continuous reforming catalyst
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1. Hydrothermal stability
2. Regenerated activity
3. Chloride maintenance
4. Higher catalytic activity
| 1. Hydrothermal stability is apparently superior to this industrial catalyst and the present industrial application of CatA and CatB and has reached or even been beyond the level of foreign continuous reforming catalyst of the latest generation in the same period. | |||
| 2. Regenerated activity can recover to live catalyst. | |||
| 3. Reaction performance and the speed of carbon-deposition is similar to higher Pt content R continuous reforming catalyst presently exploited by foreign countries under condition of lower than harshness or higher than harshness. | |||
| 4. Chloride maintenance is superior to the present industrial application of CatA and continuous reforming catalyst. | |||
| 5. Catalytic activity is higher than the present industrial application of CatA, CatB and continuous reforming catalyst can enhance more than 1% on aromatics yield. |
Storage:
| 1. Keep away from water and moisture and strictly forbid to contact with other chemicals or hydrocarbon products. | |||
| 2. Forbid to fall or roll the steel drum during transportation. | |||
| 3. It is in reduction form while out of plant. Pack on fine days, try best to shorten the time catalyst touches the air and seal the reaction vessel immediately after packing and fill nitrogen for protection. | |||
| 4. The feedstock should be controlled with S≤0.5ppm, H2O≤5ppm, As≤1ppb,and the recycle hydrogen should be controlled with H2O≤50ppm during normal production. | |||
| 5 Start-up should be strictly follow the start-up manual of PS-catalyst or under the instruction of professional technical personnel if necessary. |
above is the catalyst 's specific details..
