CN107446357A - A kind of low-density micropore diameter silicon rubber composite material and preparation method thereof - Google Patents
A kind of low-density micropore diameter silicon rubber composite material and preparation method thereof Download PDFInfo
- Publication number
- CN107446357A CN107446357A CN201710694110.6A CN201710694110A CN107446357A CN 107446357 A CN107446357 A CN 107446357A CN 201710694110 A CN201710694110 A CN 201710694110A CN 107446357 A CN107446357 A CN 107446357A
- Authority
- CN
- China
- Prior art keywords
- composite material
- rubber composite
- silicone rubber
- vinyl polysiloxane
- low
- 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.)
- Pending
Links
Classifications
-
- 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
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J9/00—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
- C08J9/04—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent
- C08J9/06—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent by a chemical blowing agent
- C08J9/08—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent by a chemical blowing agent developing carbon dioxide
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J2203/00—Foams characterized by the expanding agent
- C08J2203/02—CO2-releasing, e.g. NaHCO3 and citric acid
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J2383/00—Characterised by the use 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; Derivatives of such polymers
- C08J2383/04—Polysiloxanes
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J2483/00—Characterised by the use 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; Derivatives of such polymers
- C08J2483/04—Polysiloxanes
-
- 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
- C08K2201/00—Specific properties of additives
- C08K2201/002—Physical properties
- C08K2201/003—Additives being defined by their diameter
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L2203/00—Applications
- C08L2203/14—Applications used for foams
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L2205/00—Polymer mixtures characterised by other features
- C08L2205/02—Polymer mixtures characterised by other features containing two or more polymers of the same C08L -group
- C08L2205/025—Polymer mixtures characterised by other features containing two or more polymers of the same C08L -group containing two or more polymers of the same hierarchy C08L, and differing only in parameters such as density, comonomer content, molecular weight, structure
Landscapes
- Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
- Compositions Of Macromolecular Compounds (AREA)
Abstract
本发明涉及硅橡胶领域,具体涉及一种低密度小孔径硅橡胶复合材料及其制备方法。该硅橡胶复合材料,由如下重量百分比的原料构成:乙烯基聚硅氧烷100份,反应抑制剂0.01‑1份,交联催化剂0.01‑1份,含氢硅油2‑10份。热膨胀微球5‑30份,超细碳酸氢钠粉体5‑30份。本发明制备过程简单,将中空热膨胀微球和超细碳酸氢钠粉体按照预混比例与硅胶各组分进行共混,使其均匀分散在硅胶胶体中,经固化得到复合硅胶预混物,然后将预混复合胶体置于合适的温度,进行热处理,得到低密度微孔硅橡胶复合材料。The invention relates to the field of silicone rubber, in particular to a low-density and small-aperture silicone rubber composite material and a preparation method thereof. The silicone rubber composite material is composed of the following raw materials in weight percentage: 100 parts of vinyl polysiloxane, 0.01-1 part of reaction inhibitor, 0.01-1 part of crosslinking catalyst, and 2-10 parts of hydrogen-containing silicone oil. 5-30 parts of heat-expandable microspheres, 5-30 parts of ultrafine sodium bicarbonate powder. The preparation process of the invention is simple. The hollow heat-expandable microspheres and ultrafine sodium bicarbonate powder are blended with the components of silica gel according to the premixing ratio, so that they are evenly dispersed in the silica gel colloid, and the composite silica gel premix is obtained after curing. Then the premixed composite colloid is placed at a suitable temperature for heat treatment to obtain a low-density microporous silicone rubber composite material.
Description
技术领域technical field
本发明涉及一种硅橡胶复合产品及其制备方法,具体涉及到一种低密度微孔径硅橡胶复合材料的制备。The invention relates to a silicone rubber composite product and a preparation method thereof, in particular to the preparation of a low-density microporous silicone rubber composite material.
背景技术Background technique
微孔聚合物材料是由基体树脂(粘结料)与空心微球经过混合、固化、成型、固化得到的一种复合材料。硅橡胶复合材料结合了硅橡胶材料优异的耐高低温性、无毒、卓越的化学稳定性、优良的电绝缘性、耐光老化性以及生理惰性等优点,还具有微孔材料的低密度、质轻、阻尼性好以及高的回弹性。因其独特的结构和优异的性能,使其在化工、汽车、电子电气、机械、医学、航空航天等领域得到了广泛的应用。Microporous polymer material is a composite material obtained by mixing, curing, molding and curing matrix resin (binder) and hollow microspheres. Silicone rubber composite materials combine the advantages of silicone rubber materials such as excellent high and low temperature resistance, non-toxicity, excellent chemical stability, excellent electrical insulation, light aging resistance and physiological inertness, and also have the low density and quality of microporous materials. Lightweight, good damping and high resilience. Because of its unique structure and excellent performance, it has been widely used in chemical industry, automobile, electrical and electronic, machinery, medicine, aerospace and other fields.
