[go: up one dir, main page]

CN105498303B - A kind of organic silicon defoamer and preparation method thereof - Google Patents

A kind of organic silicon defoamer and preparation method thereof Download PDF

Info

Publication number
CN105498303B
CN105498303B CN201510925719.0A CN201510925719A CN105498303B CN 105498303 B CN105498303 B CN 105498303B CN 201510925719 A CN201510925719 A CN 201510925719A CN 105498303 B CN105498303 B CN 105498303B
Authority
CN
China
Prior art keywords
defoamer
add
preparation
main
stirring
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.)
Expired - Fee Related
Application number
CN201510925719.0A
Other languages
Chinese (zh)
Other versions
CN105498303A (en
Inventor
聂兆广
胡艳芳
林伯群
姜丛慧
郑艺华
邢雅成
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.)
Qingdao University
Original Assignee
Qingdao University
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 Qingdao University filed Critical Qingdao University
Priority to CN201510925719.0A priority Critical patent/CN105498303B/en
Publication of CN105498303A publication Critical patent/CN105498303A/en
Application granted granted Critical
Publication of CN105498303B publication Critical patent/CN105498303B/en
Expired - Fee Related 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
    • 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
    • B01D19/0418Foam dispersion or prevention by addition of chemical substances characterised by the nature of the chemical substance compounds containing P-atoms
    • 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
    • B01D19/0422Foam dispersion or prevention by addition of chemical substances characterised by the nature of the chemical substance compounds containing S-atoms
    • 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
    • B01D19/0431Foam dispersion or prevention by addition of chemical substances characterised by the nature of the chemical substance containing aromatic rings
    • B01D19/0436Foam dispersion or prevention by addition of chemical substances characterised by the nature of the chemical substance containing aromatic rings with substituted groups
    • B01D19/0454Foam dispersion or prevention by addition of chemical substances characterised by the nature of the chemical substance containing aromatic rings with substituted groups which contain S-atoms

Landscapes

  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Toxicology (AREA)
  • Dispersion Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Degasification And Air Bubble Elimination (AREA)
  • Cosmetics (AREA)

Abstract

本发明属于消泡剂及制备技术领域,涉及一种复配型有机硅消泡剂及其制备方法,有机硅消泡剂中各组份重量百分比为:蒸馏水48%‑54%,二氧化硅1.1%‑2.48%,二甲基硅油38%‑48.5%,乳化剂1%‑3%,助乳化剂1%‑6%,稳定剂0.5%‑1%,总重量百分比为100%;制备时,先用二氧化硅和二甲基硅油制得主消泡剂,然后依次按比例向反应装置中加入蒸馏水、助乳化剂、乳化剂和稳定剂至完全溶解后再加入主消泡剂乳化,即得到有机硅消泡剂;其制备工艺简单,原料易得,成本低,制备的有机硅消泡剂在保持良好消抑泡性能的同时,具有高效、稳定、耐碱和耐热等特点。The invention belongs to the technical field of defoamers and their preparation, and relates to a composite silicone defoamer and a preparation method thereof. The weight percentage of each component in the silicone defoamer is: distilled water 48%-54%, silicon dioxide 1.1%-2.48%, simethicone 38%-48.5%, emulsifier 1%-3%, co-emulsifier 1%-6%, stabilizer 0.5%-1%, the total weight percentage is 100%; when preparing , first prepare the main defoamer with silicon dioxide and simethicone oil, then add distilled water, co-emulsifier, emulsifier and stabilizer to the reaction device in proportion to complete dissolution, and then add the main defoamer for emulsification, that is The organosilicon defoamer is obtained; the preparation process is simple, the raw materials are easy to obtain, and the cost is low. The prepared organosilicon defoamer has the characteristics of high efficiency, stability, alkali resistance and heat resistance while maintaining good defoaming and antifoaming performance.

Description

一种有机硅消泡剂及其制备方法A kind of organosilicon defoamer and preparation method thereof

技术领域:Technical field:

本发明属于消泡剂及制备技术领域,涉及一种复配型有机硅消泡剂及其制备方法。The invention belongs to the technical field of defoamers and their preparation, and relates to a compound type silicone defoamer and a preparation method thereof.

