Experimental and computational analysis of immiscible liquid–liquid dispersions in stirred vessels
This work is aimed at investigating the fluid dynamic characteristics of a stirred tank of standard geometry for the dispersion of organics in water. Two different aspects have been considered. Firstly, the dispersion conditions at different impeller speeds and the flow features of both the continuo...
Saved in:
Published in | Chemical engineering research & design Vol. 87; no. 4; pp. 507 - 514 |
---|---|
Main Authors | , , , , |
Format | Journal Article |
Language | English |
Published |
Elsevier B.V
01.04.2009
|
Subjects | |
Online Access | Get full text |
ISSN | 0263-8762 1744-3563 |
DOI | 10.1016/j.cherd.2008.12.007 |
Cover
Abstract | This work is aimed at investigating the fluid dynamic characteristics of a stirred tank of standard geometry for the dispersion of organics in water. Two different aspects have been considered. Firstly, the dispersion conditions at different impeller speeds and the flow features of both the continuous and the dispersed phases have been examined. The two-phase turbulent flow fields of a dilute liquid–liquid system as measured by means of Particle Image Velocimetry (PIV) technique are presented. The mean velocity and the turbulent characteristics of water and oil droplets flow are compared with those of the corresponding single-phase flow and discussed; the influence of the dispersed phase on the continuous one is assessed. For the second aspect, starting from moderately agitated conditions, corresponding to completely separated phases, the different dispersion regimes taking place in the tank at increasing impeller speeds have been identified. The capability of a CFD approach based on the solution of Reynolds averaged Navier-Stokes equations and on an Eulerian–Eulerian description of the two phases in catching the dispersion features has been critically assessed. |
---|---|
AbstractList | This work is aimed at investigating the fluid dynamic characteristics of a stirred tank of standard geometry for the dispersion of organics in water. Two different aspects have been considered. Firstly, the dispersion conditions at different impeller speeds and the flow features of both the continuous and the dispersed phases have been examined. The two-phase turbulent flow fields of a dilute liquid-liquid system as measured by means of Particle Image Velocimetry (PIV) technique are presented. The mean velocity and the turbulent characteristics of water and oil droplets flow are compared with those of the corresponding single-phase flow and discussed; the influence of the dispersed phase on the continuous one is assessed. For the second aspect, starting from moderately agitated conditions, corresponding to completely separated phases, the different dispersion regimes taking place in the tank at increasing impeller speeds have been identified. The capability of a CFD approach based on the solution of Reynolds averaged Navier-Stokes equations and on an Eulerian-Eulerian description of the two phases in catching the dispersion features has been critically assessed. |
Author | Laurenzi, F. Coroneo, M. Paglianti, A. Magelli, F. Montante, G. |
