Zobrazeno 1 - 10
of 55
pro vyhledávání: '"M. Otterbein"'
Publikováno v:
Chemical Engineering & Technology. 30:702-708
The present study deals with the pressure effect (1 to 10 10 5 Pa) on the hydrodynamics and efficiency within packed column distillation. Three kinds of packings are used: Raschig rings and Berl saddles as random packing, and Sulzer Mellapak 250 Y as
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::1f9c9f1debe0bee139ef6ff5301a6b69
https://doi.org/10.1002/ceat.200600173
https://doi.org/10.1002/ceat.200600173
Publikováno v:
Chemical Engineering & Technology. 29:1205-1215
The main objective of this work was to propose a new process for household fume incineration treatment: the droplet column. A feature of this upward gas-liquid reactor which makes it original, is to use high superficial gas velocities (13 m s–1) wh
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::d150278a3a37fde85f81d72130a59079
https://doi.org/10.1002/ceat.200600120
https://doi.org/10.1002/ceat.200600120
Publikováno v:
Chemical Engineering and Processing: Process Intensification. 43:1389-1395
Two phase flow co-current horizontal spray column performing under high gas velocities (up to 14 m/s) is investigated in an air-water system. Experiments are carried out in order to characterize mass transfer between liquid and gas in the reactor und
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::bbb5ee41012a8cf7a7de9697706524ca
https://doi.org/10.1016/j.cep.2003.12.009
https://doi.org/10.1016/j.cep.2003.12.009
Publikováno v:
Chemical Engineering Science. 58:2365-2376
The present study deals with the pressure effects on mass transfer parameters within a bubble reactor operating at pressures up to 5 MPa . The gas–liquid systems are N2/CO2-aqueous solution of Na2CO3–NaHCO3 and N2/CO2-aqueous solution of NaOH. A
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::d0af9f9d538bad18deb0d3ca4434d2ad
https://doi.org/10.1016/s0009-2509(03)00085-x
https://doi.org/10.1016/s0009-2509(03)00085-x
Publikováno v:
Chemical Engineering & Technology. 24:77-84
The present study deals with the pressure effects on the hydrodynamic flow and mass transfer within an agitated bubble reactor operated at pressures between 10 5 and 100x10 5 Pa. In order to clarify the flow behavior within the reactor, liquid phase
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::e654411a65350136079846c107b60034
https://doi.org/10.1002/1521-4125(200101)24:1<77::aid-ceat77>3.0.co
https://doi.org/10.1002/1521-4125(200101)24:1<77::aid-ceat77>3.0.co
Publikováno v:
Chemical Engineering Science. 55:6251-6257
The aim of this study is to determine mass transfer parameters such as interfacial area a and volumetric liquid side mass transfer coefficient k L a during gas–liquid absorption in a packed column according to pressure within the range 0.1–1.3 MP
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::efed29c2ad5dfe9b2e9f639e53247083
https://doi.org/10.1016/s0009-2509(00)00206-2
https://doi.org/10.1016/s0009-2509(00)00206-2
Publikováno v:
Chemical Engineering & Technology. 22:1043-1049
Two-phase flow co-current vertical downflow reactor with gas entrainment by a liquid jet is investigated in an air-water system. Experiments are carried out in order to clarify the flow behavior of the reactor under various conditions. Gas entrainmen
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::068d5f6493c46c6dd5cd8e6e9c8aa6ca
https://doi.org/10.1002/(sici)1521-4125(199912)22:12<1043::aid-ceat1043>3.0.co
https://doi.org/10.1002/(sici)1521-4125(199912)22:12<1043::aid-ceat1043>3.0.co
Publikováno v:
Computers & Chemical Engineering. 23:S93-S96
Our former method for the assessment of the feasibility of batch extractive distillation (usually performed in a rectifier with a heavy entrainer) was extended to the case where a light entrainer is fed continuously into a rectifier or a stripper. Th
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::04916387b686a2db3ed0464bed3c7015
https://doi.org/10.1016/s0098-1354(99)80024-6
https://doi.org/10.1016/s0098-1354(99)80024-6
Publikováno v:
Scopus-Elsevier
A method has been developed for the assessment of the feasibility and for the sequencing of homoazeotropic distillation in a batch rectifier under continuous entrainer feeding. The method is based on the calculation of the still path and possible com
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_dedup___::c9d6c03fd5e8b30923f11280cbc51681
https://doi.org/10.1016/s0098-1354(98)00117-3
https://doi.org/10.1016/s0098-1354(98)00117-3
Publikováno v:
Chemical Engineering Science. 53:1331-1348
The batch realisation of the extractive distillation and the role played by the different steps in the process are analysed and on the basis of this analysis several operational policies are presented. The different BED policies are studied by simula
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::7063c9443f6ec3ba1883b8f558f1a696
https://doi.org/10.1016/s0009-2509(97)00420-x
https://doi.org/10.1016/s0009-2509(97)00420-x