[go: up one dir, main page]

CN100357088C - Preparation method of roll-type silicone rubber film - Google Patents

Preparation method of roll-type silicone rubber film Download PDF

Info

Publication number
CN100357088C
CN100357088C CNB011234628A CN01123462A CN100357088C CN 100357088 C CN100357088 C CN 100357088C CN B011234628 A CNB011234628 A CN B011234628A CN 01123462 A CN01123462 A CN 01123462A CN 100357088 C CN100357088 C CN 100357088C
Authority
CN
China
Prior art keywords
silicone rubber
rubber film
roll
film
type silicone
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
CNB011234628A
Other languages
Chinese (zh)
Other versions
CN1398714A (en
Inventor
李文炫
吴敬堂
林宗仪
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.)
FORMOSAN RUBBER GROUP INCORPORATE
Original Assignee
FORMOSAN RUBBER GROUP INCORPORATE
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 FORMOSAN RUBBER GROUP INCORPORATE filed Critical FORMOSAN RUBBER GROUP INCORPORATE
Priority to CNB011234628A priority Critical patent/CN100357088C/en
Publication of CN1398714A publication Critical patent/CN1398714A/en
Application granted granted Critical
Publication of CN100357088C publication Critical patent/CN100357088C/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Images

Landscapes

  • Manufacture Of Macromolecular Shaped Articles (AREA)
  • Compositions Of Macromolecular Compounds (AREA)

Abstract

A process for preparing the coiled silicon rubber film includes such steps as pre-mixing the silicon rubber composition, calendering to obtain film, sulfurizing in enclosed sulfurizing unit, and sulfurizing in open heating unit. The hardness Shore A of the prepared continuous roll type silicone rubber film is between 20 and 60, and the thickness range is 0.1 to 3.0mm by adopting high-temperature vulcanization type silicone rubber resin. The heat-dissipating and heat-resisting heat-insulating material has excellent heat-dissipating performance, flexibility and soft adhesion, and can be used on devices and structures which are easy to generate high heat sources to provide heat-dissipating and heat-resisting effects; has the advantages of simple preparation method, high production efficiency and capability of manufacturing the silicon rubber film with uniform thickness and wide width.

