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Method for graded modification of thickened oil

A heavy oil and upgrading technology, which is applied in the treatment of hydrocarbon oil, hydrocarbon oil cracking, petroleum industry, etc., can solve the unsolved problems of pipeline or reactor blockage, shorten the residence time of each stage of reaction, and have no graded treatment, etc., to achieve Viscosity reduction, toxicity reduction effects

Active Publication Date: 2022-07-26
CNOOC TIANJIN CHEM RES & DESIGN INST +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

This patent prevents pipeline clogging by using drainage containing water and initial hydrocarbons, but only prevents possible clogging before the normal operation of the device, and does not solve the problem of pipeline or reactor clogging caused by the formation of coke particles in supercritical reforming
[0008] It can be seen that with regard to supercritical water pyrolysis technology for upgrading heavy oil, there is no technology that utilizes the different pyrolysis effects of near-critical water, supercritical water and ultra-supercritical water to classify heavy oil. The residence time of each level of reaction is controlled, and the amount of coke is controlled

Method used

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  • Method for graded modification of thickened oil
  • Method for graded modification of thickened oil
  • Method for graded modification of thickened oil

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0052] According to the method of the present invention, the heavy oil is upgraded by classification and pyrolysis. A set of vertical tube type three-stage pyrolysis reaction equipment is used, which consists of three pyrolysis reactors connected in series. The first-stage pyrolysis reactor is a near-critical water reactor, and the second-stage pyrolysis reactor is a supercritical water reaction. The third-stage pyrolysis reactor is an ultra-supercritical water reactor, and there is a cyclone separator behind each pyrolysis reactor. The main body of the pyrolysis reactor is a single standpipe, which is fed from the inlet at the lower end and discharged from the outlet at the upper end. The pressures in the three pyrolysis reactors were controlled by three back pressure valves, respectively.

[0053] The deionized water flow was connected, and the heating temperature of the deionized water was 60 °C. The temperature of the near-critical water reactor was controlled to be 340°...

Embodiment 2

[0055] According to the method of the present invention, the heavy oil is upgraded by classification and pyrolysis. A set of vertical tube type three-stage pyrolysis reaction equipment is used, which consists of three pyrolysis reactors connected in series. The first-stage pyrolysis reactor is a near-critical water reactor, and the second-stage pyrolysis reactor is a supercritical water reaction. The third-stage pyrolysis reactor is an ultra-supercritical water reactor, and there is a cyclone separator behind each pyrolysis reactor. The main body of the pyrolysis reactor is a single standpipe, which is fed from the inlet at the lower end and discharged from the outlet at the upper end. The pressures in the three pyrolysis reactors were controlled by three back pressure valves, respectively.

[0056] The difference from Example 1 is that the deionized water flow and the heavy oil raw material flow are simultaneously connected, the heating temperature of the heavy oil is 60°C, ...

Embodiment 3

[0058] According to the method of the present invention, the heavy oil is upgraded by classification and pyrolysis. A set of vertical tube type three-stage pyrolysis reaction equipment is used, which consists of three pyrolysis reactors connected in series. The first-stage pyrolysis reactor is a near-critical water reactor, and the second-stage pyrolysis reactor is a supercritical water reaction. The third-stage pyrolysis reactor is an ultra-supercritical water reactor, and there is a cyclone separator behind each pyrolysis reactor. The main body of the pyrolysis reactor is a single standpipe, which is fed from the inlet at the lower end and discharged from the outlet at the upper end. The pressures in the three pyrolysis reactors were controlled by three back pressure valves, respectively.

[0059] A stream of deionized water was introduced, and the heating temperature of the deionized water was 70 °C. The temperature of the near-critical water reactor was controlled to be ...

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Abstract

The invention discloses a method for graded modification of thickened oil, which comprises the following steps: heating and pressurizing a mixed solution of the thickened oil and water, carrying out pyrolytic reaction on the thickened oil in a near-critical water reactor, and breaking easily-broken carbon-sulfur bonds in macromolecules of the thickened oil and carbon-carbon bonds on aromatic ring branched chains to generate small molecules; heavy component oil which is difficult to react in the near-critical water is separated out through cyclone separation and conveyed to a supercritical water reactor, and the heavy component oil is subjected to pyrolytic reaction under the action of the supercritical water, a hydrogen donor and a catalyst; super-heavy component oil which is difficult to react in the supercritical water is separated out by cyclone and is subjected to pyrolytic reaction with the ultra-supercritical water, and a gas phase flow obtained by the three-stage pyrolytic reaction is separated for multiple times to obtain cracked gas and modified oil. According to the method, the thickened oil and the super-thickened oil can be converted to the maximum extent, more light oil products are generated, the viscosity is remarkably reduced, the pipeline conveying and shipping requirements can be met, meanwhile, part of impurities such as nickel and vanadium in the thickened oil are removed, and the toxic action on a catalyst in the oil refining processing link is reduced.

Description

technical field [0001] The invention relates to the technical field of heavy oil upgrading, in particular to a treatment method for graded upgrading heavy oil by utilizing near-critical water, supercritical water and ultra-supercritical water. Background technique [0002] In the global oil resources, more than 70% of the geological reserves are heavy oil resources. With the continuous decline of the recoverable reserves of light crude oil, heavy oil resources are gradually becoming more important to the world's energy security. For countries with rich heavy oil resources such as Venezuela and Canada, the development of heavy oil resources exploitation, processing and transportation technology is highly valued. my country's Xinjiang Oilfield, Liaohe Oilfield and Bohai Oilfield also have a large number of heavy oil resources that have not been exploited on a large scale. The current exploitation cost is high, the exploitation is difficult, and the processing process has probl...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C10G69/00C10G9/00C10G47/02C10G47/04C10G47/06C10G47/32C10G47/34
CPCC10G69/00C10G9/00C10G9/007C10G47/34C10G47/32C10G47/02C10G47/04C10G47/06Y02P20/54
Inventor 范景新辛利李福双于海斌臧甲忠冯钰润薛同晖张永惠
Owner CNOOC TIANJIN CHEM RES & DESIGN INST
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