Author_xml | – sequence: 1 givenname: F. surname: Laurenzi fullname: Laurenzi, F. – sequence: 2 givenname: M. surname: Coroneo fullname: Coroneo, M. – sequence: 3 givenname: G. surname: Montante fullname: Montante, G. – sequence: 4 givenname: A. surname: Paglianti fullname: Paglianti, A. email: alessandro.paglianti@mail.ing.unibo.it – sequence: 5 givenname: F. surname: Magelli fullname: Magelli, F. |
BookMark | eNqFkL1OwzAQgC0EEqXwBCye2BLsOIndgQEh_iQkFpgt1z4LV27S-lIEG-_AG_IkuA0TA0x3urvvdPcdkf2u74CQU85Kznh7vijtCyRXVoypklclY3KPTLis60I0rdgnE1a1olCyrQ7JEeKCMZa7akLc9dsKUlhCN5hITeeo7ZerzWCG0He7ionvGJD2noblMqAN8wg0hvUmuK-PzzGhLmBeg5lBGjqKQ0gJHH0FRIh4TA68iQgnP3FKnm-un67uiofH2_ury4fCClEPhZwrCbYVM2mEk0w1tWPCeq6EVVy20ivJK4BmDtKzxrLGKDuz1je1AS99I6bkbNy7Sv16Azjo7cEQo-mg36AWYlZzJmQenI2DNvWICby2YXx5SCZEzZneetULvfOqt141r3T2mlnxi11lfya9_0NdjFTWAa8Bks4mobPgQgI7aNeHP_lvUu6ZCA |
CitedBy_id | crossref_primary_10_1016_j_ces_2020_115898 crossref_primary_10_1002_cjce_23361 crossref_primary_10_1021_ie102270p crossref_primary_10_1007_s00231_016_1876_4 crossref_primary_10_1080_01496395_2020_1715436 crossref_primary_10_1080_00986445_2014_923994 crossref_primary_10_1002_ceat_201100220 crossref_primary_10_1021_la304919p crossref_primary_10_1016_j_cep_2014_10_007 crossref_primary_10_1007_s11356_017_9827_2 crossref_primary_10_1016_j_ces_2012_03_035 crossref_primary_10_1016_j_molliq_2022_119823 crossref_primary_10_1021_acs_iecr_9b05060 crossref_primary_10_1016_j_cherd_2017_02_018 crossref_primary_10_1021_acs_iecr_7b01327 crossref_primary_10_1088_1742_6596_1064_1_012076 crossref_primary_10_16984_saufenbilder_992396 crossref_primary_10_1002_cjce_20465 crossref_primary_10_1016_j_measurement_2016_04_044 crossref_primary_10_1080_00986445_2012_717313 crossref_primary_10_1080_00986445_2021_1978074 crossref_primary_10_4028_www_scientific_net_AMM_483_238 crossref_primary_10_1016_j_cherd_2013_07_003 crossref_primary_10_1016_j_jtice_2015_10_007 crossref_primary_10_1021_acs_iecr_7b03756 crossref_primary_10_1016_j_ces_2014_12_033 crossref_primary_10_1007_s11837_022_05371_4 crossref_primary_10_1016_j_ijmultiphaseflow_2020_103547 crossref_primary_10_1016_j_cej_2016_02_064 crossref_primary_10_1115_1_4062520 crossref_primary_10_1016_j_ces_2013_06_026 crossref_primary_10_1016_j_bej_2020_107522 crossref_primary_10_1016_j_cej_2016_10_102 crossref_primary_10_1016_j_cherd_2012_01_009 crossref_primary_10_1016_j_ijheatfluidflow_2019_01_014 crossref_primary_10_1021_acs_iecr_3c00826 crossref_primary_10_1016_j_applthermaleng_2017_07_106 crossref_primary_10_1016_j_ces_2022_118226 crossref_primary_10_1002_aic_16983 |
Cites_doi | 10.1080/00986440108912898 10.1205/cherd06187 10.1205/cherd06141 10.1021/ie00005a022 10.1002/ceat.200401981 10.1016/S0009-2509(02)00067-2 10.1002/cjce.5450760316 10.1016/S0009-2509(01)00027-6 10.1016/S0009-2509(97)00437-5 10.1016/0301-9322(89)90076-1 10.1016/j.ces.2008.01.005 10.1016/S0009-2509(99)00156-6 10.1007/s00348-006-0211-0 10.1016/S0009-2509(98)00114-6 10.1115/1.2909497 10.1205/cherd06161 10.1080/10618560500081795 10.1016/S0009-2509(97)00438-7 10.1205/cherd.04167 10.1252/jcej.26.738 10.1002/aic.690440104 10.1016/j.ijmultiphaseflow.2004.11.009 10.1002/aic.690320418 |
ContentType | Journal Article |
Copyright | 2009 The Institution of Chemical Engineers |
Copyright_xml | – notice: 2009 The Institution of Chemical Engineers |
