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Hydrogenation catalyst processing method

A technology of hydrogenation catalyst and treatment method, applied in molecular sieve catalysts, chemical instruments and methods, catalyst activation/preparation and other directions, can solve the problem of self-heating of sulfided catalysts, reduce the self-heating of catalysts, etc. effect, reducing the amount of sulfur loss and improving the utilization rate

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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  • Hydrogenation catalyst processing method

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Experimental program
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Effect test

Embodiment 1

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

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

[0027] 1. After the catalyst carrier is impregnated with the active metal solution, it is dried at 80° C. for 2 hours, and the dried product contains 25% water based on the dry weight of the catalyst.

[0028] 2. The elemental sulfur powder is mixed with the catalyst obtained in step 1, and the amount of elemental sulfur introduced is 105% of the theoretical sulfur requirement of the catalyst. It is then mixed with coker diesel fraction, the amount of coker diesel fraction is 45% by weight of the catalyst.

[0029] 3. The catalyst obtained in step 2 was treated at normal pressure and 150° C. for 5 hours to obtain the hydrorefin...

Embodiment 2

[0031] The catalyst in the oxidation state is the same as in Example 1, which is FH-5A.

[0032] The specific pre-sulfurization process is as follows:

[0033] 1. After the catalyst carrier is impregnated with the active metal solution, it is dried at 50° C. for 8 hours, and the dry product contains 10% water based on the dry weight of the catalyst.

[0034] 2. Uniformly impregnating triethylamine on the catalyst obtained in step 1, the addition of triethylamine being 5% of the catalyst weight, to obtain a triethylamine-loaded aqueous catalyst.

[0035] 3. Mix elemental sulfur powder and organic solvent (the organic solvent is a mixture of catalytic cracking gasoline and rapeseed oil with a volume ratio of 8:1), the amount of organic solvent is 15% of the weight of the catalyst, and the amount of elemental sulfur is the theoretical metal content of the catalyst. 105% of the amount of sulfur, the above mixture is mixed with the catalyst loaded with triethylamine obtained in st...

Embodiment 3

[0040] The catalyst in the oxidation state is the same as in Example 1, which is FH-5A.

[0041] The specific pre-sulfurization process is as follows:

[0042] 1. After the catalyst carrier is impregnated with the active metal solution, it is dried at 110° C. for 3 hours, and the dried product contains 0.2% water based on the dry weight of the catalyst.

[0043] 2. Spray triethylamine and gluconic acid in the catalyst obtained in step 1 at a weight ratio of 4:1 to obtain a catalyst containing mixed organic additives.

[0044] 3. The volume ratio of vacuum distillate oil and peanut oil is a mixed solvent of 1:2. The amount of solvent is 0.5% of the catalyst weight. The mixed solvent is first introduced into the catalyst obtained in step 2, and then mixed with elemental sulfur solid powder. The amount of elemental sulfur is The catalyst contains 90% of the theoretical sulfur requirement of the metal.

[0045] 4. The material obtained in step 3 was treated at normal pressure at...

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Abstract

The invention relates to a processing method used for a hydrogenation catalyst, comprising the detailed process as follows: the catalyst carrier is dipped in catalyst active metal component and dried to certain water content; subsequently, organic solvent and elemental sulfur are introduced; and finally, 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 water contained in the catalyst adjusts the interaction of the sulfur and the active composition of 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 for 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 3 S 2 、WS 2 etc...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J37/20B01J23/74B01J23/24B01J29/10C10G45/04
Inventor 高玉兰曹凤兰李崇慧陈光徐黎明
Owner CHINA PETROLEUM & CHEM CORP
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