CN107903167A - A kind of low smell zinc stearate preparation method - Google Patents
A kind of low smell zinc stearate preparation method Download PDFInfo
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- 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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- vacuum
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- zinc stearate
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C51/00—Preparation of carboxylic acids or their salts, halides or anhydrides
- C07C51/41—Preparation of salts of carboxylic acids
- C07C51/412—Preparation of salts of carboxylic acids by conversion of the acids, their salts, esters or anhydrides with the same carboxylic acid part
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C51/00—Preparation of carboxylic acids or their salts, halides or anhydrides
- C07C51/42—Separation; Purification; Stabilisation; Use of additives
- C07C51/43—Separation; Purification; Stabilisation; Use of additives by change of the physical state, e.g. crystallisation
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- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Crystallography & Structural Chemistry (AREA)
- Compositions Of Macromolecular Compounds (AREA)
- Fats And Perfumes (AREA)
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
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)
- 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.
- 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.
- 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.
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CN201711161529.1A CN107903167A (en) | 2017-11-21 | 2017-11-21 | A kind of low smell zinc stearate preparation method |
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CN201711161529.1A CN107903167A (en) | 2017-11-21 | 2017-11-21 | A kind of low smell zinc stearate preparation method |
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Cited By (3)
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)
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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 |
-
2017
- 2017-11-21 CN CN201711161529.1A patent/CN107903167A/en active Pending
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
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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)
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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