Fuel Tech, Inc. 27601 Bella Vista Pkwy Warrenville, Illinois 60555 630.845.4500 www.ftek.com 

# Wheelabrator Saugus Inc. WTE Units 1 & 2 Two 750 TPD MSW Combustors 

# SNCR Optimization Report

Prepared for: John T. O’Rourke Project #: 470S January 29, 2010

Copies To: Wheelabrator: Timothy J. Porter, John T. O’Rourke, Scott Manning, William Hoen Fuel Tech: Bill Cummings, Alex Dainoff, Da ve Kieffer, Brad Gieseke, Project File 

### 100 Salem Turnpike Saugus, Massachusetts 01906-1899Wheelabrator Saugus, Inc. Service Report WTE Units 1 & 2 January 29, 2010

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## 1.0 EXECUTIVE SUMMARY Fuel Tech performed furnace gas temperat ure profiling and conducted SNCR optimization testing at the Wheelabrator Saugus J.V. waste to energy (WTE) facility in accordance with the NOx Control Optimization Program submitted to MADEP for Best Available Retrofit Technology (BART). The overall obj ective was to try and achieve lower NOx emissions while minimizing ammonia slip levels below the cu rrent permit limit of 10 ppm (dry, 7% O 2 

### ). Phase I- Furnace Temperature Profiling January 18 to 22, 2010 Furnace gas temperature profiling was done on Units 1 and 2 usin g the SpectraTemp Gas Temperature Monitor with data logger. These data were th en analyzed with boiler operating data taken from the boiler distributive contro l system (DCS) process data historian to determine present operating condition s of the furnace and NOx control. Phase II- SNCR Process Optimization Januar y 25 to 29, 2010 The SNCR system c onfiguration and operating conditions were then change d to the extent allowed by the available furn ace injector points and number of operating injectors to determine the capability of re ducing the NOx emissions while minimizing a mmonia slip. Present and alternative SNCR injector arrangements (loc ation and number of injectors in service and reagent feed rates were adju sted to determine the best SNCR system configuration to achieve and sustain lower NOx emissions. Four and six injectors were te sted on Saugus Units #1 and #2 and six injectors were tested on Saugus Unit #2 at reagent feed rates of 0, 5, and 10 gallons per hour and results show a capability of reducing NOx consistently down to 185 ppmv (dry, 7% O2) with loads at or above 150,000 lbs/hr steam flow. Based on th ese tests it was determined that:

• Injector locations are near the lower end of the optimum SNCR operating range at normal boiler operating conditions.

• There was no significant perfor mance difference between in u tilizing 4 or 6 injectors in each furnace

• Baseline NOx varied between 240 and 280 ppm (dry, 7% O 2 

### )

• A reduced NOx setpoint of 185 ppm (dry, 7% O 2 

### ) was achieved on both units even at higher NOx baselines

• Increasing reagent feed rates from 5 to 10 gph did not appreciably lower NOx Therefore, the present injector configurations ma y be maintained and reagent flow increased to reduce NOx emissions to a target of 185 ppm (dry, 7% O 2 

### ) at loads above 150,000 lbs/hr.Wheelabrator Saugus, Inc. Service Report WTE Units 1 & 2 January 29, 2010

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## 2.0 Table of Contents 1.0 Executive Summary 1 2.0 Table of Contents 2 3.0 Unit Description 3 4.0 SNCR System Description 4 5.0 Furnace Temperature Measurements 6 6.0 SNCR Optimization Testing 11 7.0 Conclusions 15Wheelabrator Saugus, Inc. Service Report WTE Units 1 & 2 January 29, 2010

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## 3.0 Unit Description The Wheelabrator Saugus J.V. waste-to-energy (W TE) facility has two Riley Stoker boilers rated for 650 psig operating steam pressure at 850 degr ees F. both driving a 56 MWg turbine/generator which is operated at approximately 35 MWg. The generator rating was originally sized for three units but only two units were in stalled. MSW is fired on early Von Roll (“L” style) grates designed for a maximum firing rate of 750 tons per day of municipal solid waste or refuse. Each unit is fit with two auxiliary oil fired burners for preheati ng the furnace prior to refuse combustion. The boiler, furnace and grate combus tion system represent the earliest Von Roll design (circa 1975) and still are reflective of current WTE European de signs where tail end boilers dominate. Primary air is fed underneath the fuel bed through individually controlled air plenums in each of three (3 ) grate zones. Secondary air is added just above the fuel bed vi a front and rear wall headers in the lower furnace. Total combusti on air flow is split between primary air and secondary air to optimize air penetration, turbul ence and air-to-fuel mixi ng, to ensure low flame height and to minimize fly ash carryove r to the boiler convection sections. Combustion testing this past year has led operators to run a mini mum rate of overfire air with enough rear wall pressure to keep the combustion pa th towards the front furnace wall. Operators use fan amps as a guide to minimizing overfire ai r flow from day-to-da y. This ensures more radiant cooling in the furnace thus minimizing attemperating water flow and lowering radiant tube metal temperatures. These adjustments also appear to have succeeded in minimizing combustion-generated NOx.Wheelabrator Saugus, Inc. Service Report WTE Units 1 & 2 January 29, 2010

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## 4.0 SNCR System Description

The Fuel Tech urea-based NOxOUT ® 

### SNCR Systems were supplied by Wheelabrator Air Pollution Control. The Systems were inst alled in 2000 to meet the USEP A’s Maximum Achievable Control Technology (MACT) limit of 205 ppm (dry, 7% O 2 

