WO2021114399A1 - Method for preparing tire curing bladder - Google Patents

Method for preparing tire curing bladder Download PDF

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WO2021114399A1
WO2021114399A1 PCT/CN2019/128108 CN2019128108W WO2021114399A1 WO 2021114399 A1 WO2021114399 A1 WO 2021114399A1 CN 2019128108 W CN2019128108 W CN 2019128108W WO 2021114399 A1 WO2021114399 A1 WO 2021114399A1
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parts
tire curing
curing bladder
bladder
vulcanization
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PCT/CN2019/128108
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French (fr)
Chinese (zh)
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赵会岩
赵海林
范屏
张学永
刘涛
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永一橡胶有限公司
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    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L23/00Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
    • C08L23/02Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers not modified by chemical after-treatment
    • C08L23/18Homopolymers or copolymers of hydrocarbons having four or more carbon atoms
    • C08L23/20Homopolymers or copolymers of hydrocarbons having four or more carbon atoms having four to nine carbon atoms
    • C08L23/22Copolymers of isobutene; Butyl rubber ; Homo- or copolymers of other iso-olefins
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J11/00Recovery or working-up of waste materials
    • C08J11/04Recovery or working-up of waste materials of polymers
    • C08J11/10Recovery or working-up of waste materials of polymers by chemically breaking down the molecular chains of polymers or breaking of crosslinks, e.g. devulcanisation
    • C08J11/18Recovery or working-up of waste materials of polymers by chemically breaking down the molecular chains of polymers or breaking of crosslinks, e.g. devulcanisation by treatment with organic material
    • C08J11/28Recovery or working-up of waste materials of polymers by chemically breaking down the molecular chains of polymers or breaking of crosslinks, e.g. devulcanisation by treatment with organic material by treatment with organic compounds containing nitrogen, sulfur or phosphorus
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2319/00Characterised by the use of rubbers not provided for in groups C08J2307/00 - C08J2317/00
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K3/00Use of inorganic substances as compounding ingredients
    • C08K3/18Oxygen-containing compounds, e.g. metal carbonyls
    • C08K3/20Oxides; Hydroxides
    • C08K3/22Oxides; Hydroxides of metals
    • C08K2003/2296Oxides; Hydroxides of metals of zinc
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2205/00Polymer mixtures characterised by other features
    • C08L2205/03Polymer mixtures characterised by other features containing three or more polymers in a blend
    • C08L2205/035Polymer mixtures characterised by other features containing three or more polymers in a blend containing four or more polymers in a blend
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2205/00Polymer mixtures characterised by other features
    • C08L2205/14Polymer mixtures characterised by other features containing polymeric additives characterised by shape
    • C08L2205/18Spheres
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2207/00Properties characterising the ingredient of the composition
    • C08L2207/20Recycled plastic
    • C08L2207/24Recycled plastic recycling of old tyres and caoutchouc and addition of caoutchouc particles
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies
    • Y02W30/62Plastics recycling; Rubber recycling

Definitions

  • the present invention relates to the technical field of preparation of tire curing bladder, in particular to a preparation method of tire curing bladder.
  • the tire vulcanizing bladder acts as an inner mold in the tire vulcanization molding and can transfer the heat required for tire vulcanization. It can expand and contract and is easy to install and disassemble before and after use. Therefore, the tire vulcanization bladder is used in the molding and vulcanization of pneumatic tires. widely.
  • the tire curing bladder can be used repeatedly 300-800 times. Because the tire curing bladder will repeatedly experience high temperature and high pressure during use, its various physical properties will decrease, especially after the number of uses reaches 700 to 800 times, the performance decline is serious and difficult to continue. use.
  • the tire curing bladder used in the production of tires is increasing every year, and the waste tire curing bladder needs to find a good way to deal with it.
  • the present invention provides a method for preparing a tire curing bladder.
  • the waste tire curing bladder is modified and applied in the processing of the tire curing bladder to solve the above technical problems.
  • the specific technical solution is a preparation method of tire curing bladder, the raw materials include: 80-100 parts of butyl rubber and 1-20 parts of modified waste tire curing bladder material, 20-50 parts of carbon black, 8 parts of vulcanized resin -10 parts, 5.5-7.5 parts of castor oil, 2-4 parts of zinc oxide, 1-3 parts of stearic acid, 3-5 parts of accelerator;
  • the general preparation method is as follows:
  • the waste tire curing bladder is crushed into granules.
  • the 50-200 mesh pellet size is 0.074-0.335mm, and the specific surface area is greatly increased.
  • the blending method can be used directly, and the waste tire curing bladder pellets can be mixed with The 2,2'-dibenzamidodiphenyl disulfide and the chlorine-containing modifier are fully contacted to complete the desulfurization and activation modification reaction.
  • 2,2'-dibenzamidodiphenyl disulfide is mainly used to desulfurize the waste tire curing bladder; the chlorine donor is used to modify the waste tire curing bladder pellets, and high content is selected.
  • Modifiers with chlorine content have a more obvious modification effect; for example, the modification effect of activated carbon with a chlorine content of 3.1-3.4mg/g increases with the increase of the chlorine content.
  • the waste tire curing bladder pellets and the chlorine-containing modifier are stirred and blended, the stirring speed is 300-600 r/min, and the blending time is 15-30 min.
  • the chlorine-containing modifier is one or more of chlorine-containing activated carbon, polyvinyl chloride, neoprene rubber, and chlorinated butyl rubber.
  • the initial temperature of banburying is 80°C
  • the debinding temperature is 130°C.
  • the mill roll temperature was 80°C.
  • the carbon black is N330
  • the accelerator is DM
  • the vulcanized resin is an alkylphenol formaldehyde resin.
  • the modified waste tire vulcanization bladder material is first blended with part of the butyl rubber. During a certain period of time, under the action of stirring, the temperature will rise, and the waste tire vulcanization bladder material will undergo a modification reaction. Part of the butyl rubber and modified waste tire vulcanization bladder materials are first banned to facilitate uniform dispersion, and then the remaining butyl rubber, carbon black, castor oil, zinc oxide, stearic acid, accelerators and other small materials are added to dense Refining, and finally adding vulcanized resin for mixing to prevent premature vulcanization.
  • the main component of the tire curing bladder is butyl rubber, which has a regular molecular chain structure and good air tightness after vulcanization.
  • the tire curing bladder will be scrapped once gas leakage occurs during use, and generally has not reached the recommended level.
