Development of a plate-laminated methanol steam reformer for hydrogen production

Author(s):  
Pan Minqiang ◽  
Tang Yong ◽  
Yu Hao ◽  
Chen Hongqing ◽  
Li Yong ◽  
...  
Author(s):  
Giovanni Pisani ◽  
Alberto Zerbinato ◽  
Carlo Tregambe ◽  
Ernesto Benini

This paper describes technological of a fuel processor for hydrogen production able to convert 10 cubic meters of methane per hour. This device has been developed to feed hydrogen CHP suitable for the most common residential applications. The measured conversion efficiencies are extremely high: after the steam reformer the results are 76%H2; 18%CO2; 0,5%CH4; 5%CO; but the carbon monoxide is totally reduced throughout the water gas shift and the partial oxidation which contemporarily increase the hydrogen to over 77%. According to these results, this fuel processor is one of the first middle sized reformer to achieve, at comparable costs per cubic meter, conversion performance that were normally obtained only by industrial reforming plants.


2013 ◽  
Vol 79 (808) ◽  
pp. 2873-2884 ◽  
Author(s):  
Katsuya HIRATA ◽  
Masashi NAKAMORI ◽  
Kazuya TANIGAWA ◽  
Fukutarou KATAOKA ◽  
Yasutaka FUJIMOTO ◽  
...  

Processes ◽  
2020 ◽  
Vol 8 (6) ◽  
pp. 708 ◽  
Author(s):  
Watcharapong Khaodee ◽  
Tara Jiwanuruk ◽  
Khunnawat Ountaksinkul ◽  
Sumittra Charojrochkul ◽  
Jarruwat Charoensuk ◽  
...  

A compact heat integrated reactor system (CHIRS) of a steam reformer, a water gas shift reactor, and a combustor were designed for stationary hydrogen production from ethanol. Different reactor integration concepts were firstly studied using Aspen Plus. The sequential steam reformer and shift reactor (SRSR) was considered as a conventional system. The efficiency of the SRSR could be improved by more than 12% by splitting water addition to the shift reactor (SRSR-WS). Two compact heat integrated reactor systems (CHIRS) were proposed and simulated by using COMSOL Multiphysics software. Although the overall efficiency of the CHIRS was quite a bit lower than the SRSR-WS, the compact systems were properly designed for portable use. CHIRS (I) design, combining the reactors in a radial direction, was large in reactor volume and provided poor temperature control. As a result, the ethanol steam reforming and water gas shift reactions were suppressed, leading to lower hydrogen selectivity. On the other hand, CHIRS (II) design, combining the process in a vertical direction, provided better temperature control. The reactions performed efficiently, resulting in higher hydrogen selectivity. Therefore, the high performance CHIRS (II) design is recommended as a suitable stationary system for hydrogen production from ethanol.


Author(s):  
Omar R. Llerena Pizarro ◽  
Carlos Ocampo-Martinez ◽  
Maria Serra Prat ◽  
Jose Luz Silveira

2018 ◽  
Vol 43 (4) ◽  
pp. 2108-2120 ◽  
Author(s):  
Celso Eduardo Tuna ◽  
José Luz Silveira ◽  
Márcio Evaristo da Silva ◽  
Ronney Mancebo Boloy ◽  
Lúcia Bolini Braga ◽  
...  

2013 ◽  
Vol 7 (1) ◽  
pp. 49-63 ◽  
Author(s):  
Katsuya HIRATA ◽  
Masashi NAKAMORI ◽  
Kazuya TANIGAWA ◽  
Fukutaro KATAOKA ◽  
Yasutaka FUJIMOTO ◽  
...  

Author(s):  
Tetsuaki Takeda ◽  
Koichi Ichimiya

A technology development of a hydrogen production system by nuclear heat is being performed as a heat application system of the Very High Temperature Reactor (VHTR) in worldwide. As for the development of the coupling technology between the VHTR and the hydrogen production system, Japan Atomic Energy Agency had carried out a coupling technology test using a steam reforming process by natural gas. In the hydrogen production system by nuclear heat, the catalyst tube of the steam reformer is heated by the high temperature helium gas from the intermediate heat exchanger (IHX). There are several methods for heat transfer enhancement. For example, there are attaching various fins on the heat transfer surface, processing the surface roughly, and so on. Disk type fins are attached on the outside surface of the catalyst tube. The catalyst tube is inserted into the guide tube to increase an amount of heat transferred from the high temperature helium gas. However, it has to take into consideration the deterioration of the structure strength by attaching the fins on the tube surface with the design of the steam reformer. The objective of this study is to clarify performances of a method for heat transfer enhancement using porous material with high porosity by an experiment. The experiment has been performed using an apparatus which simulated the passage structure of the steam reformer to obtain characteristics of heat transfer.


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