Catalytic hydrogenation method and catalytic hydrogenation apparatus for coal tar
A technology for catalytic hydrogenation and coal tar, applied in the field of coal chemical industry, can solve problems such as increased processing cost, environmental damage, and reduced yield of final products, and achieves the effects of saving equipment investment, prolonging the start-up period, and reducing operating costs.
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[0038] Preparation of the catalyst slurry. The role of the catalyst slurry is to add an appropriate amount of catalyst 12 and additives 13 to the heavy oil fraction to prepare for the catalytic hydrocracking reaction. There are three ways to prepare the catalyst slurry. The first way is to separate a small part from the heavy oil fraction 11 and add catalysts and additives to this part of the heavy oil fraction; the second way is to add catalysts and additives to all or part of the circulating tail oil. ; The third way is to separate a small part from the heavy oil fraction and mix it with all or part of the circulating tail oil and add catalysts and additives; then fully mix it under normal pressure and at a temperature of 80℃-200℃ to make a catalyst slurry. The weight percentage of solid matter in the catalyst oil slurry is 20-45%, preferably 25-40%.
[0039] Mix the catalyst oil slurry with the remaining heavy oil fraction (if it is the catalyst oil slurry obtained by route tw...
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[0046] Example 1
[0047] A typical coal tar is selected as the test raw material, and the test scale is 100.0 kg coal tar / day. The pretreatment and distillation are carried out according to step 1. The product status is shown in the following table:
[0048]
[0049] The pretreated coal tar is separated into heavy fractions at IBP~230℃, 230~370℃ and over 370℃ through distillation. The heavy distillate oil over 370℃ is used as the raw material of the suspended bed hydrogenation reactor for lightening reaction.
[0050] According to the above step 2, a small part of the circulating tail oil and a small part of the heavy oil fraction, together with the catalyst and sulfiding agent, are used to prepare a catalyst slurry at 80°C. The solid concentration of the catalyst slurry is about 25% . The catalyst used is a powdery molybdenum-iron composite catalyst with a particle size of less than 100 μm, and the molybdenum: iron is equal to 1:500 (weight ratio), and the vulcanizing agent is dim...
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