Zto 3 i 2-.U 't -j / llr ?47 li'o Z-f/ / 111 H7 3 t.r 2- 4 s"* l x 1.1 ix, r z^r" LCVdM^V •o 1 -fl^ - - tzl l^}; NkJ • 4- C 2,3" <<}V MM), ao 5,-v CO pf^A. rio 5"2^ /• 0 /« 57 ^ £? "2. 57 57^ Wl W r 0y Bo / S/\ 5-7 "7 o 41 57 ¦yfS VfeV "H 4IL tU 4? ? r-V'/ Jl- 1 C-32 ------- Exxo/U - pfife. luminary impQt - pbffJT tJOHBtR LOAD mk COfri- ¦ FU3t/J '&r MILL OUT OP SEEVlcC ot % MO* PP«.«C#,02 CO ppS%Ot 3fA S-lf - 1 3^0 r . v. .¦ <-/ V6 60 ¦ , 4 jrs) .% i ¦ 37 5 '227 >r'^ • o- / - 3 jjv, r v s 7.' ? r __ ' y,y j V7 Y ?b^.r j-o /, J J~ Y. ? £ ? s£ 2x> r jr?,r' :l t ?, 5"" , , r>i. : ihi J- X 0 • c } S~5" Lj lj ) 3 2 -f 71 10 0 r— — ¦ Q'J--. ? ua, r~ r—¦ ! r>7^ r* y- ; 2 i So t Irr,— s%o,r — ' r. i n? : (<,' Lo r J;rj, s~ —_ _ '\| 5", 1 \ Ci$~ s° to 3 n?. f~ i n'2f — i y, r. ; v o q . 7 f p i- 3 - a ?.?Y 3 iHfi- mir H~fi 1^1 11 too 3 ry,5 /. 2. ' r C-33 . ------- C-2 COMANCHE BOILER OPERATING DATA MONITORED BY B&W SERVICE ENGINEER ~ C-34 ------- pt A-aTT OfrP A TiJ<5 1>Q TPt DATA ITEM UNITS 2- Test No, e>rJLGAt> OCHAMP — Sp. Date ^ Time Hours toSo /o vr f t°t) Ulo UJJtT LofrD fi£&55 Mm) AM 2 7 "2 %0 2.7?. ? tor^puTOl boiler TEMPERATURES I PeinlTS} . TF €SD€)1 Hhf.o M t> 1,3 x 4kO,! fTl.q -j Water fcvg Ctuiv . F n>n ry/.f ¦ 5ir».z. >'¥ ln-i inn (^0 (a Lot,7 Stm Lvg RH Attemp F (SlO $ST>.7 ' S 7,1.1 sm z. Stm Lvg RH F ( (r&2') toil.Z. tot&lf to o(. S Water to SH Attemp F (SOI) .2-6/. 3 2LI.I 2-42,o 1U M Water to RH Attemp F ( TO"?) "U/,3 7.4 2-. f 2-6 2.t © T.62.,1. BOILER PRESSURES Water to E con PSIG C6e»SO ZUc.S- It ?0, i' I £.7 Ai' «. W.J' Drum Press PS1G ( 6o£) ¦2-S3I-L 2-iTll & W2-V. j? ^i'17.7 PSH in Press PSIG — — — — — Stm Lvg Sec SH PSIG boi 23H.J 1 v iH HIGH PRESS FW HEATERS . FW Lvg #1 Htr F —- FW Ent #1 Htr 4'C <"? } 129-s \Z%'~ J2^L ¦ IZt'.tj FW Ent.'#2 Htr / C if) ! ro.r m.r / J-O- z. j 't.. #1 Htr Drain. fC ( izQ.l '3V-2. 131.') IW.l #2 Htr Drain t C ( ibo, 3 isf.lt iTI.g- 1 Co-1 Stm to #1 Htr - Temp p r ^ o; & 0% 67. i b o o tS~~ Stm to # 1 Htr - Press PSIG £ap ¦ p (lo> SV43 5T2«° WW 3-v?,r To & 3 ftT£ fstc. i/VO <4Ho • 430 H30 Q6/UZeai7''eg-f£i ^ ~ i?r? '«1 17.7htF cAs-ro»rf » p«4«"uc Seitv/iar F" ou>/2Aps P^Cflto Co LotSA-d o BV: 5VT. 1 C-35 I, ------- DATA ITEM UNITS 2. Ok) i-OAH \| Caajbli 1 W» Date t»rwAJO W7/W ^ Time Hours tO 3o Hoo ft 30 LMf>uTg% AfR & GAS TEMPERATURES (Pw&?) - . fJuffiaKljrgEcaB T Tofc ( Ftee Gas Lvg AH T 120/20 2i7/iiT- ZltMf tfrW 210,1/272. Flue Gas Lvg Hot Precip F ST,H'It6f frj.tfse. 5 Flue Gas Lvg Pri AH F Air Lvg FD Fan F ( 70.7/79.7 7V/7V.3 Air Ent Sec AH F (mhs) wt'tha.i itfjjtf 1 USftlt> Air Lvg Sec AH F £)<4 /ST)?„ '' Tis-i/mi Air Lvg PA Fan F — 1 Air Ent Pri AH F - Air Lvg Pri AH F — Air Ent Pulv ""F — Ambient Air F fiKixn S4.-S- Tf.a. Ci.t MISCELLANEOUS feedwater Flow LB/HR (loz) 1 7f J. 1 <7 f, 6 iTU-t> SH Spray Flow LB/HR f lo H) — — 7, <5 %.1V RH Spray Flow LB/HR (71? 3 ) 3?."' 1 4L3 "W.?2 SH Spray Valve Posit % RH Spray Valve Posit % HP Extraction Flow LB/HR .4- O2 Lvg Econ % teoUstv s./ i-nfj-ir "it ih.Hi 17/3.2./ COj Lvg Econ % 1 NOx {if avail) 02 Lvg AH % CO, Lvg AH % Oj Lvg Hot Precip % CO2 Lvg Hot Rrecip ¦ % Oj in Windbox % C03 in Windbox % NOx or CFA Port Posit + Fuel Analysis Burner § Out Serv - Relative Humidity % Advise location of flow nozzle with respect to SH and RH spray take-off. ... Any bigH pressure steam extraction upstream of reheater, excluding FW heaterv + - Report data available - specific requirements will be requested. £2). Efficiency data 2 C-36 , ------- DATA ITEM UNITS - z 0AJ LOAD Date DITMAHlO U/1/M > ¦ Time Hours 1030 to<4< ifoo Ulo DRAFT LOSS DATA FDfan Disch ~Wg SCAM In ©at) AH Air In "Wg AH Air Out " Wg Windbox "Wg Furnace " Wg Econ Out - "Wg AH Gas In "Wg AH Gas Out "Wg Pracip In "Wg Precip Out "Wg ID Fan In "Wg SH Outlet Leg TC's F RH Outlet Leg TC's F PULVERIZER DATA Pulverizer # * Coal Flow TOOz/,H «i r i-r I1 t rt 73 MD.Zt Wo.sH >HL 07 Pri Air Flow MLB/HR * Sec Air Flow MBL/HR Pulv Amps AMPS Pulv Diff " Wg PA Inlet Temp . F Pulv Out Temp F PA Flow Damp % PA Temp Cont Damp % Pri Air Fan Amps AMPS - The DRAFT LOSS DATA listed on this page is of value, but not absolutely essential for performance analysis. * - When indicator scale is in different units, provide conversion factor. (?)- Efficiency data C-37 ------- fLA-frt ofSKb TttJ6 DflT4 DATA ITEM UNITS z 7s 1— I tefc Test No. LuJtJ o>4 Lofio Ob -oZ/ow4,Hr 2/0 Date 12 f'lt&f 1 - Time Hours ¦Mr }4o° /wr /f3o \|/Vir'J- IcUlT LaAt> &e.o Si Mu) Z b5~ 2S~1 257 25^ ZZ7 ^ih,m BOILER TEMPERATURES (Pmi^rs') WnnHBDSB f iS&D vrv.r •4XD.4 ^TO/7 Water LvgEcon F svz-r •rSr. f 5If-/ S7o. t Stm Lvg Pri SH F '5\ozy 1VZ.H fllb-l. Hr.fr -V.1- Water to SH Attemp F (•j on) W ZS'7.7 11.1 1ST. 7 Water to RH Attemp F (Oi) %PJl4 "hZZb-tJ %st(>. 7 T-flPJ PSH in Press PSIG __ — — — - Stm Lvg Sec SH PSIG hot ?-V o 2." ' / J". 4 tu o'-f.z. llfo.l XMof-3 RH Inlet PSIG bo 4 vu.r V2-/• 9 t-tilM >411,7 "?r ^ RH Outlet PSIG ioi 177."U 1t4,L ia.9 1/M HIGH PRESS FW HEATERS • FW Lvg #1 Htr F FW Ent #1 Htr 4 O o ) fZ7 1 2 (y IZG t z C? fZ3 FW Ent 02 Htr (5") tin f/1 147 -I<47 IHH #1 Htr Drain f C- C 4) 132 )3z 111. 131 n? #2 Htr Drain f C L&) 1 r • !S7 /S(, l'~7 IS 3. Stm to #1 Htr-Temp F „ 11} 52Z. T?7 Sb% S6>« r&7 Stm to #1 Htr - Press PSIG local G7 6>S" Stm to #2 Htr -Temp F a) ?7J_ . 1L9 7rr iyo 7J-7 Stm m #2 Htr-Press PSIG Lo^AL / fc3 the, i S" is ir * ¦ 1H2. C-T 3 tirfi- r£>£ 6 (?) /»? n ft nn 73 9 ?Z& stm To #3 T&t> P (IQ> 'sir i'S'3 5ff F?7 . STm To * 3 ti-Tt psit. t m H to 1400 460 4oo 370 Nu Chs-Toi£Z ' By; siff- p«,6ut sew>c£ ° f c>u>eAPo pH-E BLO Co Loft AO <5 1 .'oft sta&teo t>£C. 1. /fIV 0<1€R£<(Z£ A-irZp^T^ <^-<>SCb Af lyoot-bls. C-38 ------- DATA ITEM UNITS 2 i " ^ j Test No. Time Hours iy?{ri ,3'r /HIS ( V 3o /VQS AIR & GAS TEMPERATURES (PvjjTS ) } FIueOasLvgEcon F (2/2S> TK/ZU. zuivn r(,6/f?r Flue Gas JLwg AH F C2/2n zbrmn zulus" m'M>7 -iif/ibr Flue Gas Lvg Hot Precip F (2l>/27) SWjS^ $y 7 Isn f s-w/n? ") Flue Gas Lvg Pri AH F Air Lvg FD Fan F ( 79 j fo 1 ?l I fx s ijis ^ Air Ent Sec AH F (t<4hs) mini rzyinl Itij ") Air Lvg Sec AH F svl/svr mlsQt Air Lvg PA Fan F Air Ent Pri AH F _ ) Air Lvg Pri AH F — Air Ent Pulv F — Ambient Air F ft% CT)1 Af.V ------- DATA ITEM UNITS 2 Test No. Date - Time Hours 1 mo o N 3>o /Vi/r COMpuTO PotA/U DRAFT LOSS DATA FD Fan Disch "Wg SCAM fo Out) ~W\| AH Air In "Wg AH Air Out "Wg Windbox "Wg Furnace "Wg Econ Out "Wg AH Gas In " Wg AH Gas Out " Wg Precip In " Wg Precip Out "Wg ID Fan In ' Wg SH Outlet Leg TC's F RH Outlet Leg TC's F PULVERIZER DATA Pulverizer # i Coal Flow MLB/HR i5lK> 1 5 f.7^ i Jl"? i-M.tr Pri Air Flow MLB/HR • Sec Air Flow MBL/HR Pulv Amps AMPS Pulv Diff "Wg PA Inlet Temp . F Pulv Out Temp F PA Flow Damp -% PA Temp Cont Damp % Pri Air Fan Amps AMPS UiLI A CoAl/fiO? TO" i3 F (tk ^ mill Z-A opf-L- /ajvT — rt c.ofrLJfh)i -£>«p P n-r\ ' US- //& uy ! ------- pLA-nr Of>eK67ltJ6 Of\Tk / • DATA ITEM UNITS / 2 Test No, Time Hours r -l /gl> 15" Oo /J"/ 5" ISZ° /svr /b/ mui. mirr '-fiX.'i Water Lug Econ .... jj.. (3m £2-1,7 t^Z-1-l 57o.7 Stm Lvg Pri SH F 51 <4 /5-/S U 7.1/7J2. 7JV //75 0 '-.il-"if-n. Stm Ent Plat SH F L. — ' J Stm Lvg Plat SH F — — — — Stm Ent Sec SH F t7 / gy nzihij Will! 72W/72I lls'/HZ im/yz 1 Stm Lvg Sec SH F ( 5 5/ 5~¥3 $vs~ Stm Lvg RH Attemp F (stn svr-r rrz./ ¦ p.f.5 $" 2- 3 o>" Stm Lvq RH F ( ko2^ 9xf ? .1U,r moM ^n.h ^ 2-o.V Water to SH Attemp F (JOl) 2. 3 wr r Water to R H Attemp F ( T0"7) "2- X i' 2— i w?.\| 2-«'£- 7 Mi'/ BOILER PRESSURES Water to Econ PSIG C 60S") ZiSi'i 26ST.V 2Cl£,l WJi.V Drum Press PSIG ( & ) UlS.i' ZroJ.S- 2-af 1 T-t/jz. ^ 2-^7^1 m, PSH in Press PSIG _ — — Stm Lvg Sec SH PSIG 60/ U4 e&' 3 1-1 f h?X £bl .TS'¥ s\r^ 5-V/ Stm to #1 Htr ¦ Press PSIG Local S9. SH Stm to #2 Htr - Temp F ' t IS- 3 7s -? 7 ¥/ 143 72.?- Son to #2 Htr - Press PSIG Lq£L 'T¥X ¦ I 33 tzt lit 12-9 ¦ fw EJT 3 C (7) /JW nn HO ¦ (80 190 STM To * I HtR T&{> F (10J ^9, SHI sit Bio 5" 3/ STm To 8 3 H~r< PlE^ pSlC, 3 7o IS'd 1 3 3 0 17>0 "W 0 C •(> f1 11° Hsr lr CAsTo-mGie ' pM.GUC- S&t0 Presto Co Lo&At>0 BH; svf. 1 C—41 ------- DATA ITEM UNITS 2 Test No. Date Time Hours CtupuTgK AIR 81 GAS TEMPERATURES LP-furs) - ¦* - i ¦¦¦ r.ni ~ ¦BBC 4MN ¥ (2¥/2T> Sil/Sbl SlrtfSlZ. sssfui ssiisn z&frsb & s (D flue Gas Lug AH F (2* !m lUlihi ZUfzlo zbiim 2bc/27Z 2$?/Z7 1 Flue Gas Lvg Hot Precip F (21,/27) sVo /tvx SKISM svj j£"m 513/nl Flue Gas Lvg Pri AH • F ¦ . i Air Lvg F0 Fan F ( l2/l3> > 6 2., . / n-fhiA (5) © © © © © © © Air Ent Sec AH F !2.q ?I3£ 1 z?/fir rhoim IS l/il? 1V//S7 Air Lvg Sec AH F dim) sbs/.tosl ' $oIm$ Air Lyg PA Fan F Air Ent Pri AH F , _ Air Lvg Pri AH F —. Air Ent Pulv F Ambient Air F fiXC I>3 fn 3. 1 C 5.o t,2.1 it 2 1 iT" Srf,S~ MISCELLANEOUS Feedwater Flow LB/HR ( 7OZ) IHU.1 /•"/ff.o I VIZ.! IW-L IhlHtX- SH Spray F low Li/HR ( 75 ¥) — — - — RH Spray Flow LB/HR (71>3) . — — - — SH Spray Valve Posit % RH Spray Valve Posit % HP Extraction Flow LB/HR Oj Lvg Econ % (3 ai/U! 2.n/i.n GOj Lvg Econ % NOx {if avail! - Oi Lvg AH % COa Lvg AH % Oj Lvg Hot Precip % COj Lvg Hot Precip % Oj in WintiboK % _ COj in Windbox % NOx or CFA Port Posit + Fuel Analysis Burner # Out Serv - & Relative Humidity % Advise location of flow-iaazzle with respect to SH and RH spray take-off. * • Any high pressure steam extraction upstream of reheater, excluding FW heaters, + - Report data available • specific requirements will be requested. G> Efficiency data 2 >421 ------- /" DATA ITEM UNITS Test No. Date Time Hours DRAFT LOSS DATA FD Fan Diseh -m SOW Tn fOuti " Wg AH Air In "Wg AH Air Out . "Wg Wind box " Wg F urnace " Wg Econ Out "Wg AH Gas In "Wg AH Gas Out " Wg Precip In " Wg Precip Out " Wg ID Fan in " Wg SH Outlet Leg TC's F • RH Outlet Leg TC's F PULVERIZER DATA Pulverizer # * Coal Flow MLB/HR - % 13 11?.17 I3 7./7 * Pri Air Flow MLB/HB • * Sec Air Flow MBL/HR PulvAmps AMPS Pulv Diff " Wg PA Inlet Temp F Pulv Out Temp F PA Flow Damp % PA Temp Cont_Darnp % Pri Air Fart Amps AMPS r~ KffU A £cAL/P T£V-' H * rlLTgV.-C I- F Of- p in lib li 3 iU H7 C C^oAL lprt{L~TS?t»>§ F 1 22 m (12 \| 21 / 2 Z. O Co/it (Attl TE>,« F I0.L) nr <2^ € 1 fill (i Tc>f F — — — The DRAFT LOSS DATA listed on this page is of value, but not absolutely essential for performance analysis- * - When-indicator scale is in different units, provide conversion factor. (2)- Efficiency data C-43 ------- PMa/T PA lf\ DATA ITEM UNITS 2 -2 ' 2. JL / z. X. Test No. Date In l »°TE(X> Aj^r^d^ IUS7A/JT, (,(LSS M"J 25Z. /? 2 32. J3 zef-ii. •24 2, rj , BOJJ.EB T£JM?£HATUfl£S j fill 1 in Tiiw S»? ¦¥ ^j.r, •/¥/,r HS4.I- LfS^.Z Vi3.\| Water Lvg Econ Ji 1 F S-Z6.9 S"56 S" 3 3 3 ST>Z:U i'JV.7 Stm Lvg Pri SH S74- / fiS~ F m.i/ng.i islsfrsri 7W.f/W Kfr.y??/,: lh?.t>hn.A ~W&vh3l- Stm Ent Plat SH — F f- ^ —4^—<- Stm Lvg Plat SH —- F Stm Ent Sec SH <7 / f F viifm-t Wi.lfjvs-l 3 W2tm^ 7^4/73? Stm Lvg Sec SH f F 1>ofe.7 1011.7 !0i7^ f?7 171,? Stm to RH Attemp n F S r?6.o 4/5,3 6eS"4 Slt> Stm Lvg RH Attemp 5(1 F svo-7 S"?2, ? 7 VWi s"j r.? sT?.3 Stm Lvq RH fooz F o$ PSIG 2A3 #•/ ZbHl, M Ibnt-H ZhU.f Z&( V!• / 2 3^.3 Z3"?3.7 2393.? RH Inlet £>°4 PSIG 326. I 3.r HIGH PRESS FW HEATERS FW Lvg #1 Htr F FW Ent #1Htr 3 r c lZ^-i i 23,<5 ? 25.fr 12 «.I tl.1,2. FW Ent #2 Htr $ f C HSS wsw •7ST5,t/ frf.H1 #1 Htr Drain A / c 111.') 1 2-^.3 tzt-1 17Z /-N.1 11 J. ft #2 Htr Drain & / c. 1X1.1 J-Tf If irZ.2. if 7.9 Ho 9 /S7.i Stm to #1 Htr - Temp \| F 581.i> 5-7^,7 6 og.Q S-«fc'7 Sti.H Stm to jC 1 Htr - Press l»v,l PSIG &o 4 2. f 7 -67 ~7H 67 Stm to #2 Htr - Temp I F its- 1M 7^.6 ftof.l 7«,9 Sim to #2 Htr - Press L C L PSIG Hi, IS~1 Wo l&i 17 g ib-L Ful EtJT rtJ »(• H7£ T£MP 7 C 1 ?sT.f Ht,. L /f 3.? /M.7 tfl.o lfg.1 .CTMTo^H/'ffT rrMP IIP Ir SS1-H SLI.H S"'7W szb.s sfcV.t STM To #3 HPItrt. MESS Lm L PS16 3 y® Vdo, 2io H-30 0 fzo #3 vHAibi T£Mf» g q i 86o , PUSBlo (Lat-o£flc>o . Jo6 ^0. £i3-Soz- ^rg(£>. 3fW,#\|T Z-A P"-L\J Uiifi Q &$'- 'C-44^ ------- /?lAatt af>£f2ATii6 DATA ITEM UNITS . 2 2 Z z 2. 2~ Test No. - UalC Time Hours f 2./ c/»7 O ?PO ?95» /0O0 I 03a (fOO ttZo AIR & GAS TEMPERATURES ) FJue Gas .Lg £con 24 (2! F znzkti-i st? /m.t asfjjbw iet-iMoiJ. ) Flu Gas Lvg AH ?o/z\ F imJin LSZ>£/iSi,^ p=T 1 1 ) Flue Gas Lvg Hot Precip zihst F wtlsm 5-Jf-f/rv«- S5»-?/ra/ ^"z/ss¥,i } Flue Gas Lvfl Pri AH — F - —. — _ Air Lvg FD Fan iZ/l3 F ftt/'jrg.i n-!rr- '* . -?!$•}. 1 srvi/rU si'i/rj, "5 ) Air Ent Sec AH F iM.ljug.H hU/ns \oUho1-^ toi.rfH q.J ) Air Lvg Sec AH . 12/z3 F &Z-tilth' 5T>l.tf'«fV.I rn>v/sbi,( Air Lvg PA Fan — F ¦ ) Air Ent Pri AH — F' ) Air Lvg Pri AH — F Air Ent Pulv — F ) Ambient Air )% F 3 i Ibic.f SH Spray Flow LB/HR — . — — — ___ — R H Spray Flow fo "h LB/HR 11.0 y /?, 0 •/ j-7.^r V7.C7 2 3. 6-2 SH Spray Valve Posit — % RH Spray Valve Posit % HP Extraction Flow —• LB/HR O2 Lvg Econ jobfao/ % 3, it h.o z ^.Iifz.13 3,is/3,/o 3.e2/j ,«1 CO2 Lvg Econ % NOx (if avail) Oj Lvg AH % COj Lvg AH % Oj Lvg Hot Precip . % CO? Lvg Hot Erecip ' % O2 in Windbox % COj in Windbox % NOx or CFA Port Posit - + Fuel Analysis Burner §¦ Out Serv - Relative Humidity % Advise location of flow nozzle with respect to SH and RH spray take-off, * • Any high pressure steam extraction upstream of reheater, excluding FW heaters.- + ¦ Report data available-specific requirements will be requested. (2)- Efficiency data " 2 Cmjto»veft •. pu^Jtic S&i/ieic Of ooL£>r2 00 > pu.&llo C&lo&AOv ,Trt rt li.lt.JL4A* - 0 r3 _ £? Af C-45 ------- PlAMT opei?ATi& t>P, tA DATA ITEM UNITS ~ Test No. )?/(?/ fiU Time Hours 0^00 O^3o tooo /03 0 1 too ' !(~5D • - draft loss data . •TO FaaBiseh - 1 SCttttntDuD -Wg AM Air In " Wg AH Air Out "Wg Windbox " Wg Furnace "Wg Econ Out "Wg -AH Gas In " Wg AH Gas Out "Wg Precip In "Wg Precip Out "Wg ID Fan In "Wg SH Outlet LegTC's F RH Outlet Leg TC's F PULVERIZER DATA Pulverizer # Coal Flow %)3 MLB/HR 12?. 73 IZf.70 IZ2-17 izt-r? IZf, ?& /So .o? * Pri Air Flow MLB/HR * Sec Air Flow MBL/HR Pulv Amps AMPS Pulv Diff " Wg PA Inlet Temp F Pulv Out Temp F PA Flow Damp % PA Temp Cont Damp % Pri Air Fan Amps AMPS Pul-J. 1-A p 0 rp l -4* ¦ nin f.vn' C«sftl)PtulT£h'.3 P os-f 115-2. ili.U usr Its. s" "l'c V" - f tn.i i:«'1 tit,? !l (, 1 IZh° ./.»•«< . pui \/ l-o ioAl'Ifiifi. Tip"p' P a z.7 tiz.l Ilho iti-9 IIZ.& \tf-7 The DRAFT LOSS DATA listed on this page is of value, but not absolutely essentia) for performance analysis. - when indicator scale is in different units, provide conversion factor. £?)- Efficiency data CUSTOMER« /'H/it-14 S€(t\Jic€ OF ( Col-otZ AOa , • pH.£/3LO, CoLO(ZAOO Tkfl » >.» ... O rrfi ft ft — > '•C-Mi ------- pLflrJT t?AjA / DATA ITEM UNITS 2. '' Test No. Time Hours l£/2/rtf \3 0£> 1330 /4/00 Ml# /ST><3 tS3o INSTAsTT, 6,0.oS5 MtO Ibt-lq 25-3.zr 2?f.20 Zbtbsr z.l4',U z$i,7r BOJX.ER T£MPER ATUiLES • mmrn-mSam - 5Of ¦ •4XZ.-, ^ -tyji/W VTT.q 3-5.3 Water Lvg "Eeon 3>t F 5~Vo 511.1 s-v2-r 2. syc.tj Stm Lvg PriSH 514-/ fiS~ F ibn/mM 7rz.f S"2 3 .4 6oT-7 ioT's- ZtrW^ «/ Drum Press bob PSIG TSlj. f ¦z-rtz-z X'o7. e 2n1-i" Z5t>0,i" z^o-i PSH in Press — PSIG - _ — - — — — Stm Lvg Sec SH &ot PSIG ic/zS -6 22 ^20 i/Ztf [ ¥00 PM« T£f> g c IH3.? H6.6 iTs\T\|13,£ GuSToMei?- P"f3uc Sept/\|<^€ of CoLo/Z^Co , PueBL-a Cotoiwco. To6 'Jo. . #?8_5oz. 1 r t C»47j ------- pt-AATf ' Oj>£j2ATIh3£> DATA ITEM UNITS 2. Cs Test No. Date Time Hours i~ioo /3?o ftfOO mo /5V0 is 3o AJR & GAS TEMPERATURES ) Fine Gas i-vs-Econ 24 tlf F SUSfoiaS stzqafz. ) Flue Gas Lvg AH 2o/ZI F l&llXi-i isSlfaV.i .znkhss-i ivtifrn-i in.t/ia.i iiJ.e/^0.4 ) Flue Gas Lvg Hot Precip zUl-'t F rvM/rvi'¦&> rwi sfrrt-3 ssi'l/ssv.? sri-r/fTrt s&t-i/sTtf.i ") Flue Gas Lvg Pri AH — F _ — _¦ Air Lvg FD Fan IZf 13 F uMlia bt-HUA ii.tfiz.4 U-i/'ii.i. u-o/u.c 73.V/7/.? ) Air Em Sec AM F 1 1H1/m, ¦? ni^/iu.i ii«.i i't^r ) Air Lvg Sec AH 22 fr3 F .Sto.'l/W (su$fmn si'.'/raf.o r;3 bmi 7 ritf.t/jbt.l Air Lvg PA Fan — F ) Air Ent Pri AH — F ) Air Lvg Pri AH — F . _ . Air Ent Pulv —* F ) Ambient Air it F Q!>H 47.2 Mi".? 2, 4 mb. 7 /6 37. y »rf2. ? /sTf. ? SH Spray Flow 104 LB/HR — — — ¦??r — RH Spray Flow 3 LB/HR — 13,HI 21? lo.it SH Spray Valve Posit — % — - - RH Spray Valve Posit _ % - — — . — — - HP Extraction Flow — LB/HR - - — . — - Oj Lvg Econ 3ot,jz°7 % 3,(1 h-r;i 3,13/2,?" 3-^1 I/}? J .Olfj.oo COj Lvg Econ % 1 NOx (if avail) Oj Lvg AH % COj Lvg AH % Oj Lvg Hot Precip '% COj Lvg Hot Precip % Oj in Windbox % _ COj irtWirtdbox % NOx or CFA Port Posit + Fuel Analysis Burner # Out Serv - Relative Humidity % Advise location of flow nozzle with respect to SH and RH spray take-off. • - Any high pressure steam extraction upstream of reheater, excluding FW heaters.- + - Report data available - specific requirements will be requested. Efficiency data Cwjxci'vieT?.! c S&li/lcg OF- _ pu£(li~o Colorado JoG MU+Mitm? i P ,5- ts nf C-48 ------- Plajjt ofeRA-rins patA 1 DATA ITEM UNITS 2 . 1. z z 2. Z_ Test No. L* uIC Time Hours 1 "boo / 33 0 ft/o* /¥ 3 t JT3 0 DRAFT LOSS DATA ' -FUFanDisdi 1 -SCAHfitfGoi} -wb 1 AH Air In "Wg AH Air Out "Wg Windbox " Wg Furnace "Wg Econ Out "Wg AH Gas In " Wg AH Gas Out " Wg Precip In "Wg Prectp Out "Wg ID Fan In "Wg SH Outlet Leq TC's F RH Outlet Leg TC's F - PULVERIZER DATA Pulverizer # * Coal Flow % 13 MLB/HR / 3 0.72. Ho,Ik i3l, 0/ 13131 / 3 /x 1 f 3/.J-J * Pri Air Flow MLB/HR * Sec Air Flow MBL/HR Pulv Amps AMPS PulvDiff "Wg PA Inlet Temp F Pulv Out Temp F PA Flow Damp % PA Temp Cont Damp % Pri Air Fan Amps AMPS Put (/ 1/4- :?"U* ?: F IZf.Z 126. 0 117, i is 7.2 127,1. l2f,"L pML-V, Z C Zar'i/flul Tkr >' F 116.? 12.9,0 121,1 iis>.r nt.o 1X1.1 Put /- ^ £ C^lk:l.Tev, f= /22.¥ /Z3. 9 \lH-7 (2 <¦/ .2. II^.L /¦w.f dCoP.ilktire- ' (5 It?, L iu.y m-H (17,5 (Zl.7 iZj.f " 7. 1 I The DRAFT LOSS DATA listed on this page is of value, but not absolutely essential for performance analysis. * - When indicator scale is in different units, provide conversion factor. (2)- Efficiency data 3 _ cuStomEI' i3c<-iiL-ic S{r£(/t_or2./w>o t pn.£t$L.o, Colorado Tr.O iiuutliTO on. - ^r>7 1 C-49 ------- : -4 - ~ti •^=1- ¦= /\fJT cj't \ t mcj c?a f pf DATA ITEM UNITS Z: 2 Test No, Date Mg/rt Time Hours ibo 0 (&>30 xmstait <<;adS$ rviuj ZTZ.IO ¦Zii.7 i UsJlT 0 (J LoAO BDJ1_EJ3 T£MP£HA.TUJiES 4 Wnlr* - - 5°^ - ,4: •V^Z.7 • Water Lvjjlcon 3IS F Sti»? sirV.v StmLvgPriSH S(4-/r(S" F W Stm Ent Plat SH — F Sim Lvg Plat SH — F — — Stm Ent Sec SH 7 / $ F 7¥i h a-f Stm Lvg Sec SH ? F loO ? i&IM Water to RH Attemp 5"o1 F ZfT.g z-khH BOILER PRESSURES Water to E con £oS" PSIG ztn.f Drum Press bob PSIG 2wfr- 7 1. i't f- 7 PSH in Press — PSIG — — Stm Lvg Sec SH Uo\ PSIG RH Inlet PSIG tfttt.i RH Outlet C,o3 PSIG •jxv. /. H.t V 6. HIGH PRESS FW HEATERS FW Lvg #l Htr F FW Ent #1 Htr 3 / C /zf-7 }%l.b FW Ent #2 Htr " £ r c IH7 IS®-# #1 Htr Drain 4 r c m-i 111,4 #2 Htr Drain 6 / C- 1 rr-? ls-1-7 Stm to #1 Htr -Temp ( F 5-7C.7 & Stm to #1 Htr - Press PSIG 64 7r Stm to #2 Htr - Temp Z. F 17 «.r 7? <7.7 Stm to #2 Htr - Press L »C^L PSIG /¦r¥ m Ful £JJT S3 HP H7i T£mP 7 C lf7-3 H1 ¦ 3 CTM To 3 HP Mte re-MP /£> F* m-/ sm.l ST/U To 3rtPtrtiL PHESS Lou It PSI6 t/00 3 >+PlrtG DUfiin T£Mf 8 C 113.1 7'"? tuS ToheiS: puliu C SEkiJice of CoLo/ZA-t>o ~ Coi~0»2/»OO J06 ftJo. ; ^6-soz. 1 C-50 ------- iiilfe— pL*rc operiATihi6 P^tA DATA ITEM UNITS Test No. Date Time Hours AIR & GAS TEMPERATURES ) FtoeGwt ajfrrw 21! faf T ) Flue Gas Lvg AH LB/HR i? z?,jr SH. Spray Valve Posit — % — RH Spray Valve Posit — % —•. HP Extraction Flow — LB/HR Oj Lvg Econ jab % 3 vh'Zai COj Lvg Econ % NOx {if avail} Oj Lvg AH '¦ % C02 Lvg AH % 02 Lvg Hot Precip % . COj Lvg Hot Precip % Oj in Windbox % - COj in Windbox - % NOx or CFA Port Posit + Fuel Analysis Burner # Out Serv Relative Humidity % o Advise location of flow nozzle with respect to SH artd RH spray take-off. # - Any high pressor# steam extraction upstream of reheater, excluding FW heaters. + ¦ Report data available - specific requirements will be requested. (2)- Efficiency data "n672.: pu.\|jLl£ So2i/[C(5 Or col-0rt-A E>o pu.£fli~o d-OLO/JADu C-51 ------- Plakjt ofeftA-rin6 oat A - " DATA ITEM UNITS Test No, Date Time Hours DRAFT LOSS DATA fD¥mSmdx Hl- 19 ; ' -SWMtafiiwt) "9 AH Air In "Wg AH Air Out "Wg Wind box "Wg Furnace "Wg Econ Out "Wg AH Gas In "Wg AH Gas Out "Wg Precip In "Wg Precip Out " Wg ID Fan In "Wg SH Outlet Leg TC's F R H Outlet Leg TCs F - PULVERIZER DATA Pulverizer § } Coal Flow %/3 MLB/HR nt,5H i.V'lf.. * Pri Air Flow mlb/hr * Sec Air Flow MBL/HR Pulv Amps AMPS Pulv Diff " Wg PA Injet Temp F Pulv Out Temp F PA Flow Damp % PA Temp Cont Damp % Pri Air Fan Amps AMPS fin Ll/ 2-A I »;//>„••, Tpv-.p r- rif'i 127,3 •" "• 2-ft F .... 114.1 127,7 ?'C f \|2i-j.i iZq.a 2-0 f 12-7.5" H7." - The DRAFT LOSS DATA listed on this page is of value, but not absolutely essential for performance analysis. - When indicator scale is in different units, provide conversion factor. (T)- Efficiency data j _ _ CUSTOMER' pK/lMC S €fL\itt€ OF C«L0f2AODy CaLO(ZAC>0 Tn/? ®ifl? '' C- 52 ------- pLfifJT ' -TIIJ6 . CAfflt DATA ITEM UNITS 2 Test No, Date 'It-l/oJ fry - Time Hours O2oo Og 3o 0 0 /e>0o /o Jo I/JSTAWT M<J iSL.t 5 33 V. H5~ lii'Hjr 360.3 r ami FR TFMP£BATUfl£S ' . flfew£nm 'SB?'¦:J ¦ * mr? Htnr fir ..j 'ilia Water LvgEcon Jtl F rs3.r 511 3 T?W ffi/.Z- ft"5. J s%r. 7 Stm Lvg Pri SH $14-} nST F ns-.thsiri nozjnU Vihun ni>ln7.o 7^fV/7xy./ 7£i/ir7.i Stm Ent Plat SH — F r * 1 ¦ Stm Lvg Plat SH — F — — — Stm Ent Sec SH 1 / % F 7 W.l/7lf,/ 7 iuhsiM 7l»nhx. t ?? ilhib-1) 76o S/?i 7 7 Stm Lvg Sec SH } F ,-s-L i DOS- 6 ^»o/. 6 t ott-7 Stm to RH Attemp n F £ 31.¥ i Sf, X- GlH.i Stm Lvg RH Attemp £11 F T14.7 r?f r72.J- 5-7 r-c. rb 7-Z- Stm Lvg RH yo~z. F /cot, 9 ta Z.f, & /o,C,7 ^ o/-/, ^ 1?7L- lo/^t-f Water to SH Attemp SO? F Z.11,% Z 71? ^2/7\| V71.I 2.7 z. 1 Water to RH Attemp 5"o) F %lz.t i~7z. r 2,-)°$ PSIG zwzf ZlZi-7 2?SS t" V)Sb,* i-iw.f Liun Drum Press yob PSIG 2-51JW- li%f. z. Zrl.o3 T-£7%- I 3-SX?. 7 t- S'H t * PSH in Press — PSIG — — —. — — Stm Lvg Sec SH t,at PSIG 7. °4 PSIG srv. t ?4 /¦ 4 5^?.^ i~v 2. t- j-y f RH Outlet 4o3 PSIG 5»?. 1 ,in>.r 5 S^7.V -Ci" Sbl.7 HIGH PRESS FW HEATERS FW Lvg #1 Htr F FW Ent #1 Htr 3 f C I.11 11 M.J nw.r 137-/ ??6.7 n ^..1 FW Ent #2 Htr £ r c /Si , & /iVi 1 ir&.z. 1S1S ISl .f ~m,c. #1 Htr Drain 4 / C IVI-I !Hi-3 IW.S- /V J. 3 /la, 1 §2 Htr Drain 6 / c. it,?-! !<¦ t-2- 1 It.k HI. ? /.? 7,6 Stm to #1 Htr-Temp / F (too .0 roi'1 & ol .& i 6?. ? J 16. 3 S"?0 •? Stm to # 1 Htr • Press PSIG <% 0 8? 9/ Cfj 1 Stm to §2 Htr - Temp X F 1 "97.fi itl-l -717. r iol.s 7-?/. 7 ' 7,11 •£ Stm to #2 Htr • Press L oCflL PSIG Zfo 210 2/+ Ze? 2.0? Fu\ EtJT HI Hf> ma T£Mp n C. / 11-i 'Mi-7 m-7 20Z. ^0 0.¥ /ff.3 «TM -To #3 MP HTR TEMP to F S% 7. H S"?<5.1 nt.j r?r.» nr.fi 56?.B 0 s PueBi-o W —¦ vw w (? Oils-Hits (LoL o(2/i0o , C-53 ------- iJjft _ pc^ATT ' opaZATiMfi t>T$ UNITS UW 1 M I 1 C"l """"fc" Test No, Date Time Hours Of 0° Of$t> Cf 00 <£"? 3q !>€>o ¦—u- /Ojo AIR & GAS TEMPERATURES 0 G) (3) © FfcG»sJL»g£«» 2^^ ' MfjjLxi-l. ffi.sina.-? cuafou tti.WUi,* FHj« Gas Lvg AH 7ojX\ F 24»V2f>7.r 2io.(,/uoA ZM.s/l 72.5 in.i/ns,? Flue Gas Lvg Hot Precip zUlfi F "7 v. S7<.4/lfee.7 Sll-'-hn.i uistmi ai-kfwi,? Co<\ fa, 11 Flue Gas Lv§ Pri AH — F r — - — Air Lvg FD Fan ;2/(3 F ^2,0 fyl-i ib.it/irt.1 fz.7/ri/} Air Ent Sec AH w//5" F loi.-fMi.t' V-i/ti.l <\i'\/1.M M-S/UM © © O © © © © Air Lvg Sec AH 22/23 F r2l//j-32 £ SVT/rtlrl /xi/jvj-.J 'ZtSjssU.x snt/sr/J Air Lvg PA Fan — F Air Ent Pri AH — F Air Lvg Pri AH — F Air Ent Pulv — F Ambient Air jf F T>z,b 11.1 3 3.^ Z£.C> At.r MISCELLANEOUS Feedwater Flo«v HoZ. LB/HR Zl ZZ.3 2»£7 .t zl/z.9 Z27?.f^ Z/o/.J t« ft. ( SH Spray Flow 1oH LB/HR — — — _ — .. — RH Spray Flow foZ LB/HR 57>.a( S"?>-3 "Z- U.U :cz. jz_ SH Spray Valve Posit — % RH Spray Valve Posit — % HP Extraction Flow — LB/HR Oa Lvg E con . jofe/3 °/ % ' 1,1 If 2 <7° 3,o//.7 2. CO2 Lvg Econ % / NO* (if availl Oi Lvg AH % COa Lvg AH % Oj Lvg Hot Precip % COa Lvg Hot Precip % O2 in Windbox % - COi in Windbox % . NOx or CFA Port Posit + Fuel Analysis Burner # Out Serv Relative Humidity %. ! Advise location of flow nozzle with respect to SH and RH spray take-off. * - Any high pressure steam extraction upstream of reheater, excluding FW heaters, + - Report data available-specific requirements will be requested. Efficiency data Cm^to¦ pu.rjLic Se)2i/ic,f qf po „ puE.Ha> C«lo/Moo Jo rt kiiAi-v. iSc-o • fl.j C-54 ------- Pcawt of>eftA-r>»& t>$ ~f~ . DATA ITEM UNITS Test No. Date Time Hours c&oo o/3 o toa° jo 10 DRAFT LOSS DATA • ¦ * ; SCAMtnlDuti " AH Air In "Wg AH Air Out "Wg Windbox "Wg Furnace "Wg Econ Out "Wg AH Gas In "Wg AH Gas Out "Wg Precip In " Wg Precip Out "Wg ID Fan In "Wg SH Outlet Leg TCs F R H Outlet Leg TC's F PULVERIZER DATA Pulverizer# * Coal Flow MLB/HR nr.w HI.07 tW.il * Pri Air Flow MLB/HR "Sec Air Flow MBL/HR Pulv Amps AMPS Pulv Diff "Wg PA Inlet Temp F Pulv Out Temp F PA Flow Damp % ¦ PA Temp Cont Damp %. Pri Air Fan Amps AMPS pill ¦/ Z'A C-"'1'//- •/." Tf . / L F tiz.f 127.2. 1Z7J ni,.? ai.i I'M -''J Aa/'c/f/l? "r&f-'p £ IZJ.1 l2M.t \|iu.7 I14,t .1 >r- ? /r. f Pulv 2-c <:<>n rvo».* '? F l2o ? ,'2 1, V n hi iZl.tr , r 12.1.7 p>m.) T'O ;»/¦ 1T{ ¦¦ i-\| £ , 1?M isyf \x W ¦ 7 1 is-7 f 13 The DRAFT LOSS DATA listed on this page is of value, but riot absolutely essential for performance analysis. * - When indicator scale is in different units, provide conversion factor. Efficiency data 3 _ Cu-STOMEI* I'^thUIC S€£^'<^C OF, Coi_or2Aoo Tk/5 . i . j btO on - '' pcl£QL.0, d«LOf/»Oo C-55 ! ------- fLAfJi nwii n DATA ITEM UNITS 2 Test No. Time Hours UOo itZo 1 3o© J?3f ttfo 0 /43o 'X/^iTaiJT &£a^. CjtftSS MuJ -% %Z-LC lel-Q? z 9,070 CuJlT Load mW(D "I'OJI-Efl TEMPERATURES - f n III Tim . f. " . : H7».7 ihhS~ -i ri,i Water Lvi Icon 33.S 75i.i/kr.& "ir/.V7v?,r Tftshttn 757.3/71x7 Stm Lvg Sec SH t F iaiZ 1 ^¦W.6 ?r?,? 37/. 9 Stm to RH Attemp ;i F iUo- 7 bOl.Z r»i.n 5V4,1 f?0.3 Stm Lvg RH Attemp £II F OTi STt.H s~t y i- ¦ 511-f rMf rfo.f Stm Lvq RH frrfL F 7 Z 417.1 111-7 qte>,f /<"/"»< j Water to SH Attemp 507 F tlt.<-f itl-t l£¥. J' 3.7 lio,) Water to RH Attemp S"o1 F t-7Z,V Lift liq.f Zh%,7 7.11, 4 tier./ BOILER PRESSURES Water to Econ (t>S PSIG 2-72-1 ¦ 7 XI to'. I e.^ 2707.4 Drum Press bob PSIG •unrs.f 7-ST2 . 3 ZSM-l WiJ.t IS si. 1 PSH in Press ~ PSIG —¦ _ — — — - Stm Lvg SecSH 601 PSIG 2-Hok'S Xiy/ o.fc/ 2aq PSIG in? ¥«?•« m>i> 1 y 6 & RH Outlet £t>3 PSIG ¥1 r.7 iiy.~ FW Ent #2 Htr S f c /ri .f /sr, 4 TJ.O IS"/. I mi.t #1 Htr Drain 4 f C tHt.o }<4 0,i n?1-1 <»TM 70 #3 MP tfTJl TETMP 10 F sr? r STS-2 ruz.z. fir if SlS-k T7t>3 STM To3WHrTfi- PRESS Lit, C PS16 5-2.0 5 Itf ^60 tiQ f}Bj£ {£) [7uu/.Z'A trtfJ J TfiKQJ OpP-UJE (% ti/to ft. J Cui ToMCtf: Puflu C SeRi/o , pue(?Lo (LoLoiZaoa Jo& hlO. ; £ 13-5 OE. 1 ------- l?Lfrrr ' o fefZAT/Ma DATA ITEM UNITS ,2. - —e» Test No. _ Dtitc Time Hours lax£/Zf£, // 00 mo • i$c>o / (ft (TO t <4 3o AIR 81 GAS TEMPERATURES flue Gas LugJEcan 21/2f f WtfjtrM 136.S/&U chx/mi Floe Gas Lvg AH 7o Jz \| F j LU.s7T.7f, ¦ui-ihiu ltS.fhn.1 ni-ifa?.9 2 6 Will. 5" flue Gas lvg Hot Precip lUzi F bolD/i/o.i stnxfoftx m-vnin 5to,o/slz.1 TMS/Sl7.t ) Flue Gas Lvg Pri AH — F — — — Air Lvg FD Fan IZ//3 F k-ojio.i U.t-jiLH 7Z.4/72- W-l/Ttj ) Air Ent Sec AH !<4 hS~ F t't'sjfl.L uR.r/t'l.? /of.t/i/i •= IW/iW.C ) Air Lvg Sec AH 22/z3 F 5$Ss/rstH ssi.bjm<£ fj6"7/X4J.i, &~3&Vnr.6 rJi/si-if.i- Air Lvg PA Fan — F Air Em Pri AH - F ¦ Air Lvg Pri AH — F _ Air Ent Pulv -r F Ambient Air /? F <-/7e>¥ LB/HR — — _ — RH Spray Flow 7o3 LB/HR 3~V.i3 37. t±- 7.5r ¦ SH Spray Valve Posit — % _ — r _ ¦ — RH Spray Valve Posit — % - - .— HP Extraction Flow — LB/HR —' —. -— — O3 Lvg Econ "job fa °7 % 1,0 7/2.71. z .§th>(,z j.llhsf 3.6'/2,«y 1,01/2.17 COi Lvg Econ % NOx (if avail) Oa Lvg AH % CO, Lvg AH % 02 Lvg Hot Precip % COi Lvg Hot Erecip % Oj in Windbox % - COj in Windbox - % NOx or CFA Port Posit + Fuel Analysis Burner # Out Serv * Relative Humidity %. r I © Advise location of flow nozzle with respect to SH and RH spray take-off, * - Any high pressure steam extraction upstream of reheater, excluding FW heaters.- + - Report data available • specific requirements will be requested. (2)- Efficiency data 2 Cojtogji; f?u.fiLi£ $&zvicjf Of puE(li-a C-olo/2aOo •Jo (3 nh-w 1J pi? - 0 J- e ¦» ' C-57' ------- PtAMT opeftAT ia»6 £>4T/ :"%C? DATA ITEM UNITS <2 — ¦ ¦—p. Test No. Time Hours 1 (cro 1/ ? 0 1 5^5-0 (5>o ¦ Jfc / M J 0 DRAFT LOSS DATA FO taXfech -«h • © -SCAHhaOfcrt) , -w, • AH Air In "Wg AH Air Out "Wg Wind box "Wg Furnace " Wg Econ Out "Wg AH Gas In "Wg AH Gas Out "Wg Precip In "Wg Precip Out " Wg iD Fan In "Wg SH Outlet Leg TC's F . R H Outlet Leg TC's F PULVERIZER DATA Pulverizer # - * Coal Flow fj '5 MLB/HR , /YV3 32- W7-37 At"5. ^ * Pri Air Flow MLB/HR * Sec Air Flow MBL/HR Pulv Amps AMPS Pulv Diff "Wg PA Inlet Temp F Pulv Out Temp F PA Flow Damp % PA Temp Cont Damp % Pri Air Fan Amps AMPS p^ls) ?-* C-cr-tfitz ~ 1= (il-t no, j ¦ Ill.i' IlLl IW-7. Put\] 7-t J F ft J. 3 127.7 12,7.9 117, f tiy.L .r r->i s/ T ' 1" r- I 23 .O IZJ.) lil-t li\-7 12/, r Qui J, P-D T £>>f F )2 k • 3 Ill.l. 1 2,7. t !2 tui" ! 2.4, J The DRAFT LOSS DATA listed on this page is of value, but not absolutely essential for performance analysis. * - When indicator scale is in different units, provide conversion factor. (2)- Efficiency data 3 _ ' " CuSlOME. pHfiMC SefLsitae OF(tGL.0fLA>o, Pll£6l.O, CouOC/tCo f. s\ ... - .' —A . n /% — t' C-58 ------- ¦ 1 Rep'Oduced 1rom : I best available copy- pL^T Oft ft * TliJC OAT A DATA ITEM UNITS X — Test No. Time Hours !$3* ) boO /^3o &rli. Si A! UJ * 72. ?r Z&>! ¦ lo miAi 3 5l u>J L0A6 PfiT-'AWO „ BOJ-LEH T£MP£ RATUHES - mHJri&an S»? ¦¥ ar^sT wx-/ 4»r4- J ¦. Water Lvg Econ Jll F s"J«-3 ivi'V Stm Lvg Pri SH Sl4-/nS" F iK-ihxu ikmfai - Stm Ent Plat SH — F Stm Lvg Plat SH — F — —. — Stm Ent Sec SH 7 / % F Stm Lvq Sec SH } F l7f-f fr'r.i IB Si, Z- Stm to RH Attemp n F stoA Sli.f r^. I ioQ.o Stm Lvg BH Attemp $11 F J-7/.f s-H.7 $11,1 Stm Lvtj RH F 9rt,o 177,/ 10/O.? 471 F 2x7.1 ISi.Z irf./ Hut BOILER PRESSURES Water to Econ £»S" PSIG 1 nn-i Z61Z.i Drum Press yob PSIG tfiSjT 2£"L4-t PSH in Press — PSIG — — , - — Stm Lvg Sec SH £.ol PSIG n PSIG %1e 1 HtZ.I HIGH PRESS FW HEATERS FW Lvg #1 Htr F _— — — — FW Ent #1 HTr 3 f C rz-P.C IZC L /Z-7.2 113. jT FW Ent #2 Htr S V C /Sn, 1 H7.1 '.Hi.!- 15^.? - #1 Htr Drain 4- ? c "lit-3 13.2.3 117.2 ' ,'lif .3 #2 Htr Drain £ / c. ir -hi. isi.i /Tl.l / 4o.V Stm to #1 Htr-Temp \| F O/.r c 7d,y stfe.r Stm to #1 Htr Press local. PSIG 70 c 3 Stm to #2 Htr - Temp Z F 7S4.I 7 it,H 710.7 (?OX« 1 Stm to #2 Htr - Press L oCL PSIG /7a IS% / ^5« £{4 0 •j 3 H? Hr« Pitfl/w T£Mf g> jjiTT€i ¦^p:0"J~x t^lST'Cu^ t&f£u (ft) 1^% ftu(L) CUS TOMEfi: Jo6 fJo. ; pu&u c SeRi/ite R13-5 02. oF CoLo/tAt>0 , Pw.£'3C-o C^oLoiZAOo C-59 i ------- pi-A/JT ' Of>£tZAT!bi6 &AT& DATA ITEM UNITS 2— Test No, Date {iftvfty 't/io/ZV Time Hours IST>» IS J 0 / it m U"} 0 MR & GAS TEMPERATURES Flue Gas lg£con 24 fc? F mjJus-j Flue Gas 1_vg AH ^o/z\| F unMfm.-J itttJlTS.' "Uz.iJl? a,l Flue Gas Lvg Hot Precip ibfz' F S7flS77.3 al-iisufi 516 f/ft ?-1 mJlni.l Flue Gas Lvg Pri AH — F .— - Air Lvg FD Fan /2/l3 F Ti-shf-o is-ihn 7S<>ht.£ ivr/v.o Air Ent Sec AH \14jj5" F Ut.x/aii ntviwl nh.flai.f HS'.SjiUJ Air Lvg Sec AH 22 /z3 F sii-i/s't? g-tn/m.? «7/jWJ Air Lvg PA Fan — F Air Ent Pri AH — F Air Lvg Pri AH — F Air Ent Pulv — F Ambient Air )$ F si,.C 'sf.,7 57.1 MISCELLANEOUS Feedwater F low 10 Z. LB/HR nti.'l /toi.l HHI-? SH Spray Flow tjoH LB/HR — — — RH Spray Flow 7o I LB/HR __ - SH Spray Valve Posit — % __ , — — RH Spray Valve Posit — % — - — * HP Extraction Flow — LB/HR — _ O2 LvgEcon Jabf3°/ % • ?, (-72.fi J* 2j?h.n COj Lvg Econ % 1 * NOx (if avail) 0, Lvg AH % COi Lvg AH % Oi Lvg Hot Precip % COa Lvg Hot Pxecip % Oi in Windbox % COj in Windbox % NOx or CFA Port Posit + Fuel Analysis Burner # Out Serv - Relative Humidity % Advise location of flow nozzle with respect to SH and RH spray take-off. * - Any high pressure steam extraction upstream of reheater, excluding F.W heaters.- + - Report data available-specific requirements will be requested. (2)- Efficiency data *£1Z ¦ pu/jLl^ S£j2i/\|C(f 0F> ^ pusdt-o toi,or?^Oo CTtifi Mulvw Act 5 - 0.1-e.nf C-60 ------- PcAfJT OfEftA~Tif6 t>A"TA DATA ITEM UNITS 2- ' . to Test No. Time Hours ! c/lo/XI ' 1ST>* / b C~0 i<5 DRAFT LOSS DATA ¦ ¦sowiwtotrt) -w AH Air In " Wg AH Air Out " Wg Windbox " Wg Furnace "Wg Econ Out "Wg AH Gas In "Wg AH Gas Out '* Wg Precip In "Wg Precip Out '* Wg ID Fan In "Wg SH Outlet Leg TC's F RH Outlet Leg TC's F ' PULVERIZER DATA Pulverizer # * Coal Flow J?/'3 MLB/HR Nt7f IVT.iJ /vr.tl * Pri Air Flow MLB/HH •Sec Air Flow MBL/HR Pulv Amps AMPS Pulv Diff "Wg PA Inlet Temp F Pulv Out Temp F PA Flow Damp - % PA Temp Cont Damp % Pri Air Fan Amps AMPS PuliJ 2 -f- c^aUahi Te^p. P iff'i l-Hl - — — — 0^!.) 2-6 " " F' III.* t2 J.6- 12 2.? ,z".0 PunJ 2-C •> (Z , III. ° n/.z lZo-,3' iZ-a.y t?i0 LC-61:1 ------- YLfKrtY oj'fc't, iimu in DATA ITEM UNITS 2 ' - Test No. 1 Time Hours cm of e a oi jo o-o o«i J« /O 3 & ; . BOILER TEMPERATURES ¦ mrnacmi&mm - •' * MrHI \ W.J Ve.0 Hit's Water Lvg"Eeon J/l F $31.6 rwsW 5"5t.J m-y svo,r W3-3 Stm Lvg Pri SH 574- / X"i5" F insfinj luiibv/1 -v/ohu-i m.ihas isbxhiv- Stm Ent Plat SH -— F Stm Lvg Plat SH — F .. Strri Erit Sec-SH - <7 / « F v i.lnu 1 tiz/vH-f W'^ni-9 -"iWhii.f -?Vt.#7}U UoS~hjf. / Stm Lvg Sec SH 1 F tu-t m-g /r>i 7-7 Stm to RH Attemp n F ajv i"?i. J Tt P."L L H-!> « Stm Lvg RH Attemp SH F slf.f s-jr t. ' .TI3.L, I Stm Lvg RH toz F <5 77. 7 o 102.!,, i /6 »t/.-/ Water to SH Attemp SO"] F z 7 C m tio.z. »9t.° itti- /J1.5 /f/-¥	yz/o /©6 ' 4 o-O -/Z Wo W3 Hf rtrc pA/m T€Mf g c /ff l O0€lB£ peZts U4t£V @ oSvs.tHlS. tU5T0ME^ PwflUC S£Bi//te OF 7o6 do. - £6-5 oz. % fti.i /W.3 /$r.y at,/ Co LotfAfo J. Puerto CotoiWfto. ------- /7<_AaEfZ#TtM6 P>T# DATA ITEM UNITS - > - ^ Test No. Date iz/nliH Time Hours 0Q-50 0$O" of 3 0 5 of /o ^ 0 • AIR & GAS TEMPERATURES ) ¥MmGmLw£xn iM-hX 1= f rtjsjrff-l. rm.iifi > WoeGas Lvg AW 3o/zi F 2W. l/2?o,4 2k>.okitt it7!72&9 irt.iM 7.1 ) Flue Gas Lvg Hot Precip Z^fz") F SiiMlrn.i $7o>/s?2.» xwXfat.t- OJX'/sil-l sw.7 /ru-« Flue Gas Lvg Pri AH — F — - _ Air Lvg FD Fan I7.( 13 F U-i/it. 3 iofifou f <17/iz.} f tjfbH-i 1 ) Air Ent Sec AH jIS" F IV-^/iio.K ioe.7/,^1 lio-sful-f SiojtjmA t s>t-l/llS-1 Air Lvg Sec AH 22 (t3 F svf-f/s-ii-s Sl1-7(sxt mVx-iS'f- ri-M.i /rzt.« JUJZr, 7.? Stz Is to- 7 Air Lvg PA Fan _ F ! Air Ent Pri AH — F Air Lvg Pri AH — F Air Ent Ptifv — F Ambient Air 1$ F Hi,.') 1172.1 i&z.l.Y nio.7 7 SH Spray Flow qoH LB/HR — _ RH Spray Flow lol LB/HR — HS\oi — Ltf.m SH Spray Valve Posit _ % — — — _ RH Spray Valve Posit — % — _ • - — - — "HP Extraction Flow — LB/HR — — — - Qi Lvg Econ 30bfie"/ % 1.2.i/2.6 J 3.0r7z.4f iMhM Wk.St "5.0^.43 iM/W CO3 Lvg Eton % NOx (if avail) Oj Lvg AH % C03 Lvg AH % 0a Lvg Hot Precip % COi Lvg Hot Pxecip % Oj in Windbox % - COi in Windbox % NOx or CFA Port Posit + Fuel Analysis Burner # Out Serv ~ Relative Humidity % ¦i/ Advise location of flow nozzle with respect to SH and RH spray take-off. * - Any High pressure steam extraction upstream of reheater, excluding FW heaters. + ¦ Report data available-specific requirements will bo requested. Efficiency data omtopu^cic sea^icif oft Jn rt i'I *•>• - rt ,1 —' puEfti-o Couo£/W>o ! C-63 ------- PtAMT Of>efcA~T>»& £>4t/* lr DATA ITEM UNITS Test No, Date W/i //¦¥ Time Hours O130 Qtoo of 0& C7I <3 ! OOo "DRAFT LOSS DATA - ¦1 SCMMtaKM ' - AH Air In " Wg AH Air Out "Wg Windbox "Wg Furnace "Wg Econ Out " Wg AH Gas In " Wg AH Gas Out " Wg Precip In " Wg Precip Out "Wg ID Fan In " Wg SH Outlet Leg TC's F RH Outlet Leg TC's F PULVERIZER DATA Pulverizer # * Coal Flow 2/3 MLB/HR ISV.ll iri.ef 15-2.3? iSl.ftf irj.ro * Pri Air Flow MLB/HR "Sec Air Flow MBL/HR Pulv Amps AMPS PulvDiff "Wg PA Inlet Temp F Pulv Out Temp ¦ F . PA Flow Damp % ¦ PA Temp Cont Damp % Pri Air FanAmps AMPS p«iV. I-A CoAL/AiK T£W> F ns.i JZ.4..T lii-r 1 Lg. I iz-h.f 7-6 I17. S" f!7.3 f z. ?. S 117.0 2-C F ,11.1 III J ii3.i ur-? tli.e in.9 i-O r llfc-l uy.7 iir.1 i The DRAFT LOSS DATA listed on this page is of value, but not absolutely essential for performance analysis. * - When .indicator scale is in different units, provide conversion factor. - (D" Efficiency data 3 _ CUSTOMER- S6OF ,C«t.0f2 AOO , p^S/il-O, CatOCADO -r- /"J ... - /> —<* r* * r- - - •' C-64 ------- pLftriT ofeRAT^a OA-jPt DATA ITEM UNITS <2> ,1V o Test No. Time Hours /d 30 tf oo "So 13 eo !}S» i<4 oo ^STftrT,££WGWioiO MuJ 27129 zrt.r? HZ.qj 2 •©¥ ILL.' 24,!,?$ - . boilem temperatures fli^tar9taS0OMi <^S"X.4 W-? ¥57.7 45-5"- ra/ Water Lvg IE con J/l F s-yj.f 53f.i~ r5(#.3L Hr. u StmLvgPriSH St4-/ ft? F 7vwmn Tf 'i'" r v i irr TTJ.iA* /74/t Stm Em Plat SH —- F ( JT^/nwr — — Stm Lvg Plat SH — F .— — — — — Stm Ent Sec SH 7 / f F 7H4-3huf "WB Vw l THUHkvn ?3?5/7H.\| Stm Lvg Sec SH 1 F /Oil./ ur-r Vi'lM 17T« 3 'Jf 1.7 Stm to RH Atternp fl F r«.H koi.r T7V.4 nt-L Stm Lvg RH Atternp £11 F s-?r-7 <^9.T S~? o,J" 54 t.c rs.?.£» S7Z\ Stm Lvg RH fT. F "57;,? wo.t taa.$-,b MM f 73.? /cos. 1 Water to SH Atternp 5"£>7 F Zto-1 zrh-i 2.E&.7 2I 25 7-i tsi> i Water to RH Atternp 5"o7 F zto.l Zf7».f tSi7 2b5" PSIG zfc/r fc ¦24,7°. r ¦Liii-S" ZloH, b TJetU.r Drum Press yob PSIG 2J3fc .\| Z-Sio.l ISI%-3 zsvsJ 2 JB2«£ ZS~b7,o PSH in Press — PSIG — — - - — —' Stm Lvg Sec SH (,ol PSIG mit-7 2,517.1 Z"Jf2.7 tm-o 2 4« / 2ii1 RH Inlet PSIG m iy<° QH.O MM?- 3 4ZI-I un. 1 RH Outlet UoT> PSIG Ife/.o ILLo SU.o 44.Z..1 UtA ffei.l HIGH PRESS FW HEATERS FW Lvg #1 Htr F FW Ent #1~Htr 3 / C fz?W S24.3 IA&S- ni.7 12 f- 3 iZh.H FW Ent #2 Htr £ f C i v^'4 \4l-3 i -<3 tx-i.i ¦ ts7-t is 7.x Stm to #1 Htr - Temp I F i"l.l rfi.x s-f\|,r 5t7. 4 Stm to #1 Htr - Press L°cL PSIG 7 (¦r it * 75" 67 £5 Stmto #2 Htr-Temp 2. F 75s.U 76?.? 7?X.3 •745 J 76S.I ifzi Stm to #2 Htr - Press t odL PSIG I7«/ /re / 6o i fo t l(rO 1st Fui e/r 3 we ht n-r^p 7 C itl.7 l%7* JJj.f ' 113.4 Stni 10,7 V/o 1 4vMm TCMf 8 c ,et1-6 2°°-& 1^1 <"K\| . cus ioneiSs putiuc see^c£ of £01.0/2.>0;f>ue®LO c-vt-oe/i&o. Jo6 do. • £6-502. ., 1 / 1 i C—65] ------- PlA/jt operzflTihi6 p ^ DATA ITEM UNITS 3 - Test No. - Time Hours 11 OCi H3a I\o 0 ibJ* f C?® AIR & GAS TEMPERATURES Flue Gas Lvg Econ 7M faf F SVi-3/rh h (,07 /VI ¦1 rif rlU/R/.i' Flue Gas Lvg AH Po /zt F n 261.0/171>. uafm.x l< ,1^72.6 7t5,f^7i.2 Flue Gas Lvg Hot Precip -i(,fzr F Mz -7/ar.i ni.t/sizs 577.1/5-57. s-irxfcus .5WJy&-73 F lue Gas Lv<3 Prl AH — F — - — _ Air Lvg FD Fan 12/13 F ii.1/6 7, 5 mms m.ih4- f 7i.i! 11 J, Air Ent Sec AH 14 Jf F mm/< a.f ni.ihi.v iH.i/fle.i H/ Air Lvg Sec AH " 22/23 F S-u.y/jTj.'i sn»sts 27.2 5J5.//C2.7J Air Lvg PA Fan — F — Air Ent Pri AH — F - — Air Lvg Pri AH — F — — AirEntPulv — F — — — A-7 t Ambient Air i$ F S"2.~? TZA SX. 1 Tt.f VJi' ' J?gv£= &t.2. MISCELLANEOUS Feedwater Ftow lot. LB/HR lb2-9"7 ' ltK1< O l^to. 1 f 0 SH Spray Flow ijoH LB/HR — - — — RH Spray Flow 7o"h LB/HR i-ol — V* — — SH Spray Vaive Posit — % _ — ¦ — — — RH Spray Valve Posit — % — , — __ — •HP Extraction Flow — LB/HR — - — — 03 Lvg Econ "jofe/3'7 % ?.(z./z~67 i.f/z, tr J.0f/2.7l Lir/z>\| 3.U/2-SO COj Lvg Econ % * * NOx (if avail\| 0, Lvg AH % COj Lvg AH % Oj Lvg Hot Precip % COj Lvg Hot Precip % Oa in Windbox % COj in Windbox % NOx or CFA Port Posit + Fuel Analysis Burner # Out Serv Relative Humidity %. ' ?¦ Advise location of flow nozzle with respect to SH and RH spray take-off. j * - Any high pressure steam extraction upstream of reheater, excluding FW heaters- I + - Report data available-specific requirements will be requested. j (2)- Efficiency data j 2 l CiLt-/SLtC $0£t/(C(f of c^oLpt^AS>o pu£(lt.O C-ULOr?/^Do } •To.<3 i 2 A-^aZ. _ 1 C-66 ------- / DATA ITEM UNITS A 1 J Test No. Date Time- Hours It) Jo ILtro H3o 13«° t3 Jo /¥«•? DRAFT LOSS DATA FD Can JKxh SCAH In {Ourl ** Wg AH Air In "Wg AH Air Out "Wg Windbox "Wg Furnace " Wg Econ Out " Wg AH Gas In "Wg AH Gas Out "Wg . _ Precip In "Wg Precip Out "Wg ID Fan In "Wg > SH Outlet Leg TC's F RH Outlet Leg TC's . F PULVERIZER DATA Pulverizer # * Coal Flow f/3 MLB/HR irl.06 tsroMz (Sb.&Z, /ST.ff N1.lt> * Pri Air Flow MLB/HR * Sec Air Flow MBUHR Pulv Amps AMPS Putv Diff "Wg PA Inlet Tamp F Pulv Out Temp F PA Flow Damp % PA Temp Cont Damp % Pri Air Fan Amps AMPS Z-f\ CJOM./M TsmF- F l U.i tlS.i. 117.9 {^4 ' tM.S Ml H Z'8 ------- PLAfiJT 1 IAJ £i OA T/t DATA ITEM UNITS A JZ-' Test No. Date 'V«//V Time Hours 1H1 o tfbe [. 2° , BOILER IEUPERAJURES ¦¦ -HftMii'iXr'wi 1 ' ¦•SDQ • •\ F Vrxa" ¦ Water Lvg "Eeort Jil ¦F ill-.V StmLvgPriSH 5/4- /ri-T F wt/nn 7»w/JS4.1 Stm Ent Plat SH — F Stm Lvg Plat SH — F ¦¦ Stm Ent Sec-SH - 1/t F 1ST>j/tj3 7VJJ"/?n* Stm Lvg Sec SH f F ff7.I < Stm to RH Attemp n F g-g¥,o Stm Lvg RH Attemp SH F S~7t.l S-7V-/ Stm Lwg RH F Water to SH Attemp SO7 F vsrM' Ifh-f Water to R H Attemp So1 F 2.ST-4 2iar BOILER PRESSURES Water to Econ 6of PSIG 1-^7 US Drum Press bob PSIG Z £()¦ 2-XI J"-/ PSH in Press ~ PSIG Stm Lvg Sec SH £,o! PSIG U ff. ° RH Inlet 6>o4 PSIG yol.o VrU.o RH Outlet {,qT> PSIG m.6 HIGH PRESS FW HEATERS FW Lvg #! Htr F FW Ent, #1 Htr 3 / c (Zt.l ttk.t- FW Ent #2 Htr S f C /•/7.7 /v ?,7 _ # 1 Htr Drain A- f c li 1.7 »%•«? #2 Htr Drain & / c trio IS"? J Stm to #1 Htr-Temp J F fa G> 4 ?f.7 Stm to # 1 Htr - Press L°CAl- PSIG bj 6i" ~ Slm qi #2 HSr-Temo £' F 1 171.1 ! Sbvtv #2,'HO"-- L-&K. PSIG in FlA1 EfJT ft J HP HT/e T£/«P 7 C fit.? ttf-r STM To 3 W/9 XT* TfM/J to F ri7 TTf'3 5TM To #3HPtfT(t tofe C P5l6 t/Jo tf/O PW/M rewf g c /a . 3o{i ftifli 7 fcQ—SoZ- ¦ t C-68 ------- pLtJT ' OfalATI^a :'V / 0) (3) ^ DATA ITEM UNITS Test No. . Date 1 %/«M Time Hours NJ° iron AIR fit GAS TEMPERATURES Flue Gas Lvg Econ 2^ faf F n.i/sn ¦? stfi&w.H Flue Gas Lvg AH 2o /z 1 F ui Flue Gas Lvg Hot Precip zUtS F fis-'/rar-i' snh Flue Gas Lvg Pri AH — .f © © § © © © © © Air Lvg FD Fan (Z/\|3 F 7^.1-/7^,4 7r-f/?rJ" Air Ent Sec AH I4//5* F tH-tjtlU-t 11 j.i fti-1'4 Air Lvg Sec AH 22 fz3 F aizkioi n 7-iyiii7 Air Lvg PA Fan — F Air Ent Pri AH — F Air Lvg Pri AH — F Air Ent Ruhr — F Ambient Air j$ F i o-t iff 0. L MISCELLANEOUS Feedwater Flow 90 Z. LB/HR I H3I.Z. SH Spray Flow loH LB/HR — RH Spray Flow 705 LB/HR - ¦ _ SH Spray Valve Posit — % — — RH Spray Valve Posit — % HP Extraction Flow — LB/HR Oj Lvg Econ 3obfl°/ % l.oCllS' COi Lvg Ecan % NQx (if avail) Oj Lvg AH % CO] Lvg AH % Oi Lvg Hot Precip % COj Lvg Hot Precip % Oj in Windbox % COj in Windbox % NOx or CFA Port Posit + Fuel Analysis Burner # Out Serv C4 klUUUlillY , %. l; Advise location of flow nozzle with respect to SH and RH spray take-off, * - Any high pressure steam extraction upstream of reheater, excluding FW heaters. + ¦ Report data available • specific requirements will be requested. . (2)- Efficiency data 2 ' pu.rjcic of 00 ^ puEfh-o ColofMou ?o<3 : &A-SQZ. _ ¦C?69 ------- , KLMWl ucti'M ma»£» v' 5-14 y/ DATA ITEM UNITS 2. / i © Test No. Date i %tuim Us/n!if Time Hours DRAFT LOSS DATA - WJftmDisdi "W§ SCAHIti (Out) "Wg AH Air In "Wg AH Air Out "Wg Windbox " Wg Furnace "Wg Econ Out "Wg AH Gas In "Wg ' AH Gas Out "Wg Precip In "Wg Precip Out "Wg ID Fan In "Wg SH Outlet Leg TCs F RH Outlet Leg TCs F PULVERIZER DATA Pulverizer # 'Coal Flow #/3 mlb/hr liibti, 1 v£ f H-S-1 " 7-4 " ' f I ltd " 2-£ i. " pr 11H .0 ci>ny " Z-D >J " f U k-b 1 v?.z ' i M . V The DRAFT LOSS DATA listed on this page is of value, but not absolutely essential for performance analysis, * - When indicator scale is in different units, provide conversion factor. (Ty Efficiency data Cdj-roMETg ¦ c Se"fc«/»tC OF CeLorzAoo, pn£6t.o, Colorado .ThA R{\-5oZ. >' C-70 ------- DATA ITEM UNITS Z Test No. ri/fz/pw Time Hours Ofeo C?3o 0 ^.pO O?lo (000 folo X(JSTflJT SRA55 333. St 7/1.37 3 2.0,?(hn..i ifhihxiJ isr-sjyi-p' 7 l&.th&z Stm Ent Plat SH —i- F — ' r Stm Lvg Plat SH —¦ F — ¦ - - - — .—. Stm Ent Sec-SH _ 7/8 F 7SSMtm? 7J» isi.s/i^X isbthov-i 760/in^ 7•suzhutf. Stm Lvg Sec SH f F , Tks-U ! Water to SH Attemp SC>7 F 170 2-7/7 i tf.i 2feU Water to RH Attemp 5"o1 F ¦ 2?» %7t2 2^1, t 2tt,Z ¦ui.4 2A"?-3 ( BOILER PRESSURES Water to Econ £>oS PSIG 2")V0,P Z71P, 7 %"]%i .7 3?^.? 272 W. 7 Drum Press bob PSIG z >-?/,y 2-« ?. V z^rs.r 1ST2J.6 t-s-yr. r PSH in Press "~" PSIG — . — - — — — . Stm Lvg Sec SH £ol PSIG 2«»2.f 2V02. t HjoV.2. RH Inlet PSIG r,0 iss-.r i^y.o i rr.t_ iXS^ #1 Htr Drain 4- c / ¥©>7 H Ar . cus Tone#; puau c Sefs^/ce of Colozapo , F'uefft-a c^loisaoo. Jo6 fJo. • /? 13-5 o2- 1 C-71 ------- sir PlAaJT Of&RATI DATA ITEM UNITS Test No. ~ate J2-. Time Hours OfOO otZo O fo cqio too 0 f#3o AIR & GAS TEMPERATURES uutht-1- Fjuegati-ygfcon 2.4121 ISlJ-j&VA yyn-1 nnBG»%gH ?o/l UoSH6-i zahii'i ley jjioil? lUjhtU ' Flue Gas Lvg Hot Precip zifx &tSAfa >1,6 & of-l/hrf.? !>Sa/(t6t -f Flue Gas Lvfl Pri AH Air Lvg FD Fan (z/[3 47.1 hi. u 9S'ifyr-6 E!A 6 fa Air EntSecAfcT WM/<}7.t 1lAiltX °i7 ten/%. 9 Air Lvg Sec AH 12 23 rNl^jrV^ i'sUVsvi-t m 2/m 7.S Kitl/Mi sVl t/m Air Lvg PA Fan Air EntPri AH Air Lvg Pri AH Air Errt PuKr Ambient Air jL 3«.^ ??.3 2?<7 31,3... 3)>? 3 0.7 MISCELLANEOUS Feecfwater Flow ?o2. LB/HR «-/ ZWz.,6 llf7.7 liM2uL 1<17.0 SH Spray Flow noH- LB/HR RH Spray Flow To 3 LB/HR IS" «/2, ?2_ 3 J. ?3 4swr S2« <44 SH Spray Valve Posit RH Spray Valve Posit % 'HP Extraction Flow LB/HR, Oj Lvg Econ COi Lvg Econ ?o\|>/3»; % % 2.1 lk-7S 3.1i/z.6g (.23/2.3V 3,?W/, Z.tl 2-? NOx (if avail) 07 Lvg AH % C0f Lvg AH % 03 Lvg Hot Precip % COi Lvg Hot Precip % Oi inWindbox % COj inWindbox % NOx or CF A Port Posit + Fuel Analysis Burner # Out Serv Advise location of flow nozzle with respect to SH and RH spray take-off. * - Any high pressure steam extraction upstream of reheater, excluding FW heaters- +^- Report data available - specific requirements will be requested. ~ Efficiency data 2 CwJts^cR.-. pu-ijLI C SeaU\|C(f Of ^oi-OftA0x> , pu8lll"0 Cohort A Da C-72 ------- KtrtWT ,t>re7C«"TiA>6 PA-TA f DATA ITEM UNITS 4 ' Test No. t2j ¦ —-TV-, ' Time Hours OZoo 0$$O 0900 a9So /f Js • DRAFT LOSS DATA - - - - 1 1 ' - -"!!! 1H -"l •tMib, - • wy . < - AH Air In . "Wg AH Air Out "Wg Windbo "Wg Furnace "Wg Econ Out " —' "Wg ; AH Gas In "Wg — AH Gas Out "Wg Precip In "Wg Precip Out "Wg ID Fan In "Wg SH Outlet Leg TC's F RH Outlet Leg TC's F . PULVERIZER DATA Pulverizer # • Coal Flow % 13 MLB/HR Pj(f' 0 ?:07 IZ4.6L tvo-if t'-fz, 6 Ml, 97 * Pri Air Flow MLB/HR * Sec Air Flow MBL/HR , Pulv Amps AMPS ¦ PulvDiff "Wg PA Inlet Temp F __ Pulv Out Temp F PA Flow Damp % PA Temp Cont Damp % Pri Air Fan* Amps AMPS Z'A Tt f3 F )U )lg, O m.* 1 if.1 tt \%t, L 2". 13 » >> F •ur.t tZJ.'i it?, t iil.i it"? * (i-7.2 » 2-C '• '! F i 21.7 iZ3.o 1LIJ U3.J 11 J.o Hi.4 ,, 2-0 •' " F IZf^ I li. h itt.t iZJ.o 12,4-7 IZb.f The DRAFT LOSS DATA listed on this page is of value, but not absolutely essential for performance analysis. * ¦ When indicator scale is in different units, provide conversion factor. d> Efficiency data 3 _ CU5TPMER. pn-flt-lc SC£i/iC€" £)F CoLOfZAOo, f>H.£6L0, tZoLDlZADO -p. ** ^ » C-73 ------- KUWT* ot'&tcvn tut* path DATA ITEM UNITS Test No. »2J/ ?/(?£/ Time Hours 7 I /*¦ ilao til O I Jo 0 /3?0 jLf LfO i«? a i't/fTffKTT 6(taSS &si- 7-1 i,$r Zi 6,S2. 3 or, sz Z1o>l7 20 tujiT" oij t,o« oev><^o . BOLLEH TEMPERATURES , j 1 ¦ - - ¦ <6/9z - .jf <¥£1,y HbS.0 'j Water laleon • • 3/1 F fSW-3 SS%,t> STV. ^ ' TT7.Z sV4. 5 Stm Lvg PrJ SH 57 4- / UST F 7il. i/p/o,y isin/wj 7rih&t ^.e_ Wi>1 }fkt£ / ¦ =i ^ Stm to RH Attemp n F tot.) tik-l 6)3.9 io 0 1~(a m.1) 6 10.7 Stm Lvg RH Attemp 5 If F svi-i 5"MI. £? ST mt>, 1 HIGH PRESS FW HEATERS FWLvgll Htr F FW Ent #1 Htr 3 / £ I3/.2 nu Hhr (12. j. 1 l?e.r FW Ent #2 Htr S f c /jtj,/ /rs./T J HP HT* tr/^p 7 c ¦/fv.ar (lf-1 . ftps' t°tzj W-b- itm To 3 HP Htr temp ie> p. «.z.1 rMif.fc ^7-J i'S-Lf s-ji.t " STM To #3H?rtT£- ?/?£Si tW< L P5l6 tjSS LjfO 47s ' o 4 to vMiti TEMf 8 C 2 ol S- 2o5.o _ 20a.^ zoS.I tUS ToHSfi- P^iiLlC SER&ce aF CoLoa RueBCo CvLo&A&o To6 l°i ; . - ,^6-Soz. > C-74 ------- ^Jk1 pcfrArr o'pefcflTina "V DATA ITEM UNITS Test No. Date Time Hours It oo t(lo i?0 ® IJ!" / u. jfi^4 s^t>nku.\ "stiifcV't .1 whi-r Wfvt, Ht'ijm Air EntSec Ay vf\s t. i/ "$¦ yifoaa- f l9i.fi ITi-3 fOi .tfiol-if Air Lvg Sec AH n/23 fvr/sVfi ^ rvi. & if IN 14 PV/.yjtfj SV«iA-.?r> ru.tfsi+s CD © Air Lvg PA Fan Air EntPri AH Air Lvg Pri AH Air EntPulv Ambient Air jL 3/. 1 -ILL 1°.i£_ 3a,r MISCELLANEOUS Iftl.k FeedwaterTlow ?oZ. LB/HR nsi- Z ftlo.? Iflt, Z lUI'Z IMIlL SH Spray Flow LB/HR RH Spray Flow 1ol> LB/HR o,3 4f-or 44-<7 qf.zz ^¦37 SH Spray Valve Posit % RH Spray Valve Posit % 'HP Extraction Flow LB/HR 2.t7/2>r Oa Lvg Econ Jab/SQ't % AVz.il ¦lAt/l.tl CO] Lvg Econ % NOx (if avail) Oa Lvg AH COa Lvg AH % Oi Lvg Hot Precip % COi Lvg Hot Precip % Oa in Windbox % CO] in Windbox % NOx or CF A Port Posit + Fuel Analysis %Z Burner f Out Serv _ Br Advise location of flow nozzle with respect to SH and HH spray takeoff, - Aiiy high pressure steam extraction upstream of reheater, excluding FW heaters, + ¦ Report data available - specific requirements will be requested. (2)- Efficiency data , 2 CujTn1^E7Z > pu.f}l 1 ^ SoZ^ICf Op c-oLOfiA Do O (LoLOi?/^Oo C-75 ~~------- C-76 I~~ ------- rt-HN i z r I WW C/t ( rT DATA ITEM UNITS > 0< Test No, Data iz/a/m Time Hours ISP.o £.i"3o Lies lb 1° XJSTAiJT SSJ. (^055 3UW5 3^1,17 J BOH EB T£MP£RATXJR£S T IMaiiMSiM''" ..'•'55?-- •- F-- -i Water L-wjtcon ?H 'F 5-73.(? StmLvgPrlSH SI4-/ fiS~ F W'ffm. Stm Ent Piat SH — F Stm Lvg Plat SH '— F Stm Errt Sec-SH _ 1 / t " . F 7i»j/m3 77 Stm Lvg Sec SH i F ioH-7 lezi.7 ' Stm to RH Attemp n F {,33.1 Stm Lvg RH Attemp SH F Si 1 ri?.2 Stm Lvg RH - bol. F Ibd 2.3- Water to SH Attemp 50f F ZM nt.s" Water to RH Attemp ?on F lll.L •bti'i BOILER PRESSURES - Water to Econ 6e5" PSIG 27N-? v??7 Drum Press bob PSIG 253 4-S wm.y PSH in Press — PSIG _ —. Stm Lvg Sec SH £0/ PSIG 21^1-7 2331-? . RH Inlet PSIG S-Zlff 5T4.» RH Outlet (,o"i PSIG 473.V 5-It? HIGH PRESS FW HEATERS FW Lvg #1 Htr F FW Ent #1 Htr 3 X C I^Z.Z. m.t FW Ent #2 Htr £ F c 1 s{- i )S7>Z #1 Htr Drain 4 r c (31,0 1 «+lt0 #2 Htr Drain £ / c. 1 /4f.fc Stm to #1 Htr-Temp / F rfi izSH Stm to #1 Htr - Press PSIG ?? - Sun to #2 Htr- Temp r F 7173 fife,? Stm»#2Htr-Press L«Ct- psjg 2/0 • ItL fui EfJT j Hf> mn re/Hp 7 c 117-o i 1.f ^TM To «3 «T£ TEMP /IP p SI o Jo6 aJo- ; £6-5 02. '1 WS"5", Tc ?e?« §/S»J7T fueBi-d C-oi.o«2/udo , C—77 ------- PlAaJT o'pejZATtsM DATA ITEM Test No, UNITS Date1 Time Horns IS" Ou So AIR & GAS TEMPERATURES Flue Gai Lag Earn-1 24 h€ " * ZofZJ Tfc»€»l-»9- Air EntSecAH Mil? % >wir-7 Air Lvg Sec AH 12123 Air Lvg PA Fan Air EtrtPriAH Air Lvg Pri AH Air Ent Pulv Ambient Air dL 30 M 3SML MISCELLANEOUS Feedwater Flow Jl°A LB/HR )UoS ZlZg.l SH Spray Flow lot LB/HR 1Q.T7 RH'Spray Flow 321 LB/HR WW HI-72 SH Spray Valve Posit % RH Spray Valve Posit % 'HP Extraction Flow LB/HR Oi Lvg Econ COj Lvg Econ Soy/3o'/ % 3.W ?ui NO (if avail} 0; Lvg AH % © COj Lvg AH Oi Lvg Hot Precip % COj Lvg Hot Precip % Oj in Windbox % COj inWindbox % NOx or CFA Port Posit + Fuel Analysis Burner # Out Serv MbbwUi Advise location of flow nozzle with respect to SH and RH spray takeoff. * - Any high pressure steam extraction upstream of reheater, excluding FW heaths. + ¦ Report data available-specific requirements will be requested. (2)- Efficiency data . 2 CMJTo^en: PUBLIC - S£&VlC(r of'^LvaAOQ > puetlLO COLO#ADt* •V. A ... * c-Z8j ------- PcftfJT ,Of>eKA-Tt/t> VQtA DATA ITEM UNITS L ' 1— Test No, Date ./ViVW ; «• Time Hours iro0 1 n» DRAFT LOSS DATA • - :-4 -h 1 •SCAH In Out) "Wg AH Air In " — " Wg AH Air Out "WB Windbox "Wg Furnace "Wg - ! - ' Econ Out " "Wg \ AH Gas In 'Wg — AH Gas Out "Wg Precip In "Wg Precip Out "Wg - ID Fan In "Wfl SH Outlet Leg TCs F RH Outlet Leg TC'i F , - ... . , • PULVERIZER DATA Pulverizer # • Coal Flow fit3 MLB/HR 147. to- Pri Air Flow MLB/HR * Sec Air Flow MBUHR Pulv Amps AMPS Pulv Diff "Wg PA Inlet Temp F Pulv Out Temp F PA Flow Damp % PA Temp Ccmt Damp % Pri Air Fan Amps AMPS • pf4V. Z-fi Cefit/fi: £ -T<3+f F 124.% fU.fc t( 2-6 '< " p 12. rW u 2-C c: 111.6 fZ2J. ,v 2-s> • F its-.z - The DRAFT LOSS DATA listed on this page Is of value, hut not absolutely essential for performance-analysis. • - When indicator scale ts in different units, provide conversion factor. 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S4 JT 33 <z — ' "irr \ 7 J?? • >0' /1 ¦ r ~}C3 a> •¦ '• - t ' /pQK. fL-tSZ" ( 7 V To ?* i 6r «— - 1 ?T hr^ J?fr wi "te> fsr 1& Total i SHIFT l>URNACC SLAG COMOlTlON \| SOOT &IOWINQ, tOQ •ui af sarute Omtip 1 Oraue3 GreuO 3 Qroup A Qroue3 (}>«UP 1 Orawp I OroKJO g 1300 - 0?OO X. > V .¦ - f s < , » > / * •. % * ¦/ * QTOO - 1S0O v //. W ^ • • y- - ;•' y //-¦ X ISOO 3300 ZXyf / >-/ £KjOL.. XYxTC X ------- FORM NO 319B • . o ; VO ' <0 WVOOAK GENERATION HOUR 4' 0- f c- i -j -z r .7 tr- .T '/ 1 NET ENDING Grou Goaraiion Auitlury Tr\|ntlorm4r Siart up Tranilormar GEN Molar MW Water MW Malar MW MWH 1 ll(e< lC n 3 j - vo H 1 2 1 ? O'l '7 ^ ¦ j . i j V '¦ V ?,J? 3 ;; /, 7 ~ 1 ' ' r 3^;? 4 •4-i 7 v £<; / 2 7 M ?7 5 y1 t j ? & : 1? 4 n 1 .To G IS MH - & i , 3- J 7 0 -f o* 'J. Sub Total ?') j Z 1 1 I \|-:v / 7') p Oo 0 7 '/ 3-5 10 ; * W? '.7J d JT7 11 roz-? o ly 'J- life 1.7 \'1. "> T ^ 12 'Hfl ; V '3 ,.\0n i j (? ! J j <¦• ?>--? 14 ! ;7 ."•/ '' t 7 76 Sub Toi»> rS^t ? lk s • 5 r/7/6 5f7 70 rl7 ¦6 «"Z "7 7 / 5 7A.3' J2 7 17 <2 JSC, ^27 7 y 24 7Sl 7 10 r 3 7 ? te J LO / nri /5 J 3 1 19 S3I 17 Jr? /zrs 2 310 20 'lSQ6> 1 itl 1 39 33 O 21 1 l? 1 1 JO 12.8 22 (.HTin 'JSC. I21S O 317 SuB Total T>ct 3.?(* \ 6,<,f 7.JY 3K.11 23 AW r?/S / J 9 fob ?a- 7 24 CI "1 J «s 6 « al °i V J' 13 1 Dav Total 8Y^tf 7 / ^ rs- Prv Total Tl to Dai* Nat Main Xmlr V#ri Ool Gan Var» In Aui Xftitr ACC 1A2 MW ACC IB? MW Coal Handling P'M . 1 d- c ?. 7 Sovoi* nox4 P»ev Ol Oi j J ' <>?• arn >- ¦"/ ¦'^-1 Total 7 7 0.? I a-f _C i-. 3 - I ^ 11 / i Ifl Mo —- _ Coal Imagralon SCALES A a c ~ E HI H3 Prei vo <79^7 /O'-Ufa noiaH r^ooi Prr. " 'i ^ I0H 110 3/flf ¦.; •• •- • j'-r-O./ Total Z201H 19711 2979 1 - Ifl Mo 1 ZOt.TS ITrflM 110?. 5 — WYOOAK POWER PLANT - STATION LOG r n WYOOAK / \J PLANT OPERATOR LOG OaV J j)* - J D I/' -fly I A-9. LP's- HOUR H2 Colli Gbs Ton^ Soot Blow* Air Corn Condvntaia P'jmpi BO'lar Faad Pumot Forced Draft Fan inducaoD'a'l Fan Suont Ramat SupM Aitemp Fig* Mm Sorav WATER ENDING A B A B C A " B A a A 8 Tame Tamo A B F'0«r ( Raw Filter T '"Biao Foe' t " -n j . I- - J. ~ , •' (, /7~ ' O / r — 'O! ! ^ '. 1 7 'io , 4 ; — 1 r Sc.-T 5 t>' -'O •- 1 r : - 'J •J -• V ;: • _ -i 'V /JTO 1. - • 6 ,p" V > .•: ¦ -7 a 0 i, A--' T> ' !' ' Vf )$' /^V 'f/,1 •/ft ^ , IN PLANT SILOS 9 —: ?'V >/' ! \ it> h". //cA 7/^ pfv 7 on. /ho /7o 23 7 15 10 " ¦/ r. — - Xi,: ( i if) ?