Vulcanization method of selective hydrodesulfurization catalyst of FCC (Fluid Catalytic Cracking) gasoline

A hydrodesulfurization and selectivity technology, applied in catalyst activation/preparation, chemical instruments and methods, metal/metal oxide/metal hydroxide catalysts, etc. In order to achieve the effect of maintaining selectivity, reducing octane number loss, and enhancing the active center of desulfurization

Active Publication Date: 2014-05-07
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0008] The design of the vulcanization pressure in the above patents is carried out under the reaction pressure conditions, and none of them involves the influence of the vulcanization pressure on the activity and selectivity of the catalyst.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0034] Catalyst SHD-1 is selected as the FCC gasoline selective hydrogenation catalyst, the vulcanizing agent is dimethyl disulfide, the vulcanization conditions and process are as follows: the system pressure is 1.8MPa, after passing the airtight inspection, the reactor inlet is raised to 140°C , and then start the feed pump to feed the vulcanized oil, the liquid hourly volume space velocity is 2h -1 . The concentration of dimethyl disulfide in vulcanized oil is 4wt%. After 4 hours of constant temperature, the temperature is raised to 230°C at a rate of 15°C / h. After the temperature rises to 230°C, the temperature is kept constant. 2 After S penetrates the bed, keep the temperature constant for 8 hours. Then adjust the system pressure to 4.5MPa, then raise the temperature to 290°C at a rate of 15°C / h, and keep the temperature constant for 10 hours after the temperature rises to 290°C. After the sulfidation process of the catalyst is completed, the system pressure is reduced...

Embodiment 2

[0040] Catalyst SHD-2 is selected as the FCC gasoline selective hydrogenation catalyst, the system pressure of the low-temperature vulcanization section is 1.6MPa, other process conditions are consistent with embodiment 1, and the process conditions of the high-temperature vulcanization section are: the system pressure is changed to 4.0MPa, and the vulcanization temperature is 300 DEG C, all the other are consistent with embodiment 1.

[0041] The conditions of the FCC gasoline selective desulfurization process test also remain consistent with that of Example 1, and the results are shown in attached table 3.

Embodiment 3

[0046] Catalyst SHD-3 is selected as the FCC gasoline selective hydrogenation catalyst, the process conditions of the low-temperature vulcanization section are consistent with those in Example 1, and the process conditions of the high-temperature vulcanization section are: the system pressure is changed to 5.0 MPa, the vulcanization temperature is 310°C, and the rest are the same as those in Example 1. 1 is consistent.

[0047] The conditions of the FCC gasoline selective desulfurization process test also remain consistent with that of Example 1, and the results are shown in attached table 3.

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Abstract

The invention discloses a vulcanization method of a selective hydrodesulfurization catalyst of FCC (Fluid Catalytic Cracking) gasoline. The method is as follows: in a vulcanization process of the selective hydrodesulfurization catalyst, first vulcanizing under a low pressure and at a low temperature, then vulcanizing under a high system pressure and at a high temperature so as to facilitate production of more CoMoS phases and make the CoMoS phases more dispersive to produce more sulfur vacancies and form more desulfurization centers and promote the formation of the active center of direct desulfurization. The vulcanization method can improve the catalyst desulfurization activity, at the same time, and the olefin saturation properties basically remains unchanged, so that the hydrodesulfurization selectivity of the FCC gasoline is effectively improved. The method can be applied to a variety of hydrodesulfurization catalysts of the FCC gasoline, and is especially suitable for hydrodesulfurization catalysts containing additives with selective desulfurization effect.

Description

technical field [0001] The invention relates to a method for vulcanizing an FCC gasoline selective hydrodesulfurization catalyst, in particular to a method for starting the vulcanization of a hydrodesulfurization catalyst containing a selective desulfurization effect additive. Background technique [0002] With the increasingly stringent environmental protection regulations, developed countries and regions represented by the European Union and the United States have stricter requirements on vehicle exhaust emissions, and have successively issued relevant policies to formulate strict fuel oil quality standards, especially for gasoline products. Sulfur and olefins have strict limits. In 2006, the European Parliament passed Euro IV and Euro V vehicle emission standards. These two standards have more stringent restrictions on vehicle pollutant emissions, especially for dust particles and nitrogen oxide emissions, and the limit requirements have dropped significantly. For the s...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C10G45/08B01J23/888B01J23/885B01J31/34B01J37/20
Inventor 杨成敏孙进段为宇姚运海郭蓉丁莉
Owner CHINA PETROLEUM & CHEM CORP
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