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Catalytic conversion method for petroleum hydrocarbon

A catalytic conversion method and technology of petroleum hydrocarbons, applied in the field of catalytic conversion of integrated processes, can solve problems such as difficulty in maintaining balanced operation, low sulfur content, and reduced processing efficiency

Active Publication Date: 2015-03-18
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

When the regenerative flue gas treatment unit handles lower levels of SO X When flue gas is used, its treatment efficiency will be reduced
In addition, even though hydrogenated wax oil catalytic cracking produces gasoline with low sulfur content, it is still difficult to reduce the sulfur content in gasoline to below 10 μg / g, and gasoline still needs post-treatment
When S-Zorb technology is used to treat gasoline with low sulfur content, it is difficult to maintain the balanced operation of S-Zorb because the sulfur content in gasoline is too low, and it is necessary to supplement other sulfur compounds from the outside, resulting in a decrease in the use efficiency of the S-Zorb unit

Method used

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  • Catalytic conversion method for petroleum hydrocarbon
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Examples

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Effect test

Embodiment 1

[0066] This example illustrates the product distribution and product properties of raw material A after being treated by a medium-sized catalytic cracking unit and a medium-sized hydrocracking unit using the method provided by the present invention.

[0067]The preheated raw material A is first processed in a medium-sized catalytic cracking unit. The total height of the pre-lifting section, the first reaction zone, the second reaction zone, and the outlet zone of the reactor of the medium-sized catalytic cracking unit is 15 meters, and the diameter of the pre-lifting section is 0.025 meters, its height is 1.5 meters; the diameter of the first reaction zone is 0.025 meters, its height is 4 meters; the diameter of the second reaction zone is 0.1 meters, its height is 6.5 meters; the diameter of the outlet zone is 0.025 meters, its height is 3 meters m; the vertex angle of the isosceles trapezoid in the longitudinal section of the joint of the first and second reaction zones is 45...

Embodiment 2

[0073] This example illustrates the product distribution and product properties of raw material B treated by a medium-sized catalytic cracking unit and a medium-sized hydrocracking unit using the method provided by the present invention.

[0074] The preheated raw material B is first processed in a medium-sized catalytic cracking unit. The total height of the pre-lifting section, the first reaction zone, the second reaction zone, and the outlet zone of the reactor of the medium-sized catalytic cracking unit is 15 meters, and the diameter of the pre-lifting section is 0.025 meters, its height is 1.5 meters; the diameter of the first reaction zone is 0.025 meters, its height is 4 meters; the diameter of the second reaction zone is 0.1 meters, its height is 6.5 meters; the diameter of the outlet zone is 0.025 meters, its height is 3 meters m; the vertex angle of the isosceles trapezoid in the longitudinal section of the joint of the first and second reaction zones is 45°; the base...

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Abstract

A catalytic conversion method for petroleum hydrocarbon. High sulfur wax oil contacts with a zeolite-containing thermal regeneration catalyst at a lower part of a catalytic cracking unit reactor and generates a cracking reaction; the generated oil gas and a carbon-containing catalyst upstream generate a selective hydrogen transfer reaction and an isomerization reaction in a certain reaction environment; the reaction oil gas is separated to obtain reaction products containing liquefied gas, gasoline and catalytic wax oil; the spent catalyst is subjected to stripping and regeneration for recycling; the catalytic wax oil and an optional secondary processing wax oil enter into a hydrocracking unit for reaction; and preferably hydrocracking tail oil returns to the catalytic cracking unit. The method increases the yield and cetane number of diesel, and increases utilization ratio of hydrogen in the raw material, so as to save oil resource and provide a novel path for clean of a refining production process and refining products.

Description

technical field [0001] The invention belongs to a catalytic conversion method of petroleum hydrocarbons, more specifically, relates to a catalytic conversion method of an integrated process of catalytic cracking and hydrocracking of inferior wax oil. Background technique [0002] The processing of high-sulfur low-quality wax oil raw materials by conventional catalytic cracking technology not only makes the SO in catalytic cracking regeneration flue gas X Emissions do not meet environmental requirements, and the sulfur content in gasoline and diesel products does not meet product specifications. Therefore, usually these high-sulfur low-quality wax oil raw materials are first hydrotreated to remove impurities such as sulfur, nitrogen and metals, saturate the polycyclic aromatic hydrocarbons in the raw materials, and improve their catalytic cracking reaction performance, and then use them as raw materials for catalytic cracking to produce low Sulfur gasoline and diesel. [00...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C10G69/00
Inventor 崔守业程从礼唐津莲陈昀胡志海刘四威
Owner CHINA PETROLEUM & CHEM CORP
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