WO2021093101A1 - Method for preparing tire curing bladder - Google Patents

Method for preparing tire curing bladder Download PDF

Info

Publication number
WO2021093101A1
WO2021093101A1 PCT/CN2019/127819 CN2019127819W WO2021093101A1 WO 2021093101 A1 WO2021093101 A1 WO 2021093101A1 CN 2019127819 W CN2019127819 W CN 2019127819W WO 2021093101 A1 WO2021093101 A1 WO 2021093101A1
Authority
WO
WIPO (PCT)
Prior art keywords
rotor
rubber
internal mixer
tire curing
speed
Prior art date
Application number
PCT/CN2019/127819
Other languages
French (fr)
Chinese (zh)
Inventor
赵会岩
赵海林
范屏
张学永
刘涛
Original Assignee
永一橡胶有限公司
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 永一橡胶有限公司 filed Critical 永一橡胶有限公司
Publication of WO2021093101A1 publication Critical patent/WO2021093101A1/en

Links

Images

Classifications

    • 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
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29DPRODUCING PARTICULAR ARTICLES FROM PLASTICS OR FROM SUBSTANCES IN A PLASTIC STATE
    • B29D23/00Producing tubular articles
    • B29D23/24Endless tubes, e.g. inner tubes for pneumatic tyres
    • 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
    • C08K2003/2227Oxides; Hydroxides of metals of aluminium
    • 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