背景技术:Background technique:

自从德国实验物理学家Quincke首先提出用化学方法来消泡,到目前为止已经历了四次更新换代。第一代消泡剂为矿物油、脂肪酸及脂肪酸酯、脂肪酰胺、低级醇类等有机物,这种有机类消泡剂价格低廉,目前市场上仍在大量使用,但对致密型泡沫的消除能力较差;第二代消泡剂是聚醚类消泡剂,主要有直链聚醚和由醇、氨为起始剂的聚醚或端基酯化的聚醚衍生物,抑泡能力较强,是目前发酵行业应用的主导消泡剂,但破泡率低,需要新加一定量的消泡剂,为了适应消泡要求和操作条件多变的情况,开发了有机硅消泡剂即第三代消泡剂,有机硅类消泡剂一般为聚二甲基硅氧烷,二甲基硅油属于MDnM型的线型聚甲基硅氧烷,分子中为易绕曲的“之”字形链,这种消泡剂消泡效率很高,但是抑泡效果有时差强人意。因而,有机硅可以与脂肪酸酰胺、聚醚等其它具有消泡、抑泡活性的表面活性剂复配成复合消泡剂,这样既可以提高有机硅消泡剂的抑泡能力,又能降低产品的成本。第四代消泡剂是聚醚改性聚硅氧烷类消泡剂,是在聚硅氧烷链段上通过改性引入聚醚链段。这类消泡剂耐高温、耐强碱性,能迅速溶于水中,可单独使用,也可与其它处理剂配合使用,稳定性好,不发生破乳漂油现象,也无沉淀物产生,对非水体系也有效。中国专利CN103074784提出了一种以淀粉为稳定剂的复合有机硅消泡剂,增加了产品的稳定性,可以防止凝聚、破乳现象的发生,但是由于稳定剂的用量较大,使得消抑泡性能变差;中国专利CN104225965提出了以高沸硅油为原料之一的乳液型有机硅消泡剂,降低了生产成本,为有机硅单体副产高沸物处理提供了合理的处理渠道;以聚乙烯醇(PVA)为增稠剂,但在水溶解过称中,会产生泡沫,使生产能力降低,影响产品的质量和使用;中国专利CN103603215提出的是通过加入有机锡催化剂使硅氧烷粒子不易在强酸碱体系中断裂,产品能在苛刻的条件下使用,但生产成本较高,制备工艺较复杂;CN103830938提出了以非离子表面活性剂作为乳化剂,可以是吐温-60、司盘-40或聚醚硅油中的至少任意一种,乳化能力较高,但是产品耐碱性较差且成本较高。Since Quincke, a German experimental physicist, first proposed to use chemical methods to defoam, it has undergone four updates so far. The first generation of defoamers are organic substances such as mineral oil, fatty acids and fatty acid esters, fatty amides, and lower alcohols. The ability is poor; the second-generation defoamer is a polyether defoamer, mainly including linear polyether and polyether or end-group esterified polyether derivatives with alcohol and ammonia as initiators. Strong, it is the leading defoamer used in the fermentation industry at present, but the foam breaking rate is low, and a certain amount of defoamer needs to be added. In order to meet the defoaming requirements and changing operating conditions, a silicone defoamer has been developed That is, the third-generation defoamer. The silicone defoamer is generally polydimethylsiloxane, and dimethyl silicone oil belongs to the MDnM type linear polymethylsiloxane, and the molecule is easy to bend. "Zigzag chain, this kind of defoamer has a high defoaming efficiency, but the foam suppression effect is sometimes unsatisfactory. Therefore, silicone can be compounded with fatty acid amide, polyether and other surfactants with defoaming and antifoaming activity to form a composite defoamer, which can not only improve the antifoaming ability of the silicone defoamer, but also reduce the product the cost of. The fourth-generation defoamer is a polyether-modified polysiloxane defoamer, which is introduced into a polyether segment through modification on the polysiloxane segment. This kind of defoamer is resistant to high temperature and strong alkali, and can be quickly dissolved in water. It can be used alone or in combination with other treatment agents. It has good stability, no demulsification and oil drift, and no sediment. Also effective for non-aqueous systems. Chinese patent CN103074784 proposes a composite silicone defoamer with starch as a stabilizer, which increases the stability of the product and can prevent the occurrence of coagulation and demulsification, but due to the large amount of stabilizer, the defoaming Performance deterioration; Chinese patent CN104225965 proposes an emulsion-type silicone defoamer using high-boiling silicone oil as one of the raw materials, which reduces production costs and provides a reasonable treatment channel for the by-product high-boiler treatment of organic silicon monomers; Polyvinyl alcohol (PVA) is a thickener, but it will produce foam in the process of dissolving in water, which will reduce the production capacity and affect the quality and use of products; Chinese patent CN103603215 proposes to make siloxane Particles are not easily broken in a strong acid-base system, and the product can be used under harsh conditions, but the production cost is high and the preparation process is relatively complicated; CN103830938 proposes to use nonionic surfactants as emulsifiers, which can be Tween-60, At least any one of Span-40 or polyether silicone oil has high emulsifying ability, but the product has poor alkali resistance and high cost.

