WO2024011919A1 - Preparation method for eva material and eva material - Google Patents

Preparation method for eva material and eva material Download PDF

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Publication number
WO2024011919A1
WO2024011919A1 PCT/CN2023/078579 CN2023078579W WO2024011919A1 WO 2024011919 A1 WO2024011919 A1 WO 2024011919A1 CN 2023078579 W CN2023078579 W CN 2023078579W WO 2024011919 A1 WO2024011919 A1 WO 2024011919A1
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eva
preparation
eva material
molding
cross
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PCT/CN2023/078579
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French (fr)
Chinese (zh)
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王经逸
肖晖
陈汝盼
卢鑫
张青海
林鸿裕
詹迎旭
王育玲
刘东斌
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黎明职业大学
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Publication of WO2024011919A1 publication Critical patent/WO2024011919A1/en

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    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J3/00Processes of treating or compounding macromolecular substances
    • C08J3/24Crosslinking, e.g. vulcanising, of macromolecules
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J9/00Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
    • C08J9/0014Use of organic additives
    • C08J9/0042Use of organic additives containing silicon
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J9/00Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
    • C08J9/0066Use of inorganic compounding ingredients
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J9/00Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
    • C08J9/04Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent
    • C08J9/06Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent by a chemical blowing agent
    • C08J9/10Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent by a chemical blowing agent developing nitrogen, the blowing agent being a compound containing a nitrogen-to-nitrogen bond
    • C08J9/102Azo-compounds
    • C08J9/103Azodicarbonamide
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2323/00Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers
    • C08J2323/02Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers not modified by chemical after treatment
    • C08J2323/04Homopolymers or copolymers of ethene
    • C08J2323/08Copolymers of ethene
    • 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
    • C08K3/24Acids; Salts thereof
    • C08K3/26Carbonates; Bicarbonates
    • C08K2003/265Calcium, strontium or barium carbonate
    • 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
    • C08K3/34Silicon-containing compounds
    • C08K3/36Silica
    • 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
    • C08K5/00Use of organic ingredients
    • C08K5/54Silicon-containing compounds
    • C08K5/541Silicon-containing compounds containing oxygen
    • C08K5/5415Silicon-containing compounds containing oxygen containing at least one Si—O bond
    • C08K5/5419Silicon-containing compounds containing oxygen containing at least one Si—O bond containing at least one Si—C bond
    • 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
    • C08K9/00Use of pretreated ingredients
    • C08K9/04Ingredients treated with organic substances
    • C08K9/06Ingredients treated with organic substances with silicon-containing compounds
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies
    • Y02W30/62Plastics recycling; Rubber recycling

Definitions

  • the present invention relates to an EVA material, in particular to a preparation method of an EVA material and an EVA material.
  • EVA ethylene-vinyl acetate copolymer
  • waste EVA is mainly disposed of through incineration to obtain heat and reprocessing. It is relatively simple to obtain heat through incineration, but incineration will produce toxic chemicals and the utilization rate is low; reprocessing mainly involves chopping and grinding cross-linked EVA into fine powder, and using it as a new EVA material to replace part of the filler, which is the current cross-linked EVA recycling
  • the main method however, the compatibility of the crushed EVA colloidal particles after cross-linking with the new EVA material is low, so it can only be added or replaced in small amounts, and the utilization rate is low.
  • the purpose of the present invention is to provide a preparation method and EVA material with a relatively high utilization rate of EVA materials.
  • a preparation method of EVA material including the following steps:
  • Cross-linking put the EVA raw material into the torque rheometer for pre-dispersion, and then add the transesterification catalyst and the dynamic cross-linking agent to the torque rheometer respectively for blending processing to obtain a blend;
  • the blend is vulcanized and molded sequentially to obtain an EVA material.
  • step S1 add the ester silane coupling agent into the container in 3-5 times, and while adding the ester silane coupling agent, clean the contents in the container.
  • the solution is stirred at a stirring speed of 500-1500 r/min, and then condensed and refluxed at 70-110°C for 2 hours.
  • the filler particles are silica and/or calcium carbonate
  • the particle size of the filler particles is 20-2000 nm
  • the mass fraction of the filler particles is 1%-10%
  • the above-mentioned ester silane coupling agents are 2-carbonylmethoxyethyldimethoxymethylsilane, acetoxypropyltrimethoxysilane, and 3-(carbonylmethoxy)propyldimethylmethoxy
  • the EVA raw material is thermoplastic unvulcanized cross-linked EVA with an ethyl acetate content of 10-30%
  • the transesterification catalyst is tetrabutyl titanate, tetraethyl titanate, tetraisopropyl titanate or acetyl molybdenum.
  • step S1 the filler particles are pre-dispersed using ultrasound at 20-40°C for 20-40 minutes.
  • step S1 when performing centrifugal washing treatment, the mixture is centrifuged 3-5 times at a speed of 8000-12000 r/min, and the time of each centrifugal treatment is 3-7 min. .
  • step S1 during the drying process, the filter residue is vacuum dried at 80-120°C for 8-20 h.
  • step S2 the reaction temperature of the torque rheometer is controlled to be 100-180°C and the rotation speed is 50-200 rpm.
  • step S2 the pre-dispersion time is 5-10 min, the transesterification catalyst is added into the torque rheometer in 3-5 times, and then mixed for 10-30 min, and then The dynamic cross-linking agent is added into the torque rheometer in 3-5 times, and then blended for 10-30 minutes.
  • step S3 during molding, the molding pressure is 5-20 MPa, the molding temperature is 120-180°C, and the molding time is 0.5-2h.
  • An EVA material including 10-30 parts by mass of filler particles, 1-10 parts by mass of ester silane coupling agent, 70-100 parts by mass of EVA, 0.1-2.5 parts by mass of transesterification catalyst and 1-10 parts by mass of dynamic cross-linking
  • the agent is prepared using the above preparation method of EVA material.
  • the present invention has the following beneficial effects:
  • the present invention adopts a mechanical blending method and uses transesterification reaction under the action of a catalyst to obtain an EVA material with dynamic cross-linking bonding.
  • the dynamic cross-linking bonding allows the cross-linked EVA to be processed using conventional plastic thermal processing methods. It is recycled and processed, and it still maintains good mechanical properties after multiple cycles of processing, and maintains good physical and mechanical properties, and the utilization rate is relatively high.
  • Figure 1 is a schematic structural diagram of the dynamic cross-linking agent in the embodiment
  • Figure 2 is a scanning electron microscope image of the EVA-1 foam material in Example 3;
  • Figure 3 is a scanning electron microscope image of the EVA-2 foam material in Example 3;
  • Figure 4 is a scanning electron microscope image of the EVA-3 foam material in Example 3.
  • the present invention will be further described below with reference to specific examples.
  • the raw materials and test instruments used in the following examples and comparative examples can be purchased directly from the market.
  • the test steps or test steps without specifying specific conditions are It is carried out in accordance with conventional conditions or in accordance with the conditions recommended by the test instrument manufacturer, which will not be described in detail here.
  • the present invention provides a method for preparing EVA materials, which uses a mechanical blending method to utilize the transesterification reaction between carboxylic acid esters contained in EVA and cross-linking agents containing polyvalent alkyl esters to prepare multi-component cross-linked EVA materials. Change the use and type of cross-linking agent, control the dynamics of the cross-linking network, and regulate the dynamic cross-linking structure and physical and mechanical properties of EVA materials.
  • the method includes the following steps:
  • filler particles placed in a container, where the filler particles can be silica and/or calcium carbonate, the particle size of the filler particles is 20-2000 nm, and the mass fraction of the filler particles is 1%-10%.
  • the filler particles are pre-dispersed in a toluene solvent or an ethanol solvent to obtain a uniform suspension. Specifically, the filler particles are pre-dispersed using ultrasound at 20-40°C for 20-40 minutes. Then, an ester silane coupling agent is added to the suspension, and a mixture is obtained after a modification reaction.
  • the ester silane coupling agent can be 2-carbonylmethoxyethyldimethoxymethylsilane, acetoxy One or two of propyltrimethoxysilane, 3-(carbonylmethoxy)propyldimethylmethoxysilane and 3-(carbonylethoxy)propyldimethylethoxysilane.
