WO2021134906A1 - Environment-friendly thermoplastic elastomer foaming and setting process - Google Patents
Environment-friendly thermoplastic elastomer foaming and setting process Download PDFInfo
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- WO2021134906A1 WO2021134906A1 PCT/CN2020/078155 CN2020078155W WO2021134906A1 WO 2021134906 A1 WO2021134906 A1 WO 2021134906A1 CN 2020078155 W CN2020078155 W CN 2020078155W WO 2021134906 A1 WO2021134906 A1 WO 2021134906A1
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- shaping process
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Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C44/00—Shaping by internal pressure generated in the material, e.g. swelling or foaming ; Producing porous or cellular expanded plastics articles
- B29C44/02—Shaping by internal pressure generated in the material, e.g. swelling or foaming ; Producing porous or cellular expanded plastics articles for articles of definite length, i.e. discrete articles
- B29C44/08—Shaping by internal pressure generated in the material, e.g. swelling or foaming ; Producing porous or cellular expanded plastics articles for articles of definite length, i.e. discrete articles using several expanding or moulding steps
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C44/00—Shaping by internal pressure generated in the material, e.g. swelling or foaming ; Producing porous or cellular expanded plastics articles
- B29C44/34—Auxiliary operations
- B29C44/3403—Foaming under special conditions, e.g. in sub-atmospheric pressure, in or on a liquid
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C44/00—Shaping by internal pressure generated in the material, e.g. swelling or foaming ; Producing porous or cellular expanded plastics articles
- B29C44/34—Auxiliary operations
- B29C44/3415—Heating or cooling
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C44/00—Shaping by internal pressure generated in the material, e.g. swelling or foaming ; Producing porous or cellular expanded plastics articles
- B29C44/34—Auxiliary operations
- B29C44/3461—Making or treating expandable particles
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C44/00—Shaping by internal pressure generated in the material, e.g. swelling or foaming ; Producing porous or cellular expanded plastics articles
- B29C44/34—Auxiliary operations
- B29C44/35—Component parts; Details or accessories
- B29C44/354—Means to prevent or reduce the effect of shrinking of the foamed article
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C44/00—Shaping by internal pressure generated in the material, e.g. swelling or foaming ; Producing porous or cellular expanded plastics articles
- B29C44/34—Auxiliary operations
- B29C44/36—Feeding the material to be shaped
- B29C44/38—Feeding the material to be shaped into a closed space, i.e. to make articles of definite length
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29L—INDEXING SCHEME ASSOCIATED WITH SUBCLASS B29C, RELATING TO PARTICULAR ARTICLES
- B29L2031/00—Other particular articles
- B29L2031/48—Wearing apparel
- B29L2031/50—Footwear, e.g. shoes or parts thereof
- B29L2031/504—Soles
Definitions
- the invention relates to the field of supercritical foaming technology, in particular to a foaming and shaping technology for environmentally friendly thermoplastic elastomers.
- the conventional ETPU shock-absorbing midsole is formed by using supercritical foaming to fully foam the TPU material to obtain a foamed molded body. Since this foamed molded body still belongs to the category of semi-finished products, it has the same shock absorption as the finished product.
- the midsole also needs to undergo a setting process by a setting machine. During the molding and heating setting process of the setting machine, the TPU or PEBAX material that has not undergone cross-linking operation will produce greater shrinkage when encountering high temperatures, which seriously affects the entire product. quality.
- the main purpose of the present invention is to provide an environmentally-friendly thermoplastic elastomer foaming and shaping process to solve the contradiction between environmental protection and product quality in the prior art.
- the solution of the present invention is:
- thermoplastic elastomer foaming and shaping process which includes the following steps:
- thermoplastic elastomer materials to contact at least one inert gas in a reactor at a pressure higher than atmospheric pressure to drive the gas into the material; the pressure holding temperature of the reactor is lower than the melting temperature of the material 5 -40°C;
- thermoplastic elastomer material forms a primary foaming material, and then take the primary foaming material out of the reactor;
- step 2 it also includes the step of taking out the primary foaming material and transferring it to a cold storage below 0°C for storage; step 3 is taking out the primary foaming material from the cold storage for heating.
- step 1 before adding the thermoplastic elastomer material to the reactor, it further includes a step of processing the sole mold through a mold.
- the heating temperature is higher than the melting temperature of the material by 10-40 degrees Celsius, and the secondary foaming time is 5-60 minutes.