### ) required by the 1990 Clean Air Act. The original System was designed so th at up to eight ports per furnace wi th air-atomized injectors could be utilized to achieve the 205 ppm limit. Each injector had individual in jector air pres sure control with four injectors located on one distribution m odule for each furnace sidewall (four distribution modules in all). The original injectors were replac ed this past summer by improv ed new injectors sold by DeNOx Technologies (DNT). These inject ors are capable of higher liquid flows with larger droplets, have more open liquid internals and are th erefore less subject to plugging than the original injectors (the plant uses service water as the supply). The new DNT injectors also have an Inconel atomizing spray tube eliminating the need for a shield (the original injectors had ceramic coated 300 series stainless steel 3⁄4” tubing shields) . These new injectors improve th e overall system performance and reliability while mini mizing injector maintenance. Operator s have found that onl y four of the new injectors need be operating on each boiler with se ttings of 0.5 gpm liquid fl ow per injector and 40 psig air pressure (originally eight were used) to ensure compliance with the 205 ppm limit. The typical urea consumption for this compliance level averages between 2 and 4gph per unit. The new DNT injectors allowed the replacement of the original individual injector air pressure regulators from the distribution modu les with a single upstream air pr essure regulator to control the air to all four injector s on each distribution modul e. With the improved performance of the new DNT injectors only two injectors need to be operated on each distribution module. The injector ports are located on the sidewalls of the units as shown below in Figure 1. Due to relative differences in furnace temperature and combustion cond itions between the two furnaces, operators have been locating the injectors on Unit 1 with more of a mixed ar rangement than on Unit 2.Wheelabrator Saugus, Inc. Service Report WTE Units 1 & 2 January 29, 2010

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inj inj inj 4' 4' Port 2 A Port 2B Port 1B Port 1 A

5.9' 5.9' inj inj inj inj
4' inj

5' 5' 3.3'
EL. 62' EL. 62' (Darkened Ports are Capped) (Darkened Ports are Capped) FACING EAST

Burners FACING WEST

HEAVY ASH HEAVY ASH NORTH

UNIT #1 WHEELABRATOR SAUGUS INJECTOR PORT ARRANGEMENT

32' 32'

Burners NORTH

FACING EAST FACING WEST UNIT #2



### Figure 1 SNCR Injector Ports and Furnace Temperature Monitoring Locations 

### The original injector port locations were determined during the SNCR system design phase based on furnace temperature pr ofiling. Because of th e short furnace height and tail end boiler the optimum SNCR temperature window of 1650 to 2100 deg F in the furnace is relatively narrow and access to the furnace for SNCR in jector installation is limited.Wheelabrator Saugus, Inc. Service Report WTE Units 1 & 2 January 29, 2010

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## 5.0 Phase 1 F URNACE 

## T EMPERATURE 

## M EASUREMENTS


### Phase I furnace temperature measurements were obtained using a Spectratemp monitor. The Spectratemp monitor is an optical based pyrom eter designed to continuously monitor average furnace flue gas temperature across the entire furnace width. The Spectratemp senses light radiated from ~30 μm diameter ash particles (these particles come to equilibrium temperature with the flue gas very quickly) in three di ffering wavelengths to determine the flue gas temperature. Energy levels seen in thes e wavelengths are proportioned to find the gas temperature. The measurement principle of the Spectratemp ensures that temperature readings are not biased by water wall temperatures or radi ant heat. A Spectratemp monitor was used in the original furnace temperature prof iling during the SNCR design phase in 2000. Furnace temperature data were ut ilized to evaluate current injector locations relative to the optimum operating temperature wind ow for SNCR. By properly se lecting the zone of injection based on flue gas temperature, the SNCR process can be optimized with regard to NOx reduction, chemical flows, and ammonia sli p. Furnace temperature monitoring was conducted using two test ports located opposit e the auxiliary oil burners on each unit just above the injector locations as follows: Start Stop Unit 2A port: 1/20/10- 15:42 1/21/10- 08:01 (Boiler outage Jan 11-16, 2010) Unit 2B port: 1/21/10- 14:02 1/21/10- 15:15 Unit 1A port: 1/21/10- 16:29 1/22/10- 08:18 (Shutdown for water wash Jan 27, 2010) Unit 1B port: 1/22/10- 08:53 1/22/10- 13:09 

### The Port designations are Boiler Number (1 or 2) and front/rear wall (A for front; B for rear- see port layout in Figure 1 above). Furnace temperatures were monitored with both boilers operating at normal load between 145 to 155 klb/hr steam flow. Longer term furnace temperature data was obtained by leaving the Spectratemp in Test Port A overnight. Hourly average boiler conditions are shown in the tables following the temperatur e plots. A summary of the gathered data follows:
Port #1A Port #1B Port #2A Port #2B Average 1666.0 1653.0 1677.7 1744.6 Deg.F. Maximum 1889.4 1835.0 1908.1 1850.6 Minimum 1563.8 1551.9 1560.0 1652.5 Standard Deviation 32.5 55.5 49.2 44.6 The temperatures on both ports for Unit #1 were found to be generally lower than the temperatures on Unit 2’s ports even though Unit 1 was a few days away from a scheduled water wash. The optimum temperature window for SNCR is between 1700-2100 degrees F. The furnace temperature monitoring data indicate that available injector ports are located near the lower end of the optimum SNCR operating temperature window of 1650 degrees F.Wheelabrator Saugus, Inc. Service Report WTE Units 1 & 2 January 29, 2010

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### . Saugus Unit 1 A Port Jan 21 to 22, 2010

