Enhanced Conversion in the Direct Synthesis of Diethyl Carbonate from Ethanol and CO 2 by Process Intensification

To overcome the low equilibrium conversion in the direct synthesis of diethyl carbonate from ethanol and CO 2 under moderate reaction conditions, the reaction was conducted in a membrane reactor packed with pelletized Cu-Ni:3-1 supported on activated carbon. A SiO 2 /?-Al 2 O 3 commercial membrane a...

Full description

Autores:

Arbeláez Pérez, Oscar Felipe
Hernandez Aguirre, Enio Armando
González L.-M.
Bustamante F.
Villa A.-L.

Tipo de recurso:

Article of journal

Fecha de publicación:

2019

Institución:

Universidad Cooperativa de Colombia

Repositorio:

Repositorio UCC

Idioma:

OAI Identifier:

oai:repository.ucc.edu.co:20.500.12494/41372

Acceso en línea:

https://doi.org/10.1002/jbm.b.31976
https://www.scopus.com/inward/record.uri?eid=2-s2.0-85068720695&doi=10.3390%2fv11070582&partnerID=40&md5=2714f3155c5733d05b7c2a5079457ba2
https://hdl.handle.net/20.500.12494/41372

Palabra clave:

Activated carbon
Alumina
Aluminum oxide
Bioreactors
Carbon dioxide
Carbonation
Ethanol
Packed beds
Pelletizing
Silica
Zeolites
Catalytic membrane reactors
Commercial membranes
Diethyl carbonates
Equilibrium conversion
Ethanol conversion
Packed bed reactor
Process intensification
Reaction conditions
Gas permeable membranes

Rights

closedAccess

License

http://purl.org/coar/access_right/c_14cb