发明内容Contents of the invention

本发明的目的在于克服现有技术存在的缺点,寻求设计提供一种有机硅消泡剂及其制备方法,制备的有机硅消泡剂在具有强消泡和强抑泡能力的同时,还具有较好的稳定性、良好的抗稀释能力以及较广的pH和温度适用范围。The object of the present invention is to overcome the shortcoming that prior art exists, seek design and provide a kind of organic silicon antifoaming agent and preparation method thereof, the prepared organic silicon antifoaming agent has strong defoaming and strong antifoaming ability, also has Good stability, good anti-dilution ability and wide range of pH and temperature.

为了实现上述目的,本发明所述有机硅消泡剂包括蒸馏水、二甲基硅油、二氧化硅、乳化剂、助乳化剂和稳定剂;其各组份重量百分比为:蒸馏水48%-54%,二氧化硅1.1%-2.48%,二甲基硅油38%-48.5%,乳化剂1%-3%、助乳化剂1%-6%、稳定剂0.5%-1%,总重量百分比为100%。In order to achieve the above object, the organosilicon defoamer of the present invention includes distilled water, simethicone, silicon dioxide, emulsifier, co-emulsifier and stabilizer; its weight percentage of each component is: distilled water 48%-54% , silicon dioxide 1.1%-2.48%, simethicone 38%-48.5%, emulsifier 1%-3%, co-emulsifier 1%-6%, stabilizer 0.5%-1%, the total weight percentage is 100 %.

本发明所述乳化剂是阴离子表面活性剂,为十二烷基磺酸钠或十二烷基苯磺酸钠。The emulsifier of the present invention is an anionic surfactant, which is sodium dodecylsulfonate or sodium dodecylbenzenesulfonate.

本发明所述助乳化剂为AEO-9和磷酸三丁酯的一种或两种,其亲水亲油平衡值(HLB)为7~9。The co-emulsifier in the present invention is one or two of AEO-9 and tributyl phosphate, and its hydrophilic-lipophilic balance (HLB) is 7-9.

本发明所述稳定剂为羧甲基纤维素钠盐800~1200。The stabilizer of the present invention is carboxymethylcellulose sodium salt 800-1200.

本发明所述有机硅消泡剂的具体制备步骤为:The specific preparation steps of organosilicon defoamer of the present invention are:

(1)、主消泡剂的制备:在现有带加热和搅拌功能的反应装置中,加入3-5质量份的二氧化硅固体粉末,在搅拌下缓缓加入100质量份的二甲基硅油,在180℃温度条件下反应3h制得性能良好的主消泡剂(硅膏),将主消泡剂冷却至80℃备用;(1) Preparation of the main defoamer: In the existing reaction device with heating and stirring functions, add 3-5 parts by mass of silicon dioxide solid powder, and slowly add 100 parts by mass of dimethyl Silicone oil, react at 180°C for 3 hours to obtain a good performance main defoamer (silicone paste), cool the main defoamer to 80°C for later use;

(2)、复配乳化:在现有带加热和搅拌功能的反应装置中加入占产品总量48%-54%的蒸馏水,并加热至80℃,然后依次加入1%-6%助乳化剂、1%-3%乳化剂和0.5%-1%稳定剂,完全溶解后得到混合溶液,向混合溶液中缓缓滴加冷却至80℃的占产品总重量40%-48%的主消泡剂(硅膏)并充分搅拌,乳化0.5-1h后停止加热,均质后自然冷却至室温,得到白色粘稠乳液形态的有机硅消泡剂。(2) Compound emulsification: Add distilled water accounting for 48%-54% of the total product to the existing reaction device with heating and stirring functions, and heat it to 80°C, and then add 1%-6% co-emulsifier in turn , 1%-3% emulsifier and 0.5%-1% stabilizer, after completely dissolving to obtain a mixed solution, slowly add the main defoamer which is cooled to 80°C and accounts for 40%-48% of the total product weight After emulsifying for 0.5-1h, stop heating, homogenize and cool to room temperature naturally to obtain a silicone defoamer in the form of a white viscous emulsion.

