CN107903167A - A kind of low smell zinc stearate preparation method - Google Patents

A kind of low smell zinc stearate preparation method Download PDF

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Publication number
CN107903167A
CN107903167A CN201711161529.1A CN201711161529A CN107903167A CN 107903167 A CN107903167 A CN 107903167A CN 201711161529 A CN201711161529 A CN 201711161529A CN 107903167 A CN107903167 A CN 107903167A
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CN
China
Prior art keywords
vacuum
smell
catalyst
low
zinc stearate
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Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
CN201711161529.1A
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Chinese (zh)
Inventor
吴旅良
洪颖
熊洪龙
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JIANGXI HONGYUAN CHEMICAL CO Ltd
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JIANGXI HONGYUAN CHEMICAL CO Ltd
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Publication date
Application filed by JIANGXI HONGYUAN CHEMICAL CO Ltd filed Critical JIANGXI HONGYUAN CHEMICAL CO Ltd
Priority to CN201711161529.1A priority Critical patent/CN107903167A/en
Publication of CN107903167A publication Critical patent/CN107903167A/en
Pending legal-status Critical Current

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    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C51/00Preparation of carboxylic acids or their salts, halides or anhydrides
    • C07C51/41Preparation of salts of carboxylic acids
    • C07C51/412Preparation of salts of carboxylic acids by conversion of the acids, their salts, esters or anhydrides with the same carboxylic acid part
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C51/00Preparation of carboxylic acids or their salts, halides or anhydrides
    • C07C51/42Separation; Purification; Stabilisation; Use of additives
    • C07C51/43Separation; Purification; Stabilisation; Use of additives by change of the physical state, e.g. crystallisation

Abstract

A kind of low smell zinc stearate preparation method is that aliphatic acid is put into reaction kettle, opens stirring heating, after its melting, under the conditions of 0.01 0.02 MPa, 90 DEG C, 10 15min are evacuated by micro-vacuum, to remove the low boiling point molecule containing peculiar smell in most of stearic acid;Zinc oxide and catalyst are sequentially added afterwards, is warming up to 130 135 DEG C, opens 0.03 0.04MPa of vacuum, low vacuum is carried out and eliminates the unusual smell operation, and from milky being changed into clear up to reaction solution color, i.e. the reaction was complete;0.05 0.08 MPa of vacuum is opened afterwards, is carried out high vacuum and is eliminated the unusual smell operation, finally discharging crushing.The low smell zinc stearate preparation method of the present invention, due to eliminating the unusual smell technology with three rank vacuum of original creation during the reaction, obtained zinc stearate smell is lower, purity higher is completely suitable for low smell plastic field.

