CFD simulation on hydrogen-membrane reactor integrating cyclohexane dehydrogenation and CO2 methanation reactions: A conceptual study

2021 ◽  
Vol 235 ◽  
pp. 113989
Author(s):  
Zhoufeng Bian ◽  
Houchuan Xia ◽  
Wenqi Zhong ◽  
Bo Jiang ◽  
Yang Yu ◽  
...  
Hydrogen ◽  
2021 ◽  
Vol 2 (1) ◽  
pp. 18-32
Author(s):  
Silvano Tosti ◽  
Alfonso Pozio ◽  
Luca Farina ◽  
Alessia Santucci

Among the processes for producing hydrogen and oxygen from water via the use of solar energy, water splitting has the advantage of being carried out in onestep. According to thermodynamics, this process exhibits conversions of practical interest at very high temperatures and needs efficient separation systems in order to separate the reaction products, hydrogen and oxygen. In this conceptual work, the behavior of a membrane reactor that uses two membranes perm-selective to hydrogen and oxygen is investigated in the temperature range 2000–2500 °C of interest for coupling this device with solar receivers. The effect of the reaction pressure has been evaluated at 0.5 and 1 bar while the permeate pressure has been fixed at 100 Pa. As a first result, the use of the membrane perm-selective to oxygen in addition to the hydrogen one has improved significantly the reaction conversion that, for instance, at 0.5 bar and 2000 °C, moves from 9.8% up to 18.8%. Based on these critical data, a preliminary design of a membrane reactor consisting of a Ta tubular membrane separating the hydrogen and a hafnia camera separating the oxygen is presented: optimaloperating temperature of the reactor results in being around 2500 °C, a value making impracticable its coupling with solar receivers even in view of an optimistic development of this technology. The study has verified that at 2000 °C with a water feed flow rate of 1000 kg h−1 about 200 and 100 m3 h−1 of hydrogen and oxygen are produced. In this case, a surface of the hafnia membrane of the order of hundreds m2 is required: the design of such a membrane device may be feasible when considering special reactor configurations.


2020 ◽  
Vol 59 (37) ◽  
pp. 16170-16184
Author(s):  
A. Catarina Faria ◽  
C. V. Miguel ◽  
A. E. Rodrigues ◽  
L. M. Madeira

2014 ◽  
Vol 39 (19) ◽  
pp. 10154-10160 ◽  
Author(s):  
Manabu Miyamoto ◽  
Risa Hayakawa ◽  
Yasutaka Makino ◽  
Yasuhiro Oumi ◽  
Shigeyuki Uemiya ◽  
...  

2013 ◽  
Vol 67 ◽  
pp. 160-170 ◽  
Author(s):  
Finn Are Michelsen ◽  
Øivind Wilhelmsen ◽  
Lei Zhao ◽  
Knut Ingvar Åsen

Author(s):  
Zhewei Liu ◽  
Zhoufeng Bian ◽  
Bo Jiang ◽  
Zhigang Wang

CO2 hydrogenation is one of the important routes for CO2 utilization to address the global warming issue, which has aroused much attention in recent years. A novel water-permeable membrane reactor...


2011 ◽  
Vol 6 (1) ◽  
Author(s):  
Byron Smith R.J. ◽  
Muruganandam Loganathan ◽  
Murthy Shekhar Shantha

Membrane reactor is a process intensified equipment that carries out both the reaction and separation in a single vessel. The equilibrium limited water gas shift reaction is an ideal reaction to be carried out in a membrane reactor as it improves the conversion of the reaction and reduces the space requirement for the reactor. Computational fluid dynamics offers a virtual prototyping of the reactor and helps in design, optimization, and scale-up of the reactor. To obtain pure hydrogen from the membrane reactor, the pressure of the reactor needs to be optimized. Hence the water gas shift membrane reactor is subjected to computational fluid dynamic analysis to understand the role played by pressure on the performance of the reactor using three different gas mixtures. The CO conversion and H2 recovery for the different operating pressures are simulated and the effects of pressure are discussed in this paper.


2017 ◽  
Vol 25 (1) ◽  
pp. 18-25 ◽  
Author(s):  
Xin Wei ◽  
Hong Wang ◽  
Zhen Yin ◽  
Saood Qaseem ◽  
Jianxin Li

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