Description

The method for making of silicon rubber film coil
Technical field
The invention relates to a kind of method for making of silicon rubber film coil, it provides the method for making of normal pressure rolling calendering, add sulphur type (HTV) silicon rubber to make continuous web-like high temperature, and the silicon rubber film of thickness homogeneous, it has the film of high and low heat conducting and radiating effect purposes, can make the silicon rubber film that fabric width is 160cm.
Background technology
Traditional processing mode of general silicone rubber products is divided into three kinds substantially: (one) is hot-forming, (two) injection molded mode reaches (three) hot-air and adds sulphur.Wherein making sheet film then carries out in the mode that hot-forming and hot-air add sulphur.Its major defect is: the speed of production of thermoforming way is slow, and can't produce continuously.
Summary of the invention
At the problems referred to above, the inventor is through developmental research chronically, create a kind of method for making of silicon rubber film coil of novelty, the silicon rubber film of thickness homogeneous and wide cut not only has good thermal diffusivity, flexibility and the soft silicon rubber film that attaches property again.
Main purpose of the present invention provides a kind of method for making of silicon rubber film coil, it mainly is to add sulphur and two sections open sulphur that add of normal pressure by one section airtight coating, the type continuously rolled silicon rubber film of wide cut of the thickness homogeneous of producing, can be used for high heating product heat radiation and heat-resisting is provided, utilize the property of raw material of silicon rubber film, thermal source is derived via itself conducting to fan, reach the purpose of the execution usefulness of stable prod use.
Second purpose of the present invention provides a kind of method for making of type continuously rolled silicon rubber film, the type continuously rolled silicon rubber film of its prepared wide cut, and can be used for the large tracts of land product must ask, and reaches amplification extensibility that improves product and the purpose that improves competitiveness of product.
The 3rd purpose of the present invention provides a kind of method for making of silicon rubber film coil, its prepared type continuously rolled silicon rubber is formed film, the silicon rubber film of different hardness, proportion, thickness and fabric width be can make, diversity that increases product and the purpose that improves carrying charge reached.
The 4th purpose of the present invention provides a kind of method for making of silicon rubber film coil, reaches the purpose that method for making is simple and easy and production efficiency is high.
The object of the present invention is achieved like this: a kind of method for making of silicon rubber film coil is characterized in that: it comprises the following step:
A, batching: the parts by weight ratio of each composition is in the rubber composition: 100 parts of silicone rubber resinas, bridging agent 0.25-5.0 part, filler 20-200 part, other additives and auxiliary agent 5-20 part; Its average molecular weight range of this silicone rubber resina is 20,000-50, and 000, Shore A hardness is at 20-60; This bridging agent is an organic peroxide; This filler is aluminium oxide, boron nitride, titanium oxide, precipitated calcium carbonate, silica (Silica), talcum powder, aluminium powder, silicon calcined earth, natural fiber, glass fibre or wetting agent; These other additives are silicone oil (Silicone Oil), zinc stearate, calcium stearate, zinc oxide or antimony oxide;
B, mixing: each feedstock composition is inserted in the adding pressure type mixing arrangement, fully stir mutually and mix, its mixture is dispersed in the mixing process;
C, film output: be that the silastic mixture that mixes through the adding pressure type mixing arrangement is delivered to coiled continuously at ordinary pressure formula film generation device, be wound to cylinder simultaneously in company with the guiding medium layer and add on the sulphur device, form continuous silicon rubber film;
D, once add sulphur and build bridge: be to be wound to cylinder simultaneously in company with the guiding medium layer and to add on the sulphur device described, form continuous silicon rubber film, send into the steam adding pressure type and add in the sulphur bl bridge layer heating and build bridge, add sulphur and finish the back cooling and together roll out in company with guiding medium layer;
E, secondary add the sulphur heating: it is to add the silicon rubber film that the heating of sulphur bl bridge layer is built bridge and produced through the steam adding pressure type, roll out in company with the guiding medium layer, and bring into simultaneously in the continuous open heater and heat, cooling after heating is finished, to guide medium layer and separate distinctly with silicon rubber film and roll out, promptly get type continuously rolled silicon rubber film.
The melting temperature of this mixing process is controlled at 60-150 ℃.The melting temperature of this mixing process is lower than the decomposition temperature of this bridging agent.The temperature of this mixing processing procedure is a normal temperature to 100 ℃, and the time is 5-60 minute, and pressure is 5-15kg/cm 2The operating temperature of this film output is a room temperature to 60 ℃.Each wheel speed ratio of this film output is 1: 1-1: 1.1.This once adds bridge formation temperature controlling that sulphur builds bridge and is controlled at 2-5kg/cm at 130-170 ℃, pressure 2And the time of staying is 2-4 hour.The heating and temperature control that this secondary adds sulphur heating 130-200 ℃ and heat time heating time at 30-60 minute.Comprise in this film output processing procedure a tubular coat around get device around getting the coating processing procedure, be will the guiding medium layer and the silicon rubber film that produced of type continuously rolled film generation device, add sulphur around getting on the seat around being taken to the tubular clad type simultaneously.Should comprise a guiding medium layer in the processing procedure around getting to coat, the silicon rubber film that the guiding medium layer of this silicon rubber film layering and type continuously rolled film generation device are produced coats around getting on the device around being taken to tubular simultaneously.This guiding medium layer is to be selected from one of them of fibre, paper products or rubber film.This film generation device is to include calender, pressure vessel or open baking oven.The fabric width degree of the final products of this production is below 160cm.This silicon rubber is to select high temperature