Description

A kind of low smell zinc stearate preparation method
Technical field
The present invention relates to rubber and plastics auxiliaries field, especially a kind of low smell zinc stearate preparation method.
Background technology
The application of plastics on the living conditions is more and more, low VOC, low as people are to ride comfort, healthy and safe requirement The plastics of smell are favored be subject to vast producer, especially upper in the application such as auto plastics, Yoga mat, have gradually formed low smell Plastic industry.Zinc stearate also has the corresponding industry low as common auxiliary agent in plastics-production in low smell plastic field Odor requirements, it is necessary to tested by corresponding smell, generally require smell Deng Ji≤2.Existing smell grading reference, is divided into 1- 6 grades, 1 grade of evaluation criterion:It cannot experience;2 grades of evaluation criterions:It can experience, it is unobstructive;3 grades of evaluation marks It is accurate:Can substantially it experience, but without too big obstruction;4 grades of evaluation criterions:There is obstruction;5 grades of evaluation criterions:There is larger obstruction;6 Level evaluation criterion:It is difficult to endure.
In recent years, production zinc stearate mainly has two methods:One kind is produced using double decomposition, first in stearic acid Caustic soda is added to carry out neutralization reaction, then zincification salt carries out metathesis reaction, and the hard of monomer is formed after dehydration, dry, crushing, packaging Resin acid zinc, the zinc stearate oder levels of output are general >=and 3, and purity is low, is not suitable for low smell plastic field;Second of side Method application colter machine or kneader directly react stearic acid and zinc oxide, catalyst at a certain temperature produces monomer Zinc stearate, the zinc stearate of output is high compared with the first purity, but oder levels are generally >=2, are not also suitable for low smell plastic Field.
The content of the invention
It is an object of the invention to provide a kind of low smell zinc stearate preparation method, the preparation method technique is simple, institute The zinc stearate oder levels of preparation are less than or equal to 2 grades.
A kind of low smell zinc stearate preparation method of the present invention is that aliphatic acid is put into reaction kettle, opens stirring and rises Temperature is to 80-90 DEG C, and after its melting, under the conditions of 0.01-0.02 MPa, 90 DEG C, 10-15min is evacuated by micro-vacuum, with Remove the low boiling point molecule containing peculiar smell in most of stearic acid;Zinc oxide and catalyst, zinc oxide and fat are sequentially added afterwards The mass ratio of fat acid is 15-17:100, catalyst is divided into main effect catalyst and subsidiary catalyst, main effect catalyst for glacial acetic acid or Hydrogen peroxide or monohydric alcohol or polyalcohol or citric acid, subsidiary catalyst are water, and the addition of main effect catalyst is the 2- of aliphatic acid 2.5%, the addition of subsidiary catalyst is 5 times of main effect catalyst, is warming up to 130-135 DEG C, after keeping the temperature 30min, opens vacuum 0.03-0.04MPa, carries out low vacuum and eliminates the unusual smell operation, and being changed into clear from milky up to reaction solution color reacts Completely;Vacuum 0.05-0.08 MPa are opened afterwards, are carried out high vacuum and are eliminated the unusual smell operation, duration 20-25min, finally discharges Crush.
The present invention a kind of low smell zinc stearate preparation method, aliphatic acid selection using palmitic acid, hydrogenated oil and fat, stearic acid as Selection, design parameter is C14≤1%, C16:55-61%, C18:39-44%, acid number:205-211mgKOH/g, iodine number≤0.5 gI2/100g;Zinc oxide:Indirect method manufactures, content >=99.7%, moisture≤0.3%, 325 mesh percent of pass 99.9% of fineness;It is micro- true During sky eliminates the unusual smell, the low boiling point molecule of the peculiar smell contained in most of stearic acid can be removed, low vacuum can avoid stearic acid Molecule scatters and disappears;During low vacuum eliminates the unusual smell, after zinc oxide and catalyst is finished, more than 80% after material reaction 30min Material is reacted, carries out vacuum at this time and eliminates the unusual smell operation most preferably, farthest reduces out influence of the vacuum to reaction, And further odor molecules can be detached;High vacuum eliminates the unusual smell, which can reach the effect except aqueous vapor, and allow water to steam at the same time Gas further takes away more odor molecules, and temperature of charge can faster be reduced.Due to having used original creation during the reaction Three rank vacuum eliminate the unusual smell technology, and obtained zinc stearate smell is lower, and purity higher is completely suitable for low smell plastic field.
Embodiment
A kind of low smell zinc stearate preparation method is that 100Kg aliphatic acid is put into reaction kettle, opens stirring and is warming up to 80-90 DEG C, after its melting, under the conditions of 0.01-0.02 MPa, 90 DEG C, 15min is evacuated by micro-vacuum;Add successively afterwards Enter 16Kg zinc oxide, 2Kg hydrogen peroxide, 10Kg water, be warming up to 130-135 DEG C, after keeping the temperature 30min, open vacuum 0.03- 0.04MPa, carries out low vacuum and eliminates the unusual smell operation, is changed into clear from milky up to reaction solution color, i.e., the reaction was complete; Vacuum 0.05-0.08 MPa are opened afterwards, are carried out high vacuum and are eliminated the unusual smell operation, duration 20-25min, finally discharging crushing.