1500 1550 1600 1650 1700 1750 1800 1850 1900 1950 2000

16:19 17:19 18:19 19:19 20:19 21:19 22:19 23:19 0:19 1:19 2:19 3:19 4:19 5:19 6:19 TimeTemperature (deg F)

Saugus Unit 1 B Port Jan 22, 2010

1500 1550 1600 1650 1700 1750 1800 1850 1900 1950 2000

8:13 9:13 10:13 11:13 12:13 13:14 14:14 TimeTemperature (deg F)Wheelabrator Saugus, Inc. Service Report WTE Units 1 & 2 January 29, 2010

-CONFIDENTIAL - Page 8 -DO NOT DUPLICATESaugus Unit 2 A Port

Jan. 20 to 21, 2010

1500 1600 1700 1800 1900 2000

15:21 16:21 17:21 18:21 19:21 20:21 21:21 22:21 23:21 0:22 1:22 2:22 3:22 4:22 5:22 6:22 7:22 TimeTemperature (deg F)

Saugus Unit 2 B Port Jan 21, 2010

1500 1550 1600 1650 1700 1750 1800 1850 1900 1950 2000

13:12 14:12 15:12 16:13 TimeTemperature (deg. F)Wheelabrator Saugus, Inc. Service Report WTE Units 1 & 2 January 29, 2010

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TIME STEAM BLR FEED E FEED W MAIN I MAIN W IN NOX START FLOW MSTR SPD SPD SPD SPD PRESS FLOW CURRENT FLOW DUCT FRONT BACK CURRENT O2 AVG. 12:00 AM KLB/HR % % % % % inWC KCFM AMPS KCFM PRESS FLOW PRESS FLOW PRESS AMPS % PPM A B

0:00 FI201 #2_BLR_M AST_OUT SC230 SC240 SC231 SC241 PI208 FI208 II251 #2_SEC_AI R_FLOW PI209 FI2122 PI2114A FI2114 PI2114B II252 AI2201 AI6264B TI264 TI265 1:00 153.10 37.90 28.86 24.86 32.86 34.86 3.76 41.48 11.74 33.98 27.97 23.27 11.01 10.24 15.04 55.34 7.13 179.22 857.13 754.90 2:00 154.20 34.98 25.94 21.94 29.94 31.94 3.90 40.53 11.65 33.95 27.98 23.24 11.02 10.25 15.02 55.37 6.91 188.39 859.31 760.23 3:00 153.66 38.56 29.57 25.57 33.57 35.57 3.92 39.02 11.27 33.96 28.01 23.23 11.00 10.25 14.98 55.35 7.13 190.67 854.82 750.24 4:00 153.09 39.86 30.84 26.84 34.84 36.84 3.78 39.75 11.36 33.96 28.03 23.17 11.01 10.24 14.98 55.33 7.17 186.98 867.99 753.41 5:00 153.71 35.17 26.17 22.18 30.17 32.17 3.77 38.62 10.83 33.97 28.05 23.25 11.03 10.25 15.01 55.32 7.04 178.55 866.49 755.94 6:00 153.72 41.12 32.13 28.13 36.13 38.13 3.67 38.86 10.71 33.98 28.03 23.25 11.01 10.23 14.98 55.35 6.99 187.58 868.10 752.99 7:00 152.99 43.72 33.67 30.09 38.74 40.74 4.05 36.58 10.32 34.01 28.00 23.23 10.99 10.26 14.99 55.15 6.68 204.95 854.80 750.03 8:00 154.50 50.10 37.07 34.41 45.08 47.10 3.87 37.75 10.46 37.02 28.01 23.91 11.01 12.57 23.27 56.75 7.51 208.29 822.17 743.20 9:00 153.86 54.92 41.15 34.80 48.09 51.84 3.83 38.37 10.50 37.76 28.00 24.15 11.00 13.15 25.27 57.20 7.83 207.55 818.32 737.14 10:00 153.57 52.22 36.06 30.38 43.73 48.31 3.90 37.81 10.40 38.05 27.97 24.41 12.02 13.18 25.25 57.52 7.33 203.16 819.33 734.32 11:00 152.87 53.44 35.27 30.43 42.43 49.40 3.68 37.96 10.35 38.33 27.99 24.70 12.98 13.19 25.27 57.80 7.70 191.36 823.70 739.23 12:00 147.22 59.16 40.15 32.48 44.30 53.11 3.57 37.66 10.28 38.40 28.00 24.70 12.93 13.20 25.28 57.68 7.71 191.36 815.53 728.25 13:00 152.76 58.53 39.36 30.14 41.38 51.52 3.60 39.17 10.46 38.36 28.00 24.67 12.93 13.21 25.27 57.66 7.60 191.36 825.93 738.06 14:00 153.18 53.24 32.97 26.27 34.49 46.21 3.71 38.30 10.43 38.43 28.00 24.72 12.92 13.21 25.27 57.65 7.69 197.71 831.34 736.02 15:00 153.41 56.94 34.84 30.83 36.65 48.57 3.63 38.66 10.41 38.40 28.00 24.75 12.85 13.21 25.27 57.58 7.66 208.68 831.48 738.84 16:00 148.18 61.60 39.55 35.55 39.61 51.66 3.54 39.60 10.68 38.50 28.00 24.77 13.22 13.21 25.26 57.73 8.14 201.26 827.22 733.10 17:00 153.15 66.69 45.50 40.94 44.12 56.12 3.48 39.61 10.58 38.50 28.00 24.81 13.35 13.20 25.26 57.80 8.09 205.12 833.86 737.86 18:00 145.86 67.59 47.57 40.80 46.86 58.77 3.57 39.80 10.74 38.34 28.00 24.62 12.96 13.23 25.24 57.69 8.45 202.09 828.94 733.14 19:00 141.54 60.27 41.56 31.85 60.17 70.20 3.82 41.20 11.95 38.47 28.00 24.74 13.39 13.22 25.25 57.92 8.45 196.68 829.00 729.47 20:00 149.68 55.35 38.39 25.39 55.39 65.39 4.03 41.04 12.27 38.41 27.99 24.66 13.34 13.23 25.25 58.01 7.53 198.82 843.32 735.51 21:00 144.80 51.69 34.72 21.73 51.72 61.72 3.89 41.29 12.11 38.39 27.99 24.62 13.29 13.22 25.26 58.09 8.49 203.96 834.72 733.20 22:00 148.72 65.26 48.01 35.01 65.01 75.01 3.44 42.68 12.08 38.30 28.00 24.62 13.31 13.24 25.25 58.28 8.26 198.70 839.82 737.33 23:00 147.32 65.74 48.71 35.72 65.71 75.71 3.98 40.63 12.12 38.33 28.00 24.61 13.31 13.25 25.26 58.41 7.80 198.52 847.46 738.10 0:00 144.64 48.12 31.09 21.31 48.09 58.09 4.24 38.51 11.55 38.36 28.00 24.54 13.39 13.25 25.25 58.53 8.06 200.56 832.56 732.41 TOTAL 150.82 52.17 36.63 29.90 43.71 50.79 3.78 39.37 11.05 37.01 28.00 24.19 12.30 12.32 22.18 57.06 7.64 196.73 838.89 740.96 SECONDARY AIR PRIMARY AIR BOILER 2 1/20/2010
SH OUTLE T GAS TEMP

