Theoretical and experimental study on hydrodynamic characteristics of fluidization in air–sand conical beds
This work was aimed at modeling hydrodynamic characteristics of fluidization in conical beds using quartz sand as the inert bed material and air as the fluidizing agent. The minimum fluidization velocity, u mf , and the minimum velocity of full fluidization, u mff , were determined by Peng and Fan...
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description | This work was aimed at modeling hydrodynamic characteristics of fluidization in conical beds using quartz sand as the inert bed material and air as the fluidizing agent. The minimum fluidization velocity,
u
mf
, and the minimum velocity of full fluidization,
u
mff
, were determined by Peng and Fan's models modified for conical fluidized bed. Meanwhile, the pressure drop across a bed,
Δ
p
(including
Δ
p
max
and
Δ
p
mff
corresponding to
u
mf
and
u
mff
, respectively), was predicted by using modified Ergun's equations for variable superficial air velocity at an air distributor,
u
0
. The predicted results were validated by experimental data for some operating conditions. Effects of the sand particle size, cone angle and static bed height on the fluidization pattern and hydrodynamic characteristics are discussed. With the proposed models, the
Δ
p
–
u
0
diagram were obtained with rather high accuracy for the conical air–sand beds of 30–
45
∘
cone angles and 20–30
cm static bed heights, when using 300–
1180
μ
m
sand particles. For the predicted
u
mf
and
u
mff
, the relative computational errors were found to be within 20% for wide ranges of operating variables, whereas
Δ
p
max
and
Δ
p
mff
could be predicted with lower (10–15%) relative errors. With higher cone angles and/or bed heights, the computational accuracy was found to deteriorate. |
doi_str_mv | 10.1016/j.ces.2007.11.033 |
format | Article |
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u
mf
, and the minimum velocity of full fluidization,
u
mff
, were determined by Peng and Fan's models modified for conical fluidized bed. Meanwhile, the pressure drop across a bed,
Δ
p
(including
Δ
p
max
and
Δ
p
mff
corresponding to
u
mf
and
u
mff
, respectively), was predicted by using modified Ergun's equations for variable superficial air velocity at an air distributor,
u
0
. The predicted results were validated by experimental data for some operating conditions. Effects of the sand particle size, cone angle and static bed height on the fluidization pattern and hydrodynamic characteristics are discussed. With the proposed models, the
Δ
p
–
u
0
diagram were obtained with rather high accuracy for the conical air–sand beds of 30–
45
∘
cone angles and 20–30
cm static bed heights, when using 300–
1180
μ
m
sand particles. For the predicted
u
mf
and
u
mff
, the relative computational errors were found to be within 20% for wide ranges of operating variables, whereas
Δ
p
max
and
Δ
p
mff
could be predicted with lower (10–15%) relative errors. With higher cone angles and/or bed heights, the computational accuracy was found to deteriorate.</description><identifier>ISSN: 0009-2509</identifier><identifier>EISSN: 1873-4405</identifier><identifier>DOI: 10.1016/j.ces.2007.11.033</identifier><identifier>CODEN: CESCAC</identifier><language>eng</language><publisher>Oxford: Elsevier Ltd</publisher><subject>Applied sciences ; Chemical engineering ; Cone angle ; Exact sciences and technology ; Fluidization ; Hydrodynamics of contact apparatus ; Particle size ; Static bed height ; The [formula omitted]– [formula omitted] diagram</subject><ispartof>Chemical engineering science, 2008-03, Vol.63 (6), p.1471-1479</ispartof><rights>2007 Elsevier Ltd</rights><rights>2008 