Hydrocarbon hydroprocessing technique

A technology for hydrotreating and process method, which is applied in refining to remove heteroatoms and other directions, can solve the problems of unfavorable hydrotreating process, can not completely solve the problem of self-heating of sulfurized catalyst, low catalyst production efficiency, etc., so as to shorten the sulfurization time. , suitable for large-scale use, the effect of improving the vulcanization effect

Active Publication Date: 2008-03-26
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 above 175°C for a period of time, and then activate it with hydrogen to reduce the self-heating problem of the catalyst, but it cannot completely solve the sulfidation state The self-heating problem of the catalyst, and the storage, transportation and loading of the catalyst still have certain problems
In the above-mentioned patents, there is either the problem of self-heating of the catalyst, or the problems of storage, transportation and loading of the catalyst, and there is a problem of low production efficiency in the production of the catalyst, which has an adverse effect on the application of the hydroprocessing process.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0035] 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.

[0036] The specific pre-sulfurization process is as follows:

[0037] 1. Dissolve tetrabutylthiuram disulfide (TBTD) in benzene, evenly impregnate it on the oxidized FH-5A catalyst, and then treat it at 100°C for 3 hours to remove benzene. The TMTD addition is 3% of the catalyst weight, A catalyst supporting TMTD was obtained.

[0038] 2. Introducing molten elemental sulfur into the catalyst obtained in step 1, the amount of elemental sulfur introduced is 105% of the theoretical sulfur requirement of the catalyst. Coked diesel is then introduced in an amount of 40% by weight of the catalyst. Finally, it was treated at 160° C. for 5 hours under normal pressure and in a stagnant air atmosphere to obtain the hydrorefining catalyst EPRES-1 finally c...

Embodiment 2

[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. Dissolve tetramethylthiuram disulfide (TMTD) in benzene, evenly impregnate it on the oxidized FH-5A catalyst, and then evaporate and remove benzene at 100°C. The amount of TMTD added is 5% of the weight of the catalyst , to obtain a catalyst loaded with TMTD.

[0043] 2. Dispersing the elemental sulfur in a solvent with a volume ratio of catalytic cracking gasoline and rapeseed oil of 8:1, the amount of solvent is 12% of the catalyst weight, and the amount of elemental sulfur is 90% of the metal-containing theoretical sulfur required by the catalyst. The catalyst loaded with TMTD obtained in step 1 was impregnated in a solvent of elemental sulfur, and finally treated at 140° C. for 2 hours under nitrogen. The final hydrorefining catalyst EPRES-2 containing a sulfurizing agent was obtained.

Embodiment 3

[0047] The catalyst in the oxidation state is the same as in Example 1, which is FH-5A.

[0048] The specific pre-sulfurization process is as follows:

[0049] 1. Dissolve dithiodimethyldiphenylthiuram in acetone and introduce it into the catalyst in an oxidized state. The amount of dithiodimethyldiphenylthiuram is 20% of the catalyst weight, and then at 105°C Under treatment for 3 hours, a catalyst containing dithiodimethyldiphenylthiuram was obtained.

[0050] 2, vacuum distillate oil and peanut oil volume ratio are the miscible solvent of 1: 2, solvent consumption is 0.5% of catalyst weight, then mixes with elemental sulfur solid powder, elemental sulfur consumption is 40% of catalyzer metal-containing theoretical sulfur demand.

[0051] 3. The material obtained in step 2 was treated at 180° C. for 3 hours under normal pressure and in a stagnant air atmosphere to obtain a hydrorefining catalyst EPRES-3 finally containing a vulcanizing agent.

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PUM

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Abstract

The present invention relates to hydrocarbon hydrotreating process including the steps of loading catalyst into the reactor, activating, reaction, etc. The hydrotreating catalyst contains thiram matter in 0.5-25 wt% of the catalyst, simple substance sulfur in the amount of 30-150 % of the theoretical sulfur demand of the catalyst, and organic solvent in 0.1-50 wt% of the catalyst. The hydrotreating catalyst with the common action of thiram matter, sulfur and organic solvent has high sulfur holding rate in activation, less concentrated heat release, lowered temperature rise in the catalyst bed and high activity. It may be applied in various kinds of hydrocarbon hydrotreating process.

Description

technical field [0001] The invention relates to a hydrocarbon hydrogenation treatment process, in particular to a hydrocarbon hydrogenation treatment process for hydrocarbon raw materials such as impurity removal and upgrading. Background technique [0002] The hydrotreating process generally includes hydrofining and hydroupgrading processes. Generally, in the presence of hydrogen, using a suitable reactor form, under certain operating conditions, the hydrocarbon feedstock and hydrogen are contacted with the hydrotreating catalyst. . Hydrotreating catalysts generally use refractory oxides such as alumina, silicon aluminum, and molecular sieves as carriers, and one or more active metal components such as molybdenum, tungsten, cobalt, and nickel, and sometimes phosphorus, silicon, etc. , fluorine, titanium, zirconium, boron and other auxiliary components. Generally, the metal component of the catalyst obtained in the production process exists in an oxidized state, while in t...

Claims

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Application Information

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IPC IPC(8): C10G45/02
Inventor 高玉兰方向晨王刚曹凤兰李崇慧
Owner CHINA PETROLEUM & CHEM CORP
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