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Preparation method of heavy oil aquathermolysis catalytic viscosity reducer with hydrogen-donating double-ligand structure

A catalytic viscosity-reducing, double-ligand technology, applied in chemical instruments and methods, drilling compositions, etc., to achieve the effects of reducing the viscosity of heavy oil, strong universality, and improving the quality of heavy oil

Inactive Publication Date: 2017-06-13
CHINA UNIV OF GEOSCIENCES (WUHAN)
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Due to the inductive effect and conjugation effect of the nitrogen on the pyridine ring, the ortho- and para-picolines can stabilize the charges at the ortho- and para-positions, so the ortho- and para-picolines have side chains α-H that are more active than toluene, and the ortho- and para-picolines There is no literature report on the use of picoline as a hydrogen donor in heavy oil catalytic cracking for viscosity reduction.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0024] Preparation: Mix 1 mol of lauric acid, 0.8 mol of copper hydroxide and 8 mol of methanol and heat to 80°C, reflux and stir for 2 hours, add 1.2 mol of o-picoline dropwise, continue stirring for 0.5 hours, filter while hot, spin the filtrate to dry and recover methanol, A heavy oil hydrothermolysis catalytic viscosity reducer with hydrogen-donating double-ligand structure was obtained. Industrial production can be scaled up with industrial-grade raw materials.

[0025] Application: The product of this example is applied to Liaohe Oilfield ultra-heavy oil (viscosity is 170000mPa·s at 50°C), the catalytic viscosity reducer (product of this example), water and heavy oil are placed in a high-pressure reactor, and the A hydrothermal catalytic cracking reaction occurs at 240°C, wherein based on the mass of the entire system, the amount of viscosity reducer accounts for 0.2 to 0.3 wt% (mass percentage), and the amount of water accounts for 25 to 40 wt% (mass percentage); The o...

Embodiment 2

[0027] Preparation: Mix 1.2 mol of myristic acid, 0.8 mol of copper hydroxide and 9 mol of methanol, heat to 85°C, reflux and stir for 2.5 h, add 1.2 mol of o-picoline dropwise, continue stirring for 0.5 h, filter while hot, and spin the filtrate to dry. Methanol is recovered to obtain a heavy oil hydrothermolysis catalytic viscosity reducer with hydrogen-donating double-ligand structure. Industrial production can be scaled up with industrial-grade raw materials.

[0028] Application: The product of this example is applied to super heavy oil in Shengli Oilfield (viscosity is 180000mPa·s at 70°C), the catalytic viscosity reducer (product of this example), water and heavy oil are placed in a high-pressure reactor, and the A hydrothermal catalytic cracking reaction occurs at 240°C, wherein based on the mass of the entire system, the amount of viscosity reducer accounts for 0.2 to 0.3 wt% (mass percentage), and the amount of water accounts for 25 to 40 wt% (mass percentage); The ...

Embodiment 3

[0030] Preparation: Mix 1.5mol palmitic acid, 1mol copper hydroxide and 10mol methanol and heat to 90°C, reflux and stir for 3h, add 1.5mol p-picoline dropwise, continue stirring for 1h, filter while hot, spin the filtrate to dry and recover methanol to obtain A hydrothermal cracking catalytic viscosity reducer for heavy oil with hydrogen-donating double-ligand structure. Industrial production can be scaled up with industrial-grade raw materials.

[0031] Application: The product of this embodiment is applied to Liaohe Oilfield extra heavy oil (viscosity is 40000mPa·s at 50°C), the catalytic viscosity reducer (product of this embodiment), water and heavy oil are placed in a high-pressure reactor, and the A hydrothermal catalytic cracking reaction occurs at 240°C, wherein based on the mass of the entire system, the amount of viscosity reducer accounts for 0.2 to 0.3 wt% (mass percentage), and the amount of water accounts for 25 to 40 wt% (mass percentage); The oil viscosity re...

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Abstract

The invention discloses a preparation method of a heavy oil hydrothermal cracking catalytic viscosity reducer with a hydrogen-donating double-ligand structure. Mix long-chain carboxylic acid, copper hydroxide and methanol, heat to 80-90°C, reflux and stir for 2-3 hours; add picoline dropwise, continue stirring for 0.5-1 hour; filter while hot, spin the filtrate and recover methanol to obtain Hydrogen-donating double-ligand structure heavy oil aquathermal cracking catalytic viscosity reducer; the molar ratio of long-chain carboxylic acid, copper hydroxide, picoline and methanol is (1-1.5): (0.8-1): (1.2-1.5 ): (8~10). The viscosity reducer can be used for hydrothermal cracking catalytic viscosity reduction of extra-heavy oil and super-heavy oil. The viscosity reduction effect is good at a temperature of 240 ° C. The preparation process is simple, and it has strong universality for different types of heavy oil. Good practicability and broad market application prospects.

Description

technical field [0001] The invention relates to a preparation method of a hydrothermal cracking catalytic viscosity reducer with a hydrogen-donating double-ligand structure used in the exploitation of heavy oil. Background technique [0002] With the reduction of high-quality oil reserves, more and more attention has been paid to the exploitation of abundant heavy oil. However, due to the complex molecular structure, high content of heavy components, high freezing point and high viscosity of heavy oil, its exploitation is still a difficult problem in the world. Hydrothermal cracking catalytic viscosity reduction is a very potential ultra-heavy oil recovery method. While injecting steam, a suitable catalyst is given to the oil layer to irreversibly convert some heavy component macromolecules into small molecules. The viscosity is reduced and easy to extract. The technical key lies in the effective hydrothermal cracking catalytic viscosity reducer. [0003] Commonly used hy...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C09K8/592
Inventor 陈艳玲范大林李国锐陈宇安永
Owner CHINA UNIV OF GEOSCIENCES (WUHAN)