CN101654421A - Synthesis method of cocamidopropyl-2-hydroxy-3-sulfopropyl betaine - Google Patents

Synthesis method of cocamidopropyl-2-hydroxy-3-sulfopropyl betaine Download PDF

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CN101654421A
CN101654421A CN200910102017A CN200910102017A CN101654421A CN 101654421 A CN101654421 A CN 101654421A CN 200910102017 A CN200910102017 A CN 200910102017A CN 200910102017 A CN200910102017 A CN 200910102017A CN 101654421 A CN101654421 A CN 101654421A
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hydroxyl
sulfopropyl betaine
reaction
sodium
synthetic method
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王伟松
王新荣
金一丰
李福强
曾红舟
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ZHEJIANG HECHENG CHEMICAL CO Ltd
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ZHEJIANG HECHENG CHEMICAL CO Ltd
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Abstract

The invention discloses a synthesis method of cocoamidopropyl-2-hydroxy-3-sulfopropyl betaine, which takes coconut oil fatty acid, N-dimethyl propane diamine, epichlorohydrin and anhydrous sodium bisulfite as raw materials and comprises the following specific steps: carrying out amidation reaction on coconut oil fatty acid and N, N-dimethyl propane diamine to generate intermediate cocoamide; then, carrying out addition reaction on epoxy chloropropane and anhydrous sodium bisulfite to generate an intermediate sodium chlorohydroxypropylsulfonate; and finally, carrying out quaternization reaction on the prepared intermediate cocoamide and the intermediate sodium hydroxypropyl sulfonate in the presence of a catalyst to generate the target product cocoamidopropyl-2-hydroxy-3-sulfopropyl betaine. The product of the invention has good hard water resistance, conditioning property and antistatic property; the pH value is stable in a wide range, is not influenced in acid and alkali media, and is stable in an electrolyte system; and is degradable and non-toxic.

