Apparatus for a syngas cooler and method of maintaining the same
US-9200223-B2 · Dec 1, 2015 · US
US9487715B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9487715-B2 |
| Application number | US-201514610826-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jan 30, 2015 |
| Priority date | Oct 22, 2008 |
| Publication date | Nov 8, 2016 |
| Grant date | Nov 8, 2016 |
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Provided is a coal gasifier enabling a reduction in size of a shift reactor by generating hydrogen-rich gasified coal gas. In a coal gasifier (G) generating gasified coal gas by a gasification reaction proceeding in a furnace fed with a gasifiable raw material, such as coal, and a gasifying agent, at least one of water and steam is fed to the furnace as a material accelerating a hydrogen-generating reaction that proceeds simultaneously with the gasification reaction.
Opening claim text (preview).
The invention claimed is: 1. A process of generating gasified coal gas by a gasification reaction using a coal gasifier, wherein said coal gasifier is a two-stage entrained-bed gasifier having: a furnace comprising a combustion chamber and a reduction chamber, a gas-cooling heat exchanger communicating with a downstream side of the reduction chamber, and a water cooling wall covering outer peripheral surfaces of the combustion chamber, the reduction chamber, and the gas-cooling heat exchanger, wherein said process comprises: feeding, from outside of the furnace via a combustion chamber burner into the combustion chamber, at least one of water and steam as a material accelerating a hydrogen-generating reaction proceeding together with the gasification reaction the steam being generated from water flowing in the water cooling wall and/or the gas-cooling heat exchanger, a gasifiable raw material including coal, and a gasifying agent; feeding the gasifiable raw material from outside of the furnace via a reduction chamber burner into the reduction chamber, without feeding the gasifying agent, the water, and the steam into the reduction chamber; cooling, in the gas-cooling heat exchanger, the gasified coal gas generated in the reduction chamber; and controlling an amount of carbon (C) remaining in unreacted coal passing through the gas-cooling heat exchanger together with the gasified coal gas to 30% or more. 2. The process according to claim 1 , wherein an amount of the water or steam fed into the combustion chamber is 0.1 to 0.8 on a mass basis relative to an amount of the gasifiable raw material fed into the combustion chamber.
Steam reforming, i.e. injection of steam only · CPC title
by cooling to condense non-gaseous materials {(C10K1/001 takes precedence)} · CPC title
Integrated gasification combined cycle [IGCC], e.g. combined with carbon capture and storage [CCS] · CPC title
as steam · CPC title
Autothermal gasification by injection of oxygen or steam · CPC title
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