Carbon dioxide membrane separation system in coal gasification process, and integrated coal gasification combined cycle power generation facility using same

Patent metadata

Field	Value
Publication number	US-9863314-B2
Application number	US-201214112650-A
Country	US
Kind code	B2
Filing date	Apr 19, 2012
Priority date	Apr 28, 2011
Publication date	Jan 9, 2018
Grant date	Jan 9, 2018

Abstract

The carbon dioxide membrane separation system in a coal gasification process contains introduction of a mixed gas of hydrogen (H 2 ) and carbon dioxide (CO 2 ) in a high temperature and high pressure condition generated through water gas shift reaction from a water gas shift reaction furnace, while maintaining the temperature and pressure condition, to a zeolite membrane module containing a zeolite membrane for removing carbon dioxide, thereby removing carbon dioxide and generating a fuel gas rich in hydrogen. The fuel gas rich in hydrogen in a high temperature and high pressure condition discharged from the zeolite membrane module is fed to a gas turbine of the power generation facility while maintaining the temperature and pressure condition.

First claim

The invention claimed is:

1. A carbon dioxide membrane separation system in a coal gasification process, comprising:
a gasification furnace for generating hydrogen and carbon monoxide which are introduced into a water gas shift reaction furnace;
the water gas shift reaction furnace for generating a mixed gas of hydrogen (H 2 ) and carbon dioxide (CO 2 ) in a high temperature and high pressure condition generated through water gas shift reaction and introducing the mixed gas directly, while maintaining the temperature and pressure condition, to a zeolite membrane module;
the zeolite membrane module containing a zeolite membrane for removing carbon dioxide, thereby removing carbon dioxide and generating a fuel gas rich in hydrogen.

2. An integrated coal gasification combined cycle power generation facility comprising the carbon dioxide membrane separation system in a coal gasification process according to claim 1 , wherein the fuel gas rich in hydrogen in a high temperature and high pressure condition discharged from the zeolite membrane module is fed to a gas turbine of the power generation facility while maintaining the temperature and pressure condition.

3. A carbon dioxide membrane separation system in a fuel gas production process, comprising plural fuel gas generation and carbon dioxide separation units connected continuously, each of which contains the water gas shift reaction furnace and the zeolite membrane module containing a zeolite membrane for removing carbon dioxide according to claim 1 , by which an unreacted raw material gas contained in the fuel gas rich in hydrogen generated in the respective units is reacted in the water gas shift reaction furnace in the next unit, and carbon dioxide formed in the units is recovered.

4. An integrated coal gasification combined cycle power generation facility comprising the carbon dioxide membrane separation system in a coal gasification process according to claim 3 , wherein the fuel gas rich in hydrogen in a high temperature and high pressure condition discharged from the zeolite membrane module of the fuel gas generation and carbon dioxide separation unit of the final step is fed to a gas turbine of the power generation facility while maintaining the temperature and pressure condition.

5. A carbon dioxide membrane separation system in a coal gasification process according to claim 1 , wherein the zeolite membrane is a composite zeolite membrane.

6. A carbon dioxide membrane separation system in a coal gasification process according to claim 1 , wherein the zeolite membrane is a composite zeolite membrane formed on a porous support, which contains a zeolite membrane having an oxygen 12-membered ring structure having on the surface thereof a zeolite membrane having an oxygen 8-membered ring structure.

7. A carbon dioxide membrane separation system in a coal gasification process according to claim 6 , wherein the zeolite membrane having an oxygen 12-membered ring structure is constituted by an FAU-type zeolite membrane, and the zeolite membrane having an oxygen 8-membered ring structure is constituted by a CHA-type zeolite, MER-type zeolite or CHA-type zeolite membrane.

Assignees

• Fujita Suguru
• Sawamura Ken-Ichi
• Aizawa Masanobu
• Hitachi Shipbuilding Eng Co

Inventors

• Fujita Suguru
• Sawamura Ken-Ichi
• Aizawa Masanobu

Classifications

• B01D53/22 Primary

  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) · CPC title

• B01D71/028

  Molecular sieves (carbon B01D71/021) · CPC title

• C01B2203/042

  Purification by adsorption on solids · CPC title

• C10J3/00

  Production of combustible gases containing carbon monoxide from solid carbonaceous fuels (destructive distillation processes C10B) · CPC title

• F02C7/22

  Fuel supply systems · CPC title