DBID | AAYXX CITATION 8FD F28 FR3 |
DOI | 10.1016/j.cherd.2008.12.007 |
DatabaseName | CrossRef Technology Research Database ANTE: Abstracts in New Technology & Engineering Engineering Research Database |
DatabaseTitle | CrossRef Technology Research Database ANTE: Abstracts in New Technology & Engineering Engineering Research Database |
DatabaseTitleList | Technology Research Database |
DeliveryMethod | fulltext_linktorsrc |
Discipline | Engineering |
EISSN | 1744-3563 |
EndPage | 514 |
ExternalDocumentID | 10_1016_j_cherd_2008_12_007 S0263876208003560 |
GroupedDBID | --K --M -QF -~X .~1 0R~ 1B1 1~. 1~5 29B 3EH 4.4 457 4G. 5GY 5VS 6J9 7-5 71M 8P~ AACTN AAEDT AAEDW AAHCO AAIAV AAIKC AAIKJ AAKOC AALRI AAMNW AAOAW AAQFI AAQXK AARJD AAXUO ABDBF ABFNM ABFRF ABJNI ABMAC ABNUV ABXDB ABYKQ ACDAQ ACGFO ACIWK ACRLP ADBBV ADEWK ADEZE ADMUD AEBSH AEFWE AEKER AENEX AFFNX AFKWA AFTJW AGHFR AGUBO AGYEJ AHIDL AHPOS AI. AIAGR AIEXJ AIKHN AITUG AJBFU AJOXV AKURH ALMA_UNASSIGNED_HOLDINGS AMFUW AMRAJ ASPBG AVWKF AXJTR AZFZN BELTK BKOJK BLXMC CAG COF CS3 DU5 EBS EFJIC EFLBG EJD ENUVR EO9 EP2 EP3 ESX FDB FEDTE FGOYB FIRID FNPLU FYGXN GBLVA HVGLF HZ~ I-F IHE J1W JARJE KOM M41 ML- MO0 N9A O-L O9- OAUVE OZT P-8 P-9 P2P PC. Q38 R2- RIG ROL RPZ SDF SDG SES SJN SPC SPCBC SSG SSR SSZ T5K T9H TUS UNMZH VH1 XFK ~02 ~8M ~G- AATTM AAXKI AAYWO AAYXX ABWVN ACRPL ACUHS ACVFH ADCNI ADMLS ADNMO AEIPS AEUPX AFJKZ AFPUW AFXIZ AGCQF AGQPQ AGRNS AIGII AIIUN AKBMS AKRWK AKYEP ANKPU APXCP BNPGV CITATION SSH 8FD EFKBS F28 FR3 |
ID | FETCH-LOGICAL-c334t-7b87ec6397a3d70854d03cf183c81767f8712ee5be7f05c05a8c9ccf54aef7f53 |
IEDL.DBID | AIKHN |
ISSN | 0263-8762 |
IngestDate | Thu Sep 04 22:55:12 EDT 2025 Thu Apr 24 23:02:28 EDT 2025 Tue Jul 01 00:52:42 EDT 2025 Fri Feb 23 02:23:50 EST 2024 |
IsPeerReviewed | true |
IsScholarly | true |
Issue | 4 |
Keywords | CFD RANS equations Mixing PIV Liquid–liquid |
Language | English |
License | https://www.elsevier.com/tdm/userlicense/1.0 |
LinkModel | DirectLink |
MergedId | FETCHMERGED-LOGICAL-c334t-7b87ec6397a3d70854d03cf183c81767f8712ee5be7f05c05a8c9ccf54aef7f53 |
Notes | ObjectType-Article-2 SourceType-Scholarly Journals-1 ObjectType-Feature-1 content type line 23 |
PQID | 33941037 |
PQPubID | 23500 |
PageCount | 8 |
ParticipantIDs | proquest_miscellaneous_33941037 crossref_citationtrail_10_1016_j_cherd_2008_12_007 crossref_primary_10_1016_j_cherd_2008_12_007 elsevier_sciencedirect_doi_10_1016_j_cherd_2008_12_007 |
ProviderPackageCode | CITATION AAYXX |
PublicationCentury | 2000 |
PublicationDate | 2009-04-01 |
PublicationDateYYYYMMDD | 2009-04-01 |
PublicationDate_xml | – month: 04 year: 2009 text: 2009-04-01 day: 01 |
PublicationDecade | 2000 |
PublicationTitle | Chemical engineering research & design |
PublicationYear | 2009 |
Publisher | Elsevier B.V |
Publisher_xml | – name: Elsevier B.V |