Description

The synthetic method of cocamidopropyl propyl amide-2-hydroxyl-3-sulfopropyl betaine
Technical field
The present invention relates to the synthetic method of a kind of novel daily-use chemical industry formulation monomer cocamidopropyl propyl amide-2-hydroxyl-3-sulfopropyl betaine, belong to the synthesis technical field of zwitterionics in the organic chemistry.
Background technology
Cocamidopropyl propyl amide-2-hydroxyl-3-sulfopropyl betaine is colourless to weak yellow liquid, water-soluble, can with various tensio-active agent compatibilities, can reduce the pungency of other tensio-active agents, foam is abundant and fine and smooth and not influenced by the pH value, and stability in hard water is good, tool conditioning property and static resistance.Stable in wide ph range, unaffected in acid-alkali medium, stable in electrolyte system.Degradable is nontoxic.Cooperate with sulfated lauryl alcohol and α-Xi Jihuangsuanyan, foam and viscosity are good.Good dispersion of calcium soap is arranged.Can be used as suds booster, washing composition, cloud point inhibitor, hydrotropic agent etc.Be suitable for preparing the senior shampoo of mild, bathe with goods, amendment, skin cleaner, skin-protecting agent infant articles for washing and family expenses and dish washing detergent.
Synthetic method about cocamidopropyl propyl amide-2-hydroxyl-3-sulfopropyl betaine there is no report both at home and abroad, just occurs in some external daily necessities prescriptions, as U.S. Lonzaine company
Figure G2009101020177D00011
CS, French Rhodia company
Figure G2009101020177D00012
CBS, U.S. Stepan company
Figure G2009101020177D00013
CS-50.
Summary of the invention
In order to address the above problem, the object of the present invention is to provide a kind of novel daily-use chemical industry formulation monomer---the synthetic method of zwitterionics cocamidopropyl propyl amide-2-hydroxyl-3-sulfopropyl betaine product.Product stability in hard water of the present invention is good, tool conditioning property and static resistance; Stable in wide ph range, unaffected in acid-alkali medium, stable in electrolyte system; And degradable is nontoxic.
For reaching above-mentioned purpose, the present invention adopts following technical scheme,
The synthetic method of a kind of cocamidopropyl propyl amide-2-hydroxyl-3-sulfopropyl betaine, with commercially available coco-nut oil fatty acid, N, N-dimethylated propyl diethylenetriamine, epoxy chloropropane, anhydrous sodium sodium pyrosulfate are raw material, concrete steps are: (1) with coco-nut oil fatty acid and N, N-dimethylated propyl diethylenetriamine amidate action generates the intermediate coconut oleoyl amine; Reaction equation is:
Figure G2009101020177D00021
(RCO is a cocoyl)
(2) again epoxy chloropropane and the addition reaction of anhydrous sodium sodium pyrosulfate are generated intermediate chlorine hydroxypropyl azochlorosulfonate acid sodium; Reaction equation is:
Figure G2009101020177D00022
(3) quaterisation takes place in the intermediate hydroxypropyl azochlorosulfonate acid sodium that makes of intermediate coconut oleoyl amine that at last step (1) is made and step (1) in the presence of catalyzer, generates target product cocamidopropyl propyl amide-2-hydroxyl-3-sulfopropyl betaine; Reaction equation is:
(RCO is a cocoyl).
Described coco-nut oil fatty acid and N, the mass ratio of N-dimethylated propyl diethylenetriamine are 1: 0.49~0.78.
Described coco-nut oil fatty acid and N, the mass ratio of N-dimethylated propyl diethylenetriamine is preferably 1: 0.59.
Described coco-nut oil fatty acid and N, the amidate action of N-dimethylated propyl diethylenetriamine carries out in two stages: the fs, coco-nut oil fatty acid and N, salt-forming reaction takes place at 60~110 ℃ in the N-dimethylated propyl diethylenetriamine, generates ammonium salt, and the reaction times is 1.0~4.0h; Subordinate phase, ammonium salt generate the intermediate coconut oleoyl amine 140~200 ℃ of dehydrations, and be reflected under the negative pressure and carry out, reaction pressure 20~200Pa, the reaction times is 1.0~4.0h.
The mass ratio of described epoxy chloropropane and anhydrous sodium sodium pyrosulfate is 1: 1.12~1.46; Temperature of reaction can be 40~90 ℃, and the reaction times is 3.0~8.0h.
The mass ratio of described epoxy chloropropane and anhydrous sodium sodium pyrosulfate is preferably 1: 1.29.
The mass ratio of described intermediate coconut oleoyl amine and intermediate chlorine hydroxypropyl azochlorosulfonate acid sodium is 1: 0.65~0.70; Temperature of reaction can be 60~90 ℃, and the reaction times is 2.0~8.0h.
