Variants of the Organization of a Controlled-Temperature-Profile Catalyst Bed in a Tubular Reactor for the Single-Step Water Gas Shift Reaction Full article
Journal |
Theoretical Foundations of Chemical Engineering
ISSN: 0040-5795 , E-ISSN: 1608-3431 |
||
---|---|---|---|
Output data | Year: 2009, Volume: 43, Number: 4, Pages: 366-373 Pages count : 8 DOI: 10.1134/S0040579509040034 | ||
Tags | Fuel Cell; Oxide Catalyst; Heat Removal; Tubular Reactor; Axial Temperature | ||
Authors |
|
||
Affiliations |
|
Funding (1)
1 | International Science and Technology Center | 2327 |
Abstract:
The possibility of bringing the actual temperature profile along the catalyst bed to the profile maximizing the CO conversion in the water gas shift (WGS) reaction in a tubular reactor is considered for new, highly efficient catalysts as heat-conducting composite plates (HCCPs). It is demonstrated by the example of a controlled-temperature-profile (CTP) tubular reactor integrated into an experimental model of a fuel cell of a 5-kW power plant that the efficiency of the WGS process can be raised by using the catalyst as HCCPs. Use of these catalysts in CTP apparatuses can markedly increase the efficiency of the WGS stage of natural gas reforming for ammonia synthesis, hydrogen production, and the production of fuel gas for fuel cells.
Cite:
Baronskaya N.A.
, Khasin A.A.
, Smirnov E.I.
, Yur'eva T.M.
Variants of the Organization of a Controlled-Temperature-Profile Catalyst Bed in a Tubular Reactor for the Single-Step Water Gas Shift Reaction
Theoretical Foundations of Chemical Engineering. 2009. V.43. N4. P.366-373. DOI: 10.1134/S0040579509040034 WOS Scopus РИНЦ
Variants of the Organization of a Controlled-Temperature-Profile Catalyst Bed in a Tubular Reactor for the Single-Step Water Gas Shift Reaction
Theoretical Foundations of Chemical Engineering. 2009. V.43. N4. P.366-373. DOI: 10.1134/S0040579509040034 WOS Scopus РИНЦ
Original:
Баронская Н.А.
, Хасин А.А.
, Смирнов Е.И.
, Юрьева Т.М.
Варианты организации катализаторного слоя с управляемым температурным профилем в трубчатом аппарате одностадийного процесса паровой конверсии монооксида углерода
Теоретические основы химической технологии. 2009. Т.43. №4. С.385-393. РИНЦ
Варианты организации катализаторного слоя с управляемым температурным профилем в трубчатом аппарате одностадийного процесса паровой конверсии монооксида углерода
Теоретические основы химической технологии. 2009. Т.43. №4. С.385-393. РИНЦ
Dates:
Submitted: | Aug 11, 2008 |
Published print: | Aug 1, 2009 |
Published online: | Aug 14, 2009 |
Identifiers:
Web of science | WOS:000269008100003 |
Scopus | 2-s2.0-68949184346 |
Elibrary | 15301089 |
Chemical Abstracts | 2009:999643 |
Chemical Abstracts (print) | 153:150226 |
OpenAlex | W1983751366 |