目前,制备微孔硅橡胶复合材料的中空微球主要有硼酸盐空心玻璃微球、中空玻璃微球、酚醛空心微球、氧化锆空心微球、碳空心微球、陶瓷空心微球、热塑性中空微球、二氧化硅中空微球等。根据中空微球的外壳构成,可以将中空微球大致分为硬质微球和柔性微球。在现有技术和报道的文献中,微孔复合材料的制备可采用一种或两种微球复合(LiuQ,Journal of Materials Science,2015,50(11):3976-3983),也有专利报道将中空微球与化学发泡剂进行配合使用(章炎敏.热膨胀微球在聚乙烯发泡中的应用研究,上海交通大学硕士论文,2011)。如果单一使用硬质微球填充,硬质微球容易破损,会极大降低硅橡胶复合材料的柔性;单一使用柔性中空微球,会降低硅橡胶复合材料的强度,而采用有机发泡剂发泡,其分解产物不符合环保要求。以上均限制了微孔硅橡胶复合材料的应用。此外,由于发泡和硅橡胶固化的矛盾,使得孔径难以控制,特别是难以得到密度低,孔洞均匀细密的硅橡胶产品。At present, hollow microspheres for the preparation of microporous silicone rubber composites mainly include borate hollow glass microspheres, hollow glass microspheres, phenolic hollow microspheres, zirconia hollow microspheres, carbon hollow microspheres, ceramic hollow microspheres, thermoplastic Hollow microspheres, silica hollow microspheres, etc. According to the structure of the shell of hollow microspheres, hollow microspheres can be roughly divided into hard microspheres and flexible microspheres. In prior art and reported literature, the preparation of microporous composite material can adopt one or two kinds of microsphere composite (LiuQ, Journal of Materials Science, 2015,50 (11): 3976-3983), also has patent report to be Hollow microspheres are used in conjunction with chemical foaming agents (Zhang Yanmin. Application research of thermally expandable microspheres in polyethylene foaming, master's thesis of Shanghai Jiao Tong University, 2011). If only hard microspheres are used for filling, the hard microspheres are easy to break, which will greatly reduce the flexibility of the silicone rubber composite material; the single use of flexible hollow microspheres will reduce the strength of the silicone rubber composite material, and the use of organic foaming agents will reduce the strength of the silicone rubber composite material. Bubbles, and its decomposition products do not meet environmental protection requirements. All of the above limit the application of microporous silicone rubber composites. In addition, due to the contradiction between foaming and silicone rubber curing, it is difficult to control the pore size, especially it is difficult to obtain a silicone rubber product with low density and uniform and fine pores.
发明内容Contents of the invention
本发明的目的是在保证制备过程和最终产品环保无毒的前提下,提供一种环保的微孔径低密度硅橡胶复合材料及制备方法。该硅橡胶复合材料采用无机盐分解与中空微球填充相结合,同时通过控制无机盐及中空微球的粒径大小,使最终得到的硅橡胶复合材料的内部孔径小于20微米。该方法更为显著的优势时,制得的硅橡胶复合材料环保无毒,低密度且工艺简单。The purpose of the present invention is to provide an environmentally friendly micro-aperture low-density silicone rubber composite material and a preparation method under the premise of ensuring the preparation process and the final product are environmentally friendly and non-toxic. The silicone rubber composite material adopts the combination of inorganic salt decomposition and hollow microsphere filling, and at the same time, by controlling the particle size of the inorganic salt and hollow microspheres, the internal pore diameter of the finally obtained silicone rubber composite material is less than 20 microns. The more significant advantages of this method are that the prepared silicone rubber composite material is environmentally friendly, non-toxic, low-density and simple in process.
为了实现上述目的,本发明采用以下技术方案:In order to achieve the above object, the present invention adopts the following technical solutions:
一种低密度微孔径硅橡胶复合材料,所述低密度微孔径硅橡胶复合材料由如下组分按重量百分比构成:A low-density microporous silicon rubber composite material, said low-density microporous silicon rubber composite material is composed of the following components by weight percentage:
所述的反应抑制剂为乙炔基环已醇;所述的交联催化剂为铂金催化剂;所述超细碳酸氢钠的粒径范围为1~10微米;所述热膨胀中空微球的直径为6~9微米。The reaction inhibitor is ethynyl cyclohexanol; the cross-linking catalyst is a platinum catalyst; the particle size range of the ultrafine sodium bicarbonate is 1 to 10 microns; the diameter of the thermally expandable hollow microspheres is 6 ~9 microns.
进一步,本发明所述的铂金催化剂主要由氯铂酸及其配合物如铂-乙烯基硅氧烷配合物催化剂等组成。Furthermore, the platinum catalyst described in the present invention is mainly composed of chloroplatinic acid and its complexes such as platinum-vinylsiloxane complex catalysts and the like.
进一步,本发明所述的含氢硅油活性氢质量分数为0.18%,粘度1000mpa.s。Further, the hydrogen-containing silicone oil of the present invention has an active hydrogen mass fraction of 0.18% and a viscosity of 1000mpa.s.
进一步,本发明所述的乙烯基聚硅氧烷为含有两个或两个以上的乙烯基的乙烯基聚硅氧烷。Further, the vinyl polysiloxane described in the present invention is a vinyl polysiloxane containing two or more vinyl groups.