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 is a hollow thin-walled rubber product. It is installed in the tire vulcanizer and used as an inner mold for tire shaping during the tire vulcanization molding process. Fill the tire vulcanizing bladder with superheated water or compressed air and other media to stretch the tire vulcanizing bladder to support the tire rubber blank, which fits the tire lining, and uses the flow and heat transfer characteristics of the fluid inside the tire vulcanizing bladder to maintain the tire The temperature is relatively balanced during the vulcanization process to achieve the effect of uniform vulcanization of the tire and improve the balance performance of the tire.
  • the tire curing bladder is very important for tire production.
  • the tire curing bladder is repeatedly used for many times under high temperature and high pressure conditions, and it is required to have excellent airtightness, strength, and aging resistance. It is precisely because the tire curing bladder needs to have many characteristics, the research on its preparation process has been In progress.
  • an internal mixer is often used.
  • the internal mixer has a pair of specific shaped and relatively rotating rotors that intermittently masticate and mix polymer materials in a closed state with adjustable temperature and pressure.
  • the two rotors rotate relative to each other, and the material from the feeding port is clamped and brought into the roll gap to be squeezed and sheared by the rotor for mixing. According to the speed, the two rotors are divided into synchronous rotor and asynchronous rotor.
  • the synchronous rotor is not as good as the asynchronous rotor in terms of mixing effect.
  • the synchronous rotor requires a long time; while the asynchronous rotor can provide stronger shearing force, and it can plasticize the rubber and
  • the mixing of the compounding agent into the rubber has a promoting effect, which is conducive to uniform mixing and shortening the mixing time; but there is a problem: the temperature of the rubber on the side of the rotor with high rotation speed rises faster than the temperature of the rubber on the side of the rotor with low rotation speed. Speed, under the accumulation of time, the temperature of the rubber on the side of the rotor with high rotation speed will be significantly higher than the temperature of the rubber on the side with the rotor with low rotation speed. The rubber with higher temperature is prone to scorching, which will vulcanize the tire. The quality of the capsules is very unfavorable. Summary of the invention
  • the present invention provides a method for preparing a tire curing bladder.
  • the rotational speeds of two rotors in an internal mixer are controlled to solve the above-mentioned technical problems.
  • the specific technical solution is a method for preparing a tire curing bladder.
  • the raw rubber is butyl rubber;
  • the reinforcing filler includes: carbon black, white carbon black and aluminum oxide;
  • the active agent is chlorine Butadiene rubber;
  • processing aids include: stearic acid, paraffin wax;
  • vulcanizing agent is vulcanized resin;
  • the preparation method includes the following steps:
  • the rubber material discharged in S4 and S3 enters the rubber strainer for rubber filtering, and the discharged rubber material is added to the open mill, and the temperature of the open mill is controlled to 80-90°C.
  • the vulcanizing agent is added and mixed for 2-5 minutes. After that, convey the rubber material in the open mill to the tablet press to press out the film, and park it for more than 24 hours;
  • the injection temperature is 150-185°C
  • the vulcanization temperature is 185°C
  • the vulcanization time is 15-25min
  • the vulcanization is completed, and the tire curing bladder is taken out;
  • the speed ratio between the first rotor and the second rotor alternately changes from 1: (1-1.25) to (1-1.25):1 according to a time period of 0 ⁇ t ⁇ 300s;
  • the tire curing bladder preparation system used in the preparation method of the tire curing bladder includes:
  • the upper auxiliary machine is used for weighing materials and auxiliary feeding, and the upper auxiliary machine is located above the internal mixer;
  • the internal mixer is used for mixing raw rubber, reinforcing fillers, active agents and processing aids.
  • the hopper of the internal mixer is connected to the outlet of the upper auxiliary machine, and the outlet of the internal mixer is connected to the inlet of the rubber filter;
  • the rubber strainer breaks and disperses the gum beans and the agglomerated filler in the rubber material; the outlet of the rubber strainer is connected with the inlet of the mill;
  • the open mixer further mixes the rubber material
  • the tablet press presses the irregular rubber material into flakes, and the inlet of the tablet press is connected with the outlet of the open mill;
  • the injection vulcanizing machine is used to heat and inject the film into the mold cavity to shape and vulcanize;
  • the upper auxiliary machine, internal mixer, rubber strainer, open mill, tablet press and injection vulcanizing machine are respectively connected with the controller.
  • the upper auxiliary machine, internal mixer, rubber strainer, open mixer, tablet press and controller are connected to electrical power equipment during use. This is common knowledge in equipment application and will not be described in detail in the present invention.
  • the ratio of carbon black, white carbon black and aluminum oxide is (8-12): (1-2):1.
  • the ratio of stearic acid and paraffin wax is 1:(1-2).
  • the speed of the first rotor and the second rotor change with time in a positive half-wave alternately, and the waveform is one of a sine wave, a triangular wave, a rectangular wave, or a trapezoidal wave.
  • the mixing time between S1, S2 and S3 is equal, and the time period during which the rotation speed ratio between the first rotor and the second rotor alternately changes is equal to the mixing time of step S1.
  • the rotation speed of the first rotor in the internal mixer the rotation speed of the second rotor is (1-1.25):1; in S2, the rotation speed of the second rotor in the internal mixer: the rotation speed of the first rotor is (1-1.25):1; In S3, the speed of the first rotor in the internal mixer: the speed of the second rotor is (1-1.25):1.
  • the speed of the first rotor in the internal mixer the speed of the second rotor is (1-1.10):1; in S2, the speed of the second rotor in the internal mixer: the speed of the first rotor is (1-1.10):1; In S3, the speed of the first rotor in the internal mixer: the speed of the second rotor is (1-1.10):1.
  • the rotation speed of the second rotor in the internal mixer the rotation speed of the first rotor is (1-1.25):1; in S2, the rotation speed of the first rotor in the internal mixer: the rotation speed of the second rotor is (1-1.25):1; In S3, the speed of the second rotor in the internal mixer: the speed of the first rotor is (1-1.25):1.
  • the internal mixer in the tire curing bladder preparation system has an external mixer outer shell, an internal mixing chamber, and a first rotor and a second rotor inside the internal mixing chamber, and above the internal mixing chamber
  • the upper bolt, the middle of the upper bolt is a hollow cavity, and the upper bolt control rod is rigidly connected to the lower hammer inside the bottom; the middle side of the upper bolt is opened with an upward hopper, and the bottom of the mixing chamber has Discharge valve, a discharge gate is provided on the outer shell of the internal mixer, which is located on the side close to the rubber strainer;
  • the front end of the rubber strainer is a gear pump.
  • the gear pump has a first gear and a second gear that mesh with each other.
  • the gear pump has a revolving door on the side close to the internal mixer, and a discharge on the side far from the internal mixer.
  • the discharge port is connected to the discharge pipe, and a filter screen is installed inside the discharge pipe.
  • mixing is to mix the raw rubber and various compounding agents together through the rubber equipment according to the proportion of the compounding agent specified in the rubber formula, and make the various compounding agents uniformly dispersed in the raw rubber.
  • the purpose of compound mixing is to obtain uniform physical and mechanical performance indicators and meet the compound performance indicators specified by the formula, so as to facilitate the next process operation and ensure the quality of the finished product.
  • the speed of the first rotor when the speed of the first rotor is faster in S1, the temperature of the raw rubber near the first rotor rises faster, and the temperature of raw rubber in the mixing chamber is not uniform; in S2 The speed of the second rotor is faster, so that the temperature of the rubber material close to the second rotor rises faster, which can reduce the temperature difference or overshoot in S1; in S3, the speed of the first rotor is faster, and in S2, the temperature The slow-rising rubber material starts to heat up rapidly, and continues to reduce the temperature unevenness between the rubber materials.
  • the speed ratio between the first rotor and the second rotor is constantly adjusted and changed. While increasing the shear force, it is helpful to promote the uniform temperature of the rubber compound; avoiding the temperature of a certain part of the rubber compound under a single speed ratio The phenomenon of scorching and large temperature difference between the rubber materials occurs when the temperature rises too fast.
  • S4 is used to filter the rubber, and the agglomerated, undispersed compounding agent and carbon black are forced to disperse, which can promote the uniformity of the rubber; the filter needs to be cleaned regularly.
  • the control of temperature parameters in the rubber mixing and vulcanization process is closely related to the formula itself and the process steps; the preparation method of the present invention can realize the uniform mixing of the rubber compound in a relatively short time, and the temperature rise tends to be uniform, and can improve the tire curing bladder Production efficiency and quality.
  • the raw rubber is plasticized to increase the plasticity of the butyl rubber, which is conducive to the subsequent mixing of active agents, processing aids and reinforcing fillers;
  • Figure 1 is a schematic structural diagram of a tire curing bladder preparation system of a method for preparing a tire curing bladder in the present invention
  • Figure 2 is a schematic diagram of the internal mixer structure of a method for preparing a tire curing bladder in the present invention
  • Figure 3 is a schematic diagram of the structure of a rubber strainer of a method for preparing a tire curing bladder in the present invention
  • FIG. 4 is a schematic diagram of the state between the internal mixer and the rubber strainer in a method for preparing a tire curing bladder according to the present invention
  • Embodiment 5 is a schematic speed-time diagram of the first rotor in Embodiment 1;
  • FIG. 6 is a schematic speed-time diagram of the second rotor in Embodiment 1;
  • Figure 7 is a schematic speed-time diagram of the first rotor in Embodiment 2.
  • FIG. 11 is a schematic speed-time diagram of the first rotor in Embodiment 4.
  • FIG. 12 is a schematic speed-time diagram of the second rotor in Embodiment 4.
  • FIG. 12 is a schematic speed-time diagram of the second rotor in Embodiment 4.
  • a method for preparing tire curing bladder the tire curing bladder components, 100 parts of butyl rubber, 24-48 parts of carbon black, 3-8 parts of white carbon black, 2 aluminum oxide -6 parts, 6-8 parts of chloroprene rubber, 1-2.5 parts of stearic acid, 1.5-3.4 parts of paraffin wax, 2-6 parts of vulcanized resin.
  • the preparation method includes the following steps:
  • the raw rubber is added to the internal mixer 2 through the upper auxiliary machine 1, and the first rotor 203 and the second rotor 204 in the internal mixer 2 are controlled to rotate asynchronously.
  • the temperature in the internal mixer 2 is 100-110°C. Time 1-2min;
  • the rubber material discharged in S4 and S3 enters the rubber filter 3 for rubber filtering, and the discharged rubber material is added to the open mill 4, and the temperature of the open mill 4 is controlled to 80-90°C.
  • the vulcanizing agent is added and mixed After 2-5 minutes, convey the rubber material in the open mill 4 to the tablet press 5 to press out the film, and park it for more than 24 hours;
  • the injection temperature is 150-185°C
  • the vulcanization temperature is 185°C
  • the vulcanization time is 15-25min.
  • the rotation speed ratio between the first rotor 203 and the second rotor 204 alternately changes from 1:1-1.25 to 1-1.25:1 in a time period of 0 ⁇ t ⁇ 300s.
  • the tire curing bladder preparation system used in the preparation method of the tire curing bladder includes:
  • the upper auxiliary machine 1 is used for weighing materials and auxiliary feeding, and the upper auxiliary machine 1 is located above the internal mixer 2;
  • the internal mixer 2 is used for mixing raw rubber, reinforcing fillers, active agents and processing aids.
  • the hopper 208 of the internal mixer 2 is connected to the outlet of the upper auxiliary machine 1, and the outlet of the internal mixer 2 is connected to the rubber filter Inlet connection of machine 3;
  • the rubber strainer 3 breaks and disperses the gum beans and the agglomerated filler inside the rubber material; the outlet of the rubber strainer 3 is connected with the inlet of the mill 4;
  • the open mixer 4 further mixes the rubber
  • the tablet press 5 compresses the irregular rubber material into flakes, and the inlet of the tablet press 5 is connected with the outlet of the mill 4;
  • the injection vulcanizing machine 7 is used to heat the film, heat and inject it into the mold cavity to shape and vulcanize;
  • the upper auxiliary machine 1, the internal mixer 2, the rubber strainer 3, the open mill 4, the tablet press 5 and the injection vulcanizing machine 7 are respectively connected to the controller 6.
  • the upper auxiliary machine, internal mixer, rubber strainer, open mixer, tablet press and controller are connected to electrical power equipment during use. This is common knowledge in equipment application and will not be described in detail in the present invention.
  • the rotation speed of the second rotor 204 in the internal mixer 2 the rotation speed of the first rotor 203 is 1-1.25:1; in S2, the rotation speed of the first rotor 203 in the internal mixer 2: the rotation speed of the second rotor 204 is 1 -1.25:1; In S3, the rotation speed of the second rotor 204 in the internal mixer 2: the rotation speed of the first rotor 203 is 1-1.25:1.
  • the internal mixer 2 in the tire curing bladder preparation system has an external mixer housing 201 on the outside, a mixing chamber 202 inside, and a first rotor 203 and a second rotor 204 inside the mixing chamber 202.
  • a hopper 208 with upward opening, a discharge valve 209 at the bottom of the internal mixing chamber 202, a discharge door 210 is provided on the external mixer housing 201, and the discharge door 210 is located on the side close to the rubber strainer 3;
  • the front end of the rubber strainer 3 is a gear pump 301.
  • the gear pump 301 has a first gear 302 and a second gear 303 that mesh with each other.
  • the side of the gear pump 301 close to the internal mixer 2 is provided with a revolving door 304.
  • a discharge port 305 is provided on one side of the machine 2, the discharge port 305 is connected to a discharge pipe 306, and a filter 307 is installed inside the discharge pipe 306.
  • Examples 1-4 are shown in Table 1, in parts by weight.
  • the preparation steps and the used tire curing bladder preparation system refer to the technical scheme of the present invention, and the process conditions in the preparation steps are different.
  • Example 2 Example 3
  • Butyl rubber/part 100 100 100 100 100 Carbon black/part twenty four twenty four 48 48 White carbon black/part 3 4 6 8
  • Aluminum oxide/part 3 2 6 4 Stearic acid/part 1 1.5 1.6 2 Paraffin/part 2 1.5 3.2 3 Vulcanized resin/part 2 2 4 6 Neoprene/part 6 6 7 8
  • the mixing time between S1, S2 and S3 is equal, and the time period during which the rotation speed ratio between the first rotor 203 and the second rotor 204 alternately changes is equal to the mixing time of step S1.
  • the rotation speed of the first rotor 203 in the internal mixer 2 the rotation speed of the second rotor 204 is 1-1.25:1; in S2, the rotation speed of the second rotor 204 in the internal mixer 2: the rotation speed of the first rotor 203 The speed is 1-1.25:1; in S3, the speed of the first rotor 203 in the internal mixer 2: the speed of the second rotor 204 is 1-1.25:1.
  • the speed of the first rotor 203 and the second rotor 204 change with time in a positive half-wave alternately, the waveform is a triangular wave, and the speed change between the two is exactly half a time period.
  • v1 is the minimum speed
  • v2 is the maximum speed
  • v2 is 1.25 times of v1.
  • the speed of the first rotor 203 accelerates from v1 to v2, and then from v2 to v1; the speed of the second rotor 204 is always v1; between t1-t2, the speed of the first rotor 203 is always Is v1, the speed of the second rotor 204 accelerates from v1 to v2, and then from v2 to v1; the following t2-t4 and t0-t2 speed changes are the same, t0-t2 is a time period; the first rotor 203 and the first The rotation speed ratio between the two rotors 204 presents a periodic alternating change, and the time period t0-t2 is exactly the same as the S1 banburying time, which is 2 min.
  • Embodiment 2 The mixing time between S1, S2 and S3 is equal, and the time period during which the rotation speed ratio between the first rotor 203 and the second rotor 204 alternately changes is equal to the mixing time of step S1.
  • the rotation speed of the second rotor 204 in the internal mixer 2 the rotation speed of the first rotor 203 is 1.10:1;
  • the rotation speed of the first rotor 203 in the internal mixer 2 the rotation speed of the second rotor 204 is 1.10:1;
  • the rotation speed of the second rotor 204 in the internal mixer 2 the rotation speed of the first rotor 203 is 1.10:1.
  • the speed of the first rotor 203 and the second rotor 204 change with time in a positive half-wave alternately, and the waveform is a rectangular wave. At this time, the difference between v1 and v2 should not be too large, and the speed change between the two is exactly half a difference Time period.
  • v1 is the minimum speed
  • v2 is the maximum speed
  • v2 is 1.10 times that of v1.
  • the speed of the first rotor 203 is always v1
  • the speed of the second rotor 204 is always v2
  • the speed of the first rotor 203 is always v2
  • the speed of the second rotor 204 It is always v1; the following t2-t4 and t0-t2 speed changes are the same, the speed ratio between the first rotor 203 and the second rotor 204 presents a periodic alternate change
  • the time period t0-t2 coincides with the S1 mixing time It is equal to 2min.
  • Embodiment 3 The speed of the first rotor 203 and the second rotor 204 change with time in a positive half wave alternately, the waveform is a sine wave, and the speed change between the two is exactly half a time period.
  • v1 is the minimum speed
  • v2 is the maximum speed
  • v2 is 1.25 times of v1.
  • the speed of the first rotor 203 is always v1
  • the speed of the second rotor 204 accelerates from v1 to v2, and then from v2 to v1
  • the speed of the first rotor 203 changes from v1 accelerates to v2, and then from v2 to v1, the speed of the second rotor 204 is always v1;
  • the following t2-t4 and t0-t2 have the same speed change
  • t0-t2 is a time period
  • the first rotor 203 and the first rotor 203 The rotation speed ratio between the two rotors 204 presents a periodic alternate change, and the time period is 1 min.
  • Embodiment 4 The speed of the first rotor 203 and the second rotor 204 change with time in a positive half-wave alternately, the waveform is a trapezoidal wave, and the speed change between the two is exactly 1/4 time period.
  • v1 is the minimum speed
  • v2 is the maximum speed
  • v2 is 1.25 times of v1.
  • the speed of the first rotor 203 is always v2, and the speed of the second rotor 204 is always v1; between t1 and t2, the speed of the first rotor 203 decreases from v2 to v1, and the second rotor 204
  • the speed accelerates from v1 to v2; between t2-t3, the speed of the first rotor 203 is always v1, and the speed of the second rotor 204 is always v2; between t3-t4, the speed of the first rotor 203 is from v1 accelerates to v2, and the speed of the second rotor 204 decreases from v2 to v1; the following t4-t5 changes the same speed as t0-t1, and a new cycle starts; t0-t4 is a time period; the first rotor 203 and the first
  • the film prepared according to the method of Examples 1-4 was vulcanized on a plate vulcanizer, the film thickness was 4mm, the vulcanization temperature was 185°C, the vulcanization time was 20min, and after 24h, samples were prepared and the mechanical properties were tested.
  • 2Tensile performance testing standard GB/T528-2009, the sample is dumbbell-shaped, testing speed is 500mm/min, testing environment temperature is 23 ⁇ 2°C; testing equipment adopts GT-TCS-2000 of Taiwan High Speed Rail Technology Co., Ltd. Tensile testing machine.
  • 3Tear strength testing standard GB/T529-2008, using right-angled specimens, testing speed 500mm/min, testing environment temperature 23 ⁇ 2°C; testing equipment adopts GT-TCS-2000 of Taiwan High Speed Rail Technology Co., Ltd. Tensile testing machine.
  • the film prepared by the technical scheme of the present invention has excellent properties such as tensile strength, elongation at break, and tear strength; it shows that the technical scheme of the present invention has good rubber mixing effect.
  • the rubber material is uniform, and tire curing bladder with better mechanical properties can be prepared.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
  • Moulds For Moulding Plastics Or The Like (AREA)

Abstract

The present invention relates to the technical field of preparation of tire curing bladders, and disclosed is a method for preparing a tire curing bladder. Components of the tire curing bladder are butyl rubber, carbon black, white carbon black, aluminum oxide, chloroprene rubber, stearic acid, paraffin, and a curing resin. Plastication and segmented mixing are performed in an internal mixer, then rubber filtering, open milling, tableting, and injection curing are performed to prepare the tire curing bladder, and the speed ratio between rotors in the internal mixer is periodically and alternately changed. Compared with the prior art, the present invention has the beneficial effects that the method for preparing the tire curing bladder is optimally designed, the rotational speed between the first rotor and the second rotor is alternately changed to generate a speed difference, the rubber material mixing effect is improved, the excessive temperature difference is avoided, and the rubber material temperature uniformity is promoted; raw rubber plastication is performed, the raw rubber plasticity is improved, a reinforcing filler is added in a segmented mode, a rubber filtering operation is performed, and the rubber material uniformity is improved; injection curing molding is performed, and finally, the goal of improving the production efficiency and quality of the tire curing bladder is implemented.

