Hydroprocessing technique
A technology of hydrotreating and process method, applied in refining to remove heteroatoms, etc., can solve the problems of self-heating of sulfided catalyst, unfavorable hydrotreating process, low catalyst production efficiency, etc., and shorten the vulcanization time. , suitable for large-scale use, the effect of improving the vulcanization effect
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Embodiment 1
[0030] The commercial hydrodesulfurization catalyst FH-5A (developed by Fushun Petrochemical Research Institute, produced by Wenzhou Huahua Group Company) was selected. The main composition and properties are shown in Table 1.
[0031] The specific pre-vulcanization process is as follows:
[0032] (1) Add 23 grams of thiourea dioxide to 100 ml of purified water, heat to 60°C, and stir for 15 minutes while heating. The resulting thiourea dioxide solution was stirred for 30 minutes, and purified water was added to 150 ml. Take 200 grams of FH-5A catalyst in oxidation state and add it to a prepared rotatable or vibrating container, and spray the above-mentioned solution. The total amount of the solution is 100 ml. Then rotate or shake for 20 minutes. The immersed material was dried in air at 120°C for 5 hours. Thiourea dioxide accounts for 7.7% of the weight of the catalyst.
[0033] (2) The molten elemental sulfur is introduced into the catalyst contained in step (1), and the elemen...
Embodiment 2
[0036] The oxidation state catalyst is the same as in Example 1, and is FH-5A.
[0037] The vulcanization treatment method is the same as in Example 1, except that 3 g of citric acid is added to the thiourea dioxide solution obtained in step 1. The hydrorefining catalyst EPRES-2 containing sulfiding agent is obtained.
Embodiment 3
[0041] The oxidation state catalyst is the same as in Example 1, and is FH-5A.
[0042] The vulcanization treatment method is the same as in Example 2, except that the thiourea dioxide solution obtained in step 1 is changed to a thiourea solution, and the amount of thiourea accounts for 10% of the weight of the catalyst, and the others remain unchanged. The hydrorefining catalyst EPRES-3 containing sulfiding agent is obtained.
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