WO2021217835A1 - 一种有机硅组合物 - Google Patents
一种有机硅组合物 Download PDFInfo
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- WO2021217835A1 WO2021217835A1 PCT/CN2020/097384 CN2020097384W WO2021217835A1 WO 2021217835 A1 WO2021217835 A1 WO 2021217835A1 CN 2020097384 W CN2020097384 W CN 2020097384W WO 2021217835 A1 WO2021217835 A1 WO 2021217835A1
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- polyorganosiloxane
- platinum
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- hydrogen
- hydroxyl
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D19/00—Degasification of liquids
- B01D19/02—Foam dispersion or prevention
- B01D19/04—Foam dispersion or prevention by addition of chemical substances
- B01D19/0404—Foam dispersion or prevention by addition of chemical substances characterised by the nature of the chemical substance
- B01D19/0409—Foam dispersion or prevention by addition of chemical substances characterised by the nature of the chemical substance compounds containing Si-atoms
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D19/00—Degasification of liquids
- B01D19/02—Foam dispersion or prevention
- B01D19/04—Foam dispersion or prevention by addition of chemical substances
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G81/00—Macromolecular compounds obtained by interreacting polymers in the absence of monomers, e.g. block polymers
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K3/00—Use of inorganic substances as compounding ingredients
- C08K3/34—Silicon-containing compounds
- C08K3/36—Silica
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L83/00—Compositions of macromolecular compounds obtained by reactions forming in the main chain of the macromolecule a linkage containing silicon with or without sulfur, nitrogen, oxygen or carbon only; Compositions of derivatives of such polymers
- C08L83/04—Polysiloxanes
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L83/00—Compositions of macromolecular compounds obtained by reactions forming in the main chain of the macromolecule a linkage containing silicon with or without sulfur, nitrogen, oxygen or carbon only; Compositions of derivatives of such polymers
- C08L83/04—Polysiloxanes
- C08L83/06—Polysiloxanes containing silicon bound to oxygen-containing groups
Definitions
- the invention relates to a silicone composition that can be used in silicone emulsions. Therefore, the present invention belongs to the technical field of fine chemical preparations.
- Bubbles are a common phenomenon in life and work. But in industrial production, bubbles sometimes bring a lot of harm, such as reducing work efficiency, delaying working hours, and affecting product quality. With the substantial increase in industrial scale and production efficiency, defoamers and defoamers have been widely used. At present, defoamers have been widely used in papermaking, textile printing and dyeing, petroleum extraction and refining, coatings, emulsion polymerization, sewage treatment, metal cleaning and other industries, and have become indispensable functional additives in the production process.
- defoamers are divided into several main types, such as mineral oil type, polyether type and silicone type. Compared with other defoamers, silicone defoamers have stable chemical properties and less side effects. At the same time, they also have good defoaming ability and long-lasting foam suppression ability in the case of very low dosage, so they are very popular.
- the defoaming composition is the core of the defoaming agent, and its defoaming speed and foam suppression performance directly affect the performance of the final product.
- the improvement of the antifoaming performance of its active substances is the direction of improvement of organosilicon defoamers.
- the original polysiloxane antifoaming agent active is obtained by specific processing technology of polydimethylsiloxane and silicon dioxide, for example, DD-A056762 is mixed with the hydrophilicity of polydimethylsiloxane. Silica is heated to prepare the defoaming active, and the defoaming agent prepared by this method has poor activity.
- hydrophobic silica mixed and dispersed in polysiloxane such as DE-A2925722
- DE-A2925722 hydrophobic silica mixed and dispersed in polysiloxane
- US5153258 uses cross-linked polyorganosiloxane to improve the anti-foaming performance of active materials, such as vinyl-containing polyorganosiloxane and hydrogen-containing polyorganosiloxane, hydroxyl-containing polyorganosiloxane and silicate in The reaction occurs under the action of the platinum catalyst, but the reaction is difficult to control.
- WO2007137948A1 describes the reaction of hydrogen-containing polyorganosiloxane and vinyl polyorganosiloxane under the action of a transition metal catalyst, and then adding trimethylsiloxy-terminated polydimethylsiloxane to dilute.
- the above-mentioned patent contains
- the hydrogen polyorganosiloxane reacts with the vinyl polyorganosiloxane, the viscosity is large and it is difficult to control, and the obtained antifoaming agent composition has poor antifoaming performance.
- CN1931417A discloses a defoamer composition resistant to high temperature and strong alkali, which is obtained by cross-linking reaction of polysiloxane and organic silicon resin under the action of alkali catalyst.
- the active material is prepared into an emulsion and the performance is tested. It has good foam suppression performance, but the defoaming speed needs to be further improved, and because the viscosity of the defoaming composition is relatively high, it is difficult to emulsify and disperse.
- the defoamer composition in the above patent has either poor foam suppression performance or high viscosity and is difficult to emulsify to prepare an emulsion to disperse in water.
