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Tertiary oil recovery surfactant and preparation method thereof

A surfactant and alkaline technology, which is applied in the field of tertiary oil recovery surfactant and its preparation, can solve the problems of low oil displacement efficiency and high oil displacement efficiency, and achieve improved salt resistance, enhanced oil recovery, wide application prospects and practical effect

Active Publication Date: 2015-01-14
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] One of the technical problems to be solved by the present invention is that the surfactants in the prior art have the problem of low oil displacement efficiency under high temperature and high salt conditions, and a new surfactant for tertiary oil recovery is provided, which has Features of high oil displacement efficiency under high salinity conditions

Method used

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  • Tertiary oil recovery surfactant and preparation method thereof
  • Tertiary oil recovery surfactant and preparation method thereof
  • Tertiary oil recovery surfactant and preparation method thereof

Examples

Experimental program
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Effect test

Embodiment 1

[0024] 1. Surfactant Preparation

[0025] a) Add 0.5 mol of nonylphenol, 1.5 g of sodium hydroxide and 15 g of water into a reactor equipped with a condensing device, a stirring device, and a gas disperser, and heat to 85° C. while nitrogen is blown, and then stir for 1 hour. Turn on the vacuum system, vacuumize and dehydrate for 1 hour at a temperature of 90°C, then purge 4 times with nitrogen to remove the air in the system, then adjust the reaction temperature of the system to 150°C and slowly introduce 1mol propylene oxide to control the pressure ≤0.40MPa to react; after the reaction, purge the system with nitrogen, neutralize with glacial acetic acid after cooling, and obtain 0.49mol nonylphenol polyoxypropylene (2) ether.

[0026] b) Add the nonylphenol polyoxypropylene ether (2) obtained in step a) into a reactor equipped with a stirring device, a condensation reflux device and a water separation device, add 250 ml of benzene and 40 g of sodium hydroxide, and heat at 60...

Embodiment 2

[0036] 1. Surfactant Preparation

[0037] a) Add 0.5 mol of nonylphenol, 1.5 g of sodium hydroxide and 15 g of water into a reactor equipped with a condensing device, a stirring device, and a gas disperser, and heat to 85° C. while nitrogen is blown, and then stir for 1 hour. Turn on the vacuum system, vacuumize and dehydrate for 1 hour at a temperature of 90°C, and then blow with nitrogen gas 4 times to remove the air in the system, then adjust the reaction temperature of the system to 150°C and slowly introduce 0.5mol propylene oxide to control React at a pressure of ≤0.40 MPa; after the reaction, purge the system with nitrogen, neutralize it with glacial acetic acid after cooling, and obtain 130 g of nonylphenol polyoxypropylene (1) ether.

[0038] b) Add 0.5mol nonylphenol polyoxypropylene ether (1) obtained in step a) into a reactor equipped with a stirring device, a condensation reflux device and a water separation device, add 250 milliliters of benzene and 40 grams of s...

Embodiment 3

[0043] 1. Surfactant Preparation

[0044] a) Add 0.5 mol of nonylphenol, 1.5 g of sodium hydroxide and 15 g of water into a reactor equipped with a condensing device, a stirring device, and a gas disperser, and heat to 85° C. while nitrogen is blown, and then stir for 1 hour. Turn on the vacuum system, vacuumize and dehydrate for 1 hour at a temperature of 90°C, then purge 4 times with nitrogen to remove the air in the system, then adjust the reaction temperature of the system to 150°C and slowly introduce 2.0mol propylene oxide to control The reaction was carried out at a pressure of ≤0.40 MPa; after the reaction, the system was purged with nitrogen, and after cooling, it was neutralized with glacial acetic acid to obtain 0.49 mol of nonylphenol polyoxypropylene (4) ether.

[0045] b) Add 0.49mol nonylphenol polyoxypropylene ether (4) obtained in step a) into a reactor equipped with a stirring device, a condensation reflux device and a water separation device, add 250 millili...

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Abstract

The invention relates a tertiary oil recovery surfactant and a preparation method thereof, and mainly solves the problem that surfactants in the prior art are low in oil displacement efficiency under the conditions of high temperature and high salt. The employed tertiary oil recovery surfactant has the name of 3-(alkylphenol polyoxypropylene ether)-2-( polyoxyethylene ether)propanesulfonate and has the structure shown as a formula (I) in the specification, wherein M is any one of alkali metals and alkali earth metals, n is the molar ratio of M to SO3 group in the formula (I), n is 1 when M is an alkali metal, n is 0.5 when M is an alkali earth metal, R is an C4-C20 alkyl, x=1-10 and y=1-20. The technical scheme relatively well solves the above problem and is applicable to tertiary oil recovery production of oil fields.

Description

technical field [0001] The invention relates to a surface active agent for tertiary oil recovery and a preparation method thereof. Background technique [0002] Tertiary oil recovery is a method of increasing crude oil recovery by using physical, chemical and biological means to continue to exploit the remaining underground oil. The research on the application of surfactants in oil recovery began in the early 1930s, and has been an important means of improving oil recovery in oil fields, and has made great progress in theory and practice. . At present, the following injection systems have basically been formed: active water flooding, foam flooding, low interfacial tension system flooding, etc. After the oil field enters the high water cut period, the remaining oil is trapped in the pores of the reservoir rocks in a discontinuous oil film. The two main forces acting on the oil droplets are viscous force and capillary force. The agent system can reduce the interfacial tensi...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C09K8/584C08G65/28C08G65/334E21B43/22
CPCC08G65/2612C08G65/3346C08G2650/04C09K8/584
Inventor 鲍新宁张卫东李应成沙鸥沈之芹
Owner CHINA PETROLEUM & CHEM CORP