更进一步,本发明所述的乙烯基聚硅氧烷为经过气相白炭黑补强的乙烯基聚硅氧烷。利用气相白炭黑补强乙烯基聚硅氧烷为本领域技术人员公知的技术,本发明在1质量份的乙烯基聚硅氧烷加入0.3份白炭黑,经捏合机高强度混炼而得到补强的乙烯基聚硅氧烷。Furthermore, the vinyl polysiloxane described in the present invention is a vinyl polysiloxane reinforced with fumed silica. Utilizing fumed silica to reinforce vinyl polysiloxane is a technology well known to those skilled in the art. In the present invention, 0.3 parts of white carbon black is added to 1 mass part of vinyl polysiloxane, which is kneaded by a kneader at high intensity. A reinforced vinyl polysiloxane is obtained.
优选地,本发明所述低密度微孔径硅橡胶复合材料推荐由如下组分按重量百分比构成:Preferably, the low-density microporous silicone rubber composite material of the present invention is recommended to be composed of the following components by weight percentage:
本发明还提供一种所述的低密度微孔径硅橡胶复合材料的制备方法:The present invention also provides a method for preparing the low-density microporous silicone rubber composite material:
(1)按配比称取各组分,在乙烯基聚硅氧烷中加入交联催化剂用捏合机混炼均匀;在含氢硅油中加入反应抑制剂,用搅拌机搅拌均匀;(1) Weigh each component according to the proportion, add a crosslinking catalyst into the vinyl polysiloxane and knead evenly with a kneader; add a reaction inhibitor into the hydrogen-containing silicone oil, and stir evenly with a mixer;
(2)将上述经过预处理的各组分使用机械手段进行共混处理,使各组分分散均匀,得到预混物,将预混物进行真空除气泡处理,之后倒入模具中,然后在45~70℃下固化完全,再置于90~160℃环境下保温1~2小时,得到所述硅橡胶复合材料。(2) Blending the above-mentioned pretreated components using mechanical means to disperse the components uniformly to obtain a premix, which is subjected to vacuum degassing treatment, then poured into a mold, and then It is completely cured at 45-70° C., and then kept at 90-160° C. for 1-2 hours to obtain the silicone rubber composite material.
本发明的有益效果:1:该方法的制备过程简单,对设备要求低,可操作性强,易于工业化生产。2:该方法制备出的硅橡胶复合泡沫材料,环保无毒,密度低,且内部孔洞通过无机发泡剂分解和中空微球填充而成,即同时含有开孔和闭孔结构,且孔洞均匀细密,最低密度到达0.4g/cm3。Beneficial effects of the present invention: 1: The preparation process of the method is simple, requires less equipment, has strong operability, and is easy for industrial production. 2: The silicone rubber composite foam material prepared by this method is environmentally friendly, non-toxic, and has low density, and the internal pores are decomposed by inorganic foaming agents and filled with hollow microspheres, that is, they contain both open-cell and closed-cell structures, and the pores are uniform. Fine and dense, the lowest density reaches 0.4g/cm 3 .
附图说明Description of drawings
图1为实施例2产品的断面图。Fig. 1 is the sectional view of embodiment 2 products.
具体实施方式detailed description
下面结合具体实施例对本发明进行进一步描述,但本发明的保护范围并不仅限于此。The present invention will be further described below in conjunction with specific examples, but the protection scope of the present invention is not limited thereto.
以下实施例及对比例中,原料乙烯基聚硅氧烷皆为含有两个或两个以上的乙烯基且经过气相白炭黑补强的乙烯基聚硅氧烷,市售,购于东莞市良展有机硅科技有限公司;所用的交联催化剂剂均为铂金催化剂,市售,该催化剂为添加铂金催化剂的配合物,其铂负载量5000ppm;所用含氢硅油的粘度为1000mpas,活性氢质量分数为0.18%,购于东莞市良展有机硅科技有限公司;所用的超细碳酸氢钠粉体粒径分布为1-10μm,市售,经过形星球磨处理得到;所用热膨胀微球牌号为Expancel461DU20,瑞典AkzoNobel公司产;In the following examples and comparative examples, the raw material vinyl polysiloxane is a vinyl polysiloxane containing two or more vinyl groups and reinforced with fumed silica, which is commercially available in Dongguan City Liangzhan Silicone Technology Co., Ltd.; the cross-linking catalysts used are all platinum catalysts, which are commercially available. The catalyst is a complex with platinum catalysts, and its platinum loading is 5000ppm; the viscosity of the hydrogen-containing silicone oil used is 1000mpas, and the mass of active hydrogen The fraction is 0.18%, purchased from Dongguan Liangzhan Silicone Technology Co., Ltd.; the particle size distribution of the ultrafine sodium bicarbonate powder used is 1-10 μm, which is commercially available and obtained through a shaped ball mill; the brand name of the thermally expandable microspheres used is Expancel461DU20, produced by AkzoNobel, Sweden;
对比例1Comparative example 1
取100质量份的乙烯基聚硅氧烷,预先加入0.2份铂金催化剂;含氢硅油10质量份,预先加入0.2份反应抑制剂。然后将两组份依次加入反应容器中,然后使用机械混合20min,得到混合物;然后使用三辊研磨机对混合物料进行研磨处理,得到混合均匀的物料,同时排除混合胶体中的气泡,为了确保气泡的完全排除,再次使用真空箱对其进一步排气处理。将共混好的胶料倒入设计的模具中,然后将装有胶料的模具放入温度为60℃的真空干燥箱中,固化1小时,得到未复合的硅橡胶胶料作为对比样。Take 100 parts by mass of vinyl polysiloxane, add 0.2 parts of platinum catalyst in advance; 10 parts by mass of hydrogen-containing silicone oil, add 0.2 parts of reaction inhibitor in advance. Then add the two components into the reaction container in turn, and then use mechanical mixing for 20 minutes to obtain the mixture; then use a three-roll mill to grind the mixed material to obtain a uniformly mixed material, and at the same time remove the air bubbles in the mixed colloid. In order to ensure that the air bubbles Completely exclude, use the vacuum box again for further exhaust treatment. Pour the blended rubber into the designed mold, and then put the mold with the rubber into a vacuum drying oven at a temperature of 60°C, and cure it for 1 hour to obtain an uncomposited silicone rubber as a comparison sample.
