Bibliographic Details
Title: |
Impact of Thickness of Pd/Cu Membrane on Performance of Biogas Dry Reforming Membrane Reactor Utilizing Ni/Cr Catalyst |
Authors: |
Akira Nishimura, Syogo Ito, Mizuki Ichikawa, Mohan Lal Kolhe |
Source: |
Fuels, Vol 5, Iss 3, Pp 439-457 (2024) |
Publisher Information: |
MDPI AG, 2024. |
Publication Year: |
2024 |
Collection: |
LCC:Fuel |
Subject Terms: |
biogas dry reforming, Ni/Cr catalyst, thickness of Pd/Cu membrane, optimum experimental conditions, Fuel, TP315-360 |
More Details: |
The present study pays attention to biogas dry reforming for the purpose of producing H2. It is known that biogas contains approximately 40 vol% CO2, causing a decrease in the efficiency of power generation due to its lower heating value compared to natural gas, i.e., CH4. We suggest a hybrid system composed of a biogas dry reforming membrane reactor and a high-temperature fuel cell, i.e., a solid oxide fuel cell (SOFC). Since biogas dry reforming is an endothermic reaction, we adopt a membrane reactor, controlled by providing a non-equilibrium state via H2 separation from the reaction site. The purpose of the present study is to understand the effect of the thickness of the Pd/Cu membrane on the performance of the biogas dry reforming membrane reactor with a Pd/Cu membrane as well as a Ni/Cr catalyst. The impact of the reaction temperature, the molar ratio of CH4:CO2 and the differential pressure between the reaction chamber and the sweep chamber on the performance of the biogas dry reforming membrane reactor with the Pd/Cu membrane as well as the Ni/Cr catalyst was investigated by changing the thickness of the Pd/Cu membrane. It was revealed that we can obtain the highest concentration of H2, of 122,711 ppmV, for CH4:CO2 = 1:1 at a reaction temperature of 600 °C and a differential pressure of 0 MPa and using a Pd/Cu membrane with a thickness of 40 μm. Under these conditions, it can be concluded that the differential pressure of 0 MPa provides benefits for practical applications, especially since no power for H2 separation is necessary. Therefore, the thermal efficiency is improved, and additional equipment, e.g., a pump, is not necessary for practical applications. |
Document Type: |
article |
File Description: |
electronic resource |
Language: |
English |
ISSN: |
2673-3994 |
Relation: |
https://www.mdpi.com/2673-3994/5/3/24; https://doaj.org/toc/2673-3994 |
DOI: |
10.3390/fuels5030024 |
Access URL: |
https://doaj.org/article/3b6106be63a84abfa43380c1cdf9bf41 |
Accession Number: |
edsdoj.3b6106be63a84abfa43380c1cdf9bf41 |
Database: |
Directory of Open Access Journals |