Zobrazeno 1 - 10
of 10
pro vyhledávání: '"Paul P. A. C. Pex"'
Autor:
Jan Degrève, Adrian Verhoef, Bart Huybrechs, Henk M. van Veen, Bart Van der Bruggen, Paul P. A. C. Pex
Publikováno v:
Computers & Chemical Engineering. 32:1135-1146
This study explores the possibility of simulating a hybrid pervaporation membrane process with the help of Aspen Plus™ (Aspen Tech) flowsheeting. Because Aspen Plus does not contain membrane modules in its Model Library, the pervaporation membrane
Publikováno v:
Annales de Chimie Science des Matériaux. 32:231-244
Les separations moleculaires sont tres importantes dans de nombreux procedes de production et elles sont responsables d'une consommation d'energie considerable. Les membranes microporeuses sont une alternative tres efficace a la distillation, procede
Autor:
L.A. Correia, D.F. Meyer, George Vulpescu, Matthijs Ruitenbeek, Lambert L van Lieshout, Paul P. A. C. Pex
Publikováno v:
Catalysis Communications. 5:347-351
The concept of a Pd-based catalytic membrane reactor (CMR) for the one-pot formation of phenol from benzene oxygen and hydrogen via “in situ” generated H2O2 was studied as a model reaction. Both technical and economic feasibility studies were per
Publikováno v:
Separation and Purification Technology. :361-366
A major drawback of polymeric membranes for pervaporation is their limited solvent and temperature stability. This means that for several potential applications the membrane lifetime in combination with a relatively low performance is the limiting fa
Autor:
Olivier Camus, Yvonne C. van Delft, Semali Perera, Jean-Alain Dalmon, D.F. Meyer, Barry Crittenden, Philippe Chanaud, Ernest Groensmit, Sylvain Miachon, Steve Tennison, Paul P. A. C. Pex, Wil Nobel, Izumi Kumakiri
An extensive screening program has been performed to find a suitable membrane configuration and operating conditions for the effective recovery of ammonia from the syngas loop. All the experiments have been performed at steady state. MFI zeolite memb
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_dedup___::9f622892c18bfcffb15744b515739123
http://resolver.tudelft.nl/uuid:d55c0acf-6767-4f0c-9008-fc712fc38cb2
http://resolver.tudelft.nl/uuid:d55c0acf-6767-4f0c-9008-fc712fc38cb2
Autor:
Paul P. A. C. Pex, Yvonne C. van Delft
One of the technologies for pre-combustion decarbonization is the production of hydrogen rich fuel gas from fossil fuel feed stock by means of a water gas shift membrane reactor system. CO 2 Capture Project (CCP) sponsored this development of hydroge
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::c0f1381f3aca0a822c27b92846844580
https://doi.org/10.1016/b978-008044570-0/50103-3
https://doi.org/10.1016/b978-008044570-0/50103-3
Autor:
Jan Wilco Dijkstra, Daniel Jansen, Paul P. A. C. Pex, Henk M. van Veen, Yvonne C. van Delft, L.A. Correia
Publisher Summary This chapter provides an overview of the current status of the membrane development as a part of the R&D trajectory of hydrogen membrane reactors at Energy research Centre of the Netherlands (ECN). It focuses on the development of a
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::1b9666e732bb7a7a2f1a70511e25b873
https://doi.org/10.1016/b978-008044704-9/50377-3
https://doi.org/10.1016/b978-008044704-9/50377-3
Publisher Summary This chapter discusses that pre-combustion de-carbonization (PCDC) has been identified as promising concept to capture CO 2 in power generation systems. Membrane reactors are expected to play a key role in the development in novel P
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::8bb7f287c44e4a6082a80a0ec8a9a64e
https://doi.org/10.1016/b978-008044704-9/50112-9
https://doi.org/10.1016/b978-008044704-9/50112-9
Publikováno v:
Chemical communications (Cambridge, England). (7)
The incorporation of methyl groups in microporous silica membranes was proven to enhance the service time in the dehydration of a butanol-water mixture at 95 degrees C from a few weeks to more than 18 months with a water flux of about 4 kg m(-2) h(-1
Publikováno v:
Chemical Communications. :834
The incorporation of methyl groups in microporous silica membranes was proven to enhance the service time in the dehydration of a butanol–water mixture at 95 °C from a few weeks to more than 18 months with a water flux of about 4 kg m−2 h−1 an