  • the ester silane coupling agent is added to the container in 3-5 times, and the solution (and suspension) in the container is stirred while adding the ester silane coupling agent.
  • the stirring speed of the stirring process is 500-500. 1500 r/min, and then condense and reflux for 2 hours at 70-110°C.
  • the mixture is centrifuged and washed to obtain the filter residue.
  • the mixture is centrifuged 3-5 times at a speed of 8000-12000 r/min, and the centrifugation time for each time is 3-7 min; the filter residue is then dried.
  • the dynamic cross-linking agent is obtained through the treatment. During the drying process, the filter residue is vacuum dried at 80-120°C for 8-20 h.
  • the dynamic cross-linking agent obtained by the present invention has a hard segment structure mainly formed by filler particles 1. This hard segment structure is used to connect the ester silane coupling agent 2, which has good stability.
  • the transesterification catalyst and the dynamic cross-linking agent were respectively added to the torque rheometer for blending treatment to obtain a blend, in which the transesterification catalyst was tetrabutyl titanate, tetraethyl titanate, and tetraisotitanate. propyl ester or acetyl molybdenum.
  • the blend is vulcanized and molded in sequence to obtain EVA material.
  • the vulcanization treatment is performed using a flat vulcanizer. During molding, the molding pressure is 5-20 MPa and the molding temperature is 120-180°C. The time is 0.5-2h.
  • the invention also provides an EVA material, including 10-30 parts by mass filler particles, 1-10 parts by mass ester silane coupling agent, 70-100 parts by mass EVA, 0.1-2.5 parts by mass transesterification catalyst and 1-10 parts by mass
  • EVA material including 10-30 parts by mass filler particles, 1-10 parts by mass ester silane coupling agent, 70-100 parts by mass EVA, 0.1-2.5 parts by mass transesterification catalyst and 1-10 parts by mass
  • the mass part of dynamic cross-linking agent is prepared by using the above preparation method of EVA material.
  • the invention circumvents the traditional irreversible chemical cross-linking method and utilizes the transesterification reaction between the carboxylic acid ester contained in EVA and a specific cross-linking agent containing polyvalent alkyl esters to prepare multi-component cross-linked EVA materials.
  • Dynamic cross-linked EVA is formed through transesterification, which reduces the polymer The content of medium unsaturated double bonds effectively improves its UV resistance and high temperature stability and extends its use time.
  • the present invention adopts a pre-hydrolysis reaction between an ester-containing silane coupling agent and filler particles to obtain an ester-based dynamic cross-linking agent with a hard segment (filler particle) structure.
  • the ester-based dynamic cross-linking agent and EVA The transesterification reaction of carboxylic acid esters produces multi-element cross-linked EVA materials, which shows good reprocessability and maintains good physical and mechanical properties; reinforcing particles are embedded in the EVA molecular chain to avoid simple mechanical blending. It solves the agglomeration problem and effectively improves the mechanical properties of EVA materials that can be recycled.
  • silica is pre-dispersed in 500 mL of toluene solution, ultrasonically dispersed at 25°C for 30 minutes, and 3g of 2-carbonylmethoxyethyldimethoxymethylsilane is added.
  • Stir with an external electric stirrer Control the stirrer speed to 800 r/min, the reaction temperature to 80°C, and the condensation reflux reaction for 2 hours.
  • the mixture was centrifuged and washed 5 times at 8000 r/min for 5 minutes each time to obtain a filter residue.
  • the filter residue was vacuum dried at 100°C for 15 hours to obtain an ester silane coupling agent grafted silica dynamic cross-linking agent.
  • EVA product name is DuPont 770
  • control the temperature of the torque rheometer to 130°C, the rotation speed to 100 rpm, premix for 5 minutes; add 6g of tetrabutyl titanate catalyst, a total of Mix for 5 minutes; add 8g of dynamic cross-linking agent and blend for 30 minutes to obtain a blend.
  • the molding pressure for molding is 10Mpa, and the molding temperature is 120 °C, molding time is 2.5h, and EVA-0 material is obtained.
  • the dynamic cross-linked structure is recycled and reused: cut the EVA-0 material into 0.5-2cm blocks and repeat the molding step to obtain EVA-1 material (that is, the EVA material that has been recycled for the first time); then Repeat the shearing and molding steps to obtain EVA-n, where n represents the number of times of recycling; for example: EVA-0 means that it has not been recycled, and EVA-1 means that EVA-0 has been recycled once to obtain EVA-1.
  • pre-disperse 20g rice calcium carbonate in 500mL ethanol solution ultrasonically disperse at 25°C for 30 minutes, add 10g acetoxypropyltrimethoxysilane, and stir with an external electric stirrer. , control the stirrer speed to 800 r/min, the reaction temperature to 80°C, and conduct the condensation reflux reaction for 2 h.
  • the mixture was centrifuged and washed 5 times at 8000 r/min for 5 minutes each time to obtain a filter residue.
  • the filter residue was vacuum dried at 100°C for 15 hours to obtain an ester silane coupling agent grafted calcium carbonate dynamic cross-linking agent.
  • EVA product name: DuPont 53071
  • control the temperature of the torque rheometer to 130°C, the rotation speed to 100 rpm, and premix for 5 minutes; add 1.5g of acetyl molybdenum (analytical grade) for a total of Mix for 5 minutes; add 8g of dynamic cross-linking agent and 5g of calcium carbonate, and blend for 30 minutes to obtain a blend; place the blend in a flat vulcanizer for vulcanization and molding.
  • the molding pressure of molding is 10 MPa, and the molding temperature is 150 °C, molding time is 2h, and EVA-0 material is obtained.
  • the dynamic cross-linked structure is recycled and reused: cut the EVA-0 material into 0.5-2cm blocks and repeat the molding steps to obtain EVA-1 material; then repeat the shearing and molding steps to obtain EVA- n.
  • silica is pre-dispersed in 500 mL of toluene solution, ultrasonically dispersed at 25°C for 30 minutes, and 7g of 3-(carbonylmethoxy)propyldimethylmethoxysilane is added.
  • Use an external electric stirrer for stirring control the stirrer speed to 800 r/min, the reaction temperature to 80 °C, and the condensation reflux reaction for 2 h.
  • the mixture was centrifuged at 8000 r/min and washed 5 times for 5 min each time to obtain a filter residue.
  • the filter residue was vacuum dried at 100°C for 15 h to obtain an ester silane coupling agent grafted silica dynamic cross-linking agent. .
  • EVA product name is DuPont 53071
  • control the temperature of the torque rheometer to 130°C, the rotation speed to 100rpm, premix for 5 minutes; add 1.5g of tetrabutyl titanate, and blend 5min; add 9g of dynamic cross-linking agent and blend for 30 minutes to obtain a blend; place the blend in a flat vulcanizer for vulcanization and molding.
  • the molding pressure of molding is 10MPa
  • the molding temperature is 150°C
  • the molding time is After 2h, EVA-0 material was obtained.
  • the dynamic cross-linked structure is destroyed for recycling: put the EVA-0 material back into the torque rheometer, control the reaction temperature to 120°C, and the rotation speed to 70 rpm. After completion, perform molding again to obtain EVA-1, repeat The torque rheometer and compression molding steps were reintroduced to obtain EVA-n.
  • Example 3 Repeat the preparation method of Example 3, but add 8g of dynamic cross-linking agent (that is, change the dynamic cross-linking agent content of Example 3 from 9g to 8g), and then add 3g of ADC foaming agent (product name is Junpeng HG2097-91 ), and then blended for 30 minutes, keeping the contents of the other components unchanged, to obtain EVA-0 foam material.
  • 8g of dynamic cross-linking agent that is, change the dynamic cross-linking agent content of Example 3 from 9g to 8g
  • 3g of ADC foaming agent product name is Junpeng HG2097-91
  • EVA product name is DuPont 53071
  • control the temperature of the torque rheometer to 130°C, the rotation speed to 100rpm, premix for 5 minutes; add 1.5g of tetrabutyl titanate, and blend 5 minutes; add 9g of coupling agent KH560 silica and blend for 30 minutes to obtain a blend; place the blend in a flat vulcanizer for vulcanization and molding.
  • the molding pressure of molding is 10MPa and the molding temperature is 150 °C, molding time is 2h, and EVA-0 material is obtained.
