CN101724172B - Industrial production method for ethylene propylene diene rubber molded sealed cell sponge rubber - Google Patents
Industrial production method for ethylene propylene diene rubber molded sealed cell sponge rubber Download PDFInfo
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- CN101724172B CN101724172B CN2009102326809A CN200910232680A CN101724172B CN 101724172 B CN101724172 B CN 101724172B CN 2009102326809 A CN2009102326809 A CN 2009102326809A CN 200910232680 A CN200910232680 A CN 200910232680A CN 101724172 B CN101724172 B CN 101724172B
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- 229920001971 elastomer Polymers 0.000 title claims abstract description 73
- 239000005060 rubber Substances 0.000 title claims abstract description 73
- 229920002943 EPDM rubber Polymers 0.000 title claims abstract description 18
- 238000000034 method Methods 0.000 title abstract description 12
- 238000009776 industrial production Methods 0.000 title abstract description 9
- 239000000463 material Substances 0.000 claims abstract description 26
- 238000002156 mixing Methods 0.000 claims abstract description 25
- 238000004073 vulcanization Methods 0.000 claims abstract description 25
- 238000005187 foaming Methods 0.000 claims abstract description 23
- 239000003795 chemical substances by application Substances 0.000 claims abstract description 18
- 239000004088 foaming agent Substances 0.000 claims abstract description 18
- 238000007670 refining Methods 0.000 claims abstract description 13
- 239000006229 carbon black Substances 0.000 claims abstract description 12
- 238000004519 manufacturing process Methods 0.000 claims abstract description 12
- 238000000465 moulding Methods 0.000 claims abstract description 10
- 230000003712 anti-aging effect Effects 0.000 claims abstract description 9
- 239000006260 foam Substances 0.000 claims abstract description 6
- XLOMVQKBTHCTTD-UHFFFAOYSA-N Zinc monoxide Chemical compound [Zn]=O XLOMVQKBTHCTTD-UHFFFAOYSA-N 0.000 claims description 16
- 239000003292 glue Substances 0.000 claims description 11
- 239000011787 zinc oxide Substances 0.000 claims description 8
- QIQXTHQIDYTFRH-UHFFFAOYSA-N octadecanoic acid Chemical compound CCCCCCCCCCCCCCCCCC(O)=O QIQXTHQIDYTFRH-UHFFFAOYSA-N 0.000 claims description 7
- 238000003825 pressing Methods 0.000 claims 6
- 229920001897 terpolymer Polymers 0.000 claims 6
- 238000004513 sizing Methods 0.000 claims 5
- 238000005516 engineering process Methods 0.000 claims 4
- 239000011230 binding agent Substances 0.000 claims 2
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 claims 1
- 230000000994 depressogenic effect Effects 0.000 claims 1
- 229910052717 sulfur Inorganic materials 0.000 claims 1
- 239000011593 sulfur Substances 0.000 claims 1
- 239000012752 auxiliary agent Substances 0.000 abstract description 3
- 239000011148 porous material Substances 0.000 description 7
- 235000021355 Stearic acid Nutrition 0.000 description 5
- 238000009413 insulation Methods 0.000 description 5
- 238000004898 kneading Methods 0.000 description 5
- OQCDKBAXFALNLD-UHFFFAOYSA-N octadecanoic acid Natural products CCCCCCCC(C)CCCCCCCCC(O)=O OQCDKBAXFALNLD-UHFFFAOYSA-N 0.000 description 5
- 239000008117 stearic acid Substances 0.000 description 5
- 230000000694 effects Effects 0.000 description 4
- 230000001737 promoting effect Effects 0.000 description 4
- 230000007306 turnover Effects 0.000 description 4
- 238000010521 absorption reaction Methods 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 229920001821 foam rubber Polymers 0.000 description 2
- 239000004033 plastic Substances 0.000 description 2
- 238000002360 preparation method Methods 0.000 description 2
- 239000004604 Blowing Agent Substances 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 238000010009 beating Methods 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 239000004020 conductor Substances 0.000 description 1
- 238000004043 dyeing Methods 0.000 description 1
- 239000013013 elastic material Substances 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 230000020169 heat generation Effects 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000005342 ion exchange Methods 0.000 description 1
