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Mass Transfer of Ozone Using a Microporous Diffuser Reactor System
An ozone reactor was constructed using a tubular gas diffuser made of microporous stainless steel to significantly reduce gas bubble size and increase overall mass transfer area. Overall mass transfer coefficient, K L a [s −1 ], was correlated with gas (G) and liquid (L) flow rates using K L a = AL...
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| Published in: | Ozone: science & engineering 2005-02, Vol.27 (1), p.45-51 |
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| Main Authors: | , , , |
| Format: | Article |
| Language: | English |
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| cited_by | cdi_FETCH-LOGICAL-c376t-cac90a3d3f0f6ef4c5136903f280cae280d4fd999f12b7eaff44ac129e07b7f83 |
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| cites | cdi_FETCH-LOGICAL-c376t-cac90a3d3f0f6ef4c5136903f280cae280d4fd999f12b7eaff44ac129e07b7f83 |
| container_end_page | 51 |
| container_issue | 1 |
| container_start_page | 45 |
| container_title | Ozone: science & engineering |
| container_volume | 27 |
| creator | Mitani, Marie M. Keller, Arturo A. Sandall, Orville C. Rinker, Robert G. |
| description | An ozone reactor was constructed using a tubular gas diffuser made of microporous stainless steel to significantly reduce gas bubble size and increase overall mass transfer area. Overall mass transfer coefficient, K
L
a [s
−1
], was correlated with gas (G) and liquid (L) flow rates using K
L
a = AL
α
G
β
, with A = 3.96 × 10
8
[s
−1
], α = 1.53, and β = 0.40, with L and G in [m
3
s
−1
]. The reactor is essentially plug flow at high G or L. This system achieves one of the highest ozone mass transfer rates observed in the literature. |
| doi_str_mv | 10.1080/01919510590908995 |
| format | article |
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L
a [s
−1
], was correlated with gas (G) and liquid (L) flow rates using K
L
a = AL
α
G
β
, with A = 3.96 × 10
8
[s
−1
], α = 1.53, and β = 0.40, with L and G in [m
3
s
−1
]. The reactor is essentially plug flow at high G or L. This system achieves one of the highest ozone mass transfer rates observed in the literature.</description><identifier>ISSN: 0191-9512</identifier><identifier>EISSN: 1547-6545</identifier><identifier>DOI: 10.1080/01919510590908995</identifier><identifier>CODEN: OZSEDS</identifier><language>eng</language><publisher>Philadelphia, PA: Taylor & Francis Group</publisher><subject>Applied sciences ; Chemical engineering ; Contactor Design ; Exact sciences and technology ; Mass Transfer Coefficient ; Microporous Diffuser ; Ozone ; Pollution ; Reactor Design ; Reactors ; Remediation ; Water Treatment ; Water treatment and pollution</subject><ispartof>Ozone: science & engineering, 2005-02, Vol.27 (1), p.45-51</ispartof><rights>Copyright Taylor & Francis Group, LLC 2005</rights><rights>2006 INIST-CNRS</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c376t-cac90a3d3f0f6ef4c5136903f280cae280d4fd999f12b7eaff44ac129e07b7f83</citedby><cites>FETCH-LOGICAL-c376t-cac90a3d3f0f6ef4c5136903f280cae280d4fd999f12b7eaff44ac129e07b7f83</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><link.rule.ids>314,776,780,27903,27904</link.rule.ids><backlink>$$Uhttp://pascal-francis.inist.fr/vibad/index.php?action=getRecordDetail&idt=16616608$$DView record in Pascal Francis$$Hfree_for_read</backlink></links><search><creatorcontrib>Mitani, Marie M.</creatorcontrib><creatorcontrib>Keller, Arturo A.</creatorcontrib><creatorcontrib>Sandall, Orville C.</creatorcontrib><creatorcontrib>Rinker, Robert G.</creatorcontrib><title>Mass Transfer of Ozone Using a Microporous Diffuser Reactor System</title><title>Ozone: science & engineering</title><description>An ozone reactor was constructed using a tubular gas diffuser made of microporous stainless steel to significantly reduce gas bubble size and increase overall mass transfer area. Overall mass transfer coefficient, K
L
a [s
−1
], was correlated with gas (G) and liquid (L) flow rates using K
L
a = AL
α
G
β
, with A = 3.96 × 10
8
[s
−1
], α = 1.53, and β = 0.40, with L and G in [m
3
s
−1
