CN107469411B - A kind of preparation method of organic silicon defoamer - Google Patents

A kind of preparation method of organic silicon defoamer Download PDF

Info

Publication number
CN107469411B
CN107469411B CN201710873378.6A CN201710873378A CN107469411B CN 107469411 B CN107469411 B CN 107469411B CN 201710873378 A CN201710873378 A CN 201710873378A CN 107469411 B CN107469411 B CN 107469411B
Authority
CN
China
Prior art keywords
organic silicon
parts
preparation
silicon defoamer
reaction mixture
Prior art date
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.)
Active
Application number
CN201710873378.6A
Other languages
Chinese (zh)
Other versions
CN107469411A (en
Inventor
王秀凤
刘芳
尹凯欣
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
GUANGDONG REBON HI-TECH MATERIAL CO., LTD.
Original Assignee
Guangdong Rebon Hi-Tech Material Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Guangdong Rebon Hi-Tech Material Co Ltd filed Critical Guangdong Rebon Hi-Tech Material Co Ltd
Priority to CN201710873378.6A priority Critical patent/CN107469411B/en
Publication of CN107469411A publication Critical patent/CN107469411A/en
Application granted granted Critical
Publication of CN107469411B publication Critical patent/CN107469411B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D19/00Degasification of liquids
    • B01D19/02Foam dispersion or prevention
    • B01D19/04Foam dispersion or prevention by addition of chemical substances
    • B01D19/0404Foam dispersion or prevention by addition of chemical substances characterised by the nature of the chemical substance
    • B01D19/0409Foam dispersion or prevention by addition of chemical substances characterised by the nature of the chemical substance compounds containing Si-atoms

Landscapes

  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Toxicology (AREA)
  • Dispersion Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Silicon Polymers (AREA)

Abstract

The invention belongs to chemical technology fields, and in particular to a kind of preparation method of organic silicon defoamer.The present invention is using silicone oil as base-material; it is modified using methylvinyldichlorosilane monomer; increase the silicon oxygen bond in silicone oil, reuses maleic anhydride and protected, increase its acid-proof alkaline; then by carrying out graft reaction with allyl polyethenoxy ether; Polyether Modified Polysiloxanes Defoaming Agent is formed, while under the action of ammonium glycyrrhetate, the strong hydro-oleophobicity for defoaming agent of having releived; stability is increased, the appearance of the lamination of defoaming agent is prevented.