本发明与现有技术相比,通过以二甲基硅油为原料,加入助剂二氧化硅,二氧化硅表面羟基有利于硅油的分散,能够改善硅油的消泡性能;由于具有很好的降低水的表面张力、润湿、渗透和乳化作用的阴离子表面活性剂的加入,使得乳化剂的发泡力较小且具有较好的乳化能力。同时通过各种乳化剂的复配,有AEO-9、十二烷基磺酸钠或十二烷基苯磺酸钠、羧甲基纤维素钠盐800~1200(CMC)和磷酸三丁酯,增强了亲水亲油体系的平衡和稳定性,改进了乳液的综合性能,如耐碱、耐热等。另外,加入增稠剂羧甲基纤维素钠盐800~1200(CMC)提高了分散介质的粘度,进一步增加了乳液的稳定性;其制备工艺简单,原料易得,成本低,制备的有机硅消泡剂在保持良好消抑泡性能的同时,具有高效、稳定、耐碱和耐热等特点。Compared with the prior art, the present invention uses dimethyl silicone oil as a raw material and adds silicon dioxide as an auxiliary agent, and the hydroxyl groups on the surface of the silicon dioxide are beneficial to the dispersion of silicone oil, which can improve the defoaming performance of silicone oil; The surface tension of water, the addition of anionic surfactants for wetting, penetration and emulsification make the emulsifier less foaming force and better emulsifying ability. At the same time through the compounding of various emulsifiers, there are AEO-9, sodium dodecylsulfonate or sodium dodecylbenzenesulfonate, sodium carboxymethylcellulose 800-1200 (CMC) and tributyl phosphate , enhance the balance and stability of the hydrophilic and lipophilic system, and improve the overall performance of the emulsion, such as alkali resistance and heat resistance. In addition, adding a thickener carboxymethylcellulose sodium salt 800-1200 (CMC) increases the viscosity of the dispersion medium and further increases the stability of the emulsion; the preparation process is simple, the raw materials are easy to obtain, and the cost is low. The prepared silicone While maintaining good defoaming and antifoaming properties, the defoamer has the characteristics of high efficiency, stability, alkali resistance and heat resistance.

具体实施方式:detailed description:

下面通过实施例对本发明作进一步说明。Below by embodiment the present invention will be further described.

实施例1:Example 1:

本实施例制备有机硅消泡剂的过程为:The process of preparing the organosilicon defoamer in this embodiment is:

(1).主消泡剂的制备:在现有带加热和搅拌功能的反应装置中,加入3份质量的二氧化硅固体粉末,在搅拌下缓缓加入100份质量的二甲基硅油,在约180℃温度条件下反应3h,即制得性能良好的主消泡剂(硅膏),将主消泡剂冷却至80℃左右备用;(1). Preparation of the main defoamer: In the existing reaction device with heating and stirring functions, add 3 parts of silicon dioxide solid powder by mass, and slowly add 100 parts of mass simethicone under stirring, React at a temperature of about 180°C for 3 hours to obtain a main defoamer (silicone paste) with good performance, and cool the main defoamer to about 80°C for later use;

(2).消泡剂的制备:将占最终产品总质量49%的蒸馏水加入现有带加热和搅拌功能的反应装置中并加热至80℃,再依次加入2%的十二烷基磺酸钠、2.5%的磷酸三丁酯、0.8%的羧甲基纤维素钠盐800~1200(CMC)和2.2%的AEO-9,待完全溶解后加入43.5%的主消泡剂,经保温并在2000r/min左右搅拌,使其充分乳化50分钟后停止搅拌并冷却到室温,得到形态为白色粘稠乳液的有机硅消泡剂。(2). Preparation of defoamer: add distilled water accounting for 49% of the total mass of the final product into the existing reaction device with heating and stirring functions and heat it to 80°C, then add 2% dodecylsulfonic acid in turn Sodium, 2.5% tributyl phosphate, 0.8% carboxymethyl cellulose sodium salt 800-1200 (CMC) and 2.2% AEO-9, add 43.5% main defoamer after complete dissolution, keep warm and Stir at about 2000r/min to fully emulsify for 50 minutes, then stop stirring and cool to room temperature to obtain a silicone defoamer in the form of a white viscous emulsion.

本实施例制备有机硅消泡剂的过程为:The process of preparing the organosilicon defoamer in this embodiment is:

(1).主消泡剂的制备:在现有带加热和搅拌功能的反应装置中,加入5份质量的二氧化硅固体粉末,在搅拌下缓缓加入100份质量的二甲基硅油,在约180℃温度条件下反应3h,即制得性能良好的主消泡剂(硅膏),将主消泡剂冷却至80℃左右备用;(1). Preparation of the main defoamer: In the existing reaction device with heating and stirring functions, add 5 parts of silicon dioxide solid powder by mass, and slowly add 100 parts by mass of simethicone under stirring, React at a temperature of about 180°C for 3 hours to obtain a main defoamer (silicone paste) with good performance, and cool the main defoamer to about 80°C for later use;

