Development and Monitoring of a Continuous Polyurethane Pilot Reactor
The transition from batch to continuous polyurethane (PU) process is considered for process intensification. An integrated methodological and technological study is proposed. The development of the new process is based on modeling and product characteristics. In order to do so, the kinetics of the p...
Saved in:
Published in: | Chemical engineering & technology Vol. 33; no. 11; pp. 1900 - 1908 |
---|---|
Main Authors: | , , , |
Format: | Journal Article |
Language: | English |
Published: |
Weinheim
WILEY-VCH Verlag
01-11-2010
WILEY‐VCH Verlag Wiley-VCH Verlag |
Subjects: | |
Online Access: | Get full text |
Tags: |
Add Tag
No Tags, Be the first to tag this record!
|
Abstract | The transition from batch to continuous polyurethane (PU) process is considered for process intensification. An integrated methodological and technological study is proposed. The development of the new process is based on modeling and product characteristics. In order to do so, the kinetics of the polyaddition of polycaprolactone diol (polyol) and 4,4'‐diphenylmethane diisocyanate were studied and identified by using offline measurement of the diisocyanate concentration. Some characteristics of the final polymer were also investigated, such as the heat capacity and viscosity that affect the behavior of the continuous process. These results were used to design a tubular reactor for continuous production of PU. Since online monitoring of intensified processes is primordial, in situ near‐infrared spectroscopy was used to predict the concentration of free diisocyanate in real time.
Process intensification is important in polymer production to ensure flexibility in switching from one polymer production to another, reproducibility, enhance mixing and heat transfer, and avoid losses due to changes in raw materials or deviations of the process compounds. Based on modeling and product characteristics the transition from batch to continuous production of polyurethanes was developed. |
---|---|
AbstractList | The transition from batch to continuous polyurethane (PU) process is considered for process intensification. An integrated methodological and technological study is proposed. The development of the new process is based on modeling and product characteristics. In order to do so, the kinetics of the polyaddition of polycaprolactone diol (polyol) and 4,4'‐diphenylmethane diisocyanate were studied and identified by using offline measurement of the diisocyanate concentration. Some characteristics of the final polymer were also investigated, such as the heat capacity and viscosity that affect the behavior of the continuous process. These results were used to design a tubular reactor for continuous production of PU. Since online monitoring of intensified processes is primordial, in situ near‐infrared spectroscopy was used to predict the concentration of free diisocyanate in real time. The transition from batch to continuous polyurethane (PU) process is considered for process intensification. An integrated methodological and technological study is proposed. The development of the new process is based on modeling and