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Modeling of adsorber/desorber/catalytic reactor system for ethylene oxide removal

Modelovanje sistema adsorber/desorber/katalitički reaktor za uklanjanje etilen oksida

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2004
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Authors
Arsenijević, Zorana
Grbavčić, Željko
Grbić, Boško
Article (Published version)
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Abstract
The removal of ethylene oxide (EtO) in a combined system adsorber desorber/catalytic reactor has been investigated. The combined system was a modified draft tube spouted bed reactor loaded with Pt/Al2O3 catalyst. The annular region was divided into two sectons, the "hot" section contained about 7 % of catalyst and it behaved as a desorber and catalytic incinerator while the "cold" section, with the rest of the catalyst, behaved as a sorber. The catalyst particles were circulated between the two sections by use of a draft tube riser. The Computational Fluid Dynamics (CFD) program package FLUENT was used for simulations of the operation of the combined system. In addition, a one-dimensional numerical model for the operation of the packed bed reactor was compared with the corresponding FLUENT calculations. The results of the FLUENT simulations are in very good agreement with the experimental observations, as well as with the results of the one-dimensional numerical simulations.
U kombinovanom sistemu adsorber/desorber/katalitički reaktor izvršena su ispitivanja uklanjanja para etilen oksida (EtO). U kombinovanom sistemu je primenjen modifikovani fontanski sloj Pt/Al2O3 katalizatora sa cevnim umetkom. Anularni prostor sloja katalizatora se sastoji iz dve zone, "tople" zone koja sadrži oko 7 % ukupne količine katalizatora koja ima ulogu desorbera i katalitičkog konvertora, i "hladne" zone koja sadrži preostalu količinu katalizatora i ima ulogu adsorbera. Cirkulacija katalizatora između ove dve zone je omogućena pneumatskim transportom kroz cevni umetak. Izvršena je dvodimenziona parcijalna simulacija korišćenjem programskog paketa "FLUENT Computational Fluid Dynamics Software" u cilju simulacije odvijanja procesa u pojedinim zonama kombinovanog sistema. Jednodimenzioni model katalitičkog reaktora sa pakovanim slojem, iskorišćen je za numeričku simulaciju reakcionog dela kombinovanog sistema, i ovi rezultati su upoređeni sa odgovarajućim FLUENT-simulacijama. Dob...ijeno je veoma dobro slaganje rezultata FLUENT-simulacija sa eksperimentalnim zapažanjima i jednodimenzionim numeri čkim simulacijama.

Keywords:
draft tube spouted bed / Pt/Al2O3 catalyst / ethylene oxide removal / adsorber/desorber/catalytic reactor / numerical modeling / CFD modeling
Source:
Journal of the Serbian Chemical Society, 2004, 69, 12, 1129-1144
Publisher:
  • Serbian Chemical Society