References | Armenante, Huang (bib2) 1992; 31 Pacek, Chamsart, Nienow, Bakker (bib19) 1999; 54 Gore, Crowe (bib11) 1991; 115 Zhou, Kresta (bib25) 1998; 53 Leng, Calabrese (bib14) 2004 Calabrese, Wang, Bryner (bib7) 1986; 32 Hadinoto, Jones, Yurteri, Curtis (bib12) 2005; 31 Brucato, Grisafi, Montante (bib6) 1998; 53 Maaß, Gäbler, Zaccone, Paschedag, Kraume (bib15) 2007; 85 Montante, Magelli (bib16) 2005; 19 Bałdyga, Podgórska (bib4) 1998; 76 Alopaeus, Koskinen, Keskinen, Majander (bib1) 2002; 57 Bałdyga, Bourne, Pacek, Amanullah, Nienow (bib5) 2001; 56 Bałdyga, Bourne (bib3) 1993; 26 Lee, Yianneskis (bib13) 1998; 44 Gore, Crowe (bib10) 1989; 15 van den Akker (bib23) 2006; vol. 31 Zhou, Kresta (bib24) 1998; 53 Montante, Horn, Paglianti (bib18) 2008; 63 Svensson, Rasmuson (bib21) 2004; 27 Giapos, Pachatouridis, Stamatoudis (bib9) 2005; 83 Montante, Paglianti, Magelli (bib17) 2007; 85 Pinelli, Nocentini, Magelli (bib20) 2001; 188 Derksen, van den Akker (bib8) 2007; 85 Svensson, Rasmuson (bib22) 2006; 41 Brucato (10.1016/j.cherd.2008.12.007_bib6) 1998; 53 Maaß (10.1016/j.cherd.2008.12.007_bib15) 2007; 85 Zhou (10.1016/j.cherd.2008.12.007_bib24) 1998; 53 Svensson (10.1016/j.cherd.2008.12.007_bib21) 2004; 27 Montante (10.1016/j.cherd.2008.12.007_bib16) 2005; 19 Pinelli (10.1016/j.cherd.2008.12.007_bib20) 2001; 188 Alopaeus (10.1016/j.cherd.2008.12.007_bib1) 2002; 57 Hadinoto (10.1016/j.cherd.2008.12.007_bib12) 2005; 31 Calabrese (10.1016/j.cherd.2008.12.007_bib7) 1986; 32 Gore (10.1016/j.cherd.2008.12.007_bib10) 1989; 15 Pacek (10.1016/j.cherd.2008.12.007_bib19) 1999; 54 Bałdyga (10.1016/j.cherd.2008.12.007_bib4) 1998; 76 Derksen (10.1016/j.cherd.2008.12.007_bib8) 2007; 85 Gore (10.1016/j.cherd.2008.12.007_bib11) 1991; 115 Bałdyga (10.1016/j.cherd.2008.12.007_bib3) 1993; 26 Lee (10.1016/j.cherd.2008.12.007_bib13) 1998; 44 van den Akker (10.1016/j.cherd.2008.12.007_bib23) 2006; vol. 31 Bałdyga (10.1016/j.cherd.2008.12.007_bib5) 2001; 56 Montante (10.1016/j.cherd.2008.12.007_bib18) 2008; 63 Zhou (10.1016/j.cherd.2008.12.007_bib25) 1998; 53 Montante (10.1016/j.cherd.2008.12.007_bib17) 2007; 85 Armenante (10.1016/j.cherd.2008.12.007_bib2) 1992; 31 Giapos (10.1016/j.cherd.2008.12.007_bib9) 2005; 83 Svensson (10.1016/j.cherd.2008.12.007_bib22) 2006; 41 Leng (10.1016/j.cherd.2008.12.007_bib14) 2004 |
References_xml | – volume: 54 start-page: 4211 year: 1999 end-page: 4222 ident: bib19 article-title: The influence of impeller type on mean drop size and drop size distribution in an agitated vessel publication-title: Chem. Eng. Sci. – volume: 31 start-page: 1398 year: 1992 end-page: 1406 ident: bib2 article-title: Experimental determination of the minimum agitation speed for complete liquid–liquid dispersion in mechanically agitated vessels publication-title: Ind. Eng. Chem. Res. – volume: 44 start-page: 13 year: 1998 end-page: 24 ident: bib13 article-title: Turbulence properties of the impeller stream of a Rushton turbine publication-title: AIChE J. – volume: 15 start-page: 279 year: 1989 end-page: 285 ident: bib10 article-title: Effect of particle size on modulating turbulent intensity publication-title: Int. J. Multiphase Flow – volume: 57 start-page: 1815 year: 2002 end-page: 1825 ident: bib1 article-title: Simulation of the population balances for liquid–liquid systems in a nonideal stirred tank. Part 2–parameter fitting and the use of the multiblock model for dense dispersions publication-title: Chem. Eng. Sci. – volume: vol. 31 start-page: 151 year: 2006 end-page: 229 ident: bib23 article-title: The details of turbulent mixing process and their simulation publication-title: Advances in Chemical Engineering – volume: 