(2).消泡剂的制备:将占最终产品总质量54%的蒸馏水加入现有带加热和搅拌功能的反应装置中并加热至80℃,再依次加入2.2%的十二烷基磺酸钠、2.5%的磷酸三丁酯、0.6%的羧甲基纤维素钠盐800~1200(CMC)和0.7%的AEO-9,待完全溶解后加入40%的主消泡剂,经保温并在2000r/min左右搅拌,使其充分乳化60分钟后停止搅拌并冷却到室温,得到形态为白色粘稠乳液的有机硅消泡剂。(2).Preparation of defoamer: Add distilled water accounting for 54% of the total mass of the final product into the existing reaction device with heating and stirring functions and heat it to 80°C, then add 2.2% dodecylsulfonic acid in turn Sodium, 2.5% tributyl phosphate, 0.6% carboxymethylcellulose sodium salt 800-1200 (CMC) and 0.7% AEO-9, add 40% main defoamer after complete dissolution, keep warm and Stir at about 2000r/min to fully emulsify for 60 minutes, then stop stirring and cool to room temperature to obtain a silicone defoamer in the form of a white viscous emulsion.

实施例3:Example 3:

本实施例制备有机硅消泡剂的过程为:The process of preparing the organosilicon defoamer in this embodiment is:

(1).主消泡剂的制备:在现有带加热和搅拌功能的反应装置中,加入3份质量的二氧化硅固体粉末,在搅拌下缓缓加入100份质量的二甲基硅油,在约180℃温度条件下反应3h,即制得性能良好的主消泡剂(硅膏),将主消泡剂冷却至80℃左右备用;(1). Preparation of the main defoamer: In the existing reaction device with heating and stirring functions, add 3 parts of silicon dioxide solid powder by mass, and slowly add 100 parts of mass simethicone under stirring, React at a temperature of about 180°C for 3 hours to obtain a main defoamer (silicone paste) with good performance, and cool the main defoamer to about 80°C for later use;

(2).消泡剂的制备:将占最终产品总质量50%的蒸馏水加入现有带加热和搅拌功能的反应装置中并加热至80℃,再依次加入1%的十二烷基苯磺酸钠、3%的磷酸三丁酯和0.8%的羧甲基纤维素钠盐800~1200(CMC),待完全溶解后加入45.2%的主消泡剂,经保温并在2000r/min左右搅拌,使其充分乳化30分钟后停止搅拌并冷却到室温,得到形态为白色粘稠乳液的有机硅消泡剂。(2).Preparation of defoamer: Add distilled water accounting for 50% of the total mass of the final product into the existing reaction device with heating and stirring functions and heat it to 80°C, then add 1% dodecylbenzenesulfonate in sequence sodium phosphate, 3% tributyl phosphate and 0.8% carboxymethyl cellulose sodium salt 800~1200 (CMC), add 45.2% main defoamer after complete dissolution, keep warm and stir at about 2000r/min After fully emulsifying for 30 minutes, stop stirring and cool to room temperature to obtain a silicone defoamer in the form of a white viscous emulsion.

实施例4:Example 4:

本实施例制备有机硅消泡剂的过程为:The process of preparing the organosilicon defoamer in this embodiment is:

(1).主消泡剂的制备:在现有带加热和搅拌功能的反应装置中,加入4份质量的二氧化硅固体粉末,在搅拌下缓缓加入100份质量的二甲基硅油,在约180℃温度条件下反应3h,即制得性能良好的主消泡剂(硅膏),将主消泡剂冷却至80℃左右备用;(1). Preparation of the main defoamer: In the existing reaction device with heating and stirring functions, add 4 parts of silicon dioxide solid powder by mass, and slowly add 100 parts of mass simethicone under stirring, React at a temperature of about 180°C for 3 hours to obtain a main defoamer (silicone paste) with good performance, and cool the main defoamer to about 80°C for later use;

(2).消泡剂的制备:将占最终产品总质量52%的蒸馏水加入现有带加热和搅拌功能的反应装置中并加热至80℃,再依次加入3%的十二烷基苯磺酸钠、1%的磷酸三丁酯、0.5%的羧甲基纤维素钠盐800~1200(CMC)和3%的AEO-9,待完全溶解后加入40.5%的主消泡剂,经保温并在2000r/min左右搅拌,使其充分乳化40分钟后停止搅拌并冷却到室温,得到形态为白色粘稠乳液的有机硅消泡剂。(2).Preparation of defoamer: add distilled water accounting for 52% of the total mass of the final product into the existing reaction device with heating and stirring functions and heat it to 80°C, then add 3% dodecylbenzenesulfonate in sequence sodium phosphate, 1% tributyl phosphate, 0.5% carboxymethylcellulose sodium salt 800-1200 (CMC) and 3% AEO-9, add 40.5% main defoamer after complete dissolution, after heat preservation Stir at about 2000r/min to fully emulsify for 40 minutes, then stop stirring and cool to room temperature to obtain a silicone defoamer in the form of a white viscous emulsion.