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
轮胎硫化胶囊是一种中空薄壁橡胶制品,在轮胎的硫化成型过程中,安装在轮胎硫化机内部作为轮胎定型的内模具使用。向轮胎硫化胶囊内部充入过热水或压缩气等介质,使轮胎硫化胶囊伸张支撑轮胎胶胚,其与轮胎胎里相贴合,利用轮胎硫化胶囊内部介质流体的流动传热特点,保持轮胎硫化过程中温度相对均衡,达到轮胎硫化均匀的效果,提高轮胎的平衡性能。The tire vulcanizing bladder is a hollow thin-walled rubber product. It is installed in the tire vulcanizer and used as an inner mold for tire shaping during the tire vulcanization molding process. Fill the tire vulcanizing bladder with superheated water or compressed air and other media to stretch the tire vulcanizing bladder to support the tire rubber blank, which fits the tire lining, and uses the flow and heat transfer characteristics of the fluid inside the tire vulcanizing bladder to maintain the tire The temperature is relatively balanced during the vulcanization process to achieve the effect of uniform vulcanization of the tire and improve the balance performance of the tire.
轮胎硫化胶囊对于轮胎的生产十分重要。轮胎硫化胶囊在高温、高压条件下重复使用多次,要求其具备优良的气密性、强度、耐老化等性能,正是由于轮胎硫化胶囊需要具备的特性较多,对其制备工艺的研究一直在进行。在炼胶阶段,常使用到密炼机,密炼机中有一对特定形状并相对回转的转子、在可调温度和压力的密闭状态下间隙性地对聚合物材料进行塑炼和混炼。生胶和填充剂、各种配合剂在密炼机中混炼时,两转子相对回转,将来自加料口的物料夹住带入辊缝受到转子的挤压和剪切进行混炼。根据转速,两个转子分为同步转子和异步转子,混炼效果上同步转子不如异步转子,同步转子所需时间长;而异步转子能够提供更强的剪切力,对于胶料自身塑炼以及配合剂混入胶料中有促进作用,利于混炼均匀,缩短混炼时间;但存在问题:转速高的转子一侧的胶料温度上升速度较快于转速低的转子一侧的 胶料温度上升速度,在时间积累下,靠近转速高的转子一侧的胶料温度会明显高于靠近转速低的转子一侧的胶料的温度,温度较高的胶料易出现焦烧现象,对轮胎硫化胶囊的质量十分不利。发明内容The tire curing bladder is very important for tire production. The tire curing bladder is repeatedly used for many times under high temperature and high pressure conditions, and it is required to have excellent airtightness, strength, and aging resistance. It is precisely because the tire curing bladder needs to have many characteristics, the research on its preparation process has been In progress. In the rubber mixing stage, an internal mixer is often used. The internal mixer has a pair of specific shaped and relatively rotating rotors that intermittently masticate and mix polymer materials in a closed state with adjustable temperature and pressure. When raw rubber, fillers, and various compounding agents are mixed in the internal mixer, the two rotors rotate relative to each other, and the material from the feeding port is clamped and brought into the roll gap to be squeezed and sheared by the rotor for mixing. According to the speed, the two rotors are divided into synchronous rotor and asynchronous rotor. The synchronous rotor is not as good as the asynchronous rotor in terms of mixing effect. The synchronous rotor requires a long time; while the asynchronous rotor can provide stronger shearing force, and it can plasticize the rubber and The mixing of the compounding agent into the rubber has a promoting effect, which is conducive to uniform mixing and shortening the mixing time; but there is a problem: the temperature of the rubber on the side of the rotor with high rotation speed rises faster than the temperature of the rubber on the side of the rotor with low rotation speed. Speed, under the accumulation of time, the temperature of the rubber on the side of the rotor with high rotation speed will be significantly higher than the temperature of the rubber on the side with the rotor with low rotation speed. The rubber with higher temperature is prone to scorching, which will vulcanize the tire. The quality of the capsules is very unfavorable. Summary of the invention
本发明提供一种轮胎硫化胶囊的制备方法,该方法中对密炼机中两个转子的转速进行控制,解决上述技术问题。The present invention provides a method for preparing a tire curing bladder. In the method, the rotational speeds of two rotors in an internal mixer are controlled to solve the above-mentioned technical problems.
具体技术方案是一种轮胎硫化胶囊的制备方法,该轮胎硫化胶囊组分中,生胶是丁基橡胶;补强填充剂包括:炭黑、白炭黑和三氧化二铝;活性剂是氯丁橡胶;加工助剂包括:硬脂酸、石蜡;硫化剂是硫化树脂;The specific technical solution is a method for preparing a tire curing bladder. In the tire curing bladder component, the raw rubber is butyl rubber; the reinforcing filler includes: carbon black, white carbon black and aluminum oxide; the active agent is chlorine Butadiene rubber; processing aids include: stearic acid, paraffin wax; vulcanizing agent is vulcanized resin;
制备方法包括以下步骤:The preparation method includes the following steps:
S1、通过上辅机向密炼机中加入生胶,控制密炼机中的第一转子和第二转子异步转动,密炼机中温度为100-110℃,密炼时间1-2min;S1. Add raw rubber to the internal mixer through the upper auxiliary machine, control the first and second rotors in the internal mixer to rotate asynchronously, the temperature in the internal mixer is 100-110℃, and the mixing time is 1-2min;
S2、通过上辅机向密炼机中加入活性剂、加工助剂和1/2补强填充剂,控制密炼机中的第一转子和第二转子异步转动,密炼机中温度为100-110℃,密炼时间1-2min;S2. Add active agent, processing aid and 1/2 reinforcing filler to the internal mixer through the upper auxiliary machine to control the asynchronous rotation of the first and second rotors in the internal mixer, and the temperature in the internal mixer is 100 -110℃, banbury time 1-2min;
S3、通过上辅机向密炼机中加入剩下的1/2补强填充剂,控制密炼机中的第一转子和第二转子异步转动,密炼机中温度为100-110℃,密炼时间1-2min,排出胶料,排胶温度为100-110℃;S3. Add the remaining 1/2 reinforcing filler to the internal mixer through the upper auxiliary machine, and control the first and second rotors in the internal mixer to rotate asynchronously. The temperature in the internal mixer is 100-110°C. The banburying time is 1-2min, the rubber material is discharged, and the rubber discharge temperature is 100-110℃;
S4、S3中排出的胶料进入到滤胶机中进行滤胶,排出的胶料加入到开炼机中,控制开炼机的温度为80-90℃,加入硫化剂,混炼2-5min后,将开炼机中的胶料输送至压片机中压出胶片,停放24h以上;The rubber material discharged in S4 and S3 enters the rubber strainer for rubber filtering, and the discharged rubber material is added to the open mill, and the temperature of the open mill is controlled to 80-90°C. The vulcanizing agent is added and mixed for 2-5 minutes. After that, convey the rubber material in the open mill to the tablet press to press out the film, and park it for more than 24 hours;
S5、将S4的胶片加入到注射硫化机中,注射温度为150-185℃,硫化温度为185℃,硫化时间为15-25min,硫化完成,取出轮胎硫化胶囊;S5. Put the S4 film into the injection vulcanizer, the injection temperature is 150-185°C, the vulcanization temperature is 185°C, the vulcanization time is 15-25min, the vulcanization is completed, and the tire curing bladder is taken out;
在S1、S2、S3中,第一转子和第二转子之间的转速比按照0<t<300s的时间周期在1:(1-1.25)至(1-1.25):1间交替变化;In S1, S2, and S3, the speed ratio between the first rotor and the second rotor alternately changes from 1: (1-1.25) to (1-1.25):1 according to a time period of 0<t<300s;
轮胎硫化胶囊的制备方法所使用的轮胎硫化胶囊制备系统,包括:The tire curing bladder preparation system used in the preparation method of the tire curing bladder includes:
上辅机用于称量物料、辅助加料,上辅机位于密炼机的上方;The upper auxiliary machine is used for weighing materials and auxiliary feeding, and the upper auxiliary machine is located above the internal mixer;
密炼机用于生胶、补强填充剂、活性剂和加工助剂的混炼,密炼机的加料斗连接着上辅机的出口,密炼机的出口与滤胶机的进口连接;The internal mixer is used for mixing raw rubber, reinforcing fillers, active agents and processing aids. The hopper of the internal mixer is connected to the outlet of the upper auxiliary machine, and the outlet of the internal mixer is connected to the inlet of the rubber filter;
滤胶机使胶料内部的胶豆、团聚的填充剂破碎分散;滤胶机的出口与开炼机的进口连接;The rubber strainer breaks and disperses the gum beans and the agglomerated filler in the rubber material; the outlet of the rubber strainer is connected with the inlet of the mill;
开炼机对胶料进一步混炼;The open mixer further mixes the rubber material;
压片机将不规则的胶料压成片状,压片机的进口与开炼机的出口连接;The tablet press presses the irregular rubber material into flakes, and the inlet of the tablet press is connected with the outlet of the open mill;
注射硫化机用于对胶片加热、加热注射至模腔中定型硫化;The injection vulcanizing machine is used to heat and inject the film into the mold cavity to shape and vulcanize;
上辅机、密炼机、滤胶机、开炼机、压片机和注射硫化机分别与控制器连接。上辅机、密炼机、滤胶机、开炼机、压片机及控制器在使用中连接电气动力设备,这是设备应用中的公知常识,在本发明中不作详细说明。The upper auxiliary machine, internal mixer, rubber strainer, open mill, tablet press and injection vulcanizing machine are respectively connected with the controller. The upper auxiliary machine, internal mixer, rubber strainer, open mixer, tablet press and controller are connected to electrical power equipment during use. This is common knowledge in equipment application and will not be described in detail in the present invention.
进一步,生胶100份,补强填充剂30-60份,活性剂6-8份,加工助剂3-5份,硫化剂2-6份。Further, 100 parts of raw rubber, 30-60 parts of reinforcing fillers, 6-8 parts of active agents, 3-5 parts of processing aids, and 2-6 parts of vulcanizing agents.
进一步,补强填充剂中,炭黑、白炭黑和三氧化二铝之间的配比是(8-12):(1-2):1。Further, in the reinforcing filler, the ratio of carbon black, white carbon black and aluminum oxide is (8-12): (1-2):1.
进一步,加工助剂中,硬脂酸和石蜡之间的配比是1:(1-2)。Furthermore, in the processing aid, the ratio of stearic acid and paraffin wax is 1:(1-2).
进一步,第一转子和第二转子的速度随时间的变化呈正半波交替变化,波形是正弦波、三角波、矩形波或者梯形波中的一种。Further, the speed of the first rotor and the second rotor change with time in a positive half-wave alternately, and the waveform is one of a sine wave, a triangular wave, a rectangular wave, or a trapezoidal wave.