<> / ;< W--. rir ^ '/vv. A P f F 11 'i ' Jc? 1 j ' ^ /?> /^f . ¦ r • f 12 i -- -" ¦J? > s 3 , if' / v Ji / 'Cts ! Do '<>t /o36 / / " Oir J' ?# V- P 20 19 !?t S J r- JgO ?ir /i-y J>73 >7^ /o/Z. socY "O /i-f ff' 16 t-r — In l rV 5"7 ?M ?P c A'r 7 Vrr J7? J7f /CO! /aor nsr /?a IjkllJ OPERATOR 17 •/i XCl — SH 3"? 3f! Mb '-¦r 277 161/ joetf jjst /7o 23000700./^,- . y IB Vi' DiOb si JT3 J3 3U ^/ir <350 tool. 55' s&y 0700 1 so^ •- v 19 Y< ?.0(s — /7/ J// ?>7 /'Sr /is 2] '/f r>' j \ 7Sl TG h '„ r i ;-,o 3 CO !w /2>?7 /» vT3 24 - Yr= - 7an ,— ^.T 'At ------- Reproduced from best available copy. .1 NO J19R 9 BO WYODAK POWER PLANT - STATION LOG ? io, o WYODAK GENERATION HOUR IND INO IND Sio Oil Oil H2 EiiC EHC G'um Throttla Arno lani Eahiuil E.hauit Rimovil Colli Ena renin AiR'ht AIEH CAS n . our HOUR \| nOUR «r m ii :< (<. C-&3 17 NET ENDING GEN AUK 5TABT4JP VARS VOLTS Prait T amp Prai Prill AMPS P ^1.0 l\- 'i^'. '' "O O /o <=/ — '' t; ¦ l':l i/'7.7 1 Maiar MW Malar MW Malar MW MWH 2 :'C: U "l •"""> W-\| ,, t . /" -1 a / T fe-V -1 /• •¦ i'/.i & / «> ^ <¦•/ - n ¦ .1 ,- ' ^ -¦¦/,. .'7/ " ( 2 ss-1! L 'iQc /.ffJ » .7(3 -; Jf,C 'ytpj 7 .•) °( f 4 . ' ; ¦-> ' :o ' r 3 0 h-" ^ f ' < 1:1. 0 r?i ¦ '»i. ' l.'i " ' -r .'<* / .— ¦;¦ ; r, . - Il--, : ,v//? 4 3 .•> 11 7 A.7 7 ''o' s . i - . " "?-> -h -. '¦ ¦ •; ••f J. _ J .X- r> - ;,• , ¦.. / -r S 4 J, I. -> :> -r-j-fS- .'J / 1 i°l 6 1J0 _ lH ¦ ¦' 'j "f.i 1 h '¦/ / 7?- r2^'- ' 7 ij / ¦ '1 6 s <£• v i". 3 /"/ 1 O ,7P 7 S3 — ' iklf //L'' if ¦¦ y,1 "¦' try. / J / - " /•s* f ^ /¦'- /V 7 6 r'o 11 -3 -,"=1 / 7 ¦- - 1 - vo B 'SO ¦y 'Mr vr 0 ¦¦ .•' ^ ' "Sf n i ?> > 7/V f, A 1 /^/ / 8 Sjd roiai / 7 i lfh< 9 :'i. o V - i/T r7:; /. " .< -, /,--. •? 51: V-T if'!, ? /i). c- &v, — J f ' ' I "II.' f r a 7 A+ff A'' •n' r,» V t >>r 10 ~ r,'/ > J/i. n-j ¦?1/ 7^ 11 t X' lY ^ i //V ',U:; t"''' 'f . . * r" //!> -?s 'J ~f ft F, v>/; n 9 ry/.4. i ^ /» ' •'if 12 >t.° . J) //y /- ^ ! '/ ir"> -r / .}/¦' J,//A'.. 12 10 - ys V:,C ; fjf? TT) 0 1] .fiO "V, — v J> • ¦. h-r ^ ''' o r < 7. V - - -'1 ./ >y/ 13 1 1 J ^ < ',17- < 5V' -7»y L_^ 14 V . 3-2 !'• m i? 'h-< tfin ? yV 1?o* ¦?-/'}. i'y//cv 14 1 7 si 3 vy 360 . \r\ 15 J-HZ • 2^, ^ 7_ //y.i ft. 7. JTirD 2-,' /?£? /r?(. * $,( /rl — 1! 7 r.'/htj s.nrti i-" 15 13 i^r,'9 ¦ ^ Ml rjX 16 — % y 2- "(* /Via 9 r.o s$~r xjln,7 S.t-l'Xx 16 14 • 1 •' , I, v 2 . 1 7 Jb-L ~\P — ?/ 2?- fc !/<.0 ISiO ?< /IfY /fit > > ,r !» 20'/ s,tfh,o f.7hr.' 20 'T fe I0Y(c 3L>/ ,J £ 6t> iii 21 7-r? ^ J5 — ff.sr !/S. 0 UL JSfl nc>! %x> 3. /S>,0 l/+ 3 20/ 3-/7 .i.ft/Y-l 21 IB ?<»L / 35-29 1 f31 22 .'f-J T^O ?¦/ 2"^ ti.i t'S.o •<].Z /;reo 2"T /?r/ X //. z. /A 7 rt£ c.it/f,' dot* , 22 19 tol ? l,S yr? u r f? i h J 2,1 23 TV? Yc2 3 Hi fr (/X -ill i^7t A-T V>e..\ •¦<;?£ ( //. 7 /7/ — c s//o x.fini 23 70 U3.ll Q / ? .r < « JO J2 5 w 0 IO.) ¦ iH r- ^ r.'JtV 24 2» (.mi JxP 13 1,17 21 3-2.2. TOTAL / f ' pTOTAL 22 ^-ry 1 2,-j ¦32 sr Sub Tola! 7S5-fc im-c. rrH« 31 i xcjz HOUR H2 Cold Gas Tomp iooi Blow Air Com( Condanuta P.impi Boiiar F»«d Pumpi Porcad Drall Fan 1 nducad O'a't Fan Such, R.n..i Supni Aitame FltMi RHl Sprav WATER 23 £> 7 / 11L ?« ¦ .r% /Ml as 7.1 ~l ENDING A e A B c A B A B A e T,mo A B r to \| Raw FiH«r T-atao Fua> 0«» Toial VfeOC 7 i & 7QJ £S 1 1 I c-O^ _ .? -T6' .1' ^ f, L/i io - j* :>to /oo * IOC t V Oto tKi°. /^O u^>- fco 23 -> 1 :: 7 Pr« T olal 3 i HjT ?c.e c t ' '1 v k O r .r . i ' J l=t 15 r ¦ i'/ • Z£. i' 5 ¦ ¦ i '' t L y '. fD ' •' 1 ¦¦ X 0 y^°\ 6 •'."7 _ .7 '¦ (»<~ <<¦> ' '' O - Nil M«m Xmir War Out Can Varl In Auk Xfflii Mwar Stan Up Mvar ACC1A2 MW ACC102 MW Coal Handling 7 1 '< >'-J >i . 'Va 1 Yi/ - B I i 1)0* t ¦' t ' T$~* /> - / /; - iv ' Mf '"¦J / / Ar IN PLANT SILOS Prai '•u; .• - lU 1 Q '. n J :-v.r i V '¦' / SOin 1?013 /i 7° ? 9 1 ' — ) v ¦ 7 V \ ' A,.'/ f ¦¦' > >0 1 7/ Yr>, / ^ <- ? O 23 7 15 P'iv Total ' A ft -s> OS.!!") tfiiif.r ; f ' / --"Olfo? 10 I ' ' >:¦ :. i - .-v ( (?/ / / J :' A r A /Si V f '/ 11 u? ^ vt./ ; J '/¦>¥ ¦yS.-' ^aiT^ 'oo US' B A - lit Mo - - 13 - rv-, •— " vl V'- ^ ft y>o r&-7 .My ¦' -V y°or /£/! s To /L r C 13 / '¦>' 4»'V > r<> /// ¦i;.> ->(¦•' vyr >ijn /A? v,r .0 O Coal Intagralon SCALES 14 . — rv ('• ¦7; IfV nr- >1, ' , f/r ">^7 ta) //r" f&0 £ / A ' e c o E HI H2 16 " / me 17D\ ir/ W /l>OL y r fas' -i-y P'«« ',705 il worm fV??T7 9 ,^7iC 16 ?< jr.r 1XU ¦<,dt ><¦> 77 2 7 7 /atf ¦ /0P(9 <¦ i/2. l^NjT OPERATOR Prav •nvn U/^VI o 7 J 2 'fc» aij i fv ;j?c> 2. 17 l/f 2£>t TV j-j jjjt' jr r /t, 1 "U.C '27? 7 7^ 4 9n J00» JOS' /SJ- 2300 0700 fj/L-,- t.y/.fM , Total n i^l- iff S(tTT < - 16 / ; .ry jTJ ZB& / Gi \U6-0 279 J0o 7 'OOV / J-T nn 0700 isop A' A y-. J 1 it Mo ico2:; Mt?* ' - IB y** D c > JTJ ivy jfL «A !LX ¦ JW ?7fl /ifdJl 'i+o r/ 1500 2300 TA-. _ 20 i? —T 2^ 3 7&S 3gr /^r 17? 77/? J007 /2S s6>r 63 o - "r 5J A',T 5^-0 27 9 /'Of ?jr /6>r 22 v-r Q0") 3V r(-, /iTL 'LO ^ 7^ 27C. / r- '• O "1 ^ - r.M 1 (f) /?J 3^5 ¦j. yo ^"^5r /00 V {//-) 16 y 7.r 24 t- /-— n F" «?-! je; "J'i's 3.77 to(3 I^Otf /Co AT \ Total SHIFT FURNACE SLAG CONDITION SOOT BLOWING LOO m i a ir'» Out 0' S«viC Group 1 Group 2 Group 3 - G'oup 4 Group 6 Oroup 6 G'oup 7 ' Group 0 2300 - 070O -y v \ V ¦< Xv.yi. v v ^ K vV'Xvr (-', y 0700 - 1500 •/y/A if-* /// yx^x-. tCXx 1500 2300 tXtX XXX •> aaX . rxx X^XX KA' X - / - - - f* ¦- ------- r Reproduced from best available copy- h JAM NO 3I'JB 9 60 >0: WYODAK GENERATION C'Ott Gtnn ii '-ifeo ¦3 -s? "It I 7 H la ps m 7V71 ' 777 ^~Wr fer ES I. i ^ IJe. loVTl Wr ~7t 7 7f? a 7Z/j i Xxl V r-s-y ?^o ?•¦- J IS i/7 X7fc T7 22^ ja _-E£J JC,/ _2ii. ifeo _lt43L 2-2-2 ? ,s- Auxiliary Tr«nilorm«r t -11 s ^4^ _z2z vm , ,,Q ... tm 'M- <-1/7 js-jt / i/j 7. mg u 2 TVEJH /VJ 2 V1 fV w I'll / / _2^24 mac 7^7<& SiiitJ 3 J o -3a r^7 s Z3 rV a 2. <) -IB -il. ii h tr3'l Start up Tranmloi lb imx 5A22J -Oi ?^V7 JO. :'3 «- ZSt T?" 7T7 -ZZi, SZ liZ Hj7 -LLZ- JI o :d£h 3?T ZZzx /<¦' ->3? Coat integrator* ^3fy v-f ''7o^ ¦r* \T-tiJ 0a±£ IC,SS L0 m 'If .7? 7 ii2i C ^ iOSc C5 f WYODAK ° ' PLANT OPERATOR LOG MS-3. WYODAK POWER PLANT - STATION LOG HOUR 1N O ¦ NO ¦ NO Bio Oil LwO« Oil fcMC E H C Ofurn Th-oUi- AaPlbi«n1 E ihiutl E.nauit Air Ramovii Cohl tno Tiinp ¦ilR Ht ATER CAS iN - ou r HOUR ENOlNG GEN AUX START UP VARS VOLTS Pun T amp Pr«\|t Prau AMPS 1>'«U Pr«» Ai> Tamp Pfaii Tamp T«mo A 0 A a ENOlNG 1 . "I — L ¦ — ^ V r -!' ¦ ; ' o • — V " ' /• ¦ .. /:.. '• 1 1 r* .' u: /. -? — /"¦ ¦o !/¦>:< 2 3 •: ¦- r.") .V ' J> . .' ¦X,' '; Hw >;¦ /•• c' — /'.'V C i- - <¦ .7 '/¦- / 3 4 1 ' — if '7 1. i i / .\ lt< •1 l.f ) " 1 : ¦ /,. / 4 a J.i ; -• 1 - •r* ' • j y V I i . - ' .'CJ- — fT' r" /••' ?/,¦* 5 6 ' : J - i"1 i •¦' u .. r-.i - '? > ! '' \? -- 7, - 6 7 ¦¦ ¦ / -¦<>> Jo S- '-- // i • .'S? Of - y . D. r • //A/' fi/ 7 e '!, '¦ ~ >t}'V > r- ?t <> S - 7 //j. ,>'/- ; V/y?7 ' - 9 >r 7 "¦f — jV \>'i y-r ,/£ o he '¦n f / /. //'? ' 9 10 '"us ~ . T'-' ¦' - v4' r 1>- '• c~- 'X fj /£j> " '3> // 10 ii ';/ YV "7 J l;t' ;- //¦:',' f/A /&r- J'r' .j) Ar,)6 /1 -V ^ A); r?/ ' 1>V. 12 " '~o 'V% UL I //r 171 r -"• s r 's: ¦ ¦ >r?o fA '/a 7 >.- ¦ 7 13 y t ~~ ,'j6 , J d~ ,V_^ -"YS ?'V(! 13 14 £¦ <¦/'7(, m'- r>'' w> >>¥, / J 4? * €" ^ ¦ <>' t'f.O w.L /sy? '~ tin t/ J7~Z- Z2D/ 2/-/ r,v,i.i 16 17 ¦<(¦'/ -? / r? -2.t_ W. i ik.o Vi/ erro IV !7 /<£> r,/ 1 <-/! ¦203 ¦2J& f.lLl7j 'ir^bn. 17 IB ? ft! us.o •ft. g !<:/* ¦7<~ tit/ 1ST1.L. / ^ /— v-f Z-Z. US "S.p yy/ IS?1 2S /9vf jti r /A Z. H.T 1?C* J«7 i'.Uti.i 32 23 Ji-o c> - HO V- '<-•!. - -!l 1 sf - 1 ff.v » to 'JT \i r-IV- s.^J J '! 23 34 ¦it.- c ¦ .V.O ' .ir LI ^ r 12 1 / , t c" I vox 'l, ; J •r© W» Tank Wtr T ink Wli Tank Oil -> . !^.r - xj' ' -AT '¦¦ 1 •V r- ,! i'J t ' . 1" /.¦ 23 ' - 3 I.-', - ?r T "? / O ¦:: /-> ¦ • ¦ "> /t.T 7 / • ' 4 u L •7 fl '•j ?'t-V . ,7' ¦¦;. ;'0 ' I > ' ' ; •, /or -'-¦o /•O 15 4 , — iy& - r i • i- •i.' ¦ . •' !' t? r >.o 0 Lj^- • /iJPK. > - O'-i 7 ( V,-;, > l ¦/ S V <-> V //,'' ¦ C'/ ¦-It), ->'V '/ :a>, . V '/r 8 L'( ' • i ( ^ / m- /(7 'v> 'fro- in plant Silos 9 ' £_• . >> —- . ':/ J V y v >•- /OJ) ^ .•'J 23 7 15 10 (/ K ¦' / " ¦' : .>•.. A;-;' yi'S> r?s /OL< Vr, ' A / £* 11 U ( — w < 'V s'J , i .• (L b u-r t<-f 0 ' 13 •¦¦ 1 ^ I w -f '<7? / IX /tv }f J z-"' f ri fo/t '/r j'7'/" C a" 13 s -, >k'- ¦' 6 J ? ~'S !<->(! /^J ho o A' 14 M \U >. S'S } V l-'sjQ? i i -> //; r E ' -7 f< /yr w 16 if' 102 n 270 tO/2. /016 //i5 /f-r Y0 2300 0700 !y ^ 16 vi 201. —- JTJ isf 7>b tlH tbt mi 2.7* jaoy Jft /JJ' 7# O70O ISOO //j / . " y 19 VCr _ 26 J £~1 n< S7 /LI tM x7/ 27/ /4/0 J6JI /ir /t-r 1S00 2300 TVin, - 20 VI, — 7oi jry i'J 3iT 1?7 t(.1 /t( 2.-7? -27C. SOOO ,6ft> /6.J- ?S 21 ii 3.0Z c-> ~- <-t S'.T n('A- •7«t / > : > "mL. f : o r,' /in /,'. a ,-„n 24 /• ~ - 2)1 _ S^f j7,J- /^.? s'2> -j- <2.''." yy? y>> ; (a C3 so Total SHIFT FURNACE SLAG CONDITION . . SOOT BLOWING LOO iK'lft tR'l Out o> Sarwica Group 1 Group 2 Group 3 G'OUP 4 Group S ~ roup 6 O'oup7 Group 8 2300 - O70O V'S VV :¦' C > •¦, V '. - v 1 V ¦ ' / V " 0700 - ISOO xyy^v 1400 2300 K Mx/ xxx>- xxxy fix. X JA-31, —i r ------- Reproduced from best available copy. I JHM NO DI'JB 9 80 0 1 iS WYODAK GENERATION HOUfi " r<- / h t / LM 1 \| NET t SOiNC C'Olf Ctnl'tlion Auxiliary Trantlormar Start up Traniforinar CEN Man- MW Maiar MW Malar MW MWH 1 " )>i 'I/- l" ¦' 7 \ 2 v- r 1 <-1 1 u r '"1 3 , 7 1 ^ .'-r ? r ^ . ..¦> 1 4 : 7/ rs-'i NjrV -1 - --n 5 /1 -1 7 s - -f'' !-¦ "1 6 1" - "6 -w > ft-:/ * "7 O Sub fatal i ¦( t '.-1 '' .' " 7 ' 1 ^ 7 ?v tJL '»o a T/ln? - Toi»i 23 7 2&V7 23 'f,9VC A 3S~ 7 ¦ > t.l <'1 J7(T 24 ¦ 0 'X7 'Si XX To 3av Tol»i K',12. 7 1 11 ?/' Prv T OKI T 1 to rial Main Km\|r Van Out Gan Van in "Ao« Xmc Muar Stan Uo Mvir ACC 1A2 MW fcCC 1H2 MW Coal Handling f'tl 3-v * r ^'GL^X /w? .nun r'?/7' /??2l P'av :o -r - >.T ' . - r"'^ ??'r1 I -¦ / ~ Total / 1 7 /'/ O rr\ / y 1II Mo — — Coal Inograiorf • SCALES A a c O E HI HI Prat Soc,m ff ^ - '"J ) 7 Prav - / '.:W i o r?iv Total r - 1 -^7 J ?7£H - ', j i _ i j 11I Mo i m.-w SOO.1 1 M 1 '1. - WYODAK POWER PLANT - STATION LOG ?-7 0ay_/5_ WYODAK PLANT OPERATOH LOG -J- T HOUR IND IN O INO B-a Oil LuD* Oil "3 EhC EHC Orum Throiri. Ainbianl E.h.u.i E.h.uii Air n«mo»i Ci>!«l € no f mtno AIR HtATER GftS ¦ N . OUT HOUR ENDING GEN AU START UP VARS VOLTS Plan Tamp Prtu Praii AMPS fraif pf»»» Air Tamp Prait Tamp Tamo A 8 A B ENO'NG 1 ' "i -- t 1 •- ¦ -** / " • ¦ r T':' H '* '-r in .v3 r 7 1 2 j . ¦' - ' •O.i I /' . 6 - , >" 1-7M .?/ /f • 2 3 ;.v ' o 'ij ' '--J. ,V"C' / /< /7^ — 1/ -T ' -/^7 3 4 I '-l ; ' 'ro " / /•i 'y ; "//v 4 5 Q •• ^ ^ i -t; ¦ •> -f - ¦ //¦-.- -'. 7/i >. 7 3 6 - "O .•• u. - - r. ¦ ' < i Y«» • •- ' ' ; -9 1 > ¦ •'¦'r. . h-,. . 6 7 T / /. i/./r • i -/ 2 r / '/ .;, y / "u — i ¦ "/ - Hi /-v.- J B 4r Vt ?/ 2^ /,r / 'V/ <- /5"7.e z r /r/rt- 'i' / z- -i sc. 7^ / f 9 7T ? r> /o — /?! Zo'C. r '=//1 r r y//7 r 9 10 ' ;-Y, c. .7 , 6 - U ?- a/ y u<: / ¦0 tw, //7Z D 9 3 / wO — m zm //7. (. 10 11 Tfo // rj Z2. W/ ///:« /V o Tvr 3 JF.J /TL / ?7 2.^7 'Jill?.! J'5 //7.7 11 12 J! r© W.r nr. o /^7 o (]/ — /?? '• b~J<. ///7>. f 12 13 J> Yf yz- "T' ^ v;- '">i '1 "• 7 ir. J- /% ¦ — lot J i O f. s . 13 14 Al- J( — O >/ 7^ ^ Z- y/. V 1/^,1 V-^./ 79jTz igi 9 12 3 '.61/9.0 S, vhi.t l« 1 7 Jtv j t vz w.>' IN. S' V/. f h'fiO if 19 W /Kiff 7 %>& Ci 21/1.7 17 IB fa — a.'L- Z/^/i w,y < rnr lire l7t- / 9-k /ii7 oy Dr i,///!.(, £-.Mi t.f Ifi 19 ?r~v. TO s"/ Z. 2_ ¥.f AJT./ y/. a. MO )M 7 2_ Ji'f S 71/1 v. "///f.7 19 20 20 yo /2. ?. ? 7/f.O r/ /SiO K VL 21 J«-!f JO •— ;/ 2 7. te-,2 fSRO a_r i^-o 16 M f. 7,J /O %Z 0 s.lii.i 21 22 J'i.O JO 3/ n-i t'S.O vf.j- JS?Y ijt fifZ. 7 ?/ > .70 — ¦;• r i'-r I '->i3 .Ik t° • — - - V cliff 3 .--tf/j'-'.a. , 33 24 • r> m ¦ T'> Hl.v / * 'fj.6 /Vi j /0;3 * •5/J- • rln .¦7.4/ 34 TOTAL 1 / TOTAL. HOUR H2 Com Ga* Tenv> Sooi Blow Air Con Condanuta Pimpi Boilar Faad Pumot Fo'eaa D'»ll Fan InducM Oral! Fan Suerti R«n«ai Supnt Antmp F 'OH AM Sp»»y WATER ending A a A B c A B A a A B Tamp Tamp A . B FlOw Ran Filiar T-^aiaa Fuai i ll«- - — J - Tf / \ " V' " tO-'^ / " i 1 W(r Tin* Wtr Tank Wli Tank Oil "¦ • ""J - I - J "-f ^ /c- -? fc'- ^ ^ to X '-'O / —j, 23 .:•/ v-* - ' ; j. 3 7 7 > . S 7 Jt -l - ' / i t -'tf' r9'i^" ^ r3 ^-C7 KQ 7 "/ o C ^ r r - - , 7 L; - ' r -.'9 f I ' - r-' ^ f • / IS /^S' - >^jT s -¦ , o ' ^ /c- / - / ... '¦ . "CP . * 6 ; ru. //- I '-y :,or? V-. / '. j ,. ^ 7 c,' " >' (O sy ^ "j ¦ - ^ ;• vvy 1 / . -Y • / --a f I '/>' ¦ / Z.'* — rY .r j VJlo / ^ ^ 7 ,:- jrt>i /®/v / / » o IN PLANT SILOS Vf __ 2f). W tj ft- sir ' r ' .X y_ ^_7 2- «?«5V (aO 23 7 19 10 '// 7 ¦=-/ _ ry 7 r o /r — T J yj v StJ- J 27i- /w'a/ /-So uf> C r /=¦ " 13 J* j-v o rr<- /c.7 77r V i/l^I v<- U /r 0 ' / />i ? -'> 70 r-^S-/ ??f /olf too J /CO u/4itOperator , 17 >i; jy ^7 3ty /&T ¦w 773 /et>7 /6o7 /?o //d rfr 2300 0700 . J/- ; Js,->UA\ IB — 3?IC> /(r/ 27 O Ma /oo^ / 3(0 /70 0700 150p o • 19 rtt S 2 JtV J ft //* - (.! in ¦27/ I6<>ct / cwr /S >/ 1500 3300 7 20 ¦rf — 90l S ? ni -?f7 .7 27J 27/ /aatf lo»7 /£>f 21 Y? 202 Jf7 J£2~ X7b> 17f W3 tt>07 /r> 7/ .-.'•T'1 ; 22 —ITS' :2rj) — i-/ -T? ?s¥ Jft. /t-tf /&/ %7i 2 7/ lOlf /oo't /yr J"? 23 .ja-if .'< ? ?t 2 7.V krf f^Cm fjO /-':0 24 £ / " ."5 1 .5-r -¦ < j .? i r V - 2. y -i7 ?CC)S ftJ o2 ( Od r /o .oo Total shift' FURNACE SLAG CONOlTlON SOOT BLOWING LOG . IK « A lA'1 Out ol Sarwica' Group 1 Group 2 Group 3 Group 4 Group S Group 6 Oroup 7 Group 8 2300 • 0700 / . ¦. . V -A ¦ • y ; ' "V V 0700 - 1500 < /"* X ^ X >• X .< J(A ^ ' * - A- A A ¦' X jr 'V ¦. > { i i 1S00 2300 - XXXXX ztxrv x xJ(x X //a A X/X xxxv xx~ k - \' — 1 ------- Reproduced from best available copy rOBMNO 3IM q £ WY##AK GENEATi#N NQU« 1 O "? &> .T tSt NET tNDlNC G'OM Gmmilob Sljnt up T'lmlerrmti GIN Ma!»< MW M»«.f WW MWH 1 jfrT^ J .? 2 ? -r~ 7 V/'V :¦ I rr-r r-> i ? 1 3 'i 3 3C, a \ . x-^ « •., / ;v ^ f . . .2 7 7 '1 5 •r j fr - ** (.•' ¦ ¦ ^ 6 Ui.ii • : ¦>: 1 " ;. 1 TJO Sub Tot»r r?'H !7 7 ; ? if Af 8 93AAJ. < a l>i r .};£<» % 54 a-? 9 ?«?<.•? ¦': l£' 15 JX7 ID 3 )o j r> 3 <1 f,.; (,T«r .^ir Jo IS ts o 19 _zu. / 1 i !«» j 74 13 #r J?o t:S S r> / Jo j tx- t« < 73* .?«* 3* .^2-5 Sue fo»M 2)1 VI 4o6 i3sr 2Lt>L .?/ jjt i ?o TiXT'e ,/sV TlTTc so aa.? 7\ t$isv ->&/ /C7y/ 31 ^ ?o 23 0.G1 f PJ^yT 1 fll 1 3ir 9ut> Tot.! 7 iSI- a^7? (fl 7.11 33 tK'J?3 ¦: -y frXO! 10 24 V r 3 ? :-r !? /A tJ 1 00 7?VQ Dr ©<¦! rr?o 7/ « 7 Ol &o P.* Tool Ti to Dm* Mam Xmlr Vv> CK/t r;.'. SiwfUe ACC 11 HIN «CC »B? Con +r rt ¦^JT orjs.iT 7'.'-J??- C)?/9 < ri3i -f ?•!'•' P raw ^n'oT ar7* 2 i; 7'.Vi 1 ' r 1 -? '7/7/ /«• 7I'l Total 7< A / <> i cm — " 1 Zo f c H in Ma — — Coll • <«»»••<•••• scAies A. 8 C ~1 ~ € mi P»«, i"Jv" "-'J? yt' ^ (.'* ' !ia>ut ??6?r7 P'»* (S:1-J- r^- /•oO)/ Mill 1 to:- J-"'. TohI 3.738c -779 l''3U 3%n i .57,^ tu Mo /o'fr 6 M J^££ /Ajs^ r e~- WYttAK MWER PLANT - STATION L#G ¦X5 WYOAK _fCANr«l»eWAT«lM LAG - -V /. //— ,1 noun 1ND ¦NO jMO a.oo-t LuMa O 1 h7 IhC fMC D'y« TkigiVf E'Htutt ElNMtl s,L«. C>»»"! E><> Tmna -'n r.«>s 'N . out MDU« \| EHOINC G6N AUX START-UP VANS VOLTS piM Tkmi Pun fifH AMPS PfHI Air Tamp Pr\|il "I imp f CT\p A s A s 6<0'"0 \| I "-"7 :;.j — - "V - X t ' "'i • ' 2 1 s>: ' Jr» '^P3T <: ^ 1 7 : ¦-/ - - 3 '' O "-r C-* — - -'• -? i'jr r~ 3 4 "i<0 c? ¦ f'" ' \|1 ; . , •-« !('¦¦ > >,//'•¦ :: / a 5 • ' 0 - - .» / } " 1 r. ¦.- >. •. ¦ ' ' 1 -/.'. 5 ; S I" • j -' '.3 "' : .'/} KJ * ' -f ¦1 ¦ s t :1 n »x ti 4 it/.o J9/7 .V? «^.1 * 9 IS* 0 .CO X lr 41.t 40. V it 7 PS f%lL 1 '4-7 /«-f Ji I S.f. h-J f 8 9 3 0 <4 / '-r 214 ^iT LUHj> r 1 //>- f 10 ?c> Hi 7 \ ' r tf /S ft SS /9SJ i tuf- >•0 rt-r /L-4 ; 7r * > to J h'* 5 1 //•- ., n 12 J 0 <-/1 X «?- /'!/ •'/'}. "j »f"? { 2 ««/.$¦ /rc >17-'* if. fy >$ >:uU .- ft ? i if T F mi J ! •' i s-1 I'l/W .%.-> It! 4 "« »5 -J'3 ?'/ 2 2. //£ I WL tr-7 zi /ff/ /PjS 3S M fJV — •>7 UO s.tht.7 C/J/7.4. 15 (6 :(¦¦"' in _ 1 2-"Z~ Vy.S" ItS.Q /r 77 2T fr-T /sv _ >:-r 2"<3tiX/ 32 f s7 7 t 1°! ?~2. vy.s /#Z l?7 2<- /fSP W%¥ .i /s r S/£» 22 z. ',ohi y S.fhl,* p 23 ^ r ~ 2__ 'f, f- ffs - ' • ' > J,7 9. % <. >/ n .,«!• 23 a«- ikr. .7/ — 4. Ittf 11-J 3 ??" rV-n itSa J v,3 fs~'< p' t r'<9s!r hi ¦¦ •:. -> /'¥ 24 TOTAL I . / TOTAL .¦ » - NOU" HI CoitJ Oil Tamo So«i' i» Cam AK.DI C«nH«nf«i* Pumpi Boil' F«0 A e p»0<«i 1 Km 'Film T-,.,c • - —- j' 'f /? " 0» !/-"¦ ¦'/* ?—¦ Tv - ?<~>C ' ? - •> MTir T«n». WF> Tan« »" T»"» O" 3 ' - - Jr' ' ->o - . 1- 3"- 1 ,v r. ¦- ¦¦ -. r ¦ -) l~y~ /oci1.. /• >'-7 '5 V CS 33 ?; f "3 ' "3 " V^r" ^ . r- p^- ^ - j f 3 /'¦ :'• '." f=or /'//-J /.r& ? ">/ ^ ? ?- :r « l! 1- ".' . .• !-¦ J pi 15 ^ r >7 5 / " - / • , ^ " ? A--i 6 i • ' > ;- : "1 i"» :. -¦ }/& t /• T - T ifX 3 eo .«r¥ .< 5 til to+iJ lt>(4 II1% n» ST i VI" ? >ft X 3 j«4» .?~; i- / 7» >i* 3 90 nt> iN^I.AMTSli.05 9 ¦ 4* JaQ s' M ,-5 ^ Sit 3^6 iU !->«/ ni t J ts >0 J * 7** a"«4 V 2 -? 'j ^ 1 ? _ z.f 0 /es«4 n » fL-o- A r r ! M " tti tr> v^- 'J. ' 3 ' 17^ J >1 I7j /fr« r ic&i. i so : '¦ ~Z7 C F ' r» 3 «-// — ?Ai 3f^ J Ar Y-.K/"-¦ / /fliJ y^its ~ r P 14 us ri > r/,. t -n. 'tv&S / 7 ?c '.. '. -f'r #// is « /&r J!7? JULL -J.70 /¦-^ wz. ir '6 7-CfO r y ¦ 4-j' rr/ 3fG far i#/7. ,voy 'fS~ J UNIT OHflA'OB ,7 JO/ rr iti 3%( / &£- S/ 27-r 271 >><{ J&O /tr /^_J 230«OTOO />-: ' - • r ¦-.- ts vr 2 Of W- XJ tw /& 2- /&Q %7t> <26? f$tt ,6CU /ss /IS 7/ a too iBoflT^y 19 /9k •«— •ry ¦r-? 1l£ 3S7 -/2P- /Ai /? 3 ?r 27/ "/to sJ3" Sfrf #--1 ISOO ?3C0 " ^-. 20 Joa ' T/ JTJ ?yy /£< 27f 27/ j0OJ /CHf? /ry /&y 2.C-4 w- 3'/ n 2>y .97 f TW frj' syr 13 v.r 20} cv r rxA 7JV /£& -)-?} 2 TO />/& J0t>3 UAJC y^T ?j — ::^>o -Vv'-" ,V J .XT' r" ~ s ¦ - "? h > •!' /-TJT f£r ^ /. ?4 h'tf ¦ v r».l 1 f V» r>;? -v^/ ^a-2 it& 1/ 9 toi>f SHIP* PUfiNACE SI.AG CONDITION SOOT SLOWING LOG »<•«» 0UI St s~.ca G'ouo 1 I Or6u« 3 0'«mi> 3 G'OVS 4 O'OuP 5 Q'oup A Q'CrvO 1 G'ouo9 ajoo - ofoo vxSK r-'/Yf vr r\! y •< V s .. e-v- v- X~V 1 V OJOO - I5Q0 «S0Q 33 ------- FORM NO U'9H 9 HO 0 1 I o -p» WYMAK GENERATION HOUR n.i /^f ¦? / a >:,.i".1 '7 NET ENDING GroM Generation Auxiliary T>snifo'm«r Sti't uo Tr»nt)ormar GEN MW Maiar MW M«»«f MW MWH ' SM6--J /:¦ tji / ; : ' c> 2 7 o.'jss J '!r C? /jt 8": / ¦rt "TO 3 tQ"C>7 ^ -i"') /jy a / ?,o V 4 ¦>> 7 t-s ¦: £ IO '/ _r£> 5 < r 1 (5 Cs :: t / t 1 .70 6 9/'i^ v. /A.(3 / 0 'f Sub Total L ' — -j" ' ' .£" lb"-; /T) /L7 7ts 7 ¦?' S-s o II. O Vt~ Jo ^.^2. a J11 fr 3. 7- 39 338 1 1 IIX'O r. > ?o 13 en (. o i. 3S<» //„ 1 Sf 70 3i(. 13 ffil.i 3,\ o 1 L 130 ?2^ 3 / ft 14 iv; / ^ rv'c ; /.J C.T J'3 Sub Total r 77fO '6 7( £/' ' '» * >t, i/ / ¦< J 17 ^. -:?7 i u< <-* '¦: 1 IB fn^, ^' "I "y /. ¦7-^ 19 li.vn - y .?/) 30 ^ y 1 if 71 -'iP,!'-/ s s -S / f- !J J- 33 1'} ) yyff Arc?. f„n- l J &1 <'?;-zs ZZL} 10& S23IX. ¦f-.r; / 71 OUstU }?•'- <¦ 1V-TI /Oho -4- Ce«l Inlft^ratort SCALES A e c D E HI H? Praf Jtofcr-I 0 6- T '.i 3 /3C3V P'T 7 t from Tbt»l - 71M ^9/> Ifl Wo 1 ;^SY 11 I13CI.7 1 ^ a — iL!20,°l WYMAK PLANT OPERATOR LOG sc. eo iLsJL WViAK P9WER PLANT - STATION L«G HOUR IND IND IND B'oO" Lub« 0.1 h2 ErtC EMC Drum Throl 11» Ambilnt E ihiuvl Eahauit 4.' C0H1 E«o T«fi»o Ain KIA1ER GAS 'N . OUT HOUf ENOING GEN AUK JTAflT Kf VARS VOLTS Prat* Tim# Pratl P'tll AMPS P'«M Pun Air Tamp Pr«\|\| Tamo Ttfio A " Q A B FMO'M'j 1 ¦>7Q TO ' \|r^ 1 1 _ . / ' W ' / r // , /6 lrv - "7- - - r ¦ i--/ /> l: I'f 1 3 jO ^ V P ^ \ ¦ ; V ' / - ~J ' '-v /i- / — o-n- ? "vl S///3.? ¦:a"//t.7 7 3 / AY V- L\ 1 ^ , •. '•" 'V ¦ r ' ': 1 -.'J ' «• Koa 2 m - ^"1 3 4 —- ;? •"; rt. -¦ •f •: •t '• * ¦" ¦ ~ X ' 7 /cJ /*'' 2 ro //">¦ . . J!" x. .4 5 -TJ ? ' t - '••- 'J y - AJ / <1* " \ cy >c, / bu 1 l' fi 'JL --'7 -¦>- . /• .- 6 Co - 7 .'-J? ri ' -7. r r. ?fi.j 6 /,;'? 6 7 3 (. r> '/7 . ? ¦> Uil.ij H4 f/, \ /-V s± r?': 8 /- J ' t- ^» i. 1 Ifn 9 10 ^fr 3 r ) ? 1- W,(. it'. ' ' 1 " » n?< // 1.1 / >' jn ;-r X A J/" < 5.' //"-• 10 1 1 1L. 72^ '-/a l/J. (* / / 7.: Vr 1- / i'f / i?r f'fi- /.j Hi oaj; ,-Ti i 11 13 &5C, Y ; — 'r'/.r r" ^ ,r V/.s sr- / ,¦. / ^y ri//Ji r.f !/? ' • 7 13 3S( ? 1 7U 71 1 V V? J'po •! v:^ 71 /S < 7 :/3 < .A6- i.j hr >3 14 ?3. — jr n ¦?^v //V.* '//-j 7 /.T7< ¦2.r / / / /' •'- j-/ b. 7 f rt ^ J r//,r . ,Js . 14 19 -v J , 7'- i ' 7. - pr- '; /A"- A frC h.o 1 h\. /; 16 17 ' ? j, j Lt'LJ A'] 'j i , ! 1& T"{ %¦-- j- . s¥r (J ^h'Ia 1 7 18 i r — V / 7- t''> /J.y a; ¦ / <(> .j' ,- JJt m ! 1/y-, IB 19 ? /- %! 20 21 !> X , V1 >'r>- ,7'vf A' rf; >< P-7 '1? -r~ ' >v/ \Jt\i cms 31 22 j>V ' J . V/ >- V/r V\ 7 / /7-V t ,vT1 n'-r cf<-( 7&cj •. 17 -'//. » 33 23 T"2. -<-2 — -..1 J? ? 'H5 /' L'' "1 ' H(" r "Vju /O /rt-i «— fj"f 33 24 " 2 — J 7 ^ V 'I'M l/S" / (rs! -x'7 ! 'r- \~rjrj \ 1 ¦go !> ;o7 ,<(J i"i 74 TOTAL / / TOTAL HOUR H3 Cold Oaa Tone 5oot Blow Aft Come Congmuii PjtnM So — r C ' 5 ? .TVP / / " A 'J \ >¦ >¦¦' n Wl' Tt« Vyi' T«nh Wli Tank O-i 2 'U-J - /^.r 'fj y (¦ <=", - fc'cJ "-•2. 33 :* v 3 ( t» — . ¦ — _"r.' •, .1 /-lO- j.* ,-j " \ /->c.r /; . j to 3 -,-r 15 V - 9 V". x'.f ',' "" ¦ •¦ r_j ¦ - '•' ^' /-' • r-o 1 S — - ' -A ^ ^ r.' -J 0 K" •• t Q r- -; ' ')0^ r —, -.. 1 us y ..7M '/VI • /f-ir? /oo3 f • f f/ y s~r> 8 1b- JO'f b- 73 r 19 10 LI r Jplr .S <1 1W ¦» 9y II.¦ 'a- /"J iLt* lb' 1 H A k-- F 11 - •."2 ?/r '-V" i'&3 / /ii>3 t 7 CS / r 0 <¦/; a r' F / 13 Us /ID r/ S? W ?/f /¦«.;; y;n. J fi., //11 J?r? /* /r. D ' f- . ^ 14 J "7 7/V If/ / 0c> »e u' , M ' h ?, I 7 r > 7 TTj^ 'ff., J > ; toy ¦ 'Mjr I >° ^rr- UNIT pPE RAfOR 17 L J V,3 ' ( V vx it'/ "v/" ^ ¦> }- Ayw / -v'T /c&. /JO r^ 23000700,/ y - , IS l:\ . 'V i Ji'- - V" / -f v/ ¦ '¦V ~v/ /-/> ! O 0700 1900 19 w \| 1' ¦ ¦I V 7 '/t/ / 0 / 't-/ /aaj- 7 J' A"r' <•' ¦¦ IS003300 /¦'¦¦fft ¦¦'¦¦• ¦ S 70 1'' . ") . 0 JO/ v; 'if ¦;w I h; ' >a &J,: /toaO /T30,. / i?-s> / j - 71 c'. ) 0'' ¦ j V P V), ¦r'V ll> 7 ¦ /^o~> cool 33 ' 1 ! / :J 10 j ¦> V V! - v/- ) ?&. 7 t / hr /^.,.- 73 v r" 3<-rt .'CO " J" cJ jyrr .t f~t - p?c> /-- /tfo.7 /•T> /_fi5 ,V^3 -, 7, 'j /t-ic 7 /OO fro su. Total SH1PT FURNACE SLAG CONDITION SOOT SLOWING LOO IK 1 & Ifl 1 Out o< Sar«>«a Group ¦ Oroup 2 OrOuO 3 Group * Group 5 > G'ouot Group 7 Group 8 3300 - 0700 \'Y. v vvv' V "' K. 0700 - 1500 X /< X XV K AX -• X ¦ < < f fx X V ¦* A 15O0 2300 ///0 ------- Reproduced from best available copy. FfHM N9 3111 * B o o en WYtlAK GENERATION H«UR ^ 7 f L!S? NET fNIIMC GrOllG»n«\|ra\|iOf> Au'ilmy T'»r>» MW MWH 1 -v..1".' a /41 o a T 1 JS 3f 7 1 :a -rLl > 7 H K> <. „ ¦ .7 a. > 3 ..hO K'-b't • 4 T \(rl 7 77 J ¦7 1 S ¦//¦> P 0 -i\T 7 n 'Xi -¦a -r "> ; 6 1 • * " ' i ~\S 1 if* ': . • i ? O Sub Toval _ l' j* ItWr i °i a /la ' (ho? X'' ASl. I LI ?¦ 3JL! 9 f-> 1 O 3-5"/ 5.1 3 1 10 c 13 n ¦3J7 95 ,?> 11 e>nu(o lC.i i ao -.<7 J lV 7 09 > 5 ni; tJ ,V7 • 0 (yi 'M / " j 19 <•''<£, 'j' m i " J-3f 30 ¦ ! ') • 1)0 / J J W'Jy 21 X ¦:/ i-piq - j J-'/ 33 o; .6 , ¦f r'f '"ij Vx Sub Toial )>n ?r, I Cr } / 33 ryi o o jf' 34 OW7 //•/ )7S 1 # /ft fo? ir5 Oav Tola! y?<„- 7 r/i V7 fa Pry T Olal Tl to Oala WYMAK POWER PLANT - STATION LOG Coal Irttagratori SCALES A B c D E HI H3 Pf«l Pf«V 73«en 7o1o-V[ Jl fe6J^LXf >J£»oa. / YfCLZ^jf VclK^\ 76M.J /r.'.xJ.'l Toi»l 72t»l UPSi V1U1 7/ 7U7YI 67* vtxV • it Mo if, WYilAK PLANT tPERATtn L«G » lf)jr A J * i Jul HOUR IND IND ¦ NO flioO'i o>» h3 Ei IC EHC Drum ThrQIIIa E«h,u.i E.h.u.i Ai' namO'l1 Ci3'(1 End T«ino AIR MfHTEn GAS N - OUT HOUR I ENDING GEN AUX START UP VABS VOLTS P'tit l»«>o P'll Pren AWP3 Praif P'l« A>r Ttffio Prtll T«mo I A s A B ENO'NG 1 1 rJ.:1 ; » ' b.<: 1'' - 0 ; - ;t» "\|C> J'-W" jLtlrn- 1 ' 3 i'O ! 'T ' - ' ) - 'VJT 1 '>' ¦ ' r.¦'/ .-.OJ ¦! 3 3 ' .—T? ¦57 p. 'j "2. \'M.h l'o. f r-; "• v ^,T" / <'w f > T /ArJ ; 1 X i..i//'/ 3 4 'l-' " ' ,-n f '// /"^S- — 5-11 tKr. A 5 , ¦ - ; l\o <- l"-\| -' ¦ ¦ ' Lfl\| J f>, : " 1 "y. K /r-:: /'' ; -~ "'j (,!¦¦¦ 4 6 —1 'M j ¦ I\| 'vl 1ST r--> 2 / 0 '»"/« ai"l 6 1 351 > V ,1V 7 2 vv.4 l''S i v.T /i?.i 1 ii .7 / 5 • ?JT / :' .J w i.u /"'• /S : 1 /1 1 1 /, -- 9 10 Ar-t» vv S.D T X •W.5- if J 3 lT-rV J • 3 / v ,• ¦ ; - f.o / ^ -'7 5.¦¦//?< ' ¦¦ In IO 11 t'fc n > V !fsi w/, L 11 13 .'¦7 l "L u«'. «r /'U at. 7 t ' J .T If'.i / 71 /•yc / > ; 3 ¦""> "V /.' ^ r-i. 13 >3 i/U 7 \ //J vt. •>, /;• >: a a ?. ? J VI- "5 J J '? i j /¦¦ i f If. u 13 14 ^Lo Vv 1 "2 /'3 0,eA / •. .• 1 1 '}"¦ C 7.3 / j-n /¦; 7; * 5-i/k;- •7 1 /,"- 14 15 //^ (&L/ /f^TJ /Sr- ''Jv - rJ -¦>? V (f/,7 15 IB /1 : ¦ ^-7 V/1-; UA s b~- fy' '-J ' ^ , /V/ > KJ:- f /.J r / //¦• ' ¦ e 1 7 _> /) ,j J1 (lfr ' ¦ > ^ /- - . Sr' )<>> ^; /•' 17 18 3.LrrA ^ ) (tO ::, V?1 . V? — ¦>y? ' '. /' '.- IB ¦ 9 - ^ .- v; • ./ fjif. k (C' - " / . A . 'r >>/ ... r/ >7 //¦¦/ ->r /Yy? h' 't/< / / • 73 23 / / 33 34 / / 24 TOTAL / / TOTAL HOUR H2 Cold G»» Term Sooi Blow Air Con CondOHIi P.i(npi BO<'«r Fltd Pumoi Fo'ctd Ora<1 Fan 1 ruJucad D't'i Fia Suphi Rah«a( SuOtt AllMnO F 'ON Rhi Sorav WATER ENDING A B A e C A a • A B A B T had T«no A B F'Ow Raw Filrar x.-^r Fi,»l 1 Li:r " i r — .S . 'S:? -' r- r? i ¦ -j So r» "3 /* ' y - Wl' Tanh Wit Tank Wrr Tank Oil 2 '' rv • — r" "> -?r °t • J- • T "¦ - A'-(7 .VC-' ¦' '7 23 - 7 = 1 1 - Co ^ O J K\t.' / "V * 1 ¦ --- .A • • 1 , 'vr- ^0 '-'¦J 7 A * J7. s- / " cT 4 r-r )' ^ J * f ' ;' /.- »:'7 /o- e'~ KO '.f G 19 9 7 -J' ••' •) 1 f. /,. - 'J "r? ^ •* TcO CJ fl Li '¦ . • .; 0-7 - - • -T .1 < '1 ' , v-' v '• VJ T \3©7 S'U i ? .^So r4. ! Ltl 1 If /r>/o ^ /ft? ?f? 8 f* >6 0 Vo A lJl 1 !» &!> " 7r 1 : ' "L- J «; > 3««# nr y- ;1~>L ^<7- r.-r A e / 1 1 tjs 7-" 1 ^ 5 i 7 0 6 ((¦••' -7.-J ¦' i- /K m r 12 ft-S' . ¦) ^ .+( '1- / •• ¦ r. "o V 7/) /1) •'/ ! •i 2o 19 fJ } /f/ —- V'V / /. <"o~) J , - r .-~ il' frj 16 3^; 1 y Yi1 // ^ > /'( ¦ y ' ' - - .,J /P>S Z1// U^IIJ OPERATOR 1 7 r /' '• I": ! / 1?'/ J / /" - .\ /pj, > to; /- 23Mmtm/j/-- 'l* . r.-t IB U - ¦ ^ JV- • y h ¦ n.) '¦ ¦/'? ,s-c /it ' .Ss' 19 ¦¦: j y / /; ,' "> kj - ; i.;~t 'l?c? //^D ¦<~6 19H73M ."'j J fi* ^ 20 l in L? 7>v s'?j Vi-y S / /c> JW 'c-M /fe>6. 22 / 23 • 34 Toial SHIFT FURNACE SLAG C«N»ITI«N S««T BLOWINO LG ¦ K 1 IR i #ui •> Satwica Gr«u» 1 Oftup2 Gr«u« 3 Grau» 4 G'«u» 9 G'»u» • Or,Up 7 Gr.op • 23** - v/X\ I\'X ' \xX' -¦ f / ' •' ¦. " V. \ X/ TP .' • - 1SH * ISM , 23M X •' / V-/ ------- "n^^ed tr°m 'HI avanabtejopv^ NO 319B 9 BO ! O I, I 'O' ch WYODAK GENERATION HOUR "0(55 7? 17J/Z &&2S~sr NET ENDING - G'Oii Generation Auailipv Traniformar SlaM-uo rraniformar GEN Mai#« UW Matar MN Mat«r uuv MWH « £¦ 5 7 7 tl J 6F7 'n III 3 bt foq ft 4 /U ¦ 5 (.* d I/O /J 6 k Sub Toia' 1i <} V /~ S M UL 1 3 8 LH4 71 11 9 A X-IS3 fc 10 5" 11 •> & 12 4.M99 J- 13 /. .cm 3 «« 7 Sue Tot' IS" fl- '5 V 6 i 3 >r \|0 '? y 19 H 70 31 3 I Tom >\r6 ¦?o 23 / a. 34 bSS 4, 1 // 0V Toii' Z0(o (r Pro Toti' Tl to Dai* Nat M»in Kmir Van Out Van in A us Xmtr Wva r Slart Ud Mvi' ACC 1 A3 MW CC 102 MW Coal Handling Prn It J YH GLOIt 7j.fi t' Snots ' O o O 0 )/ 1 n Mo Coal Iniaoraion SCALES A a c o E HI H2 Pill U.S27T t7Li/07- 97 Vr.3 P'«v >JQn-Q sV:u j3C,iCX vioxh 17 Vf- ?oIhJ Toraf 6 1 11\| Mo WYODAK POWER PLANT - STATION LOG WYODAK • PLANT OPERATOR LOG 2- fr- HOUR iND ¦ NO (NO BioO'i Lui>a o>« H2 EHC EHC Drum Throl I'a Amb iant E«Haul E.hauit Air Ramova Co'«i E«0 T«mO AIR htA'ER Li AS n , out HOUR \| ENO'NG GEN AU* STARTUP VfiflS VOLTS Pim Tamp Pfill Pratl AMPS Pratl Pratl Air Tamo prail Tamo T tmo A B a B ending! 1 / / i J 7 / i 7 3 i 3 ¦ 4 / t 4 5 / i 5 6 / 6 7 / / T B i / e 9 / / 9 10 / / 10 11 / / . " 12 / 12 13 / i3 14 / / i j 15 / «5 16 - / / ¦ 6 IT / / " 18 / / IS 19 • • / /. 19 70 y / 20 21 / 2» 32 / / 23 23 / / 23 34 / / 24 TOTAL / / TOTAL HOU* H2 Cold Oas Tone Soot Blow Air Com Condanuu P-tmpi Dollar Favd Pumpi Foread Drall Pan loducaa Dra'i ^an Suont SuoM AM«mo F'om flhi Sp'iy WATER ENO'NG A B . A B C A B A B A B Tamo Tamp A 8 naw PiM«' T-«I«U Fu 9' 1 Wlr fanh Wlr Tanh VW<< ram O.I 2 1 33 jj>.r y-7 J.- /' 3 1 yt : "7 4 15 > r- S e 7 B IN PLANT SILOS 9 33 7 15 10 A 11 ¦}- •• 'i e 12 C . '3 o 4 19 16 UNIT O'ERATO" 17 73000700 TV.,,,,.* (S 0700 1S00 / '/Jf-.r/L. '4 19 i soo 3300 );!+S ' 20 21 27 23 34 Total FURNACE SLAG CONDITION SOOT SLOWING LOO 3300 - 0700 0700 - 1500 1SOO 7300 ------- Reproduced trom best available copy- FORM NO 319fl 9 80 'O I o WYODAK POWER PLANT - STATION LOG WVOOAK GENERATION hour IND 'NO (NO atoOii Luba Oil m2 ErtC EHC Drum Throttla Amt> >ant E «hau»t Eah(ui< Air Ramovai Co'.: End Tfmo Alfl HEATER GAS N - OUT HOUR \| HOUR O^c-y^i mtf 1,9 &/ NET ENDING GEN AUJ START UP V4RS VOLTS Pratl T wo Prill Prcn AMPS f'lll Prill Air T«mP Pratt Tamp Tamp A 9 A ' B ENO'NG 1 ENDING C'oli Generation Aunliiry TfantlO'mar Start up Tramlormar GEN 1 / / ' . Malar MW Matar MW Maiar MW MWH 3 / / 2 1 Ifc / s> 3 / / 3 2 6K7 2 /( 4 / / 4 3 <,ty\ i rt 5 1 / 3 4 kZbZ 6 /r e . / / <5 5 (l 9 1 / 9 7 i S4.J7 o 10 1 / 10 B LiloS // 11 1 / I" 9 11 ¦ 2 / / 12 10 LXIIX n 13 1 f 1 J - 1 1 19 14 I / 14 12 £#70 /}i'h /t 20 / 1 TO . 11 / r 21 / 1 71 1 IS yL n 27 / / 72 19 r>L()i H > i!> r -rt/ 23 / /. 73 70 lXL HT- nuv (a b«i i a- / i 24 / i 34 71 Ok J[ J. in t • 7 v 7 ?rT 9"i TOTAL / / TOTAL 73 Ob'"JZ '73/.J / ENDING A B A 8 C A e A e A B Tamp T^o A B F IOw \| Raw Pil\|»r T -atao F,.i Oav Toial (,71. T/2 II 0 3 ?S7 23 2J.< 17 Prv Total 3 7 }3.$ --1 V5 Ti io Oala 4 15 ' J-* 5/ — 5 A Nat Main Xmir ' Can V\|r\| Oul Wr,"., Aua Mmir Mvar Stan Up Mvir ACC1A2 MW ACC 101 MW Coal Handling 7 e IN PLANT SIL05 Lion otpl* oiw TJ10% n?7; 771&7 l»7tl 9 23 7 IS P'v tmt C1T'f ?3 t>y SP rrS /W77L 10 iTf A f~ Total i 1 1 B P / in Mo 12 C r F 13 rrifr,«\>i O r /" Coal Intagraior SCALES 14 E 4 £ / A a c o e H t H2 is Prt 71?S7< s-9 OK i££lZ£ IfcVOL mm <)7M2 7/Z77 16 UNIT OPERATOR Prtv 7Joer t snsa (eC-- •7/5' 1 Mil V//77 ' IT 23000100 Total :tL<° ili ------- VVYUAK GENERATION HOUR no. 7T/ />f2f ^g-9/lf NET ENOlNG G'OU Gana« t>on Au'ilii'f Trantlormar Sit'i uo T'aniforfna GEM MW Maiar MW Maiar MW MWH 1 0 i") I T / n 7 J 79 2 O.70i!> /(iir / 7* 11 XL / V2. a oyitnn r/f 1 75 0V 17 J yP 4 0'. VI 2/7 I753C, a 2- /il s i n) Jl / n$t,t 7 7 2-7 2 6 St <* i J£6 I7S1V JO J SuD T 01 Jl /V/o HIO no /7 0 /1Y0 7 C v3 ?o .IS* mm 3d a t~. 'r, 'A 11 Af7 11U 5 H 9 3 (.a llir s 7 3¦" S n(. 30 .'¦M > 14 li J 1 3 6, i / 7 S It. :< < Sue fgtii J11- 4 6 « ¦ZJf / t/ U Lf JT7 / 7 A J o f/V 16 li'-G 2, f/rf /V, -a:' v.-j »¦» j-O IB if - ->lr ~>$G -Jol ^ V 19 /7'IKI. ?(t 7 ¦: THi I, ?«rp 70 1 7 J / C ¦"YjV >XD/ L T o r>( iri, ?V>1 7e.t-' 23 IHX\7 JC?0 I I a < 3o 3? ft 2« Ifbtl 3C.T- I 6! 3 t SJ 1 D»t roui ~/iot 71? 70t> f7> 7±oZ- Pr» T OKI 'I lO Dal* y Nal M«m Xmtr Vart Owl G«n Van in Aui Xmlr Sl«" Up Mvar ACC1A2 MW CC 182 MW Coal Handling Put ?inr Oi II 0 OixtC ?3ti/ {'Jtl sin> /s-7 jpy P(«» i'loZl oiojy 612!,'/ TXtoi Tom 7lil tx. 0 •re 2 0 i/h ^2 3 1 It Mo Coal iniagraiori SCALES A e c D £ HI H2 Prat ViOiBt tjfglg i(HL! I2&10Z 7//9-Z. Pin 'r.!i ¦: .? -- ¦'. '-' J/" UC,tj 2 Weir? 11/7 7 Toial 3/»-«. JLfiVt n <£¦ 0 2xs;t > ?yf7 111 Mo Y/n v „ Day WYMAK PLANT OPERATOR LAG ¦"¦III . D SS0\ 1-/i) - if Reproduced from I beot available copy- WYMAK PBWER PLANT - STATION LOG HOliH IND ¦ NO INO Bid Oil LwU« O'l m2 EriC EHC Drum Throlda AmDltAI Eanauii E.haun An Ramovti COWT EA0 T«ino AiR MfcATER GAS iN , OUT 1 HOUR \| ENDING GEN AUK START OP VARS VOLTS Prtll Tamo Prail Prail AMPS Pnil Pnil Air Tamo Pun T« mo T«mp A 8 A a ENDING \| 1 'tt 2 & ~/7 Wf> //-T. ^ U1.1 h? 0 V 7 /».i 1 a 11 7 "i- t/i/.f /r£~ UO-O / - 7'7 n^u> /i. f /-> (:•"* »<¦//, > V. f //>¦ O . e 9 •¦ 1 ft '/ 'I V4- '1 u-i Vi" o 1 -itrf ¦> s" I V ',• /k) / / > 7-jf /IK ' j •yf/a;. V.1- 9 10 ' ?i \ ' La 1 ¦i C 1' S" MM. ( j r !¦¦ J •»',i /f / 5 "5 /•- 'i i/n ¦_ S i / n t 10 11 -V.; j / fS" 1 u j. /:/.l i r Ift /.??¦¦ ¦? ^ ' Si < /ir. cn './/><• V ¦; /)».' •¦ 11 12 .V„" \ -Vu 1 I -1 ^ • 'f /i" J.T A-::- ' / y f. / 0 J ¦¦i-'f j i tni 12 13 .ic,-. 1 I w> J i,u,d i/.r W 1. < /.y«- ;c /'A)" l /JT>I •? r 7. 7 / ' -; n i ! ai- v V.'j t •f-» / 13 14 i 1 ^ r 1' mi 9 : H'j Ht n r , -7i»o ¦ In » 14 IS ^ / j' -V • -T iJ '>7- A -7,1 /L'.V //•r- >f- l-?J 6/ ¦' "V O't '''' r r / '6 16 v. •vf .. 1 /rj ! ; f2 7 17 18 -V A'^. / //-•- — /"/y — Tr' V.T'v r' //-^ ^ 18 19 'U- y , //'/ 7 ¦ JA 'J'/ A- ¦ V/ 1 ¦ //./^ ' >9 20 ¦V- - "•' / >n\t W, t;yy ' /Ps'A' j-f yv / i <> 1~> IV 1,/17/C 20 21 )> 6< - V/ y > //V //- /> ' 'V>' S/ / ,¦ >/ j //' ' / 21 22 "T,/ '7,4' /,,y /"/Cr - /,/>% 4- r 'f-.1 //'> 'iYlly f- / V/i-1 22 23 ICf-L j{ — 2-/ ¦71. Kv /A-3 V/. 3 /JT^7 ? r /5rjr 5 n j-T~ ty />-/ %Vn,i i~! biit 24 jt 1/ 2Z, vy,; HS.U V/.0 2jT /yrr •7, J /so // /^/ S////,!- « TOTAL / t TOTAL HOUR H2 Cold Oil Ton* Sool Blow Air Come Condanuia Pjmpi 8oi'«r Fin) Pumpi Foicm Drali Fan \|ndg<«4Dil'l Pan Suplx Riwii 9uchi An«me Flow Rm Spray WATER ENDING A 0 A B ' C A a A B A B Tamo Tamp A a FlOw Raw Pillar T 'Min Full 1 2p* J7 0 /W. /vo 25/ a so it>oJ ;27 /S~ jO Wf Tank Wlr Tank Wlr Tank Oil 1 ¦/r J So 2<>1/ —- Vf V* 70 7 /¥0 /¥o 2 -?tO 0t Vj 23 -2./ 2Y. ¦ 4/,< 3 197 it>ol 7 // 7 4 16 5 t ^ 2oo Tf 5Y 7?i f* jtr n'T 2f ?f7 /ooj ?r /2D y -r A 7 10/ £rr Y ?fr 1 7 1 t 6 IN PLANT SlLOS 9 l' /." 6' 'Jtd 2 wt/ /1 i. 7o 23 7 IS 10 /S(p f ¦?' iu ! r- L l±L 7 C.U '-id /fifty "'0 > if, ' W .< r A F r . 11 'a* 7 • J> . ¦ e • Lt fr>n^< •¦",•¦. i // o 1 9 e I- 12 -.'J. i.- "V 1 \"c; - ~>cu-- JL.U ¦ r,j no 3° c F y 13 i/.7 1 •••: ';• 7 J v6y (t ¦ i. /.-., C'^ o f r. / 14 \c0 •; 't K"> I E Hi : - /<£> 19 ' -- ¦r /- ( /•.' vro nw tor, ¦ ', y 16 I , m)S ' .f - /; Y&A?' w - r?fJ /'¦. UNIT OPERATOR 1 7 C, " -• / l':v -A' U'/. • '0^ 0<" 2300 0700 TAf.xf 10 (. , — < ; r,i, )/, ; . ¦Mi ts^> /hf 0700 1500 ^ .... / 19 ' ¦ I • C ^ 2. "So /V' ¦y y% /OJ /;V Cs ^ 1500 2300 /T-A/,',;; 20 9)v . i' , r x- ¦rr /s ' :U ' r 21 c/ -• — oJr,. . r -/ V isf /W: 31:,- :u~ ? ttbf /lu i 7 "j? /,9\ Lf / 32 <. . ^ - v)/ A ,¦ H r >y > '¦> ? !hr> £>l/ 23 V ^ — icT_ iO ?7^ >// JOb 27^ 2^2. /P6 3 JWL. /5~ /it> y t 2« V-r — rir -i- ? —¦ ItpC /(,/ SQOJ /0OZ 90 /y_r ?r Total SHIFT FURNACE SLAG CONDITION soot blowinq log IK'I A lR"» Oul o' Sarvic* Group 1 Group 2 Group 3 Group 4 G'OUP5 Group 6 Group 7 Q'oup 6 2300 - OJOO 0700 - 1500 ISOO 230n a«x OCX./ V; <' >' xxz^ X. ------- 21 Reproduced from best available copy- ~ OHM NO J1«B 9 00 WYODAK POWER PLANT - STATION LOG o k WYOOAK GENERATION HOUR INO iND INO B.oO.1 Oil h3 Ei IC EHC Drum Throlll* Ambiant E ¦niuii E.nauii Air Ramowai Colli En~ Timp A,H HtaTtfl LAS 'N . OUT HOUR \| nuuR /f/W NET ENOING GEN AUX START UP VARS VOLTS Praii Tamp Prail Pratt AMPS P.... Pratl Arr Tamo Praia Tamp Tamp A B A Q ENDING \| ENDING Gioti Ganoaiion Agiiliiiy Tramformar Slarl up Traniloimn GEN , 1 M C- "7 / ?/ ? «L- ui-i ro, c 2T Ifi7 IfrU ' y ft V /J_5' 71 /Sri bfhzt i,i hi r 1 Matar MW Malar MW Malar MW MWH • 3 T / 2 1 2- Z_ at™ '(s, 1 tr(7 Ifii 2-7 7,i /J-£> /S-J s.ctv./ 3 1 ! TO XO J6/ // fcV j} 1 3 "?/ •22 //i. r 91.7 S ¦? <— •— s / .;--.o lfit /..i IV'l tW A/ h:.< h'-b 4 J IT7 V / J 1.1 / i2 2 JO -j?/ S f'of J/ iL 1L W,V mv f?.S /k'CC. XT /?5^ l?l-L jlr r. (, /iC. — ivr ;?2_ t S.bt/3. (. S 4 / (!'»' / f> 2- -C J y?i. 6 ?C2 Z. ?— w/ nr. i ii.7 / iV»7 ?-< / Itltf jr /T/ J7 >97 TMIn.l 6 S / 4>¥ fcV i 6;«3 3n J '0- , ir 2 i. / ¦ V/. 7 f Q~; r r r/c / /'¦) - /? v. r K 7. i ,j / y 1 r. o /.j-L 7 « /H2f J , r' / ¦It i ; /• / -? t/.r' 3 Sr ./. J nv — /,- . r.ihj.i f -i j. 7 8 SwO Tola' nu. 2/tfc / 7? i 7 9 /?f7 9 Jl--L- ?/ 7/" "Z a- ^ 3 //C i V> 5 / //i>- J r 7 ^ /j" j —.- / t L. V 7//JL •j.rlsi.n 9 7 17 lit ?2r ? o j y-' 10 ri. j — 31 ?2- //.r ¦/ /'<¦' /^fo ,'.i / 1 J7 y,. /C 7 rtJ r y//a, 10 8 n ¦ii /.?3 7 ! 7 o ¦>. t. c 11 3Li _ V" -JL- V-/J /A/ V 9 nvr- A/P ¦r-Y 7-V /crt= _ 2o y ¦/W/7., j'///?- ¦ 3 1 1 /« t ir 37 / ? a 7' i 14 Xs st# _ JL 2~~ <>-/-, f < -4 J c /W; f r. f hi t 14 11 ir°ini ?(¦ 3 :* o in IS "7 7 y; '.C'.Q ft, ; 7 /.rv/ ^ ? /)" 'J ~7rJ~' ) -v ^,j r?i/ \ IS 13 / 9 3K "\I=S ir-rn ??r 18 — . >11, W/-" > r ' V >" £/-¦¦ -- .y r /'t I ' •' 1 ^ 16 I 14 n Jl/ t8s r i. 7 1 7.71- 17 %> J - ' i ? ^ -Ov ijit y >t'< >.r/ / ¦/,/, ¦) ( <"' < //'V,- A t 7V'J- — id/ Sue roia' ¦T&rg, W/X 7/?i lirj IB -711 ~ ??- >¦/ l-fLtJ 'ii- - Ub<, //'•-" / / — J, S/sV \|V">' f > ?r> -Vf, «— 'r>f y,; , rA"i f 19 <6 /'"T r, 1,:/ -X 7 O 3 7/ 20 it D ^ If thy W6 /r — w? & CiAi 30 'o;? i)"7 ^,y "" Ci 31 Ay, ¦ "V — //* > '// /j /?yj //y/ — /'A, ' 21 18 IZiQ "If. V iti. > J 37 •itt ¦< / //r ' /- /fr t /?-/ i 7 — Pal Jj 9 l / 22 19 '/I \h(// 'Ck 33 y<-// 1/ 10 2 7 w. y t/S.o IIYI* //j/ ^ A - - ii i T.ohil. ' 33 30 t 7T 1 'JO 3- 34 SO-< 3 / l0 2L ii. j 1W.7 IS 7 6 ir n ib 7. ? / — °~c>3 1.7 -1 4/7 1/1,7 34 21 ¦1M V />'v^7 > f iTOTAL / 1 ^OTAL 22 ??L?/ 3 6 1 t k~r/j - s o n r i SuD Toitl 7 fC > it i 'J?f HOUR H2 Cold G«» Tone Soot Blow Ai' Corn An>pi Condanuia Pumpt Boilar Fax] Pumpt Fo'cH Draft Fan inducM Draft Fan Amo» Su„h, Rah... Suphi AI tamp F 'ova Rhl Spray WATER Full 23 2 X'lt 2 Jc. i 1 2 1 34 ZiJ'IO- )ilfh i'r ENDING A e A B c A .6 A B A 8 Tamo Tamp A B F Iowa Raw Fill/ T D»» Total £ i¦> ,? 7 11 If 1 * (,L>(r , ____ J.o( i (a r£> T? 777 77 sr }?'/ /'jf //. /£/ 'It-f 2.70 2^6 7 7/ /i? -> say sG^ /sr C VfT 23 :• i.. ¦' 1 '1 2/,i Pr» Ioiil 3 ¦V 2 OS' S(e <"-j' — •t?s 17. ib/ /Lf 2?r i76- f?r /uul 95- /(»o -7 5- 7 /?¦ Tl to ~¦>• 4 cJO(e> Vf- — 7/ jon ? ^•1 ? 5 v^ jrG r ¦:« J7% 1ZY 2 7 2, -?7J 97 foot ICO /6Q 72. VO 7, V " 6 yj" -2 e>£ -LS — JJ /(¦& f (of 2?./ X70 j ' >v.; / L, / - t. S.'/^ A' J 7 // o fa e t-r > O — jV. /r-t /'£/ '¦ 272 IN PLANT SILOS Pr„ rt-xoi 1527^1" s:i t rixftn llJOk 9 4t Joj S V ^?r y.« ,7 7 LI .-'t: ? //7)X r» ya 33 7 13 Pra. 7ii.lt ibhO £>3-2»j' 7- 7' / / hl/7J itirt /^X:- / 10 l/T 7 & i- r £, .— 'ft 7 ~ /c- o /Jl c» / w O To A A 4 Total >?r7 17 0 rto : 3Q-? 1 1 -Vt C<- 777 ;<- "j- /-x * 7Pi^ ^7/ / i>V T O t /£o /V oo\> /cca ;y-j f -r (zp Pit! 77WI /kdtn 7/H70 niw- Vieu ?°77/2 TiJ/O 16 U y /?/ fS T>/. ! ^ io/ f// ''Dol //6 >o UNIT OPE HA TOR P»a. JiCS'O Ui/, Yfi -Si " OJHo 7 HtZ, 17 H ' . " ~~>ji „ /L n Wfr 'tto j /n-3 '/->n Up 2300 0700 7/f<¦>,,! Total 7x/n iYt.fi Wt,< 0 3757 ~ is 1Z IB <-if ' )r/> S ¦! 'V »' -rr1 %> ^ 7b^ A? > 7r 0700 1600 , ,4y. 111 Mo 19 Li ¦ ~3l>! ^7— V7 — /J2p' /Oil /OJ i 15003300 /A7;h,H,) 4 HWS >?'!.* £/ )6Q r"/ /fn 7?r PLANT OPERATOR LOG 31 — , )>v r / K3 __ 'S'4 W A.-; fu>/ Jii'f /loo >OJ 1 i/r yj 33 yV _ ZOJ «r U frr S>S7" nv ! 1 :j i, rixiB s~~( ' • ' . 33 V ^ su j?£ 77? 117 teO S~ 1001 //r /&o 34 f A <(o r? ISP n-?. /tot X7/ J »0 / /vt> / f.O 6? Total FURNACE SLAG CONOITION SOOT BLOWING LOG 6AXI //// •-,* - V/X x/Vr , arc i:ysf X < < X- /> < > x — * / 4—A-A nuJ ¦* < * — x Mc'/y' y^ A l>/>v xxyL [ • / \|y Xst' n ------- Reproduced from best available copy. FORM NO 3'9fl ' 0 1 VVVODAK GENERATION HOUR 23J V4, J SrK if rt NET ENDING G'ofti GinnKon Aunlif'v Traniformat Start tip T raniformar GEN Mat.. WW Mat' MW Matar MW MWH I 2.J707 Jii/ !r 7 i X V 3 ? "Z_ 3 Xio br! JfcZ- 1 H 0 1 a o T Y 3 I'M XI JfcC ft 11 V ? ? ?T / d 7-17'1 o /et c, 7 2.7 7 ? ^ 5 JL(J 5 7 txYi 7 J © 37-} 6 ?sr / J 1 Hon, x'f J ? ?. Sub Total 0.1 L. 7 >(.7 / 7C- n<<> / ??/ 7 K.: .? 1 7.T2 14 / '1 ' ' - sir .< < a -V. -'P Sub To'' -Li(-c 7 • 5 2>7 J f J > ?7r" i 27 ' v"' ¦'/M/ ^ f ^'¦2- '» wt /& i ?y V / ¦ 'j / ie Uh 11 Sbl 6ff (r 19 hi?ii H 30 Ufr-i ?! J tsv?p. /V 33 / ^7 t,t 9 7U o i" 34 it ?rr ! IVYC, i" 0 31<^ Oav Toiii ?w3 ffOf T? sc. O rro P»w Tola Tl to Data Nat Main Xmtr Gm Van Ou Gan t Va't tn Auk Xmtr Mvar ° ACC 1A2 MW iCC 103 MW Coal • Handling P'H Prn 7'ii 77 a ma?? 7 Iftf rfrj * ( &pY < nvvz nroz / tofto? IfrlZtf Total !.to\ j SDH V" JoV ?7 1 I in WYODAK POWER PLANT - STATION LOG Coal lmagrato'f SCALES A e c O E H 1 H3 Pxt 7?&7o7 ??76?t L7hrt 7J?2jd 7/G> \ 0 yjfe nisei. Vg-Jgyp ^<3^.37 c7^/J 727/0 Total jim* ZWiX. 7i30( 0 V/J9 XSi. 1 It Mo /}«^i nis u.iv ! tt'i WYODAK PLANT OPERATOR LOG 131) 2-/Z- HOUR IND ¦ NO IND "¦O" luba Oil H? . E'lC 6HC Drum Throttle Ambiant E.h.u.i CvhauiT A.< Rtmoval Co',- E«o t«M- n. i //j". 0 V/.Y If70 i c /?j'r /^a'y jjt 'r 7 7Sf t 9 '/ It/ Y.7h2.t„ J 3 Jr.? JO ¦ ¦zS z~>- •rt.i Ui.S it/j /<;/ /jvy /W/ yA T. J //J. <> ' ' S ?e ? Z. 2- YY.} !/<.! V7.? /s ;o /J'/f /fzf Vv- 7-r /5".5 30/ >7/ tih l.f .'.//« t 6 ('< 2.7, W itfC w, y / - • 7 J- i-s" /?•> ;r 7.y /J~n X-pr i o,-. p 1 — - k 0. "11 T r ¦ C >0- i 7 "V •"'V-T h-s -7. i . i o'/7 Ll,7(^ i / 17 11 13 J,-: '1 ;rr 2 '/ V 3 I'J.'-'. I'r'.'i M'-l i r ' n-T A 3 kc.«- '• -to ¦>.?/> ;.7 • 3 13 2^ ,T./ ' " s''; i1?- <+w. M i ^ M T.5f >X 7 / fho ' •, i LP /"C r> ' ¦ '< <> '¦'"// R >3 t« 3o y ^ 'Wf ,T'1 ;1 O /- i". r'fS V7/u_f 7/':n 14 13 >-'j ^ ?-'> ¦>/ V';S //'V /J?"' / / , //>/' fv. /¦?' •f.wJX 16 1> /Q //'- r.' //"' ¦ i ^' f ^ ,oJ '¦/ fj tO t6 IT / . ¦> z 'A-T //r' <7'' ^ r '¦r r 'ft?,- uih <;;> W) l i 16 j ) 7-9 Z' / / IB 19 , / / >9 30 / / ,31 / / 3 • 33 / / 33 / / 33 34 Try 7/ 2ct •iW //c,7 ^.3 A>%Z ar /fc-r J 7 7,7 /n /•rr y. f/'J.J 74 TOTAL / / TOTAL HOUR H? Cold Oat Torre Sool Blow Air Cott Condanuta Pjmpt Soilar Fl«d Pumpt ForcM Dra't Fan inducnj D>a'i Fan gut»h. Rohaat Supttl Aliamp F 'OM ntn Sorav WATER END'NG A H A B c A B A D A B Tamo Ttmo ~ B F'Ow \| Raw F,H«< T--HIU F..«' 1 V5^ S(r rj — ?7$ 7?/ /tr 770 io'V lonl //s~ /4-0 yP Wt' T»nt> Wir Tank w». rank O-i vr ¦ S> 'n — J 7? T?f /¦>7 •ZtrC not, /'03 . /t r /C-o &-o 33 2 & 3 V/' 16C <(- r-? — ?:> ,sv? ¦— />;s ^n0 — "? j _ 1 S, '--''I /G<2fr Url r.-a _7 IN PLANT SILOS 9 Li-r^ = ,r,V VrTQ 'tf- //i-3 _ 3,-7JL 3 In /oaa fOOt) CO 23 i 15 10 A"-# T-T .r-? 'l-j' IfpTl' 3 '?-> 'J ?o /»J /OO/ / -;-r> A £ /T / 11 Lr PCjrt '¦X~ s ". .'1 . r>7 ? / £.- 7 'Y.V ¦Q J'/n w e f- 1J y-r- 0 ?c) ,%-T ¦ ,V^- 1 'ZU: if $¦ ¦ ¦-i /. rc> c/O c /- A 13 • :o AV? •3-, fa .7 K " 1 c' >>>2 lPO« 1 '.. o O 7 14 lLT • rS:^t — / >- .t> A'- . Kr /^o "E 4-/7 ^20 &/£• 15 L'/ • j /I J-J — • ~J 4 0 4>v- ^ bt~? ¦i'v. )/, . / ?,yv /Jo //t r j-J 16 y> i- _j 1 - — %f\r .v1 ¦ )7- tfn UNIT OPE HA TOR 1 7 1: i " s i —— rt>h /I.o / (-,'r? ->// ^7 fry fst? /V ? 3300 0700 7~/c~ £- 18 o.oo, 19 15003300 •/ ! 30 31 11 33 74 vf 2 — 37 t 7£> JlrV /t,o 3l',5~ /€>& ~J /e>03 /yn 2 O .Total SHIFT FURNACE 9LAG CONOlTION SOOT SLOWING LOO i« « & ifl'i Out of S«»wica G'Oun 1 Qrouo 3 Grouo 3 Group 4 Group 5 0'Oud6 G'euo7 O'oue 9 3300 - 0700 Jrxyx > xy v Xxx-y vx.jt yx,r,r yyX/ xr V ST-' ' 0700 1500 )CiA)Ci C X X v • K , -vy- VA - f> ' 1500 7300 m mC K >'X M ' Xf ------- 0 1 (\|HM N» 3191 • •• ' - ¦-¦'¦ - WVMAK GENERATION HOUP 3C> Z £ 9 > 1 VV Cc &y?7Y NET ENDING G'oll Caiion Auxiliary Tramformar Start uo T'antformar GEN Matttr MW Maiar MW Malar MW MWH 1 7 >1^1 jr/ 30 3 77 2 3/t>7^ ^5 nso fc JO rzf 3 3 >122 JSc /KJ4 JO 4 1/77? 3C,/ /?_r£fc 71/ 5 32 I £¦« J&O /&17 3' 6 3 if 1 7 Jrt- 19 i 17 30 Sub Totai xt vr i/tr ) it tn 7 » ?Xfr7^ ¦7S '1 7T.TO • ,3 7 <2~.? /¦?•£. 7/ & ¦JO XT ? 9 J-5"7 H7 i s o°t ^ 2-?' 10 Uii 7 C d o 4715 7 ir 2JT2 1 1 j y/rv5 ¦17,7 7/0 J7 S 12 _?$rv/ 7 a rw n 71 7 s > 13 XT? n s\z<~ a. v.c 14 ? 1^-) 0 X 7 9 n»rl Xi i.t / Sub rotai f6,o f DISS ¦ >fofc 11.r 19 3S-.-J10 3S~ D >« .1 5 i» » I 3U 1 M9 /3 JJ' Jie " ^.0^7 7^9 43 3.1/. IB 11 3C,(. !"»¦; 7 I .10 35<- 1» 3C. 77! 3Li- A»oo3 jo J35- 7* J 1 <41 2co ,3o 21 3L, 3 5oo fcj 3o ??3 11 ? 7S 7fl 2»M1 ,1o JAL Sub Toiai ICO 1 j^OC) tl/7 2-il Jun 23 n zzs id / Z7 jy.r 14 3i f 7 7 /fr/ X6I 3 Jo J3/ Day Total (2 JO 72? yo~7 bo Prv Total t> to Oaia Nat Main Xmir Can Van Qui Gin Van i Aua Rmlr Mvar Start Up Mvar ACC1A? MW ACC 192 MW Coal Handllnf Ptm ' lot? £>iZJ r 7r//W StYo ' 57/0 1' 17tfY flrr/^ Pin, ! :r/t rhl/Z ^2, 1 r 7Vjf? S-J7A1/ ">7S-)7 /trcC Total 7S/0 71 c ? X7? / 7 3/6' c,z to in Mo -• Coal inragrafon SCALES A G - c ~ E HI H2 P'M 9l7i! 7 1o7'YS 'iS')e / ffm IK-7'7 Wt:-; i? (? 7W2 Toial j> 9f0 7,7fcfo«jC.^7 ij. ^ 5 a 3HZ. V • If Z L ks rr ,^5. c. -0 icrC, ¦— I?."/ ao G r.o/l^'g B 9 0 0 £ R- ¦ XI ¦ft. H I H'X Of i<(-1 AT .16 ft •<=> (V h n. j y/H 9' 10 2 -JO ^2" 7.0 ~)3 't-lf- r t-o. -J. tcr.'! /19c, n?/ TT' Mfir I"" 10 11 r HM.M 'Wi' ft 1 fTirS r?.r Rt(- I ( ii# (tl J t/.v /9o fT/iiJt S t In i 16 17 Jt-f 3 t So 2- //J w* / hL<* J# r,i'/ Hi1 U l Y>1 / TOO C.I //IJ 5J /,vl 19 70 ,?Lb .1 .n WY //.f 4 7 ^ W-3 /Slo 3 rf KJ 1 /!'? 34 7 r / iV " T//> > J V //) ? -71 22 - / / 22 23 /C-& j/ —— U Z. Z~ yy>.f tfSO •/j-} /r/0 79 iy /?LIA J/ /..£ /^7 =,tJ/:.7 23 24 jf T-O "2. Vf-r //Y,f V}. Z. /-r<y 7/ rtYi ifn J0 7,0 /y 5 tSjT i-nab s-.fhxe 34 TOTAL / I TOTAL HOUR H2 Cold Gas Ton iOOl BiOwAir Carre Ampl Conainitu P impi Ampi Boi'r Fifd Pumot Amot Forc.d Draft Fan inaucioD'l'i fan Ampi Swhl Rah«at Suphl Altamp F ¦eC tOOZ, S-J- 7 e-( -¦ tr — - 4 "rf 20I S<* SJ J7t ni 3tA ieol toof /^r AO 15 11. »' 2 t. -T 9 yf 3<=k sc, SJ —, 17i> -72 >/-/ 3bJ ttob JoeV S 7«r 6 tr — 3.00 S 7 — 77* JO /6t> Z" 395 iCoX. ST ~ 73 sc> 7 7vT < u> ¦ "— JT )fe> JTV /o" :&o* Vr-j" 8 — : Ofe \ 7 5 -7 — - /CrcJ r^p Dl& 'j-** ftS tf ' j? 9^ fc.y Tr-) w — B f- r »2 "JT ¦ " ~) N 2. tf A — sT-'l Tz/i. /J* J 2/n- r- '-.'"o ?o C > r 13 Vr — J O1' — J" ,1 / £ ?;.r HO f>w> •—• D t P- F 14 ' 1.1 r, in .V^ /'TO ro '/ool ^ 1 -— Jrt M7 - " i> it? 15 Wfi" loo 4 '' ¦^78 ftoO ii-ft 1.701 26S /oOl 11x4. JhD U 16 7oo ¦v<- .f ? -L lie 7^8 /noC ict. 2 70 176 /eo 1 /©«» /;f£ ¦7f 0700.500 J-' 4. IB 4 s- It t •rt J7S /ST 170 no /CD /L.o Vo 1500 230^ -Vfiirfg- 20 . •/s ¦Kt. ,v* 1 JhJ /aT ¦ 34/ <791 f(o >T° s/ f 21 51- 5" 3 7f 7 nf 7 ^ 1 ?o !rD 3 /oo? //o 160 22 23 M s? -— 7flr^ 3>V /f+f /fro 372- 2/n ^-T 24 r< /I' • ru 5-7 777 J fV Uo 27d ¦xi/ J oof /«L //>" /Co Total SHIFT FURNACE SLAG CONDITION SOOT BLOWING LOG IKiH iR'f Oui of G'ouo 1 Group 2 G'OUP 3 G'OUD 4 Group S ' 0'OUD • O.o™ 7 G'ouo 8 2300 - 0700 KYXJC if XX ?vx .TV* JT y 7 x.x fSXK yx X sr n 0700 - 1500 v.v.w/ yxk'^X < y/ l- X '¦' k- ¦-¦ V. k v -v;. If!;. - 1S00 23DO /if A y .¦ v \L X V / X K ------- WYODAK COAL AND ASH ANALYSIS C-112 ------- WYOKAK COAL ANALYSIS Date 2-1 2-2 2-3 2-4 2-5 2-6 2-7 2-9 2-10 2-11 2-12 2-13 2-14 Avg Time 2300 1700 400 1530 1523 1010 300 2330 800 1600 434 311 500 Ultimate (wt% dry) Carbon 64.36 62.34 60.90 61.75 61.94 59.52 57.07 56.60 59.77 57.73 57.65 58.50 57.1 59.63 Hydrogen 4.77 4.90 4.66 4.31 4.59 4.82 4.43 4.20 4.45 4.17 4.14 4.58 4.45 4.50 Ni trogen .86 .80 .85 .91 .88 .84 .80 .82 .86 .84 .84 .78 .76 0.84 .68 .98 .73 .37 .58 1.86 1.09 0.63 .71 .33 .35 1.03 .67 0.76 Sulfur .67 •91 .73 .36 .59 1.89 1.03 .60 .69 .31 .34 .96 .71 Ash (ASTM) 6-81 6.31 8.38 10.32 6.49 10.03 12.11 9.57 6.64 9.67 10.99 10.57 11.14 9.16 Ash (240B) 6.00 5.56 8.08 6.08 6.40 9.99 12.18 10.33 6.37 10.30 10.89 10.05 11.03 CaO (wtX ash) 24.49 22.58 17.95 23-19 21.37 12.94 11.83 13.45 22.49 13-91 10.45 11.46 10.65 ------- WYODAK ASH SAMPLE ANALYSIS Sample NumDer 925 942 945 950 982 983 002 004 005 006 930 953 940 984 Date 2/2 2/3 2/4 2/5 2/6 2/7 2/9 2/11 2/12 2/13 ?/14 2/4 2/2 2/6 Type of Ash Fly Fly Fly Fly Fly Fly Fly Fly Fly Fly Fly Bottom Bottom Tip Ultimate (wt% dry) [ Carbon .08 .42 .09 .14., .07 .20 .12 .10 .15 .28 .28 .25 .37 .26 Hydrogen .02 .02 .01 r-01 } -01 ( .01 .02 .01 .01 .02 .04 .04 .05 .01 Ni trogen .00 .04 .02 ^00 s .00 .00 .02 .01 .02 .01 .00 .00 .06 .01 Sul fur .41 .36 .44 .47 .47 .44 1.03 .40 .37 .42 .40 .15 .09 .09 .43 .28 .43 .43 .48 .42 1.06 .41 .33 .44 .41 .17 .11 .08 Ash (ASTM) 99.68 99.60 99.76 99.76 99.73 99.74 99.29 99.73 99.73 99.75 99.70 99.58 99.13 99.44- Ash (240B) 99.66 99.36 99.79 99.58 99.83 99.75 99.26 99.79 99.81 99.48 99.71 98.76 97.39 99.45 CaO (wt% ash) 19.32 17.88 18.57 18.69 17.51 16.46 21.14 17.19 17.93 18.17 17.93 11.27 11.77 8.72 ------- PACIFIC POWER & LIBHT COAL ANALYSIS JANB5 DAY TONS XMOISTURE XASH XSULFUR BTU/LB 1 5829 31.6 5.9 .51 7957 2 5740 32 a 2 - 5.2 . 35 7924 3 5946 29.6 ,5.7 . 36 8278 4 '5832 30» 5 5.4 .39 8011 s 5941 29. 1 6a 8 .28 8126 6 5398 30.5 5.9 .27 8223 7 5446 29.1 5.8 .35 8315 B 630B 30.0 6. 1 .43 7941 9 5811 29.6 5.8 .34 B134 io 5934 29.3 6.1 .43 8261 it 5752 29.7 5.4 .45 8195 12 6013 29.3 5.9 . 37 8119 13 5851 29.1 6.1 .42 8231 14 5725 30.8 5.5 .25 7946 15 5826 30.9 5.4 .30 7983' 16 5815 30* 2 5.7 .40 8081 17 5779 30.0 5.5 .39 8127 18 5888 30.2 6. 1 .46 8008 19 6650 ' 30.4 4.6 .30 8160 20 6164 30.4 5.3 .32 8066 21 5341 27.3 6.0 .40 8289 22 6560 29.3 6.4 .78 8137 23 5752 30.7 6.6 .67 7909 24 5742 30.3 6.1 . 65 8081 25 5547 31.6 6.0 .40 7970 26 6105 31.8 6.4 .35 7812 27 6038 30.8 6.5 .52 7950 28 5945 29.0 8.0 .70 7982 29 5518 29.8 6.3 .64 8148 30 6044 30.5 6.3 . 54 7963 31 ¦ 5870 ¦ 29.5 6.3 • 44 8109 WEIBHTED AVERABES 182110 30. 1 6 .44 8077 cci Plant Manager—PIant Operation-Plant Engineering Thermal Operations Dept¦-900 PBB, Resources Dapt«-300 FSB C-115 ------- PACIFIC POWER St LIGHT COAL ANALYSIS DAY TONS XMQISTURE •/.ASH 1 5981 28.9 6.9 2 6107 29.9 6.2 3 6352 29.9 6.9 4 5980 29.5 6.3 5 5962' 29.5 6.5 6 5680 29. 1 6.5 7 5302 30.1 6.4 8 9 10 5502 29.9 6.1 X8ULFUR .57 .50 .5 6 .46 .36 .59 ,40 BTU/LB 8126 8131 7993 7987 8081 8123 8012 8028 WEIGHTED AVERAGES 46866 29.6 6.5 54 8060 ccs Plant Manager-PIant Operations-Plant Engineering Thermal Operations Dept.-900 PBB, Resources Dept.-300 PSB c-uOs-) ------- MILL NO. ¦17.^2-^ ¦ 'A PhTA TAKEN BY KW ON mill: Lino PfllMARV All? FLOW : primary air temperature \|"fILL OUTLET TEMPERATURE FEEOCK speeo• _'o Coal Pipes sailed J# • I J 4. ~ / F LSI 1= ClTS'rn. 2. ~ ~ 3. O 6. O SCRECM SCALE. ckahs mi sicrc % on SIEVE % F.AS3IM6- So f/3Z7 94. SO too 3: 293%. 5.3? zoo /2. V7 7i- /X • 73.3 ------- PULVELR\TZE.R FINENESS r>AT i= : PhlCe-ftr . :.MlLL NO — - DATA T^k£W SY -0 kw on i-wu.: V35"* k-u/ PHIHARY All} FLOW ; %¦ PRIMARY AlR TEMPERATURE. T A '76 J V ft ILL OUTLET TOj PER ATI/RE Z ¦ /30 F (175 MA.) FEEDER SPEED r . Coal PiFES sai^i-eD : L O 2. O" J, 0^ 4- ET 5_ ~ 6. ~ SCREEM scale. GRAMS mI SiCfE €JJ SIEVE. % PASS IMS- So Si £,7 ./V/i 94. yr too 7.0/SZ? 7,20$$ <12.2^ zoo /&. 3/33 /?. r/ 75" 13. ^ &RA1& IM Af TOTAL SAMPLE /T, 7/. 7 3.V32S' . — 97.3709 '/GO - REMARKS AMO COMMENTS; ------- date: PULVE.R IX ER jUul&Z FlNtNEss ttlLL NO. r. DATA TAKEN BY MujM KW on Mux: yp/Q KW PRIMARY All? FLOW : 4V '/ PRIMARY AIR TEMPER ATU RE. ftILL OUTLET TEMPERATURE t FEEDER SPEED ; , ^£1 /11 Coal pipes sAmpt-EC i I. ~ 4. ~ 2. ~ S.D. SCRECM scale. gh«ih3 #» si^ve % «m SIEVE % PASS l#/fr SO ,?&77 99J3 too i.yi23 92 ZOO /jT9f09 ;C. ------- PULVBR I2E.R FINE.NESS date: VI / MILL NO. JL DATA TAKEN SY ¦A U KW oh Hill z X'o KW PHlMARY Al FLOW PRIMARY AlR TCmPERATURE HILL OUTLET TEMPERATURE FEEDER SPEED I iio ML /e Coal pipes SAmf>i-£t> L ~ 4. 2. ~ 1 1. SCREE* SCALE GRAMS S»e\|f£ % on Sieve SO .2aV .2.7 4=7 99.7 a too 5: ?7od' Low '93. £3 too .H V531? lot 13 6AS IM ^AN L5.11UZ ^f.^zrz TOT At %AMPlM ST- /oo 'f C 175 nA>t.) 3. ~ 6. ~ REMARKS AMD COMMENTS V C-12Q' ------- PULVE.R IZ E.R F"I N ENE&5 date: \;/ F~ MILL NO, data taken ar KW OM HfUL 7 PftlMARY All? FLOW .* PRfttARV AlR TEMPERATURE. * ftiLL OUTLET TEMPERATURE Z FEEDER SPEED z y o 'o COAI, PIPES SAmf>l-Eto I L Fl 4. ~ 2. ~ s.Q F (f 75* mx.) J. ~ 6. ~ SCREEM SCALE CKfcMS a«J S«er£ % ew SIEVC % PASSIWS- 50 .^)5t . 237Z- 99.7c, foo 5". V 9 GO 3-sm . 200 9, s'Svs* tl, zrfo .' H- si 6«A«S IW MM 73.3399 ' fV. il'7 TOTAL MMftUB n^: /o<9 REMARKS AN0 COMMENT5 J ¦'V C-121 ------- C-6 WYODAK, FURNACE GAS TEMPERATURE DATA. C-122 ------- FORtihte GA6 TEAf?£&.f\TO&£ $He£T pftTE %/jj? LOCATION /<$ -fl < //z& bhmkJ 4P ' j6^H \t\€ ¦ ,^ku; &' Uto ' I ' l'-p (}Ot> fou>) <-&KcU }JJM /Go) \ /C?5 S /9?n- lb\V (/) U? fk>K /£>$ frjcJ>k- /&Z& '¦* J) if ni -u ¦ /(s&l \ f jtc^yjr* c K- 'V- '>"•<•}" ,uw ' W-'-ctv % lj ------- r Fl)Rt$i££ DAT^ijjfyf LQCAT/oaJ Uycjyl__ 4J-J81 50 SHftTS J SQUABE tl .18 3 IOOSmICIS s squarf 1 339 200 smus. S SQUae OAS TEH?ER-f\Tok£ J>Tfl S HBBT TIME FLOoft PORT DEPTH /Vd£,L£ . H,0 AM T£MP GAS TEMP "°C ££>iM£lAT /& Mil f to o no& dl Ajrffhloutea. A* tfaoilzy o-f ?.? 1> 1 3.? 7.1 Z°J%.1 to /L /£>-'/8 jr // of t&lb /£>' 0 Jn° AsiS^ 5"o // 3-3- M0CJ* i at/~ C^pt c/t //M - // 3o IKS A-h-rti /s ; 2,0 IZ. li7~& /X:Uf jA W5 i tS p&t t O L' 5.5 to // to T Pc I >/H - iKr,>t j , // I ° S U)&M htc>uM4t> .sh^dfcid t. 5 S/tW y, 0 ///o « v-mm /0 ID JZlD {/ 10 0 It 10 4^3 ------- • SCSI"* * SOdABi PuRhibte GAS -TE^ck^roit£ i>rft sHbbT ¦f 4 TIME FLOOR Port DEPTH ft Mlkiz ik rijiO RrcC""** m hlR T£MP ef GAS TEMP £j>MMEriT u W It 0 o. C P 1370 -Vto j fsi" &cnf£{JreA * H /(r 0 !W'U > i to it 10 0 /•v-vl- ¦3 (&k ^ // ------- f f jr- i ti 38i ;q;hhi$ 3 squavi m/sba I 41 %S3 '00 SNtfis i square I «M9'» 200SHECU SSOUAflE FvRf&tE GAS TEH?£Hf\Tok£ /Xrfl $HE£.T DATE t"lh^ LDtAT/oaJ U^jcJak- TIME fLQoR PoRrf DEPTH i«t (H HiO fyiUilUH »w H& T&MP GAS TEMP doHMEMT b-c>u''k&jfcr - h\6~* M.fL€jukA /Z/(f 8, u> 10 o /13 V Zo /S" / 3^5" ^ -prA -f UJ /&> /sW n /3 15 58^ I40L o -f\5 €71 •y.2. V< V.- L_ ------- dt I 1 -M» iO SHIlfi 4 SQOAHE _ JTA jasSMP O 362 100 SHtus i SQU«f f X \| <2 309 SHUTS J 5GUA8E ^ ^oR/^^£ -f-EA+pzRfiiruXC lTft SHEET DATE z/u/tfS' LOCATiok} TIME FLOOR PORT DEPTH A/Jbie A(arifw< in Hi.0 RtfUiH'n ,„M3 Arl& TfiMP IP" GAS TEMP V dDMMEfiST /VlF e 3- £s> 9 & /3/7 t-l3 i. (W i\. O £?/D U 1300 I 3Ji€ fajLOi, Arr. 3&i» t 4 ~tAjlA . t H3J> % c? S".S~ 4? 12 & . : ¦p t 33p-/3v 2 & 0 /33£ ------- I < _j-iL .•' . 'vy, . , jr \| «?•j«i so 4hehs s sou»e ir , y • >•>' JPl£fl> I 42-38? lOtt jMfflS 5SOUBI f f * ' j \| <2-2BV ?0O iHfcttS 5&CUA8F <3/15 TEH?£f\Ti>ilt; imft ?>tiEE.T 0^ X- If- Vh" /-Q^T/o/U TIME FLOoR pair pmn AMkl£ ABlnfut ia K«0 IviUiluM IA M5 A) TiEMP "f GAS TEMP dDMMEriT < - j- ___ /J& 7,5 % f-rsry\ cam. f-V fo' t jy J /34 $" \riv^- '9$,' ' ksv-i 7. - V-fcr~?-i7«? {^~^L V'/ H I V-l ¦ i i i j i f^ll /.' L S °y _ tZ 9o }y v°\ & 0Q-(3t& .,+.\g;\. „ < .. - , . V'''• -V r'ff ------- r- r\ Jt \| 42-381 50 SHEH5 5SOUAM ¦9C9 17 16? 100 SHEETS i SOUABf t 3W ?00 SNtfIS 5 SQUAftE mret ^ locations C,A6> 7T^?£^t\TUfi£ flWV SHBBT TIME fLOoR port mm AA»4t£ AtonJicc m H0 fv4£UUH i« m. T£MP GAS Ttmp CjoMMZtlT ^h- Stf }%¦' 45° 1 <)(? i/i° ludt'froi^yuJivv-s "7 - 3° ¦j-t llf "Z- S' 45° IZS 3 /3 3C> 1 hS £ 5 45" 7 6 ¦ s 9 0 1453 34 ( # L. > 7-^ /if a 13 3t {Z^ 4>.D 7.? mv / £s» f( f5o1 /fc- 3D ij ------- r FijRh&tB DATE: l LDCATtosi UJyoXb. r\ O 3av 200 SMftfS S f QUAHf <345 TEfii?Efif\roR fe £&T/V $HZ£ T TIME fLDcX MX PEfni Affair A6ri^ii< \|k i4l0 m Hg ArtR T£MP (k(K S TEMP doHMEtfT /i og 1 t5 —* 45 -7. ^ ,.0 1 o /V/r /)€^-r b y tR/5 j b}quj b Ciu.s ff >J f£.vh 3.^2 & h 'D (r- ^ ^r3 r/_ 5". 12 7 /¥~7j (Wf/J'" /^s" /k 4^ / w 77F7T /4? 3c / 1 gltes^" 3 o Ik" 4° ;37t_ '—-"^p / -/ 2. x- /j 27 _ill2_ ilH_ to I ts* I (e> ^S' 11L £C> pU 3-0 7.Q C.o k.o 55^5 /O-O fc- O 6- fe. O /y^ ;.nr /So 5 /f/y _?jW) - p^jjg3 3,-7 X- ------- r¦ f, 339 100 SHfSIS S SOUAHC FoRt&ce DATE 2 -12 ^LOCA TION lJy0)^_ lc_ GiftS TErt?££t\T0H£. £rtT/V SH&E.T TIME rice* pout pem AAlbt£ in rtiO ! v4x>jv\ m Mg AM T1&MP Of Ck s TEMP do^MEfii T 16 oo 7 -th. 3 4® 3-«> \o lllh At? hlovJ IJ 3'- <-f /W.oo Iffij f^vy m± IS i n?f i&>i i~?j H 3 y Z.o 3j> fto 7 igj> iSlU ho %Q IP 7.0 3.0 . £.0 /33y TX^y ?! fit M> 5o»"f"fc I OuJij 3 f iF T c- >£+iv" 5«.+ bt"^ ' ll#o 7 /JU3 5' 4S <.S" r.o mo 10' ij i4^ j^fvynkj- Hto-Izof 36P ftp (1 IT io 46 1.0 _x fr-0 ^yo nio I 110 II f £,-jj 3 ^ £ L— Lii> *y £»© -------