product characteristics. In order to do so, the kinetics of the polyaddition of polycaprolactone diol (polyol) and 4,4'‐diphenylmethane diisocyanate were studied and identified by using offline measurement of the diisocyanate concentration. Some characteristics of the final polymer were also investigated, such as the heat capacity and viscosity that affect the behavior of the continuous process. These results were used to design a tubular reactor for continuous production of PU. Since online monitoring of intensified processes is primordial, in situ near‐infrared spectroscopy was used to predict the concentration of free diisocyanate in real time. Process intensification is important in polymer production to ensure flexibility in switching from one polymer production to another, reproducibility, enhance mixing and heat transfer, and avoid losses due to changes in raw materials or deviations of the process compounds. Based on modeling and product characteristics the transition from batch to continuous production of polyurethanes was developed. |
Author | Sheibat-Othman, N. Févotte, G. Nadjiadjim, G. Dupuy, J. |
Author_xml | – sequence: 1 givenname: G. surname: Nadjiadjim fullname: Nadjiadjim, G. organization: Université Lyon 1, LAGEP, UMR 5007, CNRS - ESCPE, Villeurbanne, France – sequence: 2 givenname: N. surname: Sheibat-Othman fullname: Sheibat-Othman, N. email: nida.othman@lagep.cpe.fr organization: Université Lyon 1, LAGEP, UMR 5007, CNRS - ESCPE, Villeurbanne, France – sequence: 3 givenname: G. surname: Févotte fullname: Févotte, G. organization: Ecole Nationale Supérieure des Mines de Saint Etienne, LPMG, CNRS UMR 5048, St-Etienne, France – sequence: 4 givenname: J. surname: Dupuy fullname: Dupuy, J. organization: Université de Lyon, Lyon, France; INSA Lyon, Villeurbanne, France; Université Lyon 1, Villeurbanne, France; CNRS, UMR5223, Ingénierie des Matériaux Polymères, Villeurbanne, France |
BackLink | https://hal.science/hal-00578607$$DView record in HAL |
BookMark | eNqFkMFPwjAUhxuDiYBePffqYdh2dN2OZCIzohLFeGy67VWqoyXbQPnvLZkh3jy9vub7fnn5DVDPOgsIXVIyooSw6wJUO2LEvwlLohPUp5zRYEwZ76E-SUISCE6jMzRomg_PUL_00fQGdlC5zRpsi5Ut8YOzpnW1se_Yaaxw6mxr7NZtG7xw1X5bQ7tSFvDCVK7Fz6AKT5-jU62qBi5-5xC93k6XaRbMn2Z36WQeFGESR0HOwjIBWgIvtT-U64RzpkQclTCmEAHxaSWPS6GTHLSKqSgEHQuW5zrUQEk4RFdd7kpVclObtar30ikjs8lcHv4I4T6OiB317Khji9o1TQ36KFAiD4XJQ2HyWJgXkk74MhXs_6FlOp0s_7pB55qmhe-jq-pPGYlQcPn2OJPLlyjOyO29zMIfkKOAeg |
CitedBy_id | crossref_primary_10_1007_s00216_017_0371_1 |
Cites_doi | 10.1002/app.2052 10.1002/1521-3900(200208)184:1<249::AID-MASY249>3.0.CO;2-5 10.1002/(SICI)1097-4628(19960919)61:12<2207::AID-APP21>3.0.CO;2-2 10.1016/0039-9140(93)E0055-I 10.1002/(SICI)1097-4628(19980705)69:1<169::AID-APP20>3.0.CO;2-U 10.1002/app.1767 10.1002/(SICI)1521-3919(19990301)8:2<129::AID-MATS129>3.0.CO;2-D 10.1016/j.matlet.2006.07.031 10.1016/0009-2509(95)00250-2 10.1021/ma60076a004 |
ContentType | Journal Article |
Copyright | Copyright © 2010 WILEY‐VCH Verlag GmbH & Co. KGaA, Weinheim Distributed under a Creative Commons Attribution 4.0 International License |
Copyright_xml | – notice: Copyright © 2010 WILEY‐VCH Verlag GmbH & Co. KGaA, Weinheim – notice: Distributed under a Creative Commons Attribution 4.0 International License |