  • the physical properties of the tire curing bladder that is destroyed and discarded in advance are better in the number of times of use; and the physical properties of the tire curing bladder that reaches or exceeds the number of use are severely reduced. If the waste tire curing bladder can be sorted and recycled according to the number of times of use, for the waste tire curing bladder that is used less frequently, the amount of chlorine-containing modifier can be reduced during modification, or the raw material can be appropriately increased.
  • the amount of waste tire vulcanization bladder material that has been subjected to sexual treatment, that is, the waste tire vulcanization bladder that has been used less frequently is more suitable for recycling and preparing new tire vulcanization bladder.
  • the waste tire curing bladder is modified and applied again in the tire curing bladder processing.
  • Practice shows that the newly produced tire curing bladder can be used up to 300-500 times.
  • Fig. 1 is a flow chart of a method for preparing a tire curing bladder according to a specific embodiment of the present invention.
  • S2 Mixing rubber with internal mixer.
  • the initial temperature of internal mixing is 80°C.
  • the butyl rubber is banned for 40 seconds, then 40 parts of N330, 6.5 parts of castor oil, 3 parts of zinc oxide, 2 parts of stearic acid, 4 parts of accelerator DM are added, and the banquet is for 1 minute.
  • S2 Mixing rubber with internal mixer.
  • the initial temperature of internal mixing is 80°C.
  • the butyl rubber is banned for 55 seconds, then 40 parts of N330, 6.5 parts of castor oil, 3 parts of zinc oxide, 2 parts of stearic acid, 5 parts of DM accelerating agent are added, and banburying is carried out for 2 minutes at a temperature of 130°C to discharge the rubber.

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  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Sustainable Development (AREA)
  • Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)
  • Moulds For Moulding Plastics Or The Like (AREA)

Abstract

The present invention discloses a method for preparing a tire curing bladder, and relates to the technical field of tire curing bladder preparation. In the method for preparing a tire curing bladder in the present invention, raw materials comprise: 80-100 parts of a butyl rubber, 1-20 parts of a modified waste tire curing bladder material, 20-50 parts of carbon black, 8-10 parts of a vulcanized resin, 5.5-7.5 parts of castor oil, 2-4 parts of zinc oxide, 1-3 parts of stearic acid, and 3-5 parts of an accelerator. The preparation method comprises firstly carrying out a blending desulfurization and blending activation two-step modification treatment on the waste tire curing bladder material, and then carrying out internal mixing, mixing, injection and vulcanization on the waste tire curing bladder material and butyl rubber, so as to produce a new tire curing bladder. Compared with the prior art, in the present invention, the waste tire curing bladder is subjected to a modification treatment and then is applied to tire curing bladder processing again, and practice shows that the number of uses of the newly-manufactured tire curing bladder can reach 300-500 times.

Description

一种轮胎硫化胶囊的制备方法Method for preparing tire curing bladder 技术领域Technical field
本发明涉及轮胎硫化胶囊制备技术领域,特别涉及一种轮胎硫化胶囊的制备方法。The present invention relates to the technical field of preparation of tire curing bladder, in particular to a preparation method of tire curing bladder.
背景技术Background technique
轮胎硫化胶囊在轮胎硫化成型中充当成型内模具并能够传递轮胎硫化所需的热量,其自身可以胀大、收缩,在使用前后易于安装和拆卸,因此,轮胎硫化胶囊在充气轮胎成型硫化中应用广泛。The tire vulcanizing bladder acts as an inner mold in the tire vulcanization molding and can transfer the heat required for tire vulcanization. It can expand and contract and is easy to install and disassemble before and after use. Therefore, the tire vulcanization bladder is used in the molding and vulcanization of pneumatic tires. widely.
目前,轮胎硫化胶囊可以重复使用300-800次,由于轮胎硫化胶囊在使用中会反复经历高温、高压,其各项物理性能会下降,尤其使用次数达到七八百次后,性能下降严重难以再利用。每年生产轮胎所使用的轮胎硫化胶囊是不断增长的,废弃轮胎硫化胶囊需要寻求处理的好方法。At present, the tire curing bladder can be used repeatedly 300-800 times. Because the tire curing bladder will repeatedly experience high temperature and high pressure during use, its various physical properties will decrease, especially after the number of uses reaches 700 to 800 times, the performance decline is serious and difficult to continue. use. The tire curing bladder used in the production of tires is increasing every year, and the waste tire curing bladder needs to find a good way to deal with it.
发明内容Summary of the invention
本发明提供一种轮胎硫化胶囊的制备方法,将废弃轮胎硫化胶囊进行改性处理,应用在轮胎硫化胶囊加工中,解决上述技术问题。The present invention provides a method for preparing a tire curing bladder. The waste tire curing bladder is modified and applied in the processing of the tire curing bladder to solve the above technical problems.
具体技术方案是,一种轮胎硫化胶囊的制备方法,原料包括:丁基橡胶80-100份和经过改性处理的废弃轮胎硫化胶囊料1-20份,炭黑20-50份,硫化树脂8-10份,蓖麻油5.5-7.5份,氧化锌2-4份,硬脂酸1-3份,促进剂3-5份;The specific technical solution is a preparation method of tire curing bladder, the raw materials include: 80-100 parts of butyl rubber and 1-20 parts of modified waste tire curing bladder material, 20-50 parts of carbon black, 8 parts of vulcanized resin -10 parts, 5.5-7.5 parts of castor oil, 2-4 parts of zinc oxide, 1-3 parts of stearic acid, 3-5 parts of accelerator;
大致制备方法过程如下:The general preparation method is as follows:
S1、废弃轮胎硫化胶囊的两步改性处理,先将废弃轮胎硫化胶囊进行清洗、干燥,再破碎成50-200目的粒料,接着加入2,2’-二苯甲酰氨基二苯基二硫化物0.3-0.8%进行共混脱硫,共混30分钟,停放8小时;然后加入12-15%的含氯改性剂进行共混活化,得到改性处理的废弃轮胎硫化胶囊料;所述的2,2’-二苯甲酰氨基二苯基二硫化物含量和含氯改性剂的含量是以废弃轮胎硫化胶囊重量为100%计算的;S1. Two-step modification treatment of the waste tire curing bladder. First, the waste tire curing bladder is cleaned, dried, and then crushed into 50-200 mesh pellets, and then 2,2'-dibenzamidodiphenyl bismuth is added. 0.3-0.8% of the sulfide is blended for desulfurization, blended for 30 minutes, and left for 8 hours; then 12-15% of a chlorine-containing modifier is added for blending activation to obtain a modified waste tire curing bladder material; The 2,2'-dibenzamidodiphenyl disulfide content and the content of the chlorine-containing modifier are calculated based on the weight of the waste tire curing bladder as 100%;
S2、密炼机炼胶,先向密炼机中加入一半的丁基橡胶、改性处理的废弃轮胎硫化胶囊料密炼2-4分钟,再加入另一半的丁基橡胶密炼30-60秒,然后加炭黑、蓖麻油、氧化锌、硬脂酸、促进剂密炼1-2分钟,排胶,得到密炼胶片;S2. Mix rubber in an internal mixer. First add half of the butyl rubber and modified waste tire vulcanization bladder to the internal mixer for banburying for 2-4 minutes, and then add the other half of the butyl rubber for banburying for 30-60 minutes. Seconds, then add carbon black, castor oil, zinc oxide, stearic acid, accelerant and banbury for 1-2 minutes, discharge the glue, and obtain a banbury film;
S3、将密炼胶片放入开炼机中,添加硫化树脂进行混炼、薄通打三角包,压出胶片,胶片自然冷却至室温;S3. Put the banbury film into an open mill, add vulcanized resin for mixing, thin through the triangle bag, press out the film, and cool the film naturally to room temperature;
S4、将S3中压出的胶片加入到注射硫化机的喂料口,注射机温度设为60-90℃,将胶料注射在模具内;S4. Add the film extruded in S3 to the feeding port of the injection vulcanizing machine, set the temperature of the injection machine to 60-90℃, and inject the rubber into the mold;
S5、设置硫化温度180-195℃,硫化时间在20-40min,硫化完成,顶出硫化胶囊。S5. Set the vulcanization temperature to 180-195℃, and the vulcanization time is 20-40min. After the vulcanization is completed, the vulcanization bladder is ejected.