实施例1Example 1
取100质量份的乙烯基聚硅氧烷,预先加入0.2份铂金催化剂;含氢硅油10质量份,预先加入0.2份反应抑制剂,碳酸氢钠粉体5质量份,热膨胀微球5质量份,将上述组分采用机械搅拌分散,得到预混料,然后使用三辊研磨机对预混料进行进一步共混处理,使各组分分散均匀,得到预混物。然后使用辊距为0.1mm的三辊研磨机对混合物料进行研磨处理,得到混合均匀的物料,同时排除混合胶体中的气泡,为了确保气泡的完全排除,再次使用真空箱对其进一步排气处理。将共混好的胶料倒入设计的模具中,在60℃的温度下固化反应1小时,得到固化胶体。然后升温至140℃,保温处理2小时,使胶体中填充的碳酸氢钠粉体分解气化,同时热膨胀微球内部液烃气化,得到最终的硅橡胶复合材料。Get 100 parts by mass of vinyl polysiloxane, add 0.2 parts of platinum catalyst in advance; 10 parts by mass of hydrogen-containing silicone oil, add 0.2 parts of reaction inhibitor in advance, 5 parts by mass of sodium bicarbonate powder, 5 parts by mass of thermally expandable microspheres, The above components are dispersed by mechanical stirring to obtain a premix, and then the premix is further blended by using a three-roll mill to disperse the components uniformly to obtain a premix. Then use a three-roll mill with a roll distance of 0.1mm to grind the mixed material to obtain a uniformly mixed material, and at the same time remove the air bubbles in the mixed colloid. In order to ensure the complete removal of the air bubbles, use a vacuum box again to further exhaust it. . The blended rubber was poured into the designed mold, and cured at a temperature of 60° C. for 1 hour to obtain a cured gel. Then the temperature was raised to 140°C, and the heat preservation treatment was carried out for 2 hours, so that the sodium bicarbonate powder filled in the colloid was decomposed and gasified, and at the same time, the liquid hydrocarbon inside the heat-expandable microspheres was gasified to obtain the final silicone rubber composite material.
实施例2Example 2
取100质量份的乙烯基聚硅氧烷,预先加入0.1份铂金催化剂;含氢硅油10质量份,预先加入0.1份反应抑制剂,碳酸氢钠粉体10质量份,热膨胀微球10份。将上述组分采用机械搅拌分散,得到预混料,然后使用三辊研磨机对预混料进行进一步共混处理,使各组分分散均匀,得到预混物。然后使用辊距为0.1mm的三辊研磨机对混合物料进行研磨处理,得到混合均匀的物料,同时排除混合胶体中的气泡,为了确保气泡的完全排除,再次使用真空箱对其进一步排气处理。将共混好的胶料倒入设计的模具中,在70℃的温度下固化反应1小时,得到固化胶体。然后升温至140℃,保温处理2小时,使胶体中填充的碳酸氢钠粉体分解气化,同时热膨胀微球内部液烃气化,得到最终的硅橡胶复合材料。Take 100 parts by mass of vinyl polysiloxane, add 0.1 part of platinum catalyst in advance; 10 parts by mass of hydrogen-containing silicone oil, add in advance 0.1 part of reaction inhibitor, 10 parts by mass of sodium bicarbonate powder, and 10 parts of thermally expandable microspheres. The above components are dispersed by mechanical stirring to obtain a premix, and then the premix is further blended by using a three-roll mill to disperse the components uniformly to obtain a premix. Then use a three-roll mill with a roll distance of 0.1mm to grind the mixed material to obtain a uniformly mixed material, and at the same time remove the air bubbles in the mixed colloid. In order to ensure the complete removal of the air bubbles, use a vacuum box again to further exhaust it. . The blended rubber was poured into the designed mold, and cured at a temperature of 70°C for 1 hour to obtain a cured gel. Then the temperature was raised to 140°C, and the heat preservation treatment was carried out for 2 hours, so that the sodium bicarbonate powder filled in the colloid was decomposed and gasified, and at the same time, the liquid hydrocarbon inside the heat-expandable microspheres was gasified to obtain the final silicone rubber composite material.