EFA-600/7-89-015c
December 1989
FIELD EVALUATION OF LOW-EMISSION COAL BURNER
TECHNOLOGY ON UTILITY BOILERS
VOLUME III
Field Evaluations
J. A. Reese, A. R. Abele
(Energy and Environmental Research Corporation)
and
P, W. Waanders
Babcock & Wilcox
20, S. Van Buren Avenue
Barberton, OH 44203
EPA Contract 68-02-3130
EPA Project Officer: P. Jeff Chappell
Air and Energy Engineering Research Laboratory
Research Triangle Park, NC 27711
Prepared for;
U..S. Environmental Protection Agency
Office of Research and Development
Washington, DC 20460

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	 	1 TECHNICAL REPORT DATA
	 ' {Please read Instructions on the reverse before completing}
t. REPORT NO.
EPA-600/7-89-015c
2.
3. RECIPIENT'S ACCESSION NO.
4. TITLE AND SUBTITLE
Field Evaluation of Low-Emission Coal Burner Tech"
5. REPORT DATE
December 1989
nology on Utility Boilers;
uation
Volume III. Field Eval-
6. PERFORMING ORGANIZATION CODE
7. AUTHOR(S)
J. L. Reese and A. R. Abele (EERC); and
P, W, Waanders (Babcock and Wilcox)*
8. PERFORMING ORGANIZATION REPORT NO.
9. PERFORMING ORGANIZATION NAME AND ADDRESS
Energy and Environmental Research Corporation
10. PROGRAM ELEMENT NO.
18 Mason
Irvine, California 92718