由新的轮胎硫化胶囊经过使用成为废弃轮胎硫化胶囊,包括强度、弹性等物理性能会下降;回收利用这些废弃轮胎硫化胶囊时,需要对其进行改性处理,以增强其表面活性后,可以少量份加入到新的丁基橡胶中再利用。After the new tire curing bladder is used to become a waste tire curing bladder, physical properties such as strength and elasticity will be reduced; when recycling these waste tire curing bladders, they need to be modified to enhance their surface activity. Part is added to the new butyl rubber and reused.
将废弃轮胎硫化胶囊破碎成颗粒状,50-200目的粒料尺寸 0.074-0.335mm,比表面积大大增加,在改性处理时,可以直接采用共混的方式,废弃轮胎硫化胶囊粒料即可与2,2’-二苯甲酰氨基二苯基二硫化物以及含氯改性剂充分接触,完成脱硫和活化的改性反应。The waste tire curing bladder is crushed into granules. The 50-200 mesh pellet size is 0.074-0.335mm, and the specific surface area is greatly increased. In the modification treatment, the blending method can be used directly, and the waste tire curing bladder pellets can be mixed with The 2,2'-dibenzamidodiphenyl disulfide and the chlorine-containing modifier are fully contacted to complete the desulfurization and activation modification reaction.
其中,本发明中主要采用2,2’-二苯甲酰氨基二苯基二硫化物对废弃轮胎硫化胶囊进行塑解脱硫;氯给予体对废弃轮胎硫化胶囊粒料进行改性,选择高含氯量的改性剂,改性效果更明显;比如含氯量为3.1-3.4mg/g的活性炭改性效果随含氯量的增大而增强。Among them, in the present invention, 2,2'-dibenzamidodiphenyl disulfide is mainly used to desulfurize the waste tire curing bladder; the chlorine donor is used to modify the waste tire curing bladder pellets, and high content is selected. Modifiers with chlorine content have a more obvious modification effect; for example, the modification effect of activated carbon with a chlorine content of 3.1-3.4mg/g increases with the increase of the chlorine content.
进一步,S1中,废弃轮胎硫化胶囊粒料与含氯改性剂进行搅拌共混,搅拌转速为300-600r/min,共混时间为15-30min。Furthermore, in S1, the waste tire curing bladder pellets and the chlorine-containing modifier are stirred and blended, the stirring speed is 300-600 r/min, and the blending time is 15-30 min.
进一步,所述含氯改性剂是含氯活性炭、聚氯乙烯、氯丁胶、氯化丁基胶中的一种或几种。Further, the chlorine-containing modifier is one or more of chlorine-containing activated carbon, polyvinyl chloride, neoprene rubber, and chlorinated butyl rubber.
进一步,S2中,密炼起始温度为80℃,排胶温度为130℃。Furthermore, in S2, the initial temperature of banburying is 80°C, and the debinding temperature is 130°C.
进一步,S3中,开炼机辊温为80℃。Furthermore, in S3, the mill roll temperature was 80°C.
进一步,所述炭黑为N330,所述促进剂为DM,所述硫化树脂为烷基苯酚甲醛树脂。Further, the carbon black is N330, the accelerator is DM, and the vulcanized resin is an alkylphenol formaldehyde resin.
共混改性中,先将改性处理的废弃轮胎硫化胶囊料与部分丁基橡胶共混,一定时间中,在搅拌作用下,温度也会上升,废弃轮胎硫化胶囊料进行改性反应。将部分丁基橡胶与改性的废弃轮胎硫化胶囊料先进行密炼,利于分散均匀,再加入剩余的丁基橡胶及炭黑、蓖麻油、氧化锌、硬脂酸、促进剂等小料密炼,最后加入硫化树脂混炼,防止过早出现硫化现象。In blending modification, the modified waste tire vulcanization bladder material is first blended with part of the butyl rubber. During a certain period of time, under the action of stirring, the temperature will rise, and the waste tire vulcanization bladder material will undergo a modification reaction. Part of the butyl rubber and modified waste tire vulcanization bladder materials are first banned to facilitate uniform dispersion, and then the remaining butyl rubber, carbon black, castor oil, zinc oxide, stearic acid, accelerators and other small materials are added to dense Refining, and finally adding vulcanized resin for mixing to prevent premature vulcanization.