Description

A kind of preparation method of organic silicon defoamer
Technical field
The invention belongs to chemical technology fields, and in particular to a kind of preparation method of organic silicon defoamer.
Background technique
Defoaming agent is a kind of widely used fine chemicals, is mainly used for eliminating and inhibiting various unwanted bubbles.As Defoaming agent should have insoluble in foam liquid or indissoluble, surface tension lower than foam liquid, with foam liquid have certain compatibility, with Chemical reaction and the small grade fundamental characteristics of volatility do not occur for foam liquid.There are many type of defoaming agent, common on general industry It is broadly divided into three classes: organic defoaming agent (alcohols, lipid, amide etc.), organic silicon defoamer and polyether antifoam agent.It is wherein organic Silicon and polyether antifoam agent application field are the most extensive, and dosage is also larger.Organic silicon defoamer with its slightly solubility, low surface tension, The advantages that preferable chemistry and thermal stability, outstanding antifoaming performance, receives significant attention, whether aqueous systems or There are defoaming suds suppressing properties well in non-aqueous system.But due to its siloxane main chain in the environment of strong acid and strong base easy fracture and The strong hydro-oleophobicity of itself is subject to certain restrictions it in the application of the industries such as biofermentation, copy paper, printing and dyeing.Polyethers defoaming Agent is by ethylene oxide, a kind of nonionic surfactant of function admirable made from propylene oxide ring-opening polymerisation.It is widely used in In aqueous systems, there are good hydrophily and antifoaming ability.But its antifoaming speed is not good enough, and temperature sensitive, need to cloud point with Upper use.Inhibiting the common method of these foams is addition polyether antifoam agent or organic silicon defoamer, the defoaming of polyethers defoaming agent Ability is weak, and foam inhibition ability is strong, and organic silicon defoaming agent brokenly bubble power is strong, antifoaming speed is fast, but foam inhibition ability is weak.But individually make With polyether antifoam agent or the defoaming agent of organosilicon, defoaming and foam inhibition persistence duality immediately can not be often had both simultaneously Matter.Therefore the producer having sells after mixing organic silicon defoamer and polyether antifoam agent, to obtain preferable resultant effect, but Only two kinds of defoaming agents are simply mixed, not only comprehensive performance is still not ideal enough, but also this defoaming agent stability often exists Problem, the generation for phenomena such as will lead to layering, when addition, will cause different periods antifoam content and the uneven situation of performance.
Summary of the invention
The technical problems to be solved by the invention: for current defoaming agent be by organic silicon defoamer and polyether antifoam agent into Row is simply mixed, and easily leads to that defoaming agent is unstable, and the problem of layering, the present invention provides a kind of systems of organic silicon defoamer Preparation Method.
In order to solve the above technical problems, the present invention is using technical solution as described below:
A kind of preparation method of organic silicon defoamer, the preparation method include the following steps:
(1) according to parts by weight, 80~90 parts of silicone oil, 30~35 parts of linolenic acids, 20~25 parts of methyl ethylene dichloros are taken Silicone oil, linolenic acid and additive, are put by silane, 8~11 parts of maleic anhydrides, 4~7 parts of catalyst and 1~3 part of additive first In reactor, using nitrogen protection, preheated at 60~65 DEG C;
(2) after preheating, methylvinyldichlorosilane, maleic anhydride, catalyst is added, is warming up to 90~95 DEG C Under reacted, it is cooling, collect reaction mixture;
(3) reaction mixture, allyl polyethenoxy ether and dimethylbenzene are put into reaction kettle, use sodium hydroxide solution PH to 8.0~8.5 is adjusted, 1.2~1.5MPa is boosted to using carbon dioxide, is stirred at 80~95 DEG C:
(4) after stirring, emulsifier and ammonium glycyrrhetate is added, is warming up at 108~115 DEG C, is reacted, out Material, collects out material, filters, and collects filtered fluid, and distill to filtered fluid, recycles dimethylbenzene, collects distillation residue, i.e., Obtain organic silicon defoamer.
Catalyst is alumina silicate, any one in lewis acid in the step (1).
The step (1) is that additive is titanium dioxide, any one in phosphomolybdic acid.
The mass ratio of step (3) reaction mixture, allyl polyethenoxy ether and dimethylbenzene is 8~11:3~5: 13。
The additional amount of emulsifier is the 1~1.2% of reaction mixture quality, the addition of ammonium glycyrrhetate in the step (4) Amount is the 0.6~1.0% of reaction mixture quality, and emulsifier is any one in stearoyl lactate or stearyl lactate Kind.
The present invention is compared with other methods, and advantageous effects are:
The present invention is modified it using methylvinyldichlorosilane monomer using silicone oil as base-material, increases silicone oil In silicon oxygen bond, reuse maleic anhydride and protected, increase its acid-proof alkaline, then by with allyl polyethenoxy ether Carry out graft reaction, form Polyether Modified Polysiloxanes Defoaming Agent, while under the action of ammonium glycyrrhetate, defoaming agent of having releived it is strong Hydro-oleophobicity increases stability, prevents the appearance of the lamination of defoaming agent.
Specific embodiment
Catalyst is selected as alumina silicate, any one in lewis acid.
Additive is selected as titanium dioxide, any one in phosphomolybdic acid.
Any one being selected as in stearoyl lactate or stearyl lactate of emulsifier.
A kind of preparation method of organic silicon defoamer, the preparation method include the following steps:
(1) according to parts by weight, 80~90 parts of silicone oil, 30~35 parts of linolenic acids, 20~25 parts of methyl ethylene dichloros are taken Silicone oil, linolenic acid and additive, are put by silane, 8~11 parts of maleic anhydrides, 4~7 parts of catalyst and 1~3 part of additive first In reactor, using nitrogen protection, 30~35min is preheated at 60~65 DEG C;
(2) after preheating, methylvinyldichlorosilane, maleic anhydride, catalyst is added, is warming up to 90~95 DEG C Under carry out 2~4h of reaction, it is cooling, collect reaction mixture;
(3) it is in mass ratio 8~11:3~5:13, reaction mixture, allyl polyethenoxy ether and dimethylbenzene is put into In reaction kettle, pH to 8.0~8.5 is adjusted using sodium hydroxide solution, 1.2~1.5MPa is boosted to using carbon dioxide, 80 1~3h is stirred at~95 DEG C:
(4) after stirring, emulsifier and ammonium glycyrrhetate is added, the additional amount of emulsifier is reaction mixture quality 1~1.2%, the additional amount of ammonium glycyrrhetate is the 0.6~1.0% of reaction mixture quality, is warming up at 108~115 DEG C, is carried out 4~6h is reacted, material is collected out in discharging, is filtered, and collects filtered fluid, and distill to filtered fluid, recycles dimethylbenzene, is collected Residue is distilled to get organic silicon defoamer.
Example 1
Catalyst is selected as alumina silicate.
Additive is selected as phosphomolybdic acid.
Emulsifier is selected as stearyl lactate.
A kind of preparation method of organic silicon defoamer, the preparation method include the following steps:
(1) according to parts by weight, 85 parts of silicone oil, 33 parts of linolenic acids, 23 parts of methylvinyldichlorosilanes, 10 parts of Malaysias are taken Silicone oil, linolenic acid and additive, are put into reactor by acid anhydrides, 5 parts of catalyst and 2 parts of additives first, using nitrogen protection, 33min is preheated at 63 DEG C;
(2) after preheating, be added methylvinyldichlorosilane, maleic anhydride, catalyst, be warming up at 93 DEG C into Row reaction 3h, cooling, collection reaction mixture;
(3) it is in mass ratio 9:4:13, reaction mixture, allyl polyethenoxy ether and dimethylbenzene is put into reaction kettle In, pH to 8.3 is adjusted using sodium hydroxide solution, 1.3MPa is boosted to using carbon dioxide, stirs 2h at 85 DEG C:
(4) after stirring, emulsifier and ammonium glycyrrhetate is added, the additional amount of emulsifier is reaction mixture quality 1.1%, the additional amount of ammonium glycyrrhetate is the 0.8% of reaction mixture quality, is warming up at 140 DEG C, carries out reaction 5h, is discharged, Collect out material, filter, collect filtered fluid, and filtered fluid is distilled, recycle dimethylbenzene, collect distillation residue to get Organic silicon defoamer.