- a hydroxy-based polyorganosiloxane and an organosilicon resin are catalyzed by a titanium catalyst to react, a platinum catalyst is added to react with a hydrogen-containing polyorganosiloxane, and the mixture is treated with hydrophobic particles to obtain an organosilicon composition.
- the titanium catalyst catalyzes the reaction between the hydroxyl polyorganosiloxane and the hydroxyl group in the silicone resin
- the organosilicon composition has a compact siloxane space structure
- the platinum catalyst is subsequently used to catalyze the hydrogen-containing polyorganosiloxane and the system
- the hydroxyl groups react to form a more compact space structure with long chains.
- the organic silicon emulsion prepared by using the composition has a good inhibitory effect on foam in a system rich in anionic surfactants.
- the modified polyorganosiloxane of the present invention is obtained by the reaction of hydroxyl polyorganosiloxane, organosilicon resin and hydrogen-containing polyorganosiloxane.
- R 1 groups are the same or different, and are alkyl groups with 1 to 30 carbon atoms, preferably 1 to 10 carbon atoms, specifically selected from methyl, ethyl, propyl, n-propyl, butyl, isobutyl Group; or phenyl; or aralkyl group having 7-20 carbon atoms; subscript m is an integer of 500-1500; the amount of the hydroxypolyorganosiloxane is 50-70 of the total mass of the silicone composition %.
- Silicone resin is composed of units of the following general formula:
- R 2 and R 3 may be the same or different, and are a hydroxyl group or a monovalent, substituted or unsubstituted, saturated or unsaturated hydrocarbon group with 1 to 6 carbon atoms, preferably an alkyl group with 1 to 6 carbon atoms ,
- R 1 , R 2 are the total number of hydroxyl groups ⁇ 1, the subscript c is 0, 1, 2 or 3; the subscript d is 0, 1, 2 or 3; the said silicone resin contains a hydroxyl group of 0.1 %-0.5%, and the amount is 1-10% of the total mass of the organic silicon composition.
- At least one hydrogen-containing polyorganosiloxane with the general structural formula is as follows:
- Me is a methyl group, subscript n is 0, 1, a is an integer from 2 to 20, b is an integer from 20 to 300, and each molecule has at least 2 silicon-bonded hydrogen atoms.
- the amount of the hydrogen-containing polyorganosiloxane is 20-40% of the total mass of the organic silicon composition.
- Titanium catalyst refers to titanate catalyst, the structural formula is Ti(OR) 4 , where: -OR is a hydrolyzable short-chain alkoxy group, including methoxy, ethoxy, propoxy, isopropoxy, Butoxy or isobutoxy.
- the amount of the titanium catalyst is 0.1-1% of the total mass of the organosilicon composition.
- the catalyst is used to catalyze the condensation reaction between the hydrogen-containing polyorganosiloxane and the hydroxyl-containing polyorganosiloxane in the system.
- the catalyst is selected from platinum-alcohol complexes, platinum-olefin complexes, platinum-alkoxide complexes, platinum-ether complexes, platinum-ketone complexes, chloroplatinic acid isopropanol solution, Platinum-vinyl complex.
- a chloroplatinic acid isopropanol solution with a platinum content of 1-20 ppm.
- the catalyst addition amount mentioned is based on platinum.
- the hydrophobic particles are selected from silicon dioxide, titanium dioxide, quartz powder, aluminum oxide, aluminum silicate, zinc oxide, magnesium oxide, or a mixture of two or more.
- the preferred silica of the present invention has a specific surface area of 50-300 m 2 /g, specifically selected from hydrophobic precipitated silica and hydrophobic fumed silica.
- the amount of the hydrophobic particles is 1-10% of the total mass of the silicone composition.
- the preparation method of the organic silicon composition is as follows:
- a method for preparing a silicone emulsion by using the above-mentioned organosilicon composition is: mixing the organosilicon composition and emulsifier, and gradually adding water and thickening agent, and then passing through mechanical equipment, such as a colloid grinder, after mixing uniformly. , Homogenizer to prepare oil-in-water silicone emulsion.
- Emulsifiers include nonionic surfactants and anionic surfactants.
- the non-ionic surfactant is selected from the group consisting of nonylphenol polyoxyethylene ether, octylphenol polyoxyethylene ether, lauric acid polyoxyethylene ether, oleic acid polyoxyethylene ether, sorbitan monostearate, loss of Sorbitan monooleate, sorbitan tristearate, sorbitan trioleate, sorbitan monostearate polyoxyethylene ether ester, sorbitan monooleate polyoxyethylene Vinyl ether ester, sorbitan tristearate polyoxyethylene ether ester, castor oil polyoxyethylene ether.