- the at least one inert gas in step 1 is a supercritical fluid, which is nitrogen, carbon dioxide, or a mixed gas of the two, with a holding pressure of 10-70 MPa, and a holding time of 0.5-24 hours.
- step 2 the pressure reduction in step 2 is achieved by exhausting, and the exhausting speed is 5s-600s.
- thermoplastic elastomer material is one of TPE, TPU, TPEE or PEBAX or a mixture of two or more materials.
- the present invention relates to a foaming and shaping process of environmentally friendly thermoplastic elastomer. Compared with the prior art, the present invention has at least the following beneficial effects:
- the present invention keeps the reactor at a stable temperature (always kept at a temperature of 5-40°C lower than the melting temperature of the material), so that the entire foaming process consumes very little energy and does not need to be compared with existing ones.
- the same technique is used to raise and lower the temperature of the reactor, which not only reduces energy consumption and costs, but also improves production efficiency.
- the present invention performs one-time foaming in step 2, which is actually one-time partial foaming, and its volume expansion rate is generally not more than 30%.
- the inert gas located inside the thermoplastic elastomer material Part of the material will rush out to the outside of the material, which will cause the material to expand.
- the remaining gas will be in the secondary foaming process Let the material expand and play a role), such a reactor of the same volume will be able to place more materials, thereby improving the utilization efficiency of the entire reactor, thereby reducing the cost of a single material in the entire production process.
- the present invention realizes the reuse of the traditional shoe material production equipment-the shaping machine, thereby greatly reducing the production cost of the enterprise, and improving the market competitiveness of the enterprise.
- the use of the shaping machine only needs to use the current shoe material.
- the finished shoe can be obtained by conventional adjustment of the mold; the present invention innovatively proposes to perform secondary foaming in the cavity of the mold of the traditional setting machine, which is mainly to directly use the heat transfer oil in the traditional setting machine to heat the mold. Realization; Then when the foaming to the end process, the mold is directly used to complete the foaming and the finalization at the same time, which not only saves the direct cost of the equipment required for foaming, but also reduces the foaming product to the finalization process.
- This kind of labor cost is also due to the simultaneous completion of foaming and shaping, avoiding the performance problem of reheating the fully foamed material, which will cause the material to shrink, which serves multiple purposes.
- the present invention can further save the primary foaming material in a cold storage below 0°C in step 2, so that the efficiency between the primary foaming material and the secondary foaming setting in the setting machine can be inefficient.
- the problem of synchronization has been fully resolved, thereby further improving the efficiency and competitiveness of the entire process in actual production.
- the present invention does not perform cross-linking operations on thermoplastic elastomer materials, the molded products are very convenient for recycling. At the same time, because it forms the foaming and shaping process in the mold of the shaping machine at one time, it does not need The foamed product is heated and shaped again, so that it also solves the shrinkage problem caused by non-crosslinking.
- the present invention relates to a foaming and shaping process for environmentally friendly thermoplastic elastomers, which includes the following steps:
- thermoplastic elastomer materials to contact at least one inert gas in a reactor at a pressure higher than atmospheric pressure to drive the gas into the material; the pressure holding temperature of the reactor is lower than the melting temperature of the material 5 -40°C (preferably 5-10°C);
- thermoplastic elastomer material is one of TPE, TPU, TPEE or PEBAX or a mixture of two or more materials.
- the at least one inert gas in step 1 is a supercritical fluid, which is nitrogen, carbon dioxide or a mixed gas of the two, and its holding pressure is 10-70 MPa (preferably 50-70 MPa), The holding time is 0.5-24 hours.
- step 1 before adding the thermoplastic elastomer material to the reactor, it further includes a step of processing the sole mold through a mold; the mold formed in this way can be molded in the mold of the setting machine at one time to obtain a finished product The shock-absorbing midsole.
- thermoplastic elastomer material forms a primary foamed material, and then the primary foamed material is taken out of the reactor; specifically, the pressure is reduced in step 2 by means of exhaust
- the exhaust speed is 5s-600s, and the pressure is released to 0 MPa at a time within this period of time. The faster the speed, the finer the cells obtained, the slower the speed, the larger the cells obtained, and the production can be based on Actually need to adjust the exhaust speed.
- the heating temperature is higher than the melting temperature of the material by 10-40 degrees Celsius, and the secondary foaming time is 5-60 minutes.
- step 2 it also includes the step of taking out the primary foaming material and transferring it to a cold storage below 0°C for storage; step 3 is taking out the primary foaming material from the cold storage for heating.
