Integrated chemical looping air separation in large-scale oxy-fuel plants

Patent metadata

Field	Value
Publication number	US-RE48040-E
Application number	US-201215352554-A
Country	US
Kind code	E1
Filing date	Sep 21, 2012
Priority date	Sep 23, 2011
Publication date	Jun 9, 2020
Grant date	Jun 9, 2020

Abstract

An integrated chemical looping air separation unit ( 5 ) in a large-scale oxy-fuel power generating plant takes a portion of recycled flue gas ( 6 ) via a recycling conduit ( 7 ) through a heat exchanger ( 8 ) to a reduction reactor ( 9 ). The reduction reactor ( 9 ) exchanges oxidized metal oxide with an oxidation reactor ( 11 ) via transfer means ( 10 ) which return reduced metal oxide from the reduction reactor ( 9 ) to the oxidation reactor ( 11 ). This enables the reduction reactor ( 9 ) to feed a mixture of oxygen and recycled flue gas into the boiler ( 13 ) of the power generating plant in a more energy efficient manner than conventional oxy-fuel power plants using air separation units.

First claim

The invention claimed is:

1. A method of air separation in large-scale oxy-fuel power generation plants of the type having a boiler to generate steam, said method including the steps of recycling flue gas from the boiler through a reduction reactor that is connected in a chemical looping process with an oxidation reactor such that the reduction reactor produces a mixture of oxygen and recycled flue gas, wherein the oxidation reactor is located within the reduction reactor, enhancing heat transfer between the oxidation reactor and the reduction reactor, and feeding said mixture back into the boiler, wherein a controlled proportion of the recycled flue gas from the boiler is fed through the chemical looping reduction reactor, with the remaining recycled flue gas being fed directly back to the boiler.

2. A method as claimed in claim 1 , wherein the chemical looping process includes the steps of passing oxidised metal oxide and heat from the oxidation reactor to the reduction reactor, and passing reduced metal oxide from the reduction reactor to the oxidation reactor.

3. A method as claimed in claim 2 wherein the method is stabilized by manipulating the balance between the equilibrium and actual partial pressures of oxygen over the metal oxide.

4. A method as claimed in claim 3 wherein the actual partial pressure of oxygen in the oxidation reactor is maintained at levels above equilibrium oxygen partial pressure.

5. An apparatus for generating oxygen to be fed into a boiler in a large-scale oxy-fuel power generation plant, said apparatus including a reduction reactor, a flue gas recycling conduit arranged to transfer some of the flue gas emitted in use from the boiler to the reduction reactor and feed the remaining recycled flue gas directly to the boiler, an oxidation reactor connected to the reduction reactor by transfer means arranged to transfer with solid particulate material being transferred between the reduction reactor and the oxidation reactor, and an outlet conduit arranged to transfer oxygen and recycled flue gas mixture from the reduction reactor back into the boiler, wherein the oxidation reactor is located within the reduction reactor, enhancing heat transfer between the oxidation reactor and the reduction reactor.

6. An apparatus as claimed in claim 5 wherein the reduction reactor, the oxidation reactor, the transfer means, the flue gas recycling conduit and the outlet conduit form an integrated chemical looping air separation unit.

7. An apparatus as claimed in claim 6 wherein the oxidation reactor passes through the middle of the reduction reactor, enhancing heat transfer between the oxidation reactor and the reduction reactor.

8. An apparatus as claimed in claim 7 5 wherein oxidised carrier particles from the oxidation reactor are passed upwardly to a cyclone separator where reduced air is exhausted and the oxidised carrier particles returned to the reduction reactor.

9. An apparatus as claimed in claim 7 5, wherein extra heat is provided using a chemical looping based combustor which can produce oxygen by itself in its oxidation reactor.

10. An apparatus as claimed in claim 5 wherein the recycling flue gas conduit is connected to an electrostatic precipitator which reduces, a flue gas cleaner or a condenser to reduce impurities in the recycled flue gas.

11. An apparatus as claimed in claim 5 wherein the recycling flue gas conduit is connected to a flue gas cleaner which reduces impurities in the recycled flue gas.

12. An apparatus as claimed in claim 5 wherein the recycling flue gas conduit is connected to a condenser which reduces impurities in the recycled flue gas.

13. An apparatus as claimed in claim 5 wherein the recycling flue gas conduit is connected to a compressor which compresses a non-recycled portion of the flue gas.

14. A method as claimed in claim 1 wherein the flue gas is recycled after electrostatic precipitation (ESP) of the flue gas which reduces impurities in the recycled flue gas.

15. A method as claimed in claim 1 wherein the flue gas is recycled after cleaning of the flue gas which reduces impurities in the recycled flue gas.

16. A method as claimed in claim 1 wherein the flue gas is recycled after condensation of the flue gas which reduces impurities in the recycled flue gas.

17. A method as claimed in claim 1 wherein a non-recycled portion of the flue gas is compressed.

18. An apparatus as claimed in claim 8, wherein extra heat is provided using a chemical looping based combustor.

19. An apparatus for generating oxygen to be fed into a boiler in a large-scale oxy-fuel power generation plant, said apparatus including a reduction reactor, a flue gas recycling conduit arranged to transfer some of the flue gas emitted in use from the boiler to the reduction reactor and feed the remaining recycled flue gas directly to the boiler, an oxidation reactor connected to the reduction reactor by a loop seal arranged to transfer solid particulate material between the reduction reactor and the oxidation reactor, and an outlet conduit arranged to transfer oxygen and recycled flue gas mixture from the reduction reactor back into the boiler, wherein the oxidation reactor is located within the reduction reactor, enhancing heat transfer between the oxidation reactor and the reduction reactor.

20. An apparatus as claimed in claim 19 wherein the reduction reactor, the oxidation reactor, the loop seal, the flue gas recycling conduit and the outlet conduit form an integrated chemical looping air separation unit.

21. An apparatus as claimed in claim 19, wherein extra heat is provided using a chemical looping based combustor.

22. An apparatus as claimed in claim 19 wherein oxidised carrier particles from the oxidation reactor are passed upwardly to a cyclone separator where reduced air is exhausted and the oxidised carrier particles returned to the reduction reactor.

23. An apparatus as claimed in claim 22, wherein extra heat is provided using a chemical looping based combustor.

24. An apparatus as claimed in claim 19 wherein the recycling flue gas conduit is connected to an electrostatic precipitator, a flue gas cleaner or a condenser to reduce impurities in the recycled flue gas.

Assignees

• Newcastle Innovation Ltd
• Univ Newcastle

Inventors

• Moghtaderi Behdad
• Wall Terry Fitzgerald
• Shah Kalpit Vrajeshkumar

Classifications

• F01K13/00

  General layout or general methods of operation of complete plants · CPC title

• F23C2900/99008

  Unmixed combustion, i.e. without direct mixing of oxygen gas and fuel, but using the oxygen from a metal oxide, e.g. FeO · CPC title

• F23L7/007

  Supplying oxygen or oxygen-enriched air · CPC title

• B01D53/73 Primary

  After-treatment of removed components · CPC title

• C01B13/08 Primary

  from air with the aid of metal oxides, e.g. barium oxide, manganese oxide {(C01B13/0292 takes precedence)} · CPC title