- 238000010077 mastication Methods 0.000 description 1
- 230000018984 mastication Effects 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000007639 printing Methods 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 230000035939 shock Effects 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
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Abstract
一种三元乙丙橡胶模压闭孔海绵胶的工业生产方法,涉及高发泡倍率发泡材料的工业制备方法。包括生胶的塑炼、混炼、精炼、发泡硫化成型,其特征在于:混炼时加入炭黑、环烷油、发泡助剂、硫化促进剂和防老剂进行混炼;精炼时加入发泡剂Ac和硫化剂进行精炼;发泡硫化成型的硫化条件为:压力15~20MPa,温度160~180℃,硫化时间3000~3500s。本发明是基于市场需求研发,使得研究目的从实验室研究转向了工业化的研究,能够使生产条件可控,生产过程比较稳定。本发明选用国产胶料,选用发泡剂Ac替代发泡剂H,通过调整配方中各种助剂的配比和工艺条件的控制能够制备符合工业化生产要求的EPDM模压海绵胶制品。The invention relates to an industrial production method of EPDM rubber molded closed-cell sponge rubber, which relates to an industrial production method of high expansion ratio foaming materials. Including plasticizing, mixing, refining, foaming vulcanization molding of raw rubber, characterized in that: carbon black, naphthenic oil, foaming aid, vulcanization accelerator and anti-aging agent are added during mixing; Foaming agent Ac and vulcanizing agent are refined; the vulcanization conditions of foam vulcanization molding are: pressure 15-20MPa, temperature 160-180°C, vulcanization time 3000-3500s. The invention is researched and developed based on market demand, so that the research purpose is shifted from laboratory research to industrial research, and the production conditions can be controlled, and the production process is relatively stable. The present invention selects domestic rubber material, selects foaming agent Ac to replace foaming agent H, and can prepare EPDM molded sponge rubber products that meet industrial production requirements by adjusting the ratio of various auxiliary agents in the formula and controlling the process conditions.
Description
技术领域 technical field
本发明涉及一种高发泡倍率发泡材料的工业制备方法。更具体的说,本发明涉及三元乙丙橡胶(EPDM)模压闭孔海绵胶的工业生产方法。The invention relates to an industrial preparation method of a foaming material with a high expansion ratio. More specifically, the present invention relates to an industrial production method of EPDM molded closed-cell sponge rubber.
背景技术 Background technique
众所周知,泡沫橡胶是一种以气体为填料的复合材料,与橡胶相比,它具有许多可贵的性能,如质轻、比强度高、吸收冲击载荷能力强和隔热隔音效果好等。因此,在汽车、电子、化工和机械等行业中广泛使用。As we all know, foam rubber is a composite material filled with gas. Compared with rubber, it has many valuable properties, such as light weight, high specific strength, strong ability to absorb impact loads, and good heat and sound insulation effects. Therefore, it is widely used in industries such as automobile, electronics, chemical industry and machinery.
海绵橡胶是一种多孔性的高弹材料,俗称多孔橡胶、泡沫橡胶、微孔橡胶或网眼橡胶,是具有孔眼结构的各种橡胶的总称。根据孔眼结构的不同,可分为闭孔(孔眼与孔眼之间互不相通)、开孔(孔眼与孔眼相互之间未被孔壁完全隔开,具有一定程度的连通性)和混合孔(兼有开孔和闭孔两种结构)三种。海绵橡胶与其结构上的特殊性,可以产生各种特殊的效果,如:降低密度减轻重量;弹性和柔软性,提高缓冲效果;增加隔热性;提高隔声、吸声效果。海绵橡胶制品广泛应用于密封、减震、隔热、隔音印染乃至离子交换等方面。其形状有板状、长条状、辊筒、衬垫、垫圈等,规格繁多,形状各异。而且,不同的使用条件要求有不同的孔眼结构和孔径尺寸。Sponge rubber is a porous high-elastic material, commonly known as porous rubber, foam rubber, microporous rubber or mesh rubber, and is a general term for various rubbers with a porous structure. According to different pore structures, it can be divided into closed pores (the pores are not connected to each other), open pores (the pores are not completely separated by the pore wall, and have a certain degree of connectivity) and mixed pores ( Both open cell and closed cell structure) three. Sponge rubber and its special structure can produce various special effects, such as: reducing density and reducing weight; elasticity and softness, improving cushioning effect; increasing heat insulation; improving sound insulation and sound absorption effects. Sponge rubber products are widely used in sealing, shock absorption, heat insulation, sound insulation, printing and dyeing, and even ion exchange. Its shapes include plate shape, strip shape, roller, liner, gasket, etc., with various specifications and shapes. Moreover, different service conditions require different cell structures and aperture sizes.