bridge formation type silicon rubber for use, and its number average molecular weight is 300,000.It is to adopt continuous open baking oven heating that this secondary adds the sulphur processing procedure.This continuous open baking oven is to be selected from one of them of horizontal or vertical type baking oven.This filler is to be selected from one of them of heat conduction silicon rubber film that boron nitride or alumina material make.This filler is to be selected from fire proofing material to have heat conduction and the silicon rubber film of anti-the combustion as manufacturing.It is 1-5 around the quantity of getting seat that this clad type adds sulphur.It is cylindric or shaft-like one of them around the form of getting seat that this clad type adds sulphur.This clad type adds sulphur and includes and add sulphur degree and THICKNESS CONTROL program around getting seat, is to coat the whole sulphur that adds around getting seat with the synthetic rubber film, will not add the sulphur silicon rubber film in the complete closed space fully intensification add sulphur.This clad type adds sulphur around the confined space that the silicon rubber film of getting on the seat stores, and need feed organic gas and fill up whole space, and the silicon rubber film of Jia Qiaoing directly is not subjected to the organic gas effect, adds the influence that sulphur degree and thickness are avoided aqueous vapor to control it.This method makes the silicon rubber film that thickness is 0.2-3.0mm.This method makes the silicon rubber film that fabric width is 50-160cm.It is the silicon rubber film of 20-60 that this method makes Shore A hardness.This method makes the silicon rubber film that proportion is 1.0-2.0.This method makes the silicon rubber film that the coefficient of heat conduction is 0.4-3W/mk.It is to adopt hot blast to add sulphur formula baking oven that this secondary adds the sulphur section.This method is produced the silicon rubber film of different hot conduction degree.
Type continuously rolled silicon rubber film range of application of the present invention is quite extensive; be applicable to the various uses of heat conduction silicon rubber film; it comprises that plasma scope (PDP), computer cpu (CPU) and semiconductor (IC) chip panel etc. are easy to generate the electronic component or the structure of high temperature; heat radiation, heat-resisting, insulation and disconnected heat effect mainly are provided; the accurate electronic product inside of protection is operating in the execution, makes its overall performance avoid being subjected to high temperature and causes decay and occur unusual.
Method for making of the present invention is to add sulphur and the opening of two sections secondary normal pressures adds the sulphur mode with one section airtight coating, the type continuously rolled silicon rubber film of obtained thickness homogeneous, the high temperature that makes adds sulphur type silicon rubber film, have good thermal diffusivity, flexibility and soft attaching property, can use at the device that is easy to generate high thermal source and textural, the effect of heat radiation is provided; Method for making of the present invention is compared with general traditional method for making, and its method for making is simple and easy and production efficiency is high.
Describe in detail below in conjunction with preferred embodiment and accompanying drawing.
Description of drawings
Fig. 1 is a manufacturing process schematic diagram of the present invention.
The specific embodiment
Consult shown in Figure 1, heat conduction rubber composition of the present invention be contain silicon raw rubber (SiliconePolymer), add the sulphur agent (Crossling king Agent), filler (Filler) and additive (SpecialAdditives);
Silicon rubber is classified according to ASTM-D1418, can be divided into Dimethyl system, MQ-Methylvinyl system, VMQ-Methyl phenylvinyl system, PVMQ system and Fluoro Silicone system (FVMQ) according to its chemical constitution;
Silicon rubber is according to the processing conditions difference, can divide into room temperature and add sulphur type (Room-TemperatureVulcanizing, RTV), high temperature add the sulphur type (High-Temperature Vulcanizing, HTV) and liquid injection molding moulding (Liquid-injection molding, LIM) three kinds of patterns;
The average molecular weight range of silicone rubber resina is 20,000-50, and 000, hardness is at 20-60 Shore A;
Bridging agent is organic peroxide (Organic Peroxide), is divided into high temperature bridge formation type and low temperature bridge formation type organic peroxide;
Filler is aluminium oxide, boron nitride, titanium oxide, precipitated calcium carbonate, silica (Silica) (comprising dry type and wet type), talcum powder, aluminium powder, silicon calcined earth, natural fiber, glass fibre or wetting agent etc.;
Other additives are silicone oil (Silicone Oil), zinc stearate, calcium stearate, zinc oxide, antimony oxide etc.;
The parts by weight ratio of each composition is in the rubber composition: 100 parts of silicone rubber resinas, bridging agent 0.25-5.0 part, filler 20-200 part, other additives and auxiliary agent 5-20 part.
The present invention is a kind of calendering method for making of type continuously rolled silicon rubber film, and its manufacturing process is described below respectively:
Step 1: at first be batching, the parts by weight ratio of each composition is in the rubber composition: 100 parts of silicone rubber resinas, bridging agent 0.25-5.0 part, filler 20-200 part, other additives and auxiliary agent 5-20 part; Following mixingly 10, is that each feedstock composition is inserted in the adding pressure type mixing arrangement, fully mixes, and mixture is evenly disperseed, and in mixing process, melting temperature can not surpass the decomposition temperature of bridging agent, and melting temperature is controlled at 50-100 ℃;
Step 2: secondly form processing procedure 20 for film, will be through the mixed uniformly silastic mixture of adding pressure type mixing arrangement, delivering to coiled continuously at ordinary pressure formula film forming device rolls out continuously, and be wound to simultaneously on the centre position that the hollow cylinder shape adds the sulphur device with the guiding medium layer, operating temperature is a room temperature to 60 ℃, and each wheel speed ratio is 1: 1-1: 1.1;
Step 3: then for adding the wrapping processing procedure 30 of sulphur device, add on the sulphur device at the cylinder shape, cover last layer diameter adds the synthetic rubber film cover of sulphur device external diameter greater than the cylinder shape, and both-side opening is snarled sealing with rope, and the side that the hollow cylinder shape adds the sulphur device is provided with an air bleeding valve;
