Device for preventing steam from being produced in flue gas cooler for oxyfuel combustion boiler
US-2016169504-A1 · Jun 16, 2016 · US
US9541289B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9541289-B2 |
| Application number | US-201214113277-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jul 13, 2012 |
| Priority date | Jul 14, 2011 |
| Publication date | Jan 10, 2017 |
| Grant date | Jan 10, 2017 |
A practical reading order for non-experts. Skip the full description unless you need deep technical detail.
What the patent document calls the invention.
A short plain-language summary of the technical disclosure.
Who owns or filed the patent and who is credited as inventor.
Filing, priority, publication, and grant dates set the timeline.
The legal scope of protection — read this for what is actually claimed.
Technology tags used to group this patent with similar filings.
Prior art links and similar publications in this corpus.
Official abstract text for this publication.
Provided is a gas cooler for cooling a produced gas on a side from which the produced gas exits, the produced gas being produced by partially oxidizing and gasifying a carbon-containing fuel in a gasification furnace inside a pressure vessel. A distance (SL) between tubes of a tube bundle of a heat exchanger provided inside the gas cooler is set such that the tubes are in contact with each other or adjacent to each other in a gas-flow direction of the produced gas. Since the tubes are in contact with each other or adjacent to each other, a particle flowing with the gas flow is only deposited as a deposited particle in a concave portion between the tubes, whereby the decrease in heat exchange efficiency caused by particle deposition can be suppressed.
Opening claim text (preview).
The invention claimed is: 1. A pressure vessel comprising: a gasification furnace that partially oxidizes and gasifies a pulverized coal and discharges gasified gas as a produced gas; and a gas cooler including a flue gas duct that communicates with the gasification furnace and through which the produced gas passes, wherein the gas cooler includes a heat exchanger provided in the flue gas duct, the heat exchanger including a group of tubes arrayed along a gas-flow direction of the produced gas passing through the flue gas duct, and a ratio (SL/d) of a distance (SL) in the gas-flow direction of the produced gas between the tubes constituting the group of tubes to an outer diameter (d) of the tube is larger than 1 and 1.4 or smaller, such that dust particles of the produced gas are deposited only in a concave portion between the tubes. 2. The pressure vessel according to claim 1 , wherein a temperature of the produced gas inside the gas cooler is equal to an ash melting point or lower, and a dust concentration of the produced gas from the gasification furnace falls within a range of 50 g/m 3 to 20,000 g/m 3 . 3. The pressure vessel according to claim 1 , wherein pressure inside the pressure vessel is 0.5 MPa to 10 MPa. 4. An integrated gasification combined cycle for a carbon-containing fuel comprising: the pressure vessel according to claim 1 ; a gas turbine equipment to which the produced gas obtained in the pressure vessel is supplied as a fuel; and an exhausted heat recovery steam generator for recovering exhausted heat from a flue gas generated from the gas turbine equipment. 5. The integrated gasification combined cycle for a carbon-containing fuel according to claim 4 , further comprising a steam turbine equipment to which obtained steam is supplied.
Physical processes, e.g. shredding, comminuting, chopping, sorting · CPC title
in combination with an oxygen producing plant, e.g. an air separation plant · CPC title
Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines · CPC title
of coolers · CPC title
combined with waste-heat boilers · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.