56 start-page: 3377 year: 2001 end-page: 3385 ident: bib5 article-title: Effects of agitation and scale-up on drop size in turbulent dispersions: allowance for intermittency publication-title: Chem. Eng. Sci. – start-page: 639 year: 2004 end-page: 753 ident: bib14 article-title: Immiscible liquid–liquid systems publication-title: Handbook of Industrial Mixing: Science and Practice – volume: 115 start-page: 304 year: 1991 end-page: 307 ident: bib11 article-title: Modulation of turbulence by a dispersed phase publication-title: J. Fluids Eng. – volume: 32 start-page: 677 year: 1986 end-page: 680 ident: bib7 article-title: Drop breakup in turbulent stirred-tank contactors. Part III: Correlations for mean size distribution publication-title: AIChE J. – volume: 19 start-page: 253 year: 2005 end-page: 262 ident: bib16 article-title: Modelling of solids distribution in stirred tanks: analysis of simulation strategies and comparison with experimental data publication-title: Int. J. Comp. Fluid Dyn. – volume: 188 start-page: 91 year: 2001 end-page: 107 ident: bib20 article-title: Solids distribution in stirred slurry reactors: influence of some mixer configurations and limits to the applicability of a simple model for predictions publication-title: Chem. Eng. Comm. – volume: 26 start-page: 738 year: 1993 end-page: 741 ident: bib3 article-title: Drop breakup and intermittent turbulence publication-title: J. Chem. Eng. Japan – volume: 76 start-page: 456 year: 1998 end-page: 470 ident: bib4 article-title: Drop break-up in intermittent turbulence: maximum stable and transient sizes of drops publication-title: Can. J. Chem. Eng. – volume: 85 start-page: 647 year: 2007 end-page: 653 ident: bib17 article-title: Experimental analysis and computational modelling of gas–liquid stirred vessels publication-title: Chem. Eng. Res. Des. – volume: 85 start-page: 697 year: 2007 end-page: 702 ident: bib8 article-title: Multi-scale simulations of stirred liquid–liquid dispersions publication-title: Chem. Eng. Res. Des. – volume: 41 start-page: 917 year: 2006 end-page: 931 ident: bib22 article-title: PIV measurements in a liquid–liquid system at volume percentages up to 10% dispersed phase publication-title: Exp. Fluids – volume: 53 start-page: 3295 year: 1998 end-page: 3314 ident: bib6 article-title: Particle drag coefficients in turbulent fluids publication-title: Chem. Eng. Sci. – volume: 31 start-page: 416 year: 2005 end-page: 434 ident: bib12 article-title: Reynolds number dependence of gas-phase turbulence in gas–particle flows publication-title: Int. J. Multiphase Flow – volume: 83 start-page: 1425 year: 2005 end-page: 1430 ident: bib9 article-title: Effect of the number of impeller blades on the drop sizes in agitated dispersions publication-title: Chem. Eng. Res. Des. – volume: 85 start-page: 703 year: 2007 end-page: 709 ident: bib15 article-title: Experimental investigations and modelling of breakage phenomena in stirred liquid–liquid systems publication-title: Chem. Eng. Res. Des. – volume: 53 start-page: 2099 year: 1998 end-page: 2113 ident: bib24 article-title: Evolution of drop size distribution in liquid–liquid dispersions for various impellers publication-title: Chem. Eng. Sci. – volume: 63 start-page: 2107 year: 2008 end-page: 