INDIRECT THERMAL DRYING OF LIGNITE: DESIGN ASPECTS OF A ROTARY DRYER

An investigation of the thermal drying of lignite has been carried out, by using an indirect heat pilot rotary drum. The process aims at the production of dry lignite and clean steam as part of a gasification procedure. Both flighted and bare drum modes have been employed. Temperature profiles along...

Ausführliche Beschreibung

Gespeichert in:
Bibliographische Detailangaben
Veröffentlicht in:Drying technology 2000-10, Vol.18 (9), p.2009-2049
Hauptverfasser: Hatzilyberis, K.S., Androutsopoulos, G.P., Salmas, C.E.
Format: Artikel
Sprache:eng
Schlagworte:
Online-Zugang:Volltext
Tags: Tag hinzufügen
Keine Tags, Fügen Sie den ersten Tag hinzu!
container_end_page 2049
container_issue 9
container_start_page 2009
container_title Drying technology
container_volume 18
creator Hatzilyberis, K.S.
Androutsopoulos, G.P.
Salmas, C.E.
description An investigation of the thermal drying of lignite has been carried out, by using an indirect heat pilot rotary drum. The process aims at the production of dry lignite and clean steam as part of a gasification procedure. Both flighted and bare drum modes have been employed. Temperature profiles along the dryer length, the amount of evaporation (moisture conversion) and the solids residence time distribution (RTD) were measured. A non-isothermal model was tested under three different regimes of solids flow. Model integration, by taking account of experimental amount of evaporation at dryer exit and temperature profiles along the dryer length, has been utilized in the validation of drying kinetics and heat transfer correlations. Model predictions compare satisfactorily with the operating data of an indirect heat industrial lignite dryer. Overall heat transfer coefficients of the pilot rotary dryer were found to agree well with those reported for direct heat dryers.
doi_str_mv 10.1080/07373930008917824
format Article
fullrecord <record><control><sourceid>crossref_infor</sourceid><recordid>TN_cdi_crossref_primary_10_1080_07373930008917824</recordid><sourceformat>XML</sourceformat><sourcesystem>PC</sourcesystem><sourcerecordid>10_1080_07373930008917824</sourcerecordid><originalsourceid>FETCH-LOGICAL-c382t-808e767ddccebbb8953af669498f7b2c63de852396c1751f2b0e254d0a8ad2ef3</originalsourceid><addsrcrecordid>eNqFkM9Og0AQhzdGE2v1AbztC6D7B9hd44UUSkkQDOChJ7IsuwmmLWYhsX17IfXWGE8zmd_3zSQDwCNGTxhx9IwYZVRQhBAXmHHiXoEF9ihxyDS7Bos5dyaA3YK7YficOSy8BQiTLEyKaFXBahMVb0EKw2KbZDHM1zBN4iypohcYRuXUwqB8n8ByjgJY5FVQbGc6Ku7BjZG7QT_81iX4WEfVauOkeZysgtRRlJPR4Yhr5rO2VUo3TcOFR6XxfeEKblhDlE9bzT1Cha8w87AhDdLEc1skuWyJNnQJ8Hmvsv0wWG3qL9vtpT3VGNXzG-qLN0wOOzvdwfR2L797u2vrUZ52vTVWHlQ3XFr1eBwn8_Vfk_59-AdQQW5q</addsrcrecordid><sourcetype>Aggregation Database</sourcetype><iscdi>true</iscdi><recordtype>article</recordtype></control><display><type>article</type><title>INDIRECT THERMAL DRYING OF LIGNITE: DESIGN ASPECTS OF A ROTARY DRYER</title><source>Taylor &amp; Francis Journals Complete</source><creator>Hatzilyberis, K.S. ; Androutsopoulos, G.P. ; Salmas, C.E.</creator><creatorcontrib>Hatzilyberis, K.S. ; Androutsopoulos, G.P. ; Salmas, C.E.</creatorcontrib><description>An investigation of the thermal drying of lignite has been carried out, by using an indirect heat pilot rotary drum. The process aims at the production of dry lignite and clean steam as part of a gasification procedure. Both flighted and bare drum modes have been employed. Temperature profiles along the dryer length, the amount of evaporation (moisture conversion) and the solids residence time distribution (RTD) were measured. A non-isothermal model was tested under three different regimes of solids flow. Model integration, by taking account of experimental amount of evaporation at dryer exit and temperature profiles along the dryer length, has been utilized in the validation of drying kinetics and heat transfer correlations. Model predictions compare satisfactorily with the operating data of an indirect heat industrial lignite dryer. Overall heat transfer coefficients of the pilot rotary dryer were found to agree well with those reported for direct heat dryers.