实施例3Example 3
取100质量份的乙烯基聚硅氧烷,预先加入0.2份铂金催化剂;含氢硅油10质量份,预先加入2份反应抑制剂,碳酸氢钠粉体15质量份,热膨胀微球15份,将上述组分采用机械搅拌分散,得到预混料,然后使用三辊研磨机对预混料进行进一步共混处理,使各组分分散均匀,得到预混物。然后使用辊距为0.1mm的三辊研磨机对混合物料进行研磨处理,得到混合均匀的物料,同时排除混合胶体中的气泡,为了确保气泡的完全排除,再次使用真空箱对其进一步排气处理。将共混好的胶料倒入设计的模具中,在70℃的温度下固化反应1小时,得到固化胶体。然后升温至140℃,保温处理2小时,使胶体中填充的碳酸氢钠粉体分解气化,同时热膨胀微球内部液烃气化,得到最终的硅橡胶复合材料。Take 100 parts by mass of vinyl polysiloxane, add 0.2 parts of platinum catalyst in advance; The above components are dispersed by mechanical stirring to obtain a premix, and then the premix is further blended by using a three-roller mill to uniformly disperse each component to obtain a premix. Then use a three-roll mill with a roll distance of 0.1mm to grind the mixed material to obtain a uniformly mixed material, and at the same time remove the air bubbles in the mixed colloid. In order to ensure the complete removal of the air bubbles, use a vacuum box again to further exhaust it. . The blended rubber was poured into the designed mold, and cured at a temperature of 70°C for 1 hour to obtain a cured gel. Then the temperature was raised to 140°C, and the heat preservation treatment was carried out for 2 hours, so that the sodium bicarbonate powder filled in the colloid was decomposed and gasified, and at the same time, the liquid hydrocarbon inside the heat-expandable microspheres was gasified to obtain the final silicone rubber composite material.
实施例4Example 4
取100质量份的乙烯基聚硅氧烷,预先加入2份铂金催化剂;含氢硅油10质量份,预先加入2份反应抑制剂,碳酸氢钠粉体10质量份,热膨胀微球20份,将上述组分采用机械搅拌分散,得到预混料,然后使用三辊研磨机对预混胶料进行进一步共混处理,使各组分分散均匀,得到预混物。然后使用辊距为0.1mm的三辊研磨机对混合物料进行研磨处理,得到混合均匀的物料,同时排除混合胶体中的气泡,为了确保气泡的完全排除,再次使用真空箱对其进一步排气处理。将共混好的胶料倒入设计的模具中,在45℃的温度下固化反应1小时,得到固化胶体。然后升温至160℃,保温处理1小时,使胶体中填充的碳酸氢钠粉体分解气化,同时热膨胀微球内部液烃气化,得到最终的硅橡胶复合材料。Take 100 parts by mass of vinyl polysiloxane, add 2 parts of platinum catalyst in advance; The above components are dispersed by mechanical stirring to obtain a premix, and then the premix is further blended with a three-roll mill to make the components uniformly dispersed to obtain a premix. Then use a three-roll mill with a roll distance of 0.1mm to grind the mixed material to obtain a uniformly mixed material, and at the same time remove the air bubbles in the mixed colloid. In order to ensure the complete removal of the air bubbles, use a vacuum box again to further exhaust it. . The blended rubber was poured into the designed mold, and cured at a temperature of 45° C. for 1 hour to obtain a cured gel. Then the temperature is raised to 160°C, and the heat preservation treatment is carried out for 1 hour, so that the sodium bicarbonate powder filled in the colloid is decomposed and gasified, and at the same time, the liquid hydrocarbon inside the heat-expandable microspheres is gasified to obtain the final silicone rubber composite material.
实施例5Example 5
取100质量份的乙烯基聚硅氧烷,预先加入0.2份铂金催化剂;含氢硅油10质量份,预先加入0.5份反应抑制剂,碳酸氢钠粉体20质量份,热膨胀微球10份,将上述组分采用机械搅拌分散,得到预混料,然后使用三辊研磨机对预混料进行进一步共混处理,使各组分分散均匀,得到预混物。然后使用辊距为0.1mm的三辊研磨机对混合物料进行研磨处理,得到混合均匀的物料,同时排除混合胶体中的气泡,为了确保气泡的完全排除,再次使用真空箱对其进一步排气处理。将共混好的胶料倒入设计的模具中,在60℃的温度下固化反应1小时,得到固化胶体。然后升温至90℃,保温处理2小时,使胶体中填充的碳酸氢钠粉体分解气化,同时热膨胀微球内部液烃气化,得到最终的硅橡胶复合材料。Take 100 parts by mass of vinyl polysiloxane, add 0.2 parts of platinum catalyst in advance; The above components are dispersed by mechanical stirring to obtain a premix, and then the premix is further blended by using a three-roller mill to uniformly disperse each component to obtain a premix. Then use a three-roll mill with a roll distance of 0.1mm to grind the mixed material to obtain a uniformly mixed material, and at the same time remove the air bubbles in the mixed colloid. In order to ensure the complete removal of the air bubbles, use a vacuum box again to further exhaust it. . The blended rubber was poured into the designed mold, and cured at a temperature of 60° C. for 1 hour to obtain a cured gel. Then raise the temperature to 90°C and heat-preserve for 2 hours to decompose and gasify the sodium bicarbonate powder filled in the colloid, and at the same time gasify the liquid hydrocarbon inside the heat-expandable microspheres to obtain the final silicone rubber composite material.