- the present invention relates to a foaming and shaping process for environmentally friendly thermoplastic elastomers. Compared with the prior art, the present invention has at least the following beneficial effects:
- the present invention keeps the reactor at a stable temperature (always kept at a temperature of 5-40°C lower than the melting temperature of the material), so that the entire foaming process consumes very little energy and does not need to be compared with existing ones.
- the same technique is used to raise and lower the temperature of the reactor, which not only reduces energy consumption and costs, but also improves production efficiency.
- the present invention performs one-time foaming in step 2, which is actually one-time partial foaming, and its volume expansion rate is generally not more than 30%.
- the inert gas located inside the thermoplastic elastomer material Part of the material will rush out to the outside of the material, which will cause the material to expand.
- the remaining gas will be in the secondary foaming process Let the material expand and play a role), such a reactor of the same volume will be able to place more materials, thereby improving the utilization efficiency of the entire reactor, thereby reducing the cost of a single material in the entire production process.
- the present invention realizes the reuse of the traditional shoe material production equipment-the shaping machine, thereby greatly reducing the production cost of the enterprise, and improving the market competitiveness of the enterprise.
- the use of the shaping machine only needs to use the current shoe material.
- the finished shoe can be obtained by conventional adjustment of the mold; the present invention innovatively proposes to perform secondary foaming in the cavity of the mold of the traditional setting machine, which is mainly to directly use the heat transfer oil in the traditional setting machine to heat the mold. Realization; Then when the foaming to the end process, the mold is directly used to complete the foaming and the finalization at the same time, which not only saves the direct cost of the equipment required for foaming, but also reduces the foaming product to the finalization process.
- This kind of labor cost is also due to the simultaneous completion of foaming and shaping, avoiding the performance problem of reheating the fully foamed material, which will cause the material to shrink, which serves multiple purposes.
- the present invention does not perform cross-linking operations on thermoplastic elastomer materials, so the molded products are very convenient to recycle. At the same time, because it forms the foaming and shaping process in the mold of the shaping machine at one time, it does not need The foamed product is heated and shaped again, so that it also solves the shrinkage problem caused by non-crosslinking.
Abstract
Disclosed is an environment-friendly thermoplastic elastomer foaming and setting process, comprising the following steps: (1) enabling a thermoplastic elastomer material to contact at least one inert gas in a reaction kettle having the pressure higher than atmospheric pressure so that the gas is driven to enter the material, the pressure maintaining temperature of the reaction kettle is 5-40℃ lower than the melting temperature of the material; (2) maintaining the temperature and then decreasing the pressure so that the thermoplastic elastomer material is formed into a primary foaming material, and then taking the primary foaming material out from the reaction kettle; and (3) transferring the primary foaming material into a mold of a setting machine, heating for secondary foaming and performing mold setting to obtain a finished product. Compared with the prior art, in the present invention, because the thermoplastic elastomer material is not subjected to a crosslinking operation, the finished product molded thereby can be conveniently recycled; in addition, because foaming and setting are implemented in one step in the mold of the setting machine, the problem that the material shrinks due to setting is solved.
Description
本发明涉及超临界发泡工艺领域,具体涉及的是一种环保热塑性弹性体的发泡定型工艺。 The invention relates to the field of supercritical foaming technology, in particular to a foaming and shaping technology for environmentally friendly thermoplastic elastomers.
目前在鞋材领域,各式各样的减震材料得到了越来越多的亮相机会,当前比较受欢迎的两种材料是TPU或者PEBAX材料,为了取得较好的发泡效果,在发泡之前一般都需要对材料进行交联处理,交联的方式一般是通过添加交联剂的方式来实现,又或者是通过辐照交联来实现,但是由此带来的缺点也很明显,那就是交联后的材料将不能回收,即得到的产品环保性较差,不满足目前我国可持续发展的大方向。At present, in the field of shoe materials, a variety of shock-absorbing materials have obtained more and more opportunities to appear. The two most popular materials are TPU or PEBAX materials. In order to achieve better foaming effects, Previously, materials generally needed to be cross-linked. The cross-linking method was generally achieved by adding a cross-linking agent, or by irradiation cross-linking, but the disadvantages brought about by this were also obvious. That is, the cross-linked material will not be recycled, that is, the product obtained is less environmentally friendly and does not meet the current general direction of sustainable development in China.