Example 2
Catalyst is selected as alumina silicate, any one in lewis acid.
Additive is selected as titanium dioxide, any one in phosphomolybdic acid.
Any one being selected as in stearoyl lactate or stearyl lactate of emulsifier.
A kind of preparation method of organic silicon defoamer, the preparation method include the following steps:
(1) according to parts by weight, 90 parts of silicone oil, 35 parts of linolenic acids, 25 parts of methylvinyldichlorosilanes, 11 parts of Malaysias are taken Silicone oil, linolenic acid and additive, are put into reactor by acid anhydrides, 7 parts of catalyst and 3 parts of additives first, using nitrogen protection, 35min is preheated at 65 DEG C;
(2) after preheating, be added methylvinyldichlorosilane, maleic anhydride, catalyst, be warming up at 95 DEG C into Row reaction 4h, cooling, collection reaction mixture;
(3) it is in mass ratio 11:5:13, reaction mixture, allyl polyethenoxy ether and dimethylbenzene is put into reaction kettle In, pH to 8.5 is adjusted using sodium hydroxide solution, 1.5MPa is boosted to using carbon dioxide, stirs 3h at 95 DEG C:
(4) after stirring, emulsifier and ammonium glycyrrhetate is added, the additional amount of emulsifier is reaction mixture quality 1.2%, the additional amount of ammonium glycyrrhetate is the 1.0% of reaction mixture quality, is warming up at 115 DEG C, carries out reaction 6h, is discharged, Collect out material, filter, collect filtered fluid, and filtered fluid is distilled, recycle dimethylbenzene, collect distillation residue to get Organic silicon defoamer.
Example 3
Catalyst is selected as alumina silicate.
Additive is selected as titanium dioxide.
Emulsifier is selected as stearoyl lactate.
A kind of preparation method of organic silicon defoamer, the preparation method include the following steps:
(1) according to parts by weight, 80 parts of silicone oil, 30 parts of linolenic acids, 20 parts of methylvinyldichlorosilanes, 8 parts of Malaysias are taken Silicone oil, linolenic acid and additive, are put into reactor by acid anhydrides, 4 parts of catalyst and 1 part of additive first, using nitrogen protection, 30min is preheated at 60 DEG C;
(2) after preheating, be added methylvinyldichlorosilane, maleic anhydride, catalyst, be warming up at 90 DEG C into Row reaction 2h, cooling, collection reaction mixture;
(3) it is in mass ratio 8:3:13, reaction mixture, allyl polyethenoxy ether and dimethylbenzene is put into reaction kettle In, pH to 8.0 is adjusted using sodium hydroxide solution, 1.2MPa is boosted to using carbon dioxide, stirs 1h at 80 DEG C;
(4) after stirring, emulsifier and ammonium glycyrrhetate is added, the additional amount of emulsifier is reaction mixture quality 1%, the additional amount of ammonium glycyrrhetate is the 0.6% of reaction mixture quality, is warming up at 108 DEG C, carries out reaction 4h, is discharged, and is received Collect material out, filter, collect filtered fluid, and distill to filtered fluid, recycle dimethylbenzene, collects distillation residue to get having Machine silicon defoaming agent.
Comparative example: the organic silicon defoamer of Changzhou chemical company production
Method: organic silicon defoamer prepared by embodiment 1,2,3 and comparative example is compared into test, in the amount of 100ml The expanding foam solution of 50ml is added in cylinder, adds the defoaming liquid of 0.2g, closes the lid, rock, observation comparison.
Defoaming agent detection case table such as table 1
Table 1
Detection project Embodiment 1 Embodiment 2 Embodiment 3 Comparative example
Foam time/s 18.2 19.6 22.5 15.4
The foam inhibition time/min 16.8 18.5 20.0 12.3
High-temperature stability There is floating oil There is oil slick Stablize Floating oil is obvious
Low-temperature stability Stablize Stablize Stablize There is precipitate
Centrifugal stability It is not stratified It is not stratified It is not stratified Slightly it is layered
From the foregoing, it will be observed that the problem of present invention defoaming agent performance produced is stablized, is not susceptible to layering, is worthy to be popularized and makes With.