The mass ratio of described intermediate coconut oleoyl amine and intermediate chlorine hydroxypropyl azochlorosulfonate acid sodium is preferably 1: 0.67.
Described intermediate coconut oleoyl amine and intermediate chlorine hydroxypropyl azochlorosulfonate acid sodium catalyst for reaction can be a kind of in sodium hydroxide, the potassium hydroxide, and the catalyzer add-on is 1~10% of intermediate coconut oleoyl amine and an intermediate chlorine hydroxypropyl azochlorosulfonate acid sodium total mass.
The molecular weight of described product cocamidopropyl propyl amide-2-hydroxyl-3-sulfopropyl betaine is 429 (molecular weight of cocoyl RCO is in 208).
The invention has the beneficial effects as follows: the present invention is a kind of novel household chemicals raw material---cocamidopropyl propyl amide-2-hydroxyl-3-sulfopropyl betaine, and mainly as suds booster, washing composition, cloud point inhibitor, hydrotropic agent etc.Be suitable for preparing the senior shampoo of mild, bathe with goods, amendment, skin cleaner, skin-protecting agent infant articles for washing and family expenses and dish washing detergent.Can with various tensio-active agent compatibilities, can reduce the pungency of other tensio-active agents, foam is abundant and fine and smooth and not influenced by pH value, stability in hard water is good, tool is nursed one's health property and static resistance.Stable in wide ph range, unaffected in acid-alkali medium, stable in electrolyte system.Degradable is nontoxic.Cooperate with sulfated lauryl alcohol and α-Xi Jihuangsuanyan, foam and viscosity are good.Good dispersion of calcium soap is arranged.
Embodiment
Embodiment 1
Ability case step 1: add 500kg coco-nut oil fatty acid (purchasing in Shandong Boxing Huarun Grease Chemical Co., Ltd) in reactor, be stirred and heated to 85~90 ℃, begin to drip 246kgN, the N-dimethylated propyl diethylenetriamine adds insulation reaction 4.0h.At pressure 20Pa, 200 ℃ of insulation reaction 4.0h of temperature, obtain the intermediate coconut oleoyl amine then.
Step 2: add the 222kg epoxy chloropropane in reactor, be stirred and heated to 85~90 ℃, beginning adds 250kg anhydrous sodium sodium pyrosulfate in batches, adds insulation reaction 8.0h, obtains intermediate chlorine hydroxypropyl azochlorosulfonate acid sodium.
Step 3: in reactor, add 667kg intermediate coconut oleoyl amine, be heated to 85~90 ℃, add 11kg potassium hydroxide, beginning adds 434kg intermediate chlorine hydroxypropyl azochlorosulfonate acid sodium in batches, add insulation reaction 8.0h, obtain target product cocamidopropyl propyl amide-2-hydroxyl-3-sulfopropyl betaine, molecular weight is 429.
Embodiment 2
Present embodiment step 1: add 500kg coco-nut oil fatty acid (purchasing in Shandong Boxing Huarun Grease Chemical Co., Ltd) in reactor, be stirred and heated to 60~62 ℃, begin to drip 295kgN, the N-dimethylated propyl diethylenetriamine adds insulation reaction 2.0h.At pressure 100Pa, 160 ℃ of insulation reaction 3.0h of temperature, obtain the intermediate coconut oleoyl amine then.
Step 2: add the 222kg epoxy chloropropane in reactor, be stirred and heated to 60~65 ℃, beginning adds 287kg anhydrous sodium sodium pyrosulfate in batches, adds insulation reaction 5.0h, obtains intermediate chlorine hydroxypropyl azochlorosulfonate acid sodium.
Step 3: in reactor, add 667kg intermediate coconut oleoyl amine, be heated to 80~85 ℃, add 46kg potassium hydroxide, beginning adds 447kg intermediate chlorine hydroxypropyl azochlorosulfonate acid sodium in batches, add insulation reaction 4.0h, obtain target product cocamidopropyl propyl amide-2-hydroxyl-3-sulfopropyl betaine, molecular weight is 429.
Embodiment 3
Present embodiment step 1: add 500kg coco-nut oil fatty acid (purchasing in Shandong Boxing Huarun Grease Chemical Co., Ltd) in reactor, be stirred and heated to 105~110 ℃, begin to drip 390kg N, the N-dimethylated propyl diethylenetriamine adds insulation reaction 1.0h.At pressure 200Pa, 140 ℃ of insulation reaction 1.0h of temperature, obtain the intermediate coconut oleoyl amine then.
Step 2: add the 222kg epoxy chloropropane in reactor, be stirred and heated to 40~45 ℃, beginning adds 324kg anhydrous sodium sodium pyrosulfate in batches, adds insulation reaction 3.0h, obtains intermediate chlorine hydroxypropyl azochlorosulfonate acid sodium.
Step 3: in reactor, add 667kg intermediate coconut oleoyl amine, be heated to 60~65 ℃, add 113kg sodium hydroxide, beginning adds 467kg intermediate chlorine hydroxypropyl azochlorosulfonate acid sodium in batches, add insulation reaction 2.0h, obtain target product cocamidopropyl propyl amide-2-hydroxyl-3-sulfopropyl betaine, molecular weight is 429.

