Water purification of organic inclusions by the method of combustion within an inert porous media
New technology of water purification of organic inclusions or solutes by using a filtration combustion recuperative reactor (“tube-in-tube” type) is investigated numerically. An acetone aqueous solution served as a model liquid. The model was verified on the basis of experimental temperature measure...
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Veröffentlicht in: | International journal of heat and mass transfer 2010-05, Vol.53 (11), p.2484-2490 |
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container_title | International journal of heat and mass transfer |
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creator | Dobrego, K.V. Shmelev, E.S. Koznacheev, I.A. Suvorov, A.V. |
description | New technology of water purification of organic inclusions or solutes by using a filtration combustion recuperative reactor (“tube-in-tube” type) is investigated numerically. An acetone aqueous solution served as a model liquid. The model was verified on the basis of experimental temperature measurement data.
The physical reason for the comparatively high energy consumption at the startup of the reactor has been revealed. The minimum concentration limit (MCL) for self-sustained operation as a function of the reactor length, size of a packed bed particle, and of the heat transfer coefficients was investigated. Thermal insulation has the strongest effect on MCL, which may be as low as
c
=
0.12 for the acetone aqueous solution and characteristic length of the reactor
L
=
0.5
m. Increase of the length of the reactor has a limited potential for reduction of the MCL. This is connected with the exponential saturation of the recuperated heat and simultaneous increase in the heat loss with the length of the reactor. In the case of proportional elongation of reactor, when the “dead end” area grows, not a decrease but an increase in the MCL value is observed. |
doi_str_mv | 10.1016/j.ijheatmasstransfer.2010.01.030 |
format | Article |
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The physical reason for the comparatively high energy consumption at the startup of the reactor has been revealed. The minimum concentration limit (MCL) for self-sustained operation as a function of the reactor length, size of a packed bed particle, and of the heat transfer coefficients was investigated. Thermal insulation has the strongest effect on MCL, which may be as low as
c
=
0.12 for the acetone aqueous solution and characteristic length of the reactor
L
=
0.5
m. Increase of the length of the reactor has a limited potential for reduction of the MCL. This is connected with the exponential saturation of the recuperated heat and simultaneous increase in the heat loss with the length of the reactor. In the case of proportional elongation of reactor, when the “dead end” area grows, not a decrease but an increase in the MCL value is observed.</description><identifier>ISSN: 0017-9310</identifier><identifier>EISSN: 1879-2189</identifier><identifier>DOI: 10.1016/j.ijheatmasstransfer.2010.01.030</identifier><identifier>CODEN: IJHMAK</identifier><language>eng</language><publisher>Kidlington: Elsevier Ltd</publisher><subject>Acetone ; Applied sciences ; Aqueous solutions ; Combustion ; Exact sciences and technology ; Inclusions ; Mass transfer ; Mathematical models ; Optimization ; Other wastewaters ; Pollution ; Porous media ; Reactors ; Simulation ; Wastewaters ; Water purification ; Water treatment and pollution</subject><ispartof>International journal of heat and mass transfer, 2010-05, Vol.53 (11), p.2484-2490</ispartof><rights>2010 Elsevier Ltd</rights><rights>2015 INIST-CNRS</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c404t-9c23c774af908f748a50da8bac32df3586aa41753f57c24061b301c1f5e5a313</citedby><cites>FETCH-LOGICAL-c404t-9c23c774af908f748a50da8bac32df3586aa41753f57c24061b301c1f5e5a313</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktohtml>$$Uhttps://dx.doi.org/10.1016/j.ijheatmasstransfer.2010.01.030$$EHTML$$P50$$Gelsevier$$H</linktohtml><link.rule.ids>314,777,781,3537,27905,27906,45976</link.rule.ids><backlink>$$Uhttp://pascal-francis.inist.fr/vibad/index.php?action=getRecordDetail&idt=22734243$$DView record in Pascal Francis$$Hfree_for_read</backlink></links><search><creatorcontrib>Dobrego, K.V.</creatorcontrib><creatorcontrib>Shmelev, E.S.</creatorcontrib><creatorcontrib>Koznacheev, I.A.</creatorcontrib><creatorcontrib>Suvorov, A.V.</creatorcontrib><title>Water purification of organic inclusions by the method of combustion within an inert porous media</title><title>International journal of heat and mass transfer</title><description>New technology of water purification of organic inclusions or solutes by using a filtration combustion recuperative reactor (“tube-in-tube” type) is investigated numerically. An acetone aqueous solution served as a model liquid. The model was verified on the basis of experimental temperature measurement data.