DBID | BSCLL AAYXX CITATION 1XC |
DOI | 10.1002/ceat.201000296 |
DatabaseName | Istex CrossRef Hyper Article en Ligne (HAL) |
DatabaseTitle | CrossRef |
DatabaseTitleList | CrossRef |
DeliveryMethod | fulltext_linktorsrc |
Discipline | Engineering |
EISSN | 1521-4125 |
EndPage | 1908 |
ExternalDocumentID | oai_HAL_hal_00578607v1 10_1002_ceat_201000296 CEAT201000296 ark_67375_WNG_TS68H0FK_H |
Genre | article |
GrantInformation_xml | – fundername: National Agency for Development and Research in France (ANVAR) |
GroupedDBID | .3N .GA .Y3 05W 0R~ 10A 1L6 1OB 1OC 1ZS 29B 31~ 33P 3SF 3WU 4.4 4ZD 50Y 50Z 51W 51X 52M 52N 52O 52P 52S 52T 52U 52W 52X 5GY 5VS 66C 702 7PT 8-0 8-1 8-3 8-4 8-5 8UM 930 A03 AAESR AAEVG AAHHS AANLZ AAONW AASGY AAXRX AAZKR ABCQN ABCUV ABDBF ABEML ABIJN ABTAH ACAHQ ACBWZ ACCFJ ACCZN ACGFS ACPOU ACSCC ACXBN ACXQS ADBBV ADEOM ADIZJ ADKYN ADMGS ADOZA ADZMN ADZOD AEEZP AEIGN AEIMD AENEX AEQDE AEUQT AEUYR AFBPY AFFPM AFGKR AFPWT AFZJQ AHBTC AITYG AIURR AIWBW AJBDE AJXKR ALAGY ALMA_UNASSIGNED_HOLDINGS ALUQN AMBMR AMYDB ASPBG ATUGU AUFTA AVWKF AZBYB AZFZN AZVAB BAFTC BDRZF BFHJK BHBCM BLYAC BMNLL BNHUX BROTX BRXPI BSCLL BY8 CS3 D-E D-F DCZOG DPXWK DR1 DR2 DRFUL DRSTM DU5 EBS EJD F00 F01 F04 FEDTE G-S G.N GNP GODZA H.T H.X HF~ HGLYW HHY HVGLF HZ~ I-F IX1 J0M JPC KQQ LATKE LAW LC2 LC3 LEEKS LH4 LH6 LITHE LOXES LP6 LP7 LUTES LW6 LYRES MEWTI MK4 MRFUL MRSTM MSFUL MSSTM MXFUL MXSTM N04 N05 N9A NDZJH NF~ NNB O66 O9- OIG P2P P2W P2X P4D PALCI Q.N Q11 QB0 QRW R.K RBB RIWAO RJQFR ROL RWI RX1 RYL SAMSI SUPJJ TUS UB1 V2E W8V W99 WBFHL WBKPD WIB WIH WIK WOHZO WQJ WRC WSB WXSBR WYISQ XG1 XPP XV2 ZY4 ZZTAW ~IA ~WT AAMNL AAYXX CITATION 1XC |
ID | FETCH-LOGICAL-c3986-b23d9e1de5df2015f9552a786de41e6e0eacd58d7f9befa817c71472bbf3fe103 |
IEDL.DBID | 33P |
ISSN | 0930-7516 |
IngestDate | Tue Oct 15 15:22:58 EDT 2024 Thu Nov 21 22:11:19 EST 2024 Sat Aug 24 01:14:41 EDT 2024 Wed Oct 30 09:49:50 EDT 2024 |
IsPeerReviewed | true |
IsScholarly | true |
Issue | 11 |
Keywords | polymerization reactivities functional-groups Tubular reactor kinetics Polyurethane kinetic-model linear polyurethanes Process intensification Kinetics Near-infrared spectroscopy |
Language | English |
License | Distributed under a Creative Commons Attribution 4.0 International License: http://creativecommons.org/licenses/by/4.0 |
LinkModel | DirectLink |
MergedId | FETCHMERGED-LOGICAL-c3986-b23d9e1de5df2015f9552a786de41e6e0eacd58d7f9befa817c71472bbf3fe103 |
Notes | National Agency for Development and Research in France (ANVAR) ark:/67375/WNG-TS68H0FK-H istex:5EFD56776D988A25513F4C69C6978F3D49E4B10F ArticleID:CEAT201000296 |
ORCID | 0000-0002-2822-9566 0000-0002-2721-5365 |
PageCount | 9 |
ParticipantIDs | hal_primary_oai_HAL_hal_00578607v1 crossref_primary_10_1002_ceat_201000296 wiley_primary_10_1002_ceat_201000296_CEAT201000296 istex_primary_ark_67375_WNG_TS68H0FK_H |
PublicationCentury | 2000 |
PublicationDate | November, 2010 |
PublicationDateYYYYMMDD | 2010-11-01 |
PublicationDate_xml | – month: 11 year: 2010 text: November, 2010 |
PublicationDecade | 2010 |
PublicationPlace | Weinheim |
PublicationPlace_xml | – name: Weinheim |