常规的ETPU减震中底的成型方式是,采用超临界发泡的方式将TPU材料经过充分发泡之后得到发泡成型体,由于这个发泡成型体仍然属于半成品范畴,其与成品的减震中底之间还需要经过定型机进行定型处理的工序,在定型机模压加热定型过程中,未经过交联操作的TPU或PEBAX材料遇到高温会产生较大的收缩,严重影响了整个产品的品质。The conventional ETPU shock-absorbing midsole is formed by using supercritical foaming to fully foam the TPU material to obtain a foamed molded body. Since this foamed molded body still belongs to the category of semi-finished products, it has the same shock absorption as the finished product. The midsole also needs to undergo a setting process by a setting machine. During the molding and heating setting process of the setting machine, the TPU or PEBAX material that has not undergone cross-linking operation will produce greater shrinkage when encountering high temperatures, which seriously affects the entire product. quality.
由此,交联会造成无法回收利用的缺点,不交联又会影响到产品的品质,基于上述矛盾,本申请人对此进行深入研究,遂有本案产生。As a result, cross-linking will cause the disadvantage of not being able to be recycled, and non-cross-linking will affect the quality of the product. Based on the above contradiction, the applicant conducted in-depth research on this, and this case occurred.
本发明的主要目的在于提供一种环保热塑性弹性体的发泡定型工艺,以解决现有技术中存在环保和产品品质之间存在矛盾的问题。The main purpose of the present invention is to provide an environmentally-friendly thermoplastic elastomer foaming and shaping process to solve the contradiction between environmental protection and product quality in the prior art.
为了达成上述目的,本发明的解决方案是:In order to achieve the above objective, the solution of the present invention is:
一种环保热塑性弹性体的发泡定型工艺,其中,包括如下步骤:An environmentally-friendly thermoplastic elastomer foaming and shaping process, which includes the following steps:
①采用热塑性弹性体类材料在高于大气压压力的反应釜中与至少一种惰性气体接触,以驱使气体进入所述材料内;所述反应釜的保压温度低于所述材料的熔融温度5-40℃;① Use thermoplastic elastomer materials to contact at least one inert gas in a reactor at a pressure higher than atmospheric pressure to drive the gas into the material; the pressure holding temperature of the reactor is lower than the melting temperature of the material 5 -40°C;
②保持上述温度,再降低压力,所述热塑性弹性体类材料形成一次发泡材料,再将一次发泡材料从反应釜中取出;② Maintain the above temperature, and then reduce the pressure, the thermoplastic elastomer material forms a primary foaming material, and then take the primary foaming material out of the reactor;
③将一次发泡材料转移至定型机的模具中,经加热二次发泡和模具定型之后得到成品。③Transfer the primary foaming material to the mold of the setting machine, and obtain the finished product after heating the second foaming and the mold setting.
进一步,在步骤②中,还包括将一次发泡材料取出并转移至0℃以下的冷库中保存起来的步骤;步骤③则是从冷库中将一次发泡材料取出进行加热。Further, in step ②, it also includes the step of taking out the primary foaming material and transferring it to a cold storage below 0°C for storage; step ③ is taking out the primary foaming material from the cold storage for heating.
进一步,在步骤①中,所述热塑性弹性体类材料在加入反应釜之前,还包括通过模具加工成鞋底胚模的步骤。Further, in step ①, before adding the thermoplastic elastomer material to the reactor, it further includes a step of processing the sole mold through a mold.
进一步,在步骤③的二次发泡步骤中,加热的温度高于所述材料的熔融温度10-40摄氏度,二次发泡的时间为5-60分钟。Further, in the secondary foaming step of step ③, the heating temperature is higher than the melting temperature of the material by 10-40 degrees Celsius, and the secondary foaming time is 5-60 minutes.
进一步,所述步骤①中的至少一种惰性气体为超临界流体,为氮气、二氧化碳或者二者的混合气体,其保压压力为10-70兆帕,保压时间为0.5-24小时。Further, the at least one inert gas in step ① is a supercritical fluid, which is nitrogen, carbon dioxide, or a mixed gas of the two, with a holding pressure of 10-70 MPa, and a holding time of 0.5-24 hours.
进一步,所述步骤②中降低压力采用排气的方式来实现,排气速度为5s-600s。Further, the pressure reduction in step ② is achieved by exhausting, and the exhausting speed is 5s-600s.
进一步,所述热塑性弹性体类材料为TPE、TPU、TPEE或PEBAX之一或者两种或两种以上材料的混合物。Further, the thermoplastic elastomer material is one of TPE, TPU, TPEE or PEBAX or a mixture of two or more materials.