DOI: 10.2298/JSC0412129A

ISSN: 0352-5139

WoS: 000226998500013

Scopus: 2-s2.0-31644447965
[ Google Scholar ]
1
1
URI
https://cer.ihtm.bg.ac.rs/handle/123456789/143
Collections
  • Radovi istraživača / Researchers' publications
Institution/Community
IHTM
TY  - JOUR
AU  - Arsenijević, Zorana
AU  - Grbavčić, Željko
AU  - Grbić, Boško
PY  - 2004
UR  - https://cer.ihtm.bg.ac.rs/handle/123456789/143
AB  - The removal of ethylene oxide (EtO) in a combined system adsorber desorber/catalytic reactor has been investigated. The combined system was a modified draft tube spouted bed reactor loaded with Pt/Al2O3 catalyst. The annular region was divided into two sectons, the "hot" section contained about 7 % of catalyst and it behaved as a desorber and catalytic incinerator while the "cold" section, with the rest of the catalyst, behaved as a sorber. The catalyst particles were circulated between the two sections by use of a draft tube riser. The Computational Fluid Dynamics (CFD) program package FLUENT was used for simulations of the operation of the combined system. In addition, a one-dimensional numerical model for the operation of the packed bed reactor was compared with the corresponding FLUENT calculations. The results of the FLUENT simulations are in very good agreement with the experimental observations, as well as with the results of the one-dimensional numerical simulations.
AB  - U kombinovanom sistemu adsorber/desorber/katalitički reaktor izvršena su ispitivanja uklanjanja para etilen oksida (EtO). U kombinovanom sistemu je primenjen modifikovani fontanski sloj Pt/Al2O3 katalizatora sa cevnim umetkom. Anularni prostor sloja katalizatora se sastoji iz dve zone, "tople" zone koja sadrži oko 7 % ukupne količine katalizatora koja ima ulogu desorbera i katalitičkog konvertora, i "hladne" zone koja sadrži preostalu količinu katalizatora i ima ulogu adsorbera. Cirkulacija katalizatora između ove dve zone je omogućena pneumatskim transportom kroz cevni umetak. Izvršena je dvodimenziona parcijalna simulacija korišćenjem programskog paketa "FLUENT Computational Fluid Dynamics Software" u cilju simulacije odvijanja procesa u pojedinim zonama kombinovanog sistema. Jednodimenzioni model katalitičkog reaktora sa pakovanim slojem, iskorišćen je za numeričku simulaciju reakcionog dela kombinovanog sistema, i ovi rezultati su upoređeni sa odgovarajućim FLUENT-simulacijama. Dobijeno je veoma dobro slaganje rezultata FLUENT-simulacija sa eksperimentalnim zapažanjima i jednodimenzionim numeri čkim simulacijama.
PB  - Serbian Chemical Society
T2  - Journal of the Serbian Chemical Society
T1  - Modeling of adsorber/desorber/catalytic reactor system for ethylene oxide removal
T1  - Modelovanje sistema adsorber/desorber/katalitički reaktor za uklanjanje etilen oksida
VL  - 69
IS  - 12
SP  - 1129
EP  - 1144
DO  - 10.2298/JSC0412129A
ER  - 
@article{
author = "Arsenijević, Zorana and Grbavčić, Željko and Grbić, Boško",
year = "2004",
abstract = "The removal of ethylene oxide (EtO) in a combined system adsorber desorber/catalytic reactor has been investigated. The combined system was a modified draft tube spouted bed reactor loaded with Pt/Al2O3 catalyst. The annular region was divided into two sectons, the "hot" section contained about 7 % of catalyst and it behaved as a desorber and catalytic incinerator while the "cold" section, with the rest of the catalyst, behaved as a sorber. The catalyst particles were circulated between the two sections by use of a draft tube riser. The Computational Fluid Dynamics (CFD) program package FLUENT was used for simulations of the operation of the combined system. In addition, a one-dimensional numerical model for the operation of the packed bed reactor was compared with the corresponding FLUENT calculations. The results of the FLUENT simulations are in very good agreement with the experimental observations, as well as with the results of the one-dimensional numerical simulations., U kombinovanom sistemu adsorber/desorber/katalitički reaktor izvršena su ispitivanja uklanjanja para etilen oksida (EtO). U kombinovanom sistemu je primenjen modifikovani fontanski sloj Pt/Al2O3 katalizatora sa cevnim umetkom. Anularni prostor sloja katalizatora se sastoji iz dve zone, "tople" zone koja sadrži oko 7 % ukupne količine katalizatora koja ima ulogu desorbera i katalitičkog konvertora, i "hladne" zone koja sadrži preostalu količinu katalizatora i ima ulogu adsorbera. Cirkulacija katalizatora između ove dve zone je omogućena pneumatskim transportom kroz cevni umetak. Izvršena je dvodimenziona parcijalna simulacija korišćenjem programskog paketa "FLUENT Computational Fluid Dynamics Software" u cilju simulacije odvijanja procesa u pojedinim zonama kombinovanog sistema. Jednodimenzioni model katalitičkog reaktora sa pakovanim slojem, iskorišćen je za numeričku simulaciju reakcionog dela kombinovanog sistema, i ovi rezultati su upoređeni sa odgovarajućim FLUENT-simulacijama. Dobijeno je veoma dobro slaganje rezultata FLUENT-simulacija sa eksperimentalnim zapažanjima i jednodimenzionim numeri čkim simulacijama.",
publisher = "Serbian Chemical Society",
journal = "Journal of the Serbian Chemical Society",
title = "Modeling of adsorber/desorber/catalytic reactor system for ethylene oxide removal, Modelovanje sistema adsorber/desorber/katalitički reaktor za uklanjanje etilen oksida",
volume = "69",
number = "12",
pages = "1129-1144",
doi = "10.2298/JSC0412129A"
}
Arsenijević, Z., Grbavčić, Ž.,& Grbić, B.. (2004). Modeling of adsorber/desorber/catalytic reactor system for ethylene oxide removal. in Journal of the Serbian Chemical Society
Serbian Chemical Society., 69(12), 1129-1144.
https://doi.org/10.2298/JSC0412129A
Arsenijević Z, Grbavčić Ž, Grbić B. Modeling of adsorber/desorber/catalytic reactor system for ethylene oxide removal. in Journal of the Serbian Chemical Society. 2004;69(12):1129-1144.
doi:10.2298/JSC0412129A .
Arsenijević, Zorana, Grbavčić, Željko, Grbić, Boško, "Modeling of adsorber/desorber/catalytic reactor system for ethylene oxide removal" in Journal of the Serbian Chemical Society, 69, no. 12 (2004):1129-1144,
https://doi.org/10.2298/JSC0412129A . .

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