海绵橡胶不同于一般的实心橡胶制品,在硫化加热过程中同时发生两种主要过程:发泡剂分解释放出气体和橡胶在硫化剂作用下交联。由于发泡剂释放出的气体最初溶解在胶料中,当气体溶解达到饱和后即有气相产物形成,胶料在所形成气体的压力下沸腾发泡,于此同时胶料通过硫化交联而把孔眼结构固定下来。为此,要求硫化速度能调节到是析出气体所产生的对孔壁的拉伸膨胀力稍大于孔壁本身对应的阻力。如果气体相的形成速度过快,由于胶料来不及硫化,则形成的一个个气泡就会破裂,导致气体从各个孔眼扩散逸出,发泡压力降低;反之,若气体相形成速度过慢或硫化速度过快,则胶料会在形成多孔结构之前就完成硫化定性。Sponge rubber is different from ordinary solid rubber products. Two main processes occur simultaneously during the vulcanization heating process: the foaming agent decomposes to release gas and the rubber is cross-linked under the action of the vulcanizing agent. Since the gas released by the blowing agent is initially dissolved in the rubber, when the gas dissolves to saturation, a gas phase product is formed, and the rubber is boiled and foamed under the pressure of the formed gas, and at the same time the rubber is vulcanized and cross-linked. Fix the hole structure. For this reason, it is required that the vulcanization rate can be adjusted so that the tensile expansion force on the hole wall generated by the precipitated gas is slightly greater than the corresponding resistance of the hole wall itself. If the formation speed of the gas phase is too fast, the formed bubbles will burst because the rubber has no time to vulcanize, causing the gas to diffuse and escape from each hole, and the foaming pressure will decrease; on the contrary, if the formation speed of the gas phase is too slow or vulcanization If the speed is too fast, the compound will be cured before the porous structure is formed.
目前,国内对EPDM海绵胶的研究只是基于实验研究,选用的胶料多为进口,因为发泡剂H发热量比发泡剂Ac大,实验过程多选择发泡剂H。但这种实验条件只能适应于实验室内小规格的发泡材料,对于工业化的生产并不能满足要求。同时,发泡剂H发热量大而橡胶又是热的不良导体所以易发生焦烧现象。本发明则是基于市场需求研发,使得研究目的从实验室研究转向了工业化的研究,能够使生产条件可控,生产过程比较稳定。本发明选用国产胶料,选用发泡剂Ac替代发泡剂H,通过调整配方中各种助剂的配比和工艺条件的控制能够制备符合工业化生产要求的EPDM模压海绵胶制品。At present, the domestic research on EPDM sponge rubber is only based on experimental research, and most of the selected rubber materials are imported, because the heat generation of foaming agent H is greater than that of foaming agent Ac, and foaming agent H is mostly selected in the experimental process. However, this experimental condition can only be adapted to small-scale foaming materials in the laboratory, and cannot meet the requirements for industrial production. At the same time, the foaming agent H generates a large amount of heat and rubber is a poor conductor of heat, so it is prone to scorching. The present invention is researched and developed based on market demand, so that the research purpose is shifted from laboratory research to industrial research, and the production conditions can be controlled, and the production process is relatively stable. The present invention selects domestic rubber material, selects foaming agent Ac to replace foaming agent H, and can prepare EPDM molded sponge rubber products that meet industrial production requirements by adjusting the ratio of various auxiliary agents in the formula and controlling the process conditions.
发明内容 Contents of the invention
本发明的目的是提供一种EPDM模压闭孔海绵胶的工业生产方法。本工艺分为以下几个步骤:生胶的塑炼、混炼、精炼、发泡硫化成型。The purpose of this invention is to provide a kind of industrial production method of EPDM molded closed-cell sponge glue. This process is divided into the following steps: plasticizing, mixing, refining, foaming and vulcanization of raw rubber.
