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Process and device for preparing oil product by mixing oil slurry, recycle oil and coker gas oil

A technology of coking wax oil and re-refined oil, which is applied in the direction of multi-stage series refining process treatment, petroleum industry, and hydrocarbon oil treatment, can solve the problem of large utilization space, reduction of CGO nitrogen content and polycyclic aromatic hydrocarbon content, and no FCC oil slurry and re-refined oil treatment methods, etc., to achieve the effect of reducing unit consumption, reducing the circulation ratio and the re-refining ratio of the catalytic unit, and the process requires low temperature and pressure

Active Publication Date: 2021-06-18
CHINA UNIV OF PETROLEUM (BEIJING)
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0009] CN133338A discloses a combined process for producing high-quality catalytic cracking raw materials, combining coking and lubricating oil extraction, extracting CGO with lubricating oil extract, and obtaining CGO Nitrogen content and condensed ring aromatics content are significantly reduced, providing high-quality raw materials for FCC units, but the article does not mention FCC oil slurry and back refining oil treatment methods
FCC oil slurry, FCC re-refined oil and coker wax oil produced from naphthenic crude oil contain a large amount of polycyclic naphthenes. There are fewer related reports and a large space for utilization

Method used

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  • Process and device for preparing oil product by mixing oil slurry, recycle oil and coker gas oil
  • Process and device for preparing oil product by mixing oil slurry, recycle oil and coker gas oil
  • Process and device for preparing oil product by mixing oil slurry, recycle oil and coker gas oil

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Embodiment

[0054] This embodiment provides a process device for preparing oil products by mixing oil slurry, re-refined oil and coker wax oil, such as figure 1 As shown, the device includes:

[0055] Primary extraction tower 1, secondary extraction tower 2, first stripping tower 3, second stripping tower 4, third stripping tower 5 and fourth stripping tower 6, mixing tank 7, catalytic cracking unit 8, delay A coking device 9 , a first delivery pump 10 , a second delivery pump 11 , a third delivery pump 12 and a fourth delivery pump 13 .

[0056] The primary extraction tower 1 is used to extract the mixed oil of catalytic cracking oil slurry, re-refined oil and coker wax oil; Aromatic oil; the second stripper 4 is used for stripping the primary raffinate obtained by the primary extraction tower 1 extraction, thereby obtaining the primary raffinate; the secondary extraction tower 2 is used for extracting the primary raffinate; the second The third stripper 5 is used for stripping the sec...

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Abstract

The invention provides a process and a device for preparing an oil product by mixing oil slurry, recycle oil and coker gas oil. The process comprises the following steps: mixing oil slurry generated by a catalytic cracking process, recycle oil and coker gas oil generated by a delayed coking process to obtain mixed oil, and carrying out a two-stage extraction process on the mixed oil, wherein extracting agent dimethyl sulfoxide is adopted in the first-stage extraction, and first-stage extraction liquid and first-stage raffinate are obtained after extraction; performing steam stripping on the first-stage extraction liquid to obtain aromatic hydrocarbon-rich oil, and performing steam stripping on the first-stage raffinate to obtain first-stage raffinate oil, wherein the first-stage raffinate oil is subjected to second-stage extraction, extraction agent N, N-dimethylacetamide is adopted for second-stage extraction, and second-stage extraction liquid and second-stage raffinate are obtained after extraction; and performing steam stripping on the secondary extraction liquid to obtain olefin and aromatic hydrocarbon, and performing steam stripping on the secondary raffinate to obtain oil rich in saturated hydrocarbon. According to the method, three oil products are firstly mixed and extracted, an extraction phase is used for producing carbon materials such as asphalt blend oil and needle coke, and a raffinate phase is used as a catalytic raw material or is used for producing lubricating oil through hydrogenation.

Description

technical field [0001] The invention belongs to the technical field of oil product processing and relates to a process and a device for preparing oil products by mixing oil slurry, re-refined oil and coker wax oil. Background technique [0002] Fluid catalytic cracking (FCC) is an important secondary processing technology for heavy oil in my country. The processing raw materials are atmospheric residue, vacuum gas oil, vacuum residue and coking gas oil, and a certain proportion (generally 0.3 ~0.7) oil slurry and re-refined oil; products are gas, liquefied gas, gasoline and diesel. As the quality of crude oil deteriorates, the properties of catalytic raw materials also become worse and worse, and the amount of slurry thrown out of the FCC unit gradually increases. [0003] Catalytic cracking oil slurry is rich in a large amount of polycyclic aromatic hydrocarbons, and the content of aromatic hydrocarbons is 20% to 50%. Polycyclic aromatic hydrocarbons (three-ring aromatics a...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C10G53/04
CPCC10G53/04C10G2300/4006C10G2300/4012C10G2300/44
Inventor 热则耶·热合米图力彭威曹玉骁李楠刘艳升
Owner CHINA UNIV OF PETROLEUM (BEIJING)
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