进一步,S1、S2和S3之间的密炼时间相等,第一转子和第二转子之间的转速比交替变化的时间周期等于步骤S1的密炼时间。Further, the mixing time between S1, S2 and S3 is equal, and the time period during which the rotation speed ratio between the first rotor and the second rotor alternately changes is equal to the mixing time of step S1.
进一步,S1中,密炼机中的第一转子的转速:第二转子的转速为(1-1.25):1;S2中,密炼机中的第二转子的转速:第一转子的转速为(1-1.25):1;S3中,密炼机中的第一转子的转速:第二转子的转速为(1-1.25):1。Further, in S1, the rotation speed of the first rotor in the internal mixer: the rotation speed of the second rotor is (1-1.25):1; in S2, the rotation speed of the second rotor in the internal mixer: the rotation speed of the first rotor is (1-1.25):1; In S3, the speed of the first rotor in the internal mixer: the speed of the second rotor is (1-1.25):1.
进一步,S1中,密炼机中的第一转子的转速:第二转子的转速为(1-1.10):1;S2中,密炼机中的第二转子的转速:第一转子的转速为(1-1.10):1;S3中,密炼机中的第一转子的转速:第二转子的转速为(1-1.10):1。Further, in S1, the speed of the first rotor in the internal mixer: the speed of the second rotor is (1-1.10):1; in S2, the speed of the second rotor in the internal mixer: the speed of the first rotor is (1-1.10):1; In S3, the speed of the first rotor in the internal mixer: the speed of the second rotor is (1-1.10):1.
进一步,S1中,密炼机中的第二转子的转速:第一转子的转速为(1-1.25):1;S2中,密炼机中的第一转子的转速:第二转子的转速为(1-1.25):1;S3中,密炼机中的第二转子的转速:第一转子的转速为(1-1.25):1。Further, in S1, the rotation speed of the second rotor in the internal mixer: the rotation speed of the first rotor is (1-1.25):1; in S2, the rotation speed of the first rotor in the internal mixer: the rotation speed of the second rotor is (1-1.25):1; In S3, the speed of the second rotor in the internal mixer: the speed of the first rotor is (1-1.25):1.
进一步,所述的轮胎硫化胶囊制备系统中的密炼机,外侧有密炼机外壳体,内部有密炼室,密炼室内侧有第一转子和第二转子,在密炼室的上方有上顶栓,上顶栓的中间是中空腔体,内部有底部刚性连接下压锤的上顶栓控杆;上顶栓的中部一侧开有开口向上的加料斗,密炼室的底部有卸料阀,在密炼机外壳体上设有卸料门,卸料门位于靠近滤胶机的一侧;Further, the internal mixer in the tire curing bladder preparation system has an external mixer outer shell, an internal mixing chamber, and a first rotor and a second rotor inside the internal mixing chamber, and above the internal mixing chamber The upper bolt, the middle of the upper bolt is a hollow cavity, and the upper bolt control rod is rigidly connected to the lower hammer inside the bottom; the middle side of the upper bolt is opened with an upward hopper, and the bottom of the mixing chamber has Discharge valve, a discharge gate is provided on the outer shell of the internal mixer, which is located on the side close to the rubber strainer;
滤胶机的前端是齿轮泵,齿轮泵内部有相互啮合的第一齿轮和第二齿轮,齿轮泵靠近密炼机的一侧设有旋转门,在远离密炼机的一侧设有排料口,排料口连接着排料管道,排料管道的内部安装着滤网。The front end of the rubber strainer is a gear pump. The gear pump has a first gear and a second gear that mesh with each other. The gear pump has a revolving door on the side close to the internal mixer, and a discharge on the side far from the internal mixer. The discharge port is connected to the discharge pipe, and a filter screen is installed inside the discharge pipe.
在本发明中,S1中,第一转子和第二转子之间有速度差,能够提供较大的剪切力,对生胶进行塑炼,塑炼增大丁基橡胶的可塑性, 利于后续的活性剂、加工助剂和1/2补强填充剂的混入。S2中,第一转子和第二转子之间有速度差,能够提供较大的剪切力,利于活性剂、加工助剂和1/2补强填充剂混入生胶中。S3中,第一转子和第二转子之间有速度差,能够提供较大的剪切力,利于剩下的1/2补强填充剂分散进胶料中,提高混炼效果,缩短混炼时间,利于提高总体生产效率及产品质量。In the present invention, in S1, there is a speed difference between the first rotor and the second rotor, which can provide a larger shear force to masticate the raw rubber, and the mastication increases the plasticity of the butyl rubber, which is beneficial to the subsequent Mixing of active agent, processing aid and 1/2 reinforcing filler. In S2, there is a speed difference between the first rotor and the second rotor, which can provide a relatively large shear force, which facilitates the mixing of active agents, processing aids and 1/2 reinforcing fillers into the raw rubber. In S3, there is a speed difference between the first rotor and the second rotor, which can provide a larger shear force, which is conducive to dispersing the remaining 1/2 reinforcing filler into the rubber material, improving the mixing effect and shortening the mixing Time is conducive to improving overall production efficiency and product quality.
其中,混炼就是按照胶料配方规定的配合剂的比例,将生胶和各种配合剂通过橡胶设备混合在一起,并使各种配合剂均匀地分散在生胶之中。胶料进行混炼的目的就是要获得物理机械性能指标均匀一致,符合配方规定的胶料性能指标,以利于下工艺操作和保证成品质量要求。Among them, mixing is to mix the raw rubber and various compounding agents together through the rubber equipment according to the proportion of the compounding agent specified in the rubber formula, and make the various compounding agents uniformly dispersed in the raw rubber. The purpose of compound mixing is to obtain uniform physical and mechanical performance indicators and meet the compound performance indicators specified by the formula, so as to facilitate the next process operation and ensure the quality of the finished product.
需要说明的是,当在S1中,第一转子的转速较快时,这样靠近第一转子的那部分生胶温度上升较快,密炼室中的生胶温度是不均匀的;在S2中是第二转子的转速较快,这样靠近第二转子的胶料温度上升较快,可缩小S1中存在的温度差或反超;在S3中,第一转子的转速较快,在S2中,温度上升慢的胶料开始快速升温,继续缩小胶料间出现的温度不均程度。第一转子和第二转子之间的速比,不断进行调整变化,在提高剪切力的同时,有利于促进胶料各处温度趋于均匀;避免了单一速比下,某部分胶料温度上升过快出现焦烧及胶料间温度差异大的现象出现。It should be noted that when the speed of the first rotor is faster in S1, the temperature of the raw rubber near the first rotor rises faster, and the temperature of raw rubber in the mixing chamber is not uniform; in S2 The speed of the second rotor is faster, so that the temperature of the rubber material close to the second rotor rises faster, which can reduce the temperature difference or overshoot in S1; in S3, the speed of the first rotor is faster, and in S2, the temperature The slow-rising rubber material starts to heat up rapidly, and continues to reduce the temperature unevenness between the rubber materials. The speed ratio between the first rotor and the second rotor is constantly adjusted and changed. While increasing the shear force, it is helpful to promote the uniform temperature of the rubber compound; avoiding the temperature of a certain part of the rubber compound under a single speed ratio The phenomenon of scorching and large temperature difference between the rubber materials occurs when the temperature rises too fast.
S4中进行滤胶,将成团的、未分散的配合剂、炭黑进行强迫分散,能够促进胶料的均匀;滤网需要定期清理。炼胶和硫化过程中温度参数的控制,与配方本身、工艺步骤密切相关;本发明的制备方法, 能够在较短时间实现胶料的均匀混炼、温升趋于均匀,能够提高轮胎硫化胶囊的生产效率和质量。S4 is used to filter the rubber, and the agglomerated, undispersed compounding agent and carbon black are forced to disperse, which can promote the uniformity of the rubber; the filter needs to be cleaned regularly. The control of temperature parameters in the rubber mixing and vulcanization process is closely related to the formula itself and the process steps; the preparation method of the present invention can realize the uniform mixing of the rubber compound in a relatively short time, and the temperature rise tends to be uniform, and can improve the tire curing bladder Production efficiency and quality.
与现有技术相比,本发明中的有益效果,Compared with the prior art, the beneficial effects of the present invention,
1)对轮胎硫化胶囊的制备方法进行优化设计,控制密炼机中的第一转子和第二转子之间的转速呈现交替变化产生速度差,提高了胶料混炼效果,避免温差过大,促进胶料温度均匀,缩短混炼时间;1) Optimize the design of the preparation method of the tire curing bladder, control the rotation speed between the first rotor and the second rotor in the internal mixer to alternately produce a speed difference, improve the mixing effect of the rubber, and avoid excessive temperature differences. Promote the uniform temperature of the rubber material and shorten the mixing time;
2)在密炼机中,进行生胶塑炼,增大丁基橡胶的可塑性,利于后续的活性剂、加工助剂和补强填充剂的混入;2) In the internal mixer, the raw rubber is plasticized to increase the plasticity of the butyl rubber, which is conducive to the subsequent mixing of active agents, processing aids and reinforcing fillers;
3)补强填充剂分段加入及进行滤胶操作,能够提高混炼效率,增加其均匀性;将胶料进行注射硫化,最终实现提高轮胎硫化胶囊的生产效率和质量的目标。3) The stepwise addition of reinforcing fillers and rubber filtering operations can improve mixing efficiency and increase its uniformity; injection vulcanization of the rubber material will ultimately achieve the goal of improving the production efficiency and quality of the tire curing bladder.
附图说明Description of the drawings
图1为本发明中一种轮胎硫化胶囊的制备方法的轮胎硫化胶囊制备系统的结构示意图;Figure 1 is a schematic structural diagram of a tire curing bladder preparation system of a method for preparing a tire curing bladder in the present invention;
图2为本发明中一种轮胎硫化胶囊的制备方法的密炼机结构示意图;Figure 2 is a schematic diagram of the internal mixer structure of a method for preparing a tire curing bladder in the present invention;
图3为本发明中一种轮胎硫化胶囊的制备方法的滤胶机结构示意图;Figure 3 is a schematic diagram of the structure of a rubber strainer of a method for preparing a tire curing bladder in the present invention;
图4为本发明中一种轮胎硫化胶囊的制备方法的密炼机和滤胶机间的状态示意图;4 is a schematic diagram of the state between the internal mixer and the rubber strainer in a method for preparing a tire curing bladder according to the present invention;
图5为实施例1中第一转子的示意性速度-时间图;5 is a schematic speed-time diagram of the first rotor in Embodiment 1;