Claims (10)

1, the synthetic method of a kind of cocamidopropyl propyl amide-2-hydroxyl-3-sulfopropyl betaine, with coco-nut oil fatty acid, N, N-dimethylated propyl diethylenetriamine, epoxy chloropropane, anhydrous sodium sodium pyrosulfate are raw material, it is characterized in that concrete steps are:
(1) with coco-nut oil fatty acid and N, N-dimethylated propyl diethylenetriamine amidate action generates the intermediate coconut oleoyl amine; Reaction equation is:
Figure A2009101020170002C1
(RCO is a cocoyl)
(2) again epoxy chloropropane and the addition reaction of anhydrous sodium sodium pyrosulfate are generated intermediate chlorine hydroxypropyl azochlorosulfonate acid sodium; Reaction equation is:
Figure A2009101020170002C2
(3) quaterisation takes place in the intermediate hydroxypropyl azochlorosulfonate acid sodium that makes of intermediate coconut oleoyl amine that at last step (1) is made and step (1) in the presence of catalyzer, generates target product cocamidopropyl propyl amide-2-hydroxyl-3-sulfopropyl betaine; Reaction equation is:
Figure A2009101020170002C3
(RCO is a cocoyl).
2, the synthetic method of cocamidopropyl propyl amide as claimed in claim 1-2-hydroxyl-3-sulfopropyl betaine, it is characterized in that: described coco-nut oil fatty acid and N, the mass ratio of N-dimethylated propyl diethylenetriamine are 1: 0.49~0.78.
3, the synthetic method of cocamidopropyl propyl amide as claimed in claim 2-2-hydroxyl-3-sulfopropyl betaine, it is characterized in that: described coco-nut oil fatty acid and N, the mass ratio of N-dimethylated propyl diethylenetriamine are 1: 0.59.
4, the synthetic method of cocamidopropyl propyl amide as claimed in claim 1-2-hydroxyl-3-sulfopropyl betaine, it is characterized in that: described coco-nut oil fatty acid and N, the amidate action of N-dimethylated propyl diethylenetriamine carries out in two stages: the fs, coco-nut oil fatty acid and N, salt-forming reaction takes place at 60~110 ℃ in the N-dimethylated propyl diethylenetriamine, generate ammonium salt, the reaction times is 1.0~4.0h; Subordinate phase, ammonium salt generate the intermediate coconut oleoyl amine 140~200 ℃ of dehydrations, and be reflected under the negative pressure and carry out, reaction pressure 20~200Pa, the reaction times is 1.0~4.0h.
5, the synthetic method of cocamidopropyl propyl amide as claimed in claim 1-2-hydroxyl-3-sulfopropyl betaine, it is characterized in that: the mass ratio of described epoxy chloropropane and anhydrous sodium sodium pyrosulfate is 1: 1.12~1.46; Temperature of reaction can be 40~90 ℃, and the reaction times can be 3.0~8.0.
6, the synthetic method of cocamidopropyl propyl amide as claimed in claim 5-2-hydroxyl-3-sulfopropyl betaine, it is characterized in that: the mass ratio of described epoxy chloropropane and anhydrous sodium sodium pyrosulfate is 1: 1.29.
7, the synthetic method of cocamidopropyl propyl amide as claimed in claim 1-2-hydroxyl-3-sulfopropyl betaine is characterized in that: the mass ratio of described intermediate coconut oleoyl amine and intermediate chlorine hydroxypropyl azochlorosulfonate acid sodium is 1: 0.65~0.70; Temperature of reaction can be 60~90 ℃, and the reaction times can be 2.0~8.0h.
8, the synthetic method of cocamidopropyl propyl amide as claimed in claim 7-2-hydroxyl-3-sulfopropyl betaine is characterized in that: the mass ratio of described intermediate coconut oleoyl amine and intermediate chlorine hydroxypropyl azochlorosulfonate acid sodium is 1: 0.67.
9, the synthetic method of cocamidopropyl propyl amide as claimed in claim 1-2-hydroxyl-3-sulfopropyl betaine, it is characterized in that: described intermediate coconut oleoyl amine and intermediate chlorine hydroxypropyl azochlorosulfonate acid sodium catalyst for reaction are a kind of in sodium hydroxide, the potassium hydroxide, and the catalyzer add-on is 1~10% of intermediate coconut oleoyl amine and an intermediate chlorine hydroxypropyl azochlorosulfonate acid sodium total mass.
10, the synthetic method of cocamidopropyl propyl amide as claimed in claim 9-2-hydroxyl-3-sulfopropyl betaine is characterized in that: the molecular weight of described product cocamidopropyl propyl amide-2-hydroxyl-3-sulfopropyl betaine is 429.
CN200910102017A 2009-08-27 2009-08-27 Synthesis method of cocamidopropyl-2-hydroxy-3-sulfopropyl betaine Pending CN101654421A (en)

