Abstract

Natural gas (NG) and synthetic gas (SG) fired power plants are investigated. Both, NG and SG are burned in highly enriched oxygen (99.5%+) and recycled CO 2 from the flue gas. Both use the combined gas turbine-steam turbine cycle. SG is obtained from a conventional coal gasification process. Oxygen for coal gasification and oxygen/fuel combustion is obtained from an air separation unit (ASU). Liquid oxygen from the ASU is used to condense part of the CO 2 from the flue gas. The condensed CO 2 can be resold or sequestered in terrestrial or deep ocean reservoirs. The rest is recycled into the combustor of the gas turbine. By cross-integrating the ASU and the CO 2 capture, the overall efficiency, defined as electricity out/heat in, is estimated at 45% for the NG fired plant, compared to a plant without CO 2 capture of 54%. The thermal efficiency of the coal gasification-SG fired plant is estimated at about 36.6%, compared to a plant without CO 2 capture of 47.8%. The efficiency estimates include the energy spent on air separation and coal gasification. The relatively modest efficiency loss is amply compensated by producing salable byproducts (Ar and N 2) and capturing CO 2, thereby avoiding carbon taxes, if levied. The efficiency of the coal gasification plant with CO 2 capture is of the same order as modern pulverized coal fired, single cycle plants without CO 2 capture. Furthermore, these plants emit no NO x, SO 2 and particulate matter. In fact, the plants require no smokestack.

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