本发明采用的技术方案包含以下内容:The technical scheme adopted in the present invention comprises the following contents:
一、材料选择与配比(以重量份数计算)1. Material selection and proportioning (calculated in parts by weight)
生胶:EPDM: 100Raw rubber: EPDM: 100
发泡剂:Ac 0.1~0.16Foaming agent: Ac 0.1~0.16
发泡助剂:氧化锌ZnO和硬脂酸HSt,其中氧化锌为0.02~0.05;硬脂酸为0.008~0.01Foaming aids: zinc oxide ZnO and stearic acid HSt, of which zinc oxide is 0.02-0.05; stearic acid is 0.008-0.01
硫化剂:S 0.1~0.16Vulcanizing agent: S 0.1~0.16
硫化促进剂:促D、促M、促BZ和促TRAVulcanization accelerators: promote D, promote M, promote BZ and promote TRA
其中促D为0.001~0.003;促M为0.001~0.003;促BZ为0.001~0.005;促TRA为0.002~0.006。Among them, promoting D is 0.001-0.003; promoting M is 0.001-0.003; promoting BZ is 0.001-0.005; promoting TRA is 0.002-0.006.
防老剂:RD和4020,重量份数全都为0.001Antiaging agent: RD and 4020, all parts by weight are 0.001
软化剂:环烷油 40~60Softener: naphthenic oil 40~60
填充剂:碳黑(SRF N550) 50Filler: carbon black (SRF N550) 50
上述的生胶EPDM的门尼粘度ML(1+4)100℃=46。Mooney viscosity ML (1+4) 100° C. of the aforementioned raw rubber EPDM = 46.
二、制备过程:2. Preparation process:
1)塑炼1) Mastication
将开炼机温度控制在50℃以下,EPDM生胶在开炼机上塑炼2-3min直至胶料呈透明状;Control the temperature of the open mill below 50°C, and masticate EPDM raw rubber on the open mill for 2-3 minutes until the rubber material is transparent;
2)混炼(CMB)2) Mixing (CMB)
将塑炼好的胶料放入密炼机内,混炼至80~100℃时加入炭黑、环烷油、发泡助剂、硫化促进剂和防老剂,继续加压混炼至温度100~120℃时排胶;Put the masticated rubber into the internal mixer, add carbon black, naphthenic oil, foaming aid, vulcanization accelerator and anti-aging agent when mixing to 80-100°C, continue to pressurize and mix until the temperature is 100°C Glue removal at ~120°C;
3)精炼(FMB)3) Refining (FMB)
将密炼机预热至60~70℃,将混炼好的胶料装入密炼机内加压密炼60~90秒后加入发泡剂Ac和硫化剂,压力盖半闭合空打1分钟完全压下上压力盖,密炼2分钟后抬起压力盖让胶料在密炼室翻身4次后排胶;Preheat the internal mixer to 60-70°C, put the mixed rubber into the internal mixer, pressurize and internally knead for 60-90 seconds, then add foaming agent Ac and vulcanizing agent, half-close the pressure cover and air beat 1 Completely press down the upper pressure cover in 2 minutes, lift the pressure cover after 2 minutes of mixing, let the rubber turn over 4 times in the mixing room, and then discharge the glue;
4)发泡硫化成型4) Foam vulcanization molding
将硫化机温度调至160~180℃,压力调至15~20MPa,精炼好的胶料在两辊刻度为0.5情况下先开炼一次,然后辊距调整将为0,打三角包4~5次,辊距调整至2.5刻度出片,依照模具大小裁片状胶后送至压机硫化发泡,发泡时间为3000~3500s。Adjust the temperature of the vulcanizer to 160-180°C, and the pressure to 15-20MPa. The refined rubber material is first refined once when the scale of the two rollers is 0.5, and then the roller distance is adjusted to 0, and the triangle bag is 4-5. Second, adjust the roller distance to 2.5 scales to produce the sheet, cut the sheet rubber according to the size of the mold, and send it to the press for vulcanization and foaming. The foaming time is 3000-3500s.
本发明是基于市场需求研发,使得研究目的从实验室研究转向了工业化的研究,能够使生产条件可控,生产过程比较稳定。本发明选用国产胶料,选用发泡剂Ac替代发泡剂H,通过调整配方中各种助剂的配比和工艺条件的控制能够制备符合工业化生产要求的EPDM模压海绵胶制品。The invention is researched and developed based on market demand, so that the research purpose is shifted from laboratory research to industrial research, and the production conditions can be controlled, and the production process is relatively stable. The present invention selects domestic rubber material, selects foaming agent Ac to replace foaming agent H, and can prepare EPDM molded sponge rubber products that meet industrial production requirements by adjusting the ratio of various auxiliary agents in the formula and controlling the process conditions.