另外,轮胎硫化胶囊的主要成分以丁基橡胶为主,丁基橡胶分子链结构规整,硫化后气密性好,而轮胎硫化胶囊在使用中一旦发生气体泄漏就会报废,一般尚未达到建议的使用次数,这种提前破坏报废的轮胎硫化胶囊各项物理性能较好;而达到甚至超过使用次数的轮胎硫化胶囊,其各项物理性能下降严重。如果废弃的轮胎硫化胶囊能够根据使用次数进行分类回收,那么对于使用次数较少的废弃的轮胎硫化胶囊,可以在改性时减少含氯改性剂的添加量,也可以在原料中适当增加改性处理的废弃轮胎硫化胶囊料的添加量,也就是说,使用次数较少的废弃的轮胎硫化胶囊更加适于回收再制备新的轮胎硫化胶囊。In addition, the main component of the tire curing bladder is butyl rubber, which has a regular molecular chain structure and good air tightness after vulcanization. The tire curing bladder will be scrapped once gas leakage occurs during use, and generally has not reached the recommended level. The physical properties of the tire curing bladder that is destroyed and discarded in advance are better in the number of times of use; and the physical properties of the tire curing bladder that reaches or exceeds the number of use are severely reduced. If the waste tire curing bladder can be sorted and recycled according to the number of times of use, for the waste tire curing bladder that is used less frequently, the amount of chlorine-containing modifier can be reduced during modification, or the raw material can be appropriately increased. The amount of waste tire vulcanization bladder material that has been subjected to sexual treatment, that is, the waste tire vulcanization bladder that has been used less frequently is more suitable for recycling and preparing new tire vulcanization bladder.
与现有技术相比,本发明中,将废弃轮胎硫化胶囊进行改性处理,再次应用于轮胎硫化胶囊加工中,实践表明,新制作的轮胎硫化胶囊使用次数可达300-500次。Compared with the prior art, in the present invention, the waste tire curing bladder is modified and applied again in the tire curing bladder processing. Practice shows that the newly produced tire curing bladder can be used up to 300-500 times.
附图说明Description of the drawings
图1为本发明中具体实施方式的一种轮胎硫化胶囊的制备方法流程图。Fig. 1 is a flow chart of a method for preparing a tire curing bladder according to a specific embodiment of the present invention.
具体实施方式Detailed ways
下面结合附图及实施例描述本发明具体实施方式:The specific implementation of the present invention will be described below with reference to the drawings and embodiments:
需要说明的是,本说明书所附图中示意的结构、比例、大小等,均仅用以配合说明书所揭示的内容,以供熟悉此技术的人士了解与阅读,并非用以限定本发明可实施的限定条件,任何结构的修饰、比例关系的,改变或大小的调整,在不影响本发明所能产生的功效及所能达成的目的下,均应落在本发明所揭示的技术内容能涵盖的范围内。It should be noted that the structure, ratio, size, etc. shown in the drawings attached to this specification are only used to match the content disclosed in the specification for the understanding and reading of those familiar with this technology, and are not intended to limit the implementation of the present invention. The limiting conditions, any structural modification, proportional relationship, change or size adjustment, shall fall within the scope of the technical content disclosed in the present invention without affecting the effects and objectives that can be achieved by the present invention In the range.
同时,本说明书中所引用的如“上”、“下”、“左”、“右”、“中间”及“一”等的用语,亦仅为便于叙述的明了,而非用以限定本发明可实施的范围,其相对关系的改变或调整,在无实质变更技术内容下,当亦视为本发明可实施的范畴。At the same time, the terms such as "upper", "lower", "left", "right", "middle" and "one" cited in this specification are only for ease of description, not to limit the text. The scope of implementation of the invention, the change or adjustment of its relative relationship, shall be regarded as the scope of implementation of the invention without substantial changes to the technical content.
实施例1:Example 1:
轮胎硫化胶囊的制备,过程如下:The process of preparing tire curing bladder is as follows:
S1、废弃轮胎硫化胶囊的改性,先将废弃轮胎硫化胶囊进行清洗、干燥,再破碎成200目的粒料,接着加入2,2’-二苯甲酰氨基二苯基二硫化物0.3%(重量份,以废弃轮胎硫化胶囊重量为100%计算)进行共混脱硫,共混30分钟,停放8小时;然后加入15%(重量份,以废弃轮胎硫化胶囊重量为100%计算)的含氯量为3.1mg/g的含氯活性炭进行共混,搅拌转速为300r/min,共混时间为30min,得到改性处理的废弃轮胎硫化胶囊料;S1. Modification of the vulcanization bladder of waste tires. The vulcanization bladder of waste tires is first washed, dried, and then crushed into 200 mesh pellets, and then 2,2'-dibenzamidodiphenyl disulfide 0.3% ( Parts by weight, calculated based on the weight of the waste tire curing bladder as 100%) for blending and desulfurization, blending for 30 minutes, and parked for 8 hours; then adding 15% (parts by weight, calculated based on the weight of the waste tire curing bladder as 100%) of chlorine Blending with chlorine-containing activated carbon with an amount of 3.1mg/g, stirring speed of 300r/min, and blending time of 30min, to obtain modified waste tire curing bladder material;
S2、密炼机炼胶,密炼起始温度为80℃,先向密炼机中加入50份丁基橡胶、1份改性处理的废弃轮胎硫化胶囊料密炼2分钟,再加入50份丁基橡胶密炼30秒,然后加50份N330、5.5份蓖麻油、2份氧化锌、1份硬脂酸、3份促进剂DM,密炼2分钟,温度为130℃排胶,得到密炼胶片;S2. Mix rubber with internal mixer. The initial temperature of banbury is 80℃. First add 50 parts of butyl rubber and 1 part of modified waste tire vulcanization bladder material to the internal mixer for banburying for 2 minutes, and then add 50 parts The butyl rubber is banned for 30 seconds, and then 50 parts of N330, 5.5 parts of castor oil, 2 parts of zinc oxide, 1 part of stearic acid, 3 parts of accelerator DM are added, banburying is carried out for 2 minutes, and the temperature is 130°C for discharging. Refining film
S3、将密炼胶片放入开炼机中,开炼机辊温为80℃,添加8份烷基苯酚甲醛树脂进行混炼、薄通打三角包,压出胶片,胶片自然冷却至室温;S3. Put the banbury film into an open mill, the roller temperature of the open mill is 80℃, add 8 parts of alkylphenol formaldehyde resin for mixing, thin through the triangle bag, press out the film, and cool the film naturally to room temperature;
S4、将S3中压出的胶片加入到注射硫化机的喂料口,注射机温 度设为70℃,将胶料注射在模具内;S4. Add the film extruded in S3 to the feeding port of the injection vulcanizing machine, set the temperature of the injection machine to 70℃, and inject the rubber into the mold;
S5、设置硫化温度180℃,硫化时间在32min,硫化完成,顶出硫化胶囊。S5. Set the vulcanization temperature to 180°C, and the vulcanization time is 32min. After the vulcanization is completed, the vulcanization bladder is ejected.