11. CONTRACT/GRANT NO.
68-02-3130*
12. SPONSORING AGENCY NAME AND ADDRESS
EPA, Office of Research and Development
Air and Energy Engineering Research Laboratory
Research Triangle Park, NC 27711
13. TYPE OF REPORT AND PERIOD COVERED'
Final; 9/78 - 6/86
14. SPONSORING AGENCY CODE
EPA/600/13
15. supplementary notes AEERL pr0ject officer is P. Jeff Ch
3738. (*) Contract with Babcock and Wilcox, P.O. Box
0351. >1
appell. Mail Drop 63, 919/541-
351, Barberton, OH 44203"
is. abstract rep0r£ giveg results of field tests conducted to determine the emission
characteristics of a Babcock and Wilcox Circular burner and Dual Register burner
(DRB). The field tests were performed at two utility boilers, generally comparable
in design and size except for the burner equipment. The Circular burner was eval-
uated at Unit 2 of the Colorado Public Services Comanche Generating Station, and
the DRB was evaluated at Unit 1 of the Wyodak Generating Station of the Pacific Po-
wer and Light Company and the Black Hills Power and Light Company. Of particular
interest was the development of NOx amission correlations for the performance of
Circular burners and lPRBs /Under boiler conditions which could be used in inter-
. preting individual burner! tests in a subscale burner test facility. The field tests
were conducted with both boilers operating at nominal.full-load conditions. During
each test, boiler performance and operating conditions were monitored using plant
equipment, while gaseous emissions of NOx, 02, CO, S02, and C02 were contin-
uously monitored using a mobile test trailer .^fT.he nominal NOx emissions with the
Circular burner at Comanche were 550 ppm at 0'pb G2. Full-load NOx emissions at
Wyodak with all mills in service were 395 ppm at 0% 02.' Operation over a harrow /
excess 02 range precluded establishing NOx emission as a function of excess <02.
17,
KEY WORDS AND DOCUMENT ANALYSIS

a. DESCRIPTORS
b.IDENTIFIERS/OPEN ENDED TERMS
c. COSATI Field/Gioup
Pollution Nitrogen Oxides
Coal Electric Utilities
Combustion
Field Tests
Evaluation
Burners
Pollution Control
Stationary Sources
Circular Burners
Dual Register Burners
13	B 07B
21D
2 IB
14	B
14G
13 A
13. DISTRIBUTION STATEMENT

19. SECURITY CLASS (This Report)'
Unclassified
21. NO.„OF.PAGES
I 251 j
Release to Public

20. SECURITY CLASS (This page)
Unclassified
22. PRICE
EPA Fsrm 2220-1 (8-731
r
I" '. ¦ I
i

-------
NOTICE
This document has been reviewed in accordance with
U.S. Environmental Protection Agency policy and
approved for publication. Mention of trade names
or commercial products does not constitute endorse-
ment or recommendation for use.

-------
ABSTRACT
This report describes the results of field tests conducted to determine
the emission characteristics of B&W circular and dual register burners. The
field tests were performed at two different utility boilers, generally
comparable in design and size except for the burner equipment. The BIW
circular burner was evaluated at Unit 2 of the Colorado Public Services
Comanche Generating Station and the B&W dual register burner was evaluated at
Unit 1 of the Wyodak Generating Station of the Pacific Power and Light
Company and the Black Hills Power and Light Company. Of particular interest
was the development of N0X emission correlations for the performance of
circular and dual register burners under boiler conditions which could be
used in interpretation of individual burner tests in a subscale burner test
facility. The field tests were conducted with both boilers operating at
nominal full-load conditions. During each test, boiler performance and
operating conditions were monitored using plant equipment, while gaseous
emissions of NQX, O2, CO, SO2, and CO2 were continuously monitored using a
mobile test trailer. The nominal N0X emissions with the circular burner at
Comanche were 550 ppm at 0 percent O2• Full-load N0X emissions at Wyodak
with all mills in service were 395 ppm at 0 percent O2.
Since both boilers were operated over a narrow excess O2 range, the data
were not sufficient to establish N0X emission as a function of excess 02«
However, the data from both boilers do show a strong dependence of N0X on
both boiler load and firing configuration.
This work was carried out by Energy and Environmental Research
Corporation under EPA Contract 68-02-3130, through Babcock and Wilcox
Subcontract 940962 NR.

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TABLE OF CONTENTS
Section	Page
ABSTRACT		ii
1.0 INTRODUCTION. 				1-1
2.0 SUMMARY					2-1
3.0 BOILER DESCRIPTIONS AND TEST PLAN	3-1
3.1	Description of Comanche Unit 2 .... 			 3-1
3.2	Description of Wyodak Unit 1			3-5
3.3	Test Plan	3-12
4.0 TEST RESULTS			4-1
4.1	Results at Comanche Unit 2	4-1
4.2	Results at Wyodak			4-8
5.0 REFERENCE			5-1
APPENDICES
A.	TEST PROCEDURES. 						A-l
B.	QUALITY ASSURANCE.			B-l
C.	TEST DATA		 			C-l
C—1 Comanche Gaseous Emissions Data ...... 	 C-2
C-2 Comanche Boiler Operating Data 	 C-34
C-3 Wyodak Gaseous Emissions Data 	 C-80
C-4 Wyodak Plant Boiler Logs				 C-94
C-5 Wyodak Coal and Ash Analysis 		C-112
C-6 Wyodak Furnace Gas Temperature Data 	 .... C-122
J Preceding Page Blank
^

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LIST OF FIGURES
Figure	Page
2-1	NOx emissions vs. boiler load		2-4
3-1	B&W Circular Burner		3-3
3-2 Comanche Unit 2 burner settings 	 ...........	3-4
3-3 General arrangement of Wyodak Unit 1 	 ..... 3-6
3-4 Babcock & Wilcox dual register burner 			3-8
3-5	Wyodak Unit 1 burner arrangement		 .	3-10
, 3-6 Field test plan 		3-13
4-1	Daily averages of gaseous emissions—Comanche Unit 2 .....	4-2
4-2 N0X and CO vs. load - Comanche Unit 2			4-4
4-3	Comanche Unit 2 - N0X and CO vs. excess at a
load of 253-273 MWe . . 				4-6
4-4 Comanche gas stratification test ...... 	 ....	4-7
4-5	Effect of overfire air port damper position on
emissions - Comanche					4-9
4-6 Stratification test results at economizer outlet 	 . .	4-11
4-8 Correlation of NQX emissions with load 		4-18
4-9 Wyodak furnace gas temperatures			4-22
A-l Air heater inlet continuous monitoring system 	 .	A-3
A-2	Internal construction of water-cooled suction pyrometer
probes 					 .	A-6
A-3 Suction pyrometer tip construction 	 .....	A-7
B-l EPA EMSL coal audit sulfur analysis				B-6
B-2 EPA coal audit ash analysis			B-7
B-3 EPA EMSL coal audit heating value analysis			B-8

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LIST OF TABLES
Table Page
2-1 Boiler Descriptions . 	 ........ 	 2-2
2-2	Burner Operating Characteristics. 	 . 	 2-3
3-1	Comanche Plant Unit 2 Boiler Specifications ..... 	 , 3-2
3-2 Wyodak Plant Unit 1 Boiler Specifications 	 ..... 3-7
3-3	Wyodak Unit 1 Burner Settings 		3-11
4-1	Average Emissions at Comanche Unit 2 December 7-12, 1984. .... 4-3
4-2 Summary of Stratification at Economizer Outlet. 	 .	4-12
4-3 Average Emissions at Wyodak Unit 1 January 31 -
February 14, 1985 				4-14
4-4 Comparison of NO Measured by Continuous Monitoring System
and EPA Method 7 Samples at Economizer Outlet ..........	4-16
4-9 Effect of Sootblowing 						4-23
A-l Continuous Gas Analyzers—Air Heater Inlet			A-4
A-2 Coal and Ash Analyses 					 A-8
B-l Continuous Monitors Relative Accuracy Calculation 12-11-84
Comanche. ............. 	 B-3
B-2 Continuous Monitors Relative Accuracy Calculation
Wyodak 2-4-85 ........ 	 . 	 B-4

vn

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1.0	INTRODUCTION
Field evaluations to determine the emission characteristics of Babcock &
Wilcox (B&W) circular and dual register burners were conducted by Energy and
Environmental Research {EER) Corporation. These evaluations were part of a
burner development program conducted by B&W and EER for the U.S. EPA. This
burner development program involved the integration of the EPA distributed
mixing burner concept with commercial B&W hardware. The performance and
emissions of the distributed mixing burner were evaluated in the Large
Watertube Simulator, a full-scale burner test facility. B&W circular and
dual register burners were also evaluated in the LWS. The objective of the
field evaluation was to develop a correlation between the test results of the
circular and dual register burners in the LWS and in the utility boilers.
This correlation could then be used to extrapolate the performance and
emissions of the di stri buted mixing burner to a 1 arge scale utility
application.
Field testing was conducted at two boilers, one equipped with the
circular burner and one with the dual register burner. The boilers were
selected by B&W to be comparable in terms of age, capacity, coal
characteristics, and firing configuration. The circular burner was evaluated
at the Colorado Public Service Comanche Generating Station, Unit 2 located in
Pueblo, Colorado. The dual register burner was tested at the Wyodak
Generating Station, Gillette, Wyoming, owned by Pacific Power and Light
Company and the Black Hills Power and Light Company. Testing was conducted
for one week at Comanche in December 1984 and for two weeks at Wyodak in
February 1985.
Section 2.0 presents a summary of the field test results. The boilers
and test plan are described in Section 3.0. Detailed results are included in
Section 4.0. The appendices include test procedures, data, and quality
assurance.
1-1

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2.0 , SUMMARY
Table 2-1 shows the characteristics of the two boilers tested. Both
boilers fire subbi tumi nous coal and use a front and rear wall firing
configuration. The front and rear wall burners at the Comanche boiler are
directly opposed with four rows of four burners each. The front and rear
wall burners at Wyodak are offset to avoid flame interactions and are
arranged in five rows of three burners each. The boilers have comparable
furnace cross-sectional dimensions, but the Wyodak boiler has a taller
furnace to accommodate the five burner rows. Thus, the Wyodak furnace has a
lower ratio of firing rate to cooled surface area (HA/SC).
During testing, the boilers were generally operated in a normal fashion
by the operators without interference from EER. Thus, the burner settings,
load, and excess air were controlled by plant personnel. The overfire air
N0X ports were closed during the day at the Comanche boiler at the request of
EER, and returned to their normal open position of 18 percent at night.
Table 2-2 shows the typical burner settings and flame characteristics during
the tests. Both the circular and dual register burners operated
satisfactorily during the tests. Exact flame lengths could not be determined
with the available observation ports. Both burners showed a high combustion
efficiency and large imbalances of fuel or air distribution were not
observed.
Both boilers operated over a narrow excess 02 range, 2.5 to 3.5 percent
at Comanche and 3.8 to 4.0 percent at Wyodak. Thus, the data were not
sufficient to establish NQX emissions as a function of excess 02- Figure 2-1
shows N0X emissions at the two boilers as a function of load. Both
correlations show a similar slope, with lower emissions for the dual register
burner at Wyodak. Nominal N0X emissions with the circular burner at Comanche
were 550 ppm at 0 percent O2 (0.64 lbs/106 Btu). Full load emissions at
Wyodak with all mills in service were 395 ppm at 0 percent 02 (0.46 lbs/10®
Btu). More detailed test data are presented in Section 4.0.
2-1

-------
TABLE 2-1. BOILER DESCRIPTIONS
1 UNIT
COMANCHE UNIT 2
WYODAK UNIT 1
UTILITY
COLORADO PUBLIC SERVICE
PACIFIC POWER & LIGHT
BLACK HILLS POWER & LIGHT
BOILER MANUFACTURER
B&W
B&W
YEAR OF INITIAL OPERATION
1976
1978
GROSS GENERATING CAPACITY
35d MWe *
350 MWe
TYPE OF BURNER
B&W CIRCULAR
B&W DUAL REGISTER
NO. OF BURNERS
32
30
NO. OF MILLS

5
BURNER ARRANGEMENT
W x 4H ON
FRONT & REAR WALLS
3W x 5H ON
FRONT & REAR WALLS
FURNACE DIMENSIONS
43'W x 45'D x 161'H
46'W x 15'D x 180'H
COAL TYPE
SUB BITUMINOUS
SUB BITUMINOUS
ADDITIONAL FEATURES
8 NOx PORTS
SEALED N0X PORTS
OPPOSING BURNERS OFFSET
COMPARTMENTED WINDBOXES

-------
TABLE 2-2. BURNER OPERATING CHARACTERISTICS
UNIT
COMANCHE
WYODAK
BURNER TYPE
CIRCULAR
DUAL REGISTER
TYPICAL BURNER
SETTINGS
BOTTOM BURNERS-REGISTERS 50% OPEN
TOP BURNERS -REGISTERS 100% OPEN
OUTER REGISTERS 50% 'OPEN
INNER REGISTERS 25-50% OPEN
SWIRL VANES 45% OPEN
FLAME CHARACTERISTICS
LONG AND NARROW
0-2 FT STANDOFF
LONG AND NARROW
35 - 44 FT LONG
0.5-3 FT STANDOFF

-------
Load MWe
Figure 2-1. NO^ emissions vs. boiler load.