  • EVA product name: DuPont 53071
  • the temperature of the torque rheometer to 130°C
  • the rotation speed to 100rpm.
  • Premix for 5 minutes add 1.5g tetrabutyl titanate and blend for 5 minutes; add 20g of silica and 7g of dicumyl peroxide (DCP cross-linking agent) and blend for 30 minutes to obtain a blend; Place it in a flat vulcanizer for vulcanization and molding.
  • the molding pressure of molding is 10MPa, the molding temperature is 150°C, and the molding time is 2h to obtain EVA-0 material.
  • the regenerated EVA obtained in Example 3 has the best effect, and the EVA regenerated foaming material obtained in Example 4 has better performance, meeting the requirements of the ethyl acetate content of EVA and the mole ratio of cross-linking agent triisobutyl borate.
  • the ratio is 3:1; compare to Comparative Example 1, the dosage of ester silane coupling agent is 3g, and the tensile strength of the EVA material obtained due to insufficient cross-linking is low; compare to Comparative Example 2, the dosage of dynamic cross-linking agent is 10g , multiple degrees of cross-linking; compare to Comparative Example 1, silica and 3-(carbonylmethoxy)propyldimethylmethoxysilane were added directly to the torque rheometer, and the silica was not mixed with ester in advance.
  • the silane-like coupling agent was grafted to obtain a dynamic cross-linking agent, but no effective cross-linking system was formed; in Comparative Example 2, KH560 silane coupling agent was used to improve the compatibility between silica and EVA, and the mechanical properties were improved, but no formation of Effective cross-linking system; compared with Comparative Example 3, the traditional DCP cross-linking agent method is directly used.
  • the obtained EVA material has better performance, but cannot be recycled.
  • Example 3 The EVA foam material obtained in Example 3 was observed and photographed through a scanning electron microscope. The obtained photographs are shown in Figures 2 to 4. It can be seen from the figures that the cell diameter is 50 to 150 ⁇ m, and the foam has a Closed cell structure and good shrinkage resistance.

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Abstract

The present invention provides a preparation method for an EVA material. The preparation method comprises the steps of preparation, crosslinking and molding. The present invention further provides an EVA material obtained by using the preparation method. In the present invention, a mechanical blending method is used, and an ester exchange reaction is used under the action of a catalyst so as to obtain an EVA material with dynamic cross-linking bonding. Due to dynamic cross-linking bonding, the cross-linked EVA can be recycled and processed by using a conventional plastic hot-processing method, and after multiple cycles of processing, good mechanical performance is still maintained; relatively good physical and mechanical properties are kept; and the utilization rate is relatively high.

Description

一种EVA材料的制备方法及EVA材料Preparation method of EVA material and EVA material 技术领域Technical field
本发明涉及一种EVA材料,尤其是一种EVA材料的制备方法及EVA材料。The present invention relates to an EVA material, in particular to a preparation method of an EVA material and an EVA material.
背景技术Background technique
全球塑料工业的不断发展,给生活带来极大便利的同时,在世界范围内也产生了大量的塑料废弃物。因此,开发具有更长使用寿命的可持续发展塑料、升级回收或重新利用消费后的聚合物是减少塑料废弃物的有效方法之一。The continuous development of the global plastics industry has brought great convenience to life, and at the same time, it has also produced a large amount of plastic waste around the world. Therefore, developing sustainable plastics with longer lifespans, upcycling or repurposing post-consumer polymers are among the effective ways to reduce plastic waste.
乙烯-醋酸乙烯酯共聚物(EVA)塑料经交联发泡后,制品具有柔软、弹性好、耐化学腐蚀等优良性能,广泛应用于中高档旅游鞋、登山鞋、运动鞋的鞋底和内饰材料。传统的EVA交联方式主要采用不可逆化学交联,这对EVA的回收或重新利用带来了极大的挑战。After ethylene-vinyl acetate copolymer (EVA) plastic is cross-linked and foamed, the products have excellent properties such as softness, good elasticity, and chemical corrosion resistance. They are widely used in the soles and interiors of mid-to-high-end travel shoes, hiking shoes, and sports shoes. Material. The traditional EVA cross-linking method mainly uses irreversible chemical cross-linking, which brings great challenges to the recycling or reuse of EVA.
当前废弃EVA主要是通过焚烧获取热量和再加工利用来处置。焚烧获取热量较为简便,但是焚烧会产生有毒化学物质,利用率低下;再加工主要是将交联EVA通过切碎、研磨成细粉,作为填料替代部分的EVA新料,是当前交联EVA回收的主要方法,但是交联后粉碎的EVA胶粒与EVA新料的相容性较低,因此只能少量添加或少量替代,利用率低。Currently, waste EVA is mainly disposed of through incineration to obtain heat and reprocessing. It is relatively simple to obtain heat through incineration, but incineration will produce toxic chemicals and the utilization rate is low; reprocessing mainly involves chopping and grinding cross-linked EVA into fine powder, and using it as a new EVA material to replace part of the filler, which is the current cross-linked EVA recycling The main method, however, the compatibility of the crushed EVA colloidal particles after cross-linking with the new EVA material is low, so it can only be added or replaced in small amounts, and the utilization rate is low.
有鉴于此,本申请对上述问题进行了深入的研究,遂有本案产生。In view of this, this application conducted an in-depth study on the above issues, and this case emerged.
技术问题technical problem
本发明的目的在于提供一种利用率相对较高的EVA材料的制备方法及EVA材料。The purpose of the present invention is to provide a preparation method and EVA material with a relatively high utilization rate of EVA materials.
技术解决方案Technical solutions
为了实现上述目的,本发明采用如下技术方案:In order to achieve the above objects, the present invention adopts the following technical solutions:
一种EVA材料的制备方法,包括以下步骤:A preparation method of EVA material, including the following steps:
S1、制剂,将填料粒子置于容器中,并将所述填料粒子预分散于甲苯溶剂或乙醇溶剂中获得悬浮液,再往所述悬浮液中加入酯类硅烷偶联剂,经改性反应后获得混合物,将所述混合物经离心洗涤处理获得滤渣,再将所述滤渣进行干燥处理获得动态交联剂;S1. Preparation, place the filler particles in a container, pre-disperse the filler particles in a toluene solvent or an ethanol solvent to obtain a suspension, then add an ester silane coupling agent to the suspension, and undergo a modification reaction Finally, a mixture is obtained, the mixture is centrifuged and washed to obtain a filter residue, and then the filter residue is dried to obtain a dynamic cross-linking agent;
S2、交联,在转矩流变仪中投入EVA原料预分散,然后往所述转矩流变仪中分别加入酯交换催化剂和所述动态交联剂进行共混处理,获得共混物;S2. Cross-linking: put the EVA raw material into the torque rheometer for pre-dispersion, and then add the transesterification catalyst and the dynamic cross-linking agent to the torque rheometer respectively for blending processing to obtain a blend;
S3、成型,依次对所述共混物进行硫化处理和模压成型获得EVA材料。S3. Molding. The blend is vulcanized and molded sequentially to obtain an EVA material.
作为本发明的一种改进,在步骤S1中,分3-5次往所述容器中加入所述酯类硅烷偶联剂,加入所述酯类硅烷偶联剂的同时对所述容器内的溶液进行搅拌处理,搅拌处理的搅拌转速为500-1500 r/min,然后在70-110℃的条件下冷凝回流2h。As an improvement of the present invention, in step S1, add the ester silane coupling agent into the container in 3-5 times, and while adding the ester silane coupling agent, clean the contents in the container. The solution is stirred at a stirring speed of 500-1500 r/min, and then condensed and refluxed at 70-110°C for 2 hours.