- the anionic surfactant is selected from sodium lauryl polyoxyethylene ether sulfate, sodium lauryl sulfate, sodium dodecyl benzene sulfonate, sodium dodecyl sulfonate, sodium cetyl sulfonate , Sodium cetylbenzene sulfonate, sodium dodecyl diphenyl ether disulfonate.
- Thickeners are xanthan gum, guar gum, polyvinyl alcohol, sodium carboxymethyl cellulose, hydroxyethyl cellulose, polyacrylic acid, polyacrylamide, and polyacrylates.
- the reaction was carried out at 140°C for 2 hours; after the reaction was completed, 1 g of hydrophobic fumed silica (specific surface area 250m 2 /g) was added, kept at 130°C for 2 hours, and cooled to room temperature to obtain the organosilicon composition S6.
- the silicone emulsion is prepared by using the above-mentioned silicone composition of S1 to S11 and D1-D3:
- Test method Using 0.5% (mass percentage) sodium dodecylbenzene sulfonate aqueous solution as the foaming medium, add 50 mL of the above foaming medium to a 100 mL graduated cylinder with a stopper, and then add 0.010 g of silicone emulsion defoamer, Shake 50 times in the vertical direction and then stand, record the time when the foam disappears to the liquid level, which is the defoaming time T 50 , and then shake 50 times to record the defoaming time T 100 , record the defoaming time every 50 times of shaking The foaming time is until the total number of shakes reaches 400 times. Under the same shaking times, the shorter the defoaming time, the better the antifoaming effect of the silicone emulsion.
- Table 1 The test results are shown in Table 1:
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- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
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Abstract
一种有机硅组合物,基于羟基聚有机硅氧烷和有机硅树脂通过钛催化剂催化反应,再加入铂催化剂和含氢聚有机硅氧烷反应,经疏水粒子混合处理,最终得到有机硅组合物,采用该组合物制备有机硅乳液在富含阴离子表面活性剂的体系中对泡沫有良好的抑制作用。
Description
本发明涉及一种可用于有机硅乳液的有机硅组合物。因此,本发明属于精细化工制剂技术领域。
泡沫是生活和工作中常见的现象。但在工业生产中有时泡沫会带来很多的危害,例如降低工作效率、延误劳动时间、影响产品质量等。随着工业规模和生产效率的大幅提高,消泡剂消泡得到广泛的应用。目前,消泡剂已经广泛应用造纸、纺织印染、石油开采和炼制、涂料、乳液聚合、污水处理、金属清洗等行业中,成为生产过程中不可缺少的功能性助剂。