INIST-CNRS</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c426t-832ac7c48a0c031ccd073c3c754772bebdd39762acc7087fb2a97c2d194d4a8d3</citedby><cites>FETCH-LOGICAL-c426t-832ac7c48a0c031ccd073c3c754772bebdd39762acc7087fb2a97c2d194d4a8d3</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktohtml>$$Uhttps://www.sciencedirect.com/science/article/pii/S000925090700886X$$EHTML$$P50$$Gelsevier$$H</linktohtml><link.rule.ids>314,776,780,3537,27901,27902,65306</link.rule.ids><backlink>$$Uhttp://pascal-francis.inist.fr/vibad/index.php?action=getRecordDetail&idt=20126256$$DView record in Pascal Francis$$Hfree_for_read</backlink></links><search><creatorcontrib>Kaewklum, Rachadaporn</creatorcontrib><creatorcontrib>Kuprianov, Vladimir I.</creatorcontrib><title>Theoretical and experimental study on hydrodynamic characteristics of fluidization in air–sand conical beds</title><title>Chemical engineering science</title><description>This work was aimed at modeling hydrodynamic characteristics of fluidization in conical beds using quartz sand as the inert bed material and air as the fluidizing agent. The minimum fluidization velocity,
u
mf
, and the minimum velocity of full fluidization,
u
mff
, were determined by Peng and Fan's models modified for conical fluidized bed. Meanwhile, the pressure drop across a bed,
Δ
p
(including
Δ
p
max
and
Δ
p
mff
corresponding to
u
mf
and
u
mff
, respectively), was predicted by using modified Ergun's equations for variable superficial air velocity at an air distributor,
u
0
. The predicted results were validated by experimental data for some operating conditions. Effects of the sand particle size, cone angle and static bed height on the fluidization pattern and hydrodynamic characteristics are discussed. With the proposed models, the
Δ
p
–
u
0
diagram were obtained with rather high accuracy for the conical air–sand beds of 30–
45
∘
cone angles and 20–30
cm static bed heights, when using 300–
1180
μ
m
sand particles. For the predicted
u
mf
and
u
mff
, the relative computational errors were found to be within 20% for wide ranges of operating variables, whereas
Δ
p
max
and
Δ
p
mff
could be predicted with lower (10–15%) relative errors. With higher cone angles and/or bed heights, the computational accuracy was found to deteriorate.</description><subject>Applied sciences</subject><subject>Chemical engineering</subject><subject>Cone angle</subject><subject>Exact sciences and technology</subject><subject>Fluidization</subject><subject>Hydrodynamics of contact apparatus</subject><subject>Particle size</subject><subject>Static bed height</subject><subject>The [formula omitted]– [formula omitted] diagram</subject><issn>0009-2509</issn><issn>1873-4405</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2008</creationdate><recordtype>article</recordtype><recordid>eNqFkU1u2zAQhYmiAeomOUB22rQ7KcMfiRKyCoKkLRCgm3RN0MMRTEMmXVIu4qx6h96wJwldB1mmq8EMvvcGeI-xCw4NB95drhuk3AgA3XDegJTv2IL3WtZKQfueLQBgqEULwwf2Med1WbXmsGCbhxXFRLNHO1U2uIoet5T8hsJcDnneuX0VQ7XauxTdPtiNxwpXNlmcC5aLLldxrMZp551_srMvsA-V9env7z_5YIgx_DNfkstn7GS0U6bzl3nKftzdPtx8re-_f_l2c31foxLdXPdSWNSoegsIkiM60BIl6lZpLZa0dE4OuisQauj1uBR20CgcH5RTtnfylH0--m5T_LmjPJuNz0jTZAPFXTZS8K6Xuv0vyBUIqTpeQH4EMcWcE41mW1KyaW84mEMDZm1KA-bQgOHclAaK5tOLuc0lgTHZgD6_CgVw0Ym2K9zVkaMSyS9PyWT0FJCcT4SzcdG_8eUZ-BmeaQ</recordid><startdate>20080301</startdate><enddate>20080301</enddate><creator>Kaewklum, Rachadaporn</creator><creator>Kuprianov, Vladimir I.</creator><general>Elsevier Ltd</general><general>Elsevier</general><scope>IQODW</scope><scope>AAYXX</scope><scope>CITATION</scope><scope>7ST</scope><scope>C1K</scope><scope>SOI</scope><scope>7U5</scope><scope>8FD</scope><scope>F28</scope><scope>FR3</scope><scope>L7M</scope></search><sort><creationdate>20080301</creationdate><title>Theoretical and experimental study on hydrodynamic characteristics of fluidization in air–sand conical beds</title><author>Kaewklum, Rachadaporn ; Kuprianov, Vladimir I.