图6为实施例1中第二转子的示意性速度-时间图;6 is a schematic speed-time diagram of the second rotor in Embodiment 1;
图7为实施例2中第一转子的示意性速度-时间图;Figure 7 is a schematic speed-time diagram of the first rotor in Embodiment 2;
图8为实施例2中第二转子的示意性速度-时间图;8 is a schematic speed-time diagram of the second rotor in Embodiment 2;
图9为实施例3中第一转子的示意性速度-时间图;9 is a schematic speed-time diagram of the first rotor in Embodiment 3;
图10为实施例3中第二转子的示意性速度-时间图;10 is a schematic speed-time diagram of the second rotor in Embodiment 3;
图11为实施例4中第一转子的示意性速度-时间图;11 is a schematic speed-time diagram of the first rotor in Embodiment 4;
图12为实施例4中第二转子的示意性速度-时间图。FIG. 12 is a schematic speed-time diagram of the second rotor in Embodiment 4. FIG.
1、上辅机,2、密炼机,3、滤胶机,4、开炼机,5、压片机,6、控制器,7、注射硫化机;1. Upper auxiliary machine, 2. Internal mixer, 3. Rubber strainer, 4. Open mill, 5. Tablet press, 6. Controller, 7. Injection vulcanizing machine;
201、密炼机外壳体,202、密炼室,203、第一转子,204、第二转子,205、上顶栓,206、上顶栓控杆,207、下压锤,208、加料斗,209、卸料阀,210、卸料门;201. Internal mixer housing, 202, mixing chamber, 203, first rotor, 204, second rotor, 205, upper bolt, 206, upper bolt lever, 207, lower hammer, 208, charging hopper , 209, discharge valve, 210, discharge gate;
301、齿轮泵,302、第一齿轮,303、第二齿轮,304、旋转门,305、排料口,306、排料管道,307、滤网。301, gear pump, 302, first gear, 303, second gear, 304, revolving door, 305, discharge port, 306, discharge pipe, 307, filter screen.
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, without substantial changes to the technical content, shall also be regarded as the scope of implementation of the invention.
参照附图1-12,一种轮胎硫化胶囊的制备方法,该轮胎硫化胶囊组分中,丁基橡胶100份,炭黑24-48份,白炭黑3-8份,三氧化二铝2-6份,氯丁橡胶6-8份,硬脂酸1-2.5份,石蜡1.5-3.4份,硫化树脂2-6份。1-12, a method for preparing tire curing bladder, the tire curing bladder components, 100 parts of butyl rubber, 24-48 parts of carbon black, 3-8 parts of white carbon black, 2 aluminum oxide -6 parts, 6-8 parts of chloroprene rubber, 1-2.5 parts of stearic acid, 1.5-3.4 parts of paraffin wax, 2-6 parts of vulcanized resin.
制备方法包括以下步骤:The preparation method includes the following steps:
S1、通过上辅机1向密炼机2中加入生胶,控制密炼机2中的第一转子203和第二转子204异步转动,密炼机2中温度为100-110℃,密炼时间1-2min;S1. The raw rubber is added to the internal mixer 2 through the upper auxiliary machine 1, and the first rotor 203 and the second rotor 204 in the internal mixer 2 are controlled to rotate asynchronously. The temperature in the internal mixer 2 is 100-110°C. Time 1-2min;
S2、通过上辅机1向密炼机2中加入活性剂、加工助剂和1/2补强填充剂,控制密炼机2中的第一转子203和第二转子204异步转动,密炼机2中温度为100-110℃,密炼时间1-2min;S2. Add the active agent, processing aid and 1/2 reinforcing filler to the internal mixer 2 through the upper auxiliary machine 1, and control the first rotor 203 and the second rotor 204 in the internal mixer 2 to rotate asynchronously, and the internal mixer The temperature in machine 2 is 100-110℃, and the mixing time is 1-2min;
S3、通过上辅机1向密炼机2中加入剩下的1/2补强填充剂,控制密炼机2中的第一转子203和第二转子204异步转动,密炼机2中温度为100-110℃,密炼时间1-2min,排出胶料,排胶温度为100-110℃;S3. Add the remaining 1/2 reinforcing filler to the internal mixer 2 through the upper auxiliary machine 1, and control the first rotor 203 and the second rotor 204 in the internal mixer 2 to rotate asynchronously, and the temperature in the internal mixer 2 It is 100-110℃, banbury time is 1-2min, the rubber material is discharged, and the glue discharge temperature is 100-110℃;
S4、S3中排出的胶料进入到滤胶机3中进行滤胶,排出的胶料加入到开炼机4中,控制开炼机4的温度为80-90℃,加入硫化剂,混炼2-5min后,将开炼机4中的胶料输送至压片机5中压出胶片,停放24h以上;The rubber material discharged in S4 and S3 enters the rubber filter 3 for rubber filtering, and the discharged rubber material is added to the open mill 4, and the temperature of the open mill 4 is controlled to 80-90°C. The vulcanizing agent is added and mixed After 2-5 minutes, convey the rubber material in the open mill 4 to the tablet press 5 to press out the film, and park it for more than 24 hours;
S5、将S4的胶片加入到注射硫化机7中,注射温度为150-185℃,硫化温度为185℃,硫化时间为15-25min,硫化完成,取出轮胎硫化胶囊;S5. Put the S4 film into the injection vulcanizer 7, the injection temperature is 150-185°C, the vulcanization temperature is 185°C, and the vulcanization time is 15-25min. After the vulcanization is completed, take out the tire curing bladder;
在S1、S2、S3中,第一转子203和第二转子204之间的转速比 按照0<t<300s的时间周期在1:1-1.25至1-1.25:1间交替变化。In S1, S2, and S3, the rotation speed ratio between the first rotor 203 and the second rotor 204 alternately changes from 1:1-1.25 to 1-1.25:1 in a time period of 0<t<300s.
轮胎硫化胶囊的制备方法所使用的轮胎硫化胶囊制备系统,包括:The tire curing bladder preparation system used in the preparation method of the tire curing bladder includes:
上辅机1用于称量物料、辅助加料,上辅机1位于密炼机2的上方;The upper auxiliary machine 1 is used for weighing materials and auxiliary feeding, and the upper auxiliary machine 1 is located above the internal mixer 2;
密炼机2用于生胶、补强填充剂、活性剂和加工助剂的混炼,密炼机2的加料斗208连接着上辅机1的出口,密炼机2的出口与滤胶机3的进口连接;The internal mixer 2 is used for mixing raw rubber, reinforcing fillers, active agents and processing aids. The hopper 208 of the internal mixer 2 is connected to the outlet of the upper auxiliary machine 1, and the outlet of the internal mixer 2 is connected to the rubber filter Inlet connection of machine 3;
滤胶机3使胶料内部的胶豆、团聚的填充剂破碎分散;滤胶机3的出口与开炼机4的进口连接;The rubber strainer 3 breaks and disperses the gum beans and the agglomerated filler inside the rubber material; the outlet of the rubber strainer 3 is connected with the inlet of the mill 4;
开炼机4对胶料进一步混炼;The open mixer 4 further mixes the rubber;
压片机5将不规则的胶料压成片状,压片机5的进口与开炼机4的出口连接;The tablet press 5 compresses the irregular rubber material into flakes, and the inlet of the tablet press 5 is connected with the outlet of the mill 4;
注射硫化机7用于对胶片加热、加热注射至模腔中定型硫化;The injection vulcanizing machine 7 is used to heat the film, heat and inject it into the mold cavity to shape and vulcanize;
上辅机1、密炼机2、滤胶机3、开炼机4、压片机5和注射硫化机7分别与控制器6连接。上辅机、密炼机、滤胶机、开炼机、压片机及控制器在使用中连接电气动力设备,这是设备应用中的公知常识,在本发明中不作详细说明。The upper auxiliary machine 1, the internal mixer 2, the rubber strainer 3, the open mill 4, the tablet press 5 and the injection vulcanizing machine 7 are respectively connected to the controller 6. The upper auxiliary machine, internal mixer, rubber strainer, open mixer, tablet press and controller are connected to electrical power equipment during use. This is common knowledge in equipment application and will not be described in detail in the present invention.
密炼机2中的第二转子204的转速:第一转子203的转速为1-1.25:1;S2中,密炼机2中的第一转子203的转速:第二转子204的转速为1-1.25:1;S3中,密炼机2中的第二转子204的转速:第一转子203的转速为1-1.25:1。The rotation speed of the second rotor 204 in the internal mixer 2: the rotation speed of the first rotor 203 is 1-1.25:1; in S2, the rotation speed of the first rotor 203 in the internal mixer 2: the rotation speed of the second rotor 204 is 1 -1.25:1; In S3, the rotation speed of the second rotor 204 in the internal mixer 2: the rotation speed of the first rotor 203 is 1-1.25:1.
进一步,所述的轮胎硫化胶囊制备系统中的密炼机2,外侧有密炼机外壳体201,内部有密炼室202,密炼室202内侧有第一转子203和第二转子204,在密炼室202的上方有上顶栓205,上顶栓205的 中间是中空腔体,内部有底部刚性连接下压锤207的上顶栓控杆206;上顶栓205的中部一侧开有开口向上的加料斗208,密炼室202的底部有卸料阀209,在密炼机外壳体201上设有卸料门210,卸料门210位于靠近滤胶机3的一侧;Further, the internal mixer 2 in the tire curing bladder preparation system has an external mixer housing 201 on the outside, a mixing chamber 202 inside, and a first rotor 203 and a second rotor 204 inside the mixing chamber 202. There is an upper bolt 205 above the mixing chamber 202, a hollow cavity in the middle of the upper bolt 205, and an upper bolt control rod 206 rigidly connected to the lower hammer 207 at the bottom; the middle side of the upper bolt 205 is opened A hopper 208 with upward opening, a discharge valve 209 at the bottom of the internal mixing chamber 202, a discharge door 210 is provided on the external mixer housing 201, and the discharge door 210 is located on the side close to the rubber strainer 3;
滤胶机3的前端是齿轮泵301,齿轮泵301内部有相互啮合的第一齿轮302和第二齿轮303,齿轮泵301靠近密炼机2的一侧设有旋转门304,在远离密炼机2的一侧设有排料口305,排料口305连接着排料管道306,排料管道306的内部安装着滤网307。The front end of the rubber strainer 3 is a gear pump 301. The gear pump 301 has a first gear 302 and a second gear 303 that mesh with each other. The side of the gear pump 301 close to the internal mixer 2 is provided with a revolving door 304. A discharge port 305 is provided on one side of the machine 2, the discharge port 305 is connected to a discharge pipe 306, and a filter 307 is installed inside the discharge pipe 306.
实施例1-4的配方如表1,按重量份计。制备步骤和所使用的轮胎硫化胶囊制备系统参照本发明的技术方案,制备步骤中的工艺条件存在不同。The formulations of Examples 1-4 are shown in Table 1, in parts by weight. The preparation steps and the used tire curing bladder preparation system refer to the technical scheme of the present invention, and the process conditions in the preparation steps are different.
表1实施例1-4的配方表Table 1 Formulations of Examples 1-4
 To 实施例1Example 1 实施例2Example 2 实施例3Example 3 实施例4Example 4
丁基橡胶/份Butyl rubber/part 100100 100100 100100 100100
炭黑/份Carbon black/part 24twenty four 24twenty four 4848 4848
