Zobrazeno 1 - 6
of 6
pro vyhledávání: '"RD Vas Bhat"'
Publikováno v:
Chemical Engineering Communications, 189(8), 1009-1037. Taylor & Francis Group
The diffusivity of CO2 in ethanol, n-heptane and methyl tertiary butyl ether (MTBE) has been determined using a laminar jet reactor and a wetted wall column at two temperatures (293 K and 298 K). The reactors have been operated in the laminar and tra
Publikováno v:
Chemical engineering science, 54(1), 121-136. Elsevier
Chemical Engineering Science, 54(1), 121-136. Elsevier
Chemical Engineering Science, 54(1), 121-136. Elsevier
A fundamental description of gas–liquid mass transfer with reversible consecutive reaction has been derived. The Higbie penetration theory has been used and numerical simulations were carried out for isothermal absorption. Although the model can be
Publikováno v:
Chemical Engineering Science, 54(1), 137-147. Elsevier
Chemical engineering science, 1999(54), 137-147. Elsevier
Chemical engineering science, 1999(54), 137-147. Elsevier
A fundamental description of gas–liquid mass transfer with reversible consecutive reaction has been given. The Higbie penetration theory has been used and numerical simulations were carried out for isothermal absorption. Although the model can be a
Publikováno v:
Chemical Engineering Science, 52(24), 4547-4559. PERGAMON-ELSEVIER SCIENCE LTD
Chemical engineering science, 52(24), 4547-4559. Elsevier
Chemical Engineering Science, 52(24), 4547-4559. Elsevier
Chemical engineering science, 52(24), 4547-4559. Elsevier
Chemical Engineering Science, 52(24), 4547-4559. Elsevier
A new explicit relation is proposed for the prediction of the enhancement factor for reversible reactions of finite rate in chemically loaded solutions which also allows for unequal diffusivities. The relation for the enhancement factor is not based
Publikováno v:
Chemical Engineering Journal, 2000(76), 127-152. Elsevier
Chemical Engineering Journal, 76(2), 127-152. Elsevier
Chemical Engineering Journal, 76(2), 127-152. Elsevier Science
Chemical Engineering Journal, 76(2), 127-152. Elsevier
Chemical Engineering Journal, 76(2), 127-152. Elsevier Science
An absorption model to study gas¿liquid mass transfer accompanied by reversible two-step reactions in the liquid phase has been presented. This model has been used to determine mass transfer rates, enhancement factors and concentration profiles over
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_dedup___::72381c32670586302325d46384bd9741
https://research.utwente.nl/en/publications/4e757310-fb19-4c02-955b-b637963bd170
https://research.utwente.nl/en/publications/4e757310-fb19-4c02-955b-b637963bd170
Publikováno v:
Scopus-Elsevier
Chemical Engineering Science, 52(21), 4079-4094. PERGAMON-ELSEVIER SCIENCE LTD
Chemical Engineering Science, 52(21-22), 4079-4094. Elsevier
Chemical engineering science, 52(21), 4079-4094. Elsevier
Chemical Engineering Science, 52(21), 4079-4094. PERGAMON-ELSEVIER SCIENCE LTD
Chemical Engineering Science, 52(21-22), 4079-4094. Elsevier
Chemical engineering science, 52(21), 4079-4094. Elsevier
A fundamental description of non-isothermal mass transfer accompanied by a single reversible chemical reaction has been presented. The description is based on the Higbie penetration theory. Arrhenius type dependence of solubility, reaction rates and
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_dedup___::1a34cf58d149087c3e8aaf7f04a6f8fb
http://www.scopus.com/inward/record.url?eid=2-s2.0-0031278452&partnerID=MN8TOARS
http://www.scopus.com/inward/record.url?eid=2-s2.0-0031278452&partnerID=MN8TOARS