TIME STEAM BLR FEED E FEED W MAIN I MAIN W IN NOX START FLOW MSTR SPD SPD SPD SPD PRESS FLOW CURRENT FLOW DUCT FRONT BACK CURRENT O2 AVG. 12:00 AM KLB/HR % % % % % inWC KCFM AMPS KCFM PRESS FLOW PRESS FLOW PRESS AMPS % PPM A B

0:00 FI201 #2_BLR_M AST_OUT SC230 SC240 SC231 SC241 PI208 FI208 II251 #2_SEC_AI R_FLOW PI209 FI2122 PI2114A FI2114 PI2114B II252 AI2201 AI6264B TI264 TI265 1:00 152.87 52.42 35.38 32.38 52.38 62.38 4.09 39.25 11.68 38.34 28.00 24.55 13.43 13.25 25.25 58.67 7.41 209.32 844.61 739.48 2:00 157.49 54.26 37.26 34.27 54.26 66.24 4.21 38.54 11.62 38.34 28.00 24.56 13.44 13.25 25.24 58.75 7.00 194.28 854.77 747.63 3:00 158.09 43.72 26.72 23.70 43.72 58.70 4.31 37.99 11.53 38.31 28.00 24.57 13.44 13.26 25.25 58.82 6.92 195.73 859.69 746.95 4:00 148.48 62.35 45.32 42.32 62.32 77.32 4.06 39.45 11.78 38.29 28.00 24.53 13.44 13.26 25.24 58.92 7.49 199.46 836.56 742.32 5:00 148.49 45.69 26.48 18.47 45.31 59.81 3.78 40.80 11.92 38.23 28.01 24.47 13.25 13.26 25.26 58.88 7.73 194.22 842.94 739.30 6:00 146.39 60.78 40.68 20.68 55.68 65.68 3.84 47.02 16.04 38.17 28.00 24.42 12.93 13.26 25.25 58.76 8.50 204.27 846.90 742.26 7:00 143.60 68.50 49.24 28.50 63.13 73.04 4.16 45.81 15.56 38.14 28.01 24.44 12.88 13.26 25.24 58.67 8.67 229.87 850.02 740.48 8:00 154.21 63.13 43.60 26.42 54.89 63.90 4.62 48.60 18.21 38.15 28.00 24.37 12.97 13.27 25.25 58.72 8.04 183.66 883.10 748.66 9:00 148.39 62.79 41.58 27.79 50.82 61.81 4.42 46.57 16.57 38.26 28.00 24.45 13.40 13.27 25.26 58.82 8.90 188.26 852.60 742.92 10:00 152.69 61.77 39.74 26.74 47.74 58.75 4.25 46.05 15.86 38.39 28.00 24.63 13.36 13.33 25.23 58.66 8.36 203.15 877.35 748.14 11:00 151.43 76.51 54.47 41.48 61.40 72.46 3.69 44.12 13.67 38.44 28.00 24.52 13.13 13.40 25.19 58.46 8.58 197.32 859.01 746.13 12:00 147.76 63.20 41.17 28.17 46.35 59.17 3.72 42.60 12.76 38.43 28.00 24.53 12.81 13.41 25.17 58.21 8.24 195.12 849.87 739.42 13:00 148.35 75.82 53.87 40.87 58.87 71.87 3.70 43.58 13.38 38.50 28.00 24.61 13.08 13.40 25.16 58.18 8.11 201.52 852.77 739.38 14:00 157.50 58.47 35.89 22.92 41.46 53.22 3.92 43.10 13.60 38.68 28.00 24.81 13.32 13.41 25.18 58.18 7.91 207.22 866.73 749.95 15:00 149.07 66.53 45.15 32.06 52.31 60.38 3.83 43.57 13.59 38.55 28.01 24.68 12.91 13.41 25.17 57.97 8.81 203.14 850.65 739.16 16:00 156.68 59.66 43.19 30.20 57.00 50.98 4.23 43.31 14.21 38.58 28.00 24.72 12.96 13.40 25.16 57.94 8.09 207.79 861.54 748.73 17:00 156.92 61.83 50.28 42.88 58.96 52.81 4.31 44.77 15.27 38.59 28.00 24.72 13.29 13.41 25.18 58.13 8.33 193.66 873.71 749.96 18:00 152.03 73.05 62.96 62.95 71.96 63.96 4.37 45.66 15.96 38.52 28.00 24.61 13.28 13.39 25.17 58.12 8.15 196.50 876.08 747.20 19:00 145.65 58.95 47.69 56.61 51.52 46.27 4.06 46.87 16.39 38.46 28.00 24.57 13.29 13.40 25.18 58.24 8.79 199.90 874.31 739.95 20:00 154.20 56.54 46.58 58.74 52.74 52.25 4.45 42.96 14.59 38.48 28.00 24.46 13.29 13.42 25.17 58.46 7.94 205.44 861.96 748.67 21:00 157.71 40.88 35.87 35.89 40.88 40.89 4.53 39.90 12.97 38.37 28.00 24.49 13.36 13.42 25.18 58.62 7.77 200.61 861.22 748.62 22:00 157.73 45.29 40.28 40.31 45.28 45.31 4.28 38.84 12.01 38.31 27.99 24.37 13.36 13.44 25.17 58.84 7.74 192.64 862.53 749.88 23:00 157.84 38.52 33.52 33.52 38.52 38.51 4.24 36.77 10.99 38.28 28.00 24.36 13.37 13.44 25.17 58.93 7.34 191.31 861.64 748.13 0:00 158.16 38.40 31.42 31.40 38.40 38.40 4.20 36.98 11.05 38.31 28.00 24.42 13.37 13.44 25.17 59.03 7.32 206.92 862.79 749.32 TOTAL 152.57 57.88 42.02 34.97 51.91 58.09 4.14 42.63 13.80 38.38 28.00 24.54 13.22 13.35 25.20 58.54 8.00 200.06 859.31 745.11 1/21/2010 1/21/2010 BOILER 2