根据消泡组合物的不同,消泡剂分为矿物油型、聚醚型和有机硅类等几种主要类型。与其他消泡剂相比,有机硅类消泡剂化学性能稳定,副作用小,同时在用量很低的情况下也有很好的消泡能力和持久的抑泡能力,因而很受青睐。
消泡组合物是消泡剂的核心,它的消泡速度和抑泡性能直接影响最终产品的性能。对于有机硅类的消泡剂而言,其活性物的消抑泡性能的改进是有机硅消泡剂的改进方向。最初的聚硅氧烷消泡剂活性物是由聚二甲基硅氧烷和二氧化硅经过特定加工工艺处理得到的,例如DD-A056762通过混合聚二甲基硅氧烷中的亲水性二氧化硅加热来制备消泡活性物,该方法制备的消泡剂的活性较差。而改用疏水性二氧 化硅混合分散在聚硅氧烷中的,如DE-A2925722来说制备的消泡活性物性能有所改进,但是仍不尽如人意。因此,国内外的研究人员都对其性能进行了大规模的拓展研究。US5153258使用交联的聚有机硅氧烷能提高活性物的消抑泡性能,例如含乙烯基聚有机硅氧烷和含氢聚有机硅氧烷、含羟基聚有机硅氧烷和硅酸酯在铂催化剂的作用下发生反应,但是其反应难以控制。WO2007137948A1中介绍了含氢聚有机硅氧烷和乙烯基聚有机硅氧烷在过渡金属催化剂作用下反应后,加入三甲基硅氧基封端的聚二甲基硅氧烷稀释,上述专利中含氢聚有机硅氧烷和乙烯基聚有机硅氧烷反应时,粘度大,不易控制,得到的消泡剂组合物消抑泡性能差。CN1931417A公开了一种耐高温耐强碱的消泡剂组合物,它是由聚硅氧烷和有机硅树脂在碱催化剂作用下交联反应得到的,将活性物制备成乳液后测试性能,其具有较好的抑泡性能,但消泡速度有待进一步提高,且由于消泡组合物粘度较大,难以乳化分散。上述专利中的消泡剂组合物要么抑泡性能差要么粘度大较难乳化制备乳液分散在水中。
发明内容
本发明通过一种基于羟基聚有机硅氧烷和有机硅树脂通过钛催化剂催化反应,再加入铂催化剂和含氢聚有机硅氧烷反应,经疏水粒子混合处理,得到有机硅组合物。由于钛催化剂催化羟基聚有机硅氧烷与有机硅树脂中的羟基发生反应,使有机硅组合物具有紧密硅氧烷空间结构,并且后续采用铂催化剂催化含氢聚有机硅氧烷与体系中的 羟基反应,形成具有长链更紧密的空间结构。采用该组合物制备有机硅乳液在富含阴离子表面活性剂的体系中对泡沫有良好的抑制作用。
技术方案
一种有机硅组合物,其特征在于它由以下物质组成:
A.改性聚有机硅氧烷
本发明所述的改性聚有机硅氧烷是羟基聚有机硅氧烷、有机硅树脂和含氢聚有机硅氧烷反应得到的。
A1.羟基聚有机硅氧烷
所述的羟基聚有机硅氧烷的结构通式如下:
HO(SiR
1
2O)
mH
式中R
1基相同或不同,为碳原子数1~30的烷基,优选碳原子数为1~10,具体选自甲基、乙基、丙基、正丙基、丁基、异丁基;或苯基;或碳原子数为7~20的芳烷基;下标m为500~1500的整数;所述羟基聚有机硅氧烷的用量为有机硅组合物总质量的50~70%。
A2.有机硅树脂
有机硅树脂由如下通式的单元组成:
R
c
2R
d
3SiO(4-c-d)/2
其中R
2和R
3可以相同或者不同,为羟基或单价的、取代或未取代的、饱和的或不饱和的具有1-6个碳原子的烃基,优选具有1-6个碳原子的烷基,且R
1、R
2为羟基的总数量≥1,下标c是0、1、2或者3;下标d是0、1、2或者3;所述的有机硅树脂含羟基量为0.1%-0.5%,其用量为有机硅组合物总质量的1~10%。
A3.含氢聚有机硅氧烷
至少一种结构通式为如下的含氢聚有机硅氧烷:
H
n
Me
3-nSiO(
MeHSiO)
a(
Me
2SiO)
bSi
Me
3-nH
n
Me为甲基,下标n是0、1,a是2~20的整数,b是20~300的整数,每个分子具有至少2个硅键合的氢原子。所述含氢聚有机硅氧烷的用量为有机硅组合物总质量的20~40%。
A4.钛催化剂
钛催化剂是指钛酸酯催化剂,结构式为Ti(OR)
4,式中:-OR为可水解的短链烷氧基,包括甲氧基、乙氧基、丙氧基、异丙氧基、丁氧基或异丁氧基。所述钛催化剂用量为有机硅组合物总质量的0.1~1%。
A5.铂催化剂
催化剂用来催化组分含氢聚有机硅氧烷和体系中的含有羟基聚有机硅氧烷发生缩合反应。所述的催化剂选自铂-醇络合物、铂-烯烃络合物、铂-醇盐络合物、铂-醚络合物、铂-酮络合物、氯铂酸异丙醇溶液、铂-乙烯基络合物。优选铂含量为1~20ppm的氯铂酸异丙醇溶液,若无特殊说明,所提及催化剂加量均以铂计。
B.疏水粒子
疏水粒子选自二氧化硅、二氧化钛、石英粉、氧化铝、硅酸铝、氧化锌、氧化镁,或两者或两者以上的混合物。本发明优选二氧化硅,其比表面积为50~300m
2/g,具体选自疏水沉淀二氧化硅、疏水气相二氧化硅。所述疏水粒子的用量为有机硅组合物总质量的1~10%。
所述有机硅组合物的制备方法如下:
①将羟基聚有机硅氧烷A1和有机硅树脂A2加入到反应容器中,并加入催化剂A4,在40~100℃时反应0.5~3h;
②再加入含氢聚有机硅氧烷A3和催化剂A5,在50~150℃时反应0.5~3h;
③反应完毕后,加入疏水粒子B,在100~160℃保温1~3h,冷却到室温,即得所述有机硅组合物。