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Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101856600A (en) * 2010-06-25 2010-10-13 西北大学 Amphoteric ionic Gemini surfactant and synthetic method thereof
CN102503864A (en) * 2011-10-28 2012-06-20 广州花语精细化工有限公司 Method for synthesizing low-salt fatty acid amide propyl hydroxy sulfobetaine
CN102863948A (en) * 2012-10-14 2013-01-09 东北石油大学 Hydroxysulfobetaine amphoteric surfactant for flooding and preparation method of hydroxysulfobetaine amphoteric surfactant
CN106701052A (en) * 2017-01-16 2017-05-24 中国石油大学(华东) Microbial-chemical composite oil displacement agent and preparation method and application thereof
CN108948342A (en) * 2018-08-07 2018-12-07 江苏四新界面剂科技有限公司 A kind of preparation method of the chain of oxyethylene group containing poly amphoteric surfactant
CN110845372A (en) * 2019-11-26 2020-02-28 陕西科技大学 Multiolefin hook type surfactant gel fracturing fluid and preparation and gel breaking methods thereof
CN110950785A (en) * 2019-11-26 2020-04-03 陕西科技大学 Twin-tail hook type viscoelastic surfactant gel, preparation method thereof and gel removing method
CN112956478A (en) * 2021-02-19 2021-06-15 广西汇丰生物科技有限公司 Synergistic composition and application thereof in pesticide preparation of aqueous suspension
CN112980419A (en) * 2019-12-13 2021-06-18 中国石油天然气股份有限公司 Thick oil foaming agent and preparation method and application thereof

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101856600A (en) * 2010-06-25 2010-10-13 西北大学 Amphoteric ionic Gemini surfactant and synthetic method thereof
CN102503864A (en) * 2011-10-28 2012-06-20 广州花语精细化工有限公司 Method for synthesizing low-salt fatty acid amide propyl hydroxy sulfobetaine
CN102863948A (en) * 2012-10-14 2013-01-09 东北石油大学 Hydroxysulfobetaine amphoteric surfactant for flooding and preparation method of hydroxysulfobetaine amphoteric surfactant
CN106701052A (en) * 2017-01-16 2017-05-24 中国石油大学(华东) Microbial-chemical composite oil displacement agent and preparation method and application thereof
CN106701052B (en) * 2017-01-16 2019-02-19 中国石油大学(华东) A kind of microbial-chemical compound oil displacement agent and its preparation method and application
CN108948342A (en) * 2018-08-07 2018-12-07 江苏四新界面剂科技有限公司 A kind of preparation method of the chain of oxyethylene group containing poly amphoteric surfactant
CN110845372A (en) * 2019-11-26 2020-02-28 陕西科技大学 Multiolefin hook type surfactant gel fracturing fluid and preparation and gel breaking methods thereof
CN110950785A (en) * 2019-11-26 2020-04-03 陕西科技大学 Twin-tail hook type viscoelastic surfactant gel, preparation method thereof and gel removing method
CN110950785B (en) * 2019-11-26 2021-10-01 陕西科技大学 Twin-tail hook type viscoelastic surfactant gel, preparation method thereof and gel removing method
CN112980419A (en) * 2019-12-13 2021-06-18 中国石油天然气股份有限公司 Thick oil foaming agent and preparation method and application thereof
CN112980419B (en) * 2019-12-13 2023-01-10 中国石油天然气股份有限公司 Thick oil foaming agent and preparation method and application thereof
CN112956478A (en) * 2021-02-19 2021-06-15 广西汇丰生物科技有限公司 Synergistic composition and application thereof in pesticide preparation of aqueous suspension

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Application publication date: 20100224