SECONDARY AIR PRIMARY AIR SH OUTLE T GAS TEMP



## Unit 2 Boiler Operating Data for January 20 th 

## and 21 stWheelabrator Saugus, Inc. Service Report WTE Units 1 & 2 January 29, 2010

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TIME STEAM BLR FEED E FEED W MAIN I MAIN W IN NOX SH OUTLE T START FLOW MSTR SPD SPD SPD SPD PRESS FLOW CURRENT FLOW DUCT FRONT BACK CURRENT O2 AVG. 12:00 AM KLB/HR % % % % % inWC KCFM AMPS KCFM PRESS FLOW PRESS FLOW PRESS AMPS % PPM A B

0:00 FI101 #1_BLR_M AST_OUT SC130 SC140 SC131 SC141 PI108 FI108 II151 #1_SEC_AI R_FLOW PI109 FI1122 PI1114A FI1114 PI1114B II152 AI1201 AI6164B TI164 TI165 1:00 145.02 64.16 59.19 64.19 97.19 62.19 4.39 60.00 12.80 31.65 30.00 23.51 11.02 7.51 16.12 50.39 8.80 199.34 813.10 856.22 2:00 142.48 72.65 65.51 68.04 105.66 75.76 4.18 59.60 12.87 31.98 30.01 23.85 11.01 7.53 16.11 50.44 8.73 191.68 809.46 852.77 3:00 144.69 65.22 58.65 57.19 98.19 70.19 4.00 61.19 13.60 32.21 30.01 24.04 11.02 7.52 16.12 50.49 8.89 185.66 814.56 852.36 4:00 138.63 55.04 49.02 47.02 78.47 55.62 4.32 58.66 12.35 32.22 30.00 24.06 11.00 7.51 16.12 50.54 9.50 177.30 812.28 848.95 5:00 148.79 55.54 48.80 45.51 38.63 39.34 4.06 58.90 12.22 32.65 30.00 24.47 11.01 7.47 16.13 50.55 9.38 179.34 837.83 865.94 6:00 133.54 67.92 57.99 56.98 48.99 43.99 4.51 62.22 16.26 32.80 30.01 24.57 11.01 7.53 16.13 50.55 10.11 201.89 797.97 848.07 7:00 136.75 71.89 60.00 59.35 52.66 47.46 4.38 62.11 15.55 32.68 30.00 24.53 10.98 7.42 16.13 50.46 9.90 222.52 802.15 855.35 8:00 135.04 70.59 58.61 56.26 49.33 43.38 5.13 60.88 15.69 32.72 29.99 24.47 10.99 7.51 16.13 50.50 9.72 190.42 799.56 851.05 9:00 139.64 59.73 47.53 43.99 37.21 32.66 5.17 63.37 17.66 31.62 29.99 23.51 10.99 7.46 16.13 50.44 9.71 199.83 804.97 851.49 10:00 144.73 75.33 62.27 60.27 50.27 47.27 4.42 62.33 15.44 31.22 29.99 23.02 11.01 7.49 16.13 50.32 9.76 208.20 811.04 854.88 11:00 146.69 70.39 57.36 55.36 45.36 42.36 4.35 61.29 14.34 31.22 30.00 23.01 11.02 7.48 16.14 50.19 9.45 204.45 814.35 860.51 12:00 140.65 71.91 58.86 56.86 45.87 42.84 4.24 61.52 13.92 31.39 30.00 23.20 11.00 7.49 16.14 50.08 9.67 202.91 806.90 849.79 13:00 149.99 71.66 58.70 58.11 44.70 41.70 4.10 61.00 13.34 31.14 30.00 22.92 11.02 7.55 16.13 50.02 9.02 203.36 820.65 860.26 14:00 147.09 67.72 54.77 54.77 40.05 37.77 4.02 61.22 13.33 30.84 30.00 22.57 10.99 7.56 16.13 49.95 9.27 199.39 815.80 856.31 15:00 146.22 73.46 62.15 62.13 45.49 43.49 3.93 60.88 12.95 31.22 30.00 22.97 10.99 7.55 16.13 49.88 9.40 203.79 812.25 857.19 16:00 152.16 56.46 55.96 55.96 28.07 26.05 4.36 59.67 12.72 31.06 30.00 22.74 11.01 7.59 16.14 49.85 9.06 200.58 816.11 865.78 17:00 156.80 54.28 56.06 56.06 25.26 23.26 4.75 59.97 13.58 31.20 30.00 22.94 11.00 7.55 16.14 49.91 8.87 197.69 824.47 872.05 18:00 145.58 67.05 73.59 73.60 38.07 36.07 4.95 58.72 13.68 31.41 30.00 23.17 11.01 7.50 16.13 49.90 8.53 204.01 823.99 856.74 19:00 147.59 38.39 45.41 45.41 9.41 7.41 4.94 58.66 13.82 31.54 30.00 23.34 11.01 7.55 16.13 50.00 9.09 195.10 808.39 865.58 20:00 153.23 45.13 52.15 52.19 16.44 14.69 4.88 59.29 13.96 31.26 30.00 23.13 10.99 7.50 16.14 50.14 8.58 200.19 818.34 872.07 21:00 153.68 29.79 24.90 24.85 29.83 29.76 5.00 57.66 13.30 31.43 30.00 23.13 11.01 7.53 16.15 50.26 8.68 200.07 815.45 872.98 22:00 152.67 43.28 38.32 38.32 43.32 43.32 4.61 57.79 12.30 31.60 30.00 23.50 11.02 7.50 16.15 50.44 8.68 201.18 811.68 871.97 23:00 154.75 36.09 31.09 31.09 36.09 36.09 4.83 53.54 10.88 31.98 30.00 23.78 11.00 7.53 16.14 50.53 8.10 199.97 818.91 864.35 0:00 153.80 36.45 29.46 29.47 36.45 36.45 4.78 54.54 10.96 32.31 29.99 24.13 10.99 7.50 16.13 50.60 8.18 204.31 820.81 863.02 TOTAL 146.26 59.17 52.76 52.21 47.54 40.80 4.51 59.79 13.65 31.72 30.00 23.52 11.00 7.51 16.13 50.27 9.13 198.88 813.79 859.40 BOILER1

PRIMARY AIR SECONDARY AIR GAS TEMP

1/22/2010
TIME STEAM BLR FEED E FEED W MAIN I MAIN W IN NOX START FLOW MSTR SPD SPD SPD SPD PRESS FLOW CURRENT FLOW DUCT FRONT BACK CURRENT O2 AVG. 12:00 AM KLB/HR % % % % % inWC KCFM AMPS KCFM PRESS FLOW PRESS FLOW PRESS AMPS % PPM A B

