Biomass Combined Heat and Power Catalog of Technologies

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Biomass Combined Heat and Power Catalog of Technologies ( biomass-combined-heat-and-power-catalog-technologies )

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EPA Combined Heat and Power Partnership Biomass CHP Catalog Table 7-8. Biomass Circulating Fluidized Bed Power Generation System Capital Cost Estimates Biomass prep-yard Circulating fluidized bed boiler CHP—Back-Pressure Steam Turbine Back-pressure steam turbine capacity (MW) Back-pressure steam turbine cost Total capital cost—CHP/back-pressure turbine Cost $/kW—CHP/BP turbine Power Only—Condensing Turbine Condensing steam turbine capacity (MW) Condensing steam turbine cost Total capital cost—condensing turbine Cost $/kW—condensing turbine $2,639,660 $5,430,000 $6,972,000 $24,500,000 0.5 5.9 $425,000 $2,625,000 $10,036,660 $32,555,000 $20,070 $5,515 N/A 16.2 N/A $5,675,000 N/A $35,605,000 N/A $2,197 $7,110,000 $32,250,000 8.8 $3,400,000 $42,760,000 $4,860 24.3 $7,900,000 $47,260,000 $1,945 Tons/Day (as received) Installed Capital Costs 100 600 900 Capital cost for the circulating fluidized bed systems are significantly higher than the stoker power systems. Prep-yard costs are equal to the stoker prep-yard costs because they are a function of the amount of biomass handled, and steam turbine costs are only slightly higher than the stoker systems. As discussed in Chapter 5, the circulating fluidized bed costs are significantly higher than similarly sized stoke-boilers. Overall, the $/kW cost of the 100 tons/day CHP system has more than doubled to over $20,000/kW. The costs for the larger CHP systems have increased by about $900/kW, almost entirely due to the higher cost of the boiler. Table 7-9 shows estimates for O&M costs for the circulating fluidized bed direct-fired cases. Labor requirements and costs are identical to the corresponding stoker boiler cases and variable O&M costs are the same per unit of power generated. Fixed non-labor O&M is higher for the circulating fluidized bed cases, resulting in slightly higher total non-fuel O&M costs for these systems. Table 7-9. Biomass Circulating Fluidized Bed System Non-Fuel O&M Cost Estimates Prep-yard O&M Boiler section O&M Steam turbine O&M Total O&M Non-fuel O&M—back-pressure turbine ($/kWh) Non-fuel O&M—condensing turbine ($/kWh) $400,000 $260,000 $15,000 $675,000 $0.229 N/A $320,000 $1,190,000 $185,000 $1,695,000 $0.036 $0.013 $320,000 $1,205,000 $277,000 $1,802,000 $0.026 $0.009 Tons/Day (as received) O&M Cost Components 100 600 900 Table 7-10 shows the annual operating expenses and the net costs to generate power for the biomass circulating fluidized bed power generation systems. In the 100 tons/day case, the much higher cost for a small circulating fluidized bed boiler results in higher net power costs. The net power costs are comparable to the stoker boiler cases presented previously. The annual operating expenses are about 10 percent higher for the large systems, and 50 percent higher for the 100 tons/day system. However, circulating fluidized bed offers advantages in operational flexibility and reduced emissions as discussed in Chapter 5. 7. Representative Biomass CHP System Cost 87 and Performance Profiles

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