Preparation method of low-temperature thickened oil hydrothermal cracking viscosity-reduction catalyst

A thermal cracking and catalyst technology, applied in chemical instruments and methods, physical/chemical process catalysts, cracking, etc., can solve problems such as complex construction process, increased burden, and damage to crude oil quality, achieve good catalytic effect, facilitate promotion, and operate simple effect

Inactive Publication Date: 2018-06-29
XI'AN PETROLEUM UNIVERSITY
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

At present, this technology has gradually begun to be applied, and my country has also carried out large-scale tests in Liaohe Oilfield, Nanyang Oilfield and other places, but the core catalytic system in this technology is oil-soluble transition metal salts (such as nickel oleate, naphthenic acid, etc. Nickel, etc.), must first be injected into the formation through an oil-based slug, and then steam injected to heat and crack the heavy oil. The construction process is more complicated, and generally it needs to be around 250-300°C to effectively catalyze the heavy oil cracking
In addition, the addition of oil-soluble metal salts, especially nickel salts, will seriously damage the quality of crude oil and increase the burden on subsequent crude oil processing

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0012] Embodiment 1: A method for preparing a low-temperature heavy oil aquathermal cracking viscosity-reducing catalyst, comprising the following steps:

[0013] In the first step, the transition metal salt is dissolved in 5 times the mass of water in a reaction vessel at normal temperature. The transition metal salt is of industrial grade purity, the cation of the transition metal salt is manganese ion, and the anion is chloride ion. The water is industrial grade tap water;

[0014] In the second step, add a hydroxamic acid compound with a ratio of 1:1 to the transition metal salt substance into the reaction vessel under stirring, and stir evenly. The hydroxamic acid compound is industrial-grade pure methyl Hydroxamic acid;

[0015] In the third step, the solution in the reaction vessel was heated to 30° C., stirred for 4 hours, cooled to room temperature, and water was evaporated;

[0016] In the fourth step, a cocatalyst 100 times the mass of the remainder is added to th...

Embodiment 2

[0018] Embodiment 2: A method for preparing a low-temperature heavy oil aquathermal cracking viscosity-reducing catalyst, comprising the following steps:

[0019] In the first step, the transition metal salt is dissolved in 8 times the quality of water in a reaction vessel at normal temperature, the transition metal salt is analytically pure, the cation of the transition metal salt is ferrous ion, and the anion of the transition metal salt is a sulfate radical, Described water is technical grade distilled water;

[0020] In the second step, add a hydroxamic acid compound with a ratio of 2:1 to the transition metal salt substance into the reaction vessel under stirring, and stir evenly. The hydroxamic acid compound is chemically pure phenyliso hydroxamic acid;

[0021] In the third step, the solution in the reaction vessel was heated to 60° C., stirred for 4 hours, cooled to room temperature, and water was evaporated;

[0022] The fourth step is to add a co-catalyst 80 times ...

Embodiment 3

[0024] Embodiment 3: A method for preparing a low-temperature heavy oil hydrothermal cracking viscosity-reducing catalyst, comprising the following steps:

[0025] In the first step, the transition metal salt is dissolved in 10 times the mass of water in a reaction vessel at normal temperature. The transition metal salt is chemically pure, the cation of the transition metal salt is cobalt ion, and the anion of the transition metal salt is acetate. Water is industrial grade distilled water;

[0026] In the second step, add a hydroxamic acid compound with a ratio of 3:1 to the transition metal salt substance into the reaction vessel under stirring, and stir evenly. The hydroxamic acid compound is chemically pure salicyl hydroxamic acid acid;

[0027] In the third step, the solution in the reaction vessel was heated to 70° C., stirred for 3 hours, cooled to room temperature, and water was evaporated;

[0028] In the fourth step, add a co-catalyst 50 times the mass of the remain...

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PUM

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Abstract

The invention relates to a preparation method of a low-temperature thickened oil hydrothermal cracking viscosity-reduction catalyst. At normal temperature, transition metal salt is dissolved in waterin a reaction container, while stirring, a hydroxamic acid compound is added in the reaction container, and then uniformly stirred, the solution in the reaction container is heat to the temperature of30-100 DEG C, then is stirred for 1-4 hours and cooled to room temperature, and water is steamed; a cocatalyst is added in residue in the reaction container, and the thickened oil hydrothermal cracking catalyst is obtained, the prepared catalyst has good catalysis effect under low temperature, the catalytic reaction at the temperature being more than 180 DEG C can reduce viscosity of the thickened oil can reach more than 70%, the catalyst is not dissolved in crude oil, processing difficulty during a crude oil processing process cannot be increased due to increase of the metal ion content in the crude oil, the catalyst has obvious advantage of protecting quality of the crude oil, operation is simple, thickened oil recovery difficulty is obviously reduced, and the catalyst is benefit for on-site popularization.

Description

technical field [0001] The invention relates to the technical field of heavy oil thermal cracking catalysts, in particular to a preparation method of a low-temperature heavy oil hydrothermal cracking viscosity-reducing catalyst. Background technique [0002] my country is rich in heavy oil resources and widely distributed. More than 70 heavy oil fields have been discovered in 12 basins, and the estimated resources can reach 300×10 8 t above, accounting for about 15% of my country's total oil reserves. However, heavy oil has high viscosity and poor fluidity, and its exploitation is more difficult, costly and technically demanding. Commonly used methods for mining heavy oil include blending thin oil, hot water flooding, steam huff and puff and steam flooding, emulsification and viscosity reduction, heavy oil modification and viscosity reduction, etc. Among them, in-situ catalytic cracking / degradation modification of heavy oil has become a popular topic in China in recent yea...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J31/04B01J31/32C09K8/58C10G11/02
CPCB01J31/04B01J31/32C09K8/58C10G11/02C10G2300/302
Inventor 陈刚袁巍华张洁顾雪凡都伟超陈世军
Owner XI'AN PETROLEUM UNIVERSITY
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