</description><identifier>ISSN: 0737-3937</identifier><identifier>EISSN: 1532-2300</identifier><identifier>DOI: 10.1080/07373930008917824</identifier><language>eng</language><publisher>Taylor &amp; Francis Group</publisher><subject>allothermal; rotary drum; moisture conversion; drying kinetics; heat transfer coefficient; indirect heat; gasification plant</subject><ispartof>Drying technology, 2000-10, Vol.18 (9), p.2009-2049</ispartof><rights>Copyright Taylor &amp; Francis Group, LLC 2000</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c382t-808e767ddccebbb8953af669498f7b2c63de852396c1751f2b0e254d0a8ad2ef3</citedby><cites>FETCH-LOGICAL-c382t-808e767ddccebbb8953af669498f7b2c63de852396c1751f2b0e254d0a8ad2ef3</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktopdf>$$Uhttps://www.tandfonline.com/doi/pdf/10.1080/07373930008917824$$EPDF$$P50$$Ginformaworld$$H</linktopdf><linktohtml>$$Uhttps://www.tandfonline.com/doi/full/10.1080/07373930008917824$$EHTML$$P50$$Ginformaworld$$H</linktohtml><link.rule.ids>314,780,784,27924,27925,59647,60436</link.rule.ids></links><search><creatorcontrib>Hatzilyberis, K.S.</creatorcontrib><creatorcontrib>Androutsopoulos, G.P.</creatorcontrib><creatorcontrib>Salmas, C.E.</creatorcontrib><title>INDIRECT THERMAL DRYING OF LIGNITE: DESIGN ASPECTS OF A ROTARY DRYER</title><title>Drying technology</title><description>An investigation of the thermal drying of lignite has been carried out, by using an indirect heat pilot rotary drum. The process aims at the production of dry lignite and clean steam as part of a gasification procedure. Both flighted and bare drum modes have been employed. Temperature profiles along the dryer length, the amount of evaporation (moisture conversion) and the solids residence time distribution (RTD) were measured. A non-isothermal model was tested under three different regimes of solids flow. Model integration, by taking account of experimental amount of evaporation at dryer exit and temperature profiles along the dryer length, has been utilized in the validation of drying kinetics and heat transfer correlations. Model predictions compare satisfactorily with the operating data of an indirect heat industrial lignite dryer. Overall heat transfer coefficients of the pilot rotary dryer were found to agree well with those reported for direct heat dryers.</description><subject>allothermal; rotary drum; moisture conversion; drying kinetics; heat transfer coefficient; indirect heat; gasification plant</subject><issn>0737-3937</issn><issn>1532-2300</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2000</creationdate><recordtype>article</recordtype><recordid>eNqFkM9Og0AQhzdGE2v1AbztC6D7B9hd44UUSkkQDOChJ7IsuwmmLWYhsX17IfXWGE8zmd_3zSQDwCNGTxhx9IwYZVRQhBAXmHHiXoEF9ihxyDS7Bos5dyaA3YK7YficOSy8BQiTLEyKaFXBahMVb0EKw2KbZDHM1zBN4iypohcYRuXUwqB8n8ByjgJY5FVQbGc6Ku7BjZG7QT_81iX4WEfVauOkeZysgtRRlJPR4Yhr5rO2VUo3TcOFR6XxfeEKblhDlE9bzT1Cha8w87AhDdLEc1skuWyJNnQJ8Hmvsv0wWG3qL9vtpT3VGNXzG-qLN0wOOzvdwfR2L797u2vrUZ52vTVWHlQ3XFr1eBwn8_Vfk_59-AdQQW5q</recordid><startdate>20001001</startdate><enddate>20001001</enddate><creator>Hatzilyberis, K.S.</creator><creator>Androutsopoulos, G.P.</creator><creator>Salmas, C.E.