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Alkyl naphthylamine polyether naphthalene sulfonate surfactant as well as preparation method and application thereof

A technology of alkylnaphthylamine polyether and surfactant, which is applied in the field of heavy oil viscosity reducer and its preparation, can solve the problems of poor oil displacement effect, achieve strong action ability, high interface activity, and enhance oil recovery Effect

Pending Publication Date: 2022-01-07
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 the poor oil displacement effect of surfactants in heavy oil reservoirs in the existing production technology, and a novel alkylnaphthylamine polyether naphthalene sulfonate oil displacement surfactant is provided

Method used

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  • Alkyl naphthylamine polyether naphthalene sulfonate surfactant as well as preparation method and application thereof
  • Alkyl naphthylamine polyether naphthalene sulfonate surfactant as well as preparation method and application thereof
  • Alkyl naphthylamine polyether naphthalene sulfonate surfactant as well as preparation method and application thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0057] 1. Synthesis of Decyl Naphthylamine Polyoxypropylene (10) Polyoxyethylene (15) Ether Naphthalene Sulfonate

[0058] a) add 1.0mol of decanyl naphthalene in the reactor that condensing unit, stirring device are housed, dropwise the 65% concentrated nitric acid of 2.0mol, control temperature of reaction is 65 ℃, after dropwise addition, continue reaction 4 hours, Obtain 0.91mol of decanyl nitronaphthalene;

[0059] b) Add 0.91 mol of decyl nitronaphthalene to the autoclave, add 22 g of Raney nickel catalyst, and seal the autoclave. Replace with nitrogen gas for 5 times, then replace with hydrogen gas for 5 times, raise the temperature to 80°C, start hydrogenation, control the system pressure not to exceed 4MPa, and react for 6 hours to obtain 0.87mol of decanyl naphthylamine;

[0060] c) Add 0.87 mol of decanyl naphthylamine and 2.5 g of sodium hydroxide to a reactor equipped with a condensing device, a stirring device and a gas disperser, and stir for 1 hour while heati...

Embodiment 2

[0070] 1. Synthesis of dodecylnaphthylamine polyoxyethylene (5) ether naphthalene sulfonate

[0071] a) add 1.0mol of dodecylnaphthalene in the reactor that condensing unit, stirring device are housed, dropwise the vitriol oil of 1.3mol65% nitric acid and 45g 98%, control reaction temperature is 30 ℃, after dropwise, Continue to react for 1 hour to obtain 0.91mol of dodecylnitronaphthalene;

[0072] b) Add 0.91 mol of dodecylnitronaphthalene into the autoclave, add 20 g of Raney nickel catalyst, and seal the autoclave. Inflate nitrogen for 5 times, then pass hydrogen for 5 times, raise the temperature to 80°C, start hydrogenation, control the system pressure not to exceed 4MPa, and react for 6 hours to obtain 0.88 mol of dodecylnaphthylamine;

[0073] c) Add 0.88 mol of dodecylnaphthylamine and 3.0 g of sodium hydroxide to a reactor equipped with a condensing device, a stirring device and a gas disperser, and stir for 1 hour while heating to 80° C. while blowing nitrogen. Tu...

Embodiment 3

[0078] 1. Synthesis of dodecyloctylnaphthylamine polyoxypropylene (4) polyoxyethylene (9) ether naphthalene sulfonate

[0079] a) Add 1.0mol of dodecyl octanenaphthalene in the reactor equipped with condensing device and stirring device, add dropwise the concentrated sulfuric acid of 1.5mol 65% nitric acid and 50g 98%, control reaction temperature to be 40 ℃, dropwise After the addition was completed, the reaction was continued for 2 hours to obtain 0.95mol of dodecyloctylnitronaphthalene;

[0080] b) 0.95 mol of dodecyloctylnitronaphthalene was added into the autoclave, 30 g of Raney nickel catalyst was added, and the autoclave was sealed. Infuse nitrogen for 5 replacements, then pass hydrogen for 5 replacements, raise the temperature to 50°C, start hydrogenation, control the system pressure not to exceed 4MPa, and react for 6 hours to obtain 0.92 mol of dodecyloctylnaphthylamine;

[0081] c) Add 0.92mol of dodecyloctylnaphthylamine and 4.0g of sodium hydroxide to a reactor ...

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Abstract

The invention discloses an alkyl naphthylamine polyether naphthalene sulfonate surfactant as well as a preparation method and application thereof, the surfactant has a structural formula (I) as shown in the specification, and in the formula (I), R2 and R2 are independently selected from sulfonate, acetate, H or C1-C10 alkyl; R1 and R1 are independently selected from H or C1-C40 alkyl groups and are not H at the same time, m1 + m2 = 0-80, n1 + n2 = 0-60, m1 and n1 are not 0 at the same time, and m2 and n2 are not 0 at the same time; Y is selected from sulfonate. According to the technical scheme, the method is used for improving the recovery rate of the thickened oil, the island thickened oil in the Shengli oil field is adopted for a displacement experiment, the recovery rate is improved by 7.9%, and a good technical effect is achieved.

Description

technical field [0001] The invention belongs to the field of viscosity reducers, in particular to a heavy oil viscosity reducer and its preparation method and application. Background technique [0002] Heavy oil occupies a relatively large proportion of the world's oil and gas resources, and the reserves of heavy oil, super heavy oil and natural bitumen in the world are about 1000×10 8 Ton. Countries rich in heavy oil resources include Canada, Venezuela, the United States, the former Soviet Union, China, and Indonesia. The distribution of heavy oil resources in China is also very extensive, and the exploitation of heavy oil has great potential. The main difference between heavy oil and ordinary crude oil is that the viscosity of heavy oil is much higher than that of ordinary crude oil, and conventional methods are not suitable for heavy oil recovery. The most widely used heavy oil recovery methods include steam oil recovery, hot water oil recovery, burning oil reservoirs,...

Claims

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Application Information

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IPC IPC(8): C08G65/28C09K8/584C09K8/60C07C303/32C07C309/47C07C213/04C07C217/08C07C209/36C07C211/58C07C201/08C07C205/06
CPCC08G65/2627C09K8/584C09K8/604C07C309/47C07C303/32C07C213/04C07C209/36C07C201/08C07C205/06C07C211/58C07C217/08
Inventor 鲍新宁李应成吴欣悦孟勇
Owner CHINA PETROLEUM & CHEM CORP