Coal gasification characteristics in a downer reactor

Cited 54 time in webofscience Cited 0 time in scopus
  • Hit : 740
  • Download : 17
DC FieldValueLanguage
dc.contributor.authorKim, Sang Doneko
dc.contributor.authorKim, Yong jeonko
dc.contributor.authorLee, Si hoonko
dc.date.accessioned2008-04-28T09:12:44Z-
dc.date.available2008-04-28T09:12:44Z-
dc.date.created2012-02-06-
dc.date.created2012-02-06-
dc.date.issued2001-01-
dc.identifier.citationFUEL, v.80, no.13, pp.1915 - 1922-
dc.identifier.issn0016-2361-
dc.identifier.urihttp://hdl.handle.net/10203/4243-
dc.description.abstractSubbituminous coal (Shenwha) was gasified at atmospheric pressure in a downer reactor (0.1 m I.D. X 5.0 m high). The effects of reaction temperature (750-850 degreesC), steam/coal mass ratio (0.23-0.86), O-2/H2O mole ratio (0-1.81) and coal feeding rate (5.3-9.0 kg h(-1)) on the composition of product gas, carbon conversion, cold gas efficiency, gas yield and calorific value have been determined. In the case of steam injection into the loop-seal, compositions of the product gas (vol. %; N-2 free basis) in the gasification region are H-2 (35.8-39.4%), CH4 (6.8-15.5%), CO (14.9-15.9%), CO2 (20.7-29.5%), C2H4 (2.8-4.9%), C2H6 (2.5-3.5%), C3H6 (1.6-3.3%) and C3H8 (1.7-2.5%) with a calorific value of 13.0-15.2 MJ/m(3). By changing the reactant gas supplied into the loop-seal for solid circulation from steam to air, product gas yield and carbon conversion increase, whereas calorific value of the product gas decreases from 13.0-15.2 to 6.3-10.6 with reaction temperature. (C) 2001 Published by Elsevier Science Ltd.-
dc.description.sponsorshipMinistry of Commerce, Industry and Energy through the R&D Mangagement Center for Energy and Resources, Koreaen
dc.languageEnglish-
dc.language.isoen_USen
dc.publisherElsevier Sci Ltd-
dc.subjectSPOUTED BED REACTOR-
dc.subjectFLUIDIZED-BED-
dc.titleCoal gasification characteristics in a downer reactor-
dc.typeArticle-
dc.identifier.wosid000171584300009-
dc.identifier.scopusid2-s2.0-0035475187-
dc.type.rimsART-
dc.citation.volume80-
dc.citation.issue13-
dc.citation.beginningpage1915-
dc.citation.endingpage1922-
dc.citation.publicationnameFUEL-
dc.embargo.liftdate9999-12-31-
dc.embargo.terms9999-12-31-
dc.contributor.localauthorKim, Sang Done-
dc.contributor.nonIdAuthorKim, Yong jeon-
dc.contributor.nonIdAuthorLee, Si hoon-
dc.type.journalArticleArticle-
dc.subject.keywordAuthordowner-
dc.subject.keywordAuthorcoal gasification-
dc.subject.keywordAuthorcirculating fluidized bed-
dc.subject.keywordAuthormedium calorific value gas-
dc.subject.keywordPlusSPOUTED BED REACTOR-
dc.subject.keywordPlusFLUIDIZED-BED-
Appears in Collection
CBE-Journal Papers(저널논문)
Files in This Item
This item is cited by other documents in WoS
⊙ Detail Information in WoSⓡ Click to see webofscience_button
⊙ Cited 54 items in WoS Click to see citing articles in records_button

qr_code

  • mendeley

    citeulike


rss_1.0 rss_2.0 atom_1.0