采用上述结构后,本发明涉及一种环保热塑性弹性体的发泡定型工艺,与现有技术相比,本发明至少具有如下有益效果:After adopting the above structure, the present invention relates to a foaming and shaping process of environmentally friendly thermoplastic elastomer. Compared with the prior art, the present invention has at least the following beneficial effects:
一、本发明保持反应釜一直处于一个稳定的温度(一直保持在低于所述材料的熔融温度5-40℃的温度下),如此整个发泡过程中消耗能量极少,不需要和现有技术一样对反应釜进行升温和降温,不仅仅降低了能量消耗,降低了成本,而且还提高了生产效率。1. The present invention keeps the reactor at a stable temperature (always kept at a temperature of 5-40°C lower than the melting temperature of the material), so that the entire foaming process consumes very little energy and does not need to be compared with existing ones. The same technique is used to raise and lower the temperature of the reactor, which not only reduces energy consumption and costs, but also improves production efficiency.
二、本发明在步骤②中进行一次发泡,其实是一次部分发泡,其体积膨胀率一般不超过30%,在整个反应釜降低压力的过程中,位于热塑性弹性体类材料内部的惰性气体会一部分冲出到材料外部,从而让材料产生一定的膨胀,但是由于材料的当前温度是在软化点以下,故大部分气体还是保留在材料内部(这些保留的气体会在二次发泡过程中让材料发生膨胀发挥作用),如此同样体积的反应釜,将可以放置更多的材料,进而提高整个反应釜的利用效率,进而降低单个材料在整个生产过程中的成本。2. The present invention performs one-time foaming in step ②, which is actually one-time partial foaming, and its volume expansion rate is generally not more than 30%. In the process of reducing the pressure of the entire reactor, the inert gas located inside the thermoplastic elastomer material Part of the material will rush out to the outside of the material, which will cause the material to expand. However, because the current temperature of the material is below the softening point, most of the gas remains inside the material (the remaining gas will be in the secondary foaming process Let the material expand and play a role), such a reactor of the same volume will be able to place more materials, thereby improving the utilization efficiency of the entire reactor, thereby reducing the cost of a single material in the entire production process.
三、本发明实现了对传统鞋材生产设备--定型机的再次利用,从而大大降低了企业的生产成本,提升了企业的市场竞争力,对定型机的使用过程中只需要对当前鞋材的模具进行常规调整,即可得到成品鞋;本发明创新性地提出在传统定型机的模具的模腔中进行二次发泡,其主要是直接利用传统定型机中导热油对模具进行加热来实现;接着在发泡到末端程序时,直接利用模具来让发泡和定型最后同时完成,不仅仅节省了发泡所需的设备直接成本,而且还降低了发泡产品到定型过程中的各种人工成本,最终还由于发泡和定型同步完成,避免了对完全发泡好的材料进行再次加热,从而导致材料收缩的性能问题,一举多得。3. The present invention realizes the reuse of the traditional shoe material production equipment-the shaping machine, thereby greatly reducing the production cost of the enterprise, and improving the market competitiveness of the enterprise. The use of the shaping machine only needs to use the current shoe material. The finished shoe can be obtained by conventional adjustment of the mold; the present invention innovatively proposes to perform secondary foaming in the cavity of the mold of the traditional setting machine, which is mainly to directly use the heat transfer oil in the traditional setting machine to heat the mold. Realization; Then when the foaming to the end process, the mold is directly used to complete the foaming and the finalization at the same time, which not only saves the direct cost of the equipment required for foaming, but also reduces the foaming product to the finalization process. This kind of labor cost is also due to the simultaneous completion of foaming and shaping, avoiding the performance problem of reheating the fully foamed material, which will cause the material to shrink, which serves multiple purposes.
四、本发明进一步还可以通过在步骤②中将一次发泡材料保存在0℃以下的冷库中,这样可以让一次发泡后的材料和定型机中二次发泡定型两者之间效率不同步的问题得到充分的解决,从而进一步提高整个工序在实际生产中的效率和竞争力。Fourth, the present invention can further save the primary foaming material in a cold storage below 0°C in step ②, so that the efficiency between the primary foaming material and the secondary foaming setting in the setting machine can be inefficient. The problem of synchronization has been fully resolved, thereby further improving the efficiency and competitiveness of the entire process in actual production.
