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Heavy oil viscosity reduction and desulfurization method based on supercritical methanol

A supercritical methanol and heavy oil technology, which is applied in the fields of hydrocarbon oil cracking, hydrocarbon oil treatment, petroleum industry, etc., can solve the problems of low conversion rate, easy coking of the system, harsh reaction conditions of supercritical fluid processing technology, etc., and achieve the reduction of sulfur and nitrogen The effect of equal heteroatom content, increasing conversion rate and avoiding coking

Pending Publication Date: 2021-12-14
YANAN UNIV
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  • Claims
  • Application Information

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Problems solved by technology

However, this method ignores the influence of supercritical water on equipment materials
[0009] In order to solve the problems of harsh reaction conditions, low conversion rate and easy coking of the system in the current heavy oil supercritical fluid processing technology, a heavy oil viscosity reduction and desulfurization method based on supercritical methanol is provided. Quality reaction, mainly through the control of temperature and pressure, the heavy oil is placed in the supercritical methanol environment for a certain period of time. On the one hand, the supercritical methanol can adjust the dissolving ability of each component in the heavy oil, so that the macromolecules in it are cracked into smaller ones. Molecules, on the one hand, adjust the reaction performance of methanol hydrogen supply, etc., and realize the viscosity reduction and desulfurization of heavy oil under the premise of suppressing coking

Method used

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  • Heavy oil viscosity reduction and desulfurization method based on supercritical methanol
  • Heavy oil viscosity reduction and desulfurization method based on supercritical methanol
  • Heavy oil viscosity reduction and desulfurization method based on supercritical methanol

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example 1

[0063] Raw material heavy oil properties

[0064]

[0065] The reaction temperature is 350°C, the reaction pressure is maintained at 15-22MPa, the reaction time is 60min, the stirring rate is 900rpm, the mass ratio of alcohol to oil is 1:1; the yield of light components is 75wt%, the yield of asphaltene is 21wt%, residual coke is almost negligible, and the mass Conservation 95%. After testing, under the optimal conditions, the content of light product components kept below 350°C is 61wt%, and the viscosity (80°C) drops to 76mPa·s; the S content of the oil product decreases by 37wt%.

[0066] The structural changes of asphaltenes in heavy oil during the reaction were studied by infrared spectroscopy. It shows that the raw material asphaltene undergoes a certain cracking reaction under high temperature conditions, and a certain amount of secondary asphaltenes are produced.

[0067] After thermogravimetric infrared detection, supercritical methanol participated in the reacti...

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Abstract

The invention discloses a heavy oil viscosity reduction and desulfurization method based on supercritical methanol, which is characterized in that heavy oil is subjected to a modification reaction in a supercritical methanol environment, the heavy oil is placed in the supercritical methanol environment for a certain time mainly through temperature and pressure control, on one hand, the dissolving capacity of the supercritical methanol for each component in the heavy oil is adjusted, so that polymerization among macromolecules is inhibited while macromolecules are cracked into small molecules, and on one hand, the reaction performance of methanol hydrogen supply and the like is adjusted, and viscosity reduction and desulfurization of heavy oil on the premise of inhibiting coking are achieved. By adopting the method, the conversion rate and the reaction rate of the heavy oil visbreaking reaction can be improved without a catalyst, the coking phenomenon of the system is avoided, and the content of heteroatoms such as sulfur and nitrogen is reduced.

Description

technical field [0001] The invention relates to the field of heavy oil viscosity reduction and desulfurization, in particular to a heavy oil viscosity reduction and desulfurization method based on supercritical methanol. Background technique [0002] The rapid development of human society since modern times is inseparable from the support of fossil energy. Petroleum resources are currently the most widely used and most demanded energy, and their reserves are decreasing day by day, and their quality is becoming more and more serious. At present, heavy oil products such as oil sand bitumen and super heavy oil are one of the energy sources with the largest reserves in the world. The global storable and recoverable volume is about 400 billion tons, which is 2.7 times that of conventional crude oil. How to make more reasonable and effective use of heavy oil products is very important in the critical period when it is not enough to fully meet the needs of society. [0003] Althou...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C10G47/34C10G45/28
CPCC10G47/34C10G45/28C10G2300/202C10G2300/302
Inventor 闫挺罗璇赵向勃高晓明付峰杨春明王传涛
Owner YANAN UNIV
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