Naphtha catalytic reforming method of by-product reduction hydrogen
A catalytic reforming and naphtha technology, which is applied in the treatment of naphtha, petroleum industry, and hydrocarbon oil, etc., can solve the problems of large amount of activated carbon and low utilization rate of equipment, and overcome the problems of large amount of use and process operation. flexible effects
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Embodiment 1
[0045] When it is necessary to prepare hydrogen storage for reforming and reduction, it is assumed that "preparing reduced hydrogen for reforming" is carried out at the end of an operation cycle. Taking the reforming reactor 10 as an example, the reactor 10 is first cut out of the process, and the The reforming catalyst in the reactor 10 is regenerated. The remaining 3 reactors continue to carry out the reforming reaction, and the materials go through process 2.
[0046] It can be seen from Table 3 that the catalytic reforming reaction conditions of Example 1 are: weighted average temperature 484.9°C, reaction pressure 1.33MPa, volume space velocity 1.59h -1 , The volume ratio of hydrogen to oil is 1200. The resulting oil had an octane number of 93.9.
[0047] As can be seen from Table 4, after hydrogenolysis, C 2 + The hydrocarbon content was 0.06% by volume.
Embodiment 2
[0049] Material flow process is identical with embodiment 1.
[0050] It can be seen from Table 3 that the catalytic reforming reaction conditions of Example 2 are: weighted average temperature 486.6°C, reaction pressure 1.33MPa, volume space velocity 1.73h -1 , The volume ratio of hydrogen to oil is 1200. The resulting oil had an octane rating of 94.0.
[0051] As can be seen from Table 4, after hydrogenolysis, C 2 + The hydrocarbon content was 0.12% by volume.
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