实施例6Example 6
取100质量份的乙烯基聚硅氧烷,预先加入0.5份铂金催化剂;含氢硅油10质量份,预先加入0.5份反应抑制剂,碳酸氢钠粉体30质量份,热膨胀微球30份。将上述组分采用机械搅拌分散,得到预混料,然后使用三辊研磨机对预混料进行进一步共混处理,使各组分分散均匀,得到预混料。然后使用辊距为0.1mm的三辊研磨机对混合物料进行研磨处理,得到混合均匀的物料,同时排除混合胶体中的气泡,为了确保气泡的完全排除,再次使用真空箱对其进一步排气处理。将共混好的胶料倒入设计的模具中,在60℃的温度下固化反应1小时,得到固化胶体。然后升温至90℃,保温处理2小时,使胶体中填充的碳酸氢钠粉体分解气化,同时热膨胀微球内部液烃气化,得到最终的硅橡胶复合材料。Take 100 parts by mass of vinyl polysiloxane, add 0.5 parts of platinum catalyst in advance; 10 parts by mass of hydrogen-containing silicone oil, add in advance 0.5 parts of reaction inhibitor, 30 parts by mass of sodium bicarbonate powder, and 30 parts by mass of thermally expandable microspheres. The above-mentioned components are dispersed by mechanical stirring to obtain a premix, and then the premix is further blended by using a three-roller mill, so that each component is uniformly dispersed to obtain a premix. Then use a three-roll mill with a roll distance of 0.1mm to grind the mixed material to obtain a uniformly mixed material, and at the same time remove the air bubbles in the mixed colloid. In order to ensure the complete removal of the air bubbles, use a vacuum box again to further exhaust it. . The blended rubber was poured into the designed mold, and cured at a temperature of 60° C. for 1 hour to obtain a cured gel. Then raise the temperature to 90°C and heat-preserve for 2 hours to decompose and gasify the sodium bicarbonate powder filled in the colloid, and at the same time gasify the liquid hydrocarbon inside the heat-expandable microspheres to obtain the final silicone rubber composite material.
实施例7Example 7
取100质量份的乙烯基聚硅氧烷,预先加入0.2份铂金催化剂;含氢硅油2质量份,预先加入0.2份反应抑制剂,碳酸氢钠粉体5质量份,热膨胀微球5质量份,将上述组分采用机械搅拌分散,得到预混料,然后使用三辊研磨机对预混料进行进一步共混处理,使各组分分散均匀,得到预混物。然后使用辊距为0.1mm的三辊研磨机对混合物料进行研磨处理,得到混合均匀的物料,同时排除混合胶体中的气泡,为了确保气泡的完全排除,再次使用真空箱对其进一步排气处理。将共混好的胶料倒入设计的模具中,在60℃的温度下固化反应1小时,得到固化胶体。然后升温至160℃,保温处理1小时,使胶体中填充的碳酸氢钠粉体分解气化,同时热膨胀微球内部液烃气化,得到最终的硅橡胶复合材料。Get 100 parts by mass of vinyl polysiloxane, add 0.2 parts of platinum catalyst in advance; 2 parts by mass of hydrogen-containing silicone oil, add 0.2 parts of reaction inhibitor in advance, 5 parts by mass of sodium bicarbonate powder, 5 parts by mass of thermally expandable microspheres, The above components are dispersed by mechanical stirring to obtain a premix, and then the premix is further blended by using a three-roll mill to disperse the components uniformly to obtain a premix. Then use a three-roll mill with a roll distance of 0.1mm to grind the mixed material to obtain a uniformly mixed material, and at the same time remove the air bubbles in the mixed colloid. In order to ensure the complete removal of the air bubbles, use a vacuum box again to further exhaust it. . The blended rubber was poured into the designed mold, and cured at a temperature of 60° C. for 1 hour to obtain a cured gel. Then the temperature is raised to 160°C, and the heat preservation treatment is carried out for 1 hour, so that the sodium bicarbonate powder filled in the colloid is decomposed and gasified, and at the same time, the liquid hydrocarbon inside the heat-expandable microspheres is gasified to obtain the final silicone rubber composite material.
实施例8Example 8
取100质量份的乙烯基聚硅氧烷,预先加入0.2份铂金催化剂;含氢硅油7质量份,预先加入0.2份反应抑制剂,碳酸氢钠粉体5质量份,热膨胀微球5质量份,将上述组分采用机械搅拌分散,得到预混料,然后使用三辊研磨机对预混料进行进一步共混处理,使各组分分散均匀,得到预混物。然后使用辊距为0.1mm的三辊研磨机对混合物料进行研磨处理,得到混合均匀的物料,同时排除混合胶体中的气泡,为了确保气泡的完全排除,再次使用真空箱对其进一步排气处理。将共混好的胶料倒入设计的模具中,在60℃的温度下固化反应1小时,得到固化胶体。然后升温至160℃,保温处理1小时,使胶体中填充的碳酸氢钠粉体分解气化,同时热膨胀微球内部液烃气化,得到最终的硅橡胶复合材料。Get 100 parts by mass of vinyl polysiloxane, add 0.2 parts of platinum catalyst in advance; 7 parts by mass of hydrogen-containing silicone oil, add 0.2 parts of reaction inhibitor in advance, 5 parts by mass of sodium bicarbonate powder, 5 parts by mass of thermally expandable microspheres, The above components are dispersed by mechanical stirring to obtain a premix, and then the premix is further blended by using a three-roll mill to disperse the components uniformly to obtain a premix. Then use a three-roll mill with a roll distance of 0.1mm to grind the mixed material to obtain a uniformly mixed material, and at the same time remove the air bubbles in the mixed colloid. In order to ensure the complete removal of the air bubbles, use a vacuum box again to further exhaust it. . The blended rubber was poured into the designed mold, and cured at a temperature of 60° C. for 1 hour to obtain a cured gel. Then the temperature is raised to 160°C, and the heat preservation treatment is carried out for 1 hour, so that the sodium bicarbonate powder filled in the colloid is decomposed and gasified, and at the same time, the liquid hydrocarbon inside the heat-expandable microspheres is gasified to obtain the final silicone rubber composite material.
