scholarly journals An Enhanced Sherwood Number to Model the Hydrogen Transport in Membrane Steam Reformers

Membranes ◽  
2021 ◽  
Vol 11 (11) ◽  
pp. 805
Author(s):  
Maria Anna Murmura ◽  
Chiara Rocchetti ◽  
Maria Cristina Annesini

It is well known that membrane reactors are inherently two-dimensional systems in which species concentrations vary as a consequence of both the reaction and permeation across the membrane, which occurs in the direction perpendicular to that of the main gas flow. Recently, an expression for an enhanced Sherwood number was developed to describe the hydrogen concentration gradients arising in methane steam-reforming membrane reactors as a consequence of the combined effect of hydrogen production, dispersion, and permeation. Here, the analysis is developed in further detail with the aim of (i) assessing the validity of the simplifying assumptions made when developing the 1D model and (ii) identifying the operating conditions under which it is possible to employ the 1D model with the enhanced Sherwood number.

1994 ◽  
Vol 119 (2) ◽  
pp. 305-325 ◽  
Author(s):  
Jun Shu ◽  
Bernard P.A. Grandjean ◽  
Serge Kaliaguine

Desalination ◽  
2008 ◽  
Vol 233 (1-3) ◽  
pp. 359-366 ◽  
Author(s):  
Shigeki Hara ◽  
Kenji Haraya ◽  
Giuseppe Barbieri ◽  
Enrico Drioli

Author(s):  
Mingfeng Qiu ◽  
Brian Bailey ◽  
Rob Stoll ◽  
Bart Raeymaekers

The Navier-Stokes and compressible Reynolds equations are solved for gas lubricated textured parallel slider bearings under hydrodynamic lubrication for a range of realistic texture geometry parameters and operating conditions. The simplifying assumptions inherent in the Reynolds equation are validated by comparing simulation results to the solution of the Navier-Stokes equations. Using the Reynolds equation to describe shear driven gas flow in textured parallel slider bearings is justified for the range of parameters considered.


2016 ◽  
Vol 58 (1) ◽  
pp. 1-35 ◽  
Author(s):  
Adolfo Iulianelli ◽  
Simona Liguori ◽  
Jennifer Wilcox ◽  
Angelo Basile

AIChE Journal ◽  
2010 ◽  
Vol 57 (7) ◽  
pp. 1882-1888 ◽  
Author(s):  
Kazuki Akamatsu ◽  
Takuya Murakami ◽  
Takashi Sugawara ◽  
Ryuji Kikuchi ◽  
Shin-ichi Nakao

2021 ◽  
Author(s):  
Junyi Li ◽  
Zhe Dong ◽  
Bowen Li

Abstract Methane steam reforming (MSR) technology is one of the promising methods of hydrogen production and already available at an industrial scale, in which steam is added to methane to generate hydrogen. MSR carries out at a temperature of 500°C when catalysts and Pd-based membrane reactors are used. The nuclear steam supply system (NSSS) of a modular high-temperature gas-cooled reactor (MHTGR) can provide high-quality steam of around 570°C, which is an excellent heat source for MSR. MHTGR is a typical small modular reactor (SMR), of which the coolant is helium, and the moderator and structural material are graphite. The number of the MHTGR can be decided based on the thermal power required for MSR and electricity generation. In this paper, a six-modular MHTGR nuclear power plant with 1500MW thermal power coupled with the MSR process is designed. The hydrogen production rate is 9.72 tons per hour. The dynamic modeling is based on conservation laws of mass and energy. To examine the dynamic characteristics of the nuclear hydrogen production plant, open-loop responses of the model under different disturbances are presented.


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