</creator><general>Taylor &amp; Francis Group</general><scope>AAYXX</scope><scope>CITATION</scope></search><sort><creationdate>20001001</creationdate><title>INDIRECT THERMAL DRYING OF LIGNITE: DESIGN ASPECTS OF A ROTARY DRYER</title><author>Hatzilyberis, K.S. ; Androutsopoulos, G.P. ; Salmas, C.E.</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c382t-808e767ddccebbb8953af669498f7b2c63de852396c1751f2b0e254d0a8ad2ef3</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2000</creationdate><topic>allothermal; rotary drum; moisture conversion; drying kinetics; heat transfer coefficient; indirect heat; gasification plant</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Hatzilyberis, K.S.</creatorcontrib><creatorcontrib>Androutsopoulos, G.P.</creatorcontrib><creatorcontrib>Salmas, C.E.</creatorcontrib><collection>CrossRef</collection><jtitle>Drying technology</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Hatzilyberis, K.S.</au><au>Androutsopoulos, G.P.</au><au>Salmas, C.E.</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>INDIRECT THERMAL DRYING OF LIGNITE: DESIGN ASPECTS OF A ROTARY DRYER</atitle><jtitle>Drying technology</jtitle><date>2000-10-01</date><risdate>2000</risdate><volume>18</volume><issue>9</issue><spage>2009</spage><epage>2049</epage><pages>2009-2049</pages><issn>0737-3937</issn><eissn>1532-2300</eissn><abstract>An investigation of the thermal drying of lignite has been carried out, by using an indirect heat pilot rotary drum. The process aims at the production of dry lignite and clean steam as part of a gasification procedure. Both flighted and bare drum modes have been employed. Temperature profiles along the dryer length, the amount of evaporation (moisture conversion) and the solids residence time distribution (RTD) were measured. A non-isothermal model was tested under three different regimes of solids flow. Model integration, by taking account of experimental amount of evaporation at dryer exit and temperature profiles along the dryer length, has been utilized in the validation of drying kinetics and heat transfer correlations. Model predictions compare satisfactorily with the operating data of an indirect heat industrial lignite dryer. Overall heat transfer coefficients of the pilot rotary dryer were found to agree well with those reported for direct heat dryers.</abstract><pub>Taylor &amp; Francis Group</pub><doi>10.1080/07373930008917824</doi><tpages>41</tpages></addata></record>
fulltext fulltext
identifier ISSN: 0737-3937
ispartof Drying technology, 2000-10, Vol.18 (9), p.2009-2049
issn 0737-3937
1532-2300
language eng
recordid cdi_crossref_primary_10_1080_07373930008917824
source Taylor & Francis Journals Complete
subjects allothermal
rotary drum
moisture conversion
drying kinetics
heat transfer coefficient
indirect heat
gasification plant
title INDIRECT THERMAL DRYING OF LIGNITE: DESIGN ASPECTS OF A ROTARY DRYER
url https://sfx.bib-bvb.de/sfx_tum?ctx_ver=Z39.88-2004&ctx_enc=info:ofi/enc:UTF-8&ctx_tim=2025-01-03T17%3A22%3A40IST&url_ver=Z39.88-2004&url_ctx_fmt=infofi/fmt:kev:mtx:ctx&rfr_id=info:sid/primo.exlibrisgroup.com:primo3-Article-crossref_infor&rft_val_fmt=info:ofi/fmt:kev:mtx:journal&rft.genre=article&rft.atitle=INDIRECT%20THERMAL%20DRYING%20OF%20LIGNITE:%20DESIGN%20ASPECTS%20OF%20A%20ROTARY%20DRYER&rft.jtitle=Drying%20technology&rft.au=Hatzilyberis,%20K.S.&rft.date=2000-10-01&rft.volume=18&rft.issue=9&rft.spage=2009&rft.epage=2049&rft.pages=2009-2049&rft.issn=0737-3937&rft.eissn=1532-2300&rft_id=info:doi/10.1080/07373930008917824&rft_dat=%3Ccrossref_infor%3E10_1080_07373930008917824%3C/crossref_infor%3E%3Curl%3E%3C/url%3E&disable_directlink=true&sfx.directlink=off&sfx.report_link=0&rft_id=info:oai/&rft_id=info:pmid/&rfr_iscdi=true