实施例5:Example 5:

本实施例制备有机硅消泡剂的过程为:The process of preparing the organosilicon defoamer in this embodiment is:

(1).主消泡剂的制备:在现有带加热和搅拌功能的反应装置中,加入3份质量的二氧化硅固体粉末,在搅拌下缓缓加入100份质量的二甲基硅油,在约180℃温度条件下反应3h,即制得性能良好的主消泡剂(硅膏),将主消泡剂冷却至80℃左右备用;(1). Preparation of the main defoamer: In the existing reaction device with heating and stirring functions, add 3 parts of silicon dioxide solid powder by mass, and slowly add 100 parts of mass simethicone under stirring, React at a temperature of about 180°C for 3 hours to obtain a main defoamer (silicone paste) with good performance, and cool the main defoamer to about 80°C for later use;

(2).消泡剂的制备:将占最终产品总质量49.5%的蒸馏水加入现有带加热和搅拌功能的反应装置中并加热至80℃,再依次加入2.2%的十二烷基苯磺酸钠、2.5%的磷酸三丁酯、0.6%的羧甲基纤维素钠盐800~1200(CMC)和2.2%的AEO-9,待完全溶解后加入40.5%的主消泡剂,经保温并在2000r/min左右搅拌,使其充分乳化30分钟后停止搅拌并冷却到室温,得到形态为白色粘稠乳液的有机硅消泡剂。(2). Preparation of defoamer: add distilled water accounting for 49.5% of the total mass of the final product into the existing reaction device with heating and stirring functions and heat it to 80°C, then add 2.2% dodecylbenzenesulfonate in sequence Sodium phosphate, 2.5% tributyl phosphate, 0.6% sodium carboxymethyl cellulose 800-1200 (CMC) and 2.2% AEO-9, add 40.5% main defoamer after complete dissolution, after heat preservation Stir at about 2000r/min to fully emulsify for 30 minutes, then stop stirring and cool to room temperature to obtain a silicone defoamer in the form of a white viscous emulsion.

本实施例有机硅消泡剂制备的最佳条件:HLB在7~9之间,搅拌温度在80℃左右,搅拌速度在2000r/min左右。The optimal conditions for the preparation of the silicone defoamer in this example: the HLB is between 7 and 9, the stirring temperature is about 80° C., and the stirring speed is about 2000 r/min.

本实施例对制备的有机硅消泡剂分别进行稳定、耐碱、耐ATSC(丙酮缩氨基硫脲)、消泡速度、耐热和碱性条件下的消泡性能测试,具体为:In this example, the prepared silicone defoamer was tested for its stability, alkali resistance, ATSC (acetone thiosemicarbazone) resistance, defoaming speed, heat resistance and defoaming performance under alkaline conditions, specifically:

(1)离心稳定性测试:对产品和样品以3000r/min进行离心实验,测试时间20min不分层;(1) Centrifugal stability test: Centrifuge the product and sample at 3000r/min, and the test time is 20min without delamination;

(2)耐碱测试:将配制的消泡剂乳液、氢氧化钠质量分数均为5%的混合水溶液80mL置于100mL烧杯中,在高剪切力下用磁力搅拌机搅拌十分钟后静置,观察24小时后溶液的性状,不结蜡;(2) Alkali resistance test: 80 mL of the prepared defoamer emulsion and a mixed aqueous solution with a mass fraction of sodium hydroxide of 5% were placed in a 100 mL beaker, stirred with a magnetic stirrer under high shear force for ten minutes, and then left to stand. Observe the properties of the solution after 24 hours, no wax formation;

(3)耐ATSC(丙酮缩氨基硫脲)测试:将有机硅消泡剂、氢氧化钠和ATSC重量百分含量均为5%的混合水溶液80mL置于100mL烧杯中,在高剪切力下用磁力搅拌机搅拌十分钟后静置,观察24小时后溶液的性状,不分层、不结蜡;(3) Resistance to ATSC (acetone thiosemicarbazone) test: 80 mL of a mixed aqueous solution of 5% by weight of silicone defoamer, sodium hydroxide and ATSC is placed in a 100 mL beaker, under high shear force Stir with a magnetic stirrer for ten minutes and then stand still, observe the properties of the solution after 24 hours, no stratification, no wax formation;