Step 4: for once adding sulphur bridge formation processing procedure 40, be to be wound to the hollow cylinder shape simultaneously in company with the guiding medium layer and to add continuous heat conduction silicon rubber film on the sulphur device with aforementioned, send into the steam adding pressure type and add heating bridge formation in the sulphur device, its bridge formation temperature is controlled at 120-170 ℃, and pressure is controlled at 3-10kg/cm 2, time of staying 2-4 hour, cooling after adding sulphur and finishing, and together roll out in company with the guiding medium layer;
Step 5: add sulphur heating processing 50 for secondary at last, to add the heat conduction silicon rubber film that the heating of sulphur bl bridge layer is built bridge through the steam adding pressure type, roll out in company with the guiding medium layer, and bring continuous open hot-air into and add in the sulphur device and heat, add the sulphur temperature and be controlled at 100-180 ℃, add the sulphur time to be controlled at 30-120 minute, cooling after adding sulphur and finishing, and will guide medium layer and heat conduction silicon rubber film and separate and roll out, promptly form type continuously rolled heat conduction silicon rubber film.
Embodiment 1
The method for making of type continuously rolled silicon rubber film, the parts by weight of the employed composition of present embodiment are 100 parts in silicon rubber, 0.35 part of peroxide, 3 parts of silicone oil, 150 parts in aluminium oxide, 2 parts of releasing agents.
Its processing conditions is with reference to shown in the subordinate list 1, and process comprises with kneading device mixing, and through film output device output, adds sulphur after add the airtight secondary that adds under sulphur and the normal pressure hot-air of sulphur device pressurization, makes the film goods of 2.0 millimeters of thickness; Measure its expansion ratio transitivity then respectively, as hardness, proportion, tensile strength, percentage elongation, tearing strength, the coefficient of heat conduction, its measurement result is as shown in subordinate list 2.
Above-mentioned rerum natura detects according to following method carries out:
(1-1) wooden Buddhist nun's viscosity: according to the ASTMD1646-61 standard testing.
(1-2) add the sulphur time: according to the ASTMD1646-61 standard testing.
(1-3) gross thickness: with the thickness instrumentation amount of precision 0.1 * 10mm.
(1-4) proportion: according to the JISK6350 standard testing.
(1-5) hardness: shore hardness Shore A is according to the JISK6301 standard testing.
(1-6) tensile strength: according to the ASTMD412 standard testing.
(1-7) percentage elongation: according to the ASTMD412 standard testing.
(1-8) tearing strength: according to the ASTMD624 standard testing.
(1-9) heat-conduction value: according to the ASTMD5470 standard testing.
Embodiment 2
Present embodiment 2 employed composition weight umbers are 100 parts in silicon rubber, 0.45 part of low temperature peroxide, 0.25 part of high temperature peroxide, 100 parts in aluminium oxide.
Its processing conditions is with reference to shown in the subordinate list 1, and process is for mixing with kneading device, and through film output device output, adds sulphur after add the airtight secondary that adds under sulphur and the normal pressure hot-air of sulphur device pressurization, makes thickness and be 1.8 millimeters film.
Embodiment 3
The parts by weight of present embodiment 3 employed compositions are 100 parts in silicon rubber, 0.25 part of peroxide, 10 parts of silicone oil, 100 parts of boron nitride.Its processing conditions is with reference to shown in the subordinate list 1, and process is for mixing with kneading device, and through film output device output, adds sulphur after add the airtight secondary that adds under sulphur and the normal pressure hot-air of sulphur device pressurization, makes thickness and be 1.2 millimeters film.
Embodiment 4-6
The employed composition of present embodiment 4-6 is 100 parts in a silicon rubber, 0.25 part of peroxide, 7 parts of silicone oil, 3 parts of removers.Shown in its processing conditions reference table 1, process is for mixing with kneading device, and,, make the film goods that thickness is respectively 1.6,0.8 and 0.2 millimeters after add that the pressurization of sulphur device is airtight to be added two under sulphur and the normal pressure hot-air and blow and add sulphur through film output device output.
The processing procedure of table 1 silicon rubber film and processing conditions
Embodiment 1 2 3 4 5 6
Add sulphur time T S2 (annotating 1) 0-15 1-30 0-21 0-21 0-21 0-21
Add sulphur time T C90 (annotating 2) 0-30 2-10 0-40 0-40 0-40 0-40
Melting temperature ℃ Room temperature Room temperature Room temperature Room temperature Room temperature Room temperature
Mixing time (min) 60 60 60 60 60 60
Unit temp ℃ 55 55 55 55 55 55
The device speed ratio 1∶1.1 1∶1.1 1∶1.1 1∶1.1 1∶1.1 1∶1.1
Add sulphur temperature ℃ 150 150 150 150 150 150
Add sulphur pressure kg/cm 2 3 4.5 4.5 4.5 4.5 4.5
Add the sulphur time (minute) 240 240 240 240 240 240
Secondary adds sulphur temperature ℃ 200 200 200 200 180 180
Secondary add the sulphur time (minute) 40 40 40 40 60 60
Annotate 1: add sulphur time T S2 (minute) definition: reach 2% of counter balance torque need time.
Annotate 2: add sulphur time K90 (minute) definition: reach 90% of counter balance torque need time.
The rerum natura of table 2 silicon rubber film
Embodiment 1 2 3 4 5 6
Thickness mm 2.0 1.8 1.2 1.6 0.8 0.2
Width cm 100 120 150 1 60 140 1 20
Proportion 1.83 1.50 1.10 1.10 1.20 1.20
Hardness ShoreA 30 37 10 27 25 28
Tensile strength kgf/cm 2 16.5 29.2 18.5 50 48 45
Percentage elongation % 3 50 380 430 490 430 350
Tearing strength kgf/cm 9.50 2.16 18 21 23 16.5
Heat-conduction value W/m-k 1.0 1.6 3.5 - - -
In sum, the invention relates to a kind of method for making of silicon rubber film coil, it can be made, and continuous web-like HTV type silicone rubber formulations is formed and the heat radiation film of thickness homogeneous, film with high and low heat conducting and radiating effect purposes, normal pressure rolling rolling process method for making of the present invention, can make the silicon rubber film that fabric width is 160cm, and film performance and thickness homogeneous, simple and easy, the advantage of high production efficiency of method for making had simultaneously.So the present invention has novelty, creativeness and practicality.
The above is preferred embodiment of the present invention only, is not to be used for limiting protection scope of the present invention, and all equalizations of doing according to shape of the present invention, structure, feature and spirit change and modify, and all should be included within protection scope of the present invention.

