Preparation method of viscous oil hydrothermal cracking catalysis viscosity reducer having double structures of hydrogen supply and metal catalysis center

A metal catalysis and catalytic viscosity reduction technology, applied in chemical instruments and methods, drilling compositions and other directions, can solve problems such as construction equipment and construction process difficulties, achieve broad market application prospects, simple preparation process, strong universality sexual effect

Inactive Publication Date: 2015-08-05
CHINA UNIV OF GEOSCIENCES (WUHAN)
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, in practical applications, the combined use of hydrogen donors and catalytic viscosity reducers will bring certain difficulties to construction equipment and construction techniques

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0024] Raise the temperature of 1mol of tetralin to 150°C, add 1.25mol of concentrated sulfuric acid dropwise for sulfonation, complete the dropwise addition within 1 hour, raise the temperature to 150°C, and react for 2.5 hours to obtain the tetralin sulfonated product; drop in the sulfonated product Add 4mol water, then add 1.2mol Cr 2 o 3 React at 110°C for 1 hour, filter and evaporate to dryness to obtain a heavy oil hydrothermal cracking catalytic viscosity reducer with a hydrogen-donating functional structure.

[0025] The obtained complex aquathermolysis catalytic viscosity reducer with a hydrogen-donating structure, its chemical name is chromium tetrahydronaphthalenesulfonate with a hydrogen-donating structure, wherein tetrahydronaphthalenesulfonic acid is formed from tetrahydronaphthalene through sulfonation reaction Obtained, the metal oxide used is chromium oxide.

[0026] Application: The catalytic viscosity reducer (the product of this example), water and heavy ...

Embodiment 2

[0028] Raise the temperature of 1 mol of tetralin to 145°C, add 1.5 mol of concentrated sulfuric acid dropwise for sulfonation, complete the dropwise addition within 1 hour, raise the temperature to 155°C, and react for 2.5 hours to obtain tetralin sulfonated product; drop in the sulfonated product Add 5mol water and add 1.5molCr 2 o 3 React at 110°C for 1 hour, filter and evaporate to dryness to obtain a heavy oil hydrothermal cracking catalytic viscosity reducer (product) with a hydrogen-donating functional structure. Industrial production can be scaled up with industrial-grade raw materials.

[0029] The obtained complex aquathermolysis catalytic viscosity reducer with a hydrogen-donating structure, its chemical name is chromium tetrahydronaphthalenesulfonate with a hydrogen-donating structure, wherein tetrahydronaphthalenesulfonic acid is formed from tetrahydronaphthalene through sulfonation reaction Obtained, the metal oxide used is chromium oxide.

[0030] Application...

Embodiment 3

[0032] Heat 1 mol of tetralin to 155°C, add 1.25 mol of concentrated sulfuric acid dropwise for sulfonation, complete the dropwise addition within 1 hour, raise the temperature to 165°C, and react for 2 hours to obtain tetralin sulfonated product; add dropwise to the sulfonated product 4mol water, then add 1.2mol Fe 2 o 3 React at 110°C for 1 hour, filter and evaporate to dryness to obtain a heavy oil hydrothermal cracking catalytic viscosity reducer with a hydrogen-donating functional structure.

[0033] The obtained complex aquathermolysis catalytic viscosity reducer with a hydrogen-donating structure, its chemical name is iron tetrahydronaphthalenesulfonate with a hydrogen-donating structure, wherein tetrahydronaphthalenesulfonic acid is formed from tetrahydronaphthalene through sulfonation reaction Obtained, the metal oxide used is iron oxide.

[0034] Application: The catalytic viscosity reducer (the product of this example), water and heavy oil are placed in a high-pre...

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PUM

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Abstract

The present invention discloses a preparation method of a viscous oil hydrothermal cracking catalysis viscosity reducer having double structures of hydrogen supply and metal catalysis center. The preparation method comprises: heating tetrahydronaphthalene to a temperature of 145-155 DEG C, adding concentrated sulfuric acid in a dropwise manner within 1 h, carrying out sulfonation, heating to a temperature of 155-165 DEG C, reacting for 2-3 h to obtain a tetrahydronaphthalene sulfonation product, adding water to the obtained tetrahydronaphthalene sulfonation product, adding a metal oxide, reacting for 1-1.5 h at a temperature of 105-115 DEG C, filtering, and evaporating to obtain the viscous oil hydrothermal cracking catalysis viscosity reducer having the double structures of hydrogen supply and metal catalysis center, wherein the metal oxide is any one selected from chromium oxide, ferric oxide, and nickel oxide. According to the present invention, the catalysis viscosity reducer has the hydrogen supply function, such that the hydrogen protons can be provided while the catalytic viscosity reducer catalyzes the cracking of the viscous oil macromolecule; and the chromium, iron or nickel metal center provides the catalytic cracking effect so as to effectively reduce the viscosity of the viscous oil and improve the quality of the viscous oil.

Description

technical field [0001] The invention belongs to the technical field of heavy oil exploitation, and in particular relates to a method for preparing a heavy oil hydrothermal cracking catalytic viscosity reducer with a double structure of hydrogen supply and metal catalytic center. Background technique [0002] With the reduction of conventional 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, add a suitable catalyst to the oil layer to irreversibly convert part of the heavy component macromolecules into small molecules, so that Its viscosity is reduced and it is easy to extract. The key to this technology lies i...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C09K8/592
CPCC09K8/592
Inventor 陈艳玲安永王普键李国锐陈宇
Owner CHINA UNIV OF GEOSCIENCES (WUHAN)
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