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CN119331358A - A white food-grade EPDM rubber hose and preparation method thereof - Google Patents

A white food-grade EPDM rubber hose and preparation method thereof Download PDF

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CN119331358A
CN119331358A CN202411896133.1A CN202411896133A CN119331358A CN 119331358 A CN119331358 A CN 119331358A CN 202411896133 A CN202411896133 A CN 202411896133A CN 119331358 A CN119331358 A CN 119331358A
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parts
rubber
epdm rubber
oxide powder
white
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CN119331358B (en
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潘晓天
郁荣荣
李乐勤
范强
尤飞卫
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Shanghai Blue Future Industrial Technology Co ltd
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Shanghai Blue Future Industrial Technology Co ltd
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    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L23/00Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
    • C08L23/02Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers not modified by chemical after-treatment
    • C08L23/16Ethene-propene or ethene-propene-diene copolymers
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2203/00Applications
    • C08L2203/18Applications used for pipes

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  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Compositions Of Macromolecular Compounds (AREA)
  • Processes Of Treating Macromolecular Substances (AREA)

Abstract

The application relates to the technical field of ethylene propylene diene monomer rubber, in particular to a white food-grade ethylene propylene diene monomer rubber tube and a preparation method thereof. The EPDM rubber comprises EPDM rubber, white carbon black, kaolin, paraffin oil, zinc oxide powder, calcium oxide powder, 1-2 parts of stearin, a silane coupling agent, titanium pigment, sulfur and a comprehensive accelerator. The preparation method comprises the steps of mixing EDPM rubber, zinc oxide and stearic acid, heating and mixing, adding white carbon black, kaolin and the like for continuous mixing, standing, adding sulfur and the like for mixing to obtain a pre-mixed rubber material, opening the pre-mixed rubber material, turning over the rubber material, discharging the rubber sheet, cutting a hanging rod, cooling at room temperature for standby, and extruding and molding the rubber sheet at normal temperature to obtain the product. According to the application, kaolin is additionally introduced into the raw materials, so that the moisture absorption can be reduced, and the composite accelerator compounded by Altermix BGL-70, HANSUN EG M-80GE and 5-hydroxy-1, 4-naphthoquinone is adopted, so that the vulcanization efficiency can be greatly improved, the time is shortened, the vulcanization temperature range is widened, and the process is more stable and controllable.

