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Non-phosphorus polymer corrosion inhibitor and preparation method and application thereof

A technology of polymers and corrosion inhibitors, applied in chemical instruments and methods, descaling and water softening, water/sludge/sewage treatment, etc., can solve problems such as promotion of corrosion, inability to inhibit corrosion, consumption of fungicides, etc., to achieve Good corrosion inhibition effect, good corrosion inhibition effect, no three wastes

Active Publication Date: 2019-07-30
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0002] The corrosion and scale inhibitors used in cooling water treatment in my country are basically based on phosphorus-based formulas. Although the performance can basically meet the requirements for use, there are deficiencies in phosphorus-based formulas: (1) Phosphate-based formulas are easy to form during use. (2) Promote the reproduction of microorganisms in the circulating water system and consume a large amount of fungicides; (3) The discharge of a large amount of phosphorus will easily lead to eutrophication of the receiving water body
However, except for HPMA, PESA, and PASP, which have a certain corrosion inhibition ability, most of them not only fail to inhibit corrosion, but promote corrosion. In order to offset these increased corrosion, the amount of corrosion inhibitor in the formula must be increased, resulting in increased use costs.

Method used

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  • Non-phosphorus polymer corrosion inhibitor and preparation method and application thereof
  • Non-phosphorus polymer corrosion inhibitor and preparation method and application thereof
  • Non-phosphorus polymer corrosion inhibitor and preparation method and application thereof

Examples

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preparation example Construction

[0021] According to the present invention, the preparation method of the non-phosphorus polymer corrosion inhibitor comprises: under free radical polymerization conditions and in the presence of water, unsaturated carboxylic acid, allyloxy polyethylene glycol monoester carboxyl derivative , Allyloxypolyethylene glycol sulfonate is contacted with an initiator to react.

[0022] According to the present invention, preferably, in the presence of water, the unsaturated carboxylic acid, allyloxy polyethylene glycol monoester carboxyl derivatives, allyloxy polyethylene glycol sulfonate and initiator contact The method comprises: mixing unsaturated carboxylic acid, allyloxy polyethylene glycol monoester carboxyl derivative, allyloxy polyethylene glycol sulfonate and water, raising the temperature to 55-80°C, and then adding the initiator dropwise .

[0023] According to the present invention, the free radical polymerization conditions generally include reaction temperature and reactio...

Embodiment 1

[0046] Add allyloxypolyethylene glycol (27.8g, 0.1mol) and oxalic acid (9.0g, 0.1mol) with a molecular weight of 278 (that is, m=5) into the reactor for esterification reaction at a temperature of 70°C , The reaction time is 2h, generating allyloxy polyethylene glycol oxalic acid monoester derivatives.

[0047] Add allyloxypolyethylene glycol (27.8g, 0.1mol) and sulfamic acid (9.7g, 0.1mol) with a molecular weight of 278 (that is, n=5) into the reactor, and react at 100°C for 2h to form Allyloxypolyethylene glycol sulfonate.

[0048] Three polymerized monomers—acrylic acid (1.0g), allyloxypolyethylene glycol oxalate monoester derivatives (3.0g), allyloxypolyethylene glycol sulfonate (3.0g), and distilled water (20.0g) was added to the reaction kettle, stirred evenly, and 1g of ammonium persulfate solution with a mass fraction of 10% was added dropwise at 60°C for 15 minutes. After the addition, the temperature was raised to 80°C, reacted for 2 hours, and cooled to At room te...

Embodiment 2

[0050] Add allyloxypolyethylene glycol (27.8g, 0.1mol) and maleic anhydride (9.8g, 0.1mol) with a molecular weight of 278 (ie m=5) into the reactor for esterification reaction at a temperature of 80°C, the reaction time is 2h, and allyloxy polyethylene glycol maleic acid monoester derivatives are generated.

[0051] Add allyloxypolyethylene glycol (27.8g, 0.1mol) and sulfamic acid (9.7g, 0.1mol) with a molecular weight of 278 (ie n=5) into the reactor, and react at 110°C for 3h to form Allyloxypolyethylene glycol sulfonate.

[0052] Three polymerized monomers—acrylic acid (1.0g), allyloxy polyethylene glycol maleate monoester derivatives (3.0g), allyloxy polyethylene glycol sulfonate (3.0g), And distilled water (20.0g) was added to the reaction kettle, stirred evenly, and 2g of ammonium persulfate solution with a mass fraction of 10% was added dropwise at 60°C. The dropping time was 30min. After the addition was completed, the temperature was raised to 80°C and reacted for 2h...

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Abstract

The invention relates to the field of corrosion inhibitors, and discloses a non-phosphorus polymer corrosion inhibitor. The non-phosphorus polymer corrosion inhibitor is shown in the general formula in the description, wherein R1 is <->H, <->COOH or phenyl; R2 is <->H, <->CH2COOH or low-carbon alkyl of C1-C5; R3 is <->CO(CH2)kCOOH, <->COCH(OH)COOH, <->COCH(OH)CH2COOH, <->COCH2CH(OH)COOH, <->COCH(OH)CH(OH)COOH, <->COCH=CHCOOH, <->CO(o-C6H4)COOH, <->CO(p-C6H4)COOH, <->COCH2C(OH)(COOH)CH2COOH, <->COC(OH)(CH2COOH)2, <->COCH=C(COOH)CH2COOH, <->COCH2C(COOH)=CHCOOH and <->COC(CH2COOH)=CHCOOH; the polymerization degree x is 1-5000; the polymerization degree y is 1-5000; the polymerization degree z is 1-5000; the polymerization degree m is 1-100; the polymerization degree n is 1-100; the polymerization degree k is 0-8. The invention further discloses a preparation method and application of the non-phosphorus polymer corrosion inhibitor. The non-phosphorus polymer corrosion inhibitor has a goodcorrosion inhibition effect.

Description

technical field [0001] The invention relates to a phosphorus-free polymer corrosion inhibitor and its preparation method and application. Background technique [0002] The corrosion and scale inhibitors used in cooling water treatment in my country are basically based on phosphorus-based formulas. Although the performance can basically meet the requirements for use, there are deficiencies in phosphorus-based formulas: (1) Phosphate-based formulas are easy to form during use. (2) Promote the reproduction of microorganisms in the circulating water system and consume a large amount of fungicides; (3) The discharge of a large amount of phosphorus will easily lead to eutrophication of the receiving water body. Therefore, the development and use of phosphorus-free corrosion and scale inhibitors is of great significance to the treatment of circulating cooling water. [0003] Most of the common corrosion and scale inhibitors contain polymer components, such as hydrolyzed polymaleic ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C08F216/14C08F220/06C08F222/06C08F222/02C02F5/10
CPCC08F216/1466C08F216/1416C02F5/10C08F216/1433C08F216/1475C08F220/06C08F222/06C08F222/02
Inventor 孙飞余正齐傅晓萍王金华
Owner CHINA PETROLEUM & CHEM CORP
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