</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c426t-832ac7c48a0c031ccd073c3c754772bebdd39762acc7087fb2a97c2d194d4a8d3</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2008</creationdate><topic>Applied sciences</topic><topic>Chemical engineering</topic><topic>Cone angle</topic><topic>Exact sciences and technology</topic><topic>Fluidization</topic><topic>Hydrodynamics of contact apparatus</topic><topic>Particle size</topic><topic>Static bed height</topic><topic>The [formula omitted]– [formula omitted] diagram</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Kaewklum, Rachadaporn</creatorcontrib><creatorcontrib>Kuprianov, Vladimir I.</creatorcontrib><collection>Pascal-Francis</collection><collection>CrossRef</collection><collection>Environment Abstracts</collection><collection>Environmental Sciences and Pollution Management</collection><collection>Environment Abstracts</collection><collection>Solid State and Superconductivity Abstracts</collection><collection>Technology Research Database</collection><collection>ANTE: Abstracts in New Technology & Engineering</collection><collection>Engineering Research Database</collection><collection>Advanced Technologies Database with Aerospace</collection><jtitle>Chemical engineering science</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Kaewklum, Rachadaporn</au><au>Kuprianov, Vladimir I.</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Theoretical and experimental study on hydrodynamic characteristics of fluidization in air–sand conical beds</atitle><jtitle>Chemical engineering science</jtitle><date>2008-03-01</date><risdate>2008</risdate><volume>63</volume><issue>6</issue><spage>1471</spage><epage>1479</epage><pages>1471-1479</pages><issn>0009-2509</issn><eissn>1873-4405</eissn><coden>CESCAC</coden><abstract>This work was aimed at modeling hydrodynamic characteristics of fluidization in conical beds using quartz sand as the inert bed material and air as the fluidizing agent. The minimum fluidization velocity,
u
mf
, and the minimum velocity of full fluidization,
u
mff
, were determined by Peng and Fan's models modified for conical fluidized bed. Meanwhile, the pressure drop across a bed,
Δ
p
(including
Δ
p
max
and
Δ
p
mff
corresponding to
u
mf
and
u
mff
, respectively), was predicted by using modified Ergun's equations for variable superficial air velocity at an air distributor,
u
0
. The predicted results were validated by experimental data for some operating conditions. Effects of the sand particle size, cone angle and static bed height on the fluidization pattern and hydrodynamic characteristics are discussed. With the proposed models, the
Δ
p
–
u
0
diagram were obtained with rather high accuracy for the conical air–sand beds of 30–
45
∘
cone angles and 20–30
cm static bed heights, when using 300–
1180
μ
m
sand particles. For the predicted
u
mf
and
u
mff
, the relative computational errors were found to be within 20% for wide ranges of operating variables, whereas
Δ
p
max
and
Δ
p
mff
could be predicted with lower (10–15%) relative errors. With higher cone angles and/or bed heights, the computational accuracy was found to deteriorate.</abstract><cop>Oxford</cop><pub>Elsevier Ltd</pub><doi>10.1016/j.ces.2007.11.033</doi><tpages>9</tpages></addata></record> |
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source | Elsevier ScienceDirect Journals |
subjects | Applied sciences Chemical engineering Cone angle Exact sciences and technology Fluidization Hydrodynamics of contact apparatus Particle size Static bed height The [formula omitted]– [formula omitted] diagram |
title | Theoretical and experimental study on hydrodynamic characteristics of fluidization in air–sand conical beds |
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