一种采用上述有机硅组合物制备有机硅乳液的方法,实现方法为:将有机硅组合物和乳化剂混合,并逐步加入水和增稠剂,混合均匀后通过机械设备,如胶体磨碎机、均质机,制备水包油型有机硅乳液。
乳化剂包括非离子表面活性剂和阴离子表面活性剂。
所述非离子表面活性剂选自壬基酚聚氧乙烯醚、辛基酚聚氧乙烯醚、月桂酸聚氧乙烯醚、油酸聚氧乙烯醚、失水山梨醇单硬脂酸酯、失水山梨醇单油酸酯、失水山梨醇三硬脂酸酯、失水山梨醇三油酸酯、失水山梨醇单硬脂酸聚氧乙烯醚酯、失水山梨醇单油酸聚氧乙烯醚酯、失水山梨醇三硬脂酸聚氧乙烯醚酯、蓖麻油聚氧乙烯醚。
所述阴离子表面活性剂选自十二烷基聚氧乙烯醚硫酸钠、十二烷基硫酸钠、十二烷基苯磺酸钠、十二烷基磺酸钠、十六烷基磺酸钠、十六烷基苯磺酸钠、十二烷基二苯醚二磺酸钠。
增稠剂为汉生胶、瓜尔胶、聚乙烯醇、羧甲基纤维素钠、羟乙基纤维素、聚丙烯酸、聚丙烯酰胺、聚丙烯酸酯类。
实施例1
将50g羟基聚有机硅氧烷HO[Si(CH
3)
2O]
500H和10g有机硅树脂(羟基含量0.1%)加入到反应容器中,并加入0.1g钛催化剂Ti(OCH
3)
4,在40℃时反应3h;再加入30g含氢聚有机硅氧烷HMe
2SiO(MeHSiO)
2(Me2SiO)
300SiMe
2H和1ppm氯铂酸异丙醇溶液,在50℃时反应3h;反应完毕后,加入9.9g疏水沉淀法二氧化硅(比表面积50m
2/g),在100℃保温3h,冷却到室温,即得所述有机硅组合物S1。
实施例2
将70g羟基聚有机硅氧烷HO[Si(CH
3)(C
6H
5)O]
1500H和5g有机硅树脂(羟基含量0.2%)加入到反应容器中,并加入1g钛催化剂Ti(OCH
2CH
3)
4,在100℃时反应0.5h;再加入20g含氢聚有机硅氧烷Me
3SiO(MeHSiO)
2(Me2SiO)
100SiMe
3和20ppm氯铂酸异丙醇,在150℃时反应0.5h;反应完毕后,加入4g疏水沉淀法二氧化硅(比表面积300m
2/g),在160℃保温1h,冷却到室温,即得所述有机硅组合物S2。
实施例3
将65g羟基聚有机硅氧烷HO[Si(CH
3)(CH
3CH
2CH
2CH
2)O]
800H和1g有机硅树脂(羟基含量0.3%)加入到反应容器中,并加入0.5g钛催化剂Ti(OCH
2CH
2CH
3)
4,在60℃时反应1.5h;再加入25g含氢聚有机硅氧烷HMe
2SiO(MeHSiO)
20(Me2SiO)
80SiMe
2H和10ppm铂-烯烃络合物,在 80℃时反应1h;反应完毕后,加入8.5g疏水气相法法二氧化硅(比表面积100m
2/g),在140℃保温2h,冷却到室温,即得所述有机硅组合物S3。
实施例4
将54.6g羟基聚有机硅氧烷HO[Si(CH
3)(PhCH
2CH
3)O]
1200H和3g有机硅树脂(羟基含量0.4%)加入到反应容器中,并加入0.4g钛催化剂Ti(O(CH
3)
2CH)
4,在80℃时反应1h;再加入40g含氢聚有机硅氧烷HMe
2SiO(MeHSiO)
10(Me2SiO)
20SiMe
2H和15ppm铂-醇盐络合物,在120℃时反应1h;反应完毕后,加入2g疏水气相法二氧化硅(比表面积150m
2/g),在150℃保温1h,冷却到室温,即得所述有机硅组合物S4。
实施例5
将62g羟基聚有机硅氧烷HO[Si(CH
3)(C
10H
21)O]
600H和7g有机硅树脂(羟基含量0.5%)加入到反应容器中,并加入1g钛催化剂Ti(OCH
2CH
2CH
2CH
3)
4,在50℃时反应3h;再加入20g含氢聚有机硅氧烷Me
3SiO(MeHSiO)
5(Me2SiO)
200SiMe
3和5ppm铂-醚络合物,在70℃时反应2.5h;反应完毕后,加入10g疏水沉淀法二氧化硅(比表面积200m
2/g),在150℃保温1h,冷却到室温,即得所述有机硅组合物S5。
实施例6
将65g羟基聚有机硅氧烷HO[Si(CH
3)(PhC14H29)O]
500H和3.5g有机硅树脂(羟基含量0.1%)加入到反应容器中,并加入0.5g钛催化 剂Ti(O(CH
3)
2CHCH
2)
4,在90℃时反应1h;再加入30g含氢聚有机硅氧烷HMe
2SiO(MeHSiO)
15(Me2SiO)
50SiMe
2H和12ppm铂-酮络合物,在140℃时反应2h;反应完毕后,加入1g疏水气相法二氧化硅(比表面积250m
2/g),在130℃保温2h,冷却到室温,即得所述有机硅组合物S6。
实施例7
将50g羟基聚有机硅氧烷HO[Si(CH
3)(CH
2CH
3)O]
500H和10g有机硅树脂(羟基含量0.2%)加入到反应容器中,并加入0.1g钛催化剂Ti(OCH
3)
4,在40℃时反应3h;再加入30g含氢聚有机硅氧烷HMe
2SiO(MeHSiO)
8(Me2SiO)
150SiMe
2H和1ppm铂-乙烯基络合物,在50℃时反应3h;反应完毕后,加入9.9g疏水二氧化钛,在100℃保温3h,冷却到室温,即得所述有机硅组合物S7。
实施例8
