Mechanism of Fast Fluidization and Vertical Profile of Solid Concentration in Fast Fluidized Beds

The gas velocity in the circulating fluidized beds of, for example, aluminum ore calciners, petroleum crackers and boilers is larger than the particles' terminal velocity. We propose the growing chain model, in which the particles form vertical chains in the fluidized bed, in order to determine...

Ausführliche Beschreibung

Gespeichert in:
Bibliographische Detailangaben
Veröffentlicht in:JSME international journal. Series B, Fluids and thermal engineering Fluids and thermal engineering, 1996-05, Vol.39 (2), p.387-394
Hauptverfasser: FUJIMA, Yukihisa, TAGASHIRA, Kenji, TAKATSUKA, Hiromu, ARAKAWA, Yoshihisa, HASEGAWA, Takashi
Format: Artikel
Sprache:eng
Schlagworte:
Online-Zugang:Volltext
Tags: Tag hinzufügen
Keine Tags, Fügen Sie den ersten Tag hinzu!
container_end_page 394
container_issue 2
container_start_page 387
container_title JSME international journal. Series B, Fluids and thermal engineering
container_volume 39
creator FUJIMA, Yukihisa
TAGASHIRA, Kenji
TAKATSUKA, Hiromu
ARAKAWA, Yoshihisa
HASEGAWA, Takashi
description The gas velocity in the circulating fluidized beds of, for example, aluminum ore calciners, petroleum crackers and boilers is larger than the particles' terminal velocity. We propose the growing chain model, in which the particles form vertical chains in the fluidized bed, in order to determine theoretically the regimes of fast fluidization. Comparing the fluidization condition empirically recognized as the optimum operating condition for the circulating fluidized bed in boilers, the maximum fast fluidization gas velocity is found to coincide with the terminal velocity of an infinitely long chain, which is about twice as high as that of a single particle.
doi_str_mv 10.1299/jsmeb.39.387
format Article
fullrecord <record><control><sourceid>proquest</sourceid><recordid>TN_cdi_proquest_miscellaneous_745747672</recordid><sourceformat>XML</sourceformat><sourcesystem>PC</sourcesystem><sourcerecordid>3154148951</sourcerecordid><originalsourceid>FETCH-LOGICAL-n242t-8525c24bb8a2ca24fd64af68d000072cbb44eb56ef3393e472bc37a28d5b76f53</originalsourceid><addsrcrecordid>eNpdjjtPwzAYRS0EEqWw8QMsMTClOH4mI1QUkIpA4rFWfnwWjhwb4mTh11MoC9zl3uHo6CJ0WpNFTdv2ois9mAVrF6xRe2hWM64qwVS9_7NJ1RDBD9FRKR0hjAnZzpC-B_umUyg9zh6vdBnxKk7BhU89hpywTg6_wjAGqyN-HLIPEb7JpxyDw8ucLKRx2LEh_RGAw1fgyjE68DoWOPntOXpZXT8vb6v1w83d8nJdJcrpWDWCCku5MY2mVlPuneTay8aRbRS1xnAORkjwjLUMuKLGMqVp44RR0gs2R-c77_uQPyYo46YPxUKMOkGeykZxobiSim7Js39kl6chbc9tai6VIKJlhH0BVw1kkQ</addsrcrecordid><sourcetype>Aggregation Database</sourcetype><iscdi>true</iscdi><recordtype>article</recordtype><pqid>1467505930</pqid></control><display><type>article</type><title>Mechanism of Fast Fluidization and Vertical Profile of Solid Concentration in Fast Fluidized Beds</title><source>J-STAGE Free</source><source>Elektronische Zeitschriftenbibliothek - Frei zugängliche E-Journals</source><creator>FUJIMA, Yukihisa ; TAGASHIRA, Kenji ; TAKATSUKA, Hiromu ; ARAKAWA, Yoshihisa ; HASEGAWA, Takashi</creator><creatorcontrib>FUJIMA, Yukihisa ; TAGASHIRA, Kenji ; TAKATSUKA, Hiromu ; ARAKAWA, Yoshihisa ; HASEGAWA, Takashi</creatorcontrib><description>The gas velocity in the circulating fluidized beds of, for example, aluminum ore calciners, petroleum crackers and boilers is larger than the particles' terminal velocity. We propose the growing chain model, in which the particles form vertical chains in the fluidized bed, in order to determine theoretically the regimes of fast fluidization. Comparing the fluidization condition empirically recognized as the optimum operating condition for the circulating fluidized bed in boilers, the maximum fast fluidization gas velocity is found to coincide with the terminal velocity of an infinitely long chain, which is about twice as high as that of a single particle.