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Preparation method for hydrorefining of catalyst

A catalyst and two-stage hydrogenation technology, applied in chemical instruments and methods, physical/chemical process catalysts, metal/metal oxide/metal hydroxide catalysts, etc. Olefin saturation and poor hydrodesulfurization performance, etc., to achieve the effects of suppressing surface carbon, low start-up temperature, and avoiding environmental pollution

Active Publication Date: 2015-05-13
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0009] The technical problem to be solved by the present invention is the high start-up temperature of the catalyst in the prior art, the problems of colloid resistance, monoolefin saturation and poor hydrodesulfurization performance, and a new preparation method of the hydrorefining catalyst is provided

Method used

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  • Preparation method for hydrorefining of catalyst
  • Preparation method for hydrorefining of catalyst
  • Preparation method for hydrorefining of catalyst

Examples

Experimental program
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Effect test

Embodiment 1

[0018] Take by weighing 300 grams of pseudo-boehmite, 7.5 grams of fenugreek powder, mix, then add 12.5 grams of silica sol, 4.0 grams of nitric acid, 210 milliliters of an aqueous solution of 11.7 grams of 85% phosphoric acid and 4.2 grams of lithium carbonate, and extrude into mm clover, wet strips were dried at 120°C for 4 hours and then calcined at 550°C for 8 hours to obtain carrier Z1. Weigh 30.5 grams of ammonium molybdate, 27.0 grams of nickel nitrate, 18.6 grams of calcium nitrate, 1.39 grams of potassium carbonate, add 90 grams of water and mix to form an impregnation solution. The carrier is impregnated with an equal amount of impregnation solution, dried at 120°C for 18 hours, and calcined at 470°C for 12 hours to obtain Ni-Mo / Al 2 o 3 Catalyst C1 had a final Mo content of 10.3% by weight of the catalyst and a Ni content of 3.4% by weight of the catalyst. The catalyst composition is shown in Table 1, wherein the contents of each component are based on the weight...

Embodiment 2

[0020] Take by weighing 300 grams of pseudo-boehmite, 8.0 grams of asparagus powder, and 5.5 grams of diatomaceous earth, mix them, then add 220 milliliters of an aqueous solution of 4.0 grams of nitric acid and 28.5 grams of boric acid, and extrude into mm clover, wet strips were dried at 120°C for 4 hours and then calcined at 550°C for 16 hours to obtain carrier Z2. Weigh 36.4 grams of ammonium molybdate, 23.4 grams of cobalt acetate, 25.8 grams of magnesium nitrate, 11.5 grams of calcium nitrate, 2.58 grams of potassium carbonate, add 100 grams of water and mix to form an impregnation solution. The carrier was impregnated with an equal amount of impregnating solution, dried at 120°C for 24 hours, and calcined at 470°C for 8 hours to obtain Co-Mo / Al 2 o 3 Catalyst C2 had a final Mo content of 10.3% by weight of the catalyst and a Co content of 3.4% by weight of the catalyst. The catalyst composition is shown in Table 1, wherein the contents of each component are based on t...

Embodiment 3

[0022] Take by weighing 300 grams of pseudo-boehmite, 9.0 grams of fenugreek powder, 1.34 grams of silica gel powder, and 5 grams of silica sol to mix, then add 4.0 grams of nitric acid, 210 milliliters of an aqueous solution of 11.5 grams of phosphoric acid with a concentration of 85%, and 4.6 grams of boric acid, squeeze into mm clover, wet strips were dried at 120°C for 24 hours and then calcined at 620°C for 8 hours to obtain carrier Z3. Weigh 30.5 grams of ammonium molybdate, 5.9 grams of cobalt acetate, 17.5 grams of nickel acetate, 16.7 grams of magnesium nitrate, 3.0 grams of barium nitrate, 1.67 grams of potassium carbonate, add 94 grams of water and mix to form an impregnation solution. The carrier was impregnated with an equal amount of impregnation solution, dried at 120°C for 24 hours, and calcined at 480°C for 16 hours to obtain Co-Ni-Mo / Al 2 o 3 For catalyst C3, the final Mo content was 10.3% by weight of the catalyst, the content of Co was 1.0% by weight of ...

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Abstract

The invention relates to a preparation method for hydrorefining of a catalyst, and mainly aims to solve the technical problems that the starting temperature of the catalyst is high and the colloid resistance, mono-olefin saturation and hydrogen desulfurization performance of the catalyst are poor in the prior art. According to the preparation method, the problems are well solved by adopting the technical scheme which is as follows: the method comprises the following steps of: drying and roasting a preformed transition-state aluminum oxide carrier and one-step soaking ammonia-free solutions of Mo and / or W, Ni and / or Co, K and the like to prepare the catalyst. The preparation method can be used for industrial production for two-stage hydrorefining of a byproduct of pyrolysis gasoline which is generated during preparation of ethylene through steam cracking.

Description

technical field [0001] The present invention relates to a kind of preparation method of hydrorefining catalyst, especially about a kind of 6 ~C 9 +The preparation method of the hydrocarbon compound pyrolysis gasoline two-stage hydrogenation catalyst. Background technique [0002] Utilization of pyrolysis gasoline in ethylene plant is one of the main ways to improve the comprehensive economic benefits of the plant. Due to the complex composition and poor thermal stability of pyrolysis gasoline, it is usually used for the extraction of aromatics after the first stage of selective hydrogenation to remove dienes and styrene, and the second stage of hydrodesulfurization. At present, the catalysts for the second-stage hydrogenation of pyrolysis gasoline in the industry are mainly Co(Ni)-Mo(W) catalysts, and the middle distillate (C 6 ~C 8 hydrocarbon compound fraction) hydrogenation or whole fraction (C 5 Hydrocarbons to hydrocarbon fractions with a dry point of 204°C) hydrog...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J23/887B01J23/888C10G45/08
Inventor 李斯琴朱俊华唐康健程远琳王黎敏
Owner CHINA PETROLEUM & CHEM CORP