# US 2016/0256818 A1 · Production of electric power from fossil fuel with almost zero air pollution

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- Number: US 2016/0256818 A1
- Document ID: US20160256818A1
- Status: Published application
- Kind: A1
- Application number: 13/999,746
- Filed: 2014-03-19
- Published: 2016-09-08
- Earliest claimed: 2014-03-19
- Inventors: Eliot Gerber
- Web page: https://patentgrep.com/patent/US20160256818A1

## CPC

- B01D 53/226: {in serial connexion}
- B01D 53/22: by diffusion (manufacturing semi-permeable membranes B01D67/00; form, structure or properties of semi-permeable membranes B01D69/00; material for semi-permeable membranes B01D71/00)
- B01D 53/229: {Integrated processes (Diffusion and at least one other process, e.g. adsorption, absorption)}
- F01K 5/00: Plants characterised by use of means for storing steam in an alkali to increase steam pressure, e.g. of Honigmann or Koenemann type
- F01N 5/02: the devices using heat
- B01D 2053/221: {Devices}
- B01D 2257/504: Carbon dioxide
- B01D 2258/0283: Flue gases
- Y02C 20/40: of CO2
- Y02E 20/16: Combined cycle power plant [CCPP], or combined cycle gas turbine [CCGT]
- B01D: SEPARATION (separating solids from solids by wet methods B03B, B03D; by pneumatic jigs or tables B03B; by other dry methods B07; magnetic or electrostatic separation of solid materials from solid materials or fluids, separation by high-voltage electric fields B03C; centrifuges, vortex apparatus B04; presses per se for squeezing-out liquid from liquid-containing material B30B9/02; treatment of water C02F, e.g. softening by ion-exchange C02F1/42; {arrangements of air intake cleaners in gas turbine plants F02C7/05} ; arrangements or mounting of filters in air-conditioning, air-humidification or ventilation F24F13/28)
- F01K: STEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES (gas-turbine or jet-propulsion plants F02; nuclear power plants, engine arrangements therein G21D)
- F01N: GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL-COMBUSTION ENGINES (arrangements in connection with gas exhaust of propulsion units in vehicles B60K13/00; combustion-air intake silencers specially adapted for, or arranged on, internal-combustion engines F02M35/00; protecting against, or damping, noise in general G10K11/16)
- Y02C: CAPTURE, STORAGE, SEQUESTRATION OR DISPOSAL OF GREENHOUSE GASES [GHG]
- Y02E: REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION

## Abstract

The present system produces electrical power from burning coal or natural gas, with almost zero air pollution. In its lack of air pollution is similar to air and wind power, but less costly. Its power may be produced day and night and when the wind is not blowing. Its power is less costly than nuclear power, and without the possibility of radiation damage, melt down, and log-term radiation storage. The US tax law provides a $10 or $20 credit per ton CO2 for sequestration in “Secure geological storage”. See 26 USC §45Q. The estimated cost of this system's CO2 carbon capture is below that tax credit. The tax credit of $20/ton (large coal power station—800K tons of CO2) would generate a profit of millions of dollars. This system's capture cost for CO2 is about the same in gas or coal plants. However, coal plants generate about 3 times the CO2 tonnage of gas plants per unit of electric power. In one example, the system uses combined cycle gas turbine-steam units (CCGT) thermal efficiency of 50-60%. CCGT exhaust gas is relatively cool and clean, with almost no particulates, nitrogen oxide, or mercury The CO2 is separated from nitrogen (N2) using at least two cascaded stages of membrane separators. The permeance of the membranes of the first stage is at least 800 and preferably 2000-10,000. This permits low gas compression which saves the cost of larger compressors and electrical power. Also the area of the membranes are small due to their high permeance. The membranes of the second stage have a lower permeance with higher selectivity and higher pressure may be used. This does not add much to cost because the volume of gas separated is only 2-7% (gas) or 12-14% (coal) of the volume of CCGT exhaust gas. The over 90% pure separated CO2 is then compressed and sold or sequested in geological formations.

## Claims

### Claim 1

A system for the separation and non-polluting disposal of carbon dioxide derived from the exhaust of burning fossil fuel, including a gas separation system which includes: a first stage of gas membranes CO2 separators, means to transport exhaust gas to the first stage, the first stage separating CO2 from other gases in the exhaust gas, a second stage of gas membrane CO2 separators, means to transport permeant gas that passes through the membranes of the first stage to the second stage, the second stage producing CO2 permeate gas (that passes through the membranes of the second stage) of purity greater than 90%, a CO2s gas compressor, and means to transport the permeate gas that passes through the second stage to the compressor,
wherein: the membranes of the first stage have a permeance greater than 800 GPU and a CO2/N2 selectivity of greater than 10 and the membranes of second stage have a permeance greater than 10 GPU and a CO2/N2 selectivity greater than 30.

### Claim 2 (depends on 1)

A system as in claim 1 wherein the membranes of the first stage have a permeance of at least 4000 GPU.

### Claim 3 (depends on 1)

A system as in claim 1 wherein the membranes of the second stage have a selectivity for CO2 greater than 100.