五、本发明由于对热塑性弹性体类材料没有进行交联操作,如此其成型出来的成品非常方便回收,同时由于其将发泡和定型的过程在定型机的模具中一次成型,如此其不需要对发泡好的产品进行再次加热和定型,如此其也同时解决了未交联带来的收缩问题。5. Since the present invention does not perform cross-linking operations on thermoplastic elastomer materials, the molded products are very convenient for recycling. At the same time, because it forms the foaming and shaping process in the mold of the shaping machine at one time, it does not need The foamed product is heated and shaped again, so that it also solves the shrinkage problem caused by non-crosslinking.
为了进一步解释本发明的技术方案,下面通过具体实施例来对本发明进行详细阐述。In order to further explain the technical solution of the present invention, the present invention will be described in detail below through specific embodiments.
本发明涉及一种环保热塑性弹性体的发泡定型工艺,包括如下步骤:The present invention relates to a foaming and shaping process for environmentally friendly thermoplastic elastomers, which includes the following steps:
①采用热塑性弹性体类材料在高于大气压压力的反应釜中与至少一种惰性气体接触,以驱使气体进入所述材料内;所述反应釜的保压温度低于所述材料的熔融温度5-40℃(优选为5-10℃);① Use thermoplastic elastomer materials to contact at least one inert gas in a reactor at a pressure higher than atmospheric pressure to drive the gas into the material; the pressure holding temperature of the reactor is lower than the melting temperature of the material 5 -40°C (preferably 5-10°C);
优选的,所述热塑性弹性体类材料为TPE、TPU、TPEE或PEBAX之一或者两种或两种以上材料的混合物。Preferably, the thermoplastic elastomer material is one of TPE, TPU, TPEE or PEBAX or a mixture of two or more materials.
优选的,所述步骤①中的至少一种惰性气体为超临界流体,为氮气、二氧化碳或者二者的混合气体,其保压压力为10-70兆帕(优选为50-70兆帕),保压时间为0.5-24小时。Preferably, the at least one inert gas in step ① is a supercritical fluid, which is nitrogen, carbon dioxide or a mixed gas of the two, and its holding pressure is 10-70 MPa (preferably 50-70 MPa), The holding time is 0.5-24 hours.
优选的,在步骤①中,所述热塑性弹性体类材料在加入反应釜之前,还包括通过模具加工成鞋底胚模的步骤;如此形成的胚模可以在定型机的模具中一次性成型得到成品的减震中底。Preferably, in step ①, before adding the thermoplastic elastomer material to the reactor, it further includes a step of processing the sole mold through a mold; the mold formed in this way can be molded in the mold of the setting machine at one time to obtain a finished product The shock-absorbing midsole.
②保持上述温度,再降低压力,所述热塑性弹性体类材料形成一次发泡材料,再将一次发泡材料从反应釜中取出;具体地,所述步骤②中降低压力采用排气的方式来实现,排气速度为5s-600s,在该时间段内一次将压力释放到0兆帕,速度越快,得到的泡孔越细,速度越慢,得到的泡孔越大,生产时可以根据实际需要来调节排气速度。② Maintain the above temperature, and then reduce the pressure. The thermoplastic elastomer material forms a primary foamed material, and then the primary foamed material is taken out of the reactor; specifically, the pressure is reduced in step ② by means of exhaust The exhaust speed is 5s-600s, and the pressure is released to 0 MPa at a time within this period of time. The faster the speed, the finer the cells obtained, the slower the speed, the larger the cells obtained, and the production can be based on Actually need to adjust the exhaust speed.
③将一次发泡材料转移至定型机的模具中,经加热二次发泡和模具定型之后得到成品。具体地,在步骤③的二次发泡步骤中,加热的温度高于所述材料的熔融温度10-40摄氏度,二次发泡的时间为5-60分钟。③ Transfer the primary foaming material to the mold of the setting machine, and obtain the finished product after heating the second foaming and the mold setting. Specifically, in the secondary foaming step of step ③, the heating temperature is higher than the melting temperature of the material by 10-40 degrees Celsius, and the secondary foaming time is 5-60 minutes.
进一步,在步骤②中,还包括将一次发泡材料取出并转移至0℃以下的冷库中保存起来的步骤;步骤③则是从冷库中将一次发泡材料取出进行加热。这样,可以让一次发泡后的材料和定型机中二次发泡定型两者之间效率不同步的问题得到充分的解决,从而进一步提高整个工序在实际生产中的效率和竞争力。Furthermore, in step ②, it also includes the step of taking out the primary foaming material and transferring it to a cold storage below 0°C for storage; step ③ is taking out the primary foaming material from the cold storage for heating. In this way, the problem of non-synchronization of efficiency between the material after the primary foaming and the secondary foaming and setting in the setting machine can be fully solved, thereby further improving the efficiency and competitiveness of the entire process in actual production.