白炭黑/份White carbon black/part 33 44 66 88
三氧化二铝/份Aluminum oxide/part 33 22 66 44
硬脂酸/份Stearic acid/part 11 1.51.5 1.61.6 22
石蜡/份Paraffin/part 22 1.51.5 3.23.2 33
硫化树脂/份Vulcanized resin/part 22 22 44 66
氯丁橡胶/份Neoprene/part 66 66 77 88
实施例1中,S1、S2和S3之间的密炼时间相等,第一转子203和第二转子204之间的转速比交替变化的时间周期等于步骤S1的密炼时间。S1中,密炼机2中的第一转子203的转速:第二转子204的转速为1-1.25∶1;S2中,密炼机2中的第二转子204的转速:第一转子203的转速为1-1.25∶1;S3中,密炼机2中的第一转子203 的转速:第二转子204的转速为1-1.25:1。第一转子203和第二转子204的速度随时间的变化呈正半波交替变化,波形是三角波,二者之间的速度变化正好差半个时间周期。In Embodiment 1, the mixing time between S1, S2 and S3 is equal, and the time period during which the rotation speed ratio between the first rotor 203 and the second rotor 204 alternately changes is equal to the mixing time of step S1. In S1, the rotation speed of the first rotor 203 in the internal mixer 2: the rotation speed of the second rotor 204 is 1-1.25:1; in S2, the rotation speed of the second rotor 204 in the internal mixer 2: the rotation speed of the first rotor 203 The speed is 1-1.25:1; in S3, the speed of the first rotor 203 in the internal mixer 2: the speed of the second rotor 204 is 1-1.25:1. The speed of the first rotor 203 and the second rotor 204 change with time in a positive half-wave alternately, the waveform is a triangular wave, and the speed change between the two is exactly half a time period.
在图5和图6中,v1是最小的速度,v2是最大的速度,v2是v1的1.25倍。在t0-t1之间,第一转子203的转速从v1加速至v2,再从v2降至v1;第二转子204的转速始终为v1;在t1-t2之间,第一转子203的转速始终为v1,第二转子204的转速从v1加速至v2,再从v2降至v1;接下来的t2-t4与t0-t2速度变化相同,t0-t2为一个时间周期;第一转子203和第二转子204之间的转速比呈现周期性交替变化,而时间周期t0-t2恰好与S1密炼时间相等,为2min。In Figures 5 and 6, v1 is the minimum speed, v2 is the maximum speed, and v2 is 1.25 times of v1. Between t0-t1, the speed of the first rotor 203 accelerates from v1 to v2, and then from v2 to v1; the speed of the second rotor 204 is always v1; between t1-t2, the speed of the first rotor 203 is always Is v1, the speed of the second rotor 204 accelerates from v1 to v2, and then from v2 to v1; the following t2-t4 and t0-t2 speed changes are the same, t0-t2 is a time period; the first rotor 203 and the first The rotation speed ratio between the two rotors 204 presents a periodic alternating change, and the time period t0-t2 is exactly the same as the S1 banburying time, which is 2 min.
实施例2:S1、S2和S3之间的密炼时间相等,第一转子203和第二转子204之间的转速比交替变化的时间周期等于步骤S1的密炼时间。S1中,密炼机2中的第二转子204的转速:第一转子203的转速为1.10:1;S2中,密炼机2中的第一转子203的转速:第二转子204的转速为1.10:1;S3中,密炼机2中的第二转子204的转速:第一转子203的转速为1.10:1。第一转子203和第二转子204的速度随时间的变化呈正半波交替变化,波形是矩形波,此时,v1和v2之间相差不宜过大,二者之间的速度变化正好差半个时间周期。Embodiment 2: The mixing time between S1, S2 and S3 is equal, and the time period during which the rotation speed ratio between the first rotor 203 and the second rotor 204 alternately changes is equal to the mixing time of step S1. In S1, the rotation speed of the second rotor 204 in the internal mixer 2: the rotation speed of the first rotor 203 is 1.10:1; in S2, the rotation speed of the first rotor 203 in the internal mixer 2: the rotation speed of the second rotor 204 is 1.10:1; in S3, the rotation speed of the second rotor 204 in the internal mixer 2: the rotation speed of the first rotor 203 is 1.10:1. The speed of the first rotor 203 and the second rotor 204 change with time in a positive half-wave alternately, and the waveform is a rectangular wave. At this time, the difference between v1 and v2 should not be too large, and the speed change between the two is exactly half a difference Time period.
在图7和图8中,v1是最小的速度,v2是最大的速度,v2是v1的1.10倍。在t0-t1之间,第一转子203的转速始终为v1,第二转子204的转速始终为v2;在t1-t2之间,第一转子203的转速始终为v2,第二转子204的转速始终为v1;接下来的t2-t4与t0-t2速度变化相同,第一转子203和第二转子204之间的转速比呈现周期性交替变化,而时间周期t0-t2恰好与S1密炼时间相等,为2min。In Figures 7 and 8, v1 is the minimum speed, v2 is the maximum speed, and v2 is 1.10 times that of v1. Between t0-t1, the speed of the first rotor 203 is always v1, and the speed of the second rotor 204 is always v2; between t1 and t2, the speed of the first rotor 203 is always v2, and the speed of the second rotor 204 It is always v1; the following t2-t4 and t0-t2 speed changes are the same, the speed ratio between the first rotor 203 and the second rotor 204 presents a periodic alternate change, and the time period t0-t2 coincides with the S1 mixing time It is equal to 2min.
实施例3:第一转子203和第二转子204的速度随时间的变化呈 正半波交替变化,波形是正弦波,二者之间的速度变化正好差半个时间周期。Embodiment 3: The speed of the first rotor 203 and the second rotor 204 change with time in a positive half wave alternately, the waveform is a sine wave, and the speed change between the two is exactly half a time period.
在图9和图10中,v1是最小的速度,v2是最大的速度,v2是v1的1.25倍。在t0-t1之间,第一转子203的转速始终为v1,第二转子204的转速从v1加速至v2,再从v2降至v1;在t1-t2之间,第一转子203的转速从v1加速至v2,再从v2降至v1,第二转子204的转速始终为v1;接下来的t2-t4与t0-t2速度变化相同,t0-t2为一个时间周期;第一转子203和第二转子204之间的转速比呈现周期性交替变化,时间周期为1min。In Figure 9 and Figure 10, v1 is the minimum speed, v2 is the maximum speed, and v2 is 1.25 times of v1. Between t0-t1, the speed of the first rotor 203 is always v1, and the speed of the second rotor 204 accelerates from v1 to v2, and then from v2 to v1; between t1-t2, the speed of the first rotor 203 changes from v1 accelerates to v2, and then from v2 to v1, the speed of the second rotor 204 is always v1; the following t2-t4 and t0-t2 have the same speed change, t0-t2 is a time period; the first rotor 203 and the first rotor 203 The rotation speed ratio between the two rotors 204 presents a periodic alternate change, and the time period is 1 min.
实施例4:第一转子203和第二转子204的速度随时间的变化呈正半波交替变化,波形是梯形波,二者之间的速度变化正好差1/4个时间周期。Embodiment 4: The speed of the first rotor 203 and the second rotor 204 change with time in a positive half-wave alternately, the waveform is a trapezoidal wave, and the speed change between the two is exactly 1/4 time period.
在图11和图12中,v1是最小的速度,v2是最大的速度,v2是v1的1.25倍。在t0-t1之间,第一转子203的转速始终为v2,第二转子204的转速始终为v1;在t1-t2之间,第一转子203的转速从v2降至v1,第二转子204的转速从v1加速至v2;在t2-t3之间,第一转子203的转速始终为v1,第二转子204的转速始终为v2;在在t3-t4之间,第一转子203的转速从v1加速至v2,第二转子204的转速从v2降至v1;接下来的t4-t5与t0-t1速度变化相同,开始新的周期;t0-t4为一个时间周期;第一转子203和第二转子204之间的转速比呈现周期性交替变化,时间周期为4min。In Figure 11 and Figure 12, v1 is the minimum speed, v2 is the maximum speed, and v2 is 1.25 times of v1. Between t0-t1, the speed of the first rotor 203 is always v2, and the speed of the second rotor 204 is always v1; between t1 and t2, the speed of the first rotor 203 decreases from v2 to v1, and the second rotor 204 The speed accelerates from v1 to v2; between t2-t3, the speed of the first rotor 203 is always v1, and the speed of the second rotor 204 is always v2; between t3-t4, the speed of the first rotor 203 is from v1 accelerates to v2, and the speed of the second rotor 204 decreases from v2 to v1; the following t4-t5 changes the same speed as t0-t1, and a new cycle starts; t0-t4 is a time period; the first rotor 203 and the first rotor 203 The rotation speed ratio between the two rotors 204 presents a periodic and alternate change, and the time period is 4 min.
对按照实施例1-4的方法制备的胶片,在平板硫化机上进行硫化,胶片厚度4mm,硫化温度为185℃,硫化时间20min,放置24h后,制样并进行力学性能测试。The film prepared according to the method of Examples 1-4 was vulcanized on a plate vulcanizer, the film thickness was 4mm, the vulcanization temperature was 185°C, the vulcanization time was 20min, and after 24h, samples were prepared and the mechanical properties were tested.
检测标准及设备:Testing standards and equipment:
①邵氏硬度:检测标准GB/T531-2008;检测设备采用上海险峰电影机械厂的LX-A硬度计。①Shore hardness: testing standard GB/T531-2008; testing equipment adopts LX-A hardness tester from Shanghai Xianfeng Film Machinery Factory.
②拉伸性能:检测标准GB/T528-2009,样品是哑铃型的,测试速度为500mm/min,测试环境温度是23±2℃;检测设备采用台湾高铁科技股份有限公司的GT-TCS-2000拉力试验机。②Tensile performance: testing standard GB/T528-2009, the sample is dumbbell-shaped, testing speed is 500mm/min, testing environment temperature is 23±2℃; testing equipment adopts GT-TCS-2000 of Taiwan High Speed Rail Technology Co., Ltd. Tensile testing machine.
③撕裂强度:检测标准GB/T529-2008,采用直角形试样,测试速度为500mm/min,测试环境温度为23±2℃;检测设备采用台湾高铁科技股份有限公司的GT-TCS-2000拉力试验机。③Tear strength: testing standard GB/T529-2008, using right-angled specimens, testing speed 500mm/min, testing environment temperature 23±2℃; testing equipment adopts GT-TCS-2000 of Taiwan High Speed Rail Technology Co., Ltd. Tensile testing machine.
测试结果见表2。The test results are shown in Table 2.
表2实施例1-4制作出的胶片的力学性能测试数据表Table 2 Test data table of mechanical properties of films produced in Examples 1-4
Figure PCTCN2019127819-appb-000001
Figure PCTCN2019127819-appb-000001
根据表2可以看出,采用本发明中的技术方案制备的胶片在拉伸强度、扯断伸长率、撕裂强度等性能优异;说明采用本发明中的技术方案,胶料混炼效果好,胶料均匀,可以制备出力学性能更优的轮胎硫化胶囊。It can be seen from Table 2 that the film prepared by the technical scheme of the present invention has excellent properties such as tensile strength, elongation at break, and tear strength; it shows that the technical scheme of the present invention has good rubber mixing effect. , The rubber material is uniform, and tire curing bladder with better mechanical properties can be prepared.
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 (10)

