Abstract
The potential of the silica membrane reactors for use in the decomposition of hydrogen iodide (HI) was investigated by simulation with the aim of producing CO 2 -free hydrogen via the thermochemical water-splitting iodine-sulfur process. Simulation model validation was done using the data derived from an experimental membrane reactor. The simulated results showed good agreement with the experimental findings. The important process parameters determining the performance of the membrane reactor used for HI decomposition, namely, reaction temperature, total pressures on both the feed side and the permeate side, and HI feed flow rate were investigated theoritically by means of a simulation. It was found that the conversion of HI decomposition can be improved by up to four times (80%) or greater than the equilibrium conversion (20%) at 400 °C by employing a membrane reactor equipped with a tubular silica membrane. The features to design the membrane reactor module for HI decomposition of the thermochemical iodine-sulfur process were discussed under a wide range of operation conditions by evaluating the relationship between HI conversion and number of membrane tubes.
| Original language | English |
|---|---|
| Pages (from-to) | 10207-10217 |
| Number of pages | 11 |
| Journal | International Journal of Hydrogen Energy |
| Volume | 44 |
| Issue number | 21 |
| DOIs | |
| Publication status | Published - 2019 Apr 23 |
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Keywords
- HI decomposition
- Hydrogen production
- IS process
- Membrane reactor
- Silica membrane
- Thermochemical cycle
ASJC Scopus subject areas
- Renewable Energy, Sustainability and the Environment
- Fuel Technology
- Condensed Matter Physics
- Energy Engineering and Power Technology
Cite this
Module design of silica membrane reactor for hydrogen production via thermochemical IS process. / Myagmarjav, Odtsetseg; Tanaka, Nobuyuki; Nomura, Mikihiro; Kubo, Shinji.
In: International Journal of Hydrogen Energy, Vol. 44, No. 21, 23.04.2019, p. 10207-10217.Research output: Contribution to journal › Article
}
TY - JOUR
T1 - Module design of silica membrane reactor for hydrogen production via thermochemical IS process
AU - Myagmarjav, Odtsetseg
AU - Tanaka, Nobuyuki
AU - Nomura, Mikihiro
AU - Kubo, Shinji
PY - 2019/4/23
Y1 - 2019/4/23
N2 - The potential of the silica membrane reactors for use in the decomposition of hydrogen iodide (HI) was investigated by simulation with the aim of producing CO 2 -free hydrogen via the thermochemical water-splitting iodine-sulfur process. Simulation model validation was done using the data derived from an experimental membrane reactor. The simulated results showed good agreement with the experimental findings. The important process parameters determining the performance of the membrane reactor used for HI decomposition, namely, reaction temperature, total pressures on both the feed side and the permeate side, and HI feed flow rate were investigated theoritically by means of a simulation. It was found that the conversion of HI decomposition can be improved by up to four times (80%) or greater than the equilibrium conversion (20%) at 400 °C by employing a membrane reactor equipped with a tubular silica membrane. The features to design the membrane reactor module for HI decomposition of the thermochemical iodine-sulfur process were discussed under a wide range of operation conditions by evaluating the relationship between HI conversion and number of membrane tubes.
AB - The potential of the silica membrane reactors for use in the decomposition of hydrogen iodide (HI) was investigated by simulation with the aim of producing CO 2 -free hydrogen via the thermochemical water-splitting iodine-sulfur process. Simulation model validation was done using the data derived from an experimental membrane reactor. The simulated results showed good agreement with the experimental findings. The important process parameters determining the performance of the membrane reactor used for HI decomposition, namely, reaction temperature, total pressures on both the feed side and the permeate side, and HI feed flow rate were investigated theoritically by means of a simulation. It was found that the conversion of HI decomposition can be improved by up to four times (80%) or greater than the equilibrium conversion (20%) at 400 °C by employing a membrane reactor equipped with a tubular silica membrane. The features to design the membrane reactor module for HI decomposition of the thermochemical iodine-sulfur process were discussed under a wide range of operation conditions by evaluating the relationship between HI conversion and number of membrane tubes.
KW - HI decomposition
KW - Hydrogen production
KW - IS process
KW - Membrane reactor
KW - Silica membrane
KW - Thermochemical cycle
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UR - http://www.scopus.com/inward/citedby.url?scp=85063425049&partnerID=8YFLogxK
U2 - 10.1016/j.ijhydene.2019.02.192
DO - 10.1016/j.ijhydene.2019.02.192
M3 - Article
AN - SCOPUS:85063425049
VL - 44
SP - 10207
EP - 10217
JO - International Journal of Hydrogen Energy
JF - International Journal of Hydrogen Energy
SN - 0360-3199
IS - 21
ER -