对比例以及各个实施例硅橡胶复合材料的测试结果如下表所示:Comparative example and the test result of each embodiment silicone rubber composite material are shown in the table below:
经过实验和测试,制备所得的低密度微孔径硅橡胶复合材料,其内部热膨胀中空微球和碳酸氢钠颗粒在硅胶胶体中分散均匀,碳酸氢钠分解所构成泡孔孔径均在15微米内,细密均匀,热膨胀微球孔径均小于20微米,如图1所示。After experiments and tests, the prepared low-density microporous silicone rubber composite material has internal heat-expandable hollow microspheres and sodium bicarbonate particles dispersed evenly in the silica gel colloid, and the pore diameters of the cells formed by the decomposition of sodium bicarbonate are all within 15 microns. Fine and uniform, the pore size of thermal expansion microspheres is less than 20 microns, as shown in Figure 1.
需要指出的是,本发明的实施例仅为了说明本发明的技术构思及特点,其目的在与让熟悉此项技术的人士能够明白本发明的创新点和内容,并据以实施。依据本发明专利申请所述的构造、特征及原理所做的等效变化或修饰,均包括于本发明专利申请范围内。It should be pointed out that the embodiments of the present invention are only for illustrating the technical concepts and features of the present invention, and its purpose is to enable those familiar with this technology to understand the innovations and contents of the present invention and implement them accordingly. Equivalent changes or modifications based on the structures, features and principles described in the patent application of the present invention are included in the scope of the patent application of the present invention.
Claims (7)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710694110.6A CN107446357A (en) | 2017-08-11 | 2017-08-11 | A kind of low-density micropore diameter silicon rubber composite material and preparation method thereof |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710694110.6A CN107446357A (en) | 2017-08-11 | 2017-08-11 | A kind of low-density micropore diameter silicon rubber composite material and preparation method thereof |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN107446357A true CN107446357A (en) | 2017-12-08 |
Family
ID=60492290
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201710694110.6A Pending CN107446357A (en) | 2017-08-11 | 2017-08-11 | A kind of low-density micropore diameter silicon rubber composite material and preparation method thereof |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN107446357A (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111207173A (en) * | 2020-01-09 | 2020-05-29 | 苏州赛伍应用技术股份有限公司 | Buffering silica gel sheet used between electric cores of power battery pack, preparation method of buffering silica gel sheet and power battery pack comprising buffering silica gel sheet |
| CN112194901A (en) * | 2020-10-22 | 2021-01-08 | 西南大学 | Flexible foam material with energy-absorbing characteristic and preparation method thereof |
| CN113062033A (en) * | 2020-12-29 | 2021-07-02 | 张屹 | Preparation process of antibacterial wear-resistant cloth |
| CN113273735A (en) * | 2021-06-07 | 2021-08-20 | 惠州至精精密技术有限公司 | Production process of porous silica gel atomizing core |
| CN114874630A (en) * | 2022-05-25 | 2022-08-09 | 浙江恒业成有机硅有限公司 | High-rate platinum heat-vulcanized foamed silicone rubber and preparation method thereof |
| CN115948055A (en) * | 2022-12-23 | 2023-04-11 | 郑州圣莱特空心微珠新材料有限公司 | Low-density silicone rubber and preparation method thereof |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR100897899B1 (en) * | 2008-06-04 | 2009-05-18 | (주)화인 | Foam molding method of liquid silicone rubber |
| CN105907103A (en) * | 2016-06-23 | 2016-08-31 | 中国科学院化学研究所 | Silicone rubber foam material and preparation method thereof |
| CN106398256A (en) * | 2016-08-31 | 2017-02-15 | 西能化工科技(上海)有限公司 | Light paper material containing thermal expanding microspheres and preparation method thereof |
| CN106432897A (en) * | 2015-08-07 | 2017-02-22 | 现代自动车株式会社 | Foamable masterbatch and polyolefin resin composition with excellent expandability and direct metallizing property |
-
2017
- 2017-08-11 CN CN201710694110.6A patent/CN107446357A/en active Pending
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR100897899B1 (en) * | 2008-06-04 | 2009-05-18 | (주)화인 | Foam molding method of liquid silicone rubber |
| CN106432897A (en) * | 2015-08-07 | 2017-02-22 | 现代自动车株式会社 | Foamable masterbatch and polyolefin resin composition with excellent expandability and direct metallizing property |
| CN105907103A (en) * | 2016-06-23 | 2016-08-31 | 中国科学院化学研究所 | Silicone rubber foam material and preparation method thereof |
| CN106398256A (en) * | 2016-08-31 | 2017-02-15 | 西能化工科技(上海)有限公司 | Light paper material containing thermal expanding microspheres and preparation method thereof |
Non-Patent Citations (1)
| Title |
|---|
| 章炎敏: "热膨胀微球在聚乙烯发泡中的应用研究", 《中国优秀硕士学位论文全文数据库(电子期刊)工程科技I辑》 * |