(4)消泡速度测试:将所制消泡剂与水配成含消泡剂1%的稀释液备用,将鼓泡器砂芯放入500mL量筒,加入含表面活性剂质量百分数为1%的起泡液至200mL刻度,开动气泵鼓泡,当泡沫高度上升至500mL时停止鼓泡,在量筒中注入25mL所配置的质量百分数为1%的消泡剂溶液稀释液同时计时,至泡沫消失时即为消泡时间,重复3次取平均值;(4) Defoaming speed test: Prepare the prepared defoamer and water to make a diluent containing 1% defoamer for later use, put the bubbler sand core into a 500mL graduated cylinder, add a surfactant containing 1% by mass When the foaming solution reaches the 200mL mark, start the air pump to bubble, stop bubbling when the foam height reaches 500mL, inject 25mL of the prepared 1% defoamer solution diluent into the measuring cylinder and time it at the same time, until the foam disappears Time is the defoaming time, repeated 3 times to get the average value;

(5)耐热测试:取制备的有机硅消泡剂于试管中,并置于烘箱内,当温度上升到110℃时开始计时,2小时后冷却降温至室温,取出样品观察耐高温性能;(5) Heat resistance test: Take the prepared silicone defoamer in a test tube and place it in an oven. When the temperature rises to 110°C, start timing, cool down to room temperature after 2 hours, and take out the sample to observe the high temperature resistance;

(6)碱性条件下的消泡测试:在100mL量筒中加入pH=14的含表面活性剂质量百分数为1%的起泡液起泡液50mL震荡30次,后加入0.2mL由消泡剂配成含消泡剂1%的稀释液有机硅消泡剂测量剩余泡沫体积。(6) Defoaming test under alkaline conditions: Add 50mL of foaming solution containing 1% surfactant with pH=14 in a 100mL graduated cylinder and shake for 30 times, then add 0.2mL of defoaming agent Make a dilution containing 1% of the antifoaming agent silicone antifoaming agent to measure the remaining foam volume.

Claims (1)

1.一种有机硅消泡剂的制备方法,其特征在于具体制备步骤为:1. a preparation method of organosilicon defoamer, is characterized in that concrete preparation steps are: (1).主消泡剂的制备:在现有带加热和搅拌功能的反应装置中,加入3份质量的二氧化硅固体粉末,在搅拌下缓缓加入100份质量的二甲基硅油,在约180℃温度条件下反应3h,即制得性能良好的主消泡剂,将主消泡剂冷却至80℃备用;(1). Preparation of the main defoamer: In the existing reaction device with heating and stirring functions, add 3 parts of silicon dioxide solid powder by mass, and slowly add 100 parts of mass simethicone under stirring, React at a temperature of about 180°C for 3 hours to obtain a main defoamer with good performance, and cool the main defoamer to 80°C for later use; (2).消泡剂的制备:将占最终产品总质量49%的蒸馏水加入现有带加热和搅拌功能的反应装置中并加热至80℃,再依次加入2%的十二烷基磺酸钠、2.5%的磷酸三丁酯、0.8%的羧甲基纤维素钠盐800~1200和2.2%的AEO-9,待完全溶解后加入43.5%的主消泡剂,经保温并在2000r/min搅拌,使其充分乳化50分钟后停止搅拌并冷却到室温,得到形态为白色粘稠乳液的有机硅消泡剂。(2). Preparation of defoamer: add distilled water accounting for 49% of the total mass of the final product into the existing reaction device with heating and stirring functions and heat it to 80°C, then add 2% dodecylsulfonic acid in turn Sodium, 2.5% tributyl phosphate, 0.8% carboxymethylcellulose sodium salt 800-1200 and 2.2% AEO-9, add 43.5% main defoamer after complete dissolution, keep warm and heat at 2000r/ Min stirring to make it fully emulsified for 50 minutes, then stop stirring and cool to room temperature to obtain a silicone defoamer in the form of a white viscous emulsion.
CN201510925719.0A 2015-12-11 2015-12-11 A kind of organic silicon defoamer and preparation method thereof Expired - Fee Related CN105498303B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201510925719.0A CN105498303B (en) 2015-12-11 2015-12-11 A kind of organic silicon defoamer and preparation method thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201510925719.0A CN105498303B (en) 2015-12-11 2015-12-11 A kind of organic silicon defoamer and preparation method thereof

Publications (2)

Publication Number Publication Date
CN105498303A CN105498303A (en) 2016-04-20
CN105498303B true CN105498303B (en) 2017-11-14