PublicationTitle | Chemical engineering & technology |
PublicationTitleAlternate | Chem. Eng. Technol |
PublicationYear | 2010 |
Publisher | WILEY-VCH Verlag WILEY‐VCH Verlag Wiley-VCH Verlag |
Publisher_xml | – name: WILEY-VCH Verlag – name: WILEY‐VCH Verlag – name: Wiley-VCH Verlag |
References | H. Zhang et al., Mater. Lett. 2007, 61 (6), 1358. K. S. Gandhi, S. V. Babu, Macromolecules 1980, 13, 791. J. Dupuy et al., Macromol. Symp. 2002, 184, 249. H. Catalgil-Giz, A. Giz, A. Alb, W. F. Reed, J. Appl. Polym. Sci. 2001, 82, 2070. P. Krol, H. Galina, K. Kaczmarski, Macromol. Theory Simul. 1999, 8, 129. P. Krol, J. Appl. Polym. Sci. 1998, 69, 169. F. A. DeThomas, Talanta 1994, 41 (3), 425. A. K. Hipp, W. H. Ray, Chem. Eng. Sci. 1996, 51 (2), 281. B. Grepinet et al., J. Appl. Polym. Sci. 2001, 81, 3149. P. Krol, J. Appl. Polym. Sci. 1996, 61, 2207. 1996; 61 2001; 81 2001; 82 1996; 51 2007; 61 1999; 8 2002; 184 1994; 41 1980; 13 1998; 69 e_1_2_1_6_2 e_1_2_1_7_2 e_1_2_1_4_2 e_1_2_1_5_2 e_1_2_1_2_2 e_1_2_1_11_2 e_1_2_1_3_2 e_1_2_1_1_2 e_1_2_1_10_2 e_1_2_1_8_2 e_1_2_1_9_2 |
References_xml | – volume: 51 start-page: 281 issue: 2 year: 1996 publication-title: Chem. Eng. Sci. – volume: 82 start-page: 2070 year: 2001 publication-title: J. Appl. Polym. Sci. – volume: 81 start-page: 3149 year: 2001 publication-title: J. Appl. Polym. Sci. – volume: 69 start-page: 169 year: 1998 publication-title: J. Appl. Polym. Sci. – volume: 13 start-page: 791 year: 1980 publication-title: Macromolecules – volume: 8 start-page: 129 year: 1999 publication-title: Macromol. Theory Simul. – volume: 61 start-page: 1358 issue: 6 year: 2007 publication-title: Mater. Lett. – volume: 184 start-page: 249 year: 2002 publication-title: Macromol. Symp. – volume: 61 start-page: 2207 year: 1996 publication-title: J. Appl. Polym. Sci. – volume: 41 start-page: 425 issue: 3 year: 1994 publication-title: Talanta – ident: e_1_2_1_3_2 doi: 10.1002/app.2052 – ident: e_1_2_1_5_2 doi: 10.1002/1521-3900(200208)184:1<249::AID-MASY249>3.0.CO;2-5 – ident: e_1_2_1_7_2 doi: 10.1002/(SICI)1097-4628(19960919)61:12<2207::AID-APP21>3.0.CO;2-2 – ident: e_1_2_1_1_2 – ident: e_1_2_1_4_2 doi: 10.1016/0039-9140(93)E0055-I – ident: e_1_2_1_8_2 doi: 10.1002/(SICI)1097-4628(19980705)69:1<169::AID-APP20>3.0.CO;2-U – ident: e_1_2_1_10_2 doi: 10.1002/app.1767 – ident: e_1_2_1_9_2 doi: 10.1002/(SICI)1521-3919(19990301)8:2<129::AID-MATS129>3.0.CO;2-D – ident: e_1_2_1_2_2 doi: 10.1016/j.matlet.2006.07.031 – ident: e_1_2_1_11_2 doi: 10.1016/0009-2509(95)00250-2 – ident: e_1_2_1_6_2 doi: 10.1021/ma60076a004 |
SSID | ssj0001516 |
Score | 1.9376625 |
Snippet | The transition from batch to continuous polyurethane (PU) process is considered for process intensification. An integrated methodological and technological... |
SourceID | hal crossref wiley istex |
SourceType | Open Access Repository Aggregation Database Publisher |
StartPage | 1900 |
SubjectTerms | Chemical and Process Engineering Engineering Sciences Kinetics Near-infrared spectroscopy Polyurethane Process intensification Tubular reactor kinetics |
Title | Development and Monitoring of a Continuous Polyurethane Pilot Reactor |