具体实施方式 Detailed ways
实施例1:Example 1:
按下列配方称取物料:EPDM:500g,炭黑:250g,环烷油:250g,促BZ:0.6g,促D:0.5g,促TRA:0.6g,促M:0.5g,硬脂酸:8g,氧化锌:15g,Ac:30g,S:0.8gWeigh materials according to the following formula: EPDM: 500g, carbon black: 250g, naphthenic oil: 250g, pro-BZ: 0.6g, pro-D: 0.5g, pro-TRA: 0.6g, pro-M: 0.5g, stearic acid: 8g, Zinc Oxide: 15g, Ac: 30g, S: 0.8g
塑炼:控制开炼机两辊温度维持在50℃以下,生胶在辊距刻度为1的情况下先炼塑2次,然后将辊距调整至0刻度,打三角包4~6次,至胶料呈半透明状。Molding: Control the temperature of the two rollers of the open mill to be kept below 50°C. The raw rubber is smelted twice when the roller distance scale is 1, and then the roller distance is adjusted to 0 scale, and the triangular bag is made 4 to 6 times. Until the glue is translucent.
混炼:将炼塑合格的EPDM胶装入密炼机内加压密炼,温度升至80℃时升起压力盖,加入炭黑、环烷油及发泡助剂、硫化促进剂、防老剂,压力盖半闭合空打约1分钟后,完全压下上压力盖,温度升至120℃时排胶,并送至两辊开炼。混炼好的胶料在两辊刻度为0.5情况下先开炼一次;然后将辊距调整为0,打三角包4~5次;辊距调整至2.5刻度出片,停放24小时熟化后待用。Mixing: Put the qualified EPDM rubber into the internal mixer and pressurize it. When the temperature rises to 80°C, raise the pressure cover, add carbon black, naphthenic oil and foaming aids, vulcanization accelerators, anti-aging After the pressure cover is semi-closed and empty for about 1 minute, the upper pressure cover is completely pressed, and the glue is removed when the temperature rises to 120°C, and it is sent to the two-roller for kneading. The kneaded rubber material is kneaded once when the scale of the two rolls is 0.5; then the roll distance is adjusted to 0, and the triangle bag is made 4 to 5 times; use.
精炼:将密炼机预热至65℃,将炼塑合格的CMB胶装入密炼机内加压密炼70秒,升起压力盖加入发泡剂Ac和硫化剂,压力盖半闭合空打约1分钟后,完全压下上压力盖,密炼2分钟后抬起压力盖让胶料在密炼室翻身4次后排胶,并送至两辊开炼。Refining: Preheat the internal mixer to 65°C, put the qualified CMB rubber into the internal mixer and pressurize it for 70 seconds, raise the pressure cover and add foaming agent Ac and vulcanizing agent, and the pressure cover is half-closed After beating for about 1 minute, press down the upper pressure cover completely, lift the pressure cover after 2 minutes of mixing, let the rubber turn over 4 times in the mixing room, and then discharge the glue, and send it to the two rollers for mixing.
发泡硫化成型:硫化机温度调至160℃,压力调至15MPa,将混炼好的胶料在两辊刻度为0.5情况下先开炼一次,然后将辊距调整为0打三角包4~5次,辊距调整至2.5刻度出片,依照模具大小裁片状胶后送至压机硫化发泡,发泡时间为3000s。Foam vulcanization molding: adjust the temperature of the vulcanizer to 160°C, adjust the pressure to 15MPa, start the kneading of the kneaded rubber material with the scale of the two rolls at 0.5, and then adjust the roll distance to 0 to make triangle bags 4~ 5 times, the roller distance is adjusted to 2.5 scale, and the sheet is produced. The sheet rubber is cut according to the size of the mold and sent to the press for vulcanization and foaming. The foaming time is 3000s.
根据以上配方所得制品的性能如下:The performance of the product obtained according to the above formula is as follows:
实施例2:Example 2:
按下列配方称取物料:EPDM:500g,炭黑:250g,环烷油:100g,促BZ:0.6g,促D:0.5g,促TRA:0.6g,促M:0.5g,硬脂酸:4g,氧化锌:8g,Ac:16g,S:13gWeigh materials according to the following formula: EPDM: 500g, carbon black: 250g, naphthenic oil: 100g, pro-BZ: 0.6g, pro-D: 0.5g, pro-TRA: 0.6g, pro-M: 0.5g, stearic acid: 4g, Zinc Oxide: 8g, Ac: 16g, S: 13g
塑炼:控制开炼机两辊温度,将生胶在辊距刻度为1的情况下先炼塑2次,然后将辊距调整至0刻度,打三角包4~6次,至胶料呈半透明状。Plastic refining: control the temperature of the two rollers of the open mill, refine the raw rubber for 2 times when the roller distance scale is 1, then adjust the roller distance to 0 scale, make triangular bags 4 to 6 times, until the rubber material is Translucent.