0:00 FI101 #1_BLR_M AST_OUT SC130 SC140 SC131 SC141 PI108 FI108 II151 #1_SEC_AI R_FLOW PI109 FI1122 PI1114A FI1114 PI1114B II152 AI1201 AI6164B TI164 TI165 1:00 154.12 50.21 42.13 42.13 50.13 50.13 4.43 57.03 11.30 32.55 30.00 24.31 11.01 7.55 16.14 50.64 8.20 200.25 827.29 862.35 2:00 145.93 69.89 58.84 58.66 72.37 72.37 4.36 57.77 12.01 32.64 30.00 24.56 11.00 7.45 16.14 50.66 8.27 195.85 822.43 851.14 3:00 149.86 43.52 27.35 27.11 46.63 46.63 5.10 62.32 16.76 32.61 30.00 24.41 11.00 7.53 16.13 50.63 8.26 194.96 829.77 857.76 4:00 148.54 51.92 34.94 34.94 54.94 54.94 4.46 63.53 16.93 32.57 30.01 24.44 10.99 7.48 16.14 50.58 9.24 198.38 820.60 859.77 5:00 148.01 68.12 51.09 48.09 71.09 71.09 4.07 61.64 14.42 32.62 29.99 24.48 11.02 7.48 16.13 50.63 8.97 208.90 826.91 860.49 6:00 147.01 53.42 34.80 30.77 56.51 56.51 3.90 60.13 12.26 32.43 30.01 24.14 10.98 7.51 16.14 50.63 8.66 198.97 821.93 849.55 7:00 150.52 71.64 56.30 50.65 74.65 74.65 3.67 59.87 11.93 32.35 30.00 24.22 10.98 7.47 16.14 50.57 8.77 225.31 836.60 856.77 8:00 148.08 44.12 32.13 26.13 47.10 47.10 2.31 52.52 7.06 32.51 29.36 24.37 10.97 7.51 15.72 50.76 10.26 173.14 816.72 875.53 9:00 157.85 58.02 49.62 41.44 61.02 61.02 3.72 60.39 11.83 32.70 29.99 24.51 11.02 7.48 16.12 50.71 8.79 200.41 832.55 872.49 10:00 157.19 61.22 52.93 38.34 61.53 61.53 3.59 59.88 11.71 32.65 30.00 24.46 11.03 7.54 16.14 50.48 8.70 200.04 846.82 867.49 11:00 157.96 63.34 79.94 58.17 61.37 61.37 3.47 59.79 11.40 31.92 29.99 23.73 10.97 7.46 16.14 50.28 8.63 190.37 837.86 868.30 12:00 158.42 45.10 66.32 43.27 43.10 43.10 3.65 58.77 10.89 31.59 30.01 23.27 10.99 7.60 16.14 50.04 8.24 193.28 837.74 870.90 13:00 158.50 34.67 54.32 31.29 32.67 32.67 3.82 57.93 10.68 31.13 30.01 22.89 11.02 7.59 16.13 49.93 7.81 198.65 840.68 868.59 14:00 156.11 33.19 49.40 26.35 31.18 31.18 3.98 56.84 10.63 31.18 29.99 22.94 11.00 7.57 16.12 50.00 8.07 208.92 834.59 869.99 15:00 153.90 30.72 35.53 13.06 28.73 28.73 3.91 57.38 10.71 31.25 30.01 23.13 11.01 7.55 16.13 50.07 8.36 199.95 825.59 863.55 16:00 152.04 58.02 60.97 38.93 56.05 56.05 3.66 59.32 11.29 31.34 30.00 23.25 10.98 7.52 16.13 50.12 8.99 206.00 818.75 866.39 17:00 154.48 40.78 57.74 37.14 38.72 38.72 3.94 58.83 11.46 31.30 30.00 23.08 11.01 7.52 16.13 50.15 8.64 194.57 827.45 868.53 18:00 153.84 34.82 49.50 36.38 33.59 34.41 4.24 57.32 11.23 31.31 30.00 23.13 11.01 7.53 16.14 50.09 8.73 198.33 824.61 871.97 19:00 153.71 34.60 