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111207173A (en) * | 2020-01-09 | 2020-05-29 | 苏州赛伍应用技术股份有限公司 | Buffering silica gel sheet used between electric cores of power battery pack, preparation method of buffering silica gel sheet and power battery pack comprising buffering silica gel sheet |
| CN111207173B (en) * | 2020-01-09 | 2021-11-16 | 苏州赛伍应用技术股份有限公司 | Buffering silica gel sheet used between electric cores of power battery pack, preparation method of buffering silica gel sheet and power battery pack comprising buffering silica gel sheet |
| CN112194901A (en) * | 2020-10-22 | 2021-01-08 | 西南大学 | Flexible foam material with energy-absorbing characteristic and preparation method thereof |
| CN113062033A (en) * | 2020-12-29 | 2021-07-02 | 张屹 | Preparation process of antibacterial wear-resistant cloth |
| CN113273735A (en) * | 2021-06-07 | 2021-08-20 | 惠州至精精密技术有限公司 | Production process of porous silica gel atomizing core |
| CN114874630A (en) * | 2022-05-25 | 2022-08-09 | 浙江恒业成有机硅有限公司 | High-rate platinum heat-vulcanized foamed silicone rubber and preparation method thereof |
| CN114874630B (en) * | 2022-05-25 | 2023-08-11 | 浙江恒业成有机硅有限公司 | High-magnification platinum hot vulcanization foaming silicone rubber and preparation method thereof |
| CN115948055A (en) * | 2022-12-23 | 2023-04-11 | 郑州圣莱特空心微珠新材料有限公司 | Low-density silicone rubber and preparation method thereof |
| CN115948055B (en) * | 2022-12-23 | 2024-01-30 | 郑州圣莱特空心微珠新材料有限公司 | Low-density silicone rubber and preparation method thereof |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN107446357A (en) | A kind of low-density micropore diameter silicon rubber composite material and preparation method thereof | |
| Li et al. | Morphologies and electromagnetic interference shielding performances of microcellular epoxy/multi-wall carbon nanotube nanocomposite foams | |
| CN104312168B (en) | A kind of open cell type liquid RTV foam silicone rubber and preparation method thereof | |
| You et al. | Preparation and characterization of conductive carbon nanotube-polyurethane foam composites | |
| Jalalian et al. | Mechanically whipped phenolic froths as versatile templates for manufacturing phenolic and carbon foams | |
| CN104530712A (en) | Small pore diameter silicone rubber sponge and preparation method thereof | |
| CN107556753A (en) | A kind of micropore silicon rubber composite material of high temperature resistant environment-protective and preparation method thereof | |
| CN102634096B (en) | Polypropylene foaming masterbatch and production method thereof | |
| CN101250321A (en) | Preparation of Flexible Conductive Polyurethane Foam | |
| CN102010517A (en) | Method for preparing silicon rubber foam material by using supercritical carbon dioxide technology | |
| Ma et al. | The effect of surface chemistry of graphene on cellular structures and electrical properties of polycarbonate nanocomposite foams | |
| CN105623593B (en) | A kind of two-component encapsulating silica gel and preparation method thereof and encapsulating method | |
| CN114940829A (en) | Two-dimensional graphene/liquid metal/PDMS composite membrane and preparation method thereof | |
| CN108997666A (en) | A kind of polymer micro foamed material and preparation method thereof with structure of double peak holes | |
| Wang et al. | Polypropylene foaming using supercritical carbon dioxide: a review on fundamentals, technology, and applications | |
| Cipriani et al. | Direct ink writing of polyimide aerogels for battery thermal mitigation | |
| CN100425653C (en) | Preparation of low density(0.03-0.2g/cm3)conductive polyurethane foam material containing carbon nanometer tube | |
| CN114773684A (en) | A chemically cross-linked cellulose-based composite foam and its preparation method and application | |
| CN105086300A (en) | Light, conducting and shielding composite material and preparation method thereof | |
| CN111761751A (en) | Preparation method and application of carbon-containing polyolefin master batch | |
| Xiong et al. | Mechanical and flame‐resistance properties of polyurethane‐imide foams with different‐sized expandable graphite | |
| Zhou et al. | Study on the foaming behavior of density‐controllable epoxy resin composite foam under negative pressure environment | |
| Li et al. | Facile and green preparation of biobased graphene oxide/furan resin nanocomposites with enhanced thermal and mechanical properties | |
| Luo et al. | Modification of sodium bicarbonate and its effect on foaming behavior of polypropylene | |
| CN106496627B (en) | Negative pressure foaming method for preparing epoxy resin foam with air as foaming agent |
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 | ||
| RJ01 | Rejection of invention patent application after publication | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20171208 |