Claims (26)

1、一种卷式硅橡胶薄膜的制法,其特征是:它包含下列步骤:1, a kind of preparation method of roll-type silicone rubber film is characterized in that: it comprises the following steps: A、配料:硅橡胶组合物中各成分的重量份数比例为:硅橡胶树脂100份、架桥剂0.25-5.0份、填充剂20-200份、其他添加剂及助剂5-20份;该硅橡胶树脂其平均分子量范围在20,000-50,000,Shore A硬度在20-60;该架桥剂为有机过氧化物;该填充剂为氧化铝、氮化硼、氧化钛、轻质碳酸钙、二氧化硅、滑石粉、铝粉、硅煅烧土、天然纤维、玻璃纤维或湿润剂;该其他添加剂为硅油、硬脂酸锌、硬脂酸钙、氧化锌或氧化锑;A. Ingredients: The ratio of parts by weight of each component in the silicone rubber composition is: 100 parts of silicone rubber resin, 0.25-5.0 parts of bridging agent, 20-200 parts of filler, 5-20 parts of other additives and auxiliary agents; The average molecular weight range of silicone rubber resin is 20,000-50,000, and the Shore A hardness is 20-60; the bridging agent is an organic peroxide; the filler is aluminum oxide, boron nitride, titanium oxide, light calcium carbonate, Silicon oxide, talcum powder, aluminum powder, calcined silica, natural fiber, glass fiber or wetting agent; the other additive is silicone oil, zinc stearate, calcium stearate, zinc oxide or antimony oxide; B、混炼:将各原料组合物置入加压式混合装置中,充分搅拌互相混合,使其混合物均匀分散在混炼过程中;B. Mixing: Put each raw material composition into a pressurized mixing device, fully stir and mix with each other, so that the mixture is evenly dispersed in the mixing process; C、薄膜产出:是将经加压式混合装置混合的硅橡胶混合物送至常压连续卷式薄膜产生装置,随同导引媒介层同时卷绕至滚筒加硫装置上,形成连续的硅橡胶薄膜;C. Film output: the silicone rubber mixture mixed by the pressurized mixing device is sent to the normal pressure continuous roll film production device, and is wound on the drum vulcanizing device together with the guiding medium layer to form a continuous silicone rubber film; D、一次加硫架桥:是将所述随同导引媒介层同时卷绕至滚筒加硫装置上,形成连续的硅橡胶薄膜,送入蒸气加压式加硫架桥装置中加热架桥,加硫完成后冷却并随同导引媒介层一同卷出;该一次加硫架桥的架桥温度的控制在130-170℃、压力控制在2-5kg/cm2及停留时间为2-4小时;D. One-time vulcanization and bridging: the accompanying guide medium layer is wound onto the drum vulcanization device at the same time to form a continuous silicone rubber film, which is sent to the steam pressurized vulcanization and bridging device for heating and bridging. After the vulcanization is completed, cool and roll out together with the guide medium layer; the bridging temperature of this one-time vulcanization and bridging is controlled at 130-170°C, the pressure is controlled at 2-5kg/cm 2 and the residence time is 2-4 hours ; E、二次加硫加热:是将经蒸气加压式加硫架桥装置加热架桥所产生的硅橡胶薄膜,随同导引媒介层卷出,并同时带入连续开放式加热装置中加热,加热完成后冷却将导引媒介层与硅橡胶薄膜分离各别卷出,即得连续卷式硅橡胶薄膜;该二次加硫加热的加热温度控制在130-200℃及加热时间在30-60分钟。E. Secondary vulcanization heating: the silicon rubber film produced by heating and bridging with the steam pressurized vulcanizing bridging device is rolled out along with the guiding medium layer, and brought into the continuous open heating device for heating at the same time. After the heating is completed, cool down and separate the guide medium layer and the silicone rubber film and roll them out separately to obtain a continuous roll silicone rubber film; the heating temperature of the secondary vulcanization heating is controlled at 130-200°C and the heating time is 30-60°C minute. 2、根据权利要求1所述的卷式硅橡胶薄膜的制法,其特征是:该混炼过程的混炼温度控制在60-150℃。2. The roll-type silicone rubber film production method according to claim 1, characterized in that: the mixing temperature in the mixing process is controlled at 60-150°C. 3、根据权利要求1所述的卷式硅橡胶薄膜的制法,其特征是:该混炼过程的混炼温度低于该架桥剂的分解温度。3. The roll-type silicone rubber film production method according to claim 1, characterized in that: the mixing temperature in the mixing process is lower than the decomposition temperature of the bridging agent. 