URI | https://api.istex.fr/ark:/67375/WNG-TS68H0FK-H/fulltext.pdf https://onlinelibrary.wiley.com/doi/abs/10.1002%2Fceat.201000296 https://hal.science/hal-00578607 |
Volume | 33 |
hasFullText | 1 |
inHoldings | 1 |
isFullTextHit | |
isPrint | |
link | http://sdu.summon.serialssolutions.com/2.0.0/link/0/eLvHCXMwpV3dj9MwDI-48QIPfByc2PGhCJ24p2pt0zTp4zQ6KoGmiQ0db1GTuLqJqUXbeoL_njjdyvaEdDy2jVvLju3UsX8h5KrUhgkJIhDcmiDhGQvKuBQBJEbwFCQzPuFWLMTsu_yYI0xO38Xf4UP0CTe0DO-v0cBLvR39BQ01zlf50izcWELMbfer4Hs42Lx3xS6c-c3KjIWOmSg9oDaG8eiU_CQqnd1iTeRDFPOv0zWrDzrTp__P7jPyZL_gpONuhjwnD6A-J4-PYAhfkPyocoiWtaWdoeND2lS0pAhhtarbpt3SebP-3W4AE-5A56t1s6NfwZ_Z85J8m-bLSRHsj1cIDMtkGuiY2QwiC9xWjjFeZZw7NcnUQhJBCqGjtlxaUWUaqlJGwogoEbHWFasgCtkFGdRNDa8INZnRwsXDCpFJmdHuHUKDdb4iQcBBGJLrg3jVzw5FQ3V4ybFCwaheMEPy3km_H4Tg18X4i8J72Dcr01DcRUPywSunH1ZufmCBmuDqZvZJLRepLMLpZ1UMSex18o-Pqkk-XvZXl_chek0e-boC36X4hgx2mxbekrOtbd_5KfkH4oXemw |
link.rule.ids | 230,315,782,786,887,1408,27933,27934,46064,46488 |
linkProvider | Wiley-Blackwell |
linkToHtml | http://sdu.summon.serialssolutions.com/2.0.0/link/0/eLvHCXMwrV1Lb9QwEB6x7QF6oDzFAgULIThFTeL4keOq3SWoy2pFF8HNSuyJqKiSatsg-Pd4nG7aPSEhjnE8yWg8D2s88xngbVlZrjSqSAlno0zkPCrTUkWYWSUkam5Dwq04VYtv-nhKMDmTTS9Mjw8xJNzIMoK_JgOnhPThDWqo9c4q1GbRyZIcwW4mvTZSFwdfDs7YB7RwXJnz2LOTyA1uY5webtNvxaXRd6qK3CVB_9retYawM9v_Dww_gPvXe0426ZXkIdzB5hHs3UIifAzTW8VDrGwc622dXrK2ZiUjFKuzpmu7S7Zsz393a6ScO7Ll2Xl7xT5juLbnCXyZTVdHRXR9w0Jkea5lVKXc5Zg4FK72jIk6F8KvlJYOswQlxp7aCe1UnVdYlzpRViWZSquq5jUmMX8KO03b4DNgNreV8iGxJnBSbiv_DVWh8-4iI8xBHMP7jXzNRQ-kYXrI5NSQYMwgmDG88eIfJhH-dTGZGxqj1lktY_UzGcO7sDrDtHL9g2rUlDBfFx_M6lTqIp6dmGIMaViUv_zUHE0nq-Hp-b8QvYa7xerT3Mw_Lk5ewL1QZhCaFl_CztW6wwMYXbruVdDPPw6S4sM |
linkToPdf | http://sdu.summon.serialssolutions.com/2.0.0/link/0/eLvHCXMwpV1Lb9QwEB51WwnBAcpLLC3FQghOUZM4jp3jqt1tqlarFV0ENyuxx2pFlVTbBsG_x-O0oXtCosc4nmQ043nInvkM8LGqDZcKZSSFNVEmCh5VaSUjzIwUOSpuwoZbeSbn39XhlGByhi7-Hh9i2HAjywj-mgz8yrr9v6ChxvuqUJpFB0v5CLYyn4sTej7ni8EX-3gWTisLHntukvwOtjFO99fp18LS6JyKIrdIzr_Wk9YQdWbPHs7vNjy9zTjZpF8iz2EDmxfw5B4O4UuY3isdYlVjWW_p9JK1jlWMMKwumq7trtmivfzdrZB23JEtLi7bG_YFw6U9r-DrbLo8KKPb-xUiwwuVR3XKbYGJRWGdZ0y4QgivJ5VbzBLMMfbUVigrXVGjq1QijUwymda14w6TmL-GzaZt8A0wU5ha-oDoCJqUm9p_Q9ZovbPICHEQx_D5Trz6qofR0D1gcqpJMHoQzBg-eOkPkwj9upycahqjxlmVx_JnMoZPQTnDtGr1gyrUpNDf5kd6eZarMp6d6HIMadDJP36qD6aT5fD09n-I3sOjxeFMnx7PT3bgcagxCB2Lu7B5s-rwHYyubbcXVucfWCnhaQ |
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=Development+and+Monitoring+of+a+Continuous+Polyurethane+Pilot+Reactor&rft.jtitle=Chemical+engineering+%26+technology&rft.au=Nadjiadjim%2C+G.&rft.au=Sheibat%E2%80%90Othman%2C+N.&rft.au=F%C3%A9votte%2C+G.&rft.au=Dupuy%2C+J.&rft.date=2010-11-01&rft.pub=WILEY%E2%80%90VCH+Verlag&rft.issn=0930-7516&rft.eissn=1521-4125&rft.volume=33&rft.issue=11&rft.spage=1900&rft.epage=1908&rft_id=info:doi/10.1002%2Fceat.201000296&rft.externalDBID=10.1002%252Fceat.201000296&rft.externalDocID=CEAT201000296 |
thumbnail_l | http://covers-cdn.summon.serialssolutions.com/index.aspx?isbn=/lc.gif&issn=0930-7516&client=summon |
thumbnail_m | http://covers-cdn.summon.serialssolutions.com/index.aspx?isbn=/mc.gif&issn=0930-7516&client=summon |
thumbnail_s | http://covers-cdn.summon.serialssolutions.com/index.aspx?isbn=/sc.gif&issn=0930-7516&client=summon |