-------
3.0
BOILER DESCRIPTIONS AND TEST PLAN
Characteristics of the Comanche boiler are included in Section 3.1. The
Wyodak boiler is described in Section 3.2. The Test Plan for the evaluation
of both boilers is described in Section 3.3.
3.1	Description of Comanche Unit 2
Comanche Unit 2 is a horizontally opposed wall fired balanced draft
utility boiler manufactured by Babcock & Wilcox. The boiler is located via
Pueblo, Colorado and is operated by Public Service Company of Colorado. It
has a maximum continuous operating capacity of 350 MWe with a steam flowrate
of 2.54 x 10® Ibs/hr at 1005°F and 2500 psig from the superheater. The
reheater outlet temperature and pressure are 1005°F and 555 psig. The boiler
fi res a subbi tuminous coal with a higher heating value of 8400 Btu/lb and a
moi sture content of 31 percent by weight as recei ved. The coal sulfur
content is approximately 0.4 percent by weight as received. The
characteristics of the boiler are summarized in Table 3-1.
The coal for the boiler is ground in four pulverizers designated A, B, C
and D. Each mill feeds eight burners. The burners are arranged in four rows
of four burners each on two boiler walls. The unit is equipped with eight
overfire air ports for N0X control. A single port is located over each of
the top row burners. Secondary air is fed through three compartmentalized
windboxes. One windbox feeds all the burners located in the lower two rows.
Another feeds all burners in the upper two rows and a third windbox feeds all
of the overfire air ports.
The burners used on the unit are B&W high turbulence circular burners.
These are the standard burners used on B&W pre-NSPS (New Source Performance
Standards) units. Figure 3-1 shows the circular burner. Coal is supplied
through a central coal nozzle. The coal is dispersed into the furnace by an
impeller on the end of the coal nozzle. Secondary air flowrate and swirl to
each burner are controlled by a single register. Figure 3-2 shows the burner
settings during testing. These settings are normally not changed. Burners
3-1

-------
/ ;•
TABLE 3-1. COMANCHE PLANT UNIT 2 BOILER SPECIFICATIONS
I

Manufacturer
Babcock & Wilcox
Year in Commercial Operation
1971
Gross Electrical Capacity
350 MWe
Fuel
Pulverized Coal Subbituminous
Burners

Type
B&W Circular
Number
32
Configuration
Horizontal, Opposed-Fired
Array
4 Rows of 4 Burners
on Front and Rear Walls
Number of Pulverizers
4
Furnace Dimensions

Width
43 ft
Depth
45 ft
Height
174 ft
Design Efficiency
84.57% at Maximum
Continuous Rating
Steam F1owrate
2,540,000 Ib/hr at

Maximum Continuous

Rating
Steam Pressure
2500 psig
Superheat Temperature
1005°F
Reheat Temperature
1005°F
HA/SC

Design
384 x 103 Btu/hr-ft2
Fiel d
i
400 x 103 Btu/hr-ft2
3!
-2

-------

-------
s.,-1 % % %
Register Setting; 17	17	18	18
0 = Closed
18 = Open
fa fa fa
18
%

17
18
-------
on both the front and rear wall are operated with clockwise swirl, as viewed
looking at the burners, resulting in opposite rotation. The boiler is
normally operated with the N0X ports open 18 percent to provide tempering air
in order to prevent superheater fouling. During this test, the ports were
closed during the day, but opened during the night.
3.2	Description of Wyodak Unit 1
Wyodak Unit 1 is a radiant reheat boiler manufactured by the Babcock and
Wilcox Company (B&W). The plant is located near Gillette, Wyoming, and is
owned by Pacific Power & Light Company and Black Hill Power & Light Company.
Commercial operation of the plant began in 1978. The plant has a rated
capacity of 330 MWe with a steam flowrate of 2,600,000 Ib/hr at 1800 psig and
1000°F. The boiler is equipped with two superheater banks, a pendant
reheater, economizer, and regenerative air heater. A diagram of the boiler
is shown in Figure 3-3 with key boiler specifications listed in Table 3-2.
f
The boiler fuel is pulverized subbituminous coal supplied from a mine
near the plant. The coal has an average higher heating value of 8000 Btu/lb
with 30 percent moisture and 8 percent ash. The sulfur content of the coal
is consistently low at about 0.7 percent by weight.
The boiler is equipped with B&W's dual register burner compartmentalized
windbox firing system. This firing system was developed by B&W to control
fuel and air mixing in the burner zone, thus reducing NCX emissions and
enhancing complete combustion. The dual register burner (ORB), shown in
Figure 3-4, consists of a central coal nozzle surrounded by two concentric
secondary air passages. The coal nozzle incorporates a venturi to promote a
uniform coal distribution. The venturi plug shown in Figure 3-4, had been f J ~
removed about one year prior to this test program at the Wyodak plant. The
absence of this plug has apparently not compromised burner performance. Air
flow distribution between the two secondary air passages and swirl generation
is controlled by three devices: outer secondary air register, inner
secondary air register, and inner secondary air axial spin vanes. The
multiple air passages and the associated controls allow variation in the rate
3-5
-------
A> A
uttit} rim
Figure 3-3. General arrangement of Wyodak Unit 1.
3-6
-------
TABLE 3-2. WYODAK PLANT UNIT 1 BOILER SPECIFICATIONS
r •
Manufacturer
Babcock & Wilcox
Year in Commercial Operation
1978
Gross Electrical Capacity
350 MWe
Fuel
Pulverized Coal, Wyoming Sub-
bituminous
Burners

Type
B&W Dual Register
Number
30
Configuration
Horizontal, Opposed-Fired
Array
5 Rows of 3 Burners
on Front and Rear Walls
Number of Pulverizers
5
Furnace Dimensions .

Width
46 ft
Depth
45 ft
Height
180 ft
Design Efficiency
83.921 at Maximum
Continuous Rating
Steam Flowrate
2,600,000 lb/hr at
Maximum Continuous
Rating
Steam Pressure
1800 psig
Superheat Temperature
1000°F
Reheat Temperature
1Q00OF
HA/SC

Design (5 mills)
387 x 103 Btu/hr-ft2 j
Field
330 x 103 Btu/hr-ft2 j
3'
'1
-7
-------
Figure 3-4. Babcock & Wilcox dual register burner.
-------
of fuel and air mixing, thereby controlling N0X emissions. The compartmented
windbox separately controls the combustion air flow for the group of burners
associated with each pulverizer. The compartmented windbox thus permits
balancing the secondary air to each burner group in operation.
Wyodak Unit 1 has 30 dual register, burners arranged in a horizontally
opposed firing configuration, as shown in Figure 3-5. The 30 burners are
arranged in five rows of three burners on both the front and rear walls.
Opposing burners are offset avoiding direct flame tail interaction and
promoting uniform heat release across the lower furnace. In addition, the
top row of burners on both walls, supplied by D mill, is spaced 12 feet above
the lower four rows of burners.
During this two-week test period, no adjustments were made to the burner
controls. The settings for each burner maintained during this test period
are listed in Table 3-3. Each register control had 18 divisions, with
notch 1 representing closed and notch 19 representing open. Thus, each
division for the registers represents approximately five degrees of motion.
The spin controls also have 18 notches, but there is a 2:1 gear ratio that
permits 180° of travel; i.e., 0 to 90°CW and 0 to 90°CCW. It is general
practice on this unit to have the spin vanes always in the same direction as
the outer register.
The predominant firing configuration for full load operation at Wyodak
during this test was with D mill and the associated top row of burners out of
service and all the other mills and burners in service. When a mill is taken
out of service, the air flow to the idle burners is reduced to provide only
flow to cool the burner components. With D mill out of service, the windbox
compartment for burners D1-D6 is closed so that only about 10 percent of the
total secondary air is supplied for cooling. The other additional
configuration had C mill, which supplies burners C1-C6, out of service.
These three cases allowed evaluation of the effect of firing pattern on
boiler performance and emissions.
-------
-/)

-7 - -
*%, . *0
7e$\
' io;
K?s

0

-c^
Figure 3-5. Wyodak Unit 1 burner arrangement,
,3-10
-------
TABLE. 3-!3> WYODAK UNIT 1 BURNER SETTINGS
Front-Wall
Rear Wall
Burner
Outer
Register
Inner
Register
Spin
Vanes*
Burner
Outer .
Regi ster
Inner
Register*
Spin,
Vanes'*
B1
7
B2
9
B3
7
B4
7
B5
8
B6
7
€1
9
C2
8
C3
9
C4
5
C5
5
C6
9
D1
10
02
9
D3
9
6
10
10
9
10
11
10
.10
10
10
10
11
2
4
3
3
3
3
,A1
A2
A3
A4
A5
A6
El
E2
E3
E4
E5
E6 :
04
D5
D6
9
10
9
9
9
8
9
10
10
10
10
11
10
10
10
9
10
10
9
10
10
3.
7
' 5
4
4
; 4
4
4
5
3
5
^Notches Open--:
-------
3.3	Test Plan
The field evaluations consisted of monitoring boiler performance for one
week at the Comanche boiler and for two weeks at the Wyodak boiler. Testing
at Comanche was reduced because additional data was available from previous
testing by Exxon (Reference 1) for the EPA in 1977. During tests at both
boilers, boiler operating conditions were established by the boiler
operators.
Figure 3-6 shows the field test plan for both boilers. Boiler operating
condi tions and performance were monitored using plant instrumentation.
Gaseous emissions of N0X> Og, CO, SO2, and CO2 were continuously monitored
using a mobile test trailer. Sampling was performed at both boilers using an
array of probes located at the air heater inlet. Coal and ash samples were
collected from selected points throughout the boiler for analysis.
Burner performance was assessed using observations of flame
characteristics and evaluation of combustion efficiency as determined from
ash analyses and CO emissions. The relative fuel/air balance to the burners
was assessed by gas stratification measurements obtained at the air heater
inlet. In addition, furnace gas temperatures were measured at Wyodak using a
water-cooled suction pyrometer. Detailed descriptions of the test procedures
are included in Appendix A.
3-12
-------
1.0 BOILER DATA FROM PLANT INSTRUMENTATION
•	FUEL FLOWRATE
•	STEAM QUALITY AND FLOWRATE
•	WATER/STEAM TEMPERATURES AND PRESSURES
•	AIR/FLUE GAS TEMPERATURES AND PRESSURES
•	BOILER LOAD CYCLE
•	RANGE OF BURNER OPERATING CONDITIONS
2.0 EXHAUST GAS MEASUREMENTS BY EER
•	CONTINUOUS MONITORING OF NO. CO, C0?, 0?,
SO2 AT AIR HEATER INLET X	L c
•	PERIODIC ANALYSIS OF COAL AND ASH COMPOSITION
COAL FEED
FLY ASH AT AIR HEATER INLET
BOTTOM ASH
PARTICULATE COLLECTOR HOPPER
3.0 BURNER/BOILER PERFORMANCE
•	FLAME OBSERVATIONS
•	COMBUSTION EFFICIENCY FROM COAL AND FLUE
GAS MEASUREMENTS
•	FURNACE GAS TEMPERATURE WITH WATER-COOLED
PROBE AT WYODAK
Figure 3-6. Field test plan.
3-13'
-------
4.0
TEST RESULTS
4.1	Results at Comanche Unit 2
Emissions testing of the B&W circular burner was conducted by EER at
Comanche Unit 2 from December 7 through December 12, 1984. Gaseous emissions
of N0X, 02» CO, SO2, and CO2 were continuously monitored during this period.
The plant was operated in response to system demand. The N0X overfire air
ports are normally partially open. At the request of EER, the ports were
closed during the day, but opened at night. Otherwise the boiler operating
condi tions were established by the plant operators. Emissions were measured
at this unit by Exxon in 1977 as part of another EPA program. Exxon's
results are compared to the results of the current test program.
During the week of testing, boiler load varied from 150 to 360 MW. The
trends for the daily averages of gaseous emissions and boiler load are shown ^
in Figure 4-1. The overall averages are summarized in Table 4-1. During a i
portion of the testing the boiler was operated with mill A out of service.
The A mill supplies coal to the upper two burner rows on the front wall.
Excess O2 varied from only 2.5 to 3.5 percent Og. A brief series of tests
was performed at 300 MW to assess the impact of the N0X overfire air ports on
N0X emissions.
N0X and CO emissions as a function of boiler load are presented in
Figure 4-2. N0X emissions wi th all mills on and the overfire air ports '
closed showed the following correlation:
N0X (ppm @ Q% 02) = (1.136)(Load, MW) + 1487?
Nominal N0X emissions at full load of 360 MW were 550 ppm § 0 percent O2.
corresponding to 0.64 lbs/10® Btu. These emissions are substantially lower
than the N0X measured by Exxon of 847 ppm @ 0 percent O2 (0.99 lbs/106 Btu).
The Exxon data were obtained at a higher excess O2 level, 5.2 percent
compared to 2.7 percent, however. Operation with the A mill out of service
resulted in a slight decrease in N0X emissions. This result could be due to
4-1
-------
j DUU
i 400
: 300
i 200
; 100
i 0
500
400
300
4
3
2
400
350
300;
250
200
l
\	

*=		
J	L.
10 11
12
AVG
SD
368
51.73
AVG
SD
19.32
0.16
233/2
89.8
385.5
44.4
3.15
0.27
|AVG ;=.-275.2 ,
! SD T 32^7, "
DEC
4-1. Daily averages of gaseous emissions--Cornanche Unit 2.
~4-2~
-------
TABLE 4-1. AVERAGE EMISSIONS AT COMANCHE UNIT 2
DECEMBER 7-12, 1984
Species
Average Concentration
Measured
0 0% 02
lb/106 Btu
°2
3.15%
__
—
NOx
328 ppm
386 ppm
0.45
so2
313 ppm
368 ppm
—
CO
198 ppm
233 ppm
—
C02
16,4%,
19.3%
—

	— i
4-3
-------
——I	1	1	1	r
~ Mill 2A OOS ON, OFA CLOSED 3.1 - 3.4%0
800
700
600
O All Mills ON, OFA CLOSED 2.5 - 2.7% 0;
O All Mills ON, OFA CLOSED 3.2-3.4%^ u2
"A Exxon-NO OFA 5.2%02 5.6%02
~ All Mills ON, OFA CLOSED 3.5-4.0% 0
E
CL
CL
500
i
"i
>>
i-
o
CM
O
O
400
300
200
100
_L
I
±
±
60 120 180 240
Load MW
Figure 4-2.
300 360
NO and CO vs
X
350 -
300 -
S 250
>>
j-
™ 200
x
o
S 150
100 -
50 -
60 120
180 240
Load MW
300 360
load - Comanche Unit 2.
-------
a decrease in the ratio of firing rate to cooled surface area or to a degree
of combustion staging. Here, combustion staging refers to operation with the
burner zone at a lower stoichiometry and with the addition of combustion air
above the burner zone. The latter conclusion is supported by the measured CO
emissions and by the operating excess air level. With all coal mills (and
burners) in service, combustion efficiency was typical ly high, as indicated
by low CO emissions in the range of 50 to 60 ppm. However, operation with
the A mill out of service resulted in increased CO emissions of up to
500 ppm. Increased CO emissions would be consistent with a decrease in
combustion efficiency due to relatively poor fuel /air mixing that could be
associated with a degree of combustion staging occurring with the A mil 1 off.
In addition, the boiler operating excess air level was generally not
increased when the A mill was taken out of service. Since the idle burners
would need to be supplied with cooling air, operation at a constant excess
air level would result in a lower burner zone stoichiometry with the A mill
out of service, resulting in a degree of combustion staging.
Figure 4-3 shows N0X and CO emissions vs. excess 02 at a constant load
of 253 to 273 MW. In' general , the data taken during the current test do not
have enough variation in O2 level to indicate a trend. However, comparing
the current data with the previous Exxon data would suggest a strong
dependence of N0X on excess O2 • This is typically the case with
subbituminous coals as indicated in LWS tests.
Exhaust gas composition was measured using an array of 12 probes in the
two exhaust ducts upstream of the air heater. "Hie gas compositions at each
sampling location were measured on December 10 and 11, 1984 to determine gas
stratification. In wall-fired boilers, gas stratification measurements
upstream of the air heater can typically be used to evaluate the side to side
balance of fuel and air to the burners. Figure 4-4 shows the results of the
stratification measurements at Comanche. Although some variation in O2 and
CO levels is evident, no consistent imbalance between the two ducts or within
each duct can be seen from these data. Thus, adjustment of the burners to
improve the air/fuel, balance would be expected to result in only a minor
improvement in combustion performance.
-------
I
CTl
800
700
600
— 500
£?
¦o
O Mi Tl 2A 00S" - 261-273 MW-OFA" Open 1
. Q Mill 2A 00S - 257-267 MW-OFA Closed
O All Mills On - 252-269 MW-OFA Closed
A Exxon Data - All Mills On, OFA Closed 275MW
A
400
o
S* 300
200
100


Q
CP
excess 0,,,%
-S
Figure 4T3?r Comanche Unit 2 - NO and CO vs. excess 09 at a load of 253-273 MW
A	L	C
-------
12-10-84
A
of
b
'ppm
ppm-




3.29
4.59
2.89

5.24
4.74
2.49
504
480
350

379
400
306
36
77
186

94
129
-
2.99
3.26
3.74


^ ¦ 4
3:74"
478
420
335

iff-
'? 1340 :•
35
59
416

187;! (
> 228? ?./.
'122] ; /

Avg 02 3.46 ri



Avg 02 3.61%

12-11
<
00
1



B

3.73
2.67
4.72

2.00
1.92
2.52
517
476
451

475
473
426
84
91
102

43
43
56
4.12
2.57
3.55

4.02
2.17
2.87
454
479
457

483
446
417
49
45
42

48
145
57
Avg 02 3.561
i
i
|
I
Avg 02 2.58%

Figure 4-4. Comanche gas stratification test.
-------
Figure 4-5 shows the effect of opening the overfire air ports on N0X and
CO emissions. Opening the ports resulted in a substantial decrease in N0X
emissions. This trend is similar to that seen during the Exxon testing,
except that no decrease in N0X was observed until the ports were opened more
than 30 percent. Evidently the back lash in the mechanical linkage resulted
in the ports not actually opening until the indicator was past 30 percent.
Thus, although the plant normally operates with the ports 18 percent open,
they may actually be closed.
Unlike the results seen during the Exxon tests, however, opening the
overfi re air ports resulted in a large increase in CO emissions, to over
800 ppm at the maximum opening, indicating a substantial decrease in
combustion efficiency.
4.2	Results at Wyodak
Emissions and boiler performance were monitored at the Wyodak plant from
January 31 to February 14, 1985. During this test period, the unit was
operated based on normal practice following system demand. The boiler was
essentially base loaded through the test program with only brief load
variations. A short boiler outage occurred between February 7 and 10, for
necessary boiler repairs.
The primary objective of the test program was to characterize the
performance of B&W Dual Register Burners in a typical utility boiler. The
burner performance was determined based on CO emissions, flame
character!"sties, and efficiency. Emissions measured included continuous
moni toring of N0X, CO, O2, CO2 and SO2* Visual observations were made
through available inspection ports to determine flame characteristics to the
extent possible. Combustion efficiency was determined by analysis of
unburned carbon content in fly ash samples and measurement of CO emissions.
In addition, the overall boiler efficiency was determined based on
calculation of the heat rate during the test period.
-------
OFA Ports (% Open)	(OFA Ports (% Open)
Figure 4-'5. Effect of overfire air port damper position on" emissions- Comanche.
-------
4.2.1 Emissions
Emissions were monitored at the economizer outlet of Wyodak Unit 1. The
gaseous species monitored included O2, CO, COg. N0X and SO2.
A continuous emissions monitoring system was used to measure the gaseous
species with an array of eight probes. Four probes were placed in each of
the two ducts leading from the economizer to the air heater to ensure a
representative sample. The gas sample flow rate was balanced to provide an
equal sampling rate through each of the eight probes. In addition, each of
the probes was monitored individually at a typical operating condition during
the test period to determine the presence and extent of stratification of the
gas stream. The gas stratification test was conducted on February 6 between
9:30 to 11:00 AM with the unit running at 360 MWe gross output and with D
mill out of service. The results of this test are shown in Figure 4-6 and
summarized in Table 4-6. The concentration profiles of 0?, N0X, and CO shown
in Figure 4-5, indicate that the gas concentrations are slightly higher in
the west duct. Previous tests at other boilers have shown that burner-to-
burner imbalances in fuel or air flow result in non-uniform gas
concentrations across the width of the boiler. Thus, slight burner-to-burner
flow imbalances may account for the differences measured during the
stratification test.
Averaged concentrations for the two ducts are compared with gas
concentrations from balanced sampling with all . probes before and after the
individual probe stratification test in Table 4-2. Again, the O2
concentration in the west duct was siightly higher than measured in the east
duct. Associated with the higher oxygen concentration in the west duct are
higher N0X emissions. This is an indication that careful control of excess
air and proper balances of fuel and air, from burner to burner is beneficial
in reducing overall N0X emissions. Differences between averaged
concentrations from the two ducts and balanced probe sampling are about
5 percent, which is within the fluctuations typical of normal boil er
operation.
; 4-10:
-------
West Duct
East Duct
o2 <*)
N0X (ppm)
Measured -•
(0 0% o2l—
271
263
(344)
(333)
267
279
(335)
(365)
4.48
4.43
4.28
4.97
271
254
(334)
(300)
267
244
(342)
(300)
3.98
3.23
4.64
3.96
CO (ppm)


Measured
33
35
{% 0% o2) —
(41)
(45)

58
40

(73)
(52)
35
34
(43)
(40)
29
31
(37)
(38)
Figure 4-6. Stratification test results at economizer outlet.
f 4-11
-------
TABLE 4-2. SUMMARY OF STRATIFICATION AT ECONOMIZER OUTLET
Sample
?2.
>)
NOx
(ppm ® Of O2 3
CO
[ppm 0 0% O2)
Average West Duct
Average East Duct
Average Both Ducts
All Probes Balanced
4.54
3.95
'4.24
4.03
344
319
331
318
53
40
46
51


-------
Hourly averages of the gaseous emissions were calculated from the
continuous monitoring data. These hourly averages are tabulated in
Appendix C-3. The hourly averages were used to calculate daily and overall
averages for the test period. The overall averages of measured gas
concentration for the test period are summarized in Table 4-3. These values
represent essentially base-loaded operation, with only about four hours of
reduced load operation during the test period. The N0X emission rate of
0.40 lb/10® Btu is below the Federal New Source Performance Standard of
0.5 lb/106 Btu for subbituminous coal-fired boilers.
The trends for the daily averages of gaseous emissions and boiler load
are shown in Figure 4-7. A short boiler outage occurred between February 7
and 10 during which time no emissions data was collected. The plant load
it"
averaged 358 MWe during the test period when in operation, with only 1 J-
1 percent relative deviation. Close control was maintained on the operating
excess air level, indicated by 2.5 percent deviation from the average of
4.03 percent O2 measured in the flue gas. CO emissions were low throughout
the test period and averaged about 51 ppm. The variations in CO measured at
this low level are generally considered to be insignificant. The CO2 and SO2
emissions, which are directly related to the coal composition, also showed
variations that were generally small.
Gaseous emissions, including N0X emissions, were monitored primarily
with continuous analyzers. In addition, N0X emissions were measured
following ERA Method 7 procedures on one day during the test period to verify
the accuracy of the continuous monitors. The results of the EPA Method 7
sampling are summarized in Table 4-4 with details included in Appendix B:
Quality Assurance. The discrete Method 7 samples are compared with the
continuous monitor responses in the table. Each Method 7 value represents a
set of three discrete samples while the continuous monitor value is time
averaged during the Method 7 sampling period. The agreement between the two
measurement techniques is good. The continuous monitors were within about
13.7 percent, including 95 percent confidence interval, of the EPA standard
method.
4—13
-------
TABLE 4-;3^ AVERAGE EMISSIONS AT WYODAK UNIT 1
v' JANUARY 31 - FEBRUARY 14, 1985
'



Average Concentration


Species
Measured
@ 01 02
lb/10® Btu


°2
4,03%
__
—


NOx
278 ppm
344 ppm
0.40


SO 2
584 ppm
723 ppm
1.17


CO
42 ppm
52 ppm
0.03


C02
15.7% '
19.4%
216.7

4-14
-------
Boiler
Outage
so2
5 0% 02
(ppm)
CO2
0 0% 0^
(ppm)
CO
9 0% 0-
(ppm)
N0X
@ OS 0,
(ppm)
(2i
Boiler
'Load;
(MWe)
1200
1100
900
700
500
300
20
19
18
100
80
60
40
20
0
400
300
200
5
—1	1— T
—1	1	
n	1	1—
—1	T —r
T		t	








AVG = 723




•rr*
-
SD = 153
	1	i	1	
_i	1	
1 1 1
1 1 JL.
1 1
¦

400
380
360
340
320
300
1	r
t
Jk
T
wMm
	
i	)	1	1	1	r

IJSLSLJSiiiiSS^
JL
_1_
_1_

_1_
31
JAN
6
FEB
AVG = 19.35
SD = 0.12
AVG = 51.5
SD = 13.3
AVG
SD
344.5
22.6
AVG
SD
4.03
0.10
AVG
SD
358.1
5.3
10 11 12 13 14
Figure 4-7. Daily averages of gaseous emissions.
;4-^5,
-------
TABLE 4-4:. COMPARISON OF NOx MEASURED BY CONTINUOUS
MONITORING SYSTEM AND EPA METHOD 7
SAMPLES AT ECONOMIZER OUTLET




Date
Time
/ NOv @ 0% 02, dry *

Method 7
CMS

2-4-85
1603
358
395


2-4-85
1612
368
397


2-4-85
1616
368
400


2-4-85
1623
357
405

-------
N0X emissions at Wyodak were sensitive to burner firing arrangement and
boiler Toad. These effects are shown in Figure 4-8. The data are averages
of hourly emissions for three firing configurations. The primary "
configuration at Wyodak has the D mill out of service. The D mill supplies
the top row of burners on both the front and rear walls. The two other
firing configurations were: (1) all mil 1s and burners in service and (2) "C"
mill out of service. The burners supplied by C mill are the second and third
rows from the top on the front wall.
Operation with the D mill out of service resulted in the lowest average
N0X emissions {344 ppm at nominal full-load operation), while operation with
all mills and burners in service resulted in the highest N0X emissions (395
ppm at nominal full-load operation). An intermediate level, of NOx emissions
was produced with the C mill out of service. These results are somewhat
surprising since operation with the D mill out of service produces the
highest HA/SC ratio. In general, the effects of the boiler firing
configuration on N0X emissions could be due to slight variations in the
burner operating stoichiometry (combustion staging) or to changes in the
burner flame length and, consequently, changes in the degree of flame
confinement and flame-to-flame interactions. Since the excess air level was
similar for operation with all mills in service and for operation with the C
mill out of service, the burners in the latter case could have been operating
at a slightly lower stoichiometry, resulting in a decrease in burner N0X
emissions. However, when the D mill was taken out of service, the boiler was
operated at a higher excess air level. This result is consistent with the
standard B&W practice of increasing the operating excess air level as a
result of supplying additional air to cool the idle burners. Therefore, it
is likely that the burners were operating at the design stoichiometry. Since
operation with the D mill out of service would have required the burner
throughput to increase, it is possible that the flame length could have
changed. As indicated by the results of the LWS burner studies, N0X
production from the dual register burners correlates directly with flame
length. In addition, variations in the boiler firing configuration and
burner flame length would be expected to influence the boiler flow patterns
and flame-to-flame interactions and could possibly account for the variations
S4-T7 i
-------
~ ALL MILLS IN SERVICE
A C MILL OUT OF SERVICE
O D MILL OUT OF SERVICE
ERROR BARS SHOW 95%
CONFIDENCE INTERNAL
0.50
0.45
0.40
NOx = 1.043(Load)-29.
0.35
Figure 4-'8. Correlation of N0X emissions with load.
0.30
0.25
200
250
300
Boiler Load (MW , Gross)
e
350
400
-------
i n N0X emissions. Although thi s analysis is simplistic, these results do
indicate the importance of burner arrangement and firing configuration on
burner performance.
Limited data were obtained at reduced loads with D mill out of service.
For typical coal-fired boilers, N0X increases with load due to increasing
combustion intensity and fuel/air mixing rates. As shown in Figure 4-8, N0X
emissions correlate essentially linearly with boiler load. Least square
linear regression yields the following correlation for operation with the D
mill out of service:
N0X (ppm @ 01 02) = 1.043 x Load (MWe) - 29.6,
while the correlation obtained for all data taken during the field test was:
N0X (ppm 0 0% 02) = 1.25 x Load {MWe) - 77.
These relationships only apply over the small range of excess air levels at
which the boiler operated during this field test.
4.2.2 Boiler Performance
Boiler performance during the field evaluation was monitored using the
plant instrumentation and measurements performed by EER. Boiler performance
parameters of interest included:
1.	Coal characteristics
2.	Mill performance
3.	Burner performance
•	Air/fuel mixing
•	Flame characteristics
•	Combustion efficiency
•	Burner pressure drop
4.	Boiler heat rate
5.	Furnace gas temperatures
The Wyodak plant is typically base loaded and operates almost continuously at
full load of about 360 MW gross. During the two week test period, the plant
4-19
-------
experienced no significant operating problems and operated at full load with
the following brief exceptions;
1.	Two day outage on February 8 and 9, 1985.
2.	Three hour outage on February 12, 1985 caused by an electrical
disturbance in the power distribution system unrelated to station
operation.
3.	Five hours of low load operation at 275 MW on February 13, 1985 at
the request of EER.
4.	Two hours of operation at 325 MW on February 14, 1985 at the
request of EER.
Wyodak uses Powder River Basin coal , which is mined locally. The coal has a
low sulfur content with approximately 30 percent moisture and a higher
heating value of 8000 Btu/lb. Coal moisture, ash, sulfur and heating value
are monitored daily by the station. These results and coal analyses by EER
are presented in Appendix C. With the exception, of sulfur content, coal
properties did not vary substantially during the test period. Coal sulfur
varied from about 0.3 to 0.7 percent, as received.
The boiler is equipped with five mills, but can operate at full load
with only four mills in operation. During the majority of the test period,
the plant operated with the D mill out of service. The D mil 1 supplies coal
to the top row of burners on both the front and rear walls. The boiler
operated with the C mill out of service during February 4 and 5, 1985 to
allow repairs on the C mill. The boiler also operated will all mills in
service during the brief periods while the C mill was taken offline and
brought back online. Mill performance was satisfactory during the test
period. Coal fineness test results provided by the station showed fineness
to vary from 68 to 85 percent less than 200 mesh. Detailed fineness results
are included in Appendix C.
-------
Burner performance with the dual register burners was satisfactory
throughout the test program. Air/fuel distribution between burners was
relatively uniform, as shown by flame observations and by variations in
excess O2 concentrations in the exhaust duct prior to the air heater. Flame
observations showed the flame shapes to be uniform and stable for all
burners. Exact flame length was difficult to evaluate due to the lack of
observation ports in the middle of the furnace side walls. Flame lengths
appeared to be relatively long, however, extending from 1/2 to 3/4 of the
distance across the furnace. The burners on the front and rear walls are
offset to minimize flame interactions.
Combustion efficiency was very high, as measured by carbon in the fly
ash and CO emissions. Carbon in the ash averaged 0.16 percent, corresponding
to a carbon utilization of 99.98 percent. Ash analyses are included in
Appendix C. Carbon monoxide emissions were stable, averaging less than
60 ppm.
Overall boiler performance and electrical generation efficiency were
measured in terms of the gross plant heat rate, the ratio of fuel heat input
to gross electrical production {Btu/kw hr). The average heat rate during the
test period was 10,236 Btu/kw hr compared to the design heat rate of 10,177
Btu/kw hr. Thus, overall boiler performance was satisfactory, with
efficiency very near to design conditions.
Upper furnace gas temperatures were measured during full load operation
using a water-cooled suction pyrometer. Figure 4-9 shows the range of
temperatures measured. The furnace exit temperature at the inlet to the
superheater pendants varied from 1120 to 1359°C. The temperatures at the
bottom portion of the superheater are above the ash fusion temperature of
about 1200°C, and thus some buildup of ash/slag deposits could be expected in
this region. However, fouling of the superheater tubes was not observed to
be a significant operational problem during testing. The impact of
sootblowing on furnace gas temperatures was evaluated during testing. The
results shown in Table 4-9 show sootblowing to have very little effect on gas
temperatures.
4-21
-------
Figure 4-9. Wyodak furnace gas temperatures.
; 4-|2
-------
TABLE 4-9. EFFECT OF SOOTBLOWING
Port
Distance
Into
Furnace
Temp.oc
Before
Blowlng
Temp.°C
After
Blowing
Sootblowing
Location
10W
9-1/2W
9-1/2W
9-1/2W
9-1/2W
9-1/2W
12'
16'
20'
12'
16'
20'
1120
1416
1384
1377
1324
1383
13541 ¦
1345 •
1402'
1120
1370
1351-62
1315-32
1370
1351-62
1315-32
Furnace
Front of Superheater
Front of Superheater
Front of Superheater
Air Heater
i 4-2 3
-------
5.0	REFERENCE
1. Manny, E, H. and A. R. Crawford. Control of Utility Boiler and Gas
Turbine Pollutant Emissions by Combustion Modification - Phase II.
EPA-600/7-81-039 (NTIS PB 81-222267), March 1981.
5-1
-------
APPENDIX A
TEST PROCEDURES

A-1
-------
Measurements performed by EER included the following;
Flue gas composition of N0X > Og, CO, SO2» and CO2 by continuous
monitors
•	Coal and ash composition
•	Furnace gas temperatures by suction pyrometer
Flue Gas Composition
The flue gas composition (N0X, CO, CO2, O2, and SO?) was monitored with
continuous analyzers at the inlet of the air heater. Figure A-l shows a /v /.
schematic diagram of the monitoring system at the air heater inlet. The gas
sample was obtained with eight sample probes. The gas sample flow rate from
each probe is controlled with a glass rotameter to ensure equal flows through
each probe. In addition, sampling can be conducted through one probe at a
time to determine stratification of the gas concentrations. All components
of the sample system upstream of the moisture condenser are heated. A
separate sample stream for the SO2 analyzer is dried with a Perma Pure drier.
Moisture is removed from the condenser frequently using solenoid valves and a
timer to minimize contact of moisture and the sample. All components of the
system are stainless steel, Teflon, or glass to minimize possible reactions
with the sample. The continuous monitoring instrumentation is listed in 	
Table A-l.	^ ^ /
Furnace Gas Temperature
Furnace gas temperatures were measured using a water-cooled suction
pyrometer. A suction pyrometer was used due to the inaccuracies in high-
temperature measurements caused by radiation loss from standard
thermocouples. The suction pyrometer consists of a high-temperature
thermocouple in a ceramic shield. A high flow rate of furnace gas is
withdrawn through the shield and over the thermocouple so that convective
heat transfer dominates, reducing the errors caused by radiation losses to an
insignificant level. An air ejector is used to aspirate furnace gas. The
¦ A-2 •
-------
Figure A-1. Air heater inlet continuous monitoring system.
' IX-3
-------
TABLE A-1. CONTINUOUS GAS ANALYZERS — AIR HEATER INLET
GdS
Mea-
sured
Detection Principle
Manufacturer
Model No.
Range
Nominal
Calibra-
tion Gas
Level
02
Paramagnetic
Taylor
0A570
10%
8%
S02
Pulsed Fluorescence
A
J TECO
_ 40
1000 ppm
800 ppm
N0X
Chemiluminescent
TECO
10AR
1000 ppm
800 ppm
CO
Nondispersi ve
Infrared
ANARAD
AR500R
500 ppm
400 ppm
C02
Nondi spersi ve
Infrared
ANARAD
AR500R
25%
22.5%
-------
gas flow rate is monitored with a calibrated orifice to ensure an adequate
gas velocity over the thermocouple. Temperatures are measured with K or S
type thermocouples. Figure A-2 shows the design of the suction pyrometer
probe. Figure A-3 shows the construction of the pyrometer tip.
Coal and Ash Characteristics
Samples of coal and ash were collected throughout the test program to
determine chemical composition and physical characteristics. Coal samples
were collected on a daily basis. Ash samples were obtained from the bottom
hopper of the boiler, the precipitator hopper, and the high volume
particulate sampler during the field tests. Solids analytical procedures are
listed in Table A-2.
A-5
-------
Water Out
Thermocouple
Pressure Taps
Swagelock
fitting
Suction
Pipe
Tubes of same length
with Identical bends
Expansfon
Joint
Figure A-2. Internal construction of water-cooled suction pyrometer probes.
-------
Inner Ceramic Shield
Figure A-3. Suction pyrometer tip construction.
r
-------
TABLE A-2. COAL AND ASH ANALYSES
Parameter
Analytical
Procedure
-Samples
- • tdi'b'e,-
Analyzed
Coal
Ash
Proximate Analysis
Volatiles, Fixed C,
Ash
ASTM D 317 2
X

Heating Value
ASTM D2015
X

Ultimate Analysis
C, H, N» Ash, S
ASTM D3176
X

Ultimate Analysis
C, H, N, Ash
Perkin Elmer 240b
Analyzer
X
X
Sulfur
Leco SC 32 Sulfur
Analyzer
X
X
Ash
ASTM 03174
X
X
A-8
-------
APPENDIX B
QUALITY ASSURANCE

-------
Exhaust gas composi tion was measured using continuous monitors at the
air heater gas inlet. This location was selected to allow flue gas
stratification to be measured prior to dilution and mixing by the air heater.
Routine quality control procedures included daily leak checks of the sampling
system and calibration of the analyzers using standard compressed gas
certified by the manufacturer to have an accuracy within 2 percent of the
stated value.
Replicate calibrations were monitored as a measure of instrument
precision. Precision was generally less than 2 percent. Data were corrected
for instrument drift for the few occasions that precision exceeded 2 percent.
The relative accuracy of N0X. 02 and CO2 was evaluated using wet chemical
analyses using EPA Reference Methods. NQX concentrations were determined
using grab samples collected in glass sample flasks in accordance with Method
7. Sampling was performed by EER and the analysis was performed by Truesdail
Laboratories. Truesdail also analyzed the grab samples for CO2 and Og using
Method 3. Results of the relative accuracy measurement are shown in Tables
B-l and B-2. Relative accuracy of the N0X emission rate in terms of lbs/106
Btu were well within the EPA performance specifications for continuous
monitors of 20 percent. Some of the data for N0X, Oj, and CO? on an as
measured basis showed substantial differences compared to the continuous
monitors. Those differences are due to gas stratification in the exhaust
ducts. The Method 7 flasks obtain a grab sample at a single location over a
period of a few seconds. Each of the twelve flasks collected at each boiler
were obtained at different points in an attempt to obtain a representative
sample. As can be seen in Table B-l, flasks collected in the west duct
showed an Og concentration very close to the monitors, while the east duct
samples showed a large difference, apparently due to variations in O2
concentration between the two ducts. This variation was the cause of the
apparent poor relative accuracy for O2- Similar results were seen in Table
B-2. Although the overall N0X emission rate showed good instrument accuracy,
the N0X and O2 concentrations showed poor accuracy apparently due to gas
stratification at the sample points.
B-'2!
-------
TABLE B-1. CONTINUOUS MONITORS RELATIVE ACCURACY CALCULATION
12-11-84 COMANCHE
Time
N0X (ppm)

°2
(%)

C02 U)
N0X
(lbs/106 Btu)
RM
AVG RM
M
DIFF
RM
M
DIFF
RM
M
DIFF
RM
M
DIFF
0902
—

4
2

2.2
2-
65
0.45
16.7
17
.02
0.32
X


0904
366
\ 420


2
3.6


0.95
16.3


0.72
I 0.567
0.564
0.003
0907
473
)



2.7


0.05
16.4


0.62
)


0912
431
\



2.3


0.35
16.6


0.42
\


0915
456
I 410


12
2.1


0.55
17.0


0.02
> 0.540
0.564
0.024
0923
342
)

'

2.8


0.15
16.2

t
0.82
)


1003
411
)
3?
)4

5.7
2.
62
3.08
14.6
16
.53
1.93
)


1006
410
> 407


13
3.9


1.28
15.3


1.23
i 0.614
0.525
0.089
1008
399
)



4.7


2.08
14.8


1.73
)


1012
337
\



4.2


1.58
14.9


1.63
)


1021
411
> 377


17
4.3


1.68
14.9


1.63
\ 0.562
0.525
0.037
1023
384
)
- '


5.2

r
2.58
14.9


1.63
)


Avg

404

11
3-6

1.23
15.7

1.06
0.571

0.038
Confidence Coefficient
10


0.63


0.41


0.058
Relative Accuracy
5.2


51.7


9.4


16.8
Grab Samples
From
West Duct
Grab Samples
From
East Duct
-------
TABLE B-2. CONTINUOUS MONITORS RELATIVE ACCURACY CALCULATION
WYODAK 2-4-85
NOx (ppm)
02 (%)
C02 (%)
N0X (lbs/10® Btu)
Time
RM
Avg RM
M
DIFF
RM
M
DIFF
RM
M
DIFF
RM
M
DIFF
1603
287
)



5.3
3.
78
1.52
14.8
15.
58
0.78
)
0.461



> 283
324
41








> 0.415


0.046
1609
279
)



3.3


0.48
15.8


0.22
)



1614
290
)



5.5


1.72
15.6


0.02
\



1616
283
> 292


32
3.6


0.18
14.0


1.58
> 0.431


0.030
1617
304
J



4.1


0.32
14.9


0.68
)



1620
279
)


'
4.6


0.82
15.3


0.28
)





> 292


32








> 0.430


0.031
1620
304
)



4.1


0.32
14.9


0.68
)



1623
261
)



5.5


1.72
14.7


0.88
)



1625
279
> 275


49
5.3


1.52
14.9


0.68
> 0.417


0.044
1626
284
)



3.7

r
0.08
15.3

f
0.28
)



Avg

285.5

38.5
4.5

0.87
15.0

0.61
0.423

0.038
Confi dence
Coefficient

13.0


0.49


0.32


0.013
Relative Accuracy
18.0


30.2


6.2


12.1
-------
Quality assurance of the solids analysis by EER and Hagen includes
analyses of audit samples provided by the EPA EMSL for coal. Figures B-l,
B-2, and B-3 show the results of these analyses in terms of quality control
charts.
";t-S
-------
ACCURACY QUALITY CONTROL CHART
A QA Goal
O EER
A Hazen
Results for samples with
lower sulfur content are
shaded
Median of A11 Labs
High Sulfur Concentration
	Low Sulfur Concentration
J	i	i	I	I	I	I—i
Date 3/^ 9/g2 3/83 9/83 3/84 %4 3/85 9/85 3/86
Figure B-1. EPA EMSL coal audit sulfur analysis.
-------
i—i—i—I—i—i—i—i—r
O
ACCURACY QUALITY CONTROL CHART
15
10
-5
10
o
J	I	I	L
J	I	—I	L
A hazen
O eer
	 MEDIAN ALL PARTICIPANTS
RESULTS FOR SAMPLES WITH LOWER
ASH CONTENT SHADED
qA GOAL
o &
9
		— QA GOAL
3/82 9/82 3/83 9/83 3/84 9/84 3/85 9/85 3/86
DATE
Figure B-2. EPA coal audit ash analysis.
-------
ACCURACY QUALITY CONTROL CHART



1 1
1 1
1
1 1 1 1

O 1st Sample
(~1 2nd Sample
Analysis by
Hazen Research, Inc.
i

5
-






—

4
-






-

3
0
-




QA Goal
-










>>
(J
n)
J-
1
n
-
o
n
n
o


-
u
u
c

-1
-
~
o
B
~ g Q


-
4-»
n)
0)
ct
-2
-3




R
QA Goal


-4
1



LJ




-5

I ¦
~
1 1
1
1 l I l



3/82 9/82 3/83 9/83 3/84 9/s4 3/85 9/85 3/86
Figure B-3. EPA EMSL coal audit heating value analysis.
-------
REPORT
Truesdail Laboratories, Inc.
CHEMISTS - MICROBIOLOGISTS
R C9 EAM C »
CLIENT
SAMPLE
DEVELOPMENT
ENGINEERS
-	tCITINS
Energy and Environmental Research
8001 Irvine Blvd.
Santa Ana, GA 92705
Attention: Jim Reese
Preparation and shipment of N0X Flasks to Pueblo, Co.
14.201 FRANKLIN AVENUE
TUSTIN, CALIFORNIA 9Z6B0
AREA CODE 714 • 733 • 4239
AREA CODE 213 ¦ SZ9 * 1S«4
CABLE: TRJELABS
date _ • , •
December 21, 1984
RECEIVED November 16, 1984
LABORATORY NO. 00358
P.O. No. 28219
INVESTIGATION
Nitrogen Oxides
RESULTS
_ The submitted samples were analyzed for carbon dioxide (CO?) and Oxygen (02)
by Orsat and for nitrogen oxides (N0X) by phenol disulfonic acid (PDSA) method.
The results were as follows:
Sample I.D.
C0?, % • ¦
Qg» % ¦
Sftu	ppm	dry.
3606
14.9
4.3
411
1439
14.9
4.2
337
1090
•14.9
5.2
384
13S7
16.3
3.6
366
1377
14.6
5.7
411
1328
14.8
4.7
399
1437
15.3
3.9
410
612
17.0
2.1
456
611
16.6
¦ 2.3
431
1193
16.2
2.8
342
3330 .
16.7
2.2
*
1183
16.4
2.7
473
* Sample lost during analysis
r ! s-i
Respectfully submitted,
TRUESDAIL LABORATORIES, INC.
O*. JSmmk-
S. Hugh "Brawki Supervisor
Air Pollution Testing
TWi report applies oaly totfcw ample; or samples. iarestigttedl ii col Mceutrilr iwiicad-ws oi dae qutlit? c* cecdituro of ipjamidy
icUctiaki ox similar products. As ¦ mutual protection to dieats> tbe public aad these Latara tenia* tbis report is fobttitted tad tcccpwu
for the exdusive use of the client to whom it is addressed ttfid iqxn die eomiitioo that ii is act to be usea, itt whele or io part, in ftn?
uhcftUiQi or pufeliciiy natter without prior writtea imfeorfrarwm torn diese Laboratories.
;b-| j
-------
N0X SAMPLING DATA AND RESULTS
/
Sample
No.
Date
n 5i"
Time
Flask
Vol
Vf (ml)
Initial
Ba rom.
Press
''bar j
(in Hg)
Initial
Man
Vacuum
M/j
(Cm Hg)
Initial
Flask
Press
PI
(mm Hg)
Initial
Flask
Temp
TI
(°C)
Final
Barom.
Press
^barp
(in Hg)
Final
Man
Vacuum
MF
(Cm Hg)
Final
Flask
Press
PF
(mm Hg)
Final
Flask
Temp
TF
(°C)
Corr.
Sample
Vol
Vsc
(ml)
no2
in
Sample
(ng)
N0x
cone as
no2, C
(lbs/scf
N0x
cone,
C
(ppm)
/ u
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-------
REPORT
CLIENT
SAMPLE
ENERGY AND ENVIRONMENTAL RESEARCH
8001 Irvine Blvd.
Santa Ana, CA 92705
ATTENTION: Jim Reese
14301 FRANKLIN AVENUE
TUSTIN. CALIFORNIA 92489
AREA CODE 714 • 730-6239
AREA CODE 213 • 885 • 1S64
CABLE: TRUELABS
DATE February 22, 1985
RECEIVED February 6, 1985
LABORATORY NO. 05516
Preparation of 12 PDSA-Flasks-Shipment to
Pacific Power and Light Plant in Wyoming
P.O. Number: 28976
INVESTIGATION
Nitrogen Oxides
RESULTS
The submitted samples were analyzed for nitrogen oxides (N0X)
by the phenoldisulfonic acid (PDSA) method, and for carbon dioxide
(CO2) and oxygen (O2) by Orsat. The results were as, follows:
* No sample.
Sample I.D*
CQp, %
0?, %
NO,, ppm dry
1i)60
15-3
H.6-
279
3473
14.9
4.1
304
1360
15.6
3-8
302
968
14.7
5.5
261
1413
15.8
3.3
279
1474
14.8
5.3
267
3253 '
. 14.2 '
12.1
250
610
' 14.0
3.6
283
619
15.3
3.7
284
626
14.9 '
5-3
279
• 613



1442
15.6
5.5
290
Respectfully submitted,
TRUESDAIL LABORATORIES, INC.
*/? 0JWKJ
O
^	X
S. Hugh Br*t>wn, Supervisor
Air Pollution Testing
This report applies oaly to the ample, of samples, investigated audi is sot necessarily indicative of the quality or coaditica ol apparently
identical of similaf products, As a mutual protect: oa to clients, the public tad these Laboratories, this report is submitted and accepted
foj die exdusrre use of the client to whom it is addressed tad upon the condition that it Is oot to be usea. in whole Of Iq part, in say
advertising or publicity matter without prior written guihonzadcn from these Ddxmtsrica.
B-11
-------
N0X SAMPLING DATA AND RESULTS
ffl. oj . ^/ fc "3°
Pi-AnsT : W y o O f-
Citj<- &iLLfrr£	^ <•
Sample
No.
Date
Time
To Tot.
-XS~I
Flask
Vol
Vf (ml)
Initial
Barom.
Press
^bar^
(in Hg)
Initial
Man
Vacuum
M/,
(Cm Hg)
Initial
Flask
Press
PI
(mm Hg)
Initial
Flask
Temp
TI
(°C)
Final
Barom.
Press
''barp
(in Hg)
Final
Man
Vacuum
MF
(Cm Hg)
Final
Flask
Press
PF
(mm Hg)
Final
Flask
Temp
tf
(°c)
Corr.
Sample
Vol
Vsc
(ml)
no2
in
Sample
tug)
N°x
cone as
no2, c
(lbs/scf
N0X
cone,
C
(ppm)
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GAS COMCFNTPAIION P^LCI'lAHON
Date
Test
1-31-"gS^
No. /-31-/4 -? 1-31
Operator
Avg Gas Response, Davg
Actual Gas Concentration, Ga
(°avg~Zavg) x Gs/(savg zavg^
Gas Concentration-0 0%, Ga@0% = (G^ x 21)/(21-XO^)
i ^
! -i?
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8
n
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- #
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TIME
LOCATION
N0X | CO | C02
02
S02
Davg
ga
G/\@Oi | DaVg
ga
G/\@0% | Davg
GA
Ga@0%
Davg
Gd
Ga@0%
Davg
ga
gago*
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GA: CONCFUTDATION CA'.CTATICM
Date	Operator Q 	 Avg Gas Response, Dayg
Test No. 	.	Actual Gas Concentration, Ga = (Dflvg-Zavg) x Gs/(Savg-Zavg)
Gas Concentration-0 0%, Ga@0% = (G x 21)/(21-XO )
A	2


ECOfiJ ¦ OUT'

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o2
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TIME
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ga@o%
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Ga@0%
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Ga0OX

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-------
C\S fOWCEMTPATIOM CAL"ULATIOfl
Date	2' I 2-'2-- ^ Operator 	 Avg Gas Response, Dayg
Test No.	Z-Z~ 7	Actual Gas Concentration, Ga = (Davg-Zavg) x Gs/(savg~zavg)
Gas Concentration-0 0%, Ga@0% = (G. x 21)/(21-%0 )
"	2
TIME
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LOCATION
N0X bl>/
CO ^
CO2 *>~
O2 bl*-
SO2 w/».
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ga
GA0O%
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GA0OX
Davg
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Ga@0%
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GAS r.ONrFMT"ATION r/>Lv"l/TION
Date
Test No.
-rf
Operator j) ,(t
Avg Gas Response, Davg
Actual Gas Concentration, Ga = (Davg-Zavg) x Gs/(Savg-Zavg)
Gas Concentration-0 OS, Ga@0Z = (G^ x 21)/(21-560^)
TIME

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GAS CONCENTRATION CALCULATION
Date	/ - ^ f S	Operator f) 	Avg Gas Response, Davg
Test No. 			Actual Gas Concentration, Ga = (DaVg-ZaVg) x Gs/(SaVg-ZaVg)
Gas Concentration-@ 0%, Ga@0l = (G^ x 21)/(21-%02)
TIME
gr(0AJ. 0 u 1
LOCATION
N0X | CO
C02
o2
S02
"avg
GA
GA@0% | Davg
ga
Ga@0%
Davg
GA
GaGOX
Davg
Ga
GaPOX
Davq
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Operator J),
Avg Gas Response, Dayg
Actual Gas Concentration, Ga = (Davg-Zavg) x Gs/(Savg-Zavg)
Gas Concentration-@ 0%, Ga@0% = (Q^ x 21)/(21-%0^)
TIME
LOCATION
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o2
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Davg
GA
Ga@0%
Davg
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Test No. 		Actual Gas Concentration, Ga = (Davg-Zavg) x G^/fSayg-Zgyg)
Gas Concentration-0 0%, Ga@0l ' = (G^ x 21)/(21-^0^)



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Ga@0%
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Test No. ' 			Actual Gas Concentration, Ga = (t*aVg-Zavg) x Gs/^avg"zavg)
Gas Concentration-P OX, Ga@0% = (G^ x 21)/(21-%0 )
TIME
LOCATION
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CO
co2
°2
S02
°avg
ga
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Ga
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Davg
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Davg
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Date	^ — y — f- 3
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GAS CONCENTRATION CALCULATION
Operator J), f ,	
Avg Gas Response, Dayg
Actual Gas Concentration, Ga = (Davg-Zavg) x Gs/(Savg-Zavg)
Gas Concentration-P 0%, Ga@0fc = (Gfl x 21)/(Z1-%0Z)
TIME
LOCATION
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co2
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Actual Gas Concentration, Ga = (Davg-Zavg) x Gs/(Savg-Zavg)
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TIME
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TIME
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TIME
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Test Mo. 			Actual Gas Concentration, Ga = (Oavg-ZaVg) x Gs/(Savg-Zgvg)
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GA^ CONCENTRATION CALCIT/TIOM
Date	2-"y|"^S	Operator 		 Avg Gas Response, Oavg
Test No. 				Actual Gas Concentration, Ga = (Davg-Zavg) x Gs/(savg_zavg)
Gas Concentration-@ 0%, Ga@0% = (n x 21)/(2'\-%0 )
"	2
TIME
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LOCATION
N0X
CO | co2
o2
S02
Davg
ga
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Davg
ga
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§ rRfrTl F (CATiO	GAS CONCENTRATION CALCULATION
Date
Test No.
c^~~ ( (	Operator Q'C<
Avg Gas Response, Davg
Actual Gas Concentration, Ga = (Davg-Zavg) x Gs/(Savg-Zavg)
Gas Concehtratlon-0 0%, Ga@0% = (G^ x 21)/(21-%0 )

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CO
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LOCATION
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coz
o2
so?
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ga
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-------
GAS CONCENTRATION CALCULATION
Date
Test No.

