HYDROGENATION OF ETHYLENE IN TWO DIMENSIONAL GAS-SOLID FLUIDISED BED WITH PERFORATED PLATE
A fairly rapid chemical reaction, i.e., hydrogenation of ethylene by palladium catalyst, was carried out at a room temperature in a two dimensional fluidised bed with a perforated plate distributor. The results were considerably affected by the behaviour of the bed near its bottom. The measured hydr...
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Veröffentlicht in: | JOURNAL OF CHEMICAL ENGINEERING OF JAPAN 1977/08/20, Vol.10(4), pp.307-313 |
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creator | TOEI, RYOZO OICHI, MORIHIRO HAYASHI, HISATAKA KUBO, KIYOKAZU YANAGIDA, TOSHIHIRO MATSUNO, RYUICHI |
description | A fairly rapid chemical reaction, i.e., hydrogenation of ethylene by palladium catalyst, was carried out at a room temperature in a two dimensional fluidised bed with a perforated plate distributor. The results were considerably affected by the behaviour of the bed near its bottom. The measured hydrogen conversion was compared with that predicted by the so-called "coalescence model". Consistency of the experimental and calculated results was fairly good. The significance of various parameters included in the model was also investigated. The parameters examined were the gas interchange coefficients, the volume fraction of particles in the bubble, and the gas flow rate as bubbles. In conclusion, it was pointed out that the deviation of gas flow rate as bubbles from that predicted by the two phase theory at the bottom of bed affected significantly the conversion of a rapid chemical reaction. |
doi_str_mv | 10.1252/jcej.10.307 |
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In conclusion, it was pointed out that the deviation of gas flow rate as bubbles from that predicted by the two phase theory at the bottom of bed affected significantly the conversion of a rapid chemical reaction.</description><identifier>ISSN: 0021-9592</identifier><identifier>EISSN: 1881-1299</identifier><identifier>DOI: 10.1252/jcej.10.307</identifier><language>eng</language><publisher>Tokyo: The Society of Chemical Engineers, Japan</publisher><ispartof>JOURNAL OF CHEMICAL ENGINEERING OF JAPAN, 1977/08/20, Vol.10(4), pp.307-313</ispartof><rights>The Society of Chemical Engineers, Japan</rights><rights>Copyright Japan Science and Technology Agency 1977</rights><lds50>peer_reviewed</lds50><oa>free_for_read</oa><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c3387-618b688c14cb53495171a11016927005557ff469628f0637551180d31594a1203</citedby></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><link.rule.ids>314,780,784,4024,27923,27924,27925</link.rule.ids></links><search><creatorcontrib>TOEI, RYOZO</creatorcontrib><creatorcontrib>OICHI, MORIHIRO</creatorcontrib><creatorcontrib>HAYASHI, HISATAKA</creatorcontrib><creatorcontrib>KUBO, KIYOKAZU</creatorcontrib><creatorcontrib>YANAGIDA, TOSHIHIRO</creatorcontrib><creatorcontrib>MATSUNO, RYUICHI</creatorcontrib><title>HYDROGENATION OF ETHYLENE IN TWO DIMENSIONAL GAS-SOLID FLUIDISED BED WITH PERFORATED PLATE</title><title>JOURNAL OF CHEMICAL ENGINEERING OF JAPAN</title><description>A fairly rapid chemical reaction, i.e., hydrogenation of ethylene by palladium catalyst, was carried out at a room temperature in a two dimensional fluidised bed with a perforated plate distributor. The results were considerably affected by the behaviour of the bed near its bottom. The measured hydrogen conversion was compared with that predicted by the so-called "coalescence model". Consistency of the experimental and calculated results was fairly good. The significance of various parameters included in the model was also investigated. The parameters examined were the gas interchange coefficients, the volume fraction of particles in the bubble, and the gas flow rate as bubbles. 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The results were considerably affected by the behaviour of the bed near its bottom. The measured hydrogen conversion was compared with that predicted by the so-called "coalescence model". Consistency of the experimental and calculated results was fairly good. The significance of various parameters included in the model was also investigated. The parameters examined were the gas interchange coefficients, the volume fraction of particles in the bubble, and the gas flow rate as bubbles. In conclusion, it was pointed out that the deviation of gas flow rate as bubbles from that predicted by the two phase theory at the bottom of bed affected significantly the conversion of a rapid chemical reaction.</abstract><cop>Tokyo</cop><pub>The Society of Chemical Engineers, Japan</pub><doi>10.1252/jcej.10.307</doi><tpages>7</tpages><oa>free_for_read</oa></addata></record> |
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title | HYDROGENATION OF ETHYLENE IN TWO DIMENSIONAL GAS-SOLID FLUIDISED BED WITH PERFORATED PLATE |
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