2118 ident: bib18 article-title: Gas–liquid flow and bubble size distribution in stirred tanks publication-title: Chem. Eng. Sci. – volume: 27 start-page: 335 year: 2004 end-page: 339 ident: bib21 article-title: LDA-measurements in a stirred tank with a liquid–liquid system at high volume percentage dispersed phase publication-title: Chem. Eng. Technol. – volume: 53 start-page: 2063 year: 1998 end-page: 2079 ident: bib25 article-title: Correlation of mean drop size and minimum drop size with the turbulence energy dissipation and the flow in an agitated tank publication-title: Chem. Eng. Sci. – volume: 188 start-page: 91 year: 2001 ident: 10.1016/j.cherd.2008.12.007_bib20 article-title: Solids distribution in stirred slurry reactors: influence of some mixer configurations and limits to the applicability of a simple model for predictions publication-title: Chem. Eng. Comm. doi: 10.1080/00986440108912898 – volume: 85 start-page: 703 year: 2007 ident: 10.1016/j.cherd.2008.12.007_bib15 article-title: Experimental investigations and modelling of breakage phenomena in stirred liquid–liquid systems publication-title: Chem. Eng. Res. Des. doi: 10.1205/cherd06187 – volume: 85 start-page: 647 year: 2007 ident: 10.1016/j.cherd.2008.12.007_bib17 article-title: Experimental analysis and computational modelling of gas–liquid stirred vessels publication-title: Chem. Eng. Res. Des. doi: 10.1205/cherd06141 – volume: 31 start-page: 1398 year: 1992 ident: 10.1016/j.cherd.2008.12.007_bib2 article-title: Experimental determination of the minimum agitation speed for complete liquid–liquid dispersion in mechanically agitated vessels publication-title: Ind. Eng. Chem. Res. doi: 10.1021/ie00005a022 – volume: 27 start-page: 335 year: 2004 ident: 10.1016/j.cherd.2008.12.007_bib21 article-title: LDA-measurements in a stirred tank with a liquid–liquid system at high volume percentage dispersed phase publication-title: Chem. Eng. Technol. doi: 10.1002/ceat.200401981 – volume: 57 start-page: 1815 year: 2002 ident: 10.1016/j.cherd.2008.12.007_bib1 article-title: Simulation of the population balances for liquid–liquid systems in a nonideal stirred tank. Part 2–parameter fitting and the use of the multiblock model for dense dispersions publication-title: Chem. Eng. Sci. doi: 10.1016/S0009-2509(02)00067-2 – volume: 76 start-page: 456 year: 1998 ident: 10.1016/j.cherd.2008.12.007_bib4 article-title: Drop break-up in intermittent turbulence: maximum stable and transient sizes of drops publication-title: Can. J. Chem. Eng. doi: 10.1002/cjce.5450760316 – start-page: 639 year: 2004 ident: 10.1016/j.cherd.2008.12.007_bib14 article-title: Immiscible liquid–liquid systems – volume: 56 start-page: 3377 year: 2001 ident: 10.1016/j.cherd.2008.12.007_bib5 article-title: Effects of agitation and scale-up on drop size in turbulent dispersions: allowance for intermittency publication-title: Chem. Eng. Sci. doi: 10.1016/S0009-2509(01)00027-6 – volume: 53 start-page: 2099 year: 1998 ident: 10.1016/j.cherd.2008.12.007_bib24 article-title: Evolution of drop size distribution in liquid–liquid dispersions for various impellers publication-title: Chem. Eng. Sci. doi: 10.1016/S0009-2509(97)00437-5 – volume: 15 start-page: 279 year: 1989 ident: 10.1016/j.cherd.2008.12.007_bib10 