Claims (5)

1. a kind of preparation method of organic silicon defoamer, which is characterized in that the preparation method includes the following steps:
Step (1): according to parts by weight, 80~90 parts of silicone oil, 30~35 parts of linolenic acids, 20~25 parts of methyl ethylene dichloros are taken Silicone oil, linolenic acid and additive, are put by silane, 8~11 parts of maleic anhydrides, 4~7 parts of catalyst and 1~3 part of additive first In reactor, using nitrogen protection, preheated at 60~65 DEG C;
Step (2): after preheating, methylvinyldichlorosilane, maleic anhydride, catalyst is added, is warming up to 90~95 It is reacted at DEG C, it is cooling, collect reaction mixture;
Step (3): reaction mixture, allyl polyethenoxy ether and dimethylbenzene are put into reaction kettle, molten using sodium hydroxide Liquid adjusts pH to 8.0~8.5, boosts to 1.2~1.5MPa using carbon dioxide, stirs at 80~95 DEG C:
Step (4): after stirring, emulsifier and ammonium glycyrrhetate is added, the additional amount of the ammonium glycyrrhetate is reaction mixing The 0.6~1.0% of amount of substance;It is warming up at 108~115 DEG C, is reacted, discharge, collect out material, filter, collect filtering Liquid, and filtered fluid is distilled, dimethylbenzene is recycled, collects distillation residue to get organic silicon defoamer.
2. the preparation method of organic silicon defoamer according to claim 1, which is characterized in that catalyst in the step (1) For any one in alumina silicate, lewis acid.
3. the preparation method of organic silicon defoamer according to claim 1, which is characterized in that step (1) additive is Any one in titanium dioxide, phosphomolybdic acid.
4. the preparation method of organic silicon defoamer according to claim 1, which is characterized in that step (3) the reaction mixing The mass ratio of object, allyl polyethenoxy ether and dimethylbenzene is 8~11:3~5:13.
5. the preparation method of organic silicon defoamer according to claim 1, which is characterized in that emulsifier in the step (4) Additional amount be the 1~1.2% of reaction mixture quality, emulsifier is any in stearoyl lactate or stearyl lactate It is a kind of.
CN201710873378.6A 2017-09-25 2017-09-25 A kind of preparation method of organic silicon defoamer Active CN107469411B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201710873378.6A CN107469411B (en) 2017-09-25 2017-09-25 A kind of preparation method of organic silicon defoamer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201710873378.6A CN107469411B (en) 2017-09-25 2017-09-25 A kind of preparation method of organic silicon defoamer

Publications (2)

Publication Number Publication Date
CN107469411A CN107469411A (en) 2017-12-15
CN107469411B true CN107469411B (en) 2019-07-26

Family

ID=60586360

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201710873378.6A Active CN107469411B (en) 2017-09-25 2017-09-25 A kind of preparation method of organic silicon defoamer

Country Status (1)

Country Link
CN (1) CN107469411B (en)

Families Citing this family (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108654148A (en) * 2018-06-27 2018-10-16 芜湖凌岳企业管理咨询有限公司 Antifoaming agent and preparation method thereof for wastewater treatment
CN109200632A (en) * 2018-09-11 2019-01-15 蓝凤祥 Multi-functional nontoxic high temperature silicone modified polyether industrial defoaming agent of one kind and preparation method thereof
CN109364535A (en) * 2018-10-29 2019-02-22 薛向东 A kind of high temperature resistant defoaming agent
CN111569475A (en) * 2020-05-28 2020-08-25 南京澳莉峰环保科技有限公司 Organic silicon emulsion defoaming agent and preparation method thereof
CN111748327B (en) * 2020-06-30 2022-10-18 中国石油天然气集团有限公司 Environment-friendly defoaming agent for drilling fluid and preparation method thereof
CN111713493B (en) * 2020-07-23 2021-10-29 陕西农塔生物数据研究有限公司 Synergistic insecticidal auxiliary agent
CN112143342A (en) * 2020-10-19 2020-12-29 徐州中捷环保科技有限公司 Metal protective coating and preparation method thereof