作为本发明的一种改进,所述填料粒子为二氧化硅和/或碳酸钙,所述填料粒子的粒径为20~2000 nm,所述填料粒子的质量分数为1%-10%,所述酯类硅烷偶联剂为2-羰基甲氧基乙基二甲氧基甲基硅烷、乙酰氧基丙基三甲氧基硅烷、3-(羰基甲氧基)丙基二甲基甲氧基硅烷和3-(羰乙氧基)丙基二甲基乙氧基硅烷中的一种或两种,所述EVA原料为乙酸乙酯含量为10-30%的热塑性未硫化交联EVA,所述酯交换催化剂为钛酸四丁酯、钛酸四乙酯、钛酸四异丙酯或乙酰钼。As an improvement of the present invention, the filler particles are silica and/or calcium carbonate, the particle size of the filler particles is 20-2000 nm, and the mass fraction of the filler particles is 1%-10%, so The above-mentioned ester silane coupling agents are 2-carbonylmethoxyethyldimethoxymethylsilane, acetoxypropyltrimethoxysilane, and 3-(carbonylmethoxy)propyldimethylmethoxy One or both of silane and 3-(carbonylethoxy)propyldimethylethoxysilane, the EVA raw material is thermoplastic unvulcanized cross-linked EVA with an ethyl acetate content of 10-30%, so The transesterification catalyst is tetrabutyl titanate, tetraethyl titanate, tetraisopropyl titanate or acetyl molybdenum.
作为本发明的一种改进,在步骤S1中,在20-40℃的条件下利用超声进行对所述填料粒子进行预分散20-40min。As an improvement of the present invention, in step S1, the filler particles are pre-dispersed using ultrasound at 20-40°C for 20-40 minutes.
作为本发明的一种改进,在步骤S1中,进行离心洗涤处理时,将所述混合物以8000~12000 r/min的转速离心处理3-5次,每次离心处理的时间为3-7 min。As an improvement of the present invention, in step S1, when performing centrifugal washing treatment, the mixture is centrifuged 3-5 times at a speed of 8000-12000 r/min, and the time of each centrifugal treatment is 3-7 min. .
作为本发明的一种改进,在步骤S1中,进行干燥处理时,将所述滤渣在80-120℃的条件下真空干燥8-20 h。As an improvement of the present invention, in step S1, during the drying process, the filter residue is vacuum dried at 80-120°C for 8-20 h.
作为本发明的一种改进,在步骤S2中,控制所述转矩流变仪反应温度为100~180℃,转速为50~200 rpm。As an improvement of the present invention, in step S2, the reaction temperature of the torque rheometer is controlled to be 100-180°C and the rotation speed is 50-200 rpm.
作为本发明的一种改进,在步骤S2中,预分散时间为5-10min,将所述酯交换催化剂分3-5次加入所述转矩流变仪中,然后混合10-30min,再将所述动态交联剂分3-5次加入所述转矩流变仪中,然后共混处理10-30min。As an improvement of the present invention, in step S2, the pre-dispersion time is 5-10 min, the transesterification catalyst is added into the torque rheometer in 3-5 times, and then mixed for 10-30 min, and then The dynamic cross-linking agent is added into the torque rheometer in 3-5 times, and then blended for 10-30 minutes.
作为本发明的一种改进,在步骤S3中,模压成型时,模压压力为5-20 MPa ,模压温度为120-180℃,模压时间为0.5-2h。As an improvement of the present invention, in step S3, during molding, the molding pressure is 5-20 MPa, the molding temperature is 120-180°C, and the molding time is 0.5-2h.
一种EVA材料,包括10-30质量份填料粒子、1-10质量份酯类硅烷偶联剂、70-100质量份EVA、 0.1-2.5质量份酯交换催化剂和1-10质量份动态交联剂,采用上述EVA材料的制备方法制作获得。An EVA material, including 10-30 parts by mass of filler particles, 1-10 parts by mass of ester silane coupling agent, 70-100 parts by mass of EVA, 0.1-2.5 parts by mass of transesterification catalyst and 1-10 parts by mass of dynamic cross-linking The agent is prepared using the above preparation method of EVA material.
有益效果beneficial effects
采用上述技术方案,本发明具有以下有益效果:Adopting the above technical solution, the present invention has the following beneficial effects:
本发明采用机械共混法,在催化剂作用下利用酯交换反应,得到了具有动态交联键合的EVA材料,该动态交联键合使得交联后的EVA可以采用常规的塑料热加工方法进行回收加工,并在多次循环加工后仍保持良好的力学性能,并保持较好的物理力学性能,利用率相对较高。The present invention adopts a mechanical blending method and uses transesterification reaction under the action of a catalyst to obtain an EVA material with dynamic cross-linking bonding. The dynamic cross-linking bonding allows the cross-linked EVA to be processed using conventional plastic thermal processing methods. It is recycled and processed, and it still maintains good mechanical properties after multiple cycles of processing, and maintains good physical and mechanical properties, and the utilization rate is relatively high.
附图说明Description of drawings
图1为实施例中动态交联剂的结构示意图;Figure 1 is a schematic structural diagram of the dynamic cross-linking agent in the embodiment;
图2为实施例3中EVA-1发泡材料的扫描电镜图;Figure 2 is a scanning electron microscope image of the EVA-1 foam material in Example 3;
图3为实施例3中EVA-2发泡材料的扫描电镜图;Figure 3 is a scanning electron microscope image of the EVA-2 foam material in Example 3;
图4为实施例3中EVA-3发泡材料的扫描电镜图。Figure 4 is a scanning electron microscope image of the EVA-3 foam material in Example 3.
图中标识对应如下:The symbols in the figure correspond to the following:
    1-填料粒子;           2-酯类硅烷偶联剂。1-Filler particles; 2-Ester silane coupling agent.
本发明的实施方式Embodiments of the invention
下面结合具体实施例对本发明做进一步的说明,以下实施例和比较例中所采用的原料以及试验仪器都可以从市场上直接购买获得,其中未注明具体条件的试验步骤或测试步骤,都是按照常规条件,或按照试验仪器制造厂商所建议的条件进行的,此处不再详述。The present invention will be further described below with reference to specific examples. The raw materials and test instruments used in the following examples and comparative examples can be purchased directly from the market. The test steps or test steps without specifying specific conditions are It is carried out in accordance with conventional conditions or in accordance with the conditions recommended by the test instrument manufacturer, which will not be described in detail here.
本发明提供一种EVA材料的制备方法,以机械共混法,利用EVA中含有的羧酸酯和含有多元烷基酯类的交联剂之间发生酯交换反应制备多元交联EVA材料,通过改变交联剂的使用和种类,控制交联网络的动力学,调控EVA材料的动态交联结构和物理机械性能。该方法包括以下步骤:The present invention provides a method for preparing EVA materials, which uses a mechanical blending method to utilize the transesterification reaction between carboxylic acid esters contained in EVA and cross-linking agents containing polyvalent alkyl esters to prepare multi-component cross-linked EVA materials. Change the use and type of cross-linking agent, control the dynamics of the cross-linking network, and regulate the dynamic cross-linking structure and physical and mechanical properties of EVA materials. The method includes the following steps:
S1、制剂,将填料粒子置于容器中,其中,填料粒子可以为二氧化硅和/或碳酸钙,填料粒子的粒径为20~2000 nm,填料粒子的质量分数为1%-10%。S1. Preparation, place filler particles in a container, where the filler particles can be silica and/or calcium carbonate, the particle size of the filler particles is 20-2000 nm, and the mass fraction of the filler particles is 1%-10%.
接着将填料粒子预分散于甲苯溶剂或乙醇溶剂中获得均匀的悬浮液,具体的,在20-40℃的条件下利用超声进行对所述填料粒子进行预分散20-40min。接着往悬浮液中加入酯类硅烷偶联剂,经改性反应后获得混合物,其中,酯类硅烷偶联剂可以为2-羰基甲氧基乙基二甲氧基甲基硅烷、乙酰氧基丙基三甲氧基硅烷、3-(羰基甲氧基)丙基二甲基甲氧基硅烷和3-(羰乙氧基)丙基二甲基乙氧基硅烷中的一种或两种。优选的,分3-5次往容器中加入酯类硅烷偶联剂,加入酯类硅烷偶联剂的同时对容器内的溶液(及悬浮液)进行搅拌处理,搅拌处理的搅拌转速为500-1500 r/min,然后在70-110℃的条件下冷凝回流2h。Then, the filler particles are pre-dispersed in a toluene solvent or an ethanol solvent to obtain a uniform suspension. Specifically, the filler particles are pre-dispersed using ultrasound at 20-40°C for 20-40 minutes. Then, an ester silane coupling agent is added to the suspension, and a mixture is obtained after a modification reaction. The ester silane coupling agent can be 2-carbonylmethoxyethyldimethoxymethylsilane, acetoxy One or two of propyltrimethoxysilane, 3-(carbonylmethoxy)propyldimethylmethoxysilane and 3-(carbonylethoxy)propyldimethylethoxysilane. Preferably, the ester silane coupling agent is added to the container in 3-5 times, and the solution (and suspension) in the container is stirred while adding the ester silane coupling agent. The stirring speed of the stirring process is 500-500. 1500 r/min, and then condense and reflux for 2 hours at 70-110°C.