article-title: Effect of particle size on modulating turbulent intensity publication-title: Int. J. Multiphase Flow doi: 10.1016/0301-9322(89)90076-1 – volume: 63 start-page: 2107 year: 2008 ident: 10.1016/j.cherd.2008.12.007_bib18 article-title: Gas–liquid flow and bubble size distribution in stirred tanks publication-title: Chem. Eng. Sci. doi: 10.1016/j.ces.2008.01.005 – volume: 54 start-page: 4211 year: 1999 ident: 10.1016/j.cherd.2008.12.007_bib19 article-title: The influence of impeller type on mean drop size and drop size distribution in an agitated vessel publication-title: Chem. Eng. Sci. doi: 10.1016/S0009-2509(99)00156-6 – volume: 41 start-page: 917 year: 2006 ident: 10.1016/j.cherd.2008.12.007_bib22 article-title: PIV measurements in a liquid–liquid system at volume percentages up to 10% dispersed phase publication-title: Exp. Fluids doi: 10.1007/s00348-006-0211-0 – volume: 53 start-page: 3295 year: 1998 ident: 10.1016/j.cherd.2008.12.007_bib6 article-title: Particle drag coefficients in turbulent fluids publication-title: Chem. Eng. Sci. doi: 10.1016/S0009-2509(98)00114-6 – volume: 115 start-page: 304 year: 1991 ident: 10.1016/j.cherd.2008.12.007_bib11 article-title: Modulation of turbulence by a dispersed phase publication-title: J. Fluids Eng. doi: 10.1115/1.2909497 – volume: 85 start-page: 697 year: 2007 ident: 10.1016/j.cherd.2008.12.007_bib8 article-title: Multi-scale simulations of stirred liquid–liquid dispersions publication-title: Chem. Eng. Res. Des. doi: 10.1205/cherd06161 – volume: 19 start-page: 253 year: 2005 ident: 10.1016/j.cherd.2008.12.007_bib16 article-title: Modelling of solids distribution in stirred tanks: analysis of simulation strategies and comparison with experimental data publication-title: Int. J. Comp. Fluid Dyn. doi: 10.1080/10618560500081795 – volume: 53 start-page: 2063 year: 1998 ident: 10.1016/j.cherd.2008.12.007_bib25 article-title: Correlation of mean drop size and minimum drop size with the turbulence energy dissipation and the flow in an agitated tank publication-title: Chem. Eng. Sci. doi: 10.1016/S0009-2509(97)00438-7 – volume: 83 start-page: 1425 year: 2005 ident: 10.1016/j.cherd.2008.12.007_bib9 article-title: Effect of the number of impeller blades on the drop sizes in agitated dispersions publication-title: Chem. Eng. Res. Des. doi: 10.1205/cherd.04167 – volume: vol. 31 start-page: 151 year: 2006 ident: 10.1016/j.cherd.2008.12.007_bib23 article-title: The details of turbulent mixing process and their simulation – volume: 26 start-page: 738 year: 1993 ident: 10.1016/j.cherd.2008.12.007_bib3 article-title: Drop breakup and intermittent turbulence publication-title: J. Chem. Eng. Japan doi: 10.1252/jcej.26.738 – volume: 44 start-page: 13 year: 1998 ident: 10.1016/j.cherd.2008.12.007_bib13 article-title: Turbulence properties of the impeller stream of a Rushton turbine publication-title: AIChE J. doi: 10.1002/aic.690440104 – volume: 31 start-page: 416 year: 2005 ident: 10.1016/j.cherd.2008.12.007_bib12 article-title: Reynolds number dependence of gas-phase turbulence in gas–particle flows publication-title: Int. J. Multiphase Flow doi: 10.1016/j.ijmultiphaseflow.2004.11.009 – volume: 32 start-page: 677 year: 1986 ident: 10.1016/j.cherd.2008.12.007_bib7 article-title: Drop breakup in turbulent stirred-tank contactors. Part III: Correlations for mean size distribution publication-title: AIChE J. doi: 10.1002/aic.690320418 |
