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Preserving Coal in the Future Generation
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| Technology | PC subcritical |
PC supercritical |
PC ultra supercritical |
AFBC subcritical |
IGCC E-gas |
NGCC |
| Plant Size (MW) | 500 | 500 | 500 | 500 (2x250) | 590 (2x295) | 506 (2x253) |
| Total Plant Cost ($/kW) |
1186 | 1215 | 1231 | 1240 | 1306 | 455 |
| Heat Rate kJ/kWh HHV (Btu/kWh) avg annual |
10070 (9547) |
9550 (9054) |
9402 (8914) |
10224 (9693) |
8891 (8430) |
7646 (7249) |
| COE ($/MWh) |
40.3 | 40.3 | 40.5 | 43.5 | 42.1 | 31.1 |
| Table 1. Comparison of total cost of electricity (COE) for various clean coal technologies and natural gas-fired CT/CC at 80 percent capacity factor | ||||||
At a price of $2.50/GJ ($2.64/MBtu) HHV for natural gas, the NGCC was more economical. At the 80 percent capacity factor, as natural gas prices rise, the NGCC plant remained economical up to a gas price of $3.71/GJ ($3.91/MBtu) HHV.
However, since power plant dispatch is often conducted based on incremental (variable) costs, plants with high fuel costs (e.g., NGCC) are typically operated at lower capacity factors than 80 percent. At the same coal costs of $0.948/GJ ($1/MBtu) and the same natural gas costs of $2.50/GJ ($2.64/MBtu) as the previous analysis, the NGCC was roughly the same cost (total COE) at 40 percent capacity factor as the PC and IGCC plants at 80 percent capacity factor. Hence, these fuel costs are roughly the breakeven point for clean coal plants and NGCC plants operating at these different capacity factors (see Table 2).
| Technology | PC subcritical |
IGCC | NGCC | NGCC | NGCC |
| Plant Size (MW) | 500 | 590 (2x295) |
506 (2x253) |
506 (2x253) |
506 (2x253) |
| Capacity factor (%) |
80 | 80 | 80 | 65 | 40 |
| Heat Rate kJ/kWh HHV (Btu/kWh) avg annual |
10070 (9547) |
8891 (8430) |
7646 (7524) |
7936 (9693) |
8166 (7742) |
| COE ($/MWh) |
40.3 | 41.8 | 31.1 | 34.0 | 41.9 |
| Table 2. Comparison of COE for various clean coal technologies and natural gas-fired CT/CC for various capacity factors | |||||
Continued advances in the various coal technologies and changes in market-based costing of gas turbines and boilers create a need for ongoing updating of economic assessments.
Source: Updated Cost and Performance Estimates for Clean Coal Technologies - 2001 by EPRIs Neville Holt and George Booras.
A: A recent EPRI study that examined the costs of various clean coal technologies and a natural gas-fired combustion turbine/combined-cycle (NGCC) power plant (using H-class CTs) addressed the cost of CO2 removal. This study assumed a coal cost of $1.18/GJ ($1.24/MBtu) HHV and a natural gas cost of $2.56/GJ ($2.70/MBtu) HHV.
Beginning from a baseline cost of electricity (COE) for NGCC, pulverized coal (PC), and integrated gasification combined cycle (IGCC, with H-class turbines), the study recalculated the COE with the addition of CO2 removal equipment (see Table 3). For the NGCC and PCs, flue gas scrubbing using monoethanolamine (MEA) was assumed; for the IGCC plant, CO2 was removed from the syngas prior to combustion. Several studies have shown that removal of CO2 from syngas in an IGCC prior to combustion is significantly less costly than CO2 removal from the huge volumes of stack gases after combustion at atmospheric pressurethe method used in PCs and NGCCs. (However, many new CT/CC sites are unlikely to be suitable for IGCC since provision has not been made for coal delivery, gasifier trains, and associated permitting.) Despite this inherent advantage of IGCC, for the assumed fuel costs, the NGCC was the lower cost solution ($48.8/MWh) than the IGCC ($59.1/MWh) and PCs ($70 - $72/MWh).
Technology NGCC H IGCC H Supercritical PC Ultra supercritical PC COE ($/MWh) without CO2 removal 30.7 45.1 45.0 44.3 COE ($/MWh) with CO2 removal 48.8 59.1 71.9 70.7 COE ($/MWh) with CO2 removal, transportation and sequestration 53.4 67.7 82.1 81.3 Breakeven cost natural gas $/GJ ($/MBtu) with CO2 removal, transportation and sequestration 4.28
(4.52)60.02
(6.35)5.92
(6.24)Table 3. Comparison of cost of electricity (COE) for various clean coal technologies and natural gas-fired CT/CC, accounting for CO2 removal, transportation and sequestration costs When the additional costs of CO2 transportation and sequestration ($10/metric tonne of CO2) are considered, the NGCCs advantage increases due to the fewer number of tons of CO2 emitted and hence removed. In addition, as natural gas prices rise, the NGCC plant remained economical up to a gas price of $4.28/GJ ($4.52/MBtu) HHV compared to the IGCC; and the NGCC plant remained economical up to a gas price of $5.92/GJ ($6.24/MBtu) HHV compared to the ultra supercritical PC plant.
Advances in various carbon sequestration technologies and methods, and changes in market costs of turbines and boilers call for periodic updating of these engineering and economic assessments.
Source: Updated Cost and Performance Estimates for Clean Coal Technologies - 2001 by EPRIs Neville Holt and George Booras. This work is an update of original work performed by Parsons and EPRI with U.S. DOE co-funding and published in EPRI Report 1000416.
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