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Processing method before using hydrogenation catalyst

A technology of hydrogenation catalyst and treatment method, which is applied in chemical instruments and methods, catalyst activation/preparation, physical/chemical process catalyst, etc., can solve the problem of self-heating of sulfided catalysts, and reduce the self-heating of catalysts. Achieve the effect of improving vulcanization effect, reducing sulfur loss and reducing side reactions

Active Publication Date: 2009-04-29
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

CN1400056A Coat the pre-sulfurized catalyst containing sulfidation agent with oxygen-containing organic matter containing at least 16 carbon atoms, treat it for a period of time above 175 ° C, and then activate it with hydrogen to reduce the self-heating of the catalyst, but it cannot completely solve the problem of sulfide catalyst There are still some problems in the storage, transportation and loading of the catalyst.
USP6059956 (CN1076635C) is used to contain olefin or olefin cut fraction such as under the presence of vegetable oil, introduce elemental sulfur and organic polysulfide into catalyst, then activate with hydrogen, passivate with oxygen-containing gas at last, although this method can improve catalyst activity, but Since the metal on the catalyst is in a sulfide state, the same problem as above still exists

Method used

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  • Processing method before using hydrogenation catalyst

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Experimental program
Comparison scheme
Effect test

Embodiment 1

[0025] The commercial hydrodesulfurization catalyst FH-5A (developed by Fushun Petrochemical Research Institute and produced by Wenzhou Huahua Group Co., Ltd.) was selected. The main composition and properties are shown in Table 1.

[0026] The specific pre-sulfurization process is as follows:

[0027] 1. The elemental sulfur powder is mixed with the oxidized catalyst, and the amount of elemental sulfur introduced is 105% of the theoretical sulfur demand of the catalyst. Then mix and impregnate with the mixed emulsion of coked diesel oil fraction and water, the amount of coked diesel oil fraction is 45% of the weight of the catalyst, and the amount of water is 25% of the weight of the catalyst.

[0028] 2. The catalyst obtained in step 1 was treated at normal pressure and 150° C. for 5 hours to obtain the hydrorefining catalyst EPRES-1 finally containing a sulfurizing agent.

Embodiment 2

[0030] The catalyst in the oxidation state is the same as in Example 1, which is FH-5A.

[0031] The specific pre-sulfurization process is as follows:

[0032] 1. Uniformly impregnate triethylamine on the oxidized FH-5A catalyst, and the addition amount of triethylamine is 5% of the catalyst weight to obtain a catalyst loaded with triethylamine.

[0033] 2. Mix elemental sulfur powder, water, and organic solvent (the organic solvent is a mixture of catalytically cracked gasoline and rapeseed oil with a volume ratio of 8:1) to form an emulsion. The amount of organic solvent is 15% of the weight of the catalyst, and the amount of water is 1% of the catalyst weight. 10% by weight, and the amount of elemental sulfur is 105% of the theoretical sulfur requirement of the catalyst containing metal, and the above emulsion is mixed with the catalyst loaded with triethylamine obtained in step 1.

[0034] 3. The catalyst obtained in step 2 was treated at 0.3 MPa and 160° C. for 8 hours t...

Embodiment 3

[0038] The catalyst in the oxidation state is the same as in Example 1, which is FH-5A.

[0039] The specific pre-sulfurization process is as follows:

[0040] 1. Dissolve triethylamine and gluconic acid in ammonia water containing 8wt% ammonia in a weight ratio of 4:1, impregnate the catalyst in the oxidation state with the solution, the amount of the above substances is 15% of the weight of the catalyst, and then dry at 130°C for 4 hours, a catalyst containing mixed organic additives was obtained.

[0041] 2. The mixed solvent of vacuum distillate oil and peanut oil with a volume ratio of 1:2 is mixed with water to form an emulsion. The amount of solvent used is 0.5% of the weight of the catalyst, and the amount of water used is 0.2% of the weight of the catalyst. The emulsion is first introduced into the catalyst in an oxidized state. Then it is mixed with elemental sulfur solid powder, and the amount of elemental sulfur is 90% of the theoretical required sulfur amount of ...

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Abstract

The invention relates to a processing method before the application of hydrogenation catalyst, comprising the detailed process as follows: organic solvent, elemental sulfur and water are introduced in oxidated hydrogenation catalyst; subsequently, heating predisposal is carried out under a certain condition. The processing method before the application of the hydrogenation catalyst loads the sulfur-contained substance such as the elemental sulfur to the hydrogenation catalyst; a certain interaction is generated and little heat is discharged; and the water vapor which is generated during the heat disposal process of the added water adjusts the interaction of the sulfur and the catalyst and reduces the heat discharging degree during the heat disposal process. Compared with the prior art, the catalyst obtained by the method has the advantages of high utilization ratio of the sulfur-contained matter, gradual increment of the temperature of the catalyst bed and high activity of the catalyst when the activation is applied. The method can be used for processing before the application of various hydrogenation catalysts.

Description

technical field [0001] The invention relates to a treatment method before application of a hydrogenation catalyst, in particular to a treatment method for introducing elemental sulfur into other devices outside the reactor before the catalyst is used for hydrogenation reaction. Background technique [0002] Hydrofining, hydrotreating, hydrocracking and other hydrogenation catalysts generally use alumina, silicon aluminum, molecular sieve and other refractory oxides as carriers, and one or more active metal groups such as molybdenum, tungsten, cobalt, nickel, etc. Sometimes, the catalyst can also contain auxiliary components such as phosphorus, silicon, fluorine, titanium, zirconium, and boron. Generally, the metal component of the catalyst obtained in the production process exists in an oxidized state, while in the hydrogenation reaction process, the active metal component of the catalyst is in a sulfide state (the metal exists in the form of sulfide: Co 9 S 8 、MoS 2 、Ni ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J37/20B01J23/74B01J23/24C10G45/04
Inventor 高玉兰曹凤兰李崇慧陈光徐黎明
Owner CHINA PETROLEUM & CHEM CORP
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