Operator	d
Avg Gas Response, Davg
Actual Gas Concentration, Ga = (Davg-ZaVg) x Gs/(savg~zavg)
Gas Concentration-0 0%, Ga@0% = (G^ x 21)/
V
CO!
TIME
LOCATION
N0X
CO
C02
o2
so2
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GflQOl
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ga@oz
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Ga»0X
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GAS CONCENTRATION CALCULATION
Date	7_- \	Operator 			 Avg Gas Response, Davg
Test No.	^ ^	Actual Gas Concentration, Ga = (DaVg-Zavg) x Gs/(SaVg-Zavg)
Gas Concentration-@ 0%, Ga@0% = (G^ x 21)/(Zl-XO^)
-------
GAS CONCENTRATION CALCULATION
Date	.£"'2-' a o	Operator 	 Avg Gas Response, Davg
Test No. MyoXcJk.	Actual Gas Concentration, Ga = (Davg-Zavg) x Gs^Savg"Zavg)
Gas Concentration-<® Ofc, Ga@0X = x 21)/(21 )
TIME
Ou'V"
LOCATION
N0X
CO I co2
°2
SO2
Davg
Ga
GAm
Davg
GA
GA0O%
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GA
Ga@0l
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-------
GAS CONCENTRATION CALCULATION
Date	^„/3 -	Operator	Avg Gas Response, Davg
Test No. 	-	Actual Gas Concentration, Ga = (DaVg~ZaVg) * Gs/(savg"^avg^
Gas Concentration-9 0%, Ga@0l = (G^ x 21)/(zl-%0 )

TIME
boat
LOCATION
N0X
CO
C0Z
o2
SO2
Davg
Ga
GAm
Davg
GA
gago*
Davg
GA
GaPO?,
Davg
Ga
Ga90%
Davq
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3.<7-------
GAS CONCENTRATION CALCULATION
Date	7^1 3 -	Operator 	¦	Avg Gas Response, Dayg
Test No. Z'Cf -	Actual Gas Concentration, Ga = (Davg-Zavg) x Gs/(Savg-Zavg)
Gas Concentration-0 OX, Ga@0l = (G^ x Z\)/
TIME
LOCATION
N0X
CO
co2
o2
S02
Davg
ga
GAm
Davg
GA
gapo%
Davg
GA
Ga@0%
Davg
Gd
Ga@0%
Davg
ga
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-------
INSTRUMENT CALIBRATION
DATE /- 3 !-f	.	Plant Yo DAK
TEST NO.			Operator p^C,
TIME OF INITAL CALIBRATION /q ft ¦
TIME OF FINAL CALIBRATION / ? / 3 -

NOx
CO
co2
o2
. so2
Span Gas Concentration, Gs
f/2. y'
Hffi.f
11,HI
?.0
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Initial Zero Response, (01v)
i"< 0
J~ 0.

S~^ 0
5"vd
Final Zero Response, Zf (D1v)
c< o

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v-r
51 Li
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f (Sf-Zf MS1-Z1)
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0, "f
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-------
INSTRUMENT CALIBRATION
DATE- I - 1! ~ f SPlant uy-fg Q
TEST MO. -	Operator Q*t ,
TIME OF INITAL CALIBRATION fl "Xl
TIME OF FINAL CALIBRATION 0 lH\

NOx
CO
C02
°2
S02
Span Gas Concentration, Ss
		 t

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t'xo
Initial Zero Response, Z,- (Div)

TO
r 0
5* 0
S"'0
Final Zero Response, Zf (Dfv)
r.>~

r, 3

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Initial Span Response, Sf (Dfv)
S-G, 1
?r, i
f°f<0
0
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Fina-'l Span Response, Sf (Div)
ey. t


tfr^o

Avg. Zero Response, Zavg (Div)
- (Zt + Zf)/2
S-)
S,1b'


5: [ .
Avg. Span Response, Savg (Dfv)
3 + Sf)/2
Hit*

nf
&
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Zero Drift, (S) = |Zf-Zi)
t>. z
i.f
o. 3 .
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z
Span Drift, {%) * (Sf-Zf MS-j-Zf)
-l.i*
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O. I©
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-------
INSTRUMENT CALIBRATION
DATE S--( - FJ	. Plant M/y^? O&K
TEST	NO.-	Operator f) ,f,
TIME	OF INITAL CALIBRATION
TIME	OF FINAL CALIBRATION	iff TC

NOx
CO
C02
°2
so2
Span Gas Concentration, Ss
	 			 1


To

Initial Zero Response, Zj (D1v)
J- 0


r. o
S~t a
Final Zero Response, Zf (Oiv)
0
r^d

s. t
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Initial Span Response, S-j (D1v)
SO J
fi.i-
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?1,0
Final Span Response, Sf (Dlv)
ll-t
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Avg. Zero Response, Zavg (Div)
- (Z-j + 2f)/Z
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Avg. Span Response, Savg (D1v}
- (Si + Sf)/2


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Zero Drift, (*} - (Zf-Zf)
o'
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0
Of 1
-0,1
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/.r
t
0.1
-p'j
-I.J
-------
INSTRUMENT CALIBRATION
DATE J~~l
TEST NO. 	'
TIME OF INITAL CALIBRATION
TIME OF FINAL CALIBRATION

NOx
¦ CO
C02
02
S02
Span Sas Concentration, 6s

Hof^
xl'Hl
ftO
f'^-0
Initial Zero Response, Z-j (D1 v)
& 0
S i 0
0
r, i
<>
9f. C
$S,3

Avg. Zero Response, Zavg |D1v)
- (Zt + Zf}/2
f-'K


S", 2—
5- ! -
Avg. Span Response, Savg (D1v)
¦¦ (S-j + Sf)/2

U'p
ef^f.o s

$ -------
INSTRUMENT CALIBRATION
DATE • ;u/ ~t	Plant ,uyX£iM_
TEST NO. -		Operator* ¦ V	<

NOx
CO
C02
02
S02
Span Sas Concentration, Gs

Hon ¦?

r.t.

Initial Zero Response, Z-j (D1 v)


$ > o
S^d
2-
Final Zero Response, Zf (01v)
r.o
S~,f
r. d
d
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-» (Zf + Zf5/2

3 5""
£.0.
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a (Sf + Sf)/2
i
K-------
INSTRUMENT CALIBRATION
date x ~ % - Ps^
TEST NO. ,			
TIME OF INITAL CALIBRATION / Q { (p
TIME OF FINAL CALIBRATION	X.

N0X
CO
C02
o2
so2
Span Gas Concentration, 6s
//-W
tof, f

7*0

Initial Zero Response, Z\ {D1v)
S~ Q
T, 0
s\a

r. a
Final Zero Response, Zf (D1 v)
¦ r.2-
1,0
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i. Z
"f.O
0
-o.z-
ro.<
Span Drift, (%) • (Sf-Zf)
O'i
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Or!
0-5kO

Wro QfrK
Operator Q
-------
INSTRUMENT CALIBRATION
DA^	£ *>	Plant u/Y/j p/f-fc
TEST MO. 	'	Operator f)< C ,
TIME OF INITAL CALIBRATION /T 3> ^	,
TIME OF FINAL CALIBRATION

N0X
CO
co2
°2
so2
Span Gas Concentration, Gs
	:	t
tfhH '
H0(. 1

f'O
rto
Initial Zero Response, Zj (Div)
i--o
r 7
Initial Span Response, Si (D1v)
S-Q.'i
FH i (?
?%1
fr.o
27,0
Fina-1 Span Response, Sf [D1v)
TH>d
?7r0
tow
tr, 3
ts~<0
Avg. Zero Response, Zavg (Div)
- {Z^ + Zf)/2


5M
4-f

Avg. Span Response, Savg (Div)
85 i$i + Sf)/Z ;;

ycyo


§6- °
Zero Drift, (l) - (Zf-Z-j)
o
t-y
.2- ¦

-0,1
Span Drift, (I) - (Sf-Zf )-(S1-Z,-)
"23
, v
3.1
o.f
-1.7
B-46
-------
INSTRUMENT CALIBRATION
DATE 2- — 1 -I i T- Plant yui Q pftK
TEST NO. 		Operator Q - C ,
TIME Of INITAL CALIBRATION [Q0 £
TIME OF FINAL CALIBRATION Oiq 0
/ T ^

N0X
CO -
C02
02
SO2
Span Gas Concentration, Gs
?#> 1 '
y?/,  0
f, a
r. 0
s~ 0
n 0
Final Zero Response, Zf (Dlv)
r.i
y,r



Initial Span Response, Si (D1v)


19,6
fr>o

F1na-*1 Span Response, Sf (Dlv)
sr>6
tH'f
ft.r
?r,3
ti(Q
Avg. Zero Response, Zavg (Dlv)
- o
0, ir
Span Drift, (S) - (Sf-Zf)-(S1-Zf)
~oP\
o.h
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-i|
B-47
-------
INSTRUMENT CALIBRATION
DATE	i"Y—f S"~	Plant UjY(7 D A-1
TEST NO, 		Operator P < C .	
TIME OF INITAL CALIBRATION 0fOf
TIME OF FINAL CALIBRATION

NOx
CO
C02
°2
so2
Span Sas Concentration, Gs
i
pz-H'
Yf/.?

t<0
$Za
Initial Zero Response, Zn- (D1v)
fr
Zero Drift, {%) = (Zf-Zj)
(M

0. H


Span Drift, (%) • (Sf-Zf)-(S1-Z1)
V-'h

'0.1-
0.3

B-48
-------
INSTRUMENT CALIBRATION
DATE	S	¦	Plant
TEST NO.'		Operator p <-C. >
TIME OF INITAL CALIBRATION	//~3f
TIME OF FINAL CALIBRATION	/Cd
%
Initial Zero Response, Zf (D1v)
ru
ire
r. 
' M 
5,0 .
Avg. Span Response, Savg (01v)
3 (Si + Sf)/2


£x>
ST2-
^|(b tO
Zero Drift, (%) = (Zf-Z,)
o
-0' l
 c>
£>.f
0 
-------
INSTRUMENT CALIBRATION
DATE ^ - Y -	Plant W/tf d*K
TEST NO. 			Operator p <-C <
TIME OF INITAL CALIBRATION f/„ .C&
TIME OF FINAL CALIBRATION a 1^1

NOx
CO
co2
°2
S02
Span Sas Concentration, Gs
t-12-V '
Hof^
iy.t/3

fXd
Initial Zero Response, Zj (01v)
S l P

O O
r.y
r. a,
Final Zero Response, Zf (01 v)



r. i

Initial Span Response, Si (Dlv)

is"' 0


f r- o
Flna-1 Span Response, Sf (01 v)

ti.r

ir.d
f3,r
Avg. Zero Response, Zavg (D1v)
- i2\ + Zf)/2

4-fr
S\oO
S'. ¥€>
5,0
Avg. Span Response, Savg (D1v)
• (Si ~ Sf)/2 %
i^-1
Hi<
It if


Zero Drift, {%) - (Zf-Zt) .
o
¦ . L
o
o
0,0
Span Drift, (S) ¦ {Sf-Zf)-(St-Z1)
D
> (p
~ i -
PA
-\.*L
-------
INSTRUMENT CALIBRATION
DATE ' JX --(S-f-Zt)
0 ' (f !
on
0>(f
0'H
~J.o
B-51
-------
INSTRUMENT CALIBRATION
DATE ,4-5 -f j"~~ ¦	Plant \aj^(7QAK
TEST NO. ¦		Operator	P«Q
TIME Of IN1TAL CALIBRATION 	f(m P i*~
TIME OF FINAL CALIBRATION	
-------
INSTRUMENT CALIBRATION
DATE J-G >	Plant u/V 0 D4*k
TEST NO. 		Operator P > C .
TIME OF INITAL CALIBRATION O ?OQ
TIME OF FINAL , CALIBRATION (Q 1

NOx
.CO
co2
02
so2
Span Gas Concentration, Gs
$tl, «-/

jj.ii
?.o'

Initial Zero Response,. Zf C01 v}
& l d
S t 3
S~~i 0
r, 0
ritf
Final Zero Response, Zf (D1v>
CT
3,r

s~.
iT3
.Initial Span Response, S-f (D1 v J
ft, A
tr-i
°t%d


Final Span Response, Sf (01v)
tt.r
w.r
o
tf'i
fno
Avg. Zero Response, ZdVg (01v)
3 (Z< + Zf)/2
S~,/f
i0

Avg, Span Response, Sgyg (D1v)
- (Si + Sf)/2 •
HO
fj.fr
loX.e
ffor
|t.o
Zero On'ft, (%) 3 !Zf-Zi)
e-l
-/..r
o. ?
o.z

Span Drift, (%) « (Sf-Zf l-tS-j-Zf 3
O.I
~/.v
T.T
o. f
-l.-b
8-5.3
-------
INSTRUMENT CALIBRATION
Plant ^Y(JOA-£
Operator D r C '
¦
o?s~&

NQX
CO
cog
02
S02
Span Gas Concentration, Gs
in. y
Vol, ?
wjj
}r< 0
fl-O
Initial Zero Response, Zi (D1v)
r;o
S'o
5-J

5~ d
Final Zero Response, Zf (01v)
AO
r.c

r<. 0
d
Initial Span Response, S-j (D1v)

?r°i
91. f
97.0
?Ur
K.'o
Zero Drift, (%) * (Zf-Zj)
0-6


0.0

Span Drift, (%) » (Sf-Z'f)-(-Zf)

/, i"
0>1

-n
DATE ' J ~
-------
INSTRUMENT CALIBRATION
DATE	1~1~H	Plant Wjq Q
TEST NO. •		Operator j)i C~ i	(
TIME OF IMITAL CALIBRATION	lQ 0 3

Avg. Zero Response, ZaVg (Oiv)
¦ {Z-J + Zf)/2
J i J
i.r
r, o
S" x>

Avg. Span Response, Savg (01v)
(Si + Sf)/2
HJr

.97.tr
ff.ff
$5*i <5
Zero Orift, (?) ¦ (Zf-Z-f)

-/,o
0. f
o.y
o.v
Span Orift, {%) s (Sf*Zf )-(S-j-Zj)
-0.1
'O.l
-2-1
-o.t
-VI,I
B-55
-------
INSTRUMENT CALIBRATION
DATE 2 -~7-jr f~	Plant vyVtf D 4 K
4MnMHVaaaa|aaaaaaaaaaaaaaaaaaaaaaawaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaft
TEST NO, 		Operator Q < ,
TIME OF IMITAL CALIBRATION /$~^> 3
TIME OF FINAL CALIBRATION GlHjb

M0X
CO
COg
02
S02
Span Gas Concentration, as

ft! 1.7
Wj
fro

Initial Zero Response,. Zi (01 v)
r, ^
1 J
r. d
s~ 0
s~.
Final Zero Response, Zf (D1vl
r- 7
7« o
r,i~
U
SI 1—
Initial Span Response, S-) (Olv)
rc.l
gr.X
7h0-

?l,d
Final Span Response, Sf CDiv)
n,i.
n.r
103,0
fy*sl
m
Avg. Zero Response, Zavg (Div)
- (Zt + Zf5/2
r. i r
C-s
r. i
i
Q'l
-on
3.P
~o,r
- *}(0
B-56
-------
INSTRUMENT CALIBRATION
DATE rt~L0-F C	Plant VKjj Q DAK
TEST NO. 			Operator p . C.
TIME OF INITAL CALIBRATION	crf/C
TIME OF FINAL CALIBRATION	Q 1 H 0

N0X
CO
CO 2
O2
so2
Span Sas Concentration, Gs

Htl. 1
J j y?
f.tf

Initial Zero Response,. Zi (D1 v)
Tt o
rj
r.a
Si
Slo
Final Zero Response, Zf (D1v)
S\d
Z.o


r-1>
Initial Span Response, $¦) (Div)

ff.Q
9% d
J>fT£

Final Span Response, Sf (01 v)
%•*
ti>o
??*<>

ry.r
Avg. Zero Response, Z4vg (Dlv)
- Uj + Zf)/2
' S.o ¦
4.t>
So
5>
f.o
Avg. Span Response, Savg (D1v)
3 (Si +¦ Sf )/2
IL.Z
n*

3C?A
O
/-r
-VT
B-57
-------
INSTRUMENT CALIBRATION
DATE ^-1 I —'	Plant yyf Q Q&K
TEST MO. 		Operator Q-C .
TIME OF INITAL CALIBRATION g7ff '
TIME QF FINAL CALIBRATION [(*,11

NO*
CO'
. ¦ coj
02
SO 2
Span Gas Concentration, Ss
H
fot> ?

f-.o

Initial Zero Response, Zi (01 v)
Tu?


r.o
Sid
Final Zero Response, Zf (Div)
i.r
Q.f
V, e
57 c?
0
Initial Span Response, Si COiv)
%(*.r

no

?7cO
Final Span Response, Sf (01v)
n.?
??•*
HS.X
0-6
C"9
Span Drift, {%) - (Sf-Zf)-(St-Zt)
0 . ff
M
"s. y
0, 0

B-58
-------
INSTRUMENT CALIBRATION
DATE ^ ~!(Plant wy 0 QA-K
TEST NO. 		Operator 9 , f . .
TIME OF INITAL CALIBRATION	[(„ Cd	. ......
TIME OF FINAL CALIBRATION	ol^H

NOx
CO
C02
02
SO 2
Span Gas Concentration, Gs
1 '
Hob 1
ti.ii
r*o

Initial Zero Response, l\ (D1v)

r-d
fl a
-------
INSTRUMENT CALIBRATION
DATE . / - Jf~ t S~~-	Plant U/y.f j)
TEST MO. 		Operator J) t C ,
TIME OF INITAl CALIBRATION	Q ?Cl
TIME OF FINAL CALIBRATION	IC y

Xh v?
(7

Initial Zero Response,. Z-f (01 v)
3^ 0
5^ 0

S-^0
£\o
Final Zero Response, Zf (Div)
s~< o
i.r
5~ 0

$". 1
Initial Span Response, S-j (01 v)

?r.d
H%d
fn d
81,o
Final Span Response, Sf (Div)
ft

{09-1

%.l
Avg. Zero Response, Zavg (01v)
¦ (Z, + Zf)/2
f-o

Coo

5.1
Avg. Span Response, Savg (Div)
• (Si m Sf)/2

ux
Uls
0.3

Zero Orift, [%) ¦ (Zf-ZO
0
-Q45&
D
<0,3
0 (V
Span Drift, (2) =» (Sf-Zf)-(S1-Z1)
-0. 1
}¦€
h 3
£>,3
- D.°l
B-.6.0J.
-------
INSTRUMENT CALIBRATION
DATE	fSL-r .P	Plant Ws j$ j) & £
TEST NO. "	-	Operator- p, Q
TIME OF INITAL CALIBRATION	/£
TIME OF FINAL CALIBRATION	Gl 0
&0
Initial Zero Response,. Zi (01*3

S~ o

5"' 0
r. d
Final Zero Response, Zf (D1v) .
>\o
(f t s
jrvtK
S, 5

n d
Initial Span Response, Sf (01 v)



tco

Final Span Response, Sf (D1v)
5%.S~
tu
Pe-»
Srvt )C

ff'l
Avg. Zero Response, Zavg (01v)
- {Zf + Zf)/Z
5"-°

s:o
0
4.0
Avg. Span Response, S8Vg (01vI
» (Si * Sf)/2 ¦

JPt.if
eft 0


Zero Drift, il) * (Zf-Zi!
o
>r
0
a
6.0 .
Span Drift, (5) » (Sf-Zf)-(S-j-Zi)
O I
• 1
ISO
0,0
!¦'2-
¦i.l
B-61
-------
INSTRUMENT CALIBRATION
WTE 3 ~t 7	Plant UjY(7i)^/C
TEST NO. 		Operator 0 ?( ,
TIME OF IMITAL CALIBRATION /? foC
TIME OF FINAL CALIBRATION -\\fi

mx
CO *
CO 2
°2
SO£
Span Sas Concentration, Ss
tn, i
let. f
nn
t-o

Initial Zero Response,. Zt (D1v)
5~7 0 -

S~< o
P< 0
tC . zc

?r-/r
%c^
Vj,0
Zero Drift, {%) - (Zf-Zt}
t>
9
o
°<7
0<0,
Span Drift, (%) » (Sf-Zf)-CS-j-Z-j 5
-O, I
-0,7-
-1-7
o. 3

B-62
-------
INSTRUMENT CALIBRATION
DATE c* ~ I 3 \	Plant U/NL'¦'] D 4

O
-o.l
0.0
Span Drift,. (I) '¦ (Sf-ZfMS-j-Zf)
~o. 5"

i.0
D, I .
"1-t
B-63
-------
APPENDIX C
TEST DATA
C-1
-------
C-1
COMANCHE
GASEOUS EMISSIONS DATA
C-2
-------
Comanche
Instantaneous readings
N0X vs OFAf open © constant 02 -12/12
Test Dates
12/7/84 1345-1615; 209-265 MWe; 3.2-3.4% 02; OFA-Closed; "2A" MOOS
12/8/84 930-1130; "2A" MOOS; 152-286 MWe; 3.2-3.4% O2; OFA-Closed
1300-1600; 252-269 MWe; 3.2-3.41 02; OFA-Closed; all mills
12/10/84 830- 930;	334-360 MWe; 3.95-4.05% 02 OFA-Open; all mills on
1000-1330;	296-345 MWe; 2.7-3.95% 02; OFA-Closed; all mills on
1500-1600;	261-273 MWe; 2.75-2.9% 02; "2A" MOOS, OFA-Closed
1630 ;	281 MWe; 3.0% 02; OFA-Open; all mills on
12/11/84 1100-1430; 257-263 MWe; 2.5-2.7% 02; OFA-Closed; all mills on
except 1300
12/12/84 800-1430; 290-321 MW; 2.5-2.75% 02; OFA-Closed, all mills on
OFA - normally open 18%
C-3
-------
Comanche
Overfire Air
12/8/84 9:10 N0X ports	closed
12/10/84 9:40 OFA ports	closed
16:15 OFA ports	opened
12/11/84 16:15 OFA ports	opened
12/12/84 OFA Test
750 OFA
Closed


lOpen .
Time
Load

10
1445
270 MW

20
1455
295

30
1505
291
avg. load = 298 MW + 8.7
40
1515
285
t
. 50
1525
294
1
60
1535
302
+ 2.9%
70
1545
315
rel std
80
1555
305
dev
90
1610
295

100
1620
293

Normal
1628
305 MW

tf/out 315 MW
avg load = 296 + 6.7 = 2.2%
C-4
-------
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C-6
-------
GAS CONCENTRATION CALCULATION
Date /7- *7 j-10 ~ . Operator 			 Avg Gas Response, Davg
Test No. 		Actual Gas Concentration, Ga = (Davg-ZaVg) x Gs/(Savg-Zavg)
///	Gas Concentration-® Q%, Ga@0% = (G^ x 21)/(21- )



NOx

CO


co2
°2
so2

TIME
LOCATION
Davg
gA
GA0Oi
Davg
Ga
GAeo%
Davg
GA
Gam
Davg
Gd
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Davq
Ga
Ga0O%
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-------
GAS CONCENTRATION CALCULATION
Date	{¦% - /(J-fr- y Operator 		 Avg Gas Response, Davg
Test No. 			Actual Gas Concentration, Ga = (Davg"zavg) x. Gs/(savg~zavg)
t+t PP*/o,'>	Gas Concentration-0 Ofc, Ga@0% = (G^ x 21)/(21-%02)




N0X


CO


co2
02
so2

TIME
LOCATION
°avg
GA
GA@0% I
Davg
gA
ga0oxJ
Davg
GA
Ga@0%
Davg
Gd
Ga@0%
Oavq
ga
Ga0O%

OTOO-
OGOO

yr.v
loH
7 rA

; ?i
irU
£6.r
ir.r i
if, ra
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n,o
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-------
GAS CONCENTRATION CALCULATION
Date	j£~l j — Y y	Operator ' • -	 Avg Gas Response, Dayg
Test No. 				Actual Gas Concentration, Ga = {Oa¥g~ZaVg) X Gs/(SaVg-Zavg)
t+1 j-ttfiHfpw	Gas Concentration-0 0%, 6a@Q* - (r,^ * 21)/(2l-%02)




N0X


CO

co2
02
SOz

TIME
LOCATION
Davg
Ga
ga®q*
Davg
Ga
Ga§0%
Davg
GA
Ga@0i
Davg
Ga
Gam
Dava 1
gA
ga»oi

0OlO~
01 la


•

hi.r
Jt 1
Lf^ t|

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9 H
no
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32.. 0
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ni
H-
to
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73
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if. r
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-------
GAS CONCENTRATION CALCULATION
Date	/1 -/ / - Sr V
Test No.
Operator
i	
Avg Gas Response, DaVg
.Actual Gas Concentration, Ga - (DaVg~*avg) * Gs/^savg'zavg^
Gas Concentration-0 01, Ga@0X = (G x 21)/(21-%0 )
A	2
TIME LOCATION
NO*
CO
"avg
gA
Ga0O%
Javg
ga
co2
°2
GftBQl | Dayg GA GaQOl Davg Ga Ga901 ^avq G^ G^fiOl
SO?
l^-11
a.l\
1 r1'
t-aOO -
t IffO
J-X06-
nod
1^9
a
-11
WO-
XHod
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W -
0100
010»'
oloo
Oi-oo-
oi>ao
0100-
o-iio
prod
)V'
OSTJ0-
00 cd

StQO-
OlOQ
\>-
Ay
a too -
10 00
Ioto-
110 0
vy. I
7Aj

1H
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H 3.o


^7
iri \19.0
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ll»
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Ul
V70
H)ro
3U
1, t I

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(f (,?
(For data on CO2, 02> and S02, see page C-ll)
-------
GAS CONCENTRATION CALCULATION
Date	ll-ll-f
Test No.
Operator 	
Avg Gas Response, Davg
¦ Actual Gas Concentration, Ga = (Davg-Zavg) x Gs/(Savg-Zavg)
Gas Concentration-0 OS, Ga@01 » (G4 x 21)/(21-10 )
A	2
TIME
LOCATION
N0„
CO
uavg
Ga G^BOl I Dgvg G^ G^0O% I Davg
I co2
o2
so2
[ Davg
GA
GaGOl
Davg
Ga
Ga601
°avq
gA
GAeoi
bv,r
Z7./3
11,%
7 o.X


3j~>~
3(7 3'

7*r

lli~Z
3o.r
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71?

i ?,r/
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/ W
i 0 (

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333
7 h?
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3-/9

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x/ r
n •) i)
iz r

(7,30



11*
<5
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/d
140
3V3
ii-r
17,/)
/ f.rr
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x?r
33?
fS-'d
p?}¦

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»-'v
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tiQO'
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,K
Av
^ loo -
\Q 00
torn-
IIQQ
(For data on NOx and CO, see
page C-10)
-------
GAS CONCENTRATION CALCULATION
Oate	li—(-fr*/	Operator	 Avg Gas Response, Davg
Test No. 	¦	Actual Gas Concentration, Ga «. (Oavg-ZaVg) x Gs/(SaVg-ZaVg)
Gas Concentration-0 OS, Ga§QX = * 21)/{Zl-XOg)



NO*
	
CO
	:	
C02
°2
so2

TIME
LOCATION
°avq
gA
GA0OX
°avg
fiA
ga§gs
0aVg
GA
GaBOf
Davg
Ga
Ga0OS
Davq
GA
GAeo*

1UH •
tj-oa

HtS
Hit
PO i
Sr, e
Co
ft f '
1/.0
ICS*

¦J/, r
ur

xr.%
2JZ
K,(<

i-
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lu
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sv?
7>r
ro
r) !
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tvu
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ma

Hk*
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mc


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mr
sr.o
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ilf


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ifed
/
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73- o
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jf. r
$6 f
2'SI

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/(,.)&
If,<(7
lf'0


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12i

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3.r
itr
r7 H
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j/,r
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3) 1
lil.o
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;yy
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tl.Lt,
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HO
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Jiiea-
xyeo

lu-
jfi
i n
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i2(T
7fQ
p,J"
If>21
itt? f
n>f
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01 BO

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Hi
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r.?3


i7 r
i ~j r
-------
GAS CONCENTRATION CALCULATION
Date	!%-! 3 -	Operator 	 Avg Gas Response, Davg
Test No. 			Actual Gas Concentration, Ga = (Davg-Zavg) x Gs/(Savg-Zavg)
Gas Concentration-0 01, Ga@0i = (G^ x 21)/(21-%02)
TIME
LOCATION
N0X
CO I C02
°2
so2
Davg
GA
GAm
Davg
ga
G^@0Z | Dayg
GA
Gam
Davg
Gd
Ga0O%
Davq
gA
GA0O%
vioo -

¦>7-r
m
lit
y r
10
t7
oiiO
r-M
/W
01. o
*0

lUt
G7'0
6-/?

A/O
/ A/ K


01 »0-
vioo

n.r
iki

ii. r
K-d
If ^
Gi-r


(/GO
Co
ii
-------
INSTRUMENT CALIBRATION
/ 2 ~7 —	' Plant	C,o/^i4~/vc/~i£T
TEST NO. /		Operator 0 , C >	
TIME OF INITAL CALIBRATION	f 3 HO .	,
TIME OF FINAL CALIBRATION	/£ ^ (Z*>s6tr
# -2oo o
1

NOx
CO
co2
02
S02
Span Gas Concentration, Gs
s
fo-i'
W. f
/3. yi

Mo
Initial Zero Response, Zj (Div)
jT <£5
S-'d
.
¦ 5- d

V* $
Final Zero Response, Zf (Div)

5". (7
r.i
y* r
^3-
Initial Span Response, S-j (Div)
f&, y
f. d
ff.j
f f '6
f r< o
Fina-1 Span Response, Sf (Div)
rr. i
Jl^'O
ff.l
$T< Q
/y,r
Avg. Zero Response, Zavg (Div)
- (Zf + Zf)/2
¦?<&'

r./r

5- /$""
Avg. Span Response, Savg (D1v)
= (Sf + Sf)/Z


?ST'6>r
ff'O
£
-------
INSTRUMENT CALIBRATION
Plant Co/H&fcHer
Operator Q, c .	
til RktJgg~
0 -2st a
/

NO*
CO
C02
°z
S02
Span Gas Concentration, Gs
rtj-i
Ho i, f

f, <3
Mo
Initial Zero Response, 1\ £01v)
S~ a
S"-d
s" <3.
C-6
S". a
Final Zero Response, Zf (D1v)


r.*>
y. r
*3
initial Span Response, S^ (Div)
f Ci>4 )
' 2 n 4
4
?-> >d
f b~> o
Final Span Response, Sf (Div)
fT. 1
A?>o

£f> o
ry.r
Avg. Zero Response, ZaVg (Div)
* di + if)/2
¦
5 id
r>/r

sr-'*~
Avg. Span Response, Savg (oiv)
a (S-f + Sf)/2
h~'
Zf'O
9 ir- & f
ff'O
>7f
Zero Drift, (i) * (Zf-Zf)
$-0
0.(3
0*1
-
-------
INSTRUMENT CALIBRATION
DATE / 7 - ? -	, Plant Ctf/tj /yg. # £T
TEST NO. I			Operator D. $ ,.C
TIME OF INITAL CALIBRATION	\~?6 i
<7'Of. 1
/JYr"
¥'
Initial Zero Response, Zt (Div)
&~'d
ro
9f'?
£f7o
$s-
Zero Drift, {%) = Uf-Z\)
<£>./
-AZ-
0 'O
-£>. 5
-0.2-
Span Drift, (I) ¦ (Sf-Zf J-CSfZt)

0.2—

.a, t
-2. .3-
C—16 i
-------
INSTRUMENT CALIBRATION
DATE • / 2 -- S" -ST Y •	Plant rj)^JtA/Cl-f-tr
TEST' NO.		""" ~~~	Operator f), g,c -	
TIME OF INITAL CALIBRATION .J 9 ${j
TIME OF FINAL , CALIBRATION jjlf

N0X
co
co2
02
S02
Span Gas Concentration, Gs
ftf.Y'
Hdt. ?

9*0
?*d
Initial Zero Response, Z-j {Div5

f.d
9-d
5" d
3"- d
Final Zero Response, Zf (01v)
r,: d
jr. o
6
r, j~
r. a
Initial Span Response, Sf (D1v)

Af.d
?9

F1 na-l Span Response, Sf (D1v)


?%/
9f' Q
7/r -
4%-o>S~
sr. 3
$8-o
Zero Drift, {%) - (Zf-Z,) ,
o. °
Q.O
o.o
0-£—
£).C.3
Span Orlft, (%) = {Sf-Zf)-{Si )
£>. 7-
o.o
D-1
OA
-H-O
C-17
-------
INSTRUMENT CALIBRATION
J
DATE
TEST NO.
TIME OF INITAl CALIBRATION
TIME OF FINAL CALIBRATION

Plant CaMfr/VC/f£T~
Operator ft 	
0 ~7"Xi

N0X-
CO
CQz
02
so2
Span Gas Concentration, Gs
¦i'
frf.9
ja'93
?. C
fgd
Initial Zero Response, Z-j (Div)
r.d

s • &
^¦o
!T, &
Final Zero Response, Zf (D1v)

o


$< c)
Initial Span Response, Sj (Div)

^0
ff. r
TT-0
ff'O
Final Span Response, Sf (Div)
•?

V.d
f S~ 0
. $
Avg. Zero Response, Zavg (Div)
¦ (Zt + Zf)/Z
Gd
$<0
r. o
CO
f.O .
Avg. Span Response, SaVg (D1v)
- (St + Sf)/2
K'Or

n°i
?f>0

Zero Drift, {%) = (Zf-Z,)
0*0
O-o
0 . 0
o. a
a. o
Span Drift,. (J) - (Sf-Zf)-(Sf-Zi)
-0
-------
INSTRUMENT CALIBRATION
Plant /-/ /t
Operator • p 	
O 7 9	....
tt.ro

MOx
CO
C02
02
$02
Span Gas Concentration, Gs


n-j\
r-d
/*&
Initial Zero Response, 1\ (D1v)

f' d

a
5" O
Final Zero Response, Zf (D1v)
r*o
¦s\ a
T-c?
r. 3
 s
r. o
r./r
M.I
Avg. Span Response, SaVg (01v)
s (St + Sf)/Z
?G'l
-------
INSTRUMENT CALIBRATION
DATE	! X ~10 -f ¥ ¦	Plant C.0MA-/rcH6T
TEST NO. V'		. Operator V (Td	
TIME OP INITAL CALIBRATION ( 10 f
TIME OF FINAL CALIBRATION o 73C

NOx
CO
co2
02
S02
Span Gas Concentration, Gs
iO. 
f • a
Final Zero Response, If (Div)
5"-C7
y>*
Jt t
i~ o
r- 0
Initial Span Response, S-,- (D1v)
fc.r

f% 0
rr< o
17,d
Final Span Response, Sf (Div)
rc.Y
iw
/ 0 1,0
m

Avg. Zero Response, Zavg (Div)
« (Zt + Zf)/2

'hs\
fr'd
fro
S~> 0.
Avg. Span Response, Savg (Div)
- (Si -i- Sf)/2
$-(,£> r

(o a
?Y 
-------
INSTRUMENT CALIBRATION
DATE	.	Plant	Lf'
TEST NO.		'	Operator Q u c	
TIME OF INITAL CALIBRATION Q 7 5"~d	....
TIME OF FINAL CALIBRATION	/ C. / f

NOx
CO
C02
Og
S02
Span Gas Concentration, Ss
8fP. Y
vw. i
J7-¥J
P-<7

Initial Zero Response, Zf (D1v)

5" a
fio
r*o
P' *
Final Zero Response, Zf (Div)
f< o
¦C, I
 i

Fi.f

Avg. Zero Response, Zavg (Div)
- Hi + Zf)/2
<^TuO
¦5" Of
r<3f
tj.Yf
/"id ;
Avg, Span Response, SaVg (Div)
- (Si + Sf)/2



ti-7f
K-7*~
Zero Drift, (%) » (Zf-Zj)
O'O
0. t
o.7
--0 -3
0-0
Span Drift, (%) * (Sf-Zf)-(S1-Zt)
-c -X~
0>O
-0-r
-o-%
- /.r
C-21
-------
INSTRUMENT CALIBRATION
DATE }7~f f~ fry	Plant r.J mam c iter
TEST MO.			Operator p u~c_
* TIME OF IMITAL CALIBRATION	; (c£ 7 -	- ,, ,
TIME OF FINAL CALIBRATION	o 7Z 5"

NOx
CO
C02
02
. so2
Span Gas Concentration, Gs
	r
vj.'h '
Hot, f
x y;?
0

Initial Zero Response, Zj CD1v)



r*. 0
r.o
Final Zero Response, Zf (Div)
S~ &
"iA
5~ > X.
jHC
y, x_.
Initial Span Response, $1 (D1v)

H,o
n,o
gr.o
??, a
Final Sp^n Response, Sf (Div)

fcf
io/,0
Fr.t
n.i'
Avg. Zero Response, ZaVg (Div)
- (Zi + Zf)/2

H$r
r > i
it < 0
r, i
Avg. Span Response, SaVg (Div)
» (St + Sf)/2
?t.r
H'lr
la O'O

#,?r
Zero Drift, {%} = (Zf-Z,)
0,0
—Q • f
0'
0.6
a-X
Span Drift, (%) = (Sf-Zf)-(S7-Zj)
<7.7
(? " (#
hf '
O'Q
-O : ?
C-22
-------
n-'-f.
•4-%
1 ! 0
INSTRUMENT CALIBRATION
Plant CdA^A-^C/fE
Operator 0 c<-	

N0X.
CO
CO2
°2
S02
Span Gas Concentration, Gs
S7*y '
W, f
.
7T.O£~
fl.o
gr.o
8L>. ^
Zero Drift, (%) - (Zf-Zi)
0.0
0.0
-6.2-
o*(
Q'O
Span Drift, (%) »• (Sf-Zf)-(S1-Zi)
<5-0
©J
-3,8
-0, (
-L.
-------
INSTRUMENT CALIBRATION
DATE / 2 -/X - $¦ Y	;x/;i/gf	Plant C&M A
TEST NO. 	cV 		Operator 0(T C.	
TIME OF INiTAL CALIBRATION	/ G J~ 1	....
TIME OF FINAL CALIBRATION	01.

NOx
CO
C02
°2
so2
Span Gas Concentration, Gs
				"T
¥'
Ho t, <=f


%* Zo
Initial Zero Response, Z< (Div)
r.0
r.
5T<7
-ssBuy
( '
r- o
Final Zero Response, Zf (Div)
r- <=>


r:c>'
r.?
Initial Span Response, S-f (01 v)

A?
??.¦0.
Avg. Zero Response, Zavg (Div)
• (Zf + Zf)/2
z.o
Co
r. 2-

"ctr
Avg. Span Response, Savg (D1v)
a (S-j + Sf)/2
&-3

fof.o
£.s~ 3r
8c?r
¦ Zero Drift, (?) - (Zf-Zii
O ¦ o
o ¦ o
0-"4-
O .o

Span Drift, {%) * (Sf-Zf5-(SfZt)
Q.o
£>•!
3.6
£>.y

'7f
" '.I
C-24
-------
COMMANCHE DATA SUMMARY
WITH POINTS TAKEN OFF STRIP
CHART TO CORRESPOND TO
INSTANTANEOUS CONTROL ROOM READINGS
C-25
-------
f#sl|
-'' r!4
J)aia. •SuM.iM.&ry

 >
•5 ! 1 A'y
m°A

po/tJT
j jJWBER
loa-d
mk
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MILL
OUT OF
sew ice
• %
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PfO^Dt
CO
PpM&JCV

i /VjT
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1; £?0
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C-26
-------


oio
f
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441
57 ¦
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334
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til
-
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4f 3
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ns
Hi#











V
C-27
-------
c O - Hi &*«**¦ kt	|
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(jm*lkpflfk -SomrA&v-y
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OUT OF-
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+ • " I" 4h>
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C-28
-------
^rDeck. ¦5uiv\M&ry


poi/JT
fijtitjBER
LOAD
mk
CCftL-
' FLOW
'^r
MILL
OUT OF
SEJWlce
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to
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1
1 C-29
-------
r
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r
Ma- SuMPA&ry
PO//JT
tfWBZR
LOAD
MV4
C6WJ-
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OUT OP
sew ice
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C-30
-------
POl/JT
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& \fiOQ
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! '4 JO
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LOAD

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C-31
-------
r
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C-32
-------
Exxo/U -	pfife. luminary
		 impQt 		
- pbffJT
tJOHBtR
LOAD
mk
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OUT OP
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r C-33 .
-------
C-2
COMANCHE BOILER OPERATING DATA
MONITORED BY B&W SERVICE ENGINEER
~ C-34
-------
pt A-aTT OfrP A Ti*J<5 1>Q TPt
DATA ITEM
UNITS

2-








Test No,


e>rJLGAt>
OCHAMP
—


	Sp.
Date






	^
Time
Hours

toSo
/o vr
f t°t)
Ulo

UJJtT LofrD fi£&55
Mm)

AM
2 7*
"2 %0
2.7?. ?



tor^puTOl





boiler TEMPERATURES

I PeinlTS}




.

TF
€SD€)1
Hhf.o
M t> 1,3 x
*4kO,*!
fTl.q -j

Water fcvg Ctuiv
. F
n>n
ry/.f

¦ 5ir».z.
>'¥
ln-i
inn
(^0 (a
Lot,7

Stm Lvg RH Attemp
F
(SlO

$ST>.7
' S 7,1.1
sm z.

Stm Lvg RH
F
( (r&2')
toil.Z.
tot&lf
to o(. S


Water to SH Attemp
F
(SOI)
.2-6/. 3
2LI.I
2-42,o
1U M

Water to RH Attemp
F
( TO"?)
"U/,3
7.4 2-. f
2-6 2.t ©
T.62.,1.

























BOILER PRESSURES







Water to E con
PSIG
C6e»SO
ZUc.S-
It ?0, i'
I £.7 Ai'
«. W.J'

Drum Press
PS1G
( 6o£)
¦2-S3I-L
2-iTll &
W2-V. j?
^i'17.7

PSH in Press
PSIG
—
—
—
—
—

Stm Lvg Sec SH
PSIG
boi

23H.J

1 v iH

























HIGH PRESS FW HEATERS





.

FW Lvg #1 Htr
F
—-





FW Ent #1 Htr
4'C
<"? }
129-s
\Z%'~
J2^L
¦ IZt'.tj

FW Ent.'#2 Htr
/ C
if)
! ro.r
m.r
/ J-O- z.
j 't..

#1 Htr Drain.
fC
(
izQ.l
'3V-2.
131.')
IW.l

#2 Htr Drain
t C
(
ibo, 3
isf.lt
iTI.g-
1 Co-1

Stm to #1 Htr - Temp
p r ^
o;
& 0%
6*7. i

b o o tS~~

Stm to # 1 Htr - Press
PSIG
£ap
¦ p
(lo>
SV43
5T2«°
WW
3-v?,r

To & 3 ftT£
fstc.

i/VO
<4Ho •
430
H30

Q6/UZ*eai7''eg-f£i ^ ~ i?r? '«1 *17.7htF
cAs-ro*»rf » p«4«"uc Seitv/iar *F" ou>/2Aps
P^Cflto Co LotSA-d o
BV: 5VT.	1
C-35 I,
-------
DATA ITEM
UNITS

2.
Ok) i-OAH








| Caajbli 1 *W»
Date


t»rw*AJO
W7/W



	^
Time
Hours

tO 3o

Hoo
ft 30











L*Mf>uTg%





AfR & GAS TEMPERATURES

(Pw&?)


-


. fJuffiaKljrgEcaB
T


Tofc (



Ftee Gas Lvg AH
T
120/20

2i7/iiT-
ZltMf tfrW
210,1/272.

Flue Gas Lvg Hot Precip
F


ST,H'It6f
frj.tfse.

5
Flue Gas Lvg Pri AH
F






Air Lvg FD Fan
F
(

70.7/79.7

7V/7V.3

Air Ent Sec AH
F
(mhs)
wt'tha.i
itfjjtf
1 USftl*t>


Air Lvg Sec AH
F

£)<4 /ST)?„


'' Tis-i/mi

Air Lvg PA Fan
F
— 1





Air Ent Pri AH
F
-





Air Lvg Pri AH
F
—





Air Ent Pulv
""F
—





Ambient Air
F
fiKixn

S4.-S-
Tf.a.
Ci.t

















MISCELLANEOUS







feedwater Flow
LB/HR
(loz)
1 7f J.
1 <7 f, 6
iTU-t>


SH Spray Flow
LB/HR
f lo H)
—
—
7, <5
%.1V

RH Spray Flow
LB/HR
(71? 3 )

3?."' 1
4L3
"W.?2

SH Spray Valve Posit
%






RH Spray Valve Posit
%






* HP Extraction Flow
LB/HR



.4-	


O2 Lvg Econ
%
teoUstv
s./
i-nfj-ir
"it ih.Hi
1*7/3.2./

COj Lvg Econ
%



1


NOx {if avail)







02 Lvg AH
%






CO, Lvg AH
%






Oj Lvg Hot Precip
%






CO2 Lvg Hot Rrecip
¦ %






Oj in Windbox
%






C03 in Windbox
%






NOx or CFA Port Posit







+ Fuel Analysis







Burner § Out Serv




-


Relative Humidity
%







































Advise location of flow nozzle with respect to SH and RH spray take-off.
* ... Any bigH pressure steam extraction upstream of reheater, excluding FW heaterv
+ - Report data available - specific requirements will be requested.
£2). Efficiency data
2
C-36 ,
-------
DATA ITEM
UNITS

- z
0AJ LOAD




Date


DITMAHlO
U/1/M



>
¦		
Time
Hours

1030
to<4<
ifoo
Ulo

















DRAFT LOSS DATA







FDfan Disch
~Wg






SCAM In ©at)







AH Air In
"Wg






AH Air Out
" Wg






Windbox
"Wg






Furnace
" Wg






Econ Out -
"Wg






AH Gas In
"Wg






AH Gas Out
"Wg






Pracip In
"Wg






Precip Out
"Wg






ID Fan In
"Wg






SH Outlet Leg TC's
F






RH Outlet Leg TC's
F






























PULVERIZER DATA







Pulverizer #







* Coal Flow TOOz/,H
«i r i-r I1 t rt
*73
MD.Zt
Wo.sH

>HL 07

* Pri Air Flow
MLB/HR






* Sec Air Flow
MBL/HR






Pulv Amps
AMPS






Pulv Diff
" Wg






PA Inlet Temp .
F






Pulv Out Temp
F






PA Flow Damp
%






PA Temp Cont Damp
%






Pri Air Fan Amps
AMPS












-

































































The DRAFT LOSS DATA listed on this page is of value, but not absolutely essential for performance analysis.
* - When indicator scale is in different units, provide conversion factor.
(?)- Efficiency data
C-37
-------
fLA-frt ofSKb TttJ6 DflT4
DATA ITEM
UNITS

z

	7s	
1— I tefc
Test No.


LuJtJ o>4
Lofio Ob

-oZ/ow4,Hr 2/0
Date


12 f'lt&f


	1	*-
Time
Hours

¦Mr
}4o°
/wr
/f3o |/Vir'J-
IcUlT LaAt> &e.o Si
Mu)

Z b5~
2S~1
257
25^
ZZ7


^ih,m





BOILER TEMPERATURES

(Pmi^rs')





WnnHBDSB
f
iS&D
vrv.r

•4XD.4
^TO/7

Water LvgEcon
F

svz-r
•rSr. f
5If-/
S7o. t

Stm Lvg Pri SH
F
'5\ozy
1VZ.H
fllb-l.

Hr.fr
-V.1-
Water to SH Attemp
F
(•j on)
W*
ZS'7.7
1*1.1
1ST. 7

Water to RH Attemp
F
(Oi)

%PJl4
"hZZb-tJ
%st(>. 7
T-flPJ
PSH in Press
PSIG
__
—
—

—
-
Stm Lvg Sec SH
PSIG
hot
?-V o 2." '
/ J". 4
tu o'-f.z.
llfo.l
XMof-3
RH Inlet
PSIG
bo 4
vu.r
V2-/• 9
t-tilM
>411,7
"?r ^
RH Outlet
PSIG
ioi
177."U
1t4,L
ia.9

1/M
























HIGH PRESS FW HEATERS
•






FW Lvg #1 Htr
F






FW Ent #1 Htr
4 O
o )
fZ7
1 2 (y
IZG
t z C?
fZ3
FW Ent 02 Htr

(5")
tin
f*/1
1*47
-I<47
IHH
#1 Htr Drain
f C-
C 4)
132
)3z
111.
131
n?
#2 Htr Drain
f C
L&)
1 r* •
!S7
/S(,
l'~7
IS 3.
Stm to #1 Htr-Temp
F „
11}
52Z.
T?7
Sb%
S6>«
r&7
Stm to #1 Htr - Press
PSIG
local
G7


6>S"

Stm to #2 Htr -Temp
F
a)
?7J_
. 1L9
7rr
iyo
7J-7
Stm m #2 Htr-Press
PSIG
Lo^AL
/ fc3
the,
i S" is
ir *
¦ 1H2.
C-T *3 tirfi- r£>£
6
(?)
/»?
n ft
nn
73 9
?Z&
stm To #3 T&*t>
P
(IQ>
'sir

i'S'3
5ff
	F?7 .
STm To * 3 ti-Tt
psit.
t m
H to
1400
460
4oo
370
Nu
Chs-To*i£Z '
By; siff-
p«,6ut sew>c£ ° f c*>u>eAPo
pH-E BLO Co Loft AO <5
1
.'oft

sta&teo
t>£C. 1. /fIV
0<1€R£<(Z£ A-irZp^T^ <^-<>SCb
Af lyoot-bls.
C-38
-------
DATA ITEM
UNITS

2



i



" ^ j
Test No.