The physical reason for the comparatively high energy consumption at the startup of the reactor has been revealed. The minimum concentration limit (MCL) for self-sustained operation as a function of the reactor length, size of a packed bed particle, and of the heat transfer coefficients was investigated. Thermal insulation has the strongest effect on MCL, which may be as low as
c
=
0.12 for the acetone aqueous solution and characteristic length of the reactor
L
=
0.5
m. Increase of the length of the reactor has a limited potential for reduction of the MCL. This is connected with the exponential saturation of the recuperated heat and simultaneous increase in the heat loss with the length of the reactor. In the case of proportional elongation of reactor, when the “dead end” area grows, not a decrease but an increase in the MCL value is observed.</description><subject>Acetone</subject><subject>Applied sciences</subject><subject>Aqueous solutions</subject><subject>Combustion</subject><subject>Exact sciences and technology</subject><subject>Inclusions</subject><subject>Mass transfer</subject><subject>Mathematical models</subject><subject>Optimization</subject><subject>Other wastewaters</subject><subject>Pollution</subject><subject>Porous media</subject><subject>Reactors</subject><subject>Simulation</subject><subject>Wastewaters</subject><subject>Water purification</subject><subject>Water treatment and pollution</subject><issn>0017-9310</issn><issn>1879-2189</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2010</creationdate><recordtype>article</recordtype><recordid>eNqNkM1u3CAURlHVSJ0mfQc2VbvxBAw29q5VlF9FyiZSlujONXQY2WbKxa3y9mU6UTbZZIWA830XDmPfpVhLIdvz3Trstg7yBEQ5wUzepXUtyrWQa6HEB7aSnemrWnb9R7YSQpqqV1J8Yp-Jdoet0O2KwRNkl_h-ScEHhBzizKPnMf2COSAPM44LlUPim2eet45PLm_jcGAwTpuF_if-hrwNM4e5BFzKfB9TXKiwQ4AzduJhJPflZT1lj1eXjxc31f3D9e3Fz_sKtdC56rFWaIwG34vOG91BIwboNoCqHrxquhZAS9Mo3xistWjlRgmJ0jeuASXVKft2rN2n-HtxlO0UCN04wuzKW2xJGtUp1Rbyx5HEFImS83afwgTp2UphD27tzr51aw9urZC2uC0VX1-GASGMvjAY6LWnro3StVaFuztyrnz8TygthMHNWLwkh9kOMbx_6D9rV518</recordid><startdate>20100501</startdate><enddate>20100501</enddate><creator>Dobrego, K.V.</creator><creator>Shmelev, E.S.</creator><creator>Koznacheev, I.A.</creator><creator>Suvorov, A.V.</creator><general>Elsevier Ltd</general><general>Elsevier</general><scope>IQODW</scope><scope>AAYXX</scope><scope>CITATION</scope><scope>7TB</scope><scope>8FD</scope><scope>FR3</scope><scope>H8D</scope><scope>KR7</scope><scope>L7M</scope></search><sort><creationdate>20100501</creationdate><title>Water purification of organic inclusions by the method of combustion within an inert porous media</title><author>Dobrego, K.V. ; Shmelev, E.S. ; Koznacheev, I.A. ; Suvorov, A.V.</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c404t-9c23c774af908f748a50da8bac32df3586aa41753f57c24061b301c1f5e5a313</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2010</creationdate><topic>Acetone</topic><topic>Applied sciences</topic><topic>Aqueous solutions</topic><topic>Combustion</topic><topic>Exact sciences and technology</topic><topic>Inclusions</topic><topic>Mass transfer</topic><topic>Mathematical models</topic><topic>Optimization</topic><topic>Other wastewaters</topic><topic>Pollution</topic><topic>Porous media</topic><topic>Reactors</topic><topic>Simulation</topic><topic>Wastewaters</topic><topic>Water purification</topic><topic>Water treatment and pollution</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Dobrego, K.V.</creatorcontrib><creatorcontrib>Shmelev, E.S.</creatorcontrib><creatorcontrib>Koznacheev, I.A.</creatorcontrib><creatorcontrib>Suvorov, A.V.</creatorcontrib><collection>Pascal-Francis</collection><collection>CrossRef</collection><collection>Mechanical & Transportation Engineering Abstracts</collection><collection>Technology Research Database</collection><collection>Engineering Research Database</collection><collection>Aerospace Database</collection><collection>Civil Engineering Abstracts</collection><collection>Advanced Technologies Database with Aerospace</collection><jtitle>International journal of heat and mass transfer</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Dobrego, K.V.</au><au>Shmelev, E.S.</au><au>Koznacheev, I.A.</au><au>Suvorov, A.V.</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Water purification of organic inclusions by the method of combustion within an inert porous media</atitle><jtitle>International journal of heat and mass transfer</jtitle><date>2010-05-01</date><risdate>2010</risdate><volume>53</volume><issue>11</issue><spage>2484</spage><epage>2490</epage><pages>2484-2490</pages><issn>0017-9310</issn><eissn>1879-2189</eissn><coden>IJHMAK</coden><abstract>New technology of water purification of organic inclusions or solutes by using a filtration combustion recuperative reactor (“tube-in-tube” type) is investigated numerically. An acetone aqueous solution served as a model liquid. The model was verified on the basis of experimental temperature measurement data.
The physical reason for the comparatively high energy consumption at the startup of the reactor has been revealed. The minimum concentration limit (MCL) for self-sustained operation as a function of the reactor length, size of a packed bed particle, and of the heat transfer coefficients was investigated. Thermal insulation has the strongest effect on MCL, which may be as low as
c
=
0.12 for the acetone aqueous solution and characteristic length of the reactor
L
=
0.5
m. Increase of the length of the reactor has a limited potential for reduction of the MCL. This is connected with the exponential saturation of the recuperated heat and simultaneous increase in the heat loss with the length of the reactor. In the case of proportional elongation of reactor, when the “dead end” area grows, not a decrease but an increase in the MCL value is observed.</abstract><cop>Kidlington</cop><pub>Elsevier Ltd</pub><doi>10.1016/j.ijheatmasstransfer.2010.01.030</doi><tpages>7</tpages></addata></record> |
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subjects | Acetone Applied sciences Aqueous solutions Combustion Exact sciences and technology Inclusions Mass transfer Mathematical models Optimization Other wastewaters Pollution Porous media Reactors Simulation Wastewaters Water purification Water treatment and pollution |
title | Water purification of organic inclusions by the method of combustion within an inert porous media |
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