Family

ID=55706838

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201510925719.0A Expired - Fee Related CN105498303B (en) 2015-12-11 2015-12-11 A kind of organic silicon defoamer and preparation method thereof

Country Status (1)

Country Link
CN (1) CN105498303B (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110548315A (en) * 2019-08-14 2019-12-10 湖南登科材料科技有限公司 Novel organic silicon defoaming agent and preparation method thereof

Families Citing this family (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106731034A (en) * 2016-12-22 2017-05-31 新疆水处理工程技术研究中心有限公司 A kind of compound defoamer
CN106905707B (en) * 2017-04-07 2020-10-23 深圳市永万丰实业有限公司 Defoaming agent for low-viscosity rubber filling oil and preparation method thereof
CN109966786B (en) * 2019-03-14 2021-06-11 中天东方氟硅材料有限公司 Organic silicon defoaming agent of trifluoropropene modified organic silicon high-boiling residues
CN112044119A (en) * 2020-09-07 2020-12-08 安徽銮威化工科技开发有限公司 Organic silicon defoaming agent for PVC (polyvinyl chloride) and preparation method thereof
CN112807754A (en) * 2020-12-09 2021-05-18 金湖金凌新材料科技有限公司 Defoaming agent for eliminating foam in wastewater aerobic activated sludge tank and preparation method thereof
CN112827221A (en) * 2021-01-10 2021-05-25 潮州市顺冠生物科技有限公司 Defoaming agent for food processing and preparation method thereof
CN113350835A (en) * 2021-06-11 2021-09-07 江苏赛欧信越消泡剂有限公司 Modified polyether type defoaming agent for landfill leachate and preparation method thereof
CN114938802A (en) * 2022-03-09 2022-08-26 上海东旖新材料科技有限公司 Preparation of organic silicon defoaming agent for pesticide aqueous preparation
CN115463459B (en) * 2022-09-28 2024-05-14 成都科能石油技术有限公司 Defoaming agent composition for foam drainage gas production of gas well and preparation method thereof

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101987256A (en) * 2009-08-02 2011-03-23 扬州润达油田化学剂有限公司 Production process of organosilicone emulsion defoaming agent
CN103877755B (en) * 2014-03-11 2016-03-02 苏州恒康新材料有限公司 A kind of silicone defoaming agent and preparation method thereof

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110548315A (en) * 2019-08-14 2019-12-10 湖南登科材料科技有限公司 Novel organic silicon defoaming agent and preparation method thereof

Also Published As

Publication number Publication date
CN105498303A (en) 2016-04-20

Similar Documents

Publication Publication Date Title
CN105498303B (en) A kind of organic silicon defoamer and preparation method thereof
CN104830307B (en) A kind of fracturing fluid organic silicon polyether emulsion type defoaming agent and preparation method thereof
AU613748B2 (en) Silicone foam control composition
CN103028275B (en) Preparation method of solid organic silicon defoamer
CN101942293B (en) A kind of defoaming agent for drilling fluid
CN102002242B (en) Organosilicon emulsion and preparation method thereof
US9321907B2 (en) Process for preparation of stable fatty alcohol emulsion
CN105148571A (en) Preparation method of defoaming agent for waterborne system
CN108744612B (en) Mineral oil defoaming agent and preparation method thereof
CN106215466A (en) A kind of preparation method of high stability of siloxane defoamer
CN108726913A (en) A kind of silicon ether composite anti-foaming agent and its preparation method and application
CN114191854B (en) Polyether modified organosiloxane emulsion defoamer and preparation method thereof
JP2014534046A (en) Silicone foam control composition and method for producing the same
CN103641195A (en) Organic silicon defoamer and preparation method thereof
CN101927139A (en) Self-emulsifier and use thereof in tertiary oil recovery
RU2539484C1 (en) Emulsion formulation for water suppression, conformance control and well killing
CN106492707A (en) Surface activator composition
CN108499162A (en) Sea water desalination antifoaming agent and its preparation method and application
US20170341136A1 (en) Oil-in-water silicone emulsion composition for die casting release agent
CN105131697B (en) A kind of this build coating defoamer and preparation method thereof
US3250727A (en) Defoaming agents containing methylsiloxanes
CN106267913A (en) A kind of high stability of siloxane defoamer
CN106243364A (en) A kind of organic silicon modified by polyether emulsion and preparation method thereof
CN105293990B (en) A kind of self-emulsifying concrete defoamer and preparation method thereof
CN103074784B (en) Composite organic silicon defoamer for textile printing and dyeing

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20171114

Termination date: 20181211