如此,本发明涉及一种环保热塑性弹性体的发泡定型工艺,与现有技术相比,本发明至少具有如下有益效果:In this way, the present invention relates to a foaming and shaping process for environmentally friendly thermoplastic elastomers. Compared with the prior art, the present invention has at least the following beneficial effects:
一、本发明保持反应釜一直处于一个稳定的温度(一直保持在低于所述材料的熔融温度5-40℃的温度下),如此整个发泡过程中消耗能量极少,不需要和现有技术一样对反应釜进行升温和降温,不仅仅降低了能量消耗,降低了成本,而且还提高了生产效率。1. The present invention keeps the reactor at a stable temperature (always kept at a temperature of 5-40°C lower than the melting temperature of the material), so that the entire foaming process consumes very little energy and does not need to be compared with existing ones. The same technique is used to raise and lower the temperature of the reactor, which not only reduces energy consumption and costs, but also improves production efficiency.
二、本发明在步骤②中进行一次发泡,其实是一次部分发泡,其体积膨胀率一般不超过30%,在整个反应釜降低压力的过程中,位于热塑性弹性体类材料内部的惰性气体会一部分冲出到材料外部,从而让材料产生一定的膨胀,但是由于材料的当前温度是在软化点以下,故大部分气体还是保留在材料内部(这些保留的气体会在二次发泡过程中让材料发生膨胀发挥作用),如此同样体积的反应釜,将可以放置更多的材料,进而提高整个反应釜的利用效率,进而降低单个材料在整个生产过程中的成本。2. The present invention performs one-time foaming in step ②, which is actually one-time partial foaming, and its volume expansion rate is generally not more than 30%. In the process of reducing the pressure of the entire reactor, the inert gas located inside the thermoplastic elastomer material Part of the material will rush out to the outside of the material, which will cause the material to expand. However, because the current temperature of the material is below the softening point, most of the gas remains inside the material (the remaining gas will be in the secondary foaming process Let the material expand and play a role), such a reactor of the same volume will be able to place more materials, thereby improving the utilization efficiency of the entire reactor, thereby reducing the cost of a single material in the entire production process.
三、本发明实现了对传统鞋材生产设备--定型机的再次利用,从而大大降低了企业的生产成本,提升了企业的市场竞争力,对定型机的使用过程中只需要对当前鞋材的模具进行常规调整,即可得到成品鞋;本发明创新性地提出在传统定型机的模具的模腔中进行二次发泡,其主要是直接利用传统定型机中导热油对模具进行加热来实现;接着在发泡到末端程序时,直接利用模具来让发泡和定型最后同时完成,不仅仅节省了发泡所需的设备直接成本,而且还降低了发泡产品到定型过程中的各种人工成本,最终还由于发泡和定型同步完成,避免了对完全发泡好的材料进行再次加热,从而导致材料收缩的性能问题,一举多得。3. The present invention realizes the reuse of the traditional shoe material production equipment-the shaping machine, thereby greatly reducing the production cost of the enterprise, and improving the market competitiveness of the enterprise. The use of the shaping machine only needs to use the current shoe material. The finished shoe can be obtained by conventional adjustment of the mold; the present invention innovatively proposes to perform secondary foaming in the cavity of the mold of the traditional setting machine, which is mainly to directly use the heat transfer oil in the traditional setting machine to heat the mold. Realization; Then when the foaming to the end process, the mold is directly used to complete the foaming and the finalization at the same time, which not only saves the direct cost of the equipment required for foaming, but also reduces the foaming product to the finalization process. This kind of labor cost is also due to the simultaneous completion of foaming and shaping, avoiding the performance problem of reheating the fully foamed material, which will cause the material to shrink, which serves multiple purposes.
四、本发明由于对热塑性弹性体类材料没有进行交联操作,如此其成型出来的成品非常方便回收,同时由于其将发泡和定型的过程在定型机的模具中一次成型,如此其不需要对发泡好的产品进行再次加热和定型,如此其也同时解决了未交联带来的收缩问题。Fourth, the present invention does not perform cross-linking operations on thermoplastic elastomer materials, so the molded products are very convenient to recycle. At the same time, because it forms the foaming and shaping process in the mold of the shaping machine at one time, it does not need The foamed product is heated and shaped again, so that it also solves the shrinkage problem caused by non-crosslinking.
