Heat transfer in liquid-liquid spray towers
An experimental investigation of heat transfer rates in which were used three spray towers varying from 4 to 6 in. in diameter and 7 to 10 ft. in height, and distributor elements with hole sizes varying from 1/8 to 1/64 in. in diameter was carried out. The immiscible liquid system consisted of water...
Gespeichert in:
| Veröffentlicht in: | AIChE journal 1967-11, Vol.13 (6), p.1160-1166 |
|---|---|
| Hauptverfasser: | , , |
| Format: | Artikel |
| Sprache: | eng |
| Online-Zugang: | Volltext |
| Tags: |
Tag hinzufügen
Keine Tags, Fügen Sie den ersten Tag hinzu!
|
| container_end_page | 1166 |
|---|---|
| container_issue | 6 |
| container_start_page | 1160 |
| container_title | AIChE journal |
| container_volume | 13 |
| creator | Greskovich, E. J. Barton, Paul Hersh, R. E. |
| description | An experimental investigation of heat transfer rates in which were used three spray towers varying from 4 to 6 in. in diameter and 7 to 10 ft. in height, and distributor elements with hole sizes varying from 1/8 to 1/64 in. in diameter was carried out. The immiscible liquid system consisted of water and kerosene (normal boiling point range 395° to 490°F.). Volumetric heat transfer coefficients ranged from 100 to 3,600 B.t.u./(hr.)(cu. ft.)(°F.) and the overall film heat transfer coefficients ranged from 4 to 23 B.t.u./(hr.)(sq. ft.)(°F.). Height equivalent to a theoretical stage varied from 1 to 8 ft. Scale‐up correlations relating these rate data to operating variables were developed. |
| doi_str_mv | 10.1002/aic.690130623 |
| format | Article |
| fullrecord | <record><control><sourceid>istex_cross</sourceid><recordid>TN_cdi_crossref_primary_10_1002_aic_690130623</recordid><sourceformat>XML</sourceformat><sourcesystem>PC</sourcesystem><sourcerecordid>ark_67375_WNG_D0BFLM6M_S</sourcerecordid><originalsourceid>FETCH-LOGICAL-c3233-f8ec961abd13cdd13d467376a481de80104da62c32c7856aca683b7050c186053</originalsourceid><addsrcrecordid>eNp9j71PwzAQxS0EEqEwsmdHLmc7_shYAv2QUhgAMVqu40iG0BY7qOS_J1Wqionlnu70e3f3ELomMCYA9NZ4OxY5EAaCshOUEJ5JzHPgpygBAIL7ATlHFzG-9x2ViiboZu5Mm7bBrGPtQurXaeO_vn2FB0njNpgubTc7F-IlOqtNE93VQUfodfrwUsxx-TRbFJMSW0YZw7VyNhfErCrCbNWXKhOSSWEyRSqngEBWGUF72ErFhbFGKLaSwMESJYCzEcLDXhs2MQZX623wnyZ0moDeJ9V9Un1M2vNy4He-cd3_sJ4sir_OwyUfW_dzdJrwofcvc_32ONP3cDctl2Kpn9kvYZJkaQ</addsrcrecordid><sourcetype>Aggregation Database</sourcetype><iscdi>true</iscdi><recordtype>article</recordtype></control><display><type>article</type><title>Heat transfer in liquid-liquid spray towers</title><source>Wiley Online Library Journals Frontfile Complete</source><creator>Greskovich, E. J. ; Barton, Paul ; Hersh, R. E.</creator><creatorcontrib>Greskovich, E. J. ; Barton, Paul ; Hersh, R. E.</creatorcontrib><description>An experimental investigation of heat transfer rates in which were used three spray towers varying from 4 to 6 in. in diameter and 7 to 10 ft. in height, and distributor elements with hole sizes varying from 1/8 to 1/64 in. in diameter was carried out. The immiscible liquid system consisted of water and kerosene (normal boiling point range 395° to 490°F.). Volumetric heat transfer coefficients ranged from 100 to 3,600 B.t.u./(hr.)(cu. ft.)(°F.) and the overall film heat transfer coefficients ranged from 4 to 23 B.t.u./(hr.)(sq. ft.)(°F.). Height equivalent to a theoretical stage varied from 1 to 8 ft. Scale‐up correlations relating these rate data to operating variables were developed.</description><identifier>ISSN: 0001-1541</identifier><identifier>EISSN: 1547-5905</identifier><identifier>DOI: 10.1002/aic.690130623</identifier><language>eng</language><publisher>New York: American Institute of Chemical Engineers</publisher><ispartof>AIChE journal, 1967-11, Vol.13 (6), p.1160-1166</ispartof><rights>Copyright © 1967 American Institute of Chemical Engineers</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c3233-f8ec961abd13cdd13d467376a481de80104da62c32c7856aca683b7050c186053</citedby><cites>FETCH-LOGICAL-c3233-f8ec961abd13cdd13d467376a481de80104da62c32c7856aca683b7050c186053</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktopdf>$$Uhttps://onlinelibrary.wiley.com/doi/pdf/10.1002%2Faic.690130623$$EPDF$$P50$$Gwiley$$H</linktopdf><linktohtml>$$Uhttps://onlinelibrary.wiley.com/doi/full/10.1002%2Faic.690130623$$EHTML$$P50$$Gwiley$$H</linktohtml><link.rule.ids>314,778,782,1414,27907,27908,45557,45558</link.rule.ids></links><search><creatorcontrib>Greskovich, E. J.</creatorcontrib><creatorcontrib>Barton, Paul</creatorcontrib><creatorcontrib>Hersh, R. E.