  1. 一种轮胎硫化胶囊的制备方法,轮胎硫化胶囊的组分包括:生胶、补强填充剂、活性剂、加工助剂、硫化剂,其特征在于,A method for preparing a tire curing bladder. The components of the tire curing bladder include: raw rubber, reinforcing filler, active agent, processing aid, and curing agent, characterized in that:
    该轮胎硫化胶囊组分中,生胶是丁基橡胶;补强填充剂包括:炭黑、白炭黑和三氧化二铝;活性剂是氯丁橡胶;加工助剂包括:硬脂酸、石蜡;硫化剂是硫化树脂;In the tire curing bladder component, the raw rubber is butyl rubber; the reinforcing filler includes: carbon black, white carbon black and aluminum oxide; the active agent is neoprene; the processing aid includes: stearic acid, paraffin wax ; The vulcanizing agent is a vulcanized resin;
    制备方法包括以下步骤:The preparation method includes the following steps:
    S1、通过上辅机(1)向密炼机(2)中加入生胶,控制密炼机(2)中的第一转子(203)和第二转子(204)异步转动,密炼机(2)中温度为100-110℃,密炼时间1-2min;S1. Add raw rubber to the internal mixer (2) through the upper auxiliary machine (1), control the first rotor (203) and the second rotor (204) in the internal mixer (2) to rotate asynchronously, and the internal mixer ( 2) The medium temperature is 100-110℃, and the banburying time is 1-2min;
    S2、通过上辅机(1)向密炼机(2)中加入活性剂、加工助剂和1/2补强填充剂,控制密炼机(2)中的第一转子(203)和第二转子(204)异步转动,密炼机(2)中温度为100-110℃,密炼时间1-2min;S2. Add the active agent, processing aid and 1/2 reinforcing filler to the internal mixer (2) through the upper auxiliary machine (1), and control the first rotor (203) and the first rotor (203) in the internal mixer (2) The second rotor (204) rotates asynchronously, the temperature in the internal mixer (2) is 100-110℃, and the mixing time is 1-2min;
    S3、通过上辅机(1)向密炼机(2)中加入剩下的1/2补强填充剂,控制密炼机(2)中的第一转子(203)和第二转子(204)异步转动,密炼机(2)中温度为100-110℃,密炼时间1-2min,排出胶料,排胶温度为100-110℃;S3. Add the remaining 1/2 reinforcing filler to the internal mixer (2) through the upper auxiliary machine (1), and control the first rotor (203) and the second rotor (204) in the internal mixer (2) ) Asynchronous rotation, the temperature in the internal mixer (2) is 100-110℃, the mixing time is 1-2min, the rubber material is discharged, and the rubber discharge temperature is 100-110℃;
    S4、S3中排出的胶料进入到滤胶机(3)中进行滤胶,排出的胶料加入到开炼机(4)中,控制开炼机(4)的温度为80-90℃,加入硫化剂,混炼2-5min后,将开炼机(4)中的胶料输送至压片机(5)中压出胶片,停放24h以上;The rubber material discharged in S4 and S3 enters the rubber filter (3) for rubber filtering, and the discharged rubber material is added to the open mill (4), and the temperature of the open mill (4) is controlled to 80-90°C, After adding vulcanizing agent and mixing for 2-5 minutes, transport the rubber material in the open mill (4) to the tablet press (5) to press out the film, and then park for more than 24 hours;
    S5、将S4的胶片加入到注射硫化机(7)中,注射温度为150-185℃,硫化温度为185℃,硫化时间为15-25min,硫化完成,取出轮胎硫化胶囊;S5. Put the S4 film into the injection vulcanizing machine (7), the injection temperature is 150-185°C, the vulcanization temperature is 185°C, the vulcanization time is 15-25min, the vulcanization is completed, and the tire curing bladder is taken out;
    在S1、S2、S3中,第一转子(203)和第二转子(204)之间的转速比按照0<t<300s的时间周期在1:(1-1.25)至(1-1.25):1间交替变化;In S1, S2, and S3, the speed ratio between the first rotor (203) and the second rotor (204) is 1: (1-1.25) to (1-1.25) according to a time period of 0<t<300s: 1 alternately;
    轮胎硫化胶囊的制备方法所使用的轮胎硫化胶囊制备系统,包括:The tire curing bladder preparation system used in the preparation method of the tire curing bladder includes:
    上辅机(1)用于称量物料、辅助加料,上辅机(1)位于密炼机(2)的上方;The upper auxiliary machine (1) is used for weighing materials and auxiliary feeding, and the upper auxiliary machine (1) is located above the internal mixer (2);
    密炼机(2)用于生胶、补强填充剂、活性剂和加工助剂的混炼,密炼机(2)的加料斗(208)连接着上辅机(1)的出口,密炼机(2)的出口与滤胶机(3)的进口连接;The internal mixer (2) is used for mixing raw rubber, reinforcing fillers, active agents and processing aids. The feeding hopper (208) of the internal mixer (2) is connected to the outlet of the upper auxiliary machine (1). The outlet of the mixing mill (2) is connected with the inlet of the rubber strainer (3);
    滤胶机(3)使胶料内部的胶豆、团聚的填充剂破碎分散;滤胶机(3)的出口与开炼机(4)的进口连接;The rubber strainer (3) crushes and disperses the gum beans and agglomerated filler inside the rubber compound; the outlet of the rubber strainer (3) is connected with the inlet of the mill (4);
    开炼机(4)对胶料进一步混炼;The open mixer (4) further mixes the rubber;
    压片机(5)将不规则的胶料压成片状,压片机(5)的进口与开炼机(4)的出口连接;The tablet press (5) compresses the irregular rubber material into flakes, and the inlet of the tablet press (5) is connected with the outlet of the open mill (4);
    注射硫化机(7)用于对胶片加热、加热注射至模腔中定型硫化;The injection vulcanizing machine (7) is used to heat the film, heat and inject it into the mold cavity to shape and vulcanize;
    上辅机(1)、密炼机(2)、滤胶机(3)、开炼机(4)、压片机(5)和注射硫化机(7)分别与控制器(6)连接。The upper auxiliary machine (1), internal mixer (2), rubber filter (3), open mill (4), tablet press (5) and injection vulcanizer (7) are respectively connected with the controller (6).
  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,生胶100份,补强填充剂30-60份,活性剂6-8份,加工助剂3-5份,硫化剂2-6份。The method for preparing a tire curing bladder according to claim 1, wherein 100 parts of raw rubber, 30-60 parts of reinforcing fillers, 6-8 parts of active agents, 3-5 parts of processing aids, vulcanization Agent 2-6 parts.
  3. 根据权利要求2所述的一种轮胎硫化胶囊的制备方法,其特征在于,补强填充剂中,炭黑、白炭黑和三氧化二铝之间的配比是(8-12):(1-2):1。The method for preparing a tire curing bladder according to claim 2, wherein in the reinforcing filler, the ratio of carbon black, white carbon black and aluminum oxide is (8-12): ( 1-2):1.
  4. 根据权利要求2所述的一种轮胎硫化胶囊的制备方法,其特征 在于,加工助剂中,硬脂酸和石蜡之间的配比是1:(1-2)。The method for preparing a tire curing bladder according to claim 2, characterized in that, in the processing aid, the ratio of stearic acid and paraffin wax is 1: (1-2).
  5. 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,第一转子(203)和第二转子(204)的速度随时间的变化呈正半波交替变化,波形是正弦波、三角波、矩形波或者梯形波中的一种。The method for preparing a tire curing bladder according to claim 1, wherein the speed of the first rotor (203) and the second rotor (204) change with time in a positive half-wave alternately, and the waveform is a sine wave, One of triangular wave, rectangular wave or trapezoidal wave.
  6. 根据权利要求5所述的一种轮胎硫化胶囊的制备方法,其特征在于,S1、S2和S3之间的密炼时间相等,第一转子(203)和第二转子(204)之间的转速比交替变化的时间周期等于步骤S1的密炼时间。The method for preparing a tire curing bladder according to claim 5, characterized in that the mixing time between S1, S2 and S3 is equal, and the rotation speed between the first rotor (203) and the second rotor (204) The time period during which the ratio alternately changes is equal to the banburying time in step S1.
  7. 根据权利要求6所述的一种轮胎硫化胶囊的制备方法,其特征在于,S1中,密炼机(2)中的第一转子(203)的转速:第二转子(204)的转速为(1-1.25):1;S2中,密炼机(2)中的第二转子(204)的转速:第一转子(203)的转速为(1-1.25):1;S3中,密炼机(2)中的第一转子(203)的转速:第二转子(204)的转速为(1-1.25):1。The method for preparing a tire curing bladder according to claim 6, characterized in that, in S1, the speed of the first rotor (203) in the internal mixer (2): the speed of the second rotor (204) is ( 1-1.25):1; in S2, the rotation speed of the second rotor (204) in the internal mixer (2): the rotation speed of the first rotor (203) is (1-1.25):1; in S3, the internal mixer The rotation speed of the first rotor (203) in (2): the rotation speed of the second rotor (204) is (1-1.25):1.
  8. 根据权利要求7所述的一种轮胎硫化胶囊的制备方法,其特征在于,S1中,密炼机(2)中的第一转子(203)的转速:第二转子(204)的转速为(1-1.10):1;S2中,密炼机(2)中的第二转子(204)的转速:第一转子(203)的转速为(1-1.10):1;S3中,密炼机(2)中的第一转子(203)的转速:第二转子(204)的转速为(1-1.10):1。The method for preparing a tire curing bladder according to claim 7, characterized in that, in S1, the rotation speed of the first rotor (203) in the internal mixer (2): the rotation speed of the second rotor (204) is ( 1-1.10):1; in S2, the speed of the second rotor (204) in the internal mixer (2): the speed of the first rotor (203) is (1-1.10):1; in S3, the internal mixer The rotation speed of the first rotor (203) in (2): the rotation speed of the second rotor (204) is (1-1.10):1.
  9. 根据权利要求6所述的一种轮胎硫化胶囊的制备方法,其特征在于,S1中,密炼机(2)中的第二转子(204)的转速:第一转子(203)的转速为(1-1.25):1;S2中,密炼机(2)中的第一转子(203)的转速:第二转子(204)的转速为(1-1.25):1;S3中,密炼机(2)中的第二转子(204)的转速:第一转子(203)的转速 为(1-1.25):1。The method for preparing a tire curing bladder according to claim 6, characterized in that, in S1, the rotation speed of the second rotor (204) in the internal mixer (2): the rotation speed of the first rotor (203) is ( 1-1.25):1; in S2, the speed of the first rotor (203) in the internal mixer (2): the speed of the second rotor (204) is (1-1.25):1; in S3, the internal mixer The rotation speed of the second rotor (204) in (2): the rotation speed of the first rotor (203) is (1-1.25):1.
  10. 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,The method for preparing a tire curing bladder according to claim 1, wherein:
    所述的轮胎硫化胶囊制备系统中的密炼机(2),外侧有密炼机外壳体(201),内部有密炼室(202),密炼室(202)内侧有第一转子(203)和第二转子(204),在密炼室(202)的上方有上顶栓(205),上顶栓(205)的中间是中空腔体,内部有底部刚性连接下压锤(207)的上顶栓控杆(206);上顶栓(205)的中部一侧开有开口向上的加料斗(208),密炼室(202)的底部有卸料阀(209),在密炼机外壳体(201)上设有卸料门(210),卸料门(210)位于靠近滤胶机(3)的一侧;The internal mixer (2) in the tire curing bladder preparation system has an external mixer outer shell (201), an internal mixing chamber (202), and a first rotor (203) inside the internal mixing chamber (202). ) And the second rotor (204), above the mixing chamber (202) there is an upper top bolt (205), the middle of the upper top bolt (205) is a hollow cavity, and the bottom is rigidly connected to the lower hammer (207) inside The upper bolt control rod (206) of the upper bolt (205) is opened with an upward hopper (208) on the middle side of the upper bolt (205), and there is a discharge valve (209) at the bottom of the mixing chamber (202). A discharge door (210) is provided on the outer casing (201) of the machine, and the discharge door (210) is located on the side close to the rubber strainer (3);
    滤胶机(3)的前端是齿轮泵(301),齿轮泵(301)内部有相互啮合的第一齿轮(302)和第二齿轮(303),齿轮泵(301)靠近密炼机(2)的一侧设有旋转门(304),在远离密炼机(2)的一侧设有排料口(305),排料口(305)连接着排料管道(306),排料管道(306)的内部安装着滤网(307)。The front end of the rubber strainer (3) is a gear pump (301). The gear pump (301) has a first gear (302) and a second gear (303) that mesh with each other. The gear pump (301) is close to the internal mixer (2). ) Is provided with a revolving door (304), on the side far from the internal mixer (2) is provided with a discharge port (305), the discharge port (305) is connected to a discharge pipe (306), and a discharge pipe A filter screen (307) is installed inside (306).
PCT/CN2019/127819 2019-11-11 2019-12-24 Method for preparing tire curing bladder WO2021093101A1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
CN201911094326.4A CN110713663B (en) 2019-11-11 2019-11-11 Preparation method of tire curing bladder
CN201911094326.4 2019-11-11

