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Preparation method of heat-resistance and salt-tolerance polyacrylamide

A technology of polyacrylamide and acrylamide, which is applied in the field of functional polymers, can solve problems such as poor viscosity increasing effect and increased degree of hydrolysis, and achieve good solubility and filterability, convenient polymerization operation, and favorable production effects

Inactive Publication Date: 2015-03-04
ANHUI TIANRUN CHEM CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Among them, more and more attention has been paid to the mining of Type II and III oil reservoirs, which account for more than half of the total resources. At present, the formation temperature of Type II and III oil reservoir resources is 70-95°C, and the salinity of the formation is 10,000-30,000mg / L. The ion is 800mg / L. Under this condition, the commonly used hydrolyzed polyacrylamide (HPAM) will suffer from severe thermal degradation, increased degree of hydrolysis, and precipitation when encountering high-valent ions, and the viscosity-increasing effect will become poor.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0017] In a 500ml jar, first add 230g of acrylamide aqueous solution with a mass concentration of 25%, 1.0g of pure acrylic acid, and 1.15g of AMPS, then control the temperature within 15°C, and adjust the pH with sodium hydroxide liquid alkali while stirring =6.1. After cooling down to 1°C, high-purity nitrogen (nitrogen purity ≥ 99.99%) was introduced to remove oxygen in the system. When the oxygen content of the system is less than 0.01%, add 0.003g of disodium ethylenediaminetetraacetic acid complexing agent; 0.06g of azo compound azobisisobutyronitrile; 0.005g of high-efficiency chain transfer agent sodium formate; Initiator triethanolamine 0.0005g; oxidation initiator tert-butyl hydroperoxide 0.00022g, seal and seal after reaction. When the temperature of the reaction no longer rises, it is placed in a water bath at 80° C. for 1 hour. After the heat preservation, take out the colloid and mince it, add 20ml of liquid caustic soda (mass fraction 30%), and hydrolyze at 85...

Embodiment 2

[0020] In a 500ml jar, first add 230g of acrylamide aqueous solution with a mass concentration of 25%, 1.0g of pure acrylic acid, and 1.50g of AMPS, then control the temperature within 15°C, and adjust the pH with sodium hydroxide liquid alkali while stirring =6.4. After cooling down to 1°C, high-purity nitrogen (nitrogen purity ≥ 99.99%) was introduced to remove oxygen in the system. When the oxygen content of the system is less than 0.01%, 0.009 g of the complexing agent tetrasodium ethylenediaminetetraacetic acid; 0.10 g of the azo compound azobisisobutyronitrile; g; reduction initiator sodium metabisulfite 0.0008g; oxidation initiator dialkyl peroxide 0.0003g, sealed after the reaction. When the temperature of the reaction no longer rises, it is placed in a water bath at 80° C. for 1 hour. After the heat preservation, take out the colloid and mince it, add 20ml of liquid caustic soda (mass fraction 30%), and hydrolyze at 85°C for 1h. Finally, the rubber block is dried i...

Embodiment 3

[0023] In a 500ml jar, first add 230g of acrylamide aqueous solution with a mass concentration of 25%, 1.0g of pure acrylic acid, and 3.40g of AMPS, then control the temperature within 15°C, and adjust the pH with sodium hydroxide liquid alkali while stirring =5.9. After cooling down to 1°C, high-purity nitrogen (nitrogen purity ≥ 99.99%) was introduced to remove oxygen in the system. When the oxygen content of the system is less than 0.01%, add 0.005g of complexing agent disodium ethylenediaminetetraacetic acid, 0.08g of azo compound azobisisoheptanonitrile, and 0.010g of high-efficiency chain transfer agent isopropanol every 3 minutes Reduction initiator ferrous chloride 0.0008g; Oxidation initiator hydrogen peroxide 0.0003g, carry out sealing after reaction. When the temperature of the reaction no longer rises, it is placed in a water bath at 80° C. for 1 hour. After the heat preservation, take out the colloid and mince it, add 20ml of liquid caustic soda (mass fraction 3...

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PUM

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Abstract

The invention discloses a preparation method of heat-resistance and salt-tolerance polyacrylamide. The preparation method comprises the following steps: taking the aqueous solution of acrylamide with the mass concentration of 20-30 percent, adding acrylic acid accounting for 1-2 percent of the mass of an acrylamide monomer and 2-acrylamide-2-methylpropane sulfonic acid (AMPS) accounting for 2-6 percent of the mass of the acrylamide monomer, adding sodium hydroxide for regulating a pH value to 5.5-6.5, cooling to 0-4 DEG C, introducing nitrogen to remove oxygen out of the system, sequentially adding a complexing agent, an azo initiator, an efficient chain transfer agent, a reducing agent and an oxidant when the oxygen content in the system is smaller than 0.01 percent, sealing after reaction is finished, preserving heat for 1-1.5h, then taking out colloid, putting the colloid in a hydrolyzer, adding an inorganic alkali liquor accounting for 6-13 percent of the acrylamide monomer, hydrolyzing at the temperature of 80-90 DEG C for 1-2h, and drying the colloid to prepare the product. The heat-resistance and salt-tolerance polyacrylamide is good in solubility and filterability, and the apparent viscosity of the heat-resistance and salt-tolerance polyacrylamide is above 11mPa.s.

Description

Technical field [0001] The present invention is a functional polymer field, which specializes in the preparation method for a three -time oil field of oil field use of oil field. Background technique [0002] Petroleum is an important basic raw material for energy and chemical industry. International crude oil prices continue to rise, which has stimulated measures for crude oil in various countries.From the current technological level, three oil recovery with polymer oil as the core has become an oil field leading development method that is commonly used in industrial applications, and has entered a new period of rapid development.Among them, the mining problems of II and III collection of category III, which account for more than half of the total resource, pay more and more attention. At present, the temperature of the resource streaming of the resource hidden resource hidden in Class II and III is 70-95 ° C, and the level of mineralization is 10,000 to 30,000 mg / L. The second ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C08F220/56C08F220/06C08F220/58C08F2/38C08F4/40C08F4/04C08F8/12C09K8/588
Inventor 刘彭城张传银陈建波汪艳王全飞张冉李大强陶阿晖
Owner ANHUI TIANRUN CHEM CO LTD
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