### Claim 4 (depends on 1)

A system as in claim 1 and also including a first blower to compress gas entering the first stage and a second stage compressor to compress gas entering the second stage, wherein in operation the gas is compressed at a lower pressure by the blower than by the compressor.

### Claim 5

A method for the separation and non-polluting disposal of carbon dioxide in the exhaust from the burning of fossil fuel, including a gas separation method which includes: separating the CO2 from N2 using a first stage of gas membrane CO2 separators, transporting exhaust gas to the first stage of gas membrane CO2 separators, transporting permeant gas that passes through the first stage to a second stage of gas membrane CO2 separators, the second stage producing CO2 permeate gas (that passes through the second stage) of purity greater than 90%, a CO2 gas compressor, and transporting permeate gas that passes through the second stage to the compressor, wherein the membranes of the first stage have a permeance greater than 800 GPU and a CO2/N2 selectivity of greater than 10 and the membranes of the second stage have a permeance greater than 10 GPU and a CO2/N2 selectivity greater than 30.

### Claim 6 (depends on 5)

A method as in claim 5 wherein the membranes of the first stage have a permeance greater than 4000 GPU.

### Claim 7 (depends on 5)

A method as in claim 5 wherein the membrane of the second stage has a selectivity for CO2 greater than 100.

### Claim 8 (depends on 5)

A method as in claim 5 and also including a first stage blower
to compress gas entering the first stage and a second stage compressor
to compress gas entering the second stage, wherein in operation compressing gas to a lower pressure by the blower than compressing gas by the compressor.

### Claim 9

A system for the production of electrical energy from natural gas fuel with the separation and non-polluting disposal of carbon dioxide, the system including a combined cycle electrical generating plant, said plant including a natural gas fueled turbine, a heat exchange boiler (HRSG) producing steam and exhaust gas containing carbon dioxide (CO2), means to transport the exhaust gas from the gas fueled turbine to the heat exchange boiler (HRSG), a steam turbine, means to transport steam from the heat exchange boiler to the steam turbine, and an electrical generator, wherein the generator is connected to and driven by both the steam and gas fueled turbines, the system also including a gas separation sub-system which includes:
a first stage of gas membrane CO2 separators, means to transport exhaust gas from the heat exchange boiler to the first stage, the first stage separating CO2 from other gases in the exhaust gas received from the heat exchange boiler, a second stage of gas membrane CO2 separators, means to transport permeant gas that passes through the first stage membrane separators to the second stage, the second stage producing CO2 permeate gas (that passes through the second stage) of purity greater than 90%, a CO2 gas compressor, and means to transport permeate gas that passes through the second stage to the compressor, wherein:
the membrane of the first stage has a permeance greater than 800 GPU and CO2/N2 selectivity of 10-100 and the membrane of the second stage has a permeance greater than 10 GPU and a CO2/N2 selectivity greater than 30.

### Claim 10 (depends on 9)

A system as in claim 9 wherein the membrane of the first stage has a permeance greater than 4000 GPU.

### Claim 11 (depends on 9)

A system as in claim 9 wherein the membrane of the second stage has a selectivity for CO2 greater than 100.

### Claim 12 (depends on 9)

A system as in claim 9 and also including a first stage compressor
to compress gas entering the first stage and a second stage compressor
to compress gas entering the second stage, wherein in operation the gas is compressed at a lower pressure by the first compressor than by the second compressor.

### Claim 13 (depends on 5)

A method as in claim 5 for the production of electrical energy from natural gas fuel with the separation and non-polluting disposal of carbon dioxide, the method including producing electrical power from a combined cycle electrical generating plant, said plant including a natural gas fueled turbine, a heat exchange boiler (HRSG) producing steam and exhaust gas containing carbon dioxide (CO2), transporting the exhaust gas from the gas fueled turbine to the heat exchange boiler (HRSG), a steam turbine, transporting steam from the heat exchange boiler to the steam turbine, and an electrical generator,
wherein the driving the generator by both the steam and gas fueled turbines; the process including transporting the exhaust gas from the heat exchange boiler to a gas separation sub-system which includes: a first stage and a second stage of gas membrane CO2 separators; in the first stage passing CO2 from the exhaust gas through a membrane having a permeance greater than 800 GPU and a CO2/N2 selectivity of 10-100 to separate CO2 from other gases in the exhaust gas,
transporting permeate gas that passes through the first stage membrane separators to the second stage membrane having a permeance greater than 50 GPU and CO2/N2 selectivity greater than 30, in the second stage producing CO2 permeate gas (that passes through the second stage) of purity greater than 90% and transporting said permeate gas from the second stage to a CO2 gas compressor to compress CO2 for sale or sequestration.

### Claim 14 (depends on 13)

A process as in claim 13 wherein the membrane of the first stage has a permeance greater than 4000 GPU.

### Claim 15 (depends on 13)

A process as in claim 13 wherein the membrane of the second stage has a selectivity for CO2 greater than 200.

### Claim 16 (depends on 13)

A process as in claim 13 and also including a first stage compressor
to compress gas entering the first stage and a second stage compressor
to compress gas entering the second stage, wherein in operation compressing gas to a lower pressure by the first compressor than compressing gas by the second compressor.