4、根据权利要求1所述的卷式硅橡胶薄膜的制法,其特征是:该混炼制程的温度为常温至100℃,时间为5-60分钟,压力为5-15kg/cm24. The roll-type silicone rubber film production method according to claim 1, characterized in that: the temperature of the mixing process is from room temperature to 100°C, the time is 5-60 minutes, and the pressure is 5-15kg/ cm2 . 5、根据权利要求1所述的卷式硅橡胶薄膜的制法,其特征是:该薄膜产出的操作温度为室温至60℃;5. The method for making a roll-type silicone rubber film according to claim 1, characterized in that: the operating temperature of the film output is from room temperature to 60°C; 6、根据权利要求1所述的卷式硅橡胶薄膜的制法,其特征是:该薄膜产出的各轮转速比为1∶1-1∶1.1。6. The roll-type silicone rubber film production method according to claim 1, characterized in that: the rotation speed ratio of each wheel for producing the film is 1:1-1:1.1. 7、根据权利要求1所述的卷式硅橡胶薄膜的制法,其特征是:该薄膜产出制程中包含一筒状包覆绕取装置的绕取包覆制程,其是将导引媒介层与连续卷式薄膜产生装置所产生的硅橡胶薄膜,同时绕取至筒状包覆式加硫绕取座上。7. The manufacturing method of roll-type silicon rubber film according to claim 1, characterized in that: the film production process includes a winding and wrapping process of a cylindrical wrapping and winding device, which is to guide the medium The silicon rubber film produced by the multi-layer and continuous roll-type film production device is simultaneously wound to the cylindrical wrapping vulcanization winding seat. 8、根据权利要求7所述的卷式硅橡胶薄膜的制法,其特征是:该绕取包覆制程中包含一导引媒介层,该硅橡胶薄膜分层的导引媒介层与连续卷式薄膜产生装置所产生的硅橡胶薄膜,同时绕取至筒状包覆绕取装置上。8. The roll-type silicon rubber film manufacturing method according to claim 7, characterized in that: the wrapping process includes a guiding medium layer, and the layered guiding medium layer of the silicone rubber film and the continuous roll The silicone rubber film produced by the type film generating device is simultaneously wound to the cylindrical coating winding device. 9、根据权利要求8所述的卷式硅橡胶薄膜的制法,其特征是:该导引媒介层是选自纤维制品、纸制品或橡胶薄膜的其中之一。9. The roll-type silicone rubber film manufacturing method according to claim 8, characterized in that: the guiding medium layer is selected from one of fiber products, paper products and rubber films. 10、根据权利要求1所述的卷式硅橡胶薄膜的制法,其特征是:该薄膜产生装置是包含有压延机、加硫罐或开放式烘箱。10. The roll-type silicone rubber film production method according to claim 1, characterized in that: the film producing device includes a calender, a vulcanizing tank or an open oven. 11、根据权利要求1所述的卷式硅橡胶薄膜的制法,其特征是:该硅橡胶是选用高温架桥型硅橡胶,其数量平均分子量为30万。11. The roll-type silicone rubber film production method according to claim 1, characterized in that: the silicone rubber is a high-temperature bridging type silicone rubber with a number average molecular weight of 300,000. 12、根据权利要求1所述的卷式硅橡胶薄膜的制法,其特征是:该二次加硫制程是采用连续开放式烘箱加热。12. The roll-type silicone rubber film manufacturing method according to claim 1, characterized in that: the secondary vulcanization process is heated in a continuous open oven. 13、根据权利要求12述的卷式硅橡胶薄膜的制法,其特征是:该连续开放式烘箱选自为水平式或直立式烘箱的其中之一。13. The roll-type silicone rubber film production method according to claim 12, characterized in that: the continuous open oven is selected from one of horizontal or vertical ovens. 14、根据权利要求1所述的卷式硅橡胶薄膜的制法,其特征是:该填充剂是选自氮化硼或氧化铝材料制造的热传导硅橡胶薄膜的其中之一。14. The roll-type silicone rubber film manufacturing method according to claim 1, characterized in that: the filler is one of the thermally conductive silicone rubber films made of boron nitride or aluminum oxide. 15、根据权利要求1所述的卷式硅橡胶薄膜的制法,其特征是:该填充剂是选自防火材料制造的具有热传导及耐燃硅橡胶薄膜。15. The roll-type silicone rubber film manufacturing method according to claim 1, characterized in that: the filler is selected from fireproof materials with heat conduction and flame-resistant silicone rubber films. 