实施例2:Example 2:
轮胎硫化胶囊的制备,过程如下:The process of preparing tire curing bladder is as follows:
S1、废弃轮胎硫化胶囊的改性,先将废弃轮胎硫化胶囊进行清洗、干燥,再破碎成50-200目的粒料,接着加入2,2’-二苯甲酰氨基二苯基二硫化物0.8%(重量份,以废弃轮胎硫化胶囊重量为100%计算)进行共混脱硫,共混30分钟,停放8小时;然后加入12%(重量份,以废弃轮胎硫化胶囊重量为100%计算)的含氯量为3.4mg/g的含氯活性炭进行共混,搅拌转速为600r/min,共混时间为18min,得到改性处理的废弃轮胎硫化胶囊料;S1. Modification of the vulcanization bladder of waste tires. The vulcanization bladder of waste tires is cleaned and dried first, and then crushed into 50-200 mesh pellets, and then 2,2'-dibenzamidodiphenyl disulfide 0.8 is added. % (Parts by weight, calculated based on the weight of the waste tire curing bladder as 100%) for blending and desulfurization, blending for 30 minutes, parked for 8 hours; then adding 12% (parts by weight, calculated based on the weight of the waste tire curing bladder as 100%) Blending of chlorine-containing activated carbon with a chlorine content of 3.4 mg/g, a stirring speed of 600 r/min, and a blending time of 18 minutes, to obtain modified waste tire curing bladder materials;
S2、密炼机炼胶,密炼起始温度为80℃,先向密炼机中加入50份丁基橡胶、10份改性处理的废弃轮胎硫化胶囊料密炼3分钟,再加入50份丁基橡胶密炼40秒,然后加40份N330、6.5份蓖麻油、3份氧化锌、2份硬脂酸、4份促进剂DM,密炼1分钟,温度为130℃排胶,得到密炼胶片;S2: Mixing rubber with internal mixer. The initial temperature of internal mixing is 80℃. First add 50 parts of butyl rubber and 10 parts of modified waste tire vulcanization bladder material to the internal mixer for 3 minutes, and then add 50 parts. The butyl rubber is banned for 40 seconds, then 40 parts of N330, 6.5 parts of castor oil, 3 parts of zinc oxide, 2 parts of stearic acid, 4 parts of accelerator DM are added, and the banquet is for 1 minute. Refining film
S3、将密炼胶片放入开炼机中,开炼机辊温为80℃,添加9份烷基苯酚甲醛树脂进行混炼、薄通打三角包,压出胶片,胶片自然冷却至室温;S3. Put the banbury film into an open mill, the roller temperature of the open mill is 80℃, add 9 parts of alkylphenol formaldehyde resin for mixing, thin through the triangle bag, press out the film, and cool the film naturally to room temperature;
S4、将S3中压出的胶片加入到注射硫化机的喂料口,注射机温度设为75℃,将胶料注射在模具内;S4. Add the film pressed out in S3 to the feeding port of the injection vulcanizing machine, set the temperature of the injection machine to 75°C, and inject the rubber material into the mold;
S5、设置硫化温度185℃,硫化时间在36min,硫化完成,顶出硫化胶囊。S5. Set the vulcanization temperature to 185°C, the vulcanization time is 36min, the vulcanization is completed, and the vulcanization bladder is ejected.
实施例3:Example 3:
轮胎硫化胶囊的制备,过程如下:The process of preparing tire curing bladder is as follows:
S1、废弃轮胎硫化胶囊的改性,先将废弃轮胎硫化胶囊进行清洗、干燥,再破碎成50-200目的粒料,接着加入2,2’-二苯甲酰氨基二苯基二硫化物0.5%(重量份,以废弃轮胎硫化胶囊重量为100%计算)进行共混脱硫,共混30分钟,停放8小时;然后加入15%(重量份,以废弃轮胎硫化胶囊重量为100%计算)的含氯量为3.3mg/g的含氯活性炭与聚氯乙烯进行共混,含氯活性炭与聚氯乙烯质量份比是1:1,搅拌转速为400r/min,共混时间为20min,得到改性处理的废弃轮胎硫化胶囊料;S1. Modification of the vulcanization bladder of waste tires. The vulcanization bladder of waste tires is cleaned and dried first, and then crushed into pellets of 50-200 mesh, and then 2,2'-dibenzamidodiphenyl disulfide 0.5 is added. % (Parts by weight, calculated based on the weight of the waste tire curing bladder as 100%) for blending and desulfurization, blending for 30 minutes, and parked for 8 hours; then adding 15% (parts by weight, calculated based on the weight of the waste tire curing bladder as 100%) The chlorine-containing activated carbon with a chlorine content of 3.3 mg/g is blended with polyvinyl chloride, the mass ratio of the chlorine-containing activated carbon to the polyvinyl chloride is 1:1, the stirring speed is 400r/min, and the blending time is 20min. Vulcanization bladder material for waste tires that have been treated sexually;
S2、密炼机炼胶,密炼起始温度为80℃,先向密炼机中加入40份丁基橡胶、20份改性处理的废弃轮胎硫化胶囊料密炼4分钟,再加入40份丁基橡胶密炼60秒,然后加20份N330、7.5份蓖麻油、4份氧化锌、3份硬脂酸、5份促进剂DM,密炼1分钟,温度为130℃排胶,得到密炼胶片;S2. Mixing rubber with internal mixer. The initial temperature of mixing is 80℃. First add 40 parts of butyl rubber and 20 parts of modified waste tire vulcanization bladder material to the internal mixer for 4 minutes, and then add 40 parts. The butyl rubber is banned for 60 seconds, then add 20 parts of N330, 7.5 parts of castor oil, 4 parts of zinc oxide, 3 parts of stearic acid, 5 parts of accelerator DM. Refining film
S3、将密炼胶片放入开炼机中,开炼机辊温为80℃,添加10份烷基苯酚甲醛树脂进行混炼、薄通打三角包,压出胶片,胶片自然冷却至室温;S3. Put the banbury film into an open mill, the roller temperature of the open mill is 80°C, add 10 parts of alkylphenol formaldehyde resin for mixing, thin through the triangle bag, press out the film, and cool the film naturally to room temperature;
S4、将S3中压出的胶片加入到注射硫化机的喂料口,注射机温度设为90℃,将胶料注射在模具内;S4. Add the film extruded in S3 to the feeding port of the injection vulcanizing machine, set the temperature of the injection machine to 90°C, and inject the rubber material into the mold;
S5、设置硫化温度195℃,硫化时间在20min,硫化完成,顶出硫化胶囊。S5. Set the vulcanization temperature to 195℃, and the vulcanization time is 20min. After the vulcanization is completed, the vulcanization bladder is ejected.