将70g羟基聚有机硅氧烷HO[Si(CH
3)((CH3)2CH)O]
1500H和5g有机硅树脂(羟基含量0.5%)加入到反应容器中,并加入1g钛催化剂Ti(OCH
2CH
3)
4,在100℃时反应0.5h;再加入20g含氢聚有机硅氧烷HMe
2SiO(MeHSiO)
18(Me2SiO)
250SiMe
2H和20ppm铂-醇络合物,在150℃时反应0.5h;反应完毕后,加入4g疏水石英粉,在160℃保温1h,冷却到室温,即得所述有机硅组合物S8。
实施例9
将65g羟基聚有机硅氧烷HO[Si(CH
3CH
2CH
2)(CH
3CH
2CH
2CH
2)O]
800H和1g有机硅树脂(羟基含量0.4%)加入到反应容器中,并加入0.5g钛 催化剂Ti(OCH
2CH
2CH
3)
4,在60℃时反应1.5h;再加入25g含氢聚有机硅氧烷HMe
2SiO(MeHSiO)
12(Me2SiO)
270SiMe
2H和10ppm铂-醚络合物,在80℃时反应1h;反应完毕后,加入8.5g疏水氧化铝,在140℃保温2h,冷却到室温,即得所述有机硅组合物S9。
实施例10
将54.6g羟基聚有机硅氧烷HO[Si((CH
3)
2CHCH
2)(PhCH
2CH
3)O]
1200H和3g有机硅树脂(羟基含量0.1%)加入到反应容器中,并加入0.4g钛催化剂Ti(O(CH
3)
2CH)
4,在80℃时反应1h;再加入40g含氢聚有机硅氧烷HMe
2SiO(MeHSiO)
16(Me2SiO)
120SiMe
2H和15ppm铂-乙烯基络合物,在120℃时反应1h;反应完毕后,加入2g疏水氧化锌,在150℃保温1h,冷却到室温,即得所述有机硅组合物S10。
实施例11
将62g羟基聚有机硅氧烷HO[Si(CH
3)(C
30H
61)O]
600H和7g有机硅树脂(羟基含量0.1%)加入到反应容器中,并加入1g钛催化剂Ti(OCH
2CH
3)
4,在50℃时反应3h;再加入20g含氢聚有机硅氧烷HMe
2SiO(MeHSiO)
19(Me2SiO)
40SiMe
2H和5ppm铂-醚络合物,在70℃时反应2.5h;反应完毕后,加入5g硅酸铝、5g氧化镁,在150℃保温1h,冷却到室温,即得所述有机硅组合物S11。
对比例1-与实施例1对比,钛催化剂替换为铂催化剂
将50g羟基聚有机硅氧烷HO[Si(CH
3)
2O]
500H和10g有机硅树脂(羟基含量0.1%)加入到反应容器中,并加入0.1g氯铂酸异丙醇溶液,在40℃时反应3h;再加入30g含氢聚有机硅氧烷 HMe
2SiO(MeHSiO)
2(Me2SiO)
300SiMe
2H和1ppm氯铂酸异丙醇溶液,在50℃时反应3h;反应完毕后,加入9.9g疏水沉淀法二氧化硅(比表面积50m
2/g),在100℃保温3h,冷却到室温,即得所述有机硅组合物D1。
对比例2-与实施例2对比,含氢硅油一次性加入,钛催化剂
将70g羟基聚有机硅氧烷HO[Si(CH
3)(C
6H
5)O]
1500H、5g有机硅树脂(羟基含量0.2%)、20g含氢聚有机硅氧烷Me
3SiO(MeHSiO)
2(Me2SiO)
100SiMe
3加入到反应容器中,并加入1g钛催化剂Ti(OCH
2CH
3)
4,在100℃时反应1h;反应完毕后,加入4g疏水沉淀法二氧化硅(比表面积300m
2/g),在160℃保温1h,冷却到室温,即得所述有机硅组合物D2。
对比例3-与实施例3对比,含氢硅油一次性加入,铂催化剂
将65g羟基聚有机硅氧烷HO[Si(CH
3)(CH
3CH
2CH
2CH
2)O]
800H、1g有机硅树脂(羟基含量0.3%)、25g含氢聚有机硅氧烷HMe
2SiO(MeHSiO)
20(Me2SiO)
80SiMe
2H加入到反应容器中,加入10ppm铂-烯烃络合物,在80℃时反应1h;反应完毕后,加入8.5g疏水气相法法二氧化硅(比表面积100m
2/g),在140℃保温2h,冷却到室温,即得所述有机硅组合物D3。
实施例12~25
按照现有技术,采用上述S1~S11、D1-D3的有机硅组合物制备有机硅乳液:
室温下,将40份有机硅组合物、8份失水山梨醇三油酸酯和12 份油酸聚氧乙烯醚在搅拌下充分混合40min,完成后将上述体系的温度升高至80℃,然后,保持体系温度,缓慢地加入40份水,提高搅拌速度使其由油包水型乳液变为水包油型乳液,继续加20份水至质量浓度为50%,过胶体磨进一步乳化,最后用丙烯酸增稠剂水溶液稀释到含固量为30%,得有机硅乳液消泡剂M1~14。
有机硅乳液性能测试
测试方法:以0.5%(质量百分比)的十二烷基苯磺酸钠水溶液为起泡介质,往100mL具塞量筒中加入上述起泡介质50mL,然后加入0.010g的有机硅乳液消泡剂,在垂直方向上摇振50次后静置,记录泡沫消至出现液面时间,即为消泡时间T
50,再摇振50次记录消泡时间T
100,每振摇50次就记录一下消泡时间,直至总摇瓶次数达到400次为止,相同振摇次数下,消泡时间越短,表示有机硅乳液的消抑泡效果越好。测试结果见表1:
