http://rdf.ncbi.nlm.nih.gov/pubchem/patent/KR-20130032484-A

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filingDate 2011-09-23-04:00^^<http://www.w3.org/2001/XMLSchema#date>
inventor http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_0d05b533f892aca38500d2667fa2f205
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publicationDate 2013-04-02-04:00^^<http://www.w3.org/2001/XMLSchema#date>
publicationNumber KR-20130032484-A
titleOfInvention High CO2 Recovery Method for High Efficiency Coal Gasification Fuel Cell Combined Cycle System
abstract The present invention is a method for recovering CO2 of high concentration in a high efficiency coal gasification fuel cell combined cycle power generation system, the gasifier with more than 99% oxygen (2) in which air is separated from the raw material coal (1) through the air separator (9) Most of ash in the raw material supply process (S100) supplied to (3), the heat recovery process (S200) in which a part of ash and the synthetic gas from which slag was removed are cooled by the heat recovery machine (4), and the high temperature dust collector (12). The removed high temperature dust collecting step (S300), the high temperature desulfurization step (S400) for removing sulfur compounds through the high temperature desulfurization facility (13), and the synthesis gas containing hydrogen, carbon monoxide, carbon dioxide, and the like is the air separation device (9) The fuel cell process (S400) flowing into the fuel cell 10 together with the high concentration oxygen (2) of 99% or more from the, and the unreacted carbon monoxide and hydrogen supply the high concentration oxygen (2) of 99% or more to the combustor (11). Combustion process (S500) and combustion after Since the carbon dioxide acquisition process (S600) is obtained, the coal gasification fuel cell hybrid power generation system composed of a high temperature dust collecting process and a high temperature desulfurization process has a higher efficiency than an integrated process using a commercial dust collecting system and a wet process for removing acid gas. It can be obtained, and because the water gas conversion and carbon dioxide recovery process is not included, it is possible to reduce the equipment investment cost, as well as to easily recover a high concentration of carbon dioxide.
isCitedBy http://rdf.ncbi.nlm.nih.gov/pubchem/patent/CN-109266396-A
http://rdf.ncbi.nlm.nih.gov/pubchem/patent/WO-2015064793-A1
http://rdf.ncbi.nlm.nih.gov/pubchem/patent/KR-101529823-B1
http://rdf.ncbi.nlm.nih.gov/pubchem/patent/KR-20160039108-A
priorityDate 2011-09-23-04:00^^<http://www.w3.org/2001/XMLSchema#date>
type http://data.epo.org/linked-data/def/patent/Publication

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