Preparation method for vulcanization type hydrogenation catalyst

A hydrogenation catalyst and sulfurized type technology are applied in the field of preparation of sulfurized hydrogenation catalysts, and can solve the problems of equipment damage safety, complex and incomplete preparation process, etc.

Active Publication Date: 2012-12-26
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] Conventional catalyst vulcanization methods use "in-vessel" vulcanization or "in-situ" vulcanization, that is, the catalyst in the oxidized state is first loaded into the hydrogenation reactor, and then hydrogen and sulfurizing agent are introduced into the reactor during the process of continuous heating. Pre-sulfurization, this method brings the following problems: (1) special pre-sulfurization equipment should be set up on the hydrogenation unit; (2) the vulcanizing agent added during the vulcanization process and the water and hydrogen sulfide generated by the reaction can easily cause high pressure Corrosion of reactors and related equipment, resulting in equipment damage and potential safety hazards; (3) The vulcanization process is longer, delaying the start-up time
(4) The vulcanizing agent used is flammable and toxic, and pollutes the environment during the vulcanization process; (5) The cost of pre-vulcanization in the device is relatively high
The above-mentioned methods all carry out pre-sulfurization treatmen

Method used

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  • Preparation method for vulcanization type hydrogenation catalyst
  • Preparation method for vulcanization type hydrogenation catalyst
  • Preparation method for vulcanization type hydrogenation catalyst

Examples

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Embodiment 1

[0028] The invention involves catalyst CATA.Called 120g of unskilled silicon aluminum, 33GY molecular sieve (SIO 2 / Al 2 O 3 Moorebi is 40, crystal cell constant is 2.432nm, and infrared acidity 0.19mmol / g, which is 866m than the surface area 2 / g, Kong Rong 0.52ml / g), 48g nickel nitrate and 67g tetosulfonal molybdenonate, together in a roller, mix it evenly, and then add 180gConcise, mixing, crushing, making a squeeze paste, squeezing strips formed.Under the protection of nitrogen, it was dried for 6 hours at 120 ° C and 4 hours of roasting at 500 ° C.

Embodiment 2

[0030] The invention involves catalyst CATB.Called 125g unspecified silicon aluminum, 33GY molecular sieve (the same as the embodiment 1), 40g nickel nitrate and 94g tipotesulfed tungstenate, together with a mixing in a roller, then add 180gThe adhesive made of glue dissolves, mixed, crushed, and made into a squeeze paste, squeezing strip molding.Under the protection of nitrogen, it was dried for 6 hours at 110 ° C and 480 ° C for 4 hours.

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Abstract

The present invention discloses a preparation method for a vulcanization type hydrogenation catalyst. The preparation method comprises: uniformly mixing a carrier precursor, a thiomolybdate and/or thiotungstate, a nickel salt and/or a cobalt salt, adding a binder to carry out kneading, carrying out molding, and then carrying out drying and calcination in the protection of an inert gas to prepare the catalyst. The method of the present invention has characteristics of simple process and high vulcanization degree, wherein the prepared vulcanization type hydrogenation catalyst has high activity and high selectivity.

Description

Technical field [0001] The present invention involves a preparation method for a sulfide hydrogenation catalyst. Background technique [0002] In recent years, with the decline in oil reserves, international oil prices have risen, and the trend of heavy quality and inferiority of crude oil has become more and more serious.Therefore, it is particularly important to increase production of intermediate distillation oil, increase the increasing firewood ratio, and improve the contradiction of this supply and demand. The key to solving this contradiction is to develop a catalyst with high hydrogenation catalyst with high hydrogenation of the intermediate distillation oil type.At present, most of the metal active components of hydrogenation catalysts in industrialized exist in the form of oxides, and actual metal oxides on the catalyst need to be converted into sulfides during actual use.Called pre -sulfide. [0003] Conventional catalytic vulcanization method adopts "inner" vulcanizat...

Claims

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Application Information

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IPC IPC(8): B01J29/16B01J27/051B01J27/049C10G47/20
Inventor 孙晓艳樊宏飞王占宇
Owner CHINA PETROLEUM & CHEM CORP
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