混炼:将炼塑合格的EPDM胶装入密炼机内加压密炼,温度升至85℃时升起压力盖,加入炭黑、环烷油及发泡助剂、硫化促进剂、防老剂,压力盖半闭合空打约1分钟后,完全压下上压力盖,温度升至118℃时排胶,并送至两辊开炼。混炼好的胶料在两辊刻度为0.5情况下先开炼一次;然后将辊距调整为0,打三角包4~5次;辊距调整至2.5刻度出片,停放24小时熟化后待用。Mixing: put the qualified EPDM rubber into the internal mixer and pressurize it. When the temperature rises to 85°C, raise the pressure cover, add carbon black, naphthenic oil, foaming aids, vulcanization accelerators, anti-aging After the pressure cover is half-closed for about 1 minute, press the upper pressure cover completely, and when the temperature rises to 118°C, the glue will be removed and sent to the two rollers for kneading. The kneaded rubber material is kneaded once when the scale of the two rolls is 0.5; then the roll distance is adjusted to 0, and the triangle bag is made 4 to 5 times; use.
精炼:将密炼机预热至65℃,将炼塑合格的CMB胶装入密炼机内加压密炼70秒,升起压力盖加入发泡剂Ac和硫化剂。压力盖半闭合空打约1分钟后,完全压下上压力盖,密炼2分钟后抬起压力盖让胶料在密炼室翻身4次后排胶,并送至两辊开炼。Refining: Preheat the internal mixer to 65°C, put qualified CMB rubber into the internal mixer and pressurize it for 70 seconds, raise the pressure cover and add foaming agent Ac and vulcanizing agent. After the pressure cover is half-closed and empty for about 1 minute, press the upper pressure cover completely, lift the pressure cover after 2 minutes of mixing, let the rubber turn over 4 times in the mixing room, and then discharge the glue, and send it to the two rollers for mixing.
发泡硫化成型:将硫化机温度调至165℃,压力调至15MPa,混炼好的胶料在两辊刻度为0.5情况下先开炼一次;然后辊距调整将为0,打三角包4~5次;辊距调整至2.5刻度出片,依照模具大小裁片状胶后送至压机硫化发泡,发泡时间为3300s。根据以上配方所得制品性能如下:Foam vulcanization molding: Adjust the temperature of the vulcanizer to 165°C and the pressure to 15MPa. The mixed rubber material is kneaded once when the scale of the two rollers is 0.5; then the roller distance is adjusted to 0, and the triangle bag is made 4 ~ 5 times; adjust the roller distance to 2.5 scale to produce the sheet, cut the sheet rubber according to the size of the mold, and send it to the press for vulcanization and foaming. The foaming time is 3300s. The properties of the products obtained according to the above formula are as follows:
实施例3:Example 3:
按下列配方称取物料:EPDM:500g,炭黑:250g,环烷油:100,促BZ:0.6g,促D:0.5g,促TRA:0.6g,促M:0.5g,硬脂酸:8g,氧化锌:8g,Ac:16g,S:5gWeigh the materials according to the following formula: EPDM: 500g, carbon black: 250g, naphthenic oil: 100, promote BZ: 0.6g, promote D: 0.5g, promote TRA: 0.6g, promote M: 0.5g, stearic acid: 8g, Zinc Oxide: 8g, Ac: 16g, S: 5g
塑炼:控制开炼机两辊温度,将生胶在辊距刻度为1的情况下先炼塑2次,然后将辊距调整至0刻度,打三角包4~6次,至胶料呈半透明状。Plastic refining: control the temperature of the two rollers of the open mill, refine the raw rubber for 2 times when the roller distance scale is 1, then adjust the roller distance to 0 scale, make triangular bags 4 to 6 times, until the rubber material is Translucent.