将混合物经离心洗涤处理获得滤渣,进行离心洗涤处理时,将混合物以8000~12000 r/min的转速离心处理3-5次,每次离心处理的时间为3-7 min;之后将滤渣进行干燥处理获得动态交联剂,进行干燥处理时,将滤渣在80-120℃的条件下真空干燥8-20 h。如图1所示,本发明获得的动态交联剂具有主要有填料粒子1形成的硬段结构,利用该硬段结构连接酯类硅烷偶联剂2,具有较好的稳定性。The mixture is centrifuged and washed to obtain the filter residue. When performing centrifugal washing, the mixture is centrifuged 3-5 times at a speed of 8000-12000 r/min, and the centrifugation time for each time is 3-7 min; the filter residue is then dried. The dynamic cross-linking agent is obtained through the treatment. During the drying process, the filter residue is vacuum dried at 80-120°C for 8-20 h. As shown in Figure 1, the dynamic cross-linking agent obtained by the present invention has a hard segment structure mainly formed by filler particles 1. This hard segment structure is used to connect the ester silane coupling agent 2, which has good stability.
S2、交联,在转矩流变仪中投入EVA原料并进行预分散,控制转矩流变仪反应温度为100~180℃,转速为50~200 rpm,预分散的时间为5-10min。需要说明的是,上述EVA原料为乙酸乙酯含量为10-30%的热塑性未硫化交联EVA。S2. Cross-linking, put EVA raw materials into the torque rheometer and perform pre-dispersion. Control the reaction temperature of the torque rheometer to be 100-180°C, the rotation speed is 50-200 rpm, and the pre-dispersion time is 5-10 minutes. It should be noted that the above-mentioned EVA raw material is thermoplastic unvulcanized cross-linked EVA with an ethyl acetate content of 10-30%.
然后往转矩流变仪中分别加入酯交换催化剂和动态交联剂进行共混处理,获得共混物,其中,酯交换催化剂为钛酸四丁酯、钛酸四乙酯、钛酸四异丙酯或乙酰钼。将酯交换催化剂分3-5次加入转矩流变仪中,然后混合10-30min,再将动态交联剂分3-5次加入转矩流变仪中,然后共混处理10-30min。Then, the transesterification catalyst and the dynamic cross-linking agent were respectively added to the torque rheometer for blending treatment to obtain a blend, in which the transesterification catalyst was tetrabutyl titanate, tetraethyl titanate, and tetraisotitanate. propyl ester or acetyl molybdenum. Add the transesterification catalyst into the torque rheometer in 3-5 times, and then mix for 10-30 minutes. Add the dynamic cross-linking agent into the torque rheometer in 3-5 times, and then blend for 10-30 minutes.
S3、成型,依次对共混物进行硫化处理和模压成型获得EVA材料,其中,硫化处理采用平板硫化仪进行,模压成型时,模压压力为5-20 MPa ,模压温度为120-180℃,模压时间为0.5-2h。S3. Molding. The blend is vulcanized and molded in sequence to obtain EVA material. The vulcanization treatment is performed using a flat vulcanizer. During molding, the molding pressure is 5-20 MPa and the molding temperature is 120-180°C. The time is 0.5-2h.
本发明还提供了一种EVA材料,包括10-30质量份填料粒子、1-10质量份酯类硅烷偶联剂、70-100质量份EVA、 0.1-2.5质量份酯交换催化剂和1-10质量份动态交联剂,采用上述EVA材料的制备方法制作获得。The invention also provides an EVA material, including 10-30 parts by mass filler particles, 1-10 parts by mass ester silane coupling agent, 70-100 parts by mass EVA, 0.1-2.5 parts by mass transesterification catalyst and 1-10 parts by mass The mass part of dynamic cross-linking agent is prepared by using the above preparation method of EVA material.
本发明规避了传统的不可逆化学交联方法,利用EVA中含有的羧酸酯和含有多元烷基酯类的特定交联剂之间发生酯交换反应制备多元交联EVA材料。EVA中含有大量的C=O键,不饱和键的存在使得EVA对紫外线照射敏感,易被氧化,耐候性差,长时间暴露后易老化而失效,通过酯交换形成动态交联EVA,减少聚合物中不饱和双键的含量,有效提高其抗紫外性能和高温稳定性,延长使用时间。与传统热塑性塑料的比较,由于交联网络的形成,该网络有助于稳定再加工过程中的分子结构,防止聚合物链的断裂。本发明采用含酯类硅烷偶联剂与填料粒子预先水解反应,得到具有硬段(填料粒子)结构的酯基动态交联剂,在酯交换催化剂的作用下,酯基动态交联剂与EVA的羧酸酯发生酯交换反应制备多元交联EVA材料,显示出良好的再加工性,并保持较好的物理力学性能;在EVA分子链中嵌入了补强粒子,规避了简单机械共混带来的团聚问题,有效提高可以回收利用EVA材料的力学性能。The invention circumvents the traditional irreversible chemical cross-linking method and utilizes the transesterification reaction between the carboxylic acid ester contained in EVA and a specific cross-linking agent containing polyvalent alkyl esters to prepare multi-component cross-linked EVA materials. EVA contains a large number of C=O bonds. The presence of unsaturated bonds makes EVA sensitive to ultraviolet radiation, easily oxidized, and has poor weather resistance. It is prone to aging and failure after long-term exposure. Dynamic cross-linked EVA is formed through transesterification, which reduces the polymer The content of medium unsaturated double bonds effectively improves its UV resistance and high temperature stability and extends its use time. Compared with traditional thermoplastics, due to the formation of a cross-linked network, this network helps stabilize the molecular structure during reprocessing and prevents the breakage of the polymer chains. The present invention adopts a pre-hydrolysis reaction between an ester-containing silane coupling agent and filler particles to obtain an ester-based dynamic cross-linking agent with a hard segment (filler particle) structure. Under the action of the transesterification catalyst, the ester-based dynamic cross-linking agent and EVA The transesterification reaction of carboxylic acid esters produces multi-element cross-linked EVA materials, which shows good reprocessability and maintains good physical and mechanical properties; reinforcing particles are embedded in the EVA molecular chain to avoid simple mechanical blending. It solves the agglomeration problem and effectively improves the mechanical properties of EVA materials that can be recycled.
下面通过几个实施例和对比例对本发明的EVA材料的制备方法及EVA材料作进一步说明。The preparation method and EVA material of the EVA material of the present invention will be further described below through several examples and comparative examples.
实施例1Example 1
按照上述EVA材料的制备方法,将20g二氧化硅预分散于500 mL甲苯溶液中,在25℃下超声分散30min,加入3g的2-羰基甲氧基乙基二甲氧基甲基硅烷,利用外置电动搅拌器进行搅拌,控制搅拌器转速为800 r/min,反应温度为80 ℃,冷凝回流反应2h。混合物经8000 r/min离心洗涤5次,每次时间为5min,得到滤渣,滤渣经100℃真空干燥,干燥时间为15h,得到酯类硅烷偶联剂接枝二氧化硅动态交联剂。According to the preparation method of the above EVA material, 20g of silica is pre-dispersed in 500 mL of toluene solution, ultrasonically dispersed at 25°C for 30 minutes, and 3g of 2-carbonylmethoxyethyldimethoxymethylsilane is added. Stir with an external electric stirrer. Control the stirrer speed to 800 r/min, the reaction temperature to 80°C, and the condensation reflux reaction for 2 hours. The mixture was centrifuged and washed 5 times at 8000 r/min for 5 minutes each time to obtain a filter residue. The filter residue was vacuum dried at 100°C for 15 hours to obtain an ester silane coupling agent grafted silica dynamic cross-linking agent.