</description><identifier>ISSN: 1340-8054</identifier><identifier>EISSN: 1347-5371</identifier><identifier>DOI: 10.1299/jsmeb.39.387</identifier><language>eng</language><publisher>Tokyo: Japan Science and Technology Agency</publisher><subject>Chemical reactors ; Fluidization ; Gases ; Mathematical models ; Velocity</subject><ispartof>JSME international journal. Series B, Fluids and thermal engineering, 1996-05, Vol.39 (2), p.387-394</ispartof><rights>Copyright Japan Science and Technology Agency 1996</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><link.rule.ids>314,776,780,27901,27902</link.rule.ids></links><search><creatorcontrib>FUJIMA, Yukihisa</creatorcontrib><creatorcontrib>TAGASHIRA, Kenji</creatorcontrib><creatorcontrib>TAKATSUKA, Hiromu</creatorcontrib><creatorcontrib>ARAKAWA, Yoshihisa</creatorcontrib><creatorcontrib>HASEGAWA, Takashi</creatorcontrib><title>Mechanism of Fast Fluidization and Vertical Profile of Solid Concentration in Fast Fluidized Beds</title><title>JSME international journal. Series B, Fluids and thermal engineering</title><description>The gas velocity in the circulating fluidized beds of, for example, aluminum ore calciners, petroleum crackers and boilers is larger than the particles' terminal velocity. We propose the growing chain model, in which the particles form vertical chains in the fluidized bed, in order to determine theoretically the regimes of fast fluidization. Comparing the fluidization condition empirically recognized as the optimum operating condition for the circulating fluidized bed in boilers, the maximum fast fluidization gas velocity is found to coincide with the terminal velocity of an infinitely long chain, which is about twice as high as that of a single particle.</description><subject>Chemical reactors</subject><subject>Fluidization</subject><subject>Gases</subject><subject>Mathematical models</subject><subject>Velocity</subject><issn>1340-8054</issn><issn>1347-5371</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>1996</creationdate><recordtype>article</recordtype><recordid>eNpdjjtPwzAYRS0EEqWw8QMsMTClOH4mI1QUkIpA4rFWfnwWjhwb4mTh11MoC9zl3uHo6CJ0WpNFTdv2ois9mAVrF6xRe2hWM64qwVS9_7NJ1RDBD9FRKR0hjAnZzpC-B_umUyg9zh6vdBnxKk7BhU89hpywTg6_wjAGqyN-HLIPEb7JpxyDw8ucLKRx2LEh_RGAw1fgyjE68DoWOPntOXpZXT8vb6v1w83d8nJdJcrpWDWCCku5MY2mVlPuneTay8aRbRS1xnAORkjwjLUMuKLGMqVp44RR0gs2R-c77_uQPyYo46YPxUKMOkGeykZxobiSim7Js39kl6chbc9tai6VIKJlhH0BVw1kkQ</recordid><startdate>19960501</startdate><enddate>19960501</enddate><creator>FUJIMA, Yukihisa</creator><creator>TAGASHIRA, Kenji</creator><creator>TAKATSUKA, Hiromu</creator><creator>ARAKAWA, Yoshihisa</creator><creator>HASEGAWA, Takashi</creator><general>Japan Science and Technology Agency</general><scope>7TC</scope></search><sort><creationdate>19960501</creationdate><title>Mechanism of Fast Fluidization and Vertical Profile of Solid Concentration in Fast Fluidized Beds</title><author>FUJIMA, Yukihisa ; TAGASHIRA, Kenji ; TAKATSUKA, Hiromu ; ARAKAWA, Yoshihisa ; HASEGAWA, Takashi</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-n242t-8525c24bb8a2ca24fd64af68d000072cbb44eb56ef3393e472bc37a28d5b76f53</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>1996</creationdate><topic>Chemical reactors</topic><topic>Fluidization</topic><topic>Gases</topic><topic>Mathematical models</topic><topic>Velocity</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>FUJIMA, Yukihisa</creatorcontrib><creatorcontrib>TAGASHIRA, Kenji</creatorcontrib><creatorcontrib>TAKATSUKA, Hiromu</creatorcontrib><creatorcontrib>ARAKAWA, Yoshihisa</creatorcontrib><creatorcontrib>HASEGAWA, Takashi</creatorcontrib><collection>Mechanical Engineering Abstracts</collection><jtitle>JSME international journal. Series B, Fluids and thermal engineering</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>FUJIMA, Yukihisa</au><au>TAGASHIRA, Kenji</au><au>TAKATSUKA, Hiromu</au><au>ARAKAWA, Yoshihisa</au><au>HASEGAWA, Takashi</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Mechanism of Fast Fluidization and Vertical Profile of Solid Concentration in Fast Fluidized Beds</atitle><jtitle>JSME international journal. Series B, Fluids and thermal engineering</jtitle><date>1996-05-01</date><risdate>1996</risdate><volume>39</volume><issue>2</issue><spage>387</spage><epage>394</epage><pages>387-394</pages><issn>1340-8054</issn><eissn>1347-5371</eissn><abstract>The gas velocity in the circulating fluidized beds of, for example, aluminum ore calciners, petroleum crackers and boilers is larger than the particles' terminal velocity. We propose the growing chain model, in which the particles form vertical chains in the fluidized bed, in order to determine theoretically the regimes of fast fluidization. Comparing the fluidization condition empirically recognized as the optimum operating condition for the circulating fluidized bed in boilers, the maximum fast fluidization gas velocity is found to coincide with the terminal velocity of an infinitely long chain, which is about twice as high as that of a single particle.</abstract><cop>Tokyo</cop><pub>Japan Science and Technology Agency</pub><doi>10.1299/jsmeb.39.387</doi><tpages>8</tpages></addata></record>
fulltext fulltext
identifier ISSN: 1340-8054
ispartof JSME international journal. Series B, Fluids and thermal engineering, 1996-05, Vol.39 (2), p.387-394
issn 1340-8054
1347-5371
language eng
recordid cdi_proquest_miscellaneous_745747672
source J-STAGE Free; Elektronische Zeitschriftenbibliothek - Frei zugängliche E-Journals
subjects Chemical reactors
Fluidization
Gases
Mathematical models
Velocity
title Mechanism of Fast Fluidization and Vertical Profile of Solid Concentration in Fast Fluidized Beds
url https://sfx.bib-bvb.de/sfx_tum?ctx_ver=Z39.88-2004&ctx_enc=info:ofi/enc:UTF-8&ctx_tim=2025-02-04T11%3A59%3A33IST&url_ver=Z39.88-2004&url_ctx_fmt=infofi/fmt:kev:mtx:ctx&rfr_id=info:sid/primo.exlibrisgroup.com:primo3-Article-proquest&rft_val_fmt=info:ofi/fmt:kev:mtx:journal&rft.genre=article&rft.atitle=Mechanism%20of%20Fast%20Fluidization%20and%20Vertical%20Profile%20of%20Solid%20Concentration%20in%20Fast%20Fluidized%20Beds&rft.jtitle=JSME%20international%20journal.%20Series%20B,%20Fluids%20and%20thermal%20engineering&rft.au=FUJIMA,%20Yukihisa&rft.date=1996-05-01&rft.volume=39&rft.issue=2&rft.spage=387&rft.epage=394&rft.pages=387-394&rft.issn=1340-8054&rft.eissn=1347-5371&rft_id=info:doi/10.1299/jsmeb.39.387&rft_dat=%3Cproquest%3E3154148951%3C/proquest%3E%3Curl%3E%3C/url%3E&disable_directlink=true&sfx.directlink=off&sfx.report_link=0&rft_id=info:oai/&rft_pqid=1467505930&rft_id=info:pmid/&rfr_iscdi=true