实施例4:Example 4:
轮胎硫化胶囊的制备,过程如下:The process of preparing tire curing bladder is as follows:
S1、废弃轮胎硫化胶囊的改性,先将废弃轮胎硫化胶囊进行清洗、干燥,再破碎成50-200目的粒料,接着加入2,2’-二苯甲酰氨基二苯基二硫化物0.4%(重量份,以废弃轮胎硫化胶囊重量为100%计算)进行共混脱硫,共混30分钟,停放8小时;然后加入13%(重量份,以废弃轮胎硫化胶囊重量为100%计算)的聚氯乙烯进行共混,搅拌转速为500r/min,共混时间为15min,得到改性处理的废弃轮胎硫化胶囊料;S1. Modification of the vulcanization bladder of waste tires. The vulcanization bladder of waste tires is cleaned and dried first, and then crushed into 50-200 mesh pellets, and then 2,2'-dibenzamidodiphenyl disulfide 0.4 is added. % (Parts by weight, calculated based on the weight of the waste tire curing bladder as 100%) for blending and desulfurization, blending for 30 minutes, parked for 8 hours; then adding 13% (parts by weight, calculated based on the weight of the waste tire curing bladder as 100%) The polyvinyl chloride is blended, the stirring speed is 500r/min, and the blending time is 15min, to obtain the modified waste tire curing bladder material;
S2、密炼机炼胶,密炼起始温度为80℃,先向密炼机中加入45份丁基橡胶、10份改性处理的废弃轮胎硫化胶囊料密炼2分钟,再加入45份丁基橡胶密炼60秒,然后加30份N330、6.5份蓖麻油、2份氧化锌、2份硬脂酸、4份促进剂DM,密炼2分钟,温度为130℃排胶,得到密炼胶片;S2. Mixing rubber with internal mixer. The initial temperature of mixing is 80℃. First, add 45 parts of butyl rubber and 10 parts of modified waste tire vulcanization bladder material to the internal mixer for banburying for 2 minutes, and then add 45 parts. The butyl rubber is banned for 60 seconds, then 30 parts of N330, 6.5 parts of castor oil, 2 parts of zinc oxide, 2 parts of stearic acid, 4 parts of accelerator DM are added. Refining film
S3、将密炼胶片放入开炼机中,开炼机辊温为80℃,添加8份烷基苯酚甲醛树脂进行混炼、薄通打三角包,压出胶片,胶片自然冷却至室温;S3. Put the banbury film into an open mill, the roller temperature of the open mill is 80℃, add 8 parts of alkylphenol formaldehyde resin for mixing, thin through the triangle bag, press out the film, and cool the film naturally to room temperature;
S4、将S3中压出的胶片加入到注射硫化机的喂料口,注射机温度设为80℃,将胶料注射在模具内;S4. Add the film extruded in S3 to the feeding port of the injection vulcanizing machine, set the temperature of the injection machine to 80°C, and inject the rubber material into the mold;
S5、设置硫化温度190℃,硫化时间在35min,硫化完成,顶出 硫化胶囊。S5. Set the vulcanization temperature to 190℃, and the vulcanization time is 35min. After the vulcanization is completed, the vulcanization bladder is ejected.
实施例5:Example 5:
轮胎硫化胶囊的制备,过程如下:The process of preparing tire curing bladder is as follows:
S1、废弃轮胎硫化胶囊的改性,先将废弃轮胎硫化胶囊进行清洗、干燥,再破碎成50-200目的粒料,接着加入2,2’-二苯甲酰氨基二苯基二硫化物0.6%(重量份,以废弃轮胎硫化胶囊重量为100%计算)进行共混脱硫,共混30分钟,停放8小时;然后加入14%(重量份,以废弃轮胎硫化胶囊重量为100%计算)的氯丁胶进行共混,搅拌转速为350r/min,共混时间为25min,得到改性处理的废弃轮胎硫化胶囊料;S1. Modification of the vulcanization bladder of waste tires. The vulcanization bladder of waste tires is cleaned and dried first, and then crushed into 50-200 mesh pellets, and then 2,2'-dibenzamidodiphenyl disulfide 0.6 is added. % (Parts by weight, calculated based on the weight of the waste tire curing bladder as 100%) for blending and desulfurization, blending for 30 minutes, parked for 8 hours; then adding 14% (parts by weight, calculated based on the weight of the waste tire curing bladder as 100%) The neoprene rubber is blended, the stirring speed is 350r/min, the blending time is 25min, and the modified waste tire curing bladder material is obtained;
S2、密炼机炼胶,密炼起始温度为80℃,先向密炼机中加入50份丁基橡胶、20份改性处理的废弃轮胎硫化胶囊料密炼4分钟,再加入50份丁基橡胶密炼30秒,然后加40份N330、7.5份蓖麻油、3份氧化锌、2份硬脂酸、3份促进剂DM,密炼2分钟,温度为130℃排胶,得到密炼胶片;S2. Mixing rubber with internal mixer. The initial temperature of mixing is 80℃. First add 50 parts of butyl rubber and 20 parts of modified waste tire vulcanization bladder material to the internal mixer for 4 minutes, and then add 50 parts. The butyl rubber is banned for 30 seconds, then 40 parts of N330, 7.5 parts of castor oil, 3 parts of zinc oxide, 2 parts of stearic acid, 3 parts of accelerator DM are added. Refining film
S3、将密炼胶片放入开炼机中,开炼机辊温为80℃,添加9份烷基苯酚甲醛树脂进行混炼、薄通打三角包,压出胶片,胶片自然冷却至室温;S3. Put the banbury film into an open mill, the roller temperature of the open mill is 80℃, add 9 parts of alkylphenol formaldehyde resin for mixing, thin through the triangle bag, press out the film, and cool the film naturally to room temperature;
S4、将S3中压出的胶片加入到注射硫化机的喂料口,注射机温度设为85℃,将胶料注射在模具内;S4. Add the film pressed out in S3 to the feeding port of the injection vulcanizing machine, set the temperature of the injection machine to 85°C, and inject the rubber material into the mold;
S5、设置硫化温度185℃,硫化时间在40min,硫化完成,顶出硫化胶囊。S5. Set the vulcanization temperature to 185°C, and the vulcanization time is 40min. After the vulcanization is completed, the vulcanization bladder is ejected.