16、根据权利要求7所述的卷式硅橡胶薄膜的制法,其特征是:该包覆式加硫绕取座的数量为1-5个。16. The manufacturing method of roll-type silicone rubber film according to claim 7, characterized in that: the number of wrapping vulcanization and winding seats is 1-5. 17、根据权利要求7所述的卷式硅橡胶薄膜的制法,其特征是:该包覆式加硫绕取座的形态为圆筒状或杆状的其中之一。17. The manufacturing method of roll-type silicone rubber film according to claim 7, characterized in that: the shape of the wrapped vulcanized winding seat is one of cylindrical shape or rod shape. 18、根据权利要求7所述的卷式硅橡胶薄膜的制法,其特征是:该包覆式加硫绕取座包含有加硫度及厚度控制程序,是用合成橡胶薄膜包覆整个加硫绕取座,将未加硫硅橡胶薄膜于完全封闭空间中完全升温加硫。18. The roll-type silicone rubber film manufacturing method according to claim 7, characterized in that: the coated vulcanization winding seat includes a vulcanization degree and thickness control program, and the whole vulcanization film is covered with a synthetic rubber film. Sulfur is wound around the seat, and the unsulfurized silicone rubber film is completely heated and vulcanized in a completely enclosed space. 19、根据权利要求18述的卷式硅橡胶薄膜的制法,其特征是:该包覆式加硫绕取座上的硅橡胶薄膜储存的密闭空间,须要通入有机气体填满整个空间,未架桥的硅橡胶薄膜直接受到有机气体作用,以控制其加硫度及厚度免受水气的影响。19. The manufacturing method of roll-type silicone rubber film according to claim 18, characterized in that: the sealed space where the silicone rubber film is stored on the wrap-type vulcanized winding seat needs to be fed with organic gas to fill the entire space, The unbridged silicone rubber film is directly affected by organic gas to control its vulcanization degree and thickness from the influence of water vapor. 20、根据权利要求1所述的卷式硅橡胶薄膜的制法,其特征是:该方法制得厚度为0.2-3.0mm的硅橡胶薄膜。20. The method for making a roll-type silicone rubber film according to claim 1, characterized in that: the method produces a silicone rubber film with a thickness of 0.2-3.0 mm. 21、根据权利要求1所述的卷式硅橡胶薄膜的制法,其特征是:该方法制得幅宽为50-160cm的硅橡胶薄膜。21. The method for making a roll-type silicone rubber film according to claim 1, characterized in that: the method produces a silicone rubber film with a width of 50-160 cm. 22、根据权利要求1所述的卷式硅橡胶薄膜的制法,其特征是:该方法制得Shore A硬度为20-60的硅橡胶薄膜。22. The method for making a roll-type silicone rubber film according to claim 1, characterized in that: the method produces a silicone rubber film with a Shore A hardness of 20-60. 23、根据权利要求1所述的卷式硅橡胶薄膜的制法,其特征是:该方法制得比重为1.0-2.0的硅橡胶薄膜。23. The method for making a roll-type silicone rubber film according to claim 1, characterized in that: the method produces a silicone rubber film with a specific gravity of 1.0-2.0. 24、根据权利要求1所述的卷式硅橡胶薄膜的制法,其特征是:该方法制得热传导系数为0.4-3W/mk的硅橡胶薄膜。24. The method for making a roll-type silicone rubber film according to claim 1, characterized in that: the method produces a silicone rubber film with a thermal conductivity of 0.4-3W/mk. 25、根据权利要求1所述的卷式硅橡胶薄膜的制法,其特征是:该二次加硫段是采用热风加硫式烘箱。25. The roll-type silicone rubber film production method according to claim 1, characterized in that: the second vulcanization section is a hot air vulcanization oven. 26、根据权利要求1所述的卷式硅橡胶薄膜的制法,其特征是:该方法生产出不同热传导程度的硅橡胶薄膜。26. The method for making a roll-type silicone rubber film according to claim 1, characterized in that: the method produces silicone rubber films with different degrees of heat conduction.
CNB011234628A 2001-07-25 2001-07-25 Preparation method of roll-type silicone rubber film Expired - Fee Related CN100357088C (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CNB011234628A CN100357088C (en) 2001-07-25 2001-07-25 Preparation method of roll-type silicone rubber film

