IP Library Granted Patent US 8,807,054
Granted Patent B2
US 8,807,054 · App. 13/375,977 · Granted Aug 19, 2014

System for converting fuel materials

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Quick Facts
Patent No.
US 8,807,054
App. No.
13/375,977
Granted
Aug 19, 2014
Kind
B2
Abstract

The invention is related to a system ( 1 ) for converting fuel material comprising: a first reactor ( 2 ) in which a fuel material reacts with an oxide material for producing reaction products including fuel particles, ash and oxide particles, a second reactor ( 3 ) for oxidizing the oxide particles produced in the first reactor ( 2 ), a carbon separator ( 4 ) that receives fuel particles, ash and oxide particles produced in the first reactor ( 2 ) and suitable for separating the oxide particles and ash from the fuel particles, the carbon separator ( 4 ) comprising an outlet path ( 4 c ) for the oxide particles and ash exhaust, characterized in that said outlet path ( 4 c ) of the carbon separator ( 4 ) is connected to an ash separator ( 10 ) for separating the ash from the oxide particles.

Claims (26)

1. A system for converting fuel material, said system comprising:

a first reactor in which a fuel material reacts with an oxide particles for producing reaction products including fuel particles, ash and oxide particles,

a second reactor in which the oxide particles produced in the first reactor are oxidized,

a carbon separator that receives fuel particles, ash and oxide particles produced in the first reactor that separates the oxide particles and ash from the fuel particles, the carbon separator comprising a first outlet for the oxide particles and ash and a second outlet for the fuel particles;

an ash separator that receives the oxide particles and ash from the first outlet of the carbon separator, the ash separator comprising a first outlet for the ash and a second outlet for the oxide particles.

2. The system according to claim 1 , wherein the carbon separator and the ash separator are fluidized, and the system further comprises a controller to control the fluidization velocity of each separator.

3. The system according to claim 2 , wherein the fluidization velocity of the ash separator is higher than the fluidization velocity of the carbon separator.

4. The system according to claim 3 , wherein the carbon separator and the ash separator are adjacent via a common side wall.

5. The system according to claim 3 , wherein the ash separator is placed below the carbon separator.

6. The system according to claim 1 , wherein the carbon separator and the ash separator are adjacent via a common side wall.

7. The system according to claim 1 , wherein the carbon separator and the ash separator are connected by a pipe.

8. The system according to claim 7 , wherein the ash separator is placed below the carbon separator.

9. The system according to claim 1 , further comprising:

a low efficiency cyclone separator connected to the first reactor, and

a high efficiency cyclone separator, wherein the low efficiency cyclone separator includes a lower outlet connected to the carbon separator and an upper outlet connected to the high efficiency cyclone separator.

10. The system according to claim 1 , wherein the fuel material is coal.

11. The system according to claim 1 , wherein the oxide material is metal oxide.

12. The system according to claim 1 , wherein the fluidization velocity of the ash separator is higher than the fluidization velocity of the carbon separator.

13. The system according to claim 12 , further comprising:

a low efficiency cyclone separator connect to the first reactor, and

a high efficiency cyclone separator, wherein the low efficiency cyclone separator includes a lower outlet connected to the carbon separator and an upper outlet connected to the high efficiency cyclone separator.

14. The system according to claim 1 , wherein the fuel particles exiting the second outlet of the carbon separator are provided to the first reactor.

15. The system according to claim 14 , wherein the oxide particles exiting the second outlet of the ash separator are provided to the second reactor.

16. The system according to claim 1 , wherein the oxide particles exiting the second outlet of the ash separator are provided to the second reactor.

17. The system according to claim 1 , wherein the second outlet of the carbon separator includes a plurality of second outlets.

18. The system according to claim 17 , wherein the fuel particles exiting the plurality of second outlets of the carbon separator are provided to the first reactor.

Assignments (1)
CHANGE OF NAME Recorded Aug 17, 2016
From: ALSTOM TECHNOLOGY LTD
To: GENERAL ELECTRIC TECHNOLOGY GMBH
Reel/Frame 039714/0578 →