实施例6:Example 6:
轮胎硫化胶囊的制备,过程如下:The process of preparing tire curing bladder is as follows:
S1、废弃轮胎硫化胶囊的改性,先将废弃轮胎硫化胶囊进行清洗、干燥,再破碎成50-200目的粒料,接着加入2,2’-二苯甲酰氨基二苯基二硫化物0.7%(重量份,以废弃轮胎硫化胶囊重量为100%计算)进行共混脱硫,共混30分钟,停放8小时;然后加入15%(重量份,以废弃轮胎硫化胶囊重量为100%计算)的氯化丁基胶进行共混,搅拌转速为450r/min,共混时间为30min,得到改性处理的废弃轮胎硫化胶囊料;S1. Modification of the vulcanization bladder of waste tires. The vulcanization bladder of waste tires is cleaned and dried first, and then crushed into 50-200 mesh pellets, and then 2,2'-dibenzamidodiphenyl disulfide 0.7 is added. % (Parts by weight, calculated based on the weight of the waste tire curing bladder as 100%) for blending and desulfurization, blending for 30 minutes, and parked for 8 hours; then adding 15% (parts by weight, calculated based on the weight of the waste tire curing bladder as 100%) The chlorinated butyl rubber is blended, the stirring speed is 450r/min, and the blending time is 30min, to obtain the modified waste tire curing bladder material;
S2、密炼机炼胶,密炼起始温度为80℃,先向密炼机中加入45份丁基橡胶、20份改性处理的废弃轮胎硫化胶囊料密炼4分钟,再加入45份丁基橡胶密炼45秒,然后加30份N330、6.5份蓖麻油、4份氧化锌、3份硬脂酸、4份促进剂DM,密炼2分钟,温度为130℃排胶,得到密炼胶片;S2. Mix rubber in an internal mixer. The initial temperature of banbury is 80℃. First, add 45 parts of butyl rubber and 20 parts of modified waste tire vulcanization bladder material to the internal mixer for 4 minutes, and then add 45 parts. The butyl rubber is banned for 45 seconds, and then 30 parts of N330, 6.5 parts of castor oil, 4 parts of zinc oxide, 3 parts of stearic acid, 4 parts of accelerator DM are added, banburying is carried out for 2 minutes, and the temperature is 130°C for discharging. Refining film
S3、将密炼胶片放入开炼机中,开炼机辊温为80℃,添加10份烷基苯酚甲醛树脂进行混炼、薄通打三角包,压出胶片,胶片自然冷却至室温;S3. Put the banbury film into an open mill, the roller temperature of the open mill is 80°C, add 10 parts of alkylphenol formaldehyde resin for mixing, thin through the triangle bag, press out the film, and cool the film naturally to room temperature;
S4、将S3中压出的胶片加入到注射硫化机的喂料口,注射机温度设为80℃,将胶料注射在模具内;S4. Add the film extruded in S3 to the feeding port of the injection vulcanizing machine, set the temperature of the injection machine to 80°C, and inject the rubber material into the mold;
S5、设置硫化温度185℃,硫化时间在35min,硫化完成,顶出硫化胶囊。S5. Set the vulcanization temperature to 185°C, the vulcanization time is 35min, the vulcanization is completed, and the vulcanization bladder is ejected.
实施例7:Example 7:
轮胎硫化胶囊的制备,过程如下:The process of preparing tire curing bladder is as follows:
S1、废弃轮胎硫化胶囊的改性,先将废弃轮胎硫化胶囊进行清洗、干燥,再破碎成50-200目的粒料,接着加入2,2’-二苯甲酰氨基二苯基二硫化物0.3%(重量份,以废弃轮胎硫化胶囊重量为100%计算)进行共混脱硫,共混30分钟,停放8小时;然后加入15%(重量份,以废弃轮胎硫化胶囊重量为100%计算)的聚氯乙烯、氯丁胶、氯化丁基胶进行共混,聚氯乙烯、氯丁胶、氯化丁基胶质量份比为1:1:1;搅拌转速为550r/min,共混时间为27min,得到改性处理的废弃轮胎硫化胶囊料;S1. Modification of the vulcanization bladder of waste tires. The vulcanization bladder of waste tires is cleaned, dried, and then broken into 50-200 mesh pellets, and then 2,2'-dibenzamidodiphenyl disulfide 0.3 is added. % (Parts by weight, calculated based on the weight of the waste tire curing bladder as 100%) for blending and desulfurization, blending for 30 minutes, and parked for 8 hours; then adding 15% (parts by weight, calculated based on the weight of the waste tire curing bladder as 100%) Polyvinyl chloride, neoprene rubber and chlorinated butyl rubber are blended. The mass ratio of polyvinyl chloride, neoprene rubber and chlorinated butyl rubber is 1:1:1; the stirring speed is 550r/min, and the blending time It is 27 minutes to obtain modified waste tire curing bladder material;
S2、密炼机炼胶,密炼起始温度为80℃,先向密炼机中加入50份丁基橡胶、10份改性处理的废弃轮胎硫化胶囊料密炼3分钟,再加入50份丁基橡胶密炼55秒,然后加40份N330、6.5份蓖麻油、3份氧化锌、2份硬脂酸、5份促进DM剂,密炼2分钟,温度为130℃排胶,得到密炼胶片;S2: Mixing rubber with internal mixer. The initial temperature of internal mixing is 80℃. First add 50 parts of butyl rubber and 10 parts of modified waste tire vulcanization bladder material to the internal mixer for 3 minutes, and then add 50 parts. The butyl rubber is banned for 55 seconds, then 40 parts of N330, 6.5 parts of castor oil, 3 parts of zinc oxide, 2 parts of stearic acid, 5 parts of DM accelerating agent are added, and banburying is carried out for 2 minutes at a temperature of 130°C to discharge the rubber. Refining film
S3、将密炼胶片放入开炼机中,开炼机辊温为80℃,添加9份烷基苯酚甲醛树脂进行混炼、薄通打三角包,压出胶片,胶片自然冷却至室温;S3. Put the banbury film into an open mill, the roller temperature of the open mill is 80℃, add 9 parts of alkylphenol formaldehyde resin for mixing, thin through the triangle bag, press out the film, and cool the film naturally to room temperature;
S4、将S3中压出的胶片加入到注射硫化机的喂料口,注射机温度设为80℃,将胶料注射在模具内;S4. Add the film extruded in S3 to the feeding port of the injection vulcanizing machine, set the temperature of the injection machine to 80°C, and inject the rubber material into the mold;
S5、设置硫化温度185℃,硫化时间在35min,硫化完成,顶出硫化胶囊。S5. Set the vulcanization temperature to 185°C, the vulcanization time is 35min, the vulcanization is completed, and the vulcanization bladder is ejected.