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CNB011234628A CN100357088C (en) 2001-07-25 2001-07-25 Preparation method of roll-type silicone rubber film

Publications (2)

Publication Number Publication Date
CN1398714A CN1398714A (en) 2003-02-26
CN100357088C true CN100357088C (en) 2007-12-26

Family

ID=4665074

Family Applications (1)

Application Number Title Priority Date Filing Date
CNB011234628A Expired - Fee Related CN100357088C (en) 2001-07-25 2001-07-25 Preparation method of roll-type silicone rubber film

Country Status (1)

Country Link
CN (1) CN100357088C (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8242181B2 (en) 2007-10-12 2012-08-14 Dow Corning Corporation Aluminum oxide dispersion and method of preparing same

Families Citing this family (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5227801B2 (en) 2006-10-31 2013-07-03 電気化学工業株式会社 Alumina powder, production method thereof, and use thereof
CN101274986B (en) * 2008-05-10 2010-10-13 江苏强盛化工有限公司 Method for using organic amine as organic peroxide sulfuration accessory ingredient
CN101274995B (en) * 2008-05-10 2011-02-02 江苏强盛化工有限公司 Composite sulfuration improver, preparation thereof and application thereof
CN101445623B (en) * 2008-12-26 2012-07-04 大连高科阻燃橡胶有限公司 Nonpoisonous flame-retardant rubber composition, preparation method therefor and product thereof
CN101973128B (en) * 2010-09-17 2012-12-12 苏州金禾新材料股份有限公司 Production process of spiral-wound silicon rubber membrane
CN102179979A (en) * 2011-03-09 2011-09-14 苏州金禾新材料股份有限公司 Roll type rubber polyester composite film and production process thereof
CN103350477B (en) * 2013-06-14 2015-05-06 苏州金禾新材料股份有限公司 Method for producing rolled silicone rubber film through unsupported calendering
CN104943287A (en) * 2015-07-02 2015-09-30 上海茂霖高分子科技股份有限公司 Heat-conduction silicone rubber sheet and production method thereof
CN106750702A (en) * 2016-12-01 2017-05-31 陕西日日新生物科技有限公司 A kind of preparation method of flame retardant plastics film

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4657965A (en) * 1984-10-22 1987-04-14 Toshiba Silicone Co., Ltd. Silicone elastomer composition
US5925709A (en) * 1996-08-29 1999-07-20 Shin-Etsu Chemical Co., Ltd. Method for the preparation of silicone rubber
CN1247815A (en) * 1998-09-16 2000-03-22 中国科学院金属研究所 Sandwiched damping board for chassis of bus

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4657965A (en) * 1984-10-22 1987-04-14 Toshiba Silicone Co., Ltd. Silicone elastomer composition
US5925709A (en) * 1996-08-29 1999-07-20 Shin-Etsu Chemical Co., Ltd. Method for the preparation of silicone rubber
CN1247815A (en) * 1998-09-16 2000-03-22 中国科学院金属研究所 Sandwiched damping board for chassis of bus

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8242181B2 (en) 2007-10-12 2012-08-14 Dow Corning Corporation Aluminum oxide dispersion and method of preparing same

Also Published As

Publication number Publication date
CN1398714A (en) 2003-02-26

Similar Documents

Publication Publication Date Title
CN100357088C (en) Preparation method of roll-type silicone rubber film
CN100494283C (en) Silica gel foam insulation pipe and preparation method thereof
CN104403075B (en) For electrothermal floor heating polyurethane thermal insulation board combined polyether and its application process
CN102993886A (en) Reflective insulating architectural paint for exterior wall and preparation method thereof
CN108192354A (en) A kind of thermally safe silica gel of dual temperature
CN103649430B (en) Covering material
CN102220003A (en) Composition for producing foamed silica gel plate and production method of foamed silica gel plate
CN1935912A (en) Nano ceramic high-temperature-resistant thermal-insulation coating, and its preparing method and use
CN104497688A (en) Aerogel thermal insulation coating and preparation method thereof
CN102070850A (en) Flame retardant expanded polystyrene particle and preparation method thereof
CN106220231A (en) Exterior wall fire-retardant polyphenyl insulation material and preparation method thereof
CN110256880A (en) A kind of anti-flaming dope for fire-proof doors and windows
CN108859282A (en) New-energy automobile lithium-ion-power cell refuses the plate and preparation method thereof of battery fluid and high temperature resistant heat insulation with dredging
KR101658774B1 (en) Fire resistance, water resistance preparation of the foam method and apparatus the water glass mixture
CN110591424B (en) A kind of preparation method of aluminum phosphate glue-based halogen-free high-expansion flame-retardant heat-insulating fire-retardant coating
CN110105766A (en) A kind of preparation process of silicon rubber glass fibre ceramic conduit
KR20200094949A (en) A flame-retardant coating composition, a structure having the same, and a preparing method thereof
CN102531528A (en) Magnesite fireproofing heat-insulation board
CN105965923A (en) Processing process for polytetrafluoroethylene steel wire composite pipe
CN109021785A (en) A kind of efficient solar heat protection heat-proof coating material and its manufacturing method
Zhang et al. High efficiency thermal insulation material based on boron hybrid silicone rubber and hollow microspheres
CN103965499B (en) The method that phenolic resin and polystyrene mixed foaming prepare high-flame retardant heat insulation
CN107746213A (en) A kind of froth inorganic stock for the protection of industrial storage tank fire disaster emergency and preparation method thereof
KR20040050827A (en) Method of producing a porous building materials by using pearlite
TW572942B (en) Method for producing rolled silicone rubber film

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
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: 20071226

Termination date: 20180725