上述实施例并非限定本发明的产品形态和式样,任何所属技术领域的普通技术人员对其所做的适当变化或修饰,皆应视为不脱离本发明的专利范畴。The foregoing embodiments do not limit the product form and style of the present invention, and any appropriate changes or modifications made by those of ordinary skill in the art should be regarded as not departing from the patent scope of the present invention.
Claims (7)
1.一种环保热塑性弹性体的发泡定型工艺,其特征在于,包括如下步骤: 1. A foaming and shaping process for environmentally friendly thermoplastic elastomers, characterized in that it comprises the following steps:
①采用热塑性弹性体类材料在高于大气压压力的反应釜中与至少一种惰性气体接触,以驱使气体进入所述材料内;所述反应釜的保压温度低于所述材料的熔融温度5-40℃;① Use thermoplastic elastomer materials to contact at least one inert gas in a reactor at a pressure higher than atmospheric pressure to drive the gas into the material; the pressure holding temperature of the reactor is lower than the melting temperature of the material 5 -40°C;
②保持上述温度,再降低压力,所述热塑性弹性体类材料形成一次发泡材料,再将一次发泡材料从反应釜中取出;② Maintain the above temperature, and then reduce the pressure, the thermoplastic elastomer material forms a primary foaming material, and then take the primary foaming material out of the reactor;
③将一次发泡材料转移至定型机的模具中,经加热二次发泡和模具定型之后得到成品。③Transfer the primary foaming material to the mold of the setting machine, and obtain the finished product after heating the second foaming and the mold setting.
2.如权利要求1所述的一种环保热塑性弹性体的发泡定型工艺,其特征在于,在步骤②中,还包括将一次发泡材料取出并转移至0℃以下的冷库中保存起来的步骤;步骤③则是从冷库中将一次发泡材料取出进行加热。2. An environmentally friendly thermoplastic elastomer foaming and shaping process according to claim 1, characterized in that, in step ②, it also includes taking out the primary foaming material and transferring it to a cold storage below 0°C for storage. Step; Step ③ is to take out the primary foaming material from the cold storage for heating.
3.如权利要求1所述的一种环保热塑性弹性体的发泡定型工艺,其特征在于,在步骤①中,所述热塑性弹性体类材料在加入反应釜之前,还包括通过模具加工成鞋底胚模的步骤。3. An environmentally-friendly thermoplastic elastomer foaming and shaping process according to claim 1, characterized in that, in step ①, before adding the thermoplastic elastomer material to the reactor, it further comprises processing the sole through a mold. The steps of the prototype.
4.如权利要求1所述的一种环保热塑性弹性体的发泡定型工艺,其特征在于,在步骤③的二次发泡步骤中,加热的温度高于所述材料的熔融温度10-40摄氏度,二次发泡的时间为5-60分钟。4. An environmentally friendly thermoplastic elastomer foaming and shaping process according to claim 1, characterized in that, in the secondary foaming step of step ③, the heating temperature is higher than the melting temperature of the material by 10-40 In degrees Celsius, the time for secondary foaming is 5-60 minutes.
5.如权利要求1所述的一种环保热塑性弹性体的发泡定型工艺,其特征在于,所述步骤①中的至少一种惰性气体为超临界流体,为氮气、二氧化碳或者二者的混合气体,其保压压力为10-70兆帕,保压时间为0.5-24小时。5. An environmentally friendly thermoplastic elastomer foaming and shaping process according to claim 1, wherein at least one inert gas in step ① is a supercritical fluid, which is nitrogen, carbon dioxide, or a mixture of the two For gas, its holding pressure is 10-70 MPa, and the holding time is 0.5-24 hours.
6.如权利要求1所述的一种环保热塑性弹性体的发泡定型工艺,其特征在于,所述步骤②中降低压力采用排气的方式来实现,排气速度为5s-600s。6. An environmentally-friendly thermoplastic elastomer foaming and shaping process according to claim 1, wherein the pressure reduction in step ② is achieved by exhausting, and the exhausting speed is 5s-600s.
7.如权利要求1所述的一种环保热塑性弹性体的发泡定型工艺,其特征在于,所述热塑性弹性体类材料为TPE、TPU、TPEE或PEBAX之一或者两种或两种以上材料的混合物。7. An environmentally-friendly thermoplastic elastomer foaming and shaping process according to claim 1, wherein the thermoplastic elastomer material is one or two or more of TPE, TPU, TPEE or PEBAX mixture.
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