对于实施例1-7中的胶片进行测试,拉伸强度>10.0MPa,撕裂 强度>38.0kN/m,扯断伸长率>350%,硬度>72A;目前以农用轮胎的硫化胶囊型号进行制作,使用次数可达300-500次。For the film in Examples 1-7, the tensile strength>10.0MPa, the tearing strength>38.0kN/m, the elongation at break>350%, the hardness>72A; currently it is carried out with the vulcanization bladder model of agricultural tires. It can be used for 300-500 times.
不脱离本发明的构思和范围可以做出许多其他改变和改型。应当理解,本发明不限于特定的实施方式,本发明的范围由所附权利要求限定。Many other changes and modifications can be made without departing from the concept and scope of the present invention. It should be understood that the present invention is not limited to specific embodiments, and the scope of the present invention is defined by the appended claims.

Claims (6)

  1. 一种轮胎硫化胶囊的制备方法,其特征在于,A method for preparing a tire curing bladder, characterized in that:
    原料包括:丁基橡胶80-100份和经过改性处理的废弃轮胎硫化胶囊料1-20份,炭黑20-50份,硫化树脂8-10份,蓖麻油5.5-7.5份,氧化锌2-4份,硬脂酸1-3份,促进剂3-5份;The raw materials include: 80-100 parts of butyl rubber and 1-20 parts of modified waste tire curing bladder material, 20-50 parts of carbon black, 8-10 parts of vulcanized resin, 5.5-7.5 parts of castor oil, zinc oxide 2 -4 parts, 1-3 parts stearic acid, 3-5 parts accelerator;
    制备方法如下:The preparation method is as follows:
    S1、废弃轮胎硫化胶囊的两步改性处理,先将废弃轮胎硫化胶囊进行清洗、干燥,再破碎成50-200目的粒料,接着加入2,2’-二苯甲酰氨基二苯基二硫化物0.3-0.8%进行共混脱硫,共混30分钟,停放8小时;然后加入12-15%的含氯改性剂进行共混活化,得到改性处理的废弃轮胎硫化胶囊料;所述的2,2’-二苯甲酰氨基二苯基二硫化物含量和含氯改性剂的含量是以废弃轮胎硫化胶囊重量为100%计算的;S1. Two-step modification treatment of the waste tire curing bladder. First, the waste tire curing bladder is cleaned, dried, and then crushed into 50-200 mesh pellets, and then 2,2'-dibenzamidodiphenyl bismuth is added. 0.3-0.8% of the sulfide is blended for desulfurization, blended for 30 minutes, and left for 8 hours; then 12-15% of a chlorine-containing modifier is added for blending activation to obtain a modified waste tire curing bladder material; The 2,2'-dibenzamidodiphenyl disulfide content and the content of the chlorine-containing modifier are calculated based on the weight of the waste tire curing bladder as 100%;
    S2、密炼机炼胶,先向密炼机中加入一半的丁基橡胶、改性处理的废弃轮胎硫化胶囊料密炼2-4分钟,再加入另一半的丁基橡胶密炼30-60秒,然后加炭黑、蓖麻油、氧化锌、硬脂酸、促进剂密炼1-2分钟,排胶,得到密炼胶片;S2. Mix rubber in an internal mixer. First add half of the butyl rubber and modified waste tire vulcanization bladder to the internal mixer for banburying for 2-4 minutes, and then add the other half of the butyl rubber for banburying for 30-60 minutes. Seconds, then add carbon black, castor oil, zinc oxide, stearic acid, accelerant and banbury for 1-2 minutes, discharge the glue, and obtain a banbury film;
    S3、将密炼胶片放入开炼机中,添加硫化树脂进行混炼、薄通打三角包,压出胶片,胶片自然冷却至室温;S3. Put the banbury film into an open mill, add vulcanized resin for mixing, thin through the triangle bag, press out the film, and cool the film naturally to room temperature;
    S4、将S3中压出的胶片加入到注射硫化机的喂料口,注射机温度设为60-90℃,将胶料注射在模具内;S4. Put the film extruded in S3 into the feeding port of the injection vulcanizing machine, set the temperature of the injection machine to 60-90℃, and inject the rubber into the mold;
    S5、设置硫化温度180-195℃,硫化时间在20-40min,硫化完成,顶出硫化胶囊。S5. Set the vulcanization temperature to 180-195℃, and the vulcanization time is 20-40min. After the vulcanization is completed, the vulcanizing bladder is ejected.
  2. 根据权利要求1所述的一种轮胎硫化胶囊的制备方法,其特征在于,S1中,废弃轮胎硫化胶囊粒料与含氯改性剂进行搅拌共混,搅拌转速为300-600r/min,共混时间为15-30min。The method for preparing a tire curing bladder according to claim 1, wherein in S1, the waste tire curing bladder pellets and the chlorine-containing modifier are stirred and blended, and the stirring speed is 300-600r/min. The mixing time is 15-30min.
  3. 根据权利要求1或2所述的一种轮胎硫化胶囊的制备方法,其特征在于,所述含氯改性剂是含氯活性炭、聚氯乙烯、氯丁胶、氯化丁基胶中的一种或几种。The method for preparing a tire curing bladder according to claim 1 or 2, wherein the chlorine-containing modifier is one of chlorine-containing activated carbon, polyvinyl chloride, neoprene rubber, and chlorinated butyl rubber. Kind or several kinds.
  4. 根据权利要求3所述的一种轮胎硫化胶囊的制备方法,其特征在于,S2中,密炼起始温度为80℃,排胶温度为130℃。The method for preparing a tire curing bladder according to claim 3, wherein in S2, the initial temperature of banburying is 80°C, and the debinding temperature is 130°C.
  5. 根据权利要求3所述的一种轮胎硫化胶囊的制备方法,其特征在于,S3中,开炼机辊温为80℃。The method for preparing a tire curing bladder according to claim 3, wherein in S3, the roller temperature of the open mill is 80°C.
  6. 根据权利要求3所述的一种轮胎硫化胶囊的制备方法,其特征在于,所述炭黑为N330,所述促进剂为DM,所述硫化树脂为烷基苯酚甲醛树脂。The method for preparing a tire curing bladder according to claim 3, wherein the carbon black is N330, the accelerator is DM, and the curing resin is an alkylphenol formaldehyde resin.
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