Modeling of three‐phase continuously operating open‐cell foam catalyst packings: Sugar hydrogenation to sugar alcohols-Reference-Cited by-同舟云学术

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Modeling of three‐phase continuously operating open‐cell foam catalyst packings: Sugar hydrogenation to sugar alcohols

Published:2022-05-08 Issue:9 Volume:68 Page:
ISSN:0001-1541
Container-title:AIChE Journal
language:en
Short-container-title:AIChE Journal

Author:

Najarnezhadmashhadi Ali¹,Braz Catarina G.²,Russo Vincenzo³^ORCID,Eränen Kari¹,Matos Henrique A.²,Salmi Tapio¹^ORCID

Affiliation:

1. Laboratory of Industrial Chemistry and Reaction Engineering, Johan Gadolin Process Chemistry Centre (PCC) Åbo Akademi University Turku/Åbo Finland

2. Centro de Recursos Naturais e Ambiente, Instituto Superior Técnico Universidade de Lisboa Lisbon Portugal

3. Chemical Sciences Department Università di Napoli “Federico II,” Complesso Universitario Monte S. Angelo Naples

Funder

Academy of Finland

Suomen Kulttuurirahasto

Publisher

Wiley

Subject

General Chemical Engineering,Environmental Engineering,Biotechnology

Link

https://onlinelibrary.wiley.com/doi/pdf/10.1002/aic.17732

Reference50 articles.

1. Experimental measurements and multiphase flow models in solid SiC foam beds

2. Hydrodynamics of gas–liquid counter-current flow in solid foam packings

3. Hydrodynamic multiplicity in a tubular reactor with solid foam packings

4. Liquid–solid mass transfer in a tubular reactor with solid foam packings

5. Theory and Applications of Ceramic Foam Catalysts

Cited by 2 articles. 订阅此论文施引文献订阅此论文施引文献，注册后可以免费订阅5篇论文的施引文献，订阅后可以查看论文全部施引文献

1. Continuous Hydrogenation of Maltose over Raney Ni in a Trickle-Bed Reactor;Industrial & Engineering Chemistry Research;2023-09-18

2. Decoupling gaseous hydrogen production from liquid water using a magnetic‐photo‐thermal coupling reactor;AIChE Journal;2022-08-16

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