34.61 38.64 34.64 36.64 4.42 57.35 11.16 31.36 30.00 23.05 10.99 7.58 16.14 50.11 9.11 196.96 826.04 872.11 20:00 153.63 39.58 39.58 43.58 39.58 41.58 4.18 58.69 11.36 31.45 30.00 23.26 11.00 7.51 16.12 50.25 9.10 202.18 815.64 886.51 21:00 153.99 32.89 32.89 36.63 32.89 34.89 4.46 56.58 11.18 31.73 30.00 23.67 11.03 7.48 16.13 50.32 8.71 199.24 818.70 877.52 22:00 153.57 31.00 25.70 25.63 31.85 33.88 4.53 56.50 11.18 32.01 30.00 23.75 10.99 7.50 16.13 50.40 8.60 204.42 821.08 876.78 23:00 152.54 40.41 26.85 26.72 44.16 45.28 4.15 58.98 11.52 32.20 30.00 24.06 11.00 7.50 16.13 50.47 8.99 200.56 816.47 880.36 0:00 152.99 54.66 40.66 40.66 58.73 59.73 4.00 60.40 12.13 32.45 30.01 24.38 11.02 7.50 16.14 50.50 8.65 204.83 825.94 873.22 TOTAL 153.03 47.74 45.59 37.28 48.47 48.92 4.00 58.74 11.79 31.99 29.97 23.81 11.00 7.52 16.12 50.38 8.70 199.77 827.20 867.84 GAS TEMP BOILER1 1/22/2010
PRIMARY AIR SECONDARY AIR SH OUTLE T



## Unit 1 Boiler Operating Data for January 21 st 

## and 22 ndWheelabrator Saugus, Inc. Service Report WTE Units 1 & 2 January 29, 2010

-CONFIDENTIAL - Page 11 -DO NOT DUPLICATE

## 6 .0 Phase 2 SNCR Optimization Testing Phase 2 optimization tests were performe d on Units 1 and 2 on Tuesday, January 26 th 

### , 2010 and on Unit 2 on Wednesday, January 27 th 

### , 2010. Tests on Tuesday were comprised of running reagent pumps manually with approximately 0, 5, and 10 gallons of reagent an hour to each unit for enough time to gather hourly average performa nce data. Unit #1 went into a water wash outage on Wednesday, so two new style injectors were borrowed from Unit #1 and mounted in Unit #2 making use of three injectors in each sidewall on Unit 2 (see following detail). Reagent pump rate tests of 0, 5, and 10 gallons per hour were repeated for comparison to Tuesday’s performance. The following tables summarize the performance observed:

Test Injector No. of Steam Heat Urea Dilution Injector NOx NOx NOx No. Location Injectors Flow Input Flow Flow Type @ 7% O2 Baseline Reduction [Klb/Hr] [Mmbtu/hr] [GPH] [GPM] [ppmvc] [ppmvc] [%] 1 See 4 153.2 248.9 4.4 2.0 DNT 174.7 240.7 27.4% 2 Sketch 4 153.7 249.8 5.1 2.0 DNT 177.1 240.7 26.4% 3 Page 6 4 153.1 248.8 5.1 2.0 DNT 180.4 240.7 25.0% 4 4 150.9 245.3 5.1 2.0 DNT 190.6 240.7 20.8% 6 4 155.7 253.1 0.0 2.0 240.7 240.7 0.0% 8 4 153.8 250.0 10.7 2.0 DNT 166.1 240.7 31.0% 9 4 151.8 246.6 10.7 2.0 DNT 164.0 240.7 31.9% Wheelabrator Saugus Unit #1

