A new scheme is described for electricity production based on coal gasificiation with recovery of CO2. Coal is gasified into a synthesis gas, mainly consisting of hydrogen and carbon monoxide. After clean-up, this synthesis gas is separated by a membrane into a carbon-rich gas and a hydrogen-rich gas. The hydrogen-rich gas is fed to a conventional gas turbine. The carbon-rich gas is fed to another gas turbine, where it is fired in a mixture of oxygen and CO2. The exhaust of the latter is almost pure CO2 and can be stored outside the atmosphere.
The CO2 emissions of this plant are about 10% of the emissions of an IGCC plant without CO2 recovery, and the conversion efficiency is approx. 6% lower. A first estimate is that the electricity production costs are about one third higher. It is found that the specific emission reduction costs can be limited to about $16 per tonne of CO2 avoided.
The main technical problem of this new scheme is the development of a new type of gas turbine with CO2 as working fluid.
[1]
Yoshikazu Suzuki,et al.
Closed Dual Fluid Gas Turbine Power Plant without Emission of CO 2 into the Atmosphere
,
1989
.
[2]
Y. Shindo,et al.
Calculation methods for multicomponent gas separation by permeation
,
1985
.
[3]
David Gordon Wilson,et al.
The design of high-efficiency turbomachinery and gas turbines
,
1984
.
[4]
Y. Kao,et al.
Economic evaluation of gas membrane separator designs
,
1989
.
[5]
Marcel Mulder,et al.
Basic Principles of Membrane Technology
,
1991
.
[6]
Jack Janes.
Chemically recuperated gas turbine
,
1990
.
[7]
C. Pan.
Gas separation by high‐flux, asymmetric hollow‐fiber membrane
,
1986
.