混炼:将炼塑合格的EPDM胶装入密炼机内加压密炼,温度升至90℃时升起压力盖,加入炭黑、环烷油及发泡助剂、硫化促进剂、防老剂。压力盖半闭合空打约1分钟后,完全压下上压力盖,温度升至110℃时排胶,并送至两辊开炼。混炼好的胶料在两辊刻度为0.5情况下先开炼一次;然后将辊距调整为0,打三角包4~5次;辊距调整至2.5刻度出片,停放24小时熟化后待用。Mixing: Put the qualified EPDM rubber into the internal mixer and pressurize it. When the temperature rises to 90°C, raise the pressure cover, add carbon black, naphthenic oil and foaming aids, vulcanization accelerators, anti-aging agent. After the pressure cover is half-closed and empty for about 1 minute, the upper pressure cover is completely pressed, and when the temperature rises to 110°C, the glue is removed and sent to the two-roller for kneading. The kneaded rubber material is kneaded once when the scale of the two rolls is 0.5; then the roll distance is adjusted to 0, and the triangle bag is made 4 to 5 times; use.
精炼:将密炼机预热至65℃,将炼塑合格的CMB胶装入密炼机内加压密炼70秒,升起压力盖加入第二包助剂。压力盖半闭合空打约1分钟后,完全压下上压力盖,密炼2分钟后抬起压力盖让胶料在密炼室翻身4次后排胶,并送至两辊开炼。Refining: Preheat the internal mixer to 65°C, put the qualified CMB glue into the internal mixer and pressurize it for 70 seconds, lift the pressure cover and add the second package of additives. After the pressure cover is half-closed and empty for about 1 minute, press the upper pressure cover completely, lift the pressure cover after 2 minutes of mixing, let the rubber turn over 4 times in the mixing room, and then discharge the glue, and send it to the two rollers for mixing.
发泡硫化成型:硫化机温度调至165℃,压力调至20MPa,将混炼好的胶料在两辊刻度为0.5情况下先开炼一次;然后将辊距调整为0,打三角包4~5次;辊距调整至2.5刻度出片,依照模具大小裁片状胶后送至压机硫化发泡,发泡时间为3400s。Foam vulcanization molding: adjust the temperature of the vulcanizer to 165°C, adjust the pressure to 20MPa, and start the kneading of the mixed rubber with the scale of the two rollers at 0.5; then adjust the roller distance to 0, and make a triangle bag 4 ~5 times; adjust the roller distance to 2.5 scales to produce the sheet, cut the sheet rubber according to the size of the mold, and send it to the press for vulcanization and foaming. The foaming time is 3400s.
根据以上配方所得制品行性能如下:The performance of the product obtained according to the above formula is as follows:
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CN102206384B (en) * | 2011-05-10 | 2014-04-09 | 易宝(福建)高分子材料股份公司 | Halogen-free environment-friendly ethylene propylene diene monomer (EPDM) rubber closed hole foam material and preparation method thereof |
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CN105061906A (en) * | 2015-07-23 | 2015-11-18 | 韦海棉 | EPDM (ethylene-propylene-diene monomer) foaming material and preparation method therefor |
CN106566093A (en) * | 2016-11-07 | 2017-04-19 | 惠州航创密封件有限公司 | Non-porous rubber micro-foaming material for automobile sealing strip |
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CN111909461A (en) * | 2020-07-22 | 2020-11-10 | 浙江韦氏电器有限公司 | Formula and preparation process of low-hardness high-resilience closed-cell mould pressing foaming adhesive |
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Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2002146074A (en) * | 2000-11-08 | 2002-05-22 | Nitto Denko Corp | Vulcainzed epdm foam |
CN1800255A (en) * | 2004-12-24 | 2006-07-12 | 日东电工株式会社 | Open-cell foam of ethylene-propylene-diene rubber |
CN101560315A (en) * | 2008-04-14 | 2009-10-21 | 上海大裕橡胶制品有限公司 | Modified foaming ethylene propylene diene rubber |
-
2009
- 2009-12-04 CN CN2009102326809A patent/CN101724172B/en active Active
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2002146074A (en) * | 2000-11-08 | 2002-05-22 | Nitto Denko Corp | Vulcainzed epdm foam |
CN1800255A (en) * | 2004-12-24 | 2006-07-12 | 日东电工株式会社 | Open-cell foam of ethylene-propylene-diene rubber |
CN101560315A (en) * | 2008-04-14 | 2009-10-21 | 上海大裕橡胶制品有限公司 | Modified foaming ethylene propylene diene rubber |
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