Time
Hours

iy?{ri
,3*'r

/HIS
( V 3o
/VQS
















AIR & GAS TEMPERATURES

(PvjjTS )





} FIueOasLvgEcon
F
(2*/2S>


TK/ZU.
zuivn
r(,6/f?r
Flue Gas JLwg AH
F
C2*/2n
zbrmn
zulus"
m'M>7

-iif/ibr
Flue Gas Lvg Hot Precip
F
(2l>/27)
SWjS^
$y 7 Isn f


s-w/n?
") Flue Gas Lvg Pri AH
F






Air Lvg FD Fan
F
(
79 j fo
1
?l I fx

s ijis
^ Air Ent Sec AH
F
(t<4hs)
mini

rzyinl
Itij

") Air Lvg Sec AH
F


svl/svr

mlsQt

Air Lvg PA Fan
F






Air Ent Pri AH
F
_





) Air Lvg Pri AH
F
—





Air Ent Pulv
F
—





Ambient Air
F
ft% CT)1
Af.V
-------
DATA ITEM
UNITS

2








Test No.







Date

*

-		



Time
Hours

1
mo o

N 3>o
/Vi/r


COMpuTO







PotA/U





DRAFT LOSS DATA







FD Fan Disch
"Wg






SCAM fo Out)
~W|






AH Air In
"Wg






AH Air Out
"Wg






Windbox
"Wg






Furnace
"Wg






Econ Out
"Wg






AH Gas In
" Wg






AH Gas Out
" Wg






Precip In
" Wg






Precip Out
"Wg






ID Fan In
*' Wg






SH Outlet Leg TC's
F






RH Outlet Leg TC's
F






























PULVERIZER DATA







Pulverizer #







i * Coal Flow
MLB/HR

i5lK>
1 5 f.7^
i Jl*"?
i-M.tr

* Pri Air Flow
MLB/HR






• Sec Air Flow
MBL/HR






Pulv Amps
AMPS






Pulv Diff
"Wg






PA Inlet Temp .
F






Pulv Out Temp
F






PA Flow Damp
-%






PA Temp Cont Damp
%






Pri Air Fan Amps
AMPS






UiLI A CoAl/fiO? TO" i3
F
(tk ^
mill
Z-A
opf-L-
/ajvT —

rt c.ofrLJfh)i -£>«p
P
n-r\
' US-
//&
uy
!
-------
pLA-nr Of>eK67ltJ6 Of\Tk
/ • DATA ITEM
UNITS

/
2








Test No,







Time
Hours

r *-l */gl>
15" Oo
/J"/ 5"
ISZ°
/svr
/b/
mui.
mirr

'-fiX.'i

Water Lug Econ
.... jj..
(3m
£2-1,7
t^Z-1-l

57o.7

Stm Lvg Pri SH
F
51 <4 /5-/S
U 7.1/7J2.
7JV //75 0


'-.il-"if-n.
Stm Ent Plat SH
F
L.
—
' J



Stm Lvg Plat SH
F
—
—
—
	
		
—
Stm Ent Sec SH
F
t7 / gy
nzihij
Will!
72W/72I
lls'/HZ
im/yz 1
Stm Lvg Sec SH
F
(  5
5/
5~¥3
$vs~
Stm Lvg RH Attemp
F
(stn
svr-r
rrz./
¦ p.f.5

$" 2- 3 o>"
Stm Lvq RH
F
( ko2^
9xf ?
.1U,r
moM
^n.h
^ 2-o.V
Water to SH Attemp
F
(JOl)



2. 3
wr r
Water to R H Attemp
F
( *T0"7)
"2- X i' 2—
i
w?.|
2-«*'£- 7
Mi'/
























BOILER PRESSURES







Water to Econ
PSIG
C 60S")
ZiSi'i
26ST.V
2Cl£,l
WJi.V

Drum Press
PSIG
( & )
UlS.i'
ZroJ.S-
2-af 1
T-t/jz. ^
2-^7^1 m,
PSH in Press
PSIG
_
—


—
		
Stm Lvg Sec SH
PSIG
60/
U4 e&' 3
1-1 f h?X
£bl
.TS'¥
s\r^
5-V/
Stm to #1 Htr ¦ Press
PSIG
Local
S9.



SH
Stm to #2 Htr - Temp
F '
t
IS- 3
7s -?
7 ¥/
1*43
72.?-
Son to #2 Htr - Press
PSIG
Lq£*L
'T¥X ¦
I 33
tzt
lit
12-9 ¦
fw E*JT *3
C
(7)
/JW
nn
HO
¦ (80
190
STM To * I HtR T&*{>
F
(10J
^9,
SHI
sit
Bio
5" 3/
STm To 8 3 H~r< PlE^
pSlC,

3 7o
IS'd 1 3 3 0
17>0
"W 0
C •(*> f*1 11°	Hsr l*r
CAsTo-mGie ' pM.GUC- S&t0
Presto Co Lo&At>0
BH; svf.	1
C—41
-------

DATA ITEM
UNITS

2








Test No.







Date







Time
Hours
















CtupuTgK





AIR 81 GAS TEMPERATURES

LP-furs)






- *¦** - i ¦¦¦ r.ni
~ ¦BBC 4MN
¥
(2¥/2T>
Sil/Sbl
SlrtfSlZ.
sssfui
ssiisn
z&frsb
&
s
(D
flue Gas Lug AH
F
(2* !m
lUlihi
ZUfzlo
zbiim
2bc/27Z
2$?/Z7 1
Flue Gas Lvg Hot Precip
F
(21,/27)
sVo /tvx

SKISM
sv*j j£"m
513/nl
Flue Gas Lvg Pri AH
• F ¦
	.

i



Air Lvg F0 Fan
F
( l2/l3>


> 6 2., . /
n-fhiA

(5)
©
©
©
©
©
©
©
Air Ent Sec AH
F

!2.q ?I3£
1 z?/fir
rhoim
IS l/il?
1V*//S7
Air Lvg Sec AH
F
dim)
sbs/.tosl
'
$oIm$



Air Lyg PA Fan
F






Air Ent Pri AH
F
, _





Air Lvg Pri AH
F
—.





Air Ent Pulv
F






Ambient Air
F
fiXC I>3
fn 3. 1
C 5.o
t,2.1
it 2 1 iT"
Srf,S~
















MISCELLANEOUS







Feedwater Flow
LB/HR
( 7OZ)
IHU.1
/•"/ff.o
I VIZ.*!
IW-L
IhlHtX-
SH Spray F low
Li/HR
( 75 ¥)
—

—
-
—
RH Spray Flow
LB/HR
(71>3)

. —
—
-
—
SH Spray Valve Posit
%






RH Spray Valve Posit
%






*HP Extraction Flow
LB/HR






Oj Lvg Econ
%
(3 ai/U!



2.n/i.n

GOj Lvg Econ
%






NOx {if avail!






-
Oi Lvg AH
%






COa Lvg AH
%






Oj Lvg Hot Precip
%






COj Lvg Hot Precip
%






Oj in WintiboK
%




_

COj in Windbox
%






NOx or CFA Port Posit







+ Fuel Analysis








Burner # Out Serv




-


&
Relative Humidity
%










































Advise location of flow-iaazzle with respect to SH and RH spray take-off.
* • Any high pressure steam extraction upstream of reheater, excluding FW heaters,
+ - Report data available • specific requirements will be requested.
G> Efficiency data
2
>421
-------
/" DATA ITEM
UNITS






Test No.







Date







Time
Hours






















DRAFT LOSS DATA







FD Fan Diseh
-m






SOW Tn fOuti
" Wg






AH Air In
"Wg






AH Air Out
. "Wg






Wind box
" Wg






F urnace
" Wg






Econ Out
"Wg






AH Gas In
"Wg






AH Gas Out
" Wg






Precip In
" Wg






Precip Out
" Wg






ID Fan in
" Wg






SH Outlet Leg TC's
F •






RH Outlet Leg TC's
F






























PULVERIZER DATA







Pulverizer #







* Coal Flow
MLB/HR
- % 13



11?.17
I3 7./7
* Pri Air Flow
MLB/HB






• * Sec Air Flow
MBL/HR






PulvAmps
AMPS






Pulv Diff
" Wg






PA Inlet Temp
F






Pulv Out Temp
F






PA Flow Damp
%






PA Temp Cont_Darnp
%






Pri Air Fart Amps
AMPS
r~






KffU A £cAL/P T£V-' H
* rlLTgV.-C
I-
F
Of- p
in
lib
li 3
iU
H7
C C^oAL lprt{L~TS?t»>§
F

1 22
m
(12
| 21
/ 2 Z.
O Co/it (Attl TE>,«
F


I0.L)
nr
<2^

€ 1 fill (i Tc>f
F

	
—
—

—
































The DRAFT LOSS DATA listed on this page is of value, but not absolutely essential for performance analysis-
* - When-indicator scale is in different units, provide conversion factor.
(2)- Efficiency data
C-43
-------
PMa/T	PA lf\
DATA ITEM
UNITS
2
-2 '
2.
JL
/
z.
X.
Test No.
Date

In l


»°TE(X>


Aj^r^d^

IUS7A/JT, (,(L*SS M"J


25Z. /?
2 32. J3

zef-ii.
•24 2, rj
, BOJJ.EB T£JM?£HATUfl£S







j fill 1 in Tiiw S»?
¦¥
^j.r,

•*/¥/,r
HS4.I-
LfS^.Z
Vi3.|
Water Lvg Econ Ji 1
F
S-Z6.9
S"56
S" 3 3 3
ST>Z:U

i'JV.7
Stm Lvg Pri SH S74- / fiS~
F
m.i/ng.i
islsfrsri
7W.f/W
Kfr.y??/,:
lh?.t>hn.A
~W&vh3l-
Stm Ent Plat SH —
F




	f-	^
—4^—<-
Stm Lvg Plat SH —-
F






Stm Ent Sec SH <7 / f
F
viifm-t
Wi.lfjvs-l
3
W2tm^

7^4/73?
Stm Lvg Sec SH f
F
1>ofe.7
1011.7

!0i7^
f?7
171,?
Stm to RH Attemp n
F

S
r?6.o
4/5,3
6eS"4
Slt>
Stm Lvg RH Attemp 5(1
F
svo-7
S"?2, ?
7
VWi
s"j r.?
sT?.3
Stm Lvq RH fooz
F
o$
PSIG
2A3 #•*/
ZbHl, M

Ibnt-H
ZhU.f
Z&(* V!• /

2 3^.3
Z3"?3.7
2393.?
RH Inlet £>°4
PSIG
326. I
3.r
























HIGH PRESS FW HEATERS







FW Lvg #1 Htr
F






FW Ent #1Htr 3
r c
lZ^-i
i 23,<5
? 25.fr
12 «.I

tl.1,2.
FW Ent #2 Htr $
f C
HSS
wsw


•7ST5,t/
frf.H1
#1 Htr Drain A
/ c
111.')
1 2-^.3
tzt-1
17Z
/-N.1
11 J. ft
#2 Htr Drain &
/ c.
1X1.1
J-Tf If
irZ.2.
if 7.9
Ho 9
/S7.i
Stm to #1 Htr - Temp |
F
581.i>

5-7^,7
6 og.Q
S-«fc'7
Sti.H
Stm to jC 1 Htr - Press l»v,l
PSIG
&o
4 2.
f 7
-67
~7H
67
Stm to #2 Htr - Temp I
F
its-
1M
7^.6
ftof.l

7«,9
Sim to #2 Htr - Press L *C L
PSIG
Hi,
IS~1
Wo
l&i
17 g
ib-L
Ful EtJT rtJ »(• H7£ T£MP 7
C
1 ?sT.f
Ht,. L
/f 3.?
/M.7
tfl.o
lfg.1
.CTMTo^H/'ffT* rrMP IIP
Ir
SS1-H

SLI.H
S"'7W
szb.s
sfcV.t
STM To #3 HPItrt. MESS Lm
L PS16
3 y®
Vdo,
2io
H-30
0
fzo
#3	vHAibi T£Mf» g q	i 86o , PUSBlo (Lat-o£flc>o .
Jo6 ^0. £i3-Soz-
^rg(£>. 3fW,#|T Z-A P"-L\J Uiifi Q *&$'-
'C-44^
-------
/?lAatt af>£f2ATi*i6
DATA ITEM
UNITS
. 2
2
Z
z
2.
2~
Test No.



-



UalC
Time
Hours
f 2./ c/»7
O ?PO
?95»
/0O0
I 03a
(fOO
ttZo
















AIR & GAS TEMPERATURES







) FJue Gas .L*g £con 2*4 (2!
F
znzkti-i

st? */m.t
asfjjbw
iet-iMoiJ.

) Flu* Gas Lvg AH ?o/z\
F

imJin


LSZ>£/iSi,^
p=T
1
1
) Flue Gas Lvg Hot Precip zihst
F

wtlsm

5-Jf-f/rv*«-
S5»-?/ra/
^"z/ss¥,i
} Flue Gas Lvfl Pri AH —
F
- —.

—
_


Air Lvg FD Fan iZ/l3
F
ftt/'jrg.i
n-*!rr- '*

. -?!$•}. 1
srvi/rU
si'i/rj, "5
) Air Ent Sec AH
F


iM.ljug.H
hU/ns
\oUho1-^
toi.rfH q.J
) Air Lvg Sec AH . 12/z3
F

&Z-tilth'
5T>l.tf'«fV.I


rn>v/sbi,(
Air Lvg PA Fan —
F

¦




) Air Ent Pri AH —
F'






) Air Lvg Pri AH —
F






Air Ent Pulv —
F






) Ambient Air )%
F
3 i
Ibic.f
SH Spray Flow
LB/HR
—
. —
—
—
___
—
R H Spray Flow fo "h
LB/HR
11.0 y
/*?, 0 •/
j-7.^r
V7.C7
2 3. 6-2

SH Spray Valve Posit —
%






RH Spray Valve Posit 	
%






* HP Extraction Flow —•
LB/HR






O2 Lvg Econ jobfao/
%
3, it h.o z

^.Iifz.13

3,is/3,/o
3.e2/j ,«1
CO2 Lvg Econ
%






NOx (if avail)







Oj Lvg AH
%






COj Lvg AH
%






Oj Lvg Hot Precip
. %






CO? Lvg Hot Erecip
' %






O2 in Windbox
%






COj in Windbox
%






NOx or CFA Port Posit

-





+ Fuel Analysis







Burner §¦ Out Serv




-


Relative Humidity
%






































Advise location of flow nozzle with respect to SH and RH spray take-off,
* • Any high pressure steam extraction upstream of reheater, excluding FW heaters.-
+ ¦ Report data available-specific requirements will be requested.
(2)- Efficiency data
"	2
Cmjto»v*eft •. pu^Jtic S&i/ieic Of ooL£>r2* 00 > pu.&llo C&lo&AOv
,Trt rt li.lt.JL4A*	-	0 r3 _ £? A*f
C-45
-------
PlAMT opei?ATi*& t>P, tA
DATA ITEM
UNITS





~
Test No.

)?/(?/ fiU





Time
Hours
0^00
O^3o
tooo
/03 0
1 too
'
!(~5D








• -







draft loss data





.

•TO FaaBiseh



-



1 SCttttntDuD
-*Wg






AM Air In
" Wg






AH Air Out
"Wg






Windbox
" Wg






Furnace
"Wg






Econ Out
"Wg






-AH Gas In
" Wg






AH Gas Out
"Wg






Precip In
"Wg






Precip Out
"Wg






ID Fan In
"Wg






SH Outlet LegTC's
F






RH Outlet Leg TC's
F






























PULVERIZER DATA







Pulverizer #







* Coal Flow %)3
MLB/HR
12?. 73
IZf.70
IZ2-17
izt-r?
IZf, ?&
/So .o?
* Pri Air Flow
MLB/HR






* Sec Air Flow
MBL/HR






Pulv Amps
AMPS






Pulv Diff
" Wg






PA Inlet Temp
F






Pulv Out Temp
F






PA Flow Damp
%






PA Temp Cont Damp
%






Pri Air Fan Amps
AMPS






Pul-J. 1-A
p
0 rp l
	


-4* ¦
nin
f.vn' C«sftl)PtulT£h'.3
P
os-f
115-2.
ili.U
usr

Its. s"
"l'c V" -
f
tn.i
i:«'1
tit,?
!l (, 1
IZh°
./*.»•«< .
pui \/ l-o ioAl'Ifiifi. Tip"p'
P
a z.7
tiz.l
Ilho
iti-9
IIZ.&
\tf-7








































The DRAFT LOSS DATA listed on this page is of value, but not absolutely essentia) for performance analysis.
* - when indicator scale is in different units, provide conversion factor.
£?)- Efficiency data
CUSTOMER« /'H/it-14 S€(t\Jic€ OF ( Col-otZ AOa , • pH.£/3LO, CoLO(ZAOO
Tkfl » >.» ... O rrfi	ft ft —	>
'•C-Mi
-------
pLflrJT	t?AjA
/
DATA ITEM
UNITS
2. ''










Test No.







Time
Hours
l£/2/rtf
\3 0£>
1330
/4/00
Ml#
/ST><3
	
tS3o
INSTAsTT, 6,0.oS5 MtO

Ibt-lq
25-3.zr
2?f.20
Zbtbsr
z.l4',U
*z$i,7r








BOJX.ER T£MPER ATUiLES







• mmrn-mSam - 5Of
¦ *
•4XZ.-, ^


-tyji/W
VTT.q
**3-5.3
Water Lvg "Eeon 3>t
F
5~Vo
511.1
s-v2-r
2.
syc.tj

Stm Lvg PriSH 514-/ fiS~
F


ibn/mM
7rz.f
S"2 3 .4

6oT-7
ioT's-
ZtrW^
«/
Drum Press bob
PSIG
TSlj. f
¦z-rtz-z
X'o7. e
2n1-i"
Z5t>0,i"
z^o-i
PSH in Press —
PSIG
-
_
— -
—
—
—
Stm Lvg Sec SH &ot
PSIG
ic/zS -6
22
^20
i/Ztf [ ¥00
PM« T£**f> g c IH3.? H6.6 iTs\T|13,£
GuSToMei?- P"f3uc Sept/|<^€ of CoLo/Z^Co , PueBL-a Cotoiwco.
To6 'Jo. *. #?8_5oz.
1
r
t
C»47j
-------
pt-AATf ' Oj>£j2ATIh3£>
DATA ITEM
UNITS
2.









		Cs*
Test No.







Date







Time
Hours
i~ioo
/3?o
ftfOO
mo
/5V0
is 3o
















AJR & GAS TEMPERATURES







) Fine Gas i-vs-Econ 24 tlf
F

SUSfoiaS
stzqafz.



) Flue Gas Lvg AH 2o/ZI
F
l&llXi-i
isSlfaV.i
.znkhss-i
ivtifrn-i
in.t/ia.i
iiJ.e/^0.4
) Flue Gas Lvg Hot Precip zUl-'t
F
rvM/rvi'¦&>
rwi sfrrt-3

ssi'l/ssv.?
sri-r/fTrt
s&t-i/sTtf.i
") Flue Gas Lvg Pri AH —
F



_
—
_¦
Air Lvg FD Fan IZf 13
F
uMlia
bt-HUA
ii.tfiz.4
U-i/'ii.i.
u-o/u.c
73.V/7/.?
) Air Em Sec AM
F


1
1H1/m, ¦?
ni^/iu.i
ii«.i i't^r
) Air Lvg Sec AH 22 fr3
F

.Sto.'l/W
(su$fmn
si'.'/raf.o
r;3 bmi 7
ritf.t/jbt.l
Air Lvg PA Fan —
F






) Air Ent Pri AH —
F






) Air Lvg Pri AH —
F




. _

. Air Ent Pulv —*
F






) Ambient Air it
F
Q*!>H

47.2
Mi".?

2, 4
mb. 7
/6 37. y
»rf2. ?
/sTf. ?
SH Spray Flow *10*4
LB/HR
—

—
—
¦??r
—
RH Spray Flow 3
LB/HR

—

13,HI
21?
lo.it
SH Spray Valve Posit —
%
—

-


-
RH Spray Valve Posit _
%
-
—
— .
—
—
-
* HP Extraction Flow —
LB/HR
-

-
—
. —
-
Oj Lvg Econ 3ot,jz°7
%
3,(1 h-r;i
3,13/2,?"

3-^1 I/}?

J .Olfj.oo
COj Lvg Econ
%



1


NOx (if avail)







Oj Lvg AH
%






COj Lvg AH
%






Oj Lvg Hot Precip
'%






COj Lvg Hot Precip
%






Oj in Windbox
%




_

COj irtWirtdbox
%






NOx or CFA Port Posit







+ Fuel Analysis







Burner # Out Serv




-


Relative Humidity
%









	




























Advise location of flow nozzle with respect to SH and RH spray take-off.
• - Any high pressure steam extraction upstream of reheater, excluding FW heaters.-
+ - Report data available - specific requirements will be requested.
Efficiency data
Cwjxci'vieT?.!	c S&li/lcg OF-	_ pu£(li~o Colorado
JoG MU+Mitm? i P ,5- ts nf
C-48
-------
Plajjt ofeRA-rins patA
1
DATA ITEM
UNITS
2 .
1.
z
z
2.
Z_
Test No.







L* uIC
Time
Hours
1 "boo
/ 33 0
ft/o*
/¥ 3

t JT3 0
















DRAFT LOSS DATA







' -FUFanDisdi





1
-SCAHfitfGoi}
-wb



1

AH Air In
"Wg






AH Air Out
"Wg






Windbox
" Wg






Furnace
"Wg






Econ Out
"Wg






AH Gas In
" Wg






AH Gas Out
" Wg






Precip In
"Wg






Prectp Out
"Wg






ID Fan In
"Wg






SH Outlet Leq TC's
F






RH Outlet Leg TC's
F











-


















PULVERIZER DATA







Pulverizer #







* Coal Flow % 13
MLB/HR
/ 3 0.72.
Ho,Ik
i3l, 0/
13131
/ 3 /x 1
f 3/.J-J
* Pri Air Flow
MLB/HR






* Sec Air Flow
MBL/HR






Pulv Amps
AMPS






PulvDiff
"Wg






PA Inlet Temp
F






Pulv Out Temp
F






PA Flow Damp
%







PA Temp Cont Damp
%







Pri Air Fan Amps
AMPS







Put (/ 1/4- :?"U* ?:
F
IZf.Z
126. 0
117, i
is 7.2
127,1.
l2f,"L

pML-V, Z C Zar'i/flul Tkr >'
F
116.?
12.9,0
121,1
iis>.r
nt.o
1X1.1

Put /- ^ £ C^lk:l.Tev,
f=
/22.¥
/Z3. 9
\lH-7
(2 <¦/ .2.
II^.L
/¦w.f

dCoP.ilktire- '
(5
It?, L
iu.y
m-H
(17,5
(Zl.7
iZj.f

"			 7. 1









































I
The DRAFT LOSS DATA listed on this page is of value, but not absolutely essential for performance analysis.
* - When indicator scale is in different units, provide conversion factor.
(2)- Efficiency data
3 _
cuStomEI' i3c<-iiL-ic S{r£(/t_or2./w>o t pn.£t$L.o, Colorado
Tr.O iiuutliTO	on. - *^r>7 1
C-49
-------
: -4 - ~ti
•^=1- ¦=	/\fJT cj't \ t mcj c?a f pf
DATA ITEM
UNITS
Z:
2




Test No,







Date


Mg/rt




Time
Hours
ibo 0
(&>30




xmsta*it <<;adS$ rviuj

ZTZ.IO
¦Zii.7 i




UsJlT 0 (J LoAO







BDJ1_EJ3 T£MP£HA.TUJiES







4 Wnlr* - - 5°^
- ,4:

•V^Z.7



•
Water Lvjjlcon 3IS
F
Sti»?
sirV.v




StmLvgPriSH S(4-/r(S"
F


W



Stm Ent Plat SH —
F






Sim Lvg Plat SH —
F
—
—




Stm Ent Sec SH 7 / $
F
7¥i h a-f





Stm Lvg Sec SH *?
F
loO ?
i&IM




Water to RH Attemp 5"o1
F
ZfT.g
z-khH




























BOILER PRESSURES







Water to E con £oS"
PSIG

ztn.f




Drum Press bob
PSIG
2wfr- 7
1. i't f- 7




PSH in Press —
PSIG
—
—




Stm Lvg Sec SH Uo\
PSIG






RH Inlet
PSIG

tfttt.i




RH Outlet C,o3
PSIG
•jxv. /.
H.t V 6.




























HIGH PRESS FW HEATERS







FW Lvg #l Htr
F






FW Ent #1 Htr 3
/ C
/zf-7
}%l.b




FW Ent #2 Htr " £
r c
IH7
IS®-#




#1 Htr Drain 4
r c
m-i
111,4




#2 Htr Drain 6
/ C-
1 rr-?
ls-1-7




Stm to #1 Htr -Temp (
F
5-7C.7
&




Stm to #1 Htr - Press
PSIG
64
7r




Stm to #2 Htr - Temp Z.
F
17 «.r
7? <7.7




Stm to #2 Htr - Press L »C^L
PSIG
/¦r¥
m




Ful £JJT S3 HP H7i T£mP 7
C
lf7-3
H1 ¦ 3




CTM To *3 HP Mte re-MP /£>
F*
m-/
sm.l




ST/U To *3rtPtrtiL PHESS Lou
It PSI6
t/00





*3 >+PlrtG DUfiin T£Mf 8 C 113.1	7'"?
tuS ToheiS: puliu C SEkiJice of CoLo/ZA-t>o ~	Coi~0»2/»OO
J06 ftJo. ; ^6-soz.
1
C-50
-------
iiilfe—

pL**rc operiATihi6 P^tA
DATA ITEM
UNITS






Test No.







Date







Time
Hours






















AIR & GAS TEMPERATURES







) FtoeGwt ajfrrw 21! faf
T






) Flue Gas Lvg AH 
LB/HR
i?
z?,jr




SH. Spray Valve Posit —
%
—





RH Spray Valve Posit —
%
—•.





* HP Extraction Flow —
LB/HR






Oj Lvg Econ jab
%
3 vh'Zai





COj Lvg Econ
%






NOx {if avail}







Oj Lvg AH
'¦ %






C02 Lvg AH
%






02 Lvg Hot Precip
% .






COj Lvg Hot Precip
%






Oj in Windbox
%




-

COj in Windbox
- %






NOx or CFA Port Posit







+ Fuel Analysis







Burner # Out Serv







Relative Humidity
%






































o

Advise location of flow nozzle with respect to SH artd RH spray take-off.
# - Any high pressor# steam extraction upstream of reheater, excluding FW heaters.
+ ¦ Report data available - specific requirements will be requested.
(2)- Efficiency data
"n672.: pu.|jLl£ So2i/[C(5 Or c*ol-0rt-A E>o pu.£fli~o d-OLO/JADu
C-51
-------
Plakjt ofeftA-rin6 oat A
- " DATA ITEM
UNITS






Test No,







Date







Time
Hours






















DRAFT LOSS DATA







fD¥mSmdx
Hl-
1*9



;


' -SWMtafiiwt)
"*9






AH Air In
"Wg






AH Air Out
"Wg






Wind box
"Wg






Furnace
"Wg






Econ Out
"Wg






AH Gas In
"Wg






AH Gas Out
"Wg






Precip In
"Wg






Precip Out
" Wg






ID Fan In
"Wg






SH Outlet Leg TC's
F






R H Outlet Leg TCs
F









-




















PULVERIZER DATA







Pulverizer §







} * Coal Flow %/3
MLB/HR
nt,5H
i.V'lf..




* Pri Air Flow
mlb/hr






* Sec Air Flow
MBL/HR






Pulv Amps
AMPS






Pulv Diff
" Wg






PA Injet Temp
F






Pulv Out Temp
F






PA Flow Damp
%






PA Temp Cont Damp
%






Pri Air Fan Amps
AMPS






fin Ll/ 2-A I »*;//>„••, Tpv-.p
r-
rif'i
127,3




•" "• 2-ft
F ....
114.1
127,7




?'C
f
|2i-j.i
iZq.a




2-0
f
12-7.5"
H7."





































-






The DRAFT LOSS DATA listed on this page is of value, but not absolutely essential for performance analysis.
*- When indicator scale is in different units, provide conversion factor.
(T)- Efficiency data
j _	_
CUSTOMER' pK/lMC S €fL\itt€ OF C«L0f2AODy	C*aLO(ZAC>0
Tn/?	®ifl? ''
C- 52
-------
pLfifJT '	-TIIJ6 . CAfflt
DATA ITEM
UNITS
2





Test No,







Date

'It-l/oJ fry


-


Time
Hours
O2oo
Og 3o
0 0

/e>0o
/o Jo
I/JSTAWT M<*J

iSL.t 5
33 V. H5~
lii'Hjr
360.3 r










ami FR TFMP£BATUfl£S







' . flfew£nm 'SB?'¦:J
¦ *
*mr?

Htnr
fir ..j
'ilia

Water LvgEcon Jtl
F
rs3.r
511 3
T?W
ffi/.Z-
ft"5. J
s%r. 7
Stm Lvg Pri SH $14-} nST
F
ns-.thsiri
nozjnU
Vi*hun
ni>ln7.o
7^fV/7xy./
7£i/ir7.i
Stm Ent Plat SH —
F
r *


1

¦		
Stm Lvg Plat SH —
F

—

—

—
Stm Ent Sec SH 1 / %
F
7 W.l/7lf,/
7 iuhsiM
7l»nhx. t
?? ilhib-1)
76o S/?i 7 7

Stm Lvg Sec SH *}
F

,-s-L
i DOS- 6

^»o/. 6
t ott-7
Stm to RH Attemp n
F


£ 31.¥
i Sf, X-

GlH.i
Stm Lvg RH Attemp £11
F
T14.7

r?f
r72.J-
5-7 r-c.
rb 7-Z-
Stm Lvg RH yo~z.
F
/cot, 9
ta Z.f, &
/o,C,7
^ o/-/, ^
1?7L-
lo/^t-f
Water to SH Attemp SO?
F
Z.11,%
Z 71?

^2/7|
V71.I
2.7 z. 1*
Water to RH Attemp 5"o*)
F
%lz.t
i~7z. r
2,-)°$
PSIG
zwzf
ZlZi-7
2?S*S t"
V)Sb,*
i-iw.f
Liun
Drum Press yob
PSIG
2-51JW-
li%f. z.
Zrl.o3
T-£7%- I
3-SX?. 7
t- S'H t *
PSH in Press —
PSIG
—
—

—.
—
—
Stm Lvg Sec SH t,at
PSIG
7. °4
PSIG

srv. t
?4 /¦ 4
5^?.^
i~v 2. t-
j-y f
RH Outlet 4o3
PSIG
5»?. 1
,in>*.r 5
S^7.V
-Ci"

Sbl.7
























HIGH PRESS FW HEATERS







FW Lvg #1 Htr
F






FW Ent #1 Htr 3
f C
I**.11
11 M.J
nw.r
137-/
??6.7
n ^..1
FW Ent #2 Htr £
r c
/Si , &
/iVi 1
ir&.z.
1S1S
ISl .f
~m,c.
#1 Htr Drain 4
/ C

IVI-I
!Hi-3
IW.S-
/V J. 3
/la, 1
§2 Htr Drain 6
/ c.
it,?-!
!<¦ t-2-
1 It.k
HI. ?
/**.?
7,6
Stm to #1 Htr-Temp /
F
(too .0
roi'1
& ol .&
i 6?. ?
J 16. 3
S"?0 •?
Stm to # 1 Htr • Press
PSIG
<% 0
8?
9/
Cfj

*1
Stm to §2 Htr - Temp X
F
1 "97.fi
itl-l
-717. r
iol.s
7-?/. 7 '
7,11 •£	
Stm to #2 Htr • Press L oCflL
PSIG
Zfo
210
2/*+

Ze?
2.0?
Fu\ EtJT HI Hf> ma T£Mp n
C.
/ 11-i
'Mi-7
m-7
20Z.
^0 0.¥
/ff.3
«TM -To #3 MP HTR TEMP to
F
S% 7. H
S"?<5.1
nt.j
r?r.»
nr.fi
56?.B
0 s PueBi-o
W —¦ vw w
(? Oils-Hits
(LoL o(2/i0o ,
C-53
-------
iJjft _	pc^ATT ' opaZATiMfi t>*T$


UNITS







UW 1 M I 1 C"l




	""""fc"
Test No,







Date
Time
Hours
Of 0°
Of$t>
Cf 00
<£"? 3q
!*>€>o
¦—u-
/Ojo
















AIR & GAS TEMPERATURES







0
G)
(3)
©
Ffc*G»sJL»g£«*» 2^^
' *

MfjjLxi-l.
ffi.sina.-?
cuafou
tti.WUi,*

FHj« Gas Lvg AH 7ojX\
F

24»V2f>7.r
2io.(,/uoA

ZM.s/l 72.5
in.i/ns,?
Flue Gas Lvg Hot Precip zUlfi
F
"7 v.
S7<.4/lfee.7
Sll-'-hn.i
uistmi
ai-kfwi,?
Co<\ fa, 11
Flue Gas Lv§ Pri AH —
F
r
—
-

—

Air Lvg FD Fan ;2/(3
F
^2,0 fyl-i

ib.it/irt.1


fz.7/ri/}
Air Ent Sec AH w//5"
F
loi.-fMi.t'

V-i/ti.l
<\i'\/1.M
M-S/UM

©
©
O
©
©
©
©
Air Lvg Sec AH 22/23
F
r2l//j-32 £

SVT/rtlrl
/xi/jvj-.J
'ZtSjssU.x
snt/sr/J
Air Lvg PA Fan —
F






Air Ent Pri AH —
F






Air Lvg Pri AH —
F






Air Ent Pulv —
F






Ambient Air jf
F

T>z,b
11.1
3 3.^
Z£.C>
At.r
















MISCELLANEOUS







Feedwater Flo«v HoZ.
LB/HR
Zl ZZ.3
2»£7 .t
zl/z.9
Z27?.f^
Z/o/.J
t« ft. (
SH Spray Flow 1oH
LB/HR
—
—
—
_
—
.. —
RH Spray Flow foZ
LB/HR

57>.a(

S"?>-3 "Z-
U.U
:cz. jz_
SH Spray Valve Posit —
%






RH Spray Valve Posit —
%






*HP Extraction Flow —
LB/HR






Oa Lvg E con . jofe/3 °/
% '

1,1 If 2 <7°
3,o//.7*


2.
CO2 Lvg Econ
%





/
NO* (if availl







Oi Lvg AH
%






COa Lvg AH
%






Oj Lvg Hot Precip
%






COa Lvg Hot Precip
%






O2 in Windbox
%




-


COi in Windbox
%







. NOx or CFA Port Posit








+ Fuel Analysis








Burner # Out Serv








Relative Humidity
%.






























!











Advise location of flow nozzle with respect to SH and RH spray take-off.
* - Any high pressure steam extraction upstream of reheater, excluding FW heaters,
+ - Report data available-specific requirements will be requested.
Efficiency data
Cm^to¦ pu.rjLic Se)2i/ic,f qf	po „ puE.Ha> C«lo/Moo
Jo rt kiiAi-v. iSc-o • fl.j
C-54
-------
Pcawt of>eftA-r>»& t>$
~f~ . DATA ITEM
UNITS






Test No.







Date







Time
Hours
c&oo
o/3 o


toa°
jo 10
















DRAFT LOSS DATA










• ¦ *



; SCAMtnlDuti "







AH Air In
"Wg






AH Air Out
"Wg






Windbox
"Wg






Furnace
"Wg






Econ Out
"Wg






AH Gas In
"Wg






AH Gas Out
"Wg






Precip In
" Wg






Precip Out
"Wg






ID Fan In
"Wg






SH Outlet Leg TCs
F






R H Outlet Leg TC's
F






























PULVERIZER DATA







Pulverizer#







* Coal Flow
MLB/HR
nr.w


HI.07
tW.il

* Pri Air Flow
MLB/HR






"Sec Air Flow
MBL/HR






Pulv Amps
AMPS






Pulv Diff
"Wg






PA Inlet Temp
F






Pulv Out Temp
F






PA Flow Damp
%






¦ PA Temp Cont Damp
%.






Pri Air Fan Amps
AMPS






pill ¦/ Z'A C-*"'1'//- •/." Tf . / L
F
tiz.f
127.2.
1Z7J
ni,.?
ai.i
I'M
-''J Aa/'c/f/l? "r&f-'p
£
IZJ.1
l2M.t
|iu.7
I14,t
.1 >r- ?
/*r. f
Pulv 2-c <:<>n rvo».* '?
F
l2o ?
,'2 1, V
n hi
iZl.tr
, r
12.1.7
p>m.) T'O ;»/¦ 1T{ ¦¦ i-|
£ ,
1?M
isyf
\x W ¦ 7

1 is-7
f 13








































The DRAFT LOSS DATA listed on this page is of value, but riot absolutely essential for performance analysis.
* - When indicator scale is in different units, provide conversion factor.
Efficiency data
3 _
Cu-STOMEI* I'^thUIC S€*£^'<^C OF, Coi_or2Aoo
Tk/5 . i . j btO	on -	''
pcl£QL.0, d«LOf/»Oo
C-55 !
-------
fLAfJi	nwii	n
DATA ITEM
UNITS
2










Test No.







Time
Hours
UOo
itZo
1 3o©
J?3f
ttfo 0
/43o
'X/^iTaiJT &£a^. CjtftSS
MuJ
-% %Z-LC

lel-Q?

z 9,0*70

CuJlT Load





mW(D

"I'OJI-Efl TEMPERATURES







- f n III Tim
. f. "
.
:
H7».7


*ihhS~ -i
*ri,i
Water Lvi Icon 33.S
75i.i/kr.&
"ir/.V7v?,r
Tftshttn
757.3/71x7
Stm Lvg Sec SH t
F
iaiZ 1
^¦W.6

?r?,?

*37*/. 9
Stm to RH Attemp ;i
F
iUo- 7

bOl.Z
r*»i.n
5V4,1
f?0.3
Stm Lvg RH Attemp £II
F
OTi
STt.H
s~t y i- ¦
511-f
rMf
rfo.f
Stm Lvq RH frrfL
F
7 Z
417.1
111-7

qte>,f
/<"/"»< j
Water to SH Attemp 507
F
tlt.<-f
itl-t
l£¥. J'
3.7

lio,)
Water to RH Attemp S"o1
F
t-7Z,V
Lift
liq.f
Zh%,7
7.11, *4
tier./
























BOILER PRESSURES







Water to Econ (*t>S
PSIG

2-72-1 ¦ 7

XI to'. I
e.^
2707.4
Drum Press bob
PSIG
•unrs.f
7-ST2 . 3

ZSM-l
WiJ.t
IS si. 1
PSH in Press ~
PSIG
—¦
_
—
—
—
-
Stm Lvg SecSH 601
PSIG
2-Hok'S
Xiy/ o.fc/
2aq
PSIG

in?
¥«?•«
m>i> 1
y 6 &

RH Outlet £t>3
PSIG
¥1 r.7

iiy.~
FW Ent #2 Htr S
f c
/ri .f
/sr, 4

TJ.O
IS"/. I
mi.t
#1 Htr Drain 4
f C
tHt.o
}<4 0,i
n?1-1
<»TM 70 #3 MP tfTJl TETMP 10
F
sr? r
STS-2
ruz.z.
fir if
SlS-k
T7t>3
STM To*3WHrTfi- PRESS Lit,
C PS16
5-2.0
5 Itf
^60
*tiQ


f}Bj£ {£) [7uu/.Z'A trtfJ J TfiKQJ OpP-U*JE (% ti/to ft*. J
Cui ToMCtf: Puflu C SeRi/o , pue(?Lo (LoLoiZaoa
Jo& hlO. ; £ 13-5 OE.
1
-------
l?Lfr*rr ' o fefZAT/Ma
DATA ITEM
UNITS
,2. -




—e»
Test No.



_



Dtitc
Time
Hours
lax£/Zf£,
// 00
mo
• i$c>o

/ (ft (TO
t <4 3o
















AIR 81 GAS TEMPERATURES







flue Gas LugJEcan 2*1/2f
f
WtfjtrM
136.S/&U



chx/mi
Floe Gas Lvg AH 7o Jz |
F
j
LU.s7T.7f,
¦ui-ihiu
ltS.fhn.1
ni-ifa?.9
2 6 Will. 5"
flue Gas lvg Hot Precip lUzi
F
bolD/i/o.i

stnxfoftx
m-vnin
5to,o/slz.1
TMS/Sl7.t
) Flue Gas Lvg Pri AH —
F
—



—
—
Air Lvg FD Fan IZ//3
F

k-ojio.i
U.t-jiLH

7Z.4/72-
W-l/Ttj
) Air Ent Sec AH !<4 hS~
F

t't'sjfl.L
uR.r/t'l.?
/of.t/i/i •=

IW/iW.C
) Air Lvg Sec AH 22/z3
F
5$Ss/rstH
ssi.bjm<£

fj6"7/X4J.i,
&~3&Vnr.6
rJi/si-if.i-
Air Lvg PA Fan —
F






Air Em Pri AH -
F




¦

Air Lvg Pri AH —
F




_

Air Ent Pulv -r
F






Ambient Air /?
F
<-/7e>¥
LB/HR
—
—
_
—


RH Spray Flow 7o3
LB/HR
3~V.i3
37. t±-
7.5r



¦ SH Spray Valve Posit —
%


_
—
r _ ¦
—
RH Spray Valve Posit —
%

-
-
.—


* HP Extraction Flow —
LB/HR


—'
—.
-—
—
O3 Lvg Econ "job fa °7
%
1,0 7/2.71.
z .§th>(,z
j.llhsf
3.6'/2,«y
1,01/2.17

COi Lvg Econ
%






NOx (if avail)







Oa Lvg AH
%






CO, Lvg AH
%






02 Lvg Hot Precip
%






COi Lvg Hot Erecip
%






Oj in Windbox
%




-

COj in Windbox -
%






NOx or CFA Port Posit







+ Fuel Analysis







Burner # Out Serv




*


Relative Humidity
%.


r

































I
©
Advise location of flow nozzle with respect to SH and RH spray take-off,
* - Any high pressure steam extraction upstream of reheater, excluding FW heaters.-
+ - Report data available • specific requirements will be requested.
(2)- Efficiency data
2
Cojtogji; f?u.fiLi£ $&zvicjf Of	puE(li-a C-olo/2aOo
•Jo (3 nh-w 1J pi? - 0 J- e *¦» '
C-57'
-------
PtAMT opeftAT ia»6 £>4T/*
:"%C?
DATA ITEM
UNITS
<2 —




¦ ¦—p.
Test No.







Time
Hours
1 (cro
1/ ? 0
1 5^5-0
(5>o

¦	Jfc
/ M J 0
















DRAFT LOSS DATA







FO taXfech
-«h






• ©
-SCAHhaOfcrt)
, -w,


•



AH Air In
"Wg






AH Air Out
"Wg






Wind box
"Wg






Furnace
" Wg






Econ Out
"Wg






AH Gas In
"Wg






AH Gas Out
"Wg






Precip In
"Wg






Precip Out
" Wg






iD Fan In
"Wg






SH Outlet Leg TC's
F






. R H Outlet Leg TC's
F






























PULVERIZER DATA







Pulverizer #







- * Coal Flow fj '5
MLB/HR


, /YV3
32-
W7-37
At"5. ^
* Pri Air Flow
MLB/HR






* Sec Air Flow
MBL/HR






Pulv Amps
AMPS






Pulv Diff
"Wg






PA Inlet Temp
F






Pulv Out Temp
F






PA Flow Damp
%






PA Temp Cont Damp
%






Pri Air Fan Amps
AMPS






p^ls) ?-* C-cr-tfitz ~
1=
(il-t
no, j ¦
Ill.i'
IlLl
IW-7.

Put\] 7-t J
F
ft J. 3
127.7
12,7.9
117, f
tiy.L
.r

r->i s/ T ' 1"
r-
I 23 .O
IZJ.)
lil-t

li\-7
12/, r

Qui J, P-D T £>>f
F
)2 k • 3
Ill.l.
1 2,7. t
!2 tui"
! 2.4, J














































The DRAFT LOSS DATA listed on this page is of value, but not absolutely essential for performance analysis.
* - When indicator scale is in different units, provide conversion factor.
(2)- Efficiency data
3 _	'	"
CuSlOME*. pHfiMC SefLsitae OF(tGL.0fLA*>o, Pll£6l.O, CouOC/tCo
f. s\ ... - .' —A . n /% —	t'
C-58
-------
¦ 1 Rep'Oduced 1rom
: I best available copy-
pL^T Oft ft * TliJC OAT A
DATA ITEM
UNITS
X


—


Test No.







Time
Hours

!$3*
) boO
	
/^3o

		
&rli.
Si A! UJ
* 72. ?r
Z&>! ¦ lo
miAi
3 5l


u>J L0A6 PfiT-'AWO







„ BOJ-LEH T£MP£ RATUHES







- mHJri&an S»?
¦¥
ar^sT
wx*-/
4»r4- J ¦.



Water Lvg Econ Jll
F
s"J«-3


ivi'V


Stm Lvg Pri SH Sl4-/nS"
F
iK-ihxu


ikmfai
-

Stm Ent Plat SH —
F






Stm Lvg Plat SH —
F
—
—.
—



Stm Ent Sec SH 7 / %
F






Stm Lvq Sec SH *}
F
l7f-f

fr'r.i
IB Si, Z-


Stm to RH Attemp n
F
stoA
Sli.f
r^. I
ioQ.o


Stm Lvg BH Attemp $11
F

J-7/.f
s-H.7
$11,1


Stm Lvtj RH
F
9rt,o
177,/
10/O.?
471
F
2x7.1
ISi.Z
irf./
Hut


























BOILER PRESSURES







Water to Econ £»S"
PSIG

1
nn-i
Z61Z.i


Drum Press yob
PSIG
tfiSjT


2£"L*4-t


PSH in Press —
PSIG
—
— ,
-
—


Stm Lvg Sec SH £.ol
PSIG
n
PSIG
%1e 1


HtZ.I


























HIGH PRESS FW HEATERS







FW Lvg #1 Htr
F
_—
—
—
—


FW Ent #1 HTr 3
f C
rz-P.C
IZC L
/Z-7.2
113. jT


FW Ent #2 Htr S
V C
/Sn, 1
H7.1
'.Hi.!-
15^.?
-

#1 Htr Drain 4-
? c
"lit-3
13.2.3
117.2 '
,'lif .3


#2 Htr Drain £
/ c.
ir -hi.
isi.i
/Tl.l
/ 4o.V


Stm to #1 Htr-Temp |
F
O/.r
c 7d,y
stfe.r



Stm to #1 Htr * Press local.
PSIG
70

c 3



Stm to #2 Htr - Temp Z
F
7S4.I
7 it,H
710.7
(?OX« 1


Stm to #2 Htr - Press L oC*L
PSIG
/7a
IS%
/
^5«
£{4 0


•j* 3 H? Hr« Pitfl/w T£Mf g>
jjiTT€i
¦^p:0"J*~x	t^lST'Cu^	t&f£u (ft) 1^% *ftu(L)
CUS TOMEfi:
Jo6 fJo. ;
pu&u c SeRi/ite
R13-5 02.
oF CoLo/tAt>0 , Pw.£'3C-o C^oLoiZAOo
C-59 i
-------
pi-A/JT ' Of>£tZAT!bi6 &AT&
DATA ITEM
UNITS
2—









Test No,







Date


{iftvfty
't/io/ZV



Time
Hours
IST>»
IS J 0
/ it m
U"} 0


















MR & GAS TEMPERATURES







Flue Gas l*g£con 2*4 fc?
F



mjJus-j


Flue Gas 1_vg AH ^o/z|
F
unMfm.-J
itttJlTS.'

"Uz.iJl? a,l


Flue Gas Lvg Hot Precip ibfz'
F
S7flS77.3
al-iisufi
516 f/ft ?-1
mJlni.l


Flue Gas Lvg Pri AH —
F
.—

-



Air Lvg FD Fan /2/l3
F
Ti-shf-o
is-ihn
7S<>ht.£
ivr/v.o


Air Ent Sec AH \14jj5"
F
Ut.x/aii
ntviwl
nh.flai.f
HS'.SjiUJ


Air Lvg Sec AH 22 /z3
F
sii-i/s't?

g-tn/m.?
«7/jWJ


Air Lvg PA Fan —
F






Air Ent Pri AH —
F






Air Lvg Pri AH —
F






Air Ent Pulv —
F






Ambient Air )$
F
si,.C
'sf.,7

57.1


















MISCELLANEOUS







Feedwater F low 10 Z.
LB/HR
nti.'l

/toi.l
HHI-?


SH Spray Flow tjoH
LB/HR
—
—
—



RH Spray Flow 7o I
LB/HR
__
-




SH Spray Valve Posit —
%
__ ,
—
—
	


RH Spray Valve Posit —
%
—
-
—
	


* HP Extraction Flow —
LB/HR
—
_




O2 LvgEcon Jabf3°/
% •

?, (-72.fi J*

2j?h.n


COj Lvg Econ
%
1


*


NOx (if avail)







0, Lvg AH
%






COi Lvg AH
%






Oi Lvg Hot Precip
%






COa Lvg Hot Pxecip
%






Oi in Windbox
%






COj in Windbox
%






NOx or CFA Port Posit







+ Fuel Analysis







Burner # Out Serv




-


Relative Humidity
%






































Advise location of flow nozzle with respect to SH and RH spray take-off.
* - Any high pressure steam extraction upstream of reheater, excluding F.W heaters.-
+ - Report data available-specific requirements will be requested.
(2)- Efficiency data
**£1Z ¦ pu/jLl^ S£j2i/|C(f 0F>	^ pusdt-o toi,or?^Oo
CTtifi Mulvw Act 5 - 0.1-e.nf
C-60
-------
PcAfJT OfEftA~Tif*6 t>A"TA
DATA ITEM
UNITS
2- '
.






to
Test No.







Time
Hours
! c/lo/XI
' 1ST>*

/ b C~0
i<5


















DRAFT LOSS DATA













¦

¦sowiwtotrt)
-w






AH Air In
" Wg






AH Air Out
" Wg






Windbox
" Wg






Furnace
"Wg






Econ Out
"Wg






AH Gas In
"Wg






AH Gas Out
'* Wg






Precip In
"Wg






Precip Out
'* Wg






ID Fan In
"Wg






SH Outlet Leg TC's
F






RH Outlet Leg TC's
F













'
















PULVERIZER DATA







Pulverizer #







* Coal Flow J?/'3
MLB/HR

Nt7f
IVT.iJ
/vr.tl


* Pri Air Flow
MLB/HH






•Sec Air Flow
MBL/HR






Pulv Amps
AMPS






Pulv Diff
"Wg






PA Inlet Temp
F






Pulv Out Temp
F






PA Flow Damp
- %






PA Temp Cont Damp
%






Pri Air Fan Amps
AMPS






PuliJ 2 -f- c^aUahi Te^p.
P
iff'i l-Hl
- —
—
—


0^!.) 2-6 " "
F'
III.*
t2 J.6-
12 2.?
,z".0


PunJ 2-C •>
(Z ,
III. °
n/.z
lZo-,3'
iZ-a.y


t?i0
LC-61:1
-------
YLfKrtY oj'fc't*, iimu in
DATA ITEM
UNITS
2 ' -











Test No.

1





Time
Hours
cm*
of e a
oi jo
o-o
o«i J«
/O 3 &
















; . BOILER TEMPERATURES







¦ mrnacmi&mm -
•' *
MrHI \

*W.J
V*e.0

Hit's
Water Lvg"Eeon J/l
F
$31.6
rwsW
5"5t.J
m-y
svo,r
W3-3
Stm Lvg Pri SH 574- / X"i5"
F
insfinj
luiibv/1
-v/ohu-i

m.ihas
isbxhiv-
Stm Ent Plat SH -—
F






Stm Lvg Plat SH —
F



..