Publications (1)

Publication Number Publication Date
WO2021093101A1 true WO2021093101A1 (en) 2021-05-20

Family

ID=69215827

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/CN2019/127819 WO2021093101A1 (en) 2019-11-11 2019-12-24 Method for preparing tire curing bladder

Country Status (2)

Country Link
CN (1) CN110713663B (en)
WO (1) WO2021093101A1 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111055509A (en) * 2019-12-16 2020-04-24 河北莫申科技有限公司 Manufacturing method of inflatable sealing ring
CN116373197B (en) * 2023-04-19 2023-11-07 苏州恒则成智能科技有限公司 Rubber production equipment and method

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2016113584A (en) * 2014-12-17 2016-06-23 住友ゴム工業株式会社 Rubber composition for bladder and manufacturing method therefor, and bladder
CN105968593A (en) * 2016-05-30 2016-09-28 德州玲珑轮胎有限公司 Tire vulcanization bladder and production method thereof
CN108162226A (en) * 2017-12-25 2018-06-15 山东西水永橡胶有限公司 A kind of preparation method of high heat conduction type tire curing bladder

Family Cites Families (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5782560A (en) * 1996-06-24 1998-07-21 Kabushiki Kaisha Kobe Seiko Sho Internal mixer
KR100483325B1 (en) * 1998-09-17 2005-09-02 한국타이어 주식회사 Rotor Speed Control Method of Rubber Mixer
CN102166794B (en) * 2011-01-25 2013-02-20 青岛科技大学 Rubber continuous mixing dual-rotor structure and mixing equipment adopting same
CN102225317A (en) * 2011-06-10 2011-10-26 北京化工大学 Double-conical-rotor continuous mixing unit
US9259856B2 (en) * 2011-07-12 2016-02-16 Toyo Tire & Rubber Co., Ltd. Methods for controlling the mixing process of processing rubber
CN103302755A (en) * 2013-07-01 2013-09-18 三角(威海)华盛轮胎有限公司 Thermostatic mixing method of internal mixer
CN106273043B (en) * 2016-08-25 2019-04-09 特拓(青岛)轮胎技术有限公司 A kind of calendering process for large capacity mixer production finished composition
CN106113303B (en) * 2016-08-26 2019-04-23 青岛科技大学 A kind of tetragonous sawtooth pattern dynamic Varied clearance closed-smelting machine rotor
CN109385015A (en) * 2018-11-01 2019-02-26 永橡胶有限公司 A kind of preparation method improving tire curing bladder production security

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2016113584A (en) * 2014-12-17 2016-06-23 住友ゴム工業株式会社 Rubber composition for bladder and manufacturing method therefor, and bladder
CN105968593A (en) * 2016-05-30 2016-09-28 德州玲珑轮胎有限公司 Tire vulcanization bladder and production method thereof
CN108162226A (en) * 2017-12-25 2018-06-15 山东西水永橡胶有限公司 A kind of preparation method of high heat conduction type tire curing bladder

Also Published As

Publication number Publication date
CN110713663B (en) 2021-11-12
CN110713663A (en) 2020-01-21

Similar Documents

Publication Publication Date Title
WO2021093101A1 (en) Method for preparing tire curing bladder
CN108162226A (en) A kind of preparation method of high heat conduction type tire curing bladder
CN110722703B (en) Low-temperature continuous mixing production method for rubber
CN109181040A (en) A kind of preparation method of Rubber shock-absorbing pad
CN111376506A (en) Rubber tire manufacturing process
CN110815887B (en) Production method of tire curing bladder
CN113462018A (en) Method and device for regenerating waste rubber
CN206011665U (en) A kind of polyvinyl chloride raw material prepares extrusion device
CN208035052U (en) A kind of plastic processing mixing device
CN110802786A (en) Preparation method of tire curing bladder rubber material
CN211164797U (en) Preparation system of tire curing bladder sizing material
CN207327567U (en) A kind of adjustable Rubber Extruder of temperature
CN110483904A (en) Sizing material used for sealing gasket, gasket seal and preparation method thereof and the heat-exchangers of the plate type including the gasket seal
CN110815618A (en) Preparation method of tire curing bladder
CN206436402U (en) It is a kind of to be used for the banbury of rubber plastic steelmaking and mixing
US20230089028A1 (en) Apparatus and method for mixing elastomeric materials
CN111205527A (en) Production process and device of rubber sealing ring
CN108972930A (en) A kind of production thermoplastic polyurethane elastomer metering pre-mixing apparatus
CN206899708U (en) A kind of double-screw type extruder
CN209682663U (en) Plastics-production agitating device
CN211030769U (en) Continuous banburying system of sizing material for tire curing bladder
CN111421690B (en) Pretreatment processing method of rubber and plastic heat-insulating material
CN204555597U (en) Continous vacuum low-temperature microwave drying device
CN108582560A (en) A kind of rubber and plastic processing raw material kneading device
CN216266957U (en) Rubber tire internal mixer device

Legal Events

Date Code Title Description
121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 19952829

Country of ref document: EP

Kind code of ref document: A1

NENP Non-entry into the national phase

Ref country code: DE

122 Ep: pct application non-entry in european phase

Ref document number: 19952829

Country of ref document: EP

Kind code of ref document: A1