表1 有机硅乳液的消泡性能对比
从上表结果可以看出,用实施例1~11的有机硅组合物S1~11合成的有机硅乳液消泡剂M1~11的性能优于对比例的1、2和3的有机硅组合物D1、D2和D3合成的有机硅乳液消泡剂M12~14,这说明本发明的有机硅组合物在阴离子体系中具有较强的消泡能力。
Claims (5)
- 一种有机硅组合物,其特征在于所述有机硅组合物由以下组分组成:A.改性聚有机硅氧烷本发明所述的改性聚有机硅氧烷是羟基聚有机硅氧烷、有机硅树脂和含氢聚有机硅氧烷反应得到的;A1.羟基聚有机硅氧烷所述的羟基聚有机硅氧烷的结构通式如下:HO(SiR 1 2O) mH式中R 1基相同或不同,为碳原子数1~30的烷基,具体选自甲基、乙基、丙基、正丙基、丁基、异丁基;或苯基;或碳原子数为7~20的芳烷基;下标m为500~1500的整数;所述羟基聚有机硅氧烷的用量为有机硅组合物总质量的50~70%;A2.有机硅树脂有机硅树脂由如下通式的单元组成:R c 2R d 3SiO(4-c-d)/2其中R 2和R 3可以相同或者不同,为羟基或单价的、取代或未取代的、饱和的或不饱和的具有1-6个碳原子的烃基,且R1、R2为羟基的总数量≥1,下标c是0、1、2或者3;下标d是0、1、2或者3;所述的有机硅树脂含羟基量为0.1%-0.5%,其用量为有机硅组合物总质量的1~10%;A3.含氢聚有机硅氧烷至少一种结构通式为如下的含氢聚有机硅氧烷:H nMe 3-nSiO(MeHSiO) a(Me2SiO) bSiMe 3-nH nMe为甲基,下标n是0、1,a是2~20的整数,b是20~300的整数,每个分子具有至少2个硅键合的氢原子。所述含氢聚有机硅氧烷的用量为有机硅组合物总质量的20~40%;A4.钛催化剂所述的钛催化剂为钛酸酯催化剂,结构式为Ti(OR) 4,式中:-OR为可水解的短链烷氧基,包括甲氧基、乙氧基、丙氧基、异丙氧基、丁氧基或异丁氧基。所述钛催化剂用量为有机硅组合物总质量的0.1~1%;A5.铂催化剂所述的铂催化剂用来催化组分含氢聚有机硅氧烷和体系中的含有羟基聚有机硅氧烷发生缩合反应,选自铂-醇络合物、铂-烯烃络合物、铂-醇盐络合物、铂-醚络合物、铂-酮络合物、氯铂酸异丙醇溶液、铂-乙烯基络合物,催化剂加量均以铂计(铂含量为1~20ppm);B.疏水粒子疏水粒子选自二氧化硅、二氧化钛、石英粉、氧化铝、硅酸铝、氧化锌、氧化镁,或两者或两者以上的混合物;所述有机硅组合物的制备方法如下:①将羟基聚有机硅氧烷A1和有机硅树脂A2加入到反应容器中,并加入催化剂A4,在40~100℃时反应0.5~3h;②再加入含氢聚有机硅氧烷A3和催化剂A5,在50~150℃时反应 0.5~3h;③反应完毕后,加入疏水粒子B,在100~160℃保温1~3h,冷却到室温,即得所述有机硅组合物。
- 如权利要求1所述的一种有机硅组合物,其特征在于所述的羟基具有机硅氧烷中R 1为烷基时,优选碳原子数为1-10的烷基。
- 如权利要求1所述的一种有机硅组合物,其特征在于所述的有机硅树脂中R 2和R 3优选具有1-6个碳原子的烷基。
- 如权利要求1所述的一种有机硅组合物,其特征在于所述的铂催化剂优选铂含量为1~20ppm的氯铂酸异丙醇溶液。
- 如权利要求1所述的一种有机硅组合物,其特征在于所述的疏水粒子优选比表面积为50~300m 2/g的疏水沉淀二氧化硅、疏水气相二氧化硅。
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CN114344955A (zh) * | 2021-12-01 | 2022-04-15 | 大连大平油脂化学有限公司 | 一种含有氧化稀土的消泡剂及其制备方法 |
Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6344905A (ja) * | 1987-05-29 | 1988-02-25 | Dow Corning Kk | シリコ−ン消泡剤組成物の製造方法 |
US4749740A (en) * | 1984-05-30 | 1988-06-07 | Dow Corning Kabushiki Kaisha | Method of producing a silicone defoamer composition |
US4983316A (en) * | 1988-08-04 | 1991-01-08 | Dow Corning Corporation | Dispersible silicone antifoam formulations |
CN103275493A (zh) * | 2013-06-07 | 2013-09-04 | 南京四新科技应用研究所有限公司 | 一种有机硅组合物 |
CN105498304A (zh) * | 2015-12-15 | 2016-04-20 | 江苏四新科技应用研究所股份有限公司 | 一种消泡组合物及其制备方法 |