Strri Erit Sec-SH - <7 / «
F
v i.*lnu
1 tiz/vH-f
W'^ni-9
-"iWhii.f
-?Vt.#7}U
UoS~hjf. /
Stm Lvg Sec SH 1
F


tu-t

m-g
/r>i 7-7
Stm to RH Attemp n
F
ajv

i"?i. J

T*t P."L
L H-!> «
Stm Lvg RH Attemp SH
F
slf.f


s-jr t.
' .TI3.L,
I
Stm Lvg RH toz
F
<5 77. 7
o

102.!,, i
/6 »t/.-/

Water to SH Attemp SO"]
F

z 7
C
m
tio.z.
»9t.°
itti-
/J1.5
/f/-¥

yz/o */©6 ' *4 o-O *-/Z* Wo W3 Hf rtrc p*A/m T€Mf g c /ff l O0€lB*£ peZts U4t£V @ oSvs.tHlS. tU5T0ME^ PwflUC S£Bi//te OF 7o6 do. - £6-5 oz. % fti.i /W.3 /$r.y at,/ Co LotfAfo J. Puerto CotoiWfto.

-------
/7<_AaEfZ#TtM6 P>*T#
DATA ITEM
UNITS
- > -




	^
Test No.







Date

iz/nliH





Time
Hours
0Q-50
0$O"
of 3*
0 5 of

/o ^ 0








•







AIR & GAS TEMPERATURES







) ¥MmGmLw£x*n iM-hX
1=

f
rtjsjrff-l.


rm.iifi*
> WoeGas Lvg AW 3o/zi
F

2W. l/2?o,4
2k>.okitt
it7!72&9

irt.iM 7.1
) Flue Gas Lvg Hot Precip Z^fz")
F

SiiMlrn.i
$7o>/s?2.»
xwXfat.t-
OJX'/sil-l
sw.7 /ru-«
Flue Gas Lvg Pri AH —
F


—
-
_

Air Lvg FD Fan I7.( 13
F
U-i/it. 3

iofifou f
<17/iz.}
f tjfbH-i
1
) Air Ent Sec AH jIS"
F
IV-^/iio.K

ioe.7/,^1
lio-sful-f
SiojtjmA
t s>t-l/llS-1
Air Lvg Sec AH 22 (t3
F
svf-f/s-ii-s
Sl1-7(sxt
mVx-iS'f-
ri-M.i /rzt.«
JUJZr, 7.?
Stz Is to- 7
Air Lvg PA Fan _
F






! Air Ent Pri AH —
F






Air Lvg Pri AH —
F






Air Ent Ptifv —
F






Ambient Air 1$
F

Hi,.')

1172.1
i&z.l.Y
nio.7
7

SH Spray Flow qoH
LB/HR




—
_
RH Spray Flow lol
LB/HR
—
HS\oi
—


Ltf.m
SH Spray Valve Posit _
%
—

—
—

_
RH Spray Valve Posit —
%
—
_ •
-
—
-
—
"HP Extraction Flow —
LB/HR


—
—
—
-
Qi Lvg Econ 30bfie"/
%
1.2.i/2.6 J
3.0r7z.4f
iMhM
Wk.St
"5.0^.43
iM/W
CO3 Lvg Eton
%






NOx (if avail)







Oj Lvg AH
%






C03 Lvg AH
%






0a Lvg Hot Precip
%






COi Lvg Hot Pxecip
%






Oj in Windbox
%




-

COi in Windbox
%






NOx or CFA Port Posit







+ Fuel Analysis







Burner # Out Serv




~


Relative Humidity
%






































¦i/
Advise location of flow nozzle with respect to SH and RH spray take-off.
* - Any High pressure steam extraction upstream of reheater, excluding FW heaters.
+ ¦ Report data available-specific requirements will bo requested.
Efficiency data
omtopu^cic sea^icif oft
Jn rt	i'I **•>•* - rt ,1 —'
puEfti-o Couo£/W>o
! C-63

-------
PtAMT Of>efcA~T>»& £>4t/*
lr DATA ITEM
UNITS











	
Test No,







Date

W/i //¦¥





Time
Hours
O130
Qtoo

of 0&
C7I <3
! OOo
















"DRAFT LOSS DATA








-


¦1 	

SCMMtaKM '





-
AH Air In
" Wg






AH Air Out
"Wg






Windbox
"Wg






Furnace
"Wg






Econ Out
" Wg






AH Gas In
" Wg






AH Gas Out
" Wg






Precip In
" Wg






Precip Out
"Wg






ID Fan In
" Wg






SH Outlet Leg TC's
F






RH Outlet Leg TC's
F






























PULVERIZER DATA







Pulverizer #







* Coal Flow 2/3
MLB/HR
ISV.ll

iri.ef
15-2.3?
iSl.ftf
irj.ro
* Pri Air Flow
MLB/HR






"Sec Air Flow
MBL/HR






Pulv Amps
AMPS






PulvDiff
"Wg






PA Inlet Temp
F






Pulv Out Temp
¦ F .






PA Flow Damp
%



¦


PA Temp Cont Damp
%






Pri Air FanAmps
AMPS






p«iV. I-A CoAL/AiK T£W>
F
ns.i
JZ.4..T

lii-r
1 Lg. I
iz-h.f
7-6

I17. S"

f!7.3
f z. ?. S
117.0

2-C
F
,11.1
III J
ii3.i
ur-?
tli.e
in.9
i-O
r
llfc-l
uy.7
iir.1


i








































The DRAFT LOSS DATA listed on this page is of value, but not absolutely essential for performance analysis.
* - When .indicator scale is in different units, provide conversion factor.
- (D" Efficiency data
3 _
CUSTOMER-	S6OF ,C«t.0f2 AOO , p^S/il-O, CatOCADO
-r- /"J ... - /> —<*	r* * r- - - •'
C-64

-------
pLftriT ofeRAT^a OA-jPt
DATA ITEM
UNITS


<2>





,1V
o


Test No.







Time
Hours
/d 30
tf oo
"So
13 eo
!}S»
i<4 oo
^STft*rT,££WGWioiO 
MuJ
27129
zrt.r?
HZ.qj
2 •©¥
ILL.*'
24,!,?$

-






. boilem temperatures







*fli^tar9taS0OMi

<^S"X.4
W-?
¥57.7
4*5-5"-
*ra*/

Water Lvg IE con J/l
F

s-yj.f
53f.i~

r5(#.3L
Hr. u
StmLvgPriSH St4-/ ft?
F
7vwmn
Tf 'i'" r v i
irr
TTJ.iA*

/74/t
Stm Em Plat SH —-
F
(
JT^/nwr
—
—


Stm Lvg Plat SH —
F
.—
—

—
—
—
Stm Ent Sec SH 7 / f
F


7H4-3huf
"WB Vw l
THUHkvn
?3?5/7H.|
Stm Lvg Sec SH 1
F
/Oil./
ur-r
Vi'lM

17T« 3
'Jf 1.7
Stm to RH Atternp fl
F


r«.H
koi.r
T7V.4
nt-L
Stm Lvg RH Atternp £11
F
s-?r-7
<^9.T
S~? o,J"
5*4 t.c
rs.?.£»
S7Z\
Stm Lvg RH fT.
F
"57;,?
wo.t*
taa.$-,b
MM
f 73.?
/cos. 1
Water to SH Atternp 5"£>7
F
Zto-1
zrh-i
2.E&.7
2I
25 7-i
tsi> i
Water to RH Atternp 5"o*7
F
zto.l
Zf7».f
tSi7
2b5"
PSIG
zfc/r fc
¦24,7°. r
¦Liii-S"
ZloH, b
TJetU.r

Drum Press yob
PSIG
2J3fc .|
Z-Sio.l
ISI%-3
zsvsJ
2 JB2«£
ZS~b7,o
PSH in Press —
PSIG
—
—
-
-
—
—'
Stm Lvg Sec SH (,ol
PSIG
mit-7
2,517.1
Z"Jf2.7
tm-o
2 4« /
2ii1
RH Inlet
PSIG
m iy<°
QH.O
MM*?- 3

4ZI-I
un. 1
RH Outlet UoT>
PSIG
Ife/.o
ILLo
SU.o
44.Z..1
UtA
ffei.l
























HIGH PRESS FW HEATERS







FW Lvg #1 Htr
F






FW Ent #1~Htr 3
/ C
fz?W
S24.3
IA&S-
ni.7
12 f- 3
iZh.H
FW Ent #2 Htr £
f C
i v^'4
\4l-3
i -<3
tx-i.i ¦
ts7-t
is 7.x
Stm to #1 Htr - Temp I
F
i"l.l

rfi.x
s-f|,r

5t7. 4
Stm to #1 Htr - Press L°c*L
PSIG
7*
(¦r
it
* 75"
67
£5
Stmto #2 Htr-Temp 2.
F
75s.U
76?.?
7?X.3
•745 J
76S.I
ifzi
Stm to #2 Htr - Press t odL
PSIG
I7«/
/re
/ 6o
i fo
t l(rO
1st
Fui e/r *3 we ht* n-r^p 7
C
itl.7
l%7*
JJj.f '
113.4
Stni
10,7

V/o 1
4*vMm TCMf 8 c ,et1-6	2°°-& 1^1 <"K|
. cus ioneiSs putiuc see^c£ of £01.0/2*.>0;f>ue®LO c-vt-oe/i&o.
Jo6 do. • £6-502.	.,
1
/
1
i C—65]

-------
PlA/jt operzflTihi6 p
^ DATA ITEM
UNITS
3 -











Test No.






-
Time
Hours

11 OCi
H3a
I\o 0
ibJ*
f C?®
















AIR & GAS TEMPERATURES







Flue Gas Lvg Econ 7M faf
F

SVi-3/rh h

(,07 /VI ¦1
rif
rlU/R/.i'
Flue Gas Lvg AH Po /zt
F

n
261.0/171>.
uafm.x
l< *,1^72.6
7t5,f^7i.2
Flue Gas Lvg Hot Precip -i(,fzr
F
Mz -7/ar.i
ni.t/sizs
577.1/5-57.
s-irxfcus

.5WJy&-7*3
F lue Gas Lv<3 Prl AH —
F
—

-
—
_

Air Lvg FD Fan 12/13
F

ii.1/6 7, 5
mms

m.ih4- f
7i.i! 11 J,
Air Ent Sec AH 14 Jf
F
mm/< a.f
ni.ihi.v

iH.i/fle.i

H/
Air Lvg Sec AH " 22/23
F
S-u.y/jTj.'i


sn»sts 27.2
5J5.//C2.7J

Air Lvg PA Fan —
F

—




Air Ent Pri AH —
F
-
—




Air Lvg Pri AH —
F
—
—




AirEntPulv —
F
—
—
—

A-7 t

Ambient Air i$
F
S"2.~?
TZA
SX. 1
Tt.f
VJi' '
	J?gv£=
&t.2.
















MISCELLANEOUS







Feedwater Ftow lot.
LB/HR
lb2-9"7


' ltK1< O
l^to. 1
f 0
SH Spray Flow ijoH
LB/HR
—

-

—
—
RH Spray Flow 7o"h
LB/HR
i-ol

—
V*
—
—
SH Spray Vaive Posit —
%
_
— ¦
—

—
—
RH Spray Valve Posit —
%
—
, —

__ 		
—
		
•HP Extraction Flow —
LB/HR
— -



—
—
03 Lvg Econ "jofe/3'7
%

?.(z./z~67
i.f/z, tr
J.0f/2.7l
Lir/z>|
3.U/2-SO
COj Lvg Econ
%




* *

NOx (if avail|







0, Lvg AH
%






COj Lvg AH
%






Oj Lvg Hot Precip
%






COj Lvg Hot Precip
%






Oa in Windbox
%






COj in Windbox
%






NOx or CFA Port Posit







+ Fuel Analysis







Burner # Out Serv







Relative Humidity
%.








'




?¦
























Advise location of flow nozzle with respect to SH and RH spray take-off.	j
* - Any high pressure steam extraction upstream of reheater, excluding FW heaters-	I
+ - Report data available-specific requirements will be requested.	j
(2)- Efficiency data	j
2	l
CiLt-/SLtC $0£t/(C(f of c^oLpt^AS>o pu£(lt.O	C-ULOr?/^Do }
•To.<3 i 2 A-^aZ. _	1
C-66

-------
/ DATA ITEM
UNITS
A
1




J Test No.







Date






		
Time- 	
Hours
It) Jo
ILtro
H3o
13«°
t3 Jo
/¥«•?
















DRAFT LOSS DATA







FD Can JKxh







SCAH In {Ourl
** Wg






AH Air In
"Wg






AH Air Out
"Wg






Windbox
"Wg






Furnace
" Wg






Econ Out
" Wg






AH Gas In
"Wg






AH Gas Out
"Wg




. _

Precip In
"Wg






Precip Out
"Wg






ID Fan In
"Wg
>





SH Outlet Leg TC's
F






RH Outlet Leg TC's
. F






























PULVERIZER DATA







Pulverizer #







* Coal Flow f/3
MLB/HR
irl.06
tsroMz
(Sb.&Z,
/ST.ff
N1.lt>

* Pri Air Flow
MLB/HR






* Sec Air Flow
MBUHR






Pulv Amps
AMPS






Putv Diff
"Wg






PA Inlet Tamp
F






Pulv Out Temp
F






PA Flow Damp
%






PA Temp Cont Damp
%






Pri Air Fan Amps
AMPS






Z-f\ CJOM./M TsmF-
F
l U.i
tlS.i.
117.9
{^4 '
tM.S
Ml
H Z'8 
-------
PLAfiJT	1 IAJ £i OA T/t
DATA ITEM
UNITS
A
JZ-'




Test No.







Date


'V«//V




Time
Hours
1H1 o
tfbe






[. 2°













, BOILER IEUPERAJURES







¦¦ -HftMii'iXr'wi 1 ' ¦•SDQ •
•\ F

Vrxa"



¦
Water Lvg "Eeort Jil
¦F
ill-.V





StmLvgPriSH 5/4- /ri-T
F
wt/nn
7»w/JS4.1




Stm Ent Plat SH —
F






Stm Lvg Plat SH —
F



¦¦


Stm Ent Sec-SH - 1/t
F
1ST>j/tj3
7VJJ"/?n*




Stm Lvg Sec SH f
F
ff7.I



<

Stm to RH Attemp n
F

g-g¥,o




Stm Lvg RH Attemp SH
F
S~7t.l
S-7V-/




Stm Lwg RH
F






Water to SH Attemp SO7
F
vsrM'
Ifh-f




Water to R H Attemp S*o1
F
2.ST-4
2iar

























*


BOILER PRESSURES







Water to Econ 6of
PSIG

1-^7 US




Drum Press bob
PSIG
Z £()¦
2-XI J"-/




PSH in Press ~
PSIG






Stm Lvg Sec SH £,o!
PSIG
U ff. °





RH Inlet 6>o4
PSIG
yol.o
VrU.o




RH Outlet {,qT>
PSIG
m.6





























HIGH PRESS FW HEATERS







FW Lvg #! Htr
F






FW Ent, #1 Htr 3
/ c
(Zt.l
ttk.t-




FW Ent #2 Htr S
f C
/•/7.7
/v ?,7

_


# 1 Htr Drain A-
f c
li 1.7
»%•«?




#2 Htr Drain &
/ c
trio
IS"? J




Stm to #1 Htr-Temp J
F
fa G*> 4
?*f.7




Stm to # 1 Htr - Press L°CAl-
PSIG
b*j
6i"

~


Slm qi #2 HSr-Temo £'
F
1
171.1




! Sbvtv #2,'HO"-- L-&K.
PSIG
in





FlA1 EfJT ft J HP HT/e T£/«P 7
C
fit.?
ttf-r




STM To *3 W/9 XT* TfM/J to
F
ri7
TTf'3




5TM To #3HPtfT(t tofe
C P5l6
t/Jo
tf/O




PW/M rewf g c /a .
3*o{i ftifli 7 fcQ—SoZ-	¦*
t
C-68
-------


pL*tJT ' OfalATI^a
:'V
/
0)
(3)
^ DATA ITEM
UNITS






Test No.






.
Date

1 %/«M





Time
Hours
NJ°
iron




















AIR fit GAS TEMPERATURES







Flue Gas Lvg Econ 2^ faf
F
n*.i/sn ¦?
stfi&w.H




Flue Gas Lvg AH 2o /z 1
F
ui





Flue Gas Lvg Hot Precip zUtS
F
fis-'/rar-i'
snh




Flue Gas Lvg Pri AH —
.f






©
©
§
©
©
©
©
©
Air Lvg FD Fan (Z/|3
F
7^.1-/7^,4
7r-f/?rJ"




Air Ent Sec AH I4//5*
F
tH-tjtlU-t
11 j.i fti-1'4




Air Lvg Sec AH 22 fz3
F
aizkioi
n 7-iyiii*7




Air Lvg PA Fan —
F






Air Ent Pri AH —
F






Air Lvg Pri AH —
F






Air Ent Ruhr —
F






Ambient Air j$
F
i o-t
iff 0. *L




















MISCELLANEOUS







Feedwater Flow 90 Z.
LB/HR
I
H3I.Z.




SH Spray Flow loH
LB/HR

—




RH Spray Flow 70*5
LB/HR
-
¦ _




SH Spray Valve Posit —
%
—
—




RH Spray Valve Posit —
%






* HP Extraction Flow —
LB/HR






Oj Lvg Econ 3obfl°/
%
l.oCllS'





COi Lvg Ecan
%






NQx (if avail)







Oj Lvg AH
%






CO] Lvg AH
%






Oi Lvg Hot Precip
%






COj Lvg Hot Precip
%







Oj in Windbox
%







COj in Windbox
%







NOx or CFA Port Posit








+ Fuel Analysis








Burner # Out Serv







C4
klUUUlillY
, %.









l;
































Advise location of flow nozzle with respect to SH and RH spray take-off,
* - Any high pressure steam extraction upstream of reheater, excluding FW heaters.
+ ¦ Report data available • specific requirements will be requested.
. (2)- Efficiency data
2
' pu.rjcic	of	00 ^ puEfh-o ColofMou
?o<3	: &A-SQZ. _
¦C?69
-------
,	KLMWl ucti'M ma»£»
v' 5-14
y/ DATA ITEM
UNITS

2.




/
i
©
Test No.







Date

i %tuim
Us/n!if




Time
Hours






















DRAFT LOSS DATA







- WJftmDisdi
*"W§






SCAHIti (Out)
"Wg






AH Air In
"Wg






AH Air Out
"Wg






Windbox
" Wg






Furnace
"Wg






Econ Out
"Wg






AH Gas In
"Wg




'

AH Gas Out
"Wg






Precip In
"Wg






Precip Out
"Wg






ID Fan In
"Wg






SH Outlet Leg TCs
F






RH Outlet Leg TCs
F






























PULVERIZER DATA







Pulverizer #







'Coal Flow #/3
mlb/hr
liibti,
1 v£
f
H-S-1






" 7-4 "
' f
I ltd






" 2-£ i. "
pr
11H .0
ci>ny





" Z-D >J "*
f
U k-b
1 v?.z





' i











M .

V





























The DRAFT LOSS DATA listed on this page is of value, but not absolutely essential for performance analysis,
* - When indicator scale is in different units, provide conversion factor.
(Ty Efficiency data
Cdj-roMETg ¦	c Se"fc«/»tC OF CeLorzAoo, pn£6t.o, Colorado
.ThA	R{\-5oZ. >'
C-70
-------
DATA ITEM
UNITS
Z










Test No.

ri/fz/pw





Time
Hours
Ofeo
C?3o
0 ^.pO
O?lo
(000
	
folo
X(JSTfl*JT SRA55

333. St
7/1.37
3 2.0,?(hn..i
ifhihxiJ
isr-sjyi-p'
7
l&.th&z

Stm Ent Plat SH —i-
F
—


'
	r	

Stm Lvg Plat SH —¦
F
—
¦ -
-
- —

.—.
Stm Ent Sec-SH _ 7/8
F
7SSMtm?
7J»
isi.s/i^X
isbthov-i
760/in^
7•suzhutf.
Stm Lvg Sec SH f
F ,

Tks-U

! Water to SH Attemp SC>7
F
170
2-7/7

i tf.i

2feU
Water to RH Attemp 5"o1
F
¦ 2?»
%7t2
2^1, t
2tt,Z
¦ui.4
2A"?-3












(











BOILER PRESSURES







Water to Econ £>oS
PSIG
2")V0,P
Z71P, 7
%"]%i .7
3?^.?

272 W. 7
Drum Press bob
PSIG

z >-?/,y
2-« ?. V
z^rs.r
1ST2J.6
t-s-yr. r
PSH in Press "~"
PSIG
—
. —
-
—
—
— .
Stm Lvg Sec SH £ol
PSIG
2«»2.f


2V02. t
HjoV.2.

RH Inlet
PSIG
r,0
iss-.r
i^y.o
i rr.t_
iXS^
#1 Htr Drain 4-
c
/ ¥©>7
H 
 Ar	.
cus Tone#; puau c Sefs^/ce of Colozapo , F'uefft-a c^loisaoo.
Jo6 fJo. • /? 13-5 o2-
1
C-71
-------
sir
PlAaJT Of&RATI
DATA ITEM
UNITS
Test No.
~ate
J2-.

Time
Hours
OfOO
otZo
O fo
cqio
too 0
f#3o
AIR & GAS TEMPERATURES
uutht-1-
Fjuegati-ygfcon 2.4121
ISlJ-j&VA
yyn-1
nnBG»%*g*H
?o/*l
UoSH6-i
zahii'i
ley jjioil?

lUjhtU '
Flue Gas Lvg Hot Precip zifx


&tSAfa >1,6
& of-l/hrf.? !>Sa/(t6t -f
Flue Gas Lvfl Pri AH
Air Lvg FD Fan
(z/[3
47.1 hi. u




9S'ifyr-6
E!A
6 fa
Air EntSecAfcT



WM/<}7.t
1lAiltX
°i7
ten/%. 9
Air Lvg Sec AH
12 23
rNl^jrV^
i'sUVsvi-t

m 2/m 7.S Kitl/Mi sVl t/m
Air Lvg PA Fan
Air EntPri AH
Air Lvg Pri AH
Air Errt PuKr
Ambient Air
jL
3«.^
??.3
2*?<7
31,3...
3)>?
3 0.7
MISCELLANEOUS
Feecfwater Flow
*?o2.
LB/HR

«-/
ZWz.,6
llf7.7
liM2uL
1<*17.0
SH Spray Flow
noH-
LB/HR
RH Spray Flow
To 3
LB/HR
IS"
«/2, ?2_

3 J. ?3
4swr
S*2« <44
SH Spray Valve Posit
RH Spray Valve Posit
%
'HP Extraction Flow
LB/HR,

Oj Lvg Econ
COi Lvg Econ
?o|>/3»;
%
%

2.1 lk-7S
3.1i/z.6g
(.23/2.3V
3,?W/,
Z.tl
2-?
NOx (if avail)
07 Lvg AH
%
C0f Lvg AH
%
03 Lvg Hot Precip
%
COi Lvg Hot Precip
%
Oi inWindbox
%
COj inWindbox
%
NOx or CF A Port Posit
+ Fuel Analysis
Burner # Out Serv

Advise location of flow nozzle with respect to SH and RH spray take-off.
* - Any high pressure steam extraction upstream of reheater, excluding FW heaters-
+^- Report data available - specific requirements will be requested.
~ Efficiency data
2
CwJts^cR.-. pu-ijLI C SeaU|C(f Of ^oi-OftA0x> , pu8lll"0 Cohort A Da
C-72
-------
KtrtWT ,t>re7C«"TiA>6 PA-TA
f
DATA ITEM
UNITS






*4



'

Test No.

t2j




¦ —-TV-, '
Time
Hours
OZoo
0$$O
0900
a9So

/f Js








•







DRAFT LOSS DATA









- -
- - 1

1 ' -

-"!!! 1H -"l
•tMib,
- • wy

. <
-



AH Air In .
"Wg






AH Air Out
"Wg






Windbo*
"Wg






Furnace
"Wg






Econ Out " —'
"Wg




;

AH Gas In
"Wg




—

AH Gas Out
"Wg






Precip In
"Wg






Precip Out
"Wg






ID Fan In
"Wg






SH Outlet Leg TC's
F






RH Outlet Leg TC's
F














.















PULVERIZER DATA







Pulverizer #







• Coal Flow % 13
MLB/HR
Pj(f' 0
?:07
IZ4.6L
tvo-if
t'-fz, 6
Ml, 97
* Pri Air Flow
MLB/HR






* Sec Air Flow
MBL/HR

,




Pulv Amps
AMPS
¦





PulvDiff
"Wg






PA Inlet Temp
F



__


Pulv Out Temp
F






PA Flow Damp
%






PA Temp Cont Damp
%






Pri Air Fan* Amps
AMPS






Z'A Tt f3
F
)U
)lg, O
m.*
1 if.1
tt
\%t, L
2". 13 » >>
F
•ur.t
tZJ.'i
it?, t
iil.i
it"? *
(i-7.2
» 2-C '• '!
F
i 21.7
iZ3.o
1LIJ
U3.J
11 J.o
Hi.4
,, 2-0 •' "
F
IZf^
I li. h
itt.t
iZJ.o
12,4-7
IZb.f







































		
The DRAFT LOSS DATA listed on this page is of value, but not absolutely essential for performance analysis.
* ¦ When indicator scale is in different units, provide conversion factor.
d> Efficiency data
3 _
CU5TPMER. pn-flt-lc SC£i/iC€" £)F CoLOfZAOo, f>H.£6L0, tZoLDlZADO
-p.	**	^	»
C-73
-------

KUWT* ot'&tcvn tut* path
DATA ITEM
UNITS











Test No.

»2J/ ?/(?£/





Time
Hours
*7 I */**¦*
ilao
til O
I Jo 0
/3?0
jLf LfO
i«? a
i't/fTffKTT 6(taSS &s*i-

7-1 i,$r

Zi 6,S2.
3 or, sz
Z1o>l7
2*0
tujiT" oij t,o*« oev><^o







. BOLLEH TEMPERATURES ,




j 1

¦ - - ¦ <6/*9z
- .jf

<¥£1,y
HbS.0 'j


Water l*aleon • • 3/1
F
fSW-3
SS%,t>
STV. ^ '

TT7.Z
sV4. *5
Stm Lvg PrJ SH 57 4- / UST
F
7il. i/p/o,y
isin/wj

7rih&t
^.e_
Wi>1
*}fkt£

/ ¦ =i ^
Stm to RH Attemp n
F
tot.)
tik-l
6)3.9
io 0 1~(a
m.1)
6 10.7
Stm Lvg RH Attemp 5 If
F

svi-i
5"MI. £?
ST
mt>, 1
























HIGH PRESS FW HEATERS







FWLvgll Htr
F






FW Ent #1 Htr 3
/ £
I3/.2
nu
Hhr
(12. j.
1
l?e.r
FW Ent #2 Htr S
f c
/jtj,/
/rs./T *J HP HT* tr/^p 7
c
¦/fv.ar

(lf-1 .
ftps'
t°tzj
W-b-
itm To *3 HP Htr temp ie>
p.
«.z.1
rMif.fc

^7-J
i'S-Lf
s-ji.t "
STM To #3H?rtT£- ?/?£Si tW<
L P5l6
tjSS
LjfO
47s '
o

4 to
vMiti TEMf 8 C 2 ol S- 2o5.o _ 20a.^ zoS.I
tUS ToHSfi- P^iiLlC SER&ce aF CoLoa RueBCo CvLo&A&o
To6 *l°i ; . - ,^6-Soz.
>
C-74
-------
^Jk1
pcfrArr o'pefcflTina
"V
DATA ITEM
UNITS
Test No.
Date

Time
Hours
It oo
t(lo
i?0 ®
IJ!"
/ 
u.
jfi^4
s^t>nku.\ "stiifcV't .1

whi-r
Wfvt,
Ht'ijm
Air EntSec Ay
vf\s

t. i/
"$¦

yifoaa- f
l9i.fi ITi-3
fOi .tfiol-if

Air Lvg Sec AH
n/23
fvr/sVfi ^
rvi.

& if IN 14
PV/.yjtfj
SV«iA-.?r>
ru.tfsi+s
CD
©
Air Lvg PA Fan
Air EntPri AH
Air Lvg Pri AH
Air EntPulv
Ambient Air
jL
3/. 1
-ILL
1°.i£_
3a,r

MISCELLANEOUS
Iftl.k
FeedwaterTlow
*?oZ.
LB/HR
nsi- Z
ftlo.?
Iflt, Z
lUI'Z
IMIlL
SH Spray Flow

LB/HR
RH Spray Flow
1ol>
LB/HR
o,3
4f-or
44-<7

qf.zz
^¦37
SH Spray Valve Posit
%
RH Spray Valve Posit
%
'HP Extraction Flow
LB/HR
2.t7/2>r

Oa Lvg Econ
Jab/SQ't
%
AVz.il


¦lAt/l.tl
CO] Lvg Econ
%
NOx (if avail)
Oa Lvg AH
COa Lvg AH
%
Oi Lvg Hot Precip
%
COi Lvg Hot Precip
%
Oa in Windbox
%
CO] in Windbox
%
NOx or CF A Port Posit
+ Fuel Analysis
%Z
Burner f Out Serv
_
Br

Advise location of flow nozzle with respect to SH and HH spray takeoff,
* - Aiiy high pressure steam extraction upstream of reheater, excluding FW heaters,
+ ¦ Report data available - specific requirements will be requested.
(2)- Efficiency data	,
2
CujTn1^E7Z > pu.f}l 1 ^ SoZ^ICf Op c-oLOfiA Do	O (LoLOi?/^Oo
C-75
-------
C-76 I
-------
rt-HN i
z
r I WW C/t ( rT
DATA ITEM
UNITS
*>





0<



Test No,







Data

iz/a/m





Time
Hours
ISP.o
£.i"3o
Lies
lb 1°


XJSTAiJT SSJ. (^055

3UW5
3^1,17












J BOH	EB T£MP£RATXJR£S







T IMaiiMSiM''" ..'•'55?--
•*- F--
-i





Water L-wjtcon ?H
'F

5-73.(?




StmLvgPrlSH SI4-/ fiS~
F
W'ffm.





Stm Ent Piat SH —
F






Stm Lvg Plat SH '—
F






Stm Errt Sec-SH _ 1 / t
" . F
7i»j/m3
7*7




Stm Lvg Sec SH i
F
ioH-7
lezi.7


'

Stm to RH Attemp n
F
{,33.1





Stm Lvg RH Attemp SH
F
Si 1
ri?.2




Stm Lvg RH - bol.
F
Ibd 2.3-





Water to SH Attemp 50f
F
ZM
nt.s"




Water to RH Attemp ?on
F
lll.L
•bti'i




























BOILER PRESSURES






-
Water to Econ 6e5"
PSIG
27N-?
v??*7




Drum Press bob
PSIG
253 4-S
wm.y




PSH in Press —
PSIG
_
—.




Stm Lvg Sec SH £0/
PSIG
21^1-7
2331-?



.
RH Inlet
PSIG
S-Zlff
5T4.»




RH Outlet (,o"i
PSIG
473.V
5-It?




























HIGH PRESS FW HEATERS







FW Lvg #1 Htr
F






FW Ent #1 Htr 3
X C
I^Z.Z.
m.t




FW Ent #2 Htr £
F c
1 s*{- i
)S7>Z




#1 Htr Drain 4
r c
(31,0
1 «+lt0




#2 Htr Drain £
/ c.
1
/4f.fc




Stm to #1 Htr-Temp /
F
rfi
izSH




Stm to #1 Htr - Press
PSIG
??


-


Sun to #2 Htr- Temp r
F
*7173
fife,?




Stm»#2Htr-Press L«C*t-
psjg
2/0 •
ItL




fui EfJT *j Hf> mn re/Hp 7
c
117-o
i *1.f




^TM To «3 «T£ TEMP /IP
p
SI o
Jo6 aJo- ; £6-5 02.
'1
WS"5", Tc ?e?« §/S»J7T*
fueBi-d C-oi.o«2/udo ,
C—77
-------
PlAaJT o'pejZATtsM
DATA ITEM
Test No,
UNITS

Date1
Time
Horns
IS" Ou
So
AIR & GAS TEMPERATURES
Flue Gai Lag Earn-1 24 h€ " *
ZofZJ

Tfc»€»l-»9-

Air EntSecAH
Mil?
%

*>wir-7
Air Lvg Sec AH
12123

Air Lvg PA Fan
Air EtrtPriAH
Air Lvg Pri AH
Air Ent Pulv
Ambient Air
dL
30 M
3SML
MISCELLANEOUS
Feedwater Flow
Jl°A
LB/HR
)UoS
ZlZg.l
SH Spray Flow
lot
LB/HR
1Q.T7
RH'Spray Flow
321
LB/HR
WW
HI-72
SH Spray Valve Posit
%
RH Spray Valve Posit
%
'HP Extraction Flow
LB/HR
Oi Lvg Econ
COj Lvg Econ
Soy/3o'/
%

3.W
?ui
NO* (if avail}
0; Lvg AH
%
©
COj Lvg AH
Oi Lvg Hot Precip
%
COj Lvg Hot Precip
%
Oj in Windbox
%
COj inWindbox
%
NOx or CFA Port Posit
+ Fuel Analysis
Burner # Out Serv
MbbwUi
Advise location of flow nozzle with respect to SH and RH spray takeoff.
* - Any high pressure steam extraction upstream of reheater, excluding FW heaths.
+ ¦ Report data available-specific requirements will be requested.
(2)- Efficiency data	.
2
CMJTo^en: PUBLIC - S£&VlC(r of'^LvaAOQ > puetlLO COLO#ADt*
•V. A ... *
c-Z8j
-------
PcftfJT ,Of>eKA-Tt/*t> VQtA

DATA ITEM
UNITS
L
' 1—




Test No,







Date


./ViVW
;
«•


Time
Hours
iro0
1 n»




















DRAFT LOSS DATA







•	-	:-4

	 -h





1
•SCAH In *Out)
"Wg






AH Air In " —
" Wg






AH Air Out
"WB






Windbox
"Wg






Furnace
"Wg



- !

- '
Econ Out "
"Wg




\

AH Gas In
*'Wg




—

AH Gas Out
"Wg






Precip In
"Wg






Precip Out
"Wg



-


ID Fan In
"Wfl






SH Outlet Leg TCs
F






RH Outlet Leg TC'i
F

, -












... . , •















PULVERIZER DATA







Pulverizer #







• Coal Flow fit3
MLB/HR
147. to-





* Pri Air Flow
MLB/HR






* Sec Air Flow
MBUHR






Pulv Amps
AMPS






Pulv Diff
"Wg






PA Inlet Temp
F






Pulv Out Temp
F







PA Flow Damp
%







PA Temp Ccmt Damp
%







Pri Air Fan Amps
AMPS



•



pf*4V. Z-fi Cefit/fi: £ -T<3+f
F
124.%
fU.fc





t( 2-6 '< "
p
12. rW






u 2-C
c:
111.6
fZ2J.





,v 2-s> •
F
its-.z


-















































The DRAFT LOSS DATA listed on this page Is of value, hut not absolutely essential for performance-analysis.
• - When indicator scale ts in different units, provide conversion factor.
(2)- Efficiency data
,3 _	"
/•jitTRMrt. liutXi.tr $etL\tiCJe OF Cot-OliAOo . pH-EftLO, OtOfiADo
;€-79!
-------
C-3
WYQDAK
GASEOUS EMISSION DATA
C-80
-------
C—81
-------
C-82
-------
C-83
-------

P kit.
ML
W*»U
(Ml-VA
Pu* Of
iiKgiyi':
NO*
Co
mA.
LPi.
UL
Pv
ML
5®V
iM.
coM-fn-rkr, n. ° V />¦»-
w
(Mi"V>
bo
L&i,
1*1^
50w
iti^X

OjDO
I*/
oWo
35i
bioo
W

a
Offio
3sr
0400

o?i?o
m
t>W
353
looo
3*1
M>


o
00
4*
/30
im.
i£L
3ty

3<£
flee
345"
il£l
3 to
/f^3
5^3
2^>*>
35&
2/w
1H.
two
3*r
t
l*>00
310

Xy«>0
117
Wt
5"J-

Y-'£-
51



tfto
11
tf.Sa
__

5&.r
0«
m
W>
il
li.SS"
tA*
w
Mi
n
ilL
51
It.uv
jut:
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Date
Test No.
J-3I- *5

PAS CONCENTRATION r<\! CMLAT10M
Operator 	

Avg Gas Response, Davg
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TOTAL.
HOUR
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FURNACE SLAG CONOlTlON
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/
/
TOTAL
HOUR
H3 Cold
Oaa Tone
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Congmuii PjtnM
So
—
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5 ?
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Total


















SH1PT
FURNACE SLAG CONDITION
SOOT SLOWING LOO
IK 1 & Ifl 1
Out o< Sar«>«a


Group ¦
Oroup 2
OrOuO 3
Group *
Group 5
> G'ouot
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3300 - 0700

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vvv'
V "'
K.

0700 - 1500

X /<
X XV
K AX
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V ¦* A


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-------
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best available copy.
FfHM N9 3111 * B
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WYtlAK GENERATION
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SCALES


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33
34


















/
/
24
TOTAL


















/
/
TOTAL
HOUR
H2 Cold
G»» Term
Sooi Blow Air Con
CondOHIi P.i(npi
BO<'«r Fltd Pumoi
Fo'ctd Ora<1 Fan
1 ruJucad D't'i Fia
Suphi
Rah«a(
SuOtt AllMnO
F 'ON
Rhi
Sorav
WATER

ENDING

A
B
A
e
C
A
a •
A
B
A
B
T had
T«no
A
B
F'Ow

Raw
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SHIFT
FURNACE SLAG C«N»ITI«N
S««T BLOWINO L*G
¦ K 1 * IR i
#ui •> Satwica


Gr«u» 1
Oftup2
Gr«u« 3
Grau» 4
G'«u» 9
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NO 319B 9 BO
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WYODAK GENERATION
HOUR
"0(5*5 7?
17J/Z
&&2S~sr
NET
ENDING -
G'Oii Generation
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WYODAK POWER PLANT - STATION LOG
WYODAK •
PLANT OPERATOR LOG

2- fr-
HOUR
iND
¦ NO
(NO


BioO'i
Lui>a
o>«
H2
EHC
EHC
Drum
Throl I'a
Amb iant
E«Hau*l
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Air
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Co'«i E«0 T«mO
AIR htA'ER Li AS
n , out
HOUR |
ENO'NG
GEN
AU*
STARTUP
VfiflS
VOLTS
Pim
Tamp
Pfill
Pratl
AMPS
Pratl
Pratl
Air Tamo
prail
Tamo
T tmo
A
B
a B
ending!
1


















/
/
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7


















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10


















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19
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/
20
21


















/

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32


















/
/
23
23


















/
/
23
34


















/
/
24
TOTAL


















/
/
TOTAL
HOU*
H2 Cold
Oas Tone
Soot Blow Air Com
Condanuu P-tmpi
Dollar Favd Pumpi
Foread Drall Pan
loducaa Dra'i ^an
Suont

SuoM AM«mo
F'om
flhi
Sp'iy
WATER

ENO'NG

A
B .
A
B
C
A
B
A
B
A
B
Tamo
Tamp
A
8


naw
PiM«'
T-*«I«U
Fu 9'
1


















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Wlr Tanh
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33
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IN PLANT SILOS

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7
15

10

















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11








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19






















16

















UNIT O'ERATO"
17

















73000700 TV.,,,,.*
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0700 1S00 / '/Jf-.r/L. 	'4
19

















i soo 3300 );*!+S '
20














*



21


















27


















23


















34


















Total


















FURNACE SLAG CONDITION
SOOT SLOWING LOO
3300 - 0700
0700 - 1500
1SOO 7300
-------
Reproduced trom
best available copy-
FORM NO 319fl 9 80
'O
I
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WYODAK POWER PLANT - STATION LOG

WVOOAK GENERATION

hour
IND
'NO
(NO


atoOii
Luba
Oil
m2
ErtC
EHC
Drum
Throttla
Amt> >ant
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N - OUT
HOUR |
HOUR
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NET
ENDING
GEN
AUJ
START UP
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Pratt
Tamp
Tamp
A
9
A ' B
ENO'NG 1
ENDING
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Aunliiry TfantlO'mar
Start up Tramlormar
GEN
1


















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15003300 /A7;h,H,) *4

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7?r

PLANT OPERATOR LOG
31

— ,
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Total


















FURNACE SLAG CONOITION
SOOT BLOWING LOG
6AXI	////		•-,*	- V/X	x/Vr	,	arc i:ysf
X < < X-	/> < > x		— * /	4—A-A	nuJ	¦* < * — x			
Mc'/y'	y^ A l>/>v xxy*L [ • / |y Xst' n	
-------
Reproduced from
best available copy.
FORM NO 3'9fl '
0
1

VVVODAK GENERATION
HOUR
23J V4,
J SrK if rt

NET
ENDING
G'ofti GinnKon
Aunlif'v Traniformat
Start tip T raniformar
GEN

Mat..
WW
Mat*'
MW
Matar
MW
MWH
I
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Nat
Main Xmtr
Gm
Van Ou
Gan
t Va't tn
Auk Xmtr
Mvar °
ACC 1A2
MW
iCC 103
MW
Coal
• Handling
P'H
Prn
7'ii 77

a ma??
7 Iftf
rfrj * (
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nvvz
nroz
/ tofto?
IfrlZtf
Total
!.to\
j

SDH
V"
JoV
?7
1 I
in








WYODAK POWER PLANT - STATION LOG
Coal lmagrato'f
SCALES


A
e
c
O
E
H 1
H3

Pxt
7?&7o7
??76?t
L7hrt
7J?2jd
7/G> \ 0
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727/0

Total
jim*
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7i30(
0

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1 It Mo








/}«^i nis
u.iv 	! tt'i
WYODAK
PLANT OPERATOR LOG
131)
2-/Z-

HOUR
IND
¦ NO
IND


"¦O"
luba
Oil
H? .
E'lC
6HC
Drum
Throttle
Ambiant
E.h.u.i
CvhauiT
A.<
Rtmoval
Co',- E«o t«M-
n. i
//j". 0
V/.Y
If70
i c
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74
TOTAL


















/
/
TOTAL
HOUR
H? Cold
Oat Torre
Sool Blow Air Cott
Condanuta Pjmpt
Soilar Fl«d Pumpt
ForcM Dra't Fan
inducnj D>a'i Fan
gut»h.
Rohaat
Supttl Aliamp
F 'OM
ntn
Sorav
WATER

END'NG

A
H
A
B
c
A
B
A
D
A
B
Tamo
Ttmo
~
B
F'Ow
| Raw
F,H«<
T--HIU
F..«'
1
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rj
—
?7$
7?/
/tr

770

io'V
lonl
//s~
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yP

Wt' T»nt>
Wir Tank
w». rank
O-i
vr
¦		

S> 'n

—
J 7?
T?f
/¦>7


•ZtrC
not,
/'03
. /t r
/C-o
&-o
33

2 &
		

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IN PLANT SILOS

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SHIFT
FURNACE 9LAG CONOlTION
SOOT SLOWING LOO
i« « & ifl'i
Out of S«»wica


G'Oun 1
Qrouo 3
Grouo 3
Group 4
Group 5
0'Oud6
G'euo7
O'oue 9

3300 - 0700

Jrxyx
> xy v
Xxx-y
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yx,r,r
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V
ST-' '
0700 1500


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1500 7300

m
mC
K
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M '

Xf


-------
0
1
(|HM N» 3191 • ••
	' - ¦-¦'¦ -

WVMAK GENERATION
HOUP
3C> Z £ 9
> 1 VV Cc
&y?7Y
NET
ENDING
G'oll Caiion
Auxiliary Tramformar
Start uo T'antformar
GEN

Matttr
MW
Maiar
MW
Malar
MW
MWH
1
7 *>1^1
jr/

30


3 77
2
3/t>7^
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3 >122
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23
n zzs

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14
3i f 7 7
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Day Total
(2 JO
72?
yo~7
bo



Prv Total







t> to Oaia
















Nat
Main Xmir
Can
Van Qui
Gin
Van i
Aua Rmlr
Mvar
Start Up
Mvar
ACC1A?
MW
ACC 192
MW
Coal
Handllnf
Ptm
' lot?

£>iZJ
r 7r//W
StYo
' 57/0 1'
17tfY
flrr/^
Pin,
! :r/t
rhl/Z
^2, 1
r 7Vjf?

S-J7A1/
">7S-)7
/trcC
Total
7S/0
71
c
? X7?
/
7 3/6'
c,z
to
in Mo








-•
Coal inragrafon
SCALES


A
G
- c
~
E
HI
H2

P'M
9l7i! 7
1o7'YS
'iS')e


/


ffm
IK-7'7
Wt:-;

i?

(?
7W*2

Toial
*j> 9f0
7,7fcfo«jC.^7 ij. ^
5
a
3HZ.
V
•	
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ks rr

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c. -0
icrC,
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ao G

r.o/l^'g
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9
0 0
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¦	
XI

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I
H'X Of
i<(-1
AT


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9'
10
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7.0
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r
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TT*'

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10
11
r

		


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ft *1
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fT/iiJt
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16
17
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2*-

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r,i'/
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19
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4
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34
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" T//> >
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-71
22

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/
/
22
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34
TOTAL


















/
I
TOTAL
HOUR
H2 Cold
Gas Ton*
iOOl BiOwAir Carre
Ampl
Conainitu P impi
Ampi
Boi'r Fifd Pumot
Amot
Forc.d Draft Fan
inaucioD'l'i fan
Ampi
Swhl
Rah«at
Suphl Altamp
F ¦eC
tOOZ,
S-J-


7
e-(
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—
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4
"rf

20I
S<*
SJ
	
J7t
ni


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15
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sc,
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—,
17i>
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>/-/

3bJ

ttob
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6
tr
—
3.00

S 7
—
77*
JO

/6t>
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395
iCoX.
ST
~ *73
s*c>

7
7vT
	

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176

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nf

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1 ?o
!r*D 3
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22


















23

M
		
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24
r<
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•
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777
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Total


















SHIFT
FURNACE SLAG CONDITION
SOOT BLOWING LOG
IKiH iR'f
Oui of


G'ouo 1
Group 2
G'OUP 3
G'OUD 4
Group S
' 0'OUD •
O.o™ 7
G'ouo 8

2300 - 0700

KYXJC
if XX
?vx*
.TV* JT
y 7 x.x
fSXK
yx
X
sr n
0700 - 1500

v.v.w/
yxk'^X
< y/
l- X
'¦' k-
¦-¦ V.
k v
-v;.
If!;. -
1S00 23DO

/if A

y
.¦ v \L
X V /
X

K

-------
WYODAK
COAL AND ASH ANALYSIS
C-112
-------
WYOKAK COAL ANALYSIS
Date
2-1
2-2
2-3
2-4
2-5
2-6
2-7
2-9
2-10
2-11
2-12
2-13
2-14
Avg
Time
2300
1700
400
1530
1523
1010
300
2330
800
1600
434
311
500

Ultimate (wt% dry)














Carbon
64.36
62.34
60.90
61.75
61.94
59.52
57.07
56.60
59.77
57.73
57.65
58.50
57.1
59.63
Hydrogen
4.77
4.90
4.66
4.31
4.59
4.82
4.43
4.20
4.45
4.17
4.14
4.58
4.45
4.50
Ni trogen
.86
.80
.85
.91
.88
.84
.80
.82
.86
.84
.84
.78
.76
0.84

.68
.98
.73
.37
.58
1.86
1.09
0.63
.71
.33
.35
1.03
.67
0.76
Sulfur
.67
•91
.73
.36
.59
1.89
1.03
.60
.69
.31
.34
.96
.71
Ash (ASTM)
6-81
6.31
8.38
10.32
6.49
10.03
12.11
9.57
6.64
9.67
10.99
10.57
11.14
9.16
Ash (240B)
6.00
5.56
8.08
6.08
6.40
9.99
12.18
10.33
6.37
10.30
10.89
10.05
11.03

CaO (wtX ash)
24.49
22.58
17.95
23-19
21.37
12.94
11.83
13.45
22.49
13-91
10.45
11.46
10.65

-------
WYODAK ASH SAMPLE ANALYSIS
Sample NumDer
925
942
945
950
982
983
002
004
005
006
930
953
940
984
Date
2/2
2/3
2/4
2/5
2/6
2/7
2/9
2/11
2/12
2/13
?/14
2/4
2/2
2/6
Type of Ash
Fly
Fly
Fly
Fly
Fly
Fly
Fly
Fly
Fly
Fly
Fly
Bottom
Bottom
Tip
Ultimate (wt% dry)











[


Carbon
.08
.42
.09
.14.,
.07
.20
.12
.10
.15
.28
.28
.25
.37
.26
Hydrogen
.02
.02
.01
r-01
} -01
(
.01
.02
.01
.01
.02
.04
.04
.05
.01
Ni trogen
.00
.04
.02
^00
s
.00
.00
.02
.01
.02
.01
.00
.00
.06
.01
Sul fur
.41
.36
.44
.47
.47
.44
1.03
.40
.37
.42
.40
.15
.09
.09

.43
.28
.43
.43
.48
.42
1.06
.41
.33
.44
.41
.17
.11
.08
Ash (ASTM)
99.68
99.60
99.76
99.76
99.73
99.74
99.29
99.73
99.73
99.75
99.70
99.58
99.13
99.44-
Ash (240B)
99.66
99.36
99.79
99.58
99.83
99.75
99.26
99.79
99.81
99.48
99.71
98.76
97.39
99.45
CaO (wt% ash)
19.32
17.88
18.57
18.69
17.51
16.46
21.14
17.19
17.93
18.17
17.93
11.27
11.77
8.72
-------
PACIFIC POWER & LIBHT
COAL ANALYSIS	JANB5
DAY
TONS
XMOISTURE
XASH
XSULFUR
BTU/LB
1
5829
31.6
5.9
.51
7957
2
5740
32 a 2
- 5.2
. 35
7924
3
5946
29.6
,5.7
. 36
8278
4
'5832
30» 5
5.4
.39
8011
s
5941
29. 1
6a 8
.28
8126
6
5398
30.5
5.9
.27
8223
7
5446
29.1
5.8
.35
8315
B
630B
30.0
6. 1
.43
7941
9
5811
29.6
5.8
.34
B134
io
5934
29.3
6.1
.43
8261
it
5752
29.7
5.4
.45
8195
12
6013
29.3
5.9
. 37
8119
13
5851
29.1
6.1
.42
8231
14
5725
30.8
5.5
.25
7946
15
5826
30.9
5.4
.30
7983'
16
5815
30* 2
5.7
.40
8081
17
5779
30.0
5.5
.39
8127
18
5888
30.2
6. 1
.46
8008
19
6650 '
30.4
4.6
.30
8160
20
6164
30.4
5.3
.32
8066
21
5341
27.3
6.0
.40
8289
22
6560
29.3
6.4
.78
8137
23
5752
30.7
6.6
.67
7909
24
5742
30.3
6.1
. 65
8081
25
5547
31.6
6.0
.40
7970
26
6105
31.8
6.4
.35
7812
27
6038
30.8
6.5
.52
7950
28
5945
29.0
8.0
.70
7982
29
5518
29.8
6.3
.64
8148
30
6044
30.5
6.3
. 54
7963
31
¦ 5870 ¦
29.5
6.3
• 44
8109
WEIBHTED AVERABES




182110
30. 1
6
.44
8077
cci Plant Manager—PIant Operation*-Plant Engineering
Thermal Operations Dept¦-900 PBB, Resources Dapt«-300 FSB
C-115
-------
PACIFIC POWER St LIGHT
COAL ANALYSIS
DAY
TONS
XMQISTURE
•/.ASH
1
5981
28.9
6.9
2
6107
29.9
6.2
3
6352
29.9
6.9
4
5980
29.5
6.3
5
5962'
29.5
6.5
6
5680
29. 1
6.5
7
5302
30.1
6.4
8



9



10
5502
29.9
6.1
X8ULFUR
.57
.50
.5 6
.46
.36
.59
,40
BTU/LB
8126
8131
7993
7987
8081
8123
8012
8028
WEIGHTED AVERAGES
46866	29.6
6.5
54
8060
ccs Plant Manager-PIant Operations-Plant Engineering
Thermal Operations Dept.-900 PBB, Resources Dept.-300 PSB
c-uOs-)
-------
MILL NO.
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REMARKS AMO COMMENTS;
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