Test Injector No. of Steam Heat Urea Dilution Injector NOx NOx NOx No. Location Injectors Flow Input Flow Flow Type @ 7% O2 Baseline Reduction [Klb/Hr] [Mmbtu/hr] [GPH] [GPM] [ppmvc] [ppmvc] [%] 1 See 4 153.6 249.6 4.4 2.0 DNT 189.0 268.0 29.5% 2 Sketch 4 153.5 249.4 4.7 2.0 DNT 192.7 268.0 28.1% 3 Page 6 4 153.1 248.8 4.7 2.0 DNT 195.0 268.0 27.2% 4 4 153.0 248.7 4.8 2.0 DNT 185.7 268.0 30.7% 5 4 154.4 250.9 0.0 2.0 268.0 268.0 0.0% 6 4 151.1 245.5 10.3 2.0 DNT 185.5 268.0 30.8% 7 4 153.7 249.8 10.3 2.0 DNT 175.4 268.0 34.6%
8 6 153.7 249.7 4.9 2.0 DNT 210.6 280.0 24.8% 9 6 155.0 251.9 5.1 2.0 DNT 204.6 280.0 26.9% 10 6 158.7 257.9 5.2 2.0 DNT 186.4 280.0 33.4% 11 6 157.7 256.3 9.9 2.0 DNT 181.3 280.0 35.3% 12 6 158.0 256.7 10.1 2.0 DNT 156.4 280.0 44.1% 13 6 156.0 253.5 0.0 2.0 DNT 280.0 280.0 0.0% Note: Added one injector towards rear wall same level Unit #2 Wheelabrator SaugusWheelabrator Saugus, Inc. Service Report WTE Units 1 & 2 January 29, 2010

-CONFIDENTIAL - Page 12 -DO NOT DUPLICATE24'

Added Injector inj inj 4' Port 2 A Port 2B

Added 5.9' Injecto r inj inj
4'

5' 3.3'
EL. 62' 32'

Burners NORTH

FACING EAST FACING WEST UNIT #2

HEAVY ASH (Darkened Ports are Capped)Wheelabrator Saugus, Inc. Service Report WTE Units 1 & 2 January 29, 2010

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### Note: Added injectors in service on Unit #2 for second set of tests on January

27 Saugus Unit #1

150.0 200.0 250.0 300.0

0.0 2.0 4.0 6.0 8.0 10.0 12.0 Urea Flow (GPH)NOx (ppmv, 7%)

Saugus Unit #2- 4 Injectors

150.0 200.0 250.0 300.0

0.0 2.0 4.0 6.0 8.0 10.0 12.0 Urea Flow (GPH)NOx (ppmv, 7%)Wheelabrator Saugus, Inc. Service Report WTE Units 1 & 2 January 29, 2010

-CONFIDENTIAL - Page 14 -DO NOT DUPLICATESaugus Unit #2- 6 Injectors

150.0 200.0 250.0 300.0

0.0 2.0 4.0 6.0 8.0 10.0 12.0 Urea Flow (GPH)NOx (ppmv, 7%)



### The results show a small incremental increase in NOx reduction and decrease in NOx emissions by doubling reagent flow from 5 to 10 gallons pe r hour. This marginal improvement in NOx removal and NOx reduction at twice the reagent fl ow rate is indicative that the injectors are located at the lower end of of the SNCR operating window wher e potential for ammonia slip generation is highest due to limited reaction time in SNCR operating window. It should be noted that there was an extremely hea vy rainfall the weekend before these tests and that due to the wet refuse, higher than normal pr imary air flow was needed for the combustion; the baseline NOx was therefore higher during these tests than typically found on th ese units, but baselines which can be expected during the course of the year.Wheelabrator Saugus, Inc. Service Report WTE Units 1 & 2 January 29, 2010

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## 7.0 SNCR Optimization Test Conclusions
Four and six injectors were te sted on Saugus Units #1 and #2 and six injectors were tested on Saugus Unit #2 at reagent feed rates of 0, 5, and 10 gallons per hour and results show a capability of reducing NOx consistently down to 185 ppmv (dry, 7% O2) over a 24 hour average with loads at or above 150,000 lbs/hr steam flow . Based on these tests it was determined that:

• Because of furnace configuration, there was no significant performance difference between in utilizing 4 or 6 injectors in each furnace using the DNT injectors.

• Baseline NOx varied between 240 and 280 ppm (dry, 7% O 2 

### )

• A reduced NOx setpoint of 185 ppm (dry, 7% O 2 

### ) was achieved on both units even at higher baselines

• Increasing reagent feed rates from 5 to 10 gph did not appreciably lower NOx or increase NOx reduction.

• This marginal improvement in NOx removal and NOx reduction at twice the reagent flow rate (5 gpm to 10 gpm) indicates that the in jector locations are the lower end of the SNCR operating window where potential for amm onia slip generation is highest due to limited reaction time in optimum SNCR operating window. Therefore, a reduced NOx emissions target of 185 ppm (dry, 7% O 2 

### ) at current boiler operating loads of approximately 150,000lbs/hr may be achieved with the existing SNCR system configuration and an increase in reagent feed rate from 2-4 gpm to 4-6 gpm. Long term operation at this lower NOx target should be eval uated with ammonia slip testing to verify the current limit of 10 ppm 7% O2 is consistently achieved..