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102005006962A1 (en) * 2005-02-16 2006-08-24 Goldschmidt Gmbh Use of polysiloxane compound containing an organo silyloxycarbon bond, as antifoaming agent for liquid fuels e.g. hydraulic-, gear oil and fuel oil
CN100457803C (en) * 2006-11-28 2009-02-04 苏州大学 Fluoric alkoxyl propyl methyl silicone oil and its prepn process
CN105531005B (en) * 2013-08-13 2018-12-28 美国陶氏有机硅公司 The method for forming defoaming agent particle
CN104436767B (en) * 2014-12-24 2016-05-18 江苏四新科技应用研究所股份有限公司 A kind of silicon composition and preparation thereof, application
CN106621477A (en) * 2016-10-18 2017-05-10 合肥新万成环保科技有限公司 Hyperbranched polyether modified organic silicon defoamer with low dosage and preparation method of defoamer

Also Published As

Publication number Publication date
CN107469411A (en) 2017-12-15

Similar Documents

Publication Publication Date Title
CN107469411B (en) A kind of preparation method of organic silicon defoamer
CN104307215B (en) Vegetable oil modified defoaming agent and preparation method thereof
CN104245912B (en) The manufacture method of steel plate alkalis composition
CN103923323B (en) Preparation method of terpolymer defoamer
CN104436766B (en) A kind of silicon composition
CN103641195A (en) Organic silicon defoamer and preparation method thereof
CN102895805B (en) The preparation method of non-silicon defoaming agent
CN101798781A (en) Silicone defoaming agent for papermaking and pulping and preparation method thereof
CN106731034A (en) A kind of compound defoamer
CN103669108A (en) Organic silicon defoamer for paper making industry and preparation method thereof
CN104906832A (en) Polyether ester/mineral oil composite defoaming agent and preparation method thereof
CN105289048A (en) Organic silicon-modified polyether ester emulsion defoamer and preparation method thereof
CN102716600B (en) Method for improving foam suppression performance of organosilicone emulsion
CN106362441A (en) Organic silicon defoamer containing hydroxyl polyether modified epoxidized soybean oil and preparation method thereof
CN106390531A (en) Emulsified type hyperbranched polyether modified organic siliconde foamer and preparation method thereof
CN107537185A (en) A kind of self-emulsifying type defoamer and preparation method thereof
CN106215468A (en) A kind of silicone antifoaming agent and preparation method thereof
CN110960892A (en) Efficient water-based paint defoaming agent and preparation method thereof
JP3162593B2 (en) W / O emulsion type defoamer composition and defoaming method using the same
CN104606926B (en) Siloxane modified vegetable oil high molecular polyether defoaming agent and preparation method thereof
CN107648890A (en) A kind of oil industry defoaming agent composition and preparation method thereof
CN103111101A (en) Double-end-blocked polyether modified silicone-oil defoaming agent and method for preparing same
CN102718978B (en) Method for reducing viscosity of organic silicone emulsion
CN100355478C (en) High-temp. resistance organosilicon emulsion defoaming agents, and its synthetic method
CN104874208B (en) Acid and alkali-resistant organosilicone composite antifoaming agent and preparation method thereof

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
TA01 Transfer of patent application right
TA01 Transfer of patent application right

Effective date of registration: 20190612

Address after: 213000 35 North Zhijie street, Zhong Lou District, Changzhou, Jiangsu

Applicant after: Zou Feng

Address before: 213102 Jiangsu Changzhou Tianning District, Tsuen Shan Fu Qiang village, Zhou Jia Cun 321.

Applicant before: Changzhou Su Tong Ping Electromechanical Technology Co., Ltd.

TA01 Transfer of patent application right
TA01 Transfer of patent application right

Effective date of registration: 20190703

Address after: 510130 South China New Material Innovation Park G2 Building 619, No. 31 Kefeng Road, Science City, Guangzhou High-tech Industrial Development Zone, Guangdong Province

Applicant after: GUANGDONG REBON HI-TECH MATERIAL CO., LTD.

Address before: 213000 35 North Zhijie street, Zhong Lou District, Changzhou, Jiangsu

Applicant before: Zou Feng

GR01 Patent grant
GR01 Patent grant