CN106890485A (zh) * | 2015-12-18 | 2017-06-27 | 滁州四新科技有限责任公司 | 一种用于漂洗的消泡组合物的制备方法 |
Family Cites Families (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4558109A (en) * | 1984-07-25 | 1985-12-10 | Sws Silicones Corporation | Curable organopolysiloxane compositions |
CN85100879B (zh) * | 1985-04-01 | 1988-11-16 | 中国科学院化学研究所 | 高稳定性多羟基硅油乳液及其制法 |
DE19936289A1 (de) * | 1999-08-02 | 2001-02-15 | Wacker Chemie Gmbh | Entschäumerformulierung |
CN100594968C (zh) * | 2008-01-18 | 2010-03-24 | 滁州四新科技有限责任公司 | 一种分散高粘度有机硅混合物的方法 |
CN101280112A (zh) * | 2008-05-16 | 2008-10-08 | 卢儒 | 发泡硅橡胶 |
CN101555385B (zh) * | 2009-05-07 | 2012-10-24 | 中国科学院广州化学研究所 | 一种水稀释型有机硅涂料及其制备方法 |
WO2012058798A1 (en) * | 2010-11-02 | 2012-05-10 | Henkel China Co. Ltd. | Hydrosilicone resin and preparation process thereof |
CN103182271B (zh) * | 2011-12-27 | 2015-10-28 | 广东标美硅氟新材料有限公司 | 一种有机硅表面活性剂及其制备方法和应用 |
CN104784980B (zh) * | 2015-04-02 | 2016-05-11 | 江苏四新科技应用研究所股份有限公司 | 一种消泡组合物 |
CN105107237B (zh) * | 2015-10-12 | 2017-03-29 | 江苏四新科技应用研究所股份有限公司 | 一种有机硅消泡组合物及其制备方法 |
CN110898467B (zh) * | 2019-12-05 | 2021-02-05 | 浙江新安化工集团股份有限公司 | 消泡活性物、其制备方法及消泡剂 |
-
2020
- 2020-04-30 CN CN202010365009.8A patent/CN113577837B/zh active Active
- 2020-06-22 WO PCT/CN2020/097384 patent/WO2021217835A1/zh active Application Filing
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4749740A (en) * | 1984-05-30 | 1988-06-07 | Dow Corning Kabushiki Kaisha | Method of producing a silicone defoamer composition |
JPS6344905A (ja) * | 1987-05-29 | 1988-02-25 | Dow Corning Kk | シリコ−ン消泡剤組成物の製造方法 |
US4983316A (en) * | 1988-08-04 | 1991-01-08 | Dow Corning Corporation | Dispersible silicone antifoam formulations |
CN103275493A (zh) * | 2013-06-07 | 2013-09-04 | 南京四新科技应用研究所有限公司 | 一种有机硅组合物 |
CN105498304A (zh) * | 2015-12-15 | 2016-04-20 | 江苏四新科技应用研究所股份有限公司 | 一种消泡组合物及其制备方法 |
CN106890485A (zh) * | 2015-12-18 | 2017-06-27 | 滁州四新科技有限责任公司 | 一种用于漂洗的消泡组合物的制备方法 |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN114344955A (zh) * | 2021-12-01 | 2022-04-15 | 大连大平油脂化学有限公司 | 一种含有氧化稀土的消泡剂及其制备方法 |
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