Methane rich city gas has been synthesized by means of steam reforming of naphtha; however, the produced gas always contains significant concentration of CO and CO
2. Therefore, development of a methane production process containing no CO and CO
2 removal processes is strongly requested.
Authors reported in the previous paper that C
3H
8→2CH
4+C(1) took place over Ni/SiO
2 with 90%selectivity. In this paper, the catalyst supports were studied and found that neutral SiO
2 and a-Al
2O
3 are suitable but the activity was much reduced over Ni supported on acidic SiO
2-Al
2O
3. Catalyst was diluted by various materials to avoid blocking-up by the deposited carbon. Several diluted materials affected the conversion. α-Al
2O
3 and basic MgO accelerated the reaction which may be due to interaction between Ni and dilution materials with direct contact. Over Ni/SiO
2, reaction (1) took place with 90%selectivity, so that the produced gas always contained H
2 formed by the C
3H
8→3C+4H
2 (2). It has confirmed that H
2 in a high concentration of CH
4 can be reacted with C
3H
8 to produce CH
4. From these results, a following simple synthesis process can be constituted; the first step is CH
4, H
2, and solid C formation from C
3H
8, and the second step is succeeding H
2 consumption process of the produced gas in the first step.
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