在转矩流变仪中,投入100g的 EVA(产品名称为杜邦770),控制转矩流变仪温度为130 ℃,转速为100 rpm,预混合5min;加入6g钛酸四丁酯催化剂,共混5min;加入8g动态交联剂,共混30min获得共混物,停放一段时间之后,将共混物放置于平板硫化仪进行硫化处理和模压成型,模压成型的模压压力为10Mpa,模压温度为120 ℃,模压时间为2.5h,得到EVA-0材料。In the torque rheometer, put 100g of EVA (product name is DuPont 770), control the temperature of the torque rheometer to 130°C, the rotation speed to 100 rpm, premix for 5 minutes; add 6g of tetrabutyl titanate catalyst, a total of Mix for 5 minutes; add 8g of dynamic cross-linking agent and blend for 30 minutes to obtain a blend. After leaving it for a period of time, place the blend in a flat vulcanizer for vulcanization and molding. The molding pressure for molding is 10Mpa, and the molding temperature is 120 ℃, molding time is 2.5h, and EVA-0 material is obtained.
最后,采用不破坏动态交联结构回收再利用:将EVA-0材料剪切成0.5-2cm块状,重复模压成型步骤,得到EVA-1材料(即经过第一次回收的EVA材料);之后重复剪切和模压成型步骤,得到EVA-n,其中,n代表回收第几次;例:EVA-0表示未经过回收,EVA-1表示EVA-0经过回收1次得到EVA-1。Finally, the dynamic cross-linked structure is recycled and reused: cut the EVA-0 material into 0.5-2cm blocks and repeat the molding step to obtain EVA-1 material (that is, the EVA material that has been recycled for the first time); then Repeat the shearing and molding steps to obtain EVA-n, where n represents the number of times of recycling; for example: EVA-0 means that it has not been recycled, and EVA-1 means that EVA-0 has been recycled once to obtain EVA-1.
实施例2Example 2
按照上述EVA材料的制备方法,将20g米碳酸钙预分散于500mL乙醇溶液中,25 ℃下超声分散30min,加入10g的乙酰氧基丙基三甲氧基硅烷,,利用外置电动搅拌器进行搅拌,控制搅拌器转速为800 r/min,反应温度为80 ℃,冷凝回流反应2 h。混合物经8000 r/min离心洗涤5次,每次时间为5min,得到滤渣,滤渣经100℃真空干燥,干燥时间为15h,得到酯类硅烷偶联剂接枝碳酸钙动态交联剂。According to the above preparation method of EVA material, pre-disperse 20g rice calcium carbonate in 500mL ethanol solution, ultrasonically disperse at 25°C for 30 minutes, add 10g acetoxypropyltrimethoxysilane, and stir with an external electric stirrer. , control the stirrer speed to 800 r/min, the reaction temperature to 80°C, and conduct the condensation reflux reaction for 2 h. The mixture was centrifuged and washed 5 times at 8000 r/min for 5 minutes each time to obtain a filter residue. The filter residue was vacuum dried at 100°C for 15 hours to obtain an ester silane coupling agent grafted calcium carbonate dynamic cross-linking agent.
在转矩流变仪中,投入100g的EVA(产品名称为杜邦53071),控制转矩流变仪温度为130 ℃,转速为100 rpm,预混合5min;加入1.5g乙酰钼(分析纯)共混5min;加入8g动态交联剂,5g碳酸钙,共混30min获得共混物;将共混物放置于平板硫化仪进行硫化处理和模压成型,模压成型的模压压力为10 MPa,模压温度为150 ℃,模压时间为2h,得到EVA-0材料。In the torque rheometer, put 100g of EVA (product name: DuPont 53071), control the temperature of the torque rheometer to 130°C, the rotation speed to 100 rpm, and premix for 5 minutes; add 1.5g of acetyl molybdenum (analytical grade) for a total of Mix for 5 minutes; add 8g of dynamic cross-linking agent and 5g of calcium carbonate, and blend for 30 minutes to obtain a blend; place the blend in a flat vulcanizer for vulcanization and molding. The molding pressure of molding is 10 MPa, and the molding temperature is 150 ℃, molding time is 2h, and EVA-0 material is obtained.
最后,采用不破坏动态交联结构回收再利用:将EVA-0材料剪切成0.5-2cm块状,重复模压成型步骤,得到EVA-1材料;之后重复剪切和模压成型步骤,得到EVA-n。Finally, the dynamic cross-linked structure is recycled and reused: cut the EVA-0 material into 0.5-2cm blocks and repeat the molding steps to obtain EVA-1 material; then repeat the shearing and molding steps to obtain EVA- n.
实施例3Example 3
按照上述EVA材料的制备方法,将20g二氧化硅预分散于500 mL甲苯溶液中,25 ℃下超声分散30min,加入7g的3-(羰基甲氧基)丙基二甲基甲氧基硅烷,利用外置电动搅拌器进行搅拌,控制搅拌器转速为800 r/min,反应温度为80 ℃,冷凝回流反应2 h。混合物经8000 r/min离心洗涤5次,每次时间为5 min,得到滤渣,滤渣经100℃真空干燥,干燥时间为15 h,得到酯类硅烷偶联剂接枝二氧化硅动态交联剂。According to the preparation method of the above EVA material, 20g of silica is pre-dispersed in 500 mL of toluene solution, ultrasonically dispersed at 25°C for 30 minutes, and 7g of 3-(carbonylmethoxy)propyldimethylmethoxysilane is added. Use an external electric stirrer for stirring, control the stirrer speed to 800 r/min, the reaction temperature to 80 °C, and the condensation reflux reaction for 2 h. The mixture was centrifuged at 8000 r/min and washed 5 times for 5 min each time to obtain a filter residue. The filter residue was vacuum dried at 100°C for 15 h to obtain an ester silane coupling agent grafted silica dynamic cross-linking agent. .
在转矩流变仪中,投入100g的EVA(产品名称为杜邦53071),控制转矩流变仪温度为130 ℃,转速为100rpm,预混合5min;加入1.5g钛酸四丁酯,共混5min;加入9g动态交联剂,共混30min获得共混物;将共混物放置于平板硫化仪进行硫化处理和模压成型,模压成型的模压压力为10MPa,模压温度为150 ℃,模压时间为2h,得到EVA-0材料。In the torque rheometer, put 100g of EVA (product name is DuPont 53071), control the temperature of the torque rheometer to 130°C, the rotation speed to 100rpm, premix for 5 minutes; add 1.5g of tetrabutyl titanate, and blend 5min; add 9g of dynamic cross-linking agent and blend for 30 minutes to obtain a blend; place the blend in a flat vulcanizer for vulcanization and molding. The molding pressure of molding is 10MPa, the molding temperature is 150°C, and the molding time is After 2h, EVA-0 material was obtained.
最后,采用破坏动态交联结构回收再利用:将EVA-0材料重新投入转矩流变仪中,控制反应温度为120 ℃,转速为70rpm,完成之后再次进行模压成型,得到EVA-1,重复重新投入转矩流变仪和模压成型步骤,得到EVA-n。Finally, the dynamic cross-linked structure is destroyed for recycling: put the EVA-0 material back into the torque rheometer, control the reaction temperature to 120°C, and the rotation speed to 70 rpm. After completion, perform molding again to obtain EVA-1, repeat The torque rheometer and compression molding steps were reintroduced to obtain EVA-n.
实施例4Example 4
重复实施例3的制备方法,但是加入8g动态交联剂(即将实施例3的动态交联剂含量由9g改为8g),随后加入3g的ADC发泡剂(产品名称为骏鹏HG2097-91),再共混30min,其余组分的含量保持不变,得到EVA-0发泡材料。Repeat the preparation method of Example 3, but add 8g of dynamic cross-linking agent (that is, change the dynamic cross-linking agent content of Example 3 from 9g to 8g), and then add 3g of ADC foaming agent (product name is Junpeng HG2097-91 ), and then blended for 30 minutes, keeping the contents of the other components unchanged, to obtain EVA-0 foam material.
采用破坏动态交联结构回收再利用:将EVA-0材料重新投入转矩流变仪中,控制反应温度为120 ℃,转速为70rpm,同时添加3g的ADC发泡剂,完成之后再次进行模压成型,得到EVA-1,重复重新投入转矩流变仪和模压成型步骤,得到EVA-n。Recycling and reusing by destroying the dynamic cross-linked structure: Put the EVA-0 material back into the torque rheometer, control the reaction temperature to 120°C, the rotation speed to 70rpm, and add 3g of ADC foaming agent at the same time. After completion, mold it again , EVA-1 was obtained, and the steps of re-entering the torque rheometer and molding were repeated to obtain EVA-n.