Claims (3)

  1. A kind of 1. low smell zinc stearate preparation method, it is characterised in that:Aliphatic acid is put into reaction kettle first, opens stirring 80-90 DEG C is warming up to, after its melting, under the conditions of 0.01-0.02 MPa, 90 DEG C, 10-15min is evacuated by micro-vacuum; Zinc oxide and catalyst are sequentially added afterwards, and catalyst is divided into main effect catalyst and subsidiary catalyst, and main effect catalyst is ice vinegar Acid or hydrogen peroxide or monohydric alcohol or polyalcohol or citric acid, subsidiary catalyst are water, are warming up to 130-135 DEG C, keep the temperature 30min Afterwards, vacuum 0.03-0.04MPa is opened, low vacuum is carried out and eliminates the unusual smell operation, be changed into clarifying from milky up to reaction solution color It is transparent that i.e. the reaction was complete;Vacuum 0.05-0.08 MPa are opened afterwards, are carried out high vacuum and are eliminated the unusual smell operation, duration 20- 25min, finally discharging crush.
  2. A kind of 2. low smell zinc stearate preparation method according to claim 1, it is characterised in that:The zinc oxide with The mass ratio of aliphatic acid is 15-17:100.
  3. A kind of 3. low smell zinc stearate preparation method according to claim 1, it is characterised in that:The main effect catalyst Addition be aliphatic acid 2-2.5%, the addition of subsidiary catalyst is 5 times of main effect catalyst.
CN201711161529.1A 2017-11-21 2017-11-21 A kind of low smell zinc stearate preparation method Pending CN107903167A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201711161529.1A CN107903167A (en) 2017-11-21 2017-11-21 A kind of low smell zinc stearate preparation method

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Application Number Priority Date Filing Date Title
CN201711161529.1A CN107903167A (en) 2017-11-21 2017-11-21 A kind of low smell zinc stearate preparation method

Publications (1)

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CN107903167A true CN107903167A (en) 2018-04-13

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CN (1) CN107903167A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110205179A (en) * 2019-06-11 2019-09-06 中山华明泰科技股份有限公司 A kind of preparation method and application of hydroxy fatty acid lithium
CN113717040A (en) * 2020-05-26 2021-11-30 东莞市汉维科技股份有限公司 Clean production process for synthesizing zinc laurate by melting method
CN115193475A (en) * 2022-08-11 2022-10-18 广州天赐高新材料股份有限公司 Preparation and application of catalyst for fatty acyl sulfonate surfactant synthesis

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105131203A (en) * 2015-07-28 2015-12-09 绍兴佳华高分子材料股份有限公司 Preparation method for polypropylene grafted maleic anhydride with high graft ratio and low odor
CN105348072A (en) * 2015-11-11 2016-02-24 江门市胜鹏化工实业有限公司 Modified zinc stearate production technology
CN107311855A (en) * 2017-07-31 2017-11-03 郑州庆宏塑胶科技有限公司 A kind of preparation method of stearate

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105131203A (en) * 2015-07-28 2015-12-09 绍兴佳华高分子材料股份有限公司 Preparation method for polypropylene grafted maleic anhydride with high graft ratio and low odor
CN105348072A (en) * 2015-11-11 2016-02-24 江门市胜鹏化工实业有限公司 Modified zinc stearate production technology
CN107311855A (en) * 2017-07-31 2017-11-03 郑州庆宏塑胶科技有限公司 A kind of preparation method of stearate

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110205179A (en) * 2019-06-11 2019-09-06 中山华明泰科技股份有限公司 A kind of preparation method and application of hydroxy fatty acid lithium
CN110205179B (en) * 2019-06-11 2021-08-17 中山华明泰科技股份有限公司 Preparation method and application of hydroxy fatty acid lithium
CN113717040A (en) * 2020-05-26 2021-11-30 东莞市汉维科技股份有限公司 Clean production process for synthesizing zinc laurate by melting method
CN115193475A (en) * 2022-08-11 2022-10-18 广州天赐高新材料股份有限公司 Preparation and application of catalyst for fatty acyl sulfonate surfactant synthesis

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Application publication date: 20180413

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