System and method for gasification

Patent metadata

Field	Value
Publication number	US-9803151-B2
Application number	US-201615080043-A
Country	US
Kind code	B2
Filing date	Mar 24, 2016
Priority date	Mar 24, 2016
Publication date	Oct 31, 2017
Grant date	Oct 31, 2017

Abstract

A system includes a first reactor that may gasify a first feed to generate a first syngas. The first feed has a first particle size distribution (PSD 1 ). The system also includes a second reactor that may receive the first feed, a second feed, and at least a portion of the first syngas. The second reactor may gasify the second feed to generate additional syngas, and the second feed has a second particle size distribution (PSD 2 ) that is different from the first PSD. The second reactor includes an elutriation zone disposed on a first end of the second reactor. The elutriation zone may receive the first and second feed. The second reactor also includes a fluidized bed disposed at a second end of the second reactor that is substantially opposite the first end. The fluidized bed is fluidly coupled to the first reactor and may receive the portion of the first syngas via a syngas inlet. The system also includes a gas-solids separation section fluidly coupled to the first and second reactors. The gas-solids separation section may receive the first feed and partially reacted particles of the second feed from the elutriation zone and may feed a combined feed consisting of the first feed and the partially reacted particles of the second feed to the first reactor.

First claim

The invention claimed is:

1. A system, comprising:
a first reactor configured to gasify a first feed to generate a first syngas, wherein the first feed has a first particle size distribution (PSD 1 );
a second reactor configured to receive the first feed, a second feed, and at least a portion of the first syngas, wherein the second reactor is configured to gasify the second feed to generate additional syngas, and the second feed has a second particle size distribution (PSD 2 ) that is different from the first PSD, and wherein the second reactor comprises:
an elutriation zone disposed on a first end of the second reactor, wherein the elutriation zone is configured to receive the first and second feed;
a fluidized bed disposed at a second end of the second reactor that is substantially opposite the first end, wherein the fluidized bed is fluidly coupled to the first reactor and configured to receive the portion of the first syngas via a syngas inlet; and

a gas-solids separation section fluidly coupled to the first and second reactors, wherein the gas-solids separation section is configured to receive the first feed and partially reacted particles of the second feed from the elutriation zone and to feed a combined feed consisting of the first feed and the partially reacted particles of the second feed to the first reactor.

2. The system of claim 1 , wherein the gas-solids separation section comprises a first cyclone and a second cyclone, wherein the first cyclone is configured to separate a first portion of the partially reacted second feed particles from a product syngas and the second cyclone is configured to separate first feed particles and a second portion of the partially reacted second feed particles from the product syngas.

3. The system of claim 2 , wherein the first cyclone is fluidly coupled to the second reactor and configured to feed the first portion of the partially reacted second feed particles to the fluidized bed and the second cyclone is fluidly coupled to the first cyclone and configured to feed the first feed particles and the second portion of the partially reacted second feed particles to the first reactor.

4. The system of claim 1 , wherein the gas-solids separation section comprises a cyclone and a filter, wherein the cyclone and the filter are configured to separate first feed particles and at least a portion of the partially reacted second feed particles from the product syngas, and wherein the cyclone and the filter are fluidly coupled to the first reactor and configured to feed the first feed particles and at least a portion of the partially reacted second feed particles to the first reactor.

5. The system of claim 1 , comprising a particulate removal system disposed upstream of the second reactor and fluidly coupled to the first reactor and the fluidized bed, wherein the particulate removal system is configured to remove particulates from the first syngas to generate the portion of the syngas fed to the fluidized bed.

6. The system of claim 1 , comprising a first reactor feed system and a second reactor feed system, wherein the second reactor feed system is fluidly coupled to the elutriation zone and the first reactor feed system, the second reactor feed system is configured to supply the first feed and the second feed to the second reactor, and wherein the first reactor feed system is fluidly coupled to the second reactor feed system, the first reactor, and the gas-solids separation section and configured to supply the first reactor with the first feed and with a combined feed consisting of the first feed and partially reacted second feed particles.

7. The system of claim 6 , wherein the second reactor feed system comprises a flow diverter configured to direct a flow of the first feed to the first reactor feed system, the second reactor, or a combination thereof.

8. The system of claim 6 , wherein the first reactor feed system comprises an eductor.

9. The system of claim 1 , wherein the second reactor comprises a tapered column disposed between the elutriation zone and the fluidized bed, wherein the tapered column comprises a first diameter adjacent to the elutriation zone and a second diameter adjacent to the fluidized bed, and wherein the second diameter is greater than the first diameter.

10. The system of claim 1 , wherein the second reactor comprises a feed inlet disposed on the first end of the second reactor configured to direct the first and second feed into the second reactor in a direction that is substantially opposite a flow direction of the product syngas.

Assignees

• Gen Electric

Inventors

• Leininger Thomas Frederick

Classifications

• C10K1/026

  by centrifugal forces (cyclones B04C) · CPC title

• C10J3/466

  Entrained flow processes · CPC title

• C01B3/02

  Production of hydrogen; Production of gaseous mixtures containing hydrogen · CPC title

• C10J3/721 Primary

  Multistage gasification, e.g. plural parallel or serial gasification stages · CPC title

• C10J3/84

  with means for removing dust or tar from the gas · CPC title