对比例1Comparative example 1
参照上述EVA材料的制备方法中的步骤S2和步骤S3,在转矩流变仪中,投入100g的EVA(杜邦53071),控制转矩流变仪温度为130 ℃,转速为100rpm,预混合5min;加入1.5g钛酸四丁酯,共混5min;加入9g未改性二氧化硅,共混30 min获得共混物;将共混物放置于平板硫化仪进行硫化处理和模压成型,模压成型的模压压力为10MPa,模压温度为150 ℃,模压时间为2h,得到EVA-0材料。Referring to steps S2 and S3 in the preparation method of the above EVA material, put 100g of EVA (DuPont 53071) into the torque rheometer, control the temperature of the torque rheometer to 130°C, the rotation speed to 100rpm, and premix for 5 minutes. ;Add 1.5g tetrabutyl titanate and blend for 5 minutes; add 9g of unmodified silica and blend for 30 minutes to obtain a blend; place the blend in a flat vulcanizer for vulcanization and molding, and molding The molding pressure is 10MPa, the molding temperature is 150°C, the molding time is 2h, and the EVA-0 material is obtained.
采用破坏动态交联结构回收再利用:将EVA-0材料重新投入转矩流变仪中,控制反应温度为120 ℃,转速为70rpm,完成之后再次进行模压成型,得到EVA-1,重复重新投入转矩流变仪和模压成型步骤,得到EVA-n。Recycling and reusing by destroying the dynamic cross-linked structure: Put the EVA-0 material back into the torque rheometer, control the reaction temperature to 120 ℃, and the rotation speed to 70 rpm. After completion, mold it again to obtain EVA-1, and put it back in again. Torque rheometer and compression molding steps to obtain EVA-n.
对比例2Comparative example 2
参照上述EVA材料的制备方法,将20质量份二氧化硅预分散于500mL甲苯溶液中,25 ℃下超声分散30min,加入常规的硅烷偶联剂KH560,利用外置电动搅拌器进行搅拌,控制搅拌器转速为800 r/min,反应温度为80 ℃,冷凝回流反应2 h。混合物经过8000 r/min离心洗涤5次,每次时间为4 min,得到滤渣,滤渣经100℃真空干燥,干燥时间为12h,得到偶联剂KH560接枝二氧化硅。Referring to the above preparation method of EVA material, pre-disperse 20 parts by mass of silica in 500 mL of toluene solution, ultrasonically disperse at 25°C for 30 minutes, add conventional silane coupling agent KH560, stir with an external electric stirrer, and control the stirring The rotation speed of the reactor was 800 r/min, the reaction temperature was 80°C, and the condensation reflux reaction was carried out for 2 h. The mixture was centrifuged and washed 5 times at 8000 r/min for 4 minutes each time to obtain a filter residue. The filter residue was vacuum dried at 100°C for 12 hours to obtain the coupling agent KH560 grafted silica.
在转矩流变仪中,投入100g的EVA(产品名称为杜邦53071),控制转矩流变仪温度为130 ℃,转速为100rpm,预混合5min;加入1.5g钛酸四丁酯,共混5 min;加入9g偶联剂KH560二氧化硅,共混30 min获得共混物;将共混物放置于平板硫化仪进行硫化处理和模压成型,模压成型的模压压力为10MPa ,模压温度为150 ℃,模压时间为2h,得到EVA-0材料。In the torque rheometer, put 100g of EVA (product name is DuPont 53071), control the temperature of the torque rheometer to 130°C, the rotation speed to 100rpm, premix for 5 minutes; add 1.5g of tetrabutyl titanate, and blend 5 minutes; add 9g of coupling agent KH560 silica and blend for 30 minutes to obtain a blend; place the blend in a flat vulcanizer for vulcanization and molding. The molding pressure of molding is 10MPa and the molding temperature is 150 ℃, molding time is 2h, and EVA-0 material is obtained.
采用破坏动态交联结构回收再利用:将EVA-0材料重新投入转矩流变仪中,控制反应温度为120 ℃,转速为70rpm,完成之后再次进行模压成型,得到EVA-1,重复重新投入转矩流变仪和模压成型步骤,得到EVA-n。Recycling and reusing by destroying the dynamic cross-linked structure: Put the EVA-0 material back into the torque rheometer, control the reaction temperature to 120 ℃, and the rotation speed to 70 rpm. After completion, mold it again to obtain EVA-1, and put it back in again. Torque rheometer and compression molding steps to obtain EVA-n.
对比例3Comparative example 3
参照上述EVA材料的制备方法中的步骤S2和步骤S3,在转矩流变仪中,投入100g的EVA(产品名称为杜邦53071),控制转矩流变仪温度为130℃,转速为100rpm,预混合5min;加入1.5g钛酸四丁酯,共混5min;加入20g二氧化硅,7g过氧化二异丙苯(DCP交联剂),共混30 min获得共混物;将共混物放置于平板硫化仪进行硫化处理和模压成型,模压成型的模压压力为10MPa ,模压温度为150℃,模压时间为2h,得到EVA-0材料。Referring to steps S2 and S3 in the preparation method of the above EVA material, put 100g of EVA (product name: DuPont 53071) into the torque rheometer, control the temperature of the torque rheometer to 130°C, and the rotation speed to 100rpm. Premix for 5 minutes; add 1.5g tetrabutyl titanate and blend for 5 minutes; add 20g of silica and 7g of dicumyl peroxide (DCP cross-linking agent) and blend for 30 minutes to obtain a blend; Place it in a flat vulcanizer for vulcanization and molding. The molding pressure of molding is 10MPa, the molding temperature is 150°C, and the molding time is 2h to obtain EVA-0 material.
采用破坏动态交联结构回收再利用:将EVA-0材料重新投入转矩流变仪中,控制反应温度为120 ℃,转速为70rpm,完成之后再次进行模压成型,得到EVA-1,重复重新投入转矩流变仪和模压成型步骤,得到EVA-n。Recycling and reusing by destroying the dynamic cross-linked structure: Put the EVA-0 material back into the torque rheometer, control the reaction temperature to 120 ℃, and the rotation speed to 70 rpm. After completion, mold it again to obtain EVA-1, and put it back in again. Torque rheometer and compression molding steps to obtain EVA-n.
对上述各实施例和各对比例所获得的EVA材料的物理机械性能进行检测,结果如下表所示。The physical and mechanical properties of the EVA materials obtained in each of the above examples and comparative examples were tested, and the results are as shown in the table below.
从上表可以看出,实施例3得到的再生EVA效果最好,实施例4得到的EVA再生发泡材料的性能较好,满足EVA的乙酸乙酯含量与交联剂硼酸三异丁酯摩尔比为3:1;比较对比例1,其酯类硅烷偶联剂用量为3g,因交联不充分得到的EVA材料拉伸强度较低;比较对比例2,其动态交联剂量用量为10g,多度交联;比较对比例1,在转矩流变仪中直接加入二氧化硅和3-(羰基甲氧基)丙基二甲基甲氧基硅烷,二氧化硅并未预先和酯类硅烷偶联剂接枝得到动态交联剂,没有形成有效交联体系;对比实施例2,采取KH560硅烷偶联剂,提高二氧化硅和EVA的相容性,力学性能提高,但是没有形成有效交联体系;对比对比例3,直接采用传统的DCP交联剂方式,得到的EVA材料性能较好,但无法回收使用。As can be seen from the above table, the regenerated EVA obtained in Example 3 has the best effect, and the EVA regenerated foaming material obtained in Example 4 has better performance, meeting the requirements of the ethyl acetate content of EVA and the mole ratio of cross-linking agent triisobutyl borate. The ratio is 3:1; compare to Comparative Example 1, the dosage of ester silane coupling agent is 3g, and the tensile strength of the EVA material obtained due to insufficient cross-linking is low; compare to Comparative Example 2, the dosage of dynamic cross-linking agent is 10g , multiple degrees of cross-linking; compare to Comparative Example 1, silica and 3-(carbonylmethoxy)propyldimethylmethoxysilane were added directly to the torque rheometer, and the silica was not mixed with ester in advance. The silane-like coupling agent was grafted to obtain a dynamic cross-linking agent, but no effective cross-linking system was formed; in Comparative Example 2, KH560 silane coupling agent was used to improve the compatibility between silica and EVA, and the mechanical properties were improved, but no formation of Effective cross-linking system; compared with Comparative Example 3, the traditional DCP cross-linking agent method is directly used. The obtained EVA material has better performance, but cannot be recycled.