</creatorcontrib><title>Heat transfer in liquid-liquid spray towers</title><title>AIChE journal</title><addtitle>AIChE J</addtitle><description>An experimental investigation of heat transfer rates in which were used three spray towers varying from 4 to 6 in. in diameter and 7 to 10 ft. in height, and distributor elements with hole sizes varying from 1/8 to 1/64 in. in diameter was carried out. The immiscible liquid system consisted of water and kerosene (normal boiling point range 395° to 490°F.). Volumetric heat transfer coefficients ranged from 100 to 3,600 B.t.u./(hr.)(cu. ft.)(°F.) and the overall film heat transfer coefficients ranged from 4 to 23 B.t.u./(hr.)(sq. ft.)(°F.). Height equivalent to a theoretical stage varied from 1 to 8 ft. Scale‐up correlations relating these rate data to operating variables were developed.</description><issn>0001-1541</issn><issn>1547-5905</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>1967</creationdate><recordtype>article</recordtype><recordid>eNp9j71PwzAQxS0EEqEwsmdHLmc7_shYAv2QUhgAMVqu40iG0BY7qOS_J1Wqionlnu70e3f3ELomMCYA9NZ4OxY5EAaCshOUEJ5JzHPgpygBAIL7ATlHFzG-9x2ViiboZu5Mm7bBrGPtQurXaeO_vn2FB0njNpgubTc7F-IlOqtNE93VQUfodfrwUsxx-TRbFJMSW0YZw7VyNhfErCrCbNWXKhOSSWEyRSqngEBWGUF72ErFhbFGKLaSwMESJYCzEcLDXhs2MQZX623wnyZ0moDeJ9V9Un1M2vNy4He-cd3_sJ4sir_OwyUfW_dzdJrwofcvc_32ONP3cDctl2Kpn9kvYZJkaQ</recordid><startdate>196711</startdate><enddate>196711</enddate><creator>Greskovich, E. J.</creator><creator>Barton, Paul</creator><creator>Hersh, R. E.</creator><general>American Institute of Chemical Engineers</general><scope>BSCLL</scope><scope>AAYXX</scope><scope>CITATION</scope></search><sort><creationdate>196711</creationdate><title>Heat transfer in liquid-liquid spray towers</title><author>Greskovich, E. J. ; Barton, Paul ; Hersh, R. E.</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c3233-f8ec961abd13cdd13d467376a481de80104da62c32c7856aca683b7050c186053</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>1967</creationdate><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Greskovich, E. J.</creatorcontrib><creatorcontrib>Barton, Paul</creatorcontrib><creatorcontrib>Hersh, R. E.</creatorcontrib><collection>Istex</collection><collection>CrossRef</collection><jtitle>AIChE journal</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Greskovich, E. J.</au><au>Barton, Paul</au><au>Hersh, R. E.</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Heat transfer in liquid-liquid spray towers</atitle><jtitle>AIChE journal</jtitle><addtitle>AIChE J</addtitle><date>1967-11</date><risdate>1967</risdate><volume>13</volume><issue>6</issue><spage>1160</spage><epage>1166</epage><pages>1160-1166</pages><issn>0001-1541</issn><eissn>1547-5905</eissn><abstract>An experimental investigation of heat transfer rates in which were used three spray towers varying from 4 to 6 in. in diameter and 7 to 10 ft. in height, and distributor elements with hole sizes varying from 1/8 to 1/64 in. in diameter was carried out. The immiscible liquid system consisted of water and kerosene (normal boiling point range 395° to 490°F.). Volumetric heat transfer coefficients ranged from 100 to 3,600 B.t.u./(hr.)(cu. ft.)(°F.) and the overall film heat transfer coefficients ranged from 4 to 23 B.t.u./(hr.)(sq. ft.)(°F.). Height equivalent to a theoretical stage varied from 1 to 8 ft. Scale‐up correlations relating these rate data to operating variables were developed.</abstract><cop>New York</cop><pub>American Institute of Chemical Engineers</pub><doi>10.1002/aic.690130623</doi><tpages>7</tpages></addata></record> |
| fulltext | fulltext |
| identifier | ISSN: 0001-1541 |
| ispartof | AIChE journal, 1967-11, Vol.13 (6), p.1160-1166 |
| issn | 0001-1541 1547-5905 |
| language | eng |
| recordid | cdi_crossref_primary_10_1002_aic_690130623 |
| source | Wiley Online Library Journals Frontfile Complete |
| title | Heat transfer in liquid-liquid spray towers |
| url | https://sfx.bib-bvb.de/sfx_tum?ctx_ver=Z39.88-2004&ctx_enc=info:ofi/enc:UTF-8&ctx_tim=2025-01-16T21%3A11%3A53IST&url_ver=Z39.88-2004&url_ctx_fmt=infofi/fmt:kev:mtx:ctx&rfr_id=info:sid/primo.exlibrisgroup.com:primo3-Article-istex_cross&rft_val_fmt=info:ofi/fmt:kev:mtx:journal&rft.genre=article&rft.atitle=Heat%20transfer%20in%20liquid-liquid%20spray%20towers&rft.jtitle=AIChE%20journal&rft.au=Greskovich,%20E.%20J.&rft.date=1967-11&rft.volume=13&rft.issue=6&rft.spage=1160&rft.epage=1166&rft.pages=1160-1166&rft.issn=0001-1541&rft.eissn=1547-5905&rft_id=info:doi/10.1002/aic.690130623&rft_dat=%3Cistex_cross%3Eark_67375_WNG_D0BFLM6M_S%3C/istex_cross%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 |