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Gasification of Greek lignite in an indirect heat (allothermal) rotary kiln gasifier

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dc.contributor.author Androutsopoulos, GP en
dc.contributor.author Hatzilyberis, KS en
dc.contributor.author Theofilou, NA en
dc.contributor.author Agalianos, DS en
dc.contributor.author Chronis, CG en
dc.contributor.author Kapassakalis, VN en
dc.contributor.author Karsakos, AG en
dc.contributor.author Katsaros, AN en
dc.contributor.author Stamatakis, CP en
dc.contributor.author Zissis, CL en
dc.date.accessioned 2014-03-01T01:19:00Z
dc.date.available 2014-03-01T01:19:00Z
dc.date.issued 2003 en
dc.identifier.issn 0098-6445 en
dc.identifier.uri https://dspace.lib.ntua.gr/xmlui/handle/123456789/15318
dc.subject Allothermal gasification en
dc.subject IGCC system en
dc.subject Lignite conversion en
dc.subject Rotary kiln en
dc.subject Synthesis gas en
dc.subject.classification Engineering, Chemical en
dc.subject.other Coal gasification en
dc.subject.other Energy conversion en
dc.subject.other Energy efficiency en
dc.subject.other Environmental protection en
dc.subject.other Fluidized beds en
dc.subject.other Pulverized fuel en
dc.subject.other Rotary kilns en
dc.subject.other Thermoelectric power plants en
dc.subject.other Gasifiers en
dc.subject.other Lignite en
dc.subject.other gasification en
dc.title Gasification of Greek lignite in an indirect heat (allothermal) rotary kiln gasifier en
heal.type journalArticle en
heal.identifier.primary 10.1080/00986440302165 en
heal.identifier.secondary http://dx.doi.org/10.1080/00986440302165 en
heal.language English en
heal.publicationDate 2003 en
heal.abstract This work reports the performance results of a pilot-size lignite gasification plant. The feed material was Greek lignite (Megalopolis), currently being employed for electricity generation in pulverized lignite-fired thermoelectric stations. Low energy conversion efficiency, low station availability, and environmental issues call for developing improved processes, e.g., an IGCC (Integrated Gasification Combined Cycle). An indirect heat (allothermal) rotary kiln was selected as the lignite gasification reactor for developing an overall gasification process of improved efficiency. Weeklong gasification runs, at near atmospheric pressure and maximum temperature in the range 900-950degreesC, validated high DAF lignite conversions, i.e., 90-95%, and the production of a medium heating value synthesis gas (i.e., 11-13 MJ/Nm(3) dry basis), despite the use of air for burning recycled product gas for process heating. Gas composition is equivalent to that of autothermal gasifiers (e.g., Lurgi, Winkler, Koppers-Totzek), which operate on oxygen, under pressure and strict moisture and particle size specifications. Similarly, the kiln gas is comparable to that of an allothermal, high-pressure, fluidized bed gasifier running with a high rank coal feed. The data indicate satisfactory gasification efficiency and a good thermal efficiency that should be improved further through heat integration of a scaled-up process based on an indirect heat rotary kiln gasifier. en
heal.publisher TAYLOR & FRANCIS LTD en
heal.journalName Chemical Engineering Communications en
dc.identifier.doi 10.1080/00986440302165 en
dc.identifier.isi ISI:000184793400007 en
dc.identifier.volume 190 en
dc.identifier.issue 9 en
dc.identifier.spage 1200 en
dc.identifier.epage 1232 en


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