通过扫描电镜对实施例3所获得的EVA发泡材料进行观察并拍照,所获得的照片如图2-图4所示,从图中可以看出,泡孔直径为50~150 μm,泡沫呈闭孔结构并具有良好的抗收缩性。The EVA foam material obtained in Example 3 was observed and photographed through a scanning electron microscope. The obtained photographs are shown in Figures 2 to 4. It can be seen from the figures that the cell diameter is 50 to 150 μm, and the foam has a Closed cell structure and good shrinkage resistance.
上面结合具体实施例对本发明做了详细的说明,但是本发明的实施方式并不仅限于上述实施方式,本领域技术人员根据现有技术可以对本发明做出各种变形,这些都属于本发明的保护范围。The present invention has been described in detail above with reference to specific embodiments. However, the implementation of the present invention is not limited to the above-mentioned embodiments. Those skilled in the art can make various modifications to the present invention based on the existing technology, and these all belong to the protection of the present invention. scope.

Claims (10)

  1. 一种EVA材料的制备方法,其特征在于,包括以下步骤:A method for preparing EVA material, which is characterized by including the following steps:
    S1、制剂,将填料粒子置于容器中,并将所述填料粒子预分散于甲苯溶剂或乙醇溶剂中获得悬浮液,再往所述悬浮液中加入酯类硅烷偶联剂,经改性反应后获得混合物,将所述混合物经离心洗涤处理获得滤渣,再将所述滤渣进行干燥处理获得动态交联剂;S1. Preparation, place the filler particles in a container, pre-disperse the filler particles in a toluene solvent or an ethanol solvent to obtain a suspension, then add an ester silane coupling agent to the suspension, and undergo a modification reaction Finally, a mixture is obtained, the mixture is centrifuged and washed to obtain a filter residue, and then the filter residue is dried to obtain a dynamic cross-linking agent;
    S2、交联,在转矩流变仪中投入EVA原料预分散,然后往所述转矩流变仪中分别加入酯交换催化剂和所述动态交联剂进行共混处理,获得共混物;S2. Cross-linking: put the EVA raw material into the torque rheometer for pre-dispersion, and then add the transesterification catalyst and the dynamic cross-linking agent to the torque rheometer respectively for blending processing to obtain a blend;
    S3、成型,依次对所述共混物进行硫化处理和模压成型获得EVA材料。S3. Molding. The blend is vulcanized and molded sequentially to obtain an EVA material.
  2. 如权利要求1所述的EVA材料的制备方法,其特征在于,在步骤S1中,分3-5次往所述容器中加入所述酯类硅烷偶联剂,加入所述酯类硅烷偶联剂的同时对所述容器内的溶液进行搅拌处理,搅拌处理的搅拌转速为500-1500 r/min,然后在70-110℃的条件下冷凝回流2h。The preparation method of EVA material according to claim 1, characterized in that, in step S1, add the ester silane coupling agent into the container in 3-5 times, add the ester silane coupling agent While adding the solution, stir the solution in the container at a stirring speed of 500-1500 r/min, and then condense and reflux for 2 hours at 70-110°C.
  3. 如权利要求1所述的EVA材料的制备方法,其特征在于,所述填料粒子为二氧化硅和/或碳酸钙,所述填料粒子的粒径为20~2000 nm,所述填料粒子的质量分数为1%-10%,所述酯类硅烷偶联剂为2-羰基甲氧基乙基二甲氧基甲基硅烷、乙酰氧基丙基三甲氧基硅烷、3-(羰基甲氧基)丙基二甲基甲氧基硅烷和3-(羰乙氧基)丙基二甲基乙氧基硅烷中的一种或两种,所述EVA原料为乙酸乙酯含量为10-30%的热塑性未硫化交联EVA,所述酯交换催化剂为钛酸四丁酯、钛酸四乙酯、钛酸四异丙酯或乙酰钼。The preparation method of EVA material according to claim 1, characterized in that the filler particles are silica and/or calcium carbonate, the particle size of the filler particles is 20-2000 nm, and the mass of the filler particles The fraction is 1%-10%, and the ester silane coupling agent is 2-carbonylmethoxyethyldimethoxymethylsilane, acetoxypropyltrimethoxysilane, 3-(carbonylmethoxy ) one or two of propyldimethylmethoxysilane and 3-(carbonylethoxy)propyldimethylethoxysilane, the EVA raw material is ethyl acetate with a content of 10-30% Thermoplastic unvulcanized cross-linked EVA, the transesterification catalyst is tetrabutyl titanate, tetraethyl titanate, tetraisopropyl titanate or acetyl molybdenum.
  4. 如权利要求1所述的EVA材料的制备方法,其特征在于,在步骤S1中,在20-40℃的条件下利用超声进行对所述填料粒子进行预分散20-40min。The preparation method of EVA material according to claim 1, characterized in that, in step S1, the filler particles are pre-dispersed using ultrasound under the conditions of 20-40°C for 20-40 minutes.
  5. 如权利要求1所述的EVA材料的制备方法,其特征在于,在步骤S1中,进行离心洗涤处理时,将所述混合物以8000~12000 r/min的转速离心处理3-5次,每次离心处理的时间为3-7 min。The preparation method of EVA material according to claim 1, characterized in that, in step S1, when performing centrifugal washing, the mixture is centrifuged 3-5 times at a speed of 8000-12000 r/min, each time The centrifugation time is 3-7 minutes.
  6. 如权利要求1所述的EVA材料的制备方法,其特征在于,在步骤S1中,进行干燥处理时,将所述滤渣在80-120℃的条件下真空干燥8-20 h。The preparation method of EVA material according to claim 1, characterized in that, in step S1, during the drying process, the filter residue is vacuum dried at 80-120°C for 8-20 h.
  7. 如权利要求1所述的EVA材料的制备方法,其特征在于,在步骤S2中,控制所述转矩流变仪反应温度为100~180℃,转速为50~200 rpm。The preparation method of EVA material according to claim 1, characterized in that, in step S2, the reaction temperature of the torque rheometer is controlled to be 100-180°C, and the rotation speed is 50-200 rpm.
  8. 如权利要求1所述的EVA材料的制备方法,其特征在于,在步骤S2中,预分散时间为5-10min,将所述酯交换催化剂分3-5次加入所述转矩流变仪中,然后混合10-30min,再将所述动态交联剂分3-5次加入所述转矩流变仪中,然后共混处理10-30min。The preparation method of EVA material according to claim 1, characterized in that, in step S2, the pre-dispersion time is 5-10 min, and the transesterification catalyst is added into the torque rheometer in 3-5 times. , then mix for 10-30 minutes, then add the dynamic cross-linking agent into the torque rheometer in 3-5 times, and then blend for 10-30 minutes.
  9. 如权利要求1所述的EVA材料的制备方法,其特征在于,在步骤S3中,模压成型时,模压压力为5-20 MPa ,模压温度为120-180℃,模压时间为0.5-2h。The preparation method of EVA material according to claim 1, characterized in that, in step S3, during molding, the molding pressure is 5-20 MPa, the molding temperature is 120-180°C, and the molding time is 0.5-2h.
  10. 一种EVA材料,其特征在于,包括10-30质量份填料粒子、1-10质量份酯类硅烷偶联剂、70-100质量份EVA、 0.1-2.5质量份酯交换催化剂和1-10质量份动态交联剂,采用如权利要求1-9中任一权利要求所述的EVA材料的制备方法制作获得。An EVA material, characterized in that it includes 10-30 parts by mass filler particles, 1-10 parts by mass ester silane coupling agent, 70-100 parts by mass EVA, 0.1-2.5 parts by mass transesterification catalyst and 1-10 parts by mass The dynamic cross-linking agent is prepared by the preparation method of the EVA material as described in any one of claims 1-9.
PCT/CN2023/078579 2022-07-15 2023-02-28 Preparation method for eva material and eva material WO2024011919A1 (en)

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