SSID | ssj0001748 |
Score | 2.0563176 |
Snippet | This work is aimed at investigating the fluid dynamic characteristics of a stirred tank of standard geometry for the dispersion of organics in water. Two... |
SourceID | proquest crossref elsevier |
SourceType | Aggregation Database Enrichment Source Index Database Publisher |
StartPage | 507 |
SubjectTerms | CFD Liquid–liquid Mixing PIV RANS equations |
Title | Experimental and computational analysis of immiscible liquid–liquid dispersions in stirred vessels |
URI | https://dx.doi.org/10.1016/j.cherd.2008.12.007 https://www.proquest.com/docview/33941037 |
Volume | 87 |
hasFullText | 1 |
inHoldings | 1 |
isFullTextHit | |
isPrint | |
link | http://utb.summon.serialssolutions.com/2.0.0/link/0/eLvHCXMwnV3JTsMwEB3RcoEDYhVlKT5wJDSJ7SzHqmpVViEWqbcodmwpqE1LF46If-AP-RLGWRAgxIFbZMVRNLZn3oxn3gAcK9OjyBa25TLBLBYLYQXawXOlEF54gtM4z825uvb6D-x8wAdL0KlqYUxaZan7C52ea-typFVKszVJ09Ydeg_UnGWDeSga7hosuzT0eB2W22cX_etPhYygOyhCLTQ__BX5UJ7mZUSTFDmVJixo2sr-bqB-qOrc_vTWYa0EjqRd_NsGLKlsE1a_0AluQdL9QtdP4iwhMu_ZUMb7cKQgICFjTdLRyNTjiqEiw_RpkSbvr2_FA0lSwx5uomgzkmYEdcB0qhLybFjGh7NteOh17zt9q-yiYElK2dzyReArae7vYpr4iLBYYlOJ60Fl4Pier9FlcpXiQvna5tLmcSBDKTVnsdK-5nQH6tk4U7tAnMCn6J842uMhunVuaLsiRswkAo9qHrMGuJXoIllSjJtOF8OoyiV7jHJ5F80vHTdCeTfg5HPSpGDY-Pt1r1qT6NtGidAG_D3xqFrByEjYJJdlaryYRZSGzJRL7v330_uwUl0y2c4B1OfThTpErDIXTaidvjhN3JGd28ubZrkzPwAlNeyq |
linkProvider | Elsevier |
linkToHtml | http://utb.summon.serialssolutions.com/2.0.0/link/0/eLvHCXMwnV07T8MwED5BGYAB8RTl6YGRqElsJ-lYVUWFQheo1M2KHVsKKin0wcx_4B_ySzjnURWEOrBFVhxFd_bdd-fzdwBX2vYocqXr-Ewyh8VSOpHxcF9phBeB5DTOa3Me-kF3wO6GfLgG7eoujC2rLG1_YdNza12ONEppNl7TtPGI0QO1e9liHoqOex02GMdorwYbrdtet78wyAi6oyLVQvPNX5EP5WVeVjRJUVNp04K2rezfDuqXqc79z80u7JTAkbSKf9uDNZ3tw_YSneABJJ0lun4SZwlRec-GMt-HIwUBCRkbkr682Pu4cqTJKH2bp8nXx2fxQJLUsofbLNqUpBlBGzCZ6IS8W5bx0fQQBjedp3bXKbsoOIpSNnNCGYVa2fO7mCYhIiyWuFShPqiKvDAIDYZMvtZc6tC4XLk8jlRTKcNZrE1oOD2CWjbO9DEQLwopxieeCXgTwzq_6foyRswko4AaHrM6-JXohCopxm2ni5GoasmeRS7vovml5wuUdx2uF5NeC4aN1a8HlU7Ej4Ui0AesnnhZaVBYCdviskyP51NBaZPZ65In__30JWx2nx7uxf1tv3cKW9WBk-udQW02metzxC0zeVGuy29qMu0E |
openUrl | ctx_ver=Z39.88-2004&ctx_enc=info%3Aofi%2Fenc%3AUTF-8&rfr_id=info%3Asid%2Fsummon.serialssolutions.com&rft_val_fmt=info%3Aofi%2Ffmt%3Akev%3Amtx%3Ajournal&rft.genre=article&rft.atitle=Experimental+and+computational+analysis+of+immiscible+liquid%E2%80%93liquid+dispersions+in+stirred+vessels&rft.jtitle=Chemical+engineering+research+%26+design&rft.au=Laurenzi%2C+F.&rft.au=Coroneo%2C+M.&rft.au=Montante%2C+G.&rft.au=Paglianti%2C+A.&rft.date=2009-04-01&rft.issn=0263-8762&rft.volume=87&rft.issue=4&rft.spage=507&rft.epage=514&rft_id=info:doi/10.1016%2Fj.cherd.2008.12.007&rft.externalDBID=n%2Fa&rft.externalDocID=10_1016_j_cherd_2008_12_007 |
thumbnail_l | http://covers-cdn.summon.serialssolutions.com/index.aspx?isbn=/lc.gif&issn=0263-8762&client=summon |
thumbnail_m | http://covers-cdn.summon.serialssolutions.com/index.aspx?isbn=/mc.gif&issn=0263-8762&client=summon |
thumbnail_s | http://covers-cdn.summon.serialssolutions.com/index.aspx?isbn=/sc.gif&issn=0263-8762&client=summon |