]. The reactor is essentially plug flow at high G or L. This system achieves one of the highest ozone mass transfer rates observed in the literature.</description><subject>Applied sciences</subject><subject>Chemical engineering</subject><subject>Contactor Design</subject><subject>Exact sciences and technology</subject><subject>Mass Transfer Coefficient</subject><subject>Microporous Diffuser</subject><subject>Ozone</subject><subject>Pollution</subject><subject>Reactor Design</subject><subject>Reactors</subject><subject>Remediation</subject><subject>Water Treatment</subject><subject>Water treatment and pollution</subject><issn>0191-9512</issn><issn>1547-6545</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2005</creationdate><recordtype>article</recordtype><recordid>eNqFkE1Lw0AQhhdRsFZ_gLe9eIzOZrNJFrxo_YSWgrbnMN3sSCTNlt0Urb_eLVU8CArDzGHe550Pxk4FnAso4QKEFloJUBo0lFqrPTYQKiuSXGVqnw22_SQK0kN2FMIrQJoKUQ7Y9QRD4DOPXSDruSM-_XCd5fPQdC8c-aQx3q2cd-vAbxqidYiqJ4umd54_b0Jvl8fsgLAN9uSrDtn87nY2ekjG0_vH0dU4MbLI-8Sg0YCylgSUW8qMEjLXICktwaCNuc6o1lqTSBeFRaIsQyNSbaFYFFTKIRM737hRCN5StfLNEv2mElBtn1D9ekJkznbMCoPBluKdpgk_YJ7HgK335U7XdOT8Et-cb-uqx03r_Dck_xpT_Iv_oqr-vZef_saBsg</recordid><startdate>20050201</startdate><enddate>20050201</enddate><creator>Mitani, Marie M.</creator><creator>Keller, Arturo A.</creator><creator>Sandall, Orville C.</creator><creator>Rinker, Robert G.</creator><general>Taylor & Francis Group</general><general>Taylor & Francis</general><scope>IQODW</scope><scope>AAYXX</scope><scope>CITATION</scope></search><sort><creationdate>20050201</creationdate><title>Mass Transfer of Ozone Using a Microporous Diffuser Reactor System</title><author>Mitani, Marie M. ; Keller, Arturo A. ; Sandall, Orville C. ; Rinker, Robert G.</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c376t-cac90a3d3f0f6ef4c5136903f280cae280d4fd999f12b7eaff44ac129e07b7f83</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2005</creationdate><topic>Applied sciences</topic><topic>Chemical engineering</topic><topic>Contactor Design</topic><topic>Exact sciences and technology</topic><topic>Mass Transfer Coefficient</topic><topic>Microporous Diffuser</topic><topic>Ozone</topic><topic>Pollution</topic><topic>Reactor Design</topic><topic>Reactors</topic><topic>Remediation</topic><topic>Water Treatment</topic><topic>Water treatment and pollution</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Mitani, Marie M.</creatorcontrib><creatorcontrib>Keller, Arturo A.</creatorcontrib><creatorcontrib>Sandall, Orville C.</creatorcontrib><creatorcontrib>Rinker, Robert G.</creatorcontrib><collection>Pascal-Francis</collection><collection>CrossRef</collection><jtitle>Ozone: science & engineering</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Mitani, Marie M.</au><au>Keller, Arturo A.</au><au>Sandall, Orville C.</au><au>Rinker, Robert G.</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Mass Transfer of Ozone Using a Microporous Diffuser Reactor System</atitle><jtitle>Ozone: science & engineering</jtitle><date>2005-02-01</date><risdate>2005</risdate><volume>27</volume><issue>1</issue><spage>45</spage><epage>51</epage><pages>45-51</pages><issn>0191-9512</issn><eissn>1547-6545</eissn><coden>OZSEDS</coden><abstract>An ozone reactor was constructed using a tubular gas diffuser made of microporous stainless steel to significantly reduce gas bubble size and increase overall mass transfer area. Overall mass transfer coefficient, K
L
a [s
−1
], was correlated with gas (G) and liquid (L) flow rates using K
L
a = AL
α
G
β
, with A = 3.96 × 10
8
[s
−1
], α = 1.53, and β = 0.40, with L and G in [m
3
s
−1
]. The reactor is essentially plug flow at high G or L. This system achieves one of the highest ozone mass transfer rates observed in the literature.</abstract><cop>Philadelphia, PA</cop><pub>Taylor & Francis Group</pub><doi>10.1080/01919510590908995</doi><tpages>7</tpages></addata></record> |
| fulltext | fulltext |
| identifier | ISSN: 0191-9512 |
| ispartof | Ozone: science & engineering, 2005-02, Vol.27 (1), p.45-51 |
| issn | 0191-9512 1547-6545 |
| language | eng |
| recordid | cdi_crossref_primary_10_1080_01919510590908995 |
| source | Taylor and Francis Science and Technology Collection |
| subjects | Applied sciences Chemical engineering Contactor Design Exact sciences and technology Mass Transfer Coefficient Microporous Diffuser Ozone Pollution Reactor Design Reactors Remediation Water Treatment Water treatment and pollution |
| title | Mass Transfer of Ozone Using a Microporous Diffuser Reactor System |
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