Description

White food-grade ethylene propylene diene monomer rubber tube and preparation method thereof
Technical Field
The application relates to the technical field of ethylene propylene diene monomer rubber, in particular to a white food-grade ethylene propylene diene monomer rubber tube and a preparation method thereof.
Background
Ethylene Propylene Diene Monomer (EPDM) as a general purpose rubber material with excellent performance and superior cost performance shows a wide application potential in numerous fields, especially in the food and medical industries where extremely high requirements on material safety and durability are required. In these sensitive and critical industries, the quality of EPDM articles is directly related to the safety and reliability of the product. However, microwave vulcanization, a vital step in the preparation of EPDM extruded tubes, presents a significant challenge for food grade EPDM materials.
Specifically, food grade EPDM white compounds contain various fillers, such as white carbon black and calcium carbonate, which have extremely strong hygroscopicity. Once the compound absorbs too much moisture, it can have a significant adverse effect on the subsequent vulcanization. The existence of moisture not only can cause bubbles in the vulcanization process, thereby influencing the appearance quality and the internal structure stability of the product, but also can reduce the vulcanization efficiency, so that the product is difficult to meet the established performance standard.
In addition, food grade EPDM white compounds are also very demanding in terms of the choice of vulcanization accelerators. Since vulcanization accelerators are directly related to vulcanization speed and the quality of the vulcanization product, it is necessary to select vulcanization accelerators which meet the vulcanization speed requirements without jeopardizing the safety of the product. However, in practical applications, such vulcanization accelerators tend to have limited options and it is difficult to fully meet the rapid vulcanization conditions required for microwave vulcanization.
Disclosure of Invention
In order to solve the problems, the application provides a white food-grade ethylene propylene diene monomer and a preparation method thereof, which aim to overcome the difficult problem of microwave vulcanization caused by the hygroscopicity of a filler and the selection limitation of a vulcanization accelerator in the preparation process and realize the efficient and rapid production of a food-grade extrusion pipe.
In a first aspect, the application provides a white food-grade ethylene propylene diene monomer rubber tube, which adopts the following technical scheme:
the raw materials for preparing the white food-grade ethylene propylene diene monomer rubber pipe comprise the following components in parts by weight:
100 parts of EPDM rubber
20-40 Parts of white carbon black
100-150 Parts of kaolin
Paraffin oil 10-30 parts
3-5 Parts of zinc oxide powder
10-15 Parts of calcium oxide powder
Stearic acid 1-2 parts
1-3 Parts of silane coupling agent
5-10 Parts of titanium dioxide
0.5 To 1.5 portions of sulfur
3-5 Parts of comprehensive accelerator.
By adopting the technical scheme, the method optimizes the selection and the proportion of raw materials, effectively solves the difficult problem of microwave vulcanization caused by the hygroscopicity of the filler and the selection limit of the vulcanization accelerator in the preparation process, realizes the efficient and rapid production of the food-grade extrusion pipe, and ensures the safety and the reliability of the product.
Optionally, the raw materials for preparing the white food-grade ethylene propylene diene monomer rubber tube comprise the following components in parts by weight:
100 parts of EPDM rubber
30-40 Parts of white carbon black
130-150 Parts of kaolin
20-30 Parts of paraffin oil
3-5 Parts of zinc oxide powder
10-15 Parts of calcium oxide powder
Stearic acid 1-2 parts
1-3 Parts of silane coupling agent
5-8 Parts of titanium dioxide
0.5 To 1.5 portions of sulfur
3-5 Parts of comprehensive accelerator.
Further, optionally, the raw materials for preparing the white food-grade ethylene propylene diene monomer rubber tube are prepared from the following components in parts by weight:
100 parts of EPDM rubber
30 Parts of white carbon black
130 Parts of kaolin
20 Parts of paraffin oil
5 Parts of zinc oxide powder
10 Parts of calcium oxide powder
Stearic acid 1 part
3 Parts of silane coupling agent
Titanium dioxide 8 parts
0.5 Part of sulfur
5 Parts of comprehensive accelerator.
By adopting the technical scheme, the optimized preparation of the white food-grade ethylene propylene diene monomer rubber tube can be realized by precisely controlling the weight parts of the components, the performance, the safety and the production efficiency of the product are improved, and the requirements of the food and medical industry on high-quality rubber products are met.
Further optionally, the comprehensive promoter is a mixture prepared by compounding Altermix BGL-70, HANSUN EG, 6M-80GE and 5-hydroxy-1, 4-naphthoquinone according to the mass percent of 43% to 56% to 1%.
By adopting the technical scheme, the mixture prepared by compounding Altermix BGL-70, HANSUN EG6M-80GE and 5-hydroxy-1, 4-naphthoquinone according to a specific mass percentage is used as a comprehensive accelerator, so that the vulcanization process is optimized, the performance and the production efficiency of the product are improved, the safety and the reliability of the product are ensured, the compound composition has unique advantages and characteristics, and an efficient, environment-friendly and reliable solution is provided for the preparation of the white food-grade ethylene propylene diene monomer rubber tube;
the three components generate remarkable synergistic effect after being compounded, altermix BGL-70 and HANSUN EG M-80GE are used as main vulcanization accelerators, and respectively have different vulcanization active points and action mechanisms, and the compounding of the three components can widen the vulcanization temperature range, improve the vulcanization speed and reduce side effects in the vulcanization process.
The 5-hydroxy-1, 4-naphthoquinone has the key regulation function although the proportion is smaller, and can finely adjust the process of the vulcanization reaction, so that the vulcanization process is more stable, the phenomenon of oversulfiding or undersulfidation is avoided, and the cross-linking structure in the vulcanized product is more compact due to more sufficient and uniform vulcanization reaction, thereby reducing the generation of internal defects and bubbles, and further improving the overall quality of the product.
The compound composition can obviously improve the vulcanization efficiency, shorten the vulcanization time, quickly reach the required vulcanization temperature under the microwave vulcanization condition, and maintain the stable vulcanization rate, thereby accelerating the production flow and improving the production efficiency.
Further optionally, the silane coupling agent is selected from one or more of bis (triethoxysilylpropyl) disulfide, bis- (γ -triethoxysilylpropyl) tetrasulfide wax.
In a specific embodiment, the bis (triethoxysilylpropyl) disulfide can be one of SG-Si996, SG-Si 998, SG-Si 1589, the bis- (gamma-triethoxysilylpropyl) tetrasulfide can be KH-845-4 or SG-Si 1289, and the bis- (gamma-triethoxysilylpropyl) tetrasulfide wax can be Rsi-E.
Further alternatively, the EPDM rubber has an ethylene content of 70.0 to 70.5wt% and a norbornene content of 0.5 to 5.0wt%.
In a second aspect, the preparation method of the white food-grade ethylene propylene diene monomer rubber tube provided by the application adopts the following technical scheme:
a preparation method of a white food-grade ethylene propylene diene monomer rubber tube comprises the following preparation steps:
S1, banburying, namely adding EDPM rubber, zinc oxide powder and stearic acid, heating and mixing for 1-2min at a constant speed of 10-20 ℃ per min, adding white carbon black, kaolin, paraffin oil, silane coupling agent and titanium dioxide, continuously mixing for 5-8min until the temperature reaches 110-120 ℃, discharging rubber to obtain a crude rubber material, standing the crude rubber material at room temperature for 24h, mixing the rubber material with sulfur, a comprehensive accelerator and calcium oxide powder, mixing for 2-3min until the temperature reaches 110-120 ℃, and discharging rubber to obtain a pre-refined rubber material;
s2, open milling, namely open milling the pre-mixed rubber material at the speed of 30-40rpm/min, and turning rubber for 3-7min and then discharging tablets;
s3, preforming, namely cutting the film obtained after the film is discharged from the S2 into strips, hanging the strips, and naturally cooling the strips to below 25 ℃ at room temperature for later use;
And S4, extrusion molding, namely extruding and molding the normal-temperature adhesive tape obtained after cooling in the step S3 to obtain a product.
Further alternatively, the specific process of extrusion molding is extrusion molding by using a cold feed extruder, wherein the screw temperature is 50-60 ℃, the plasticizing temperature is 65-75 ℃, the head temperature is 75-85 ℃, and the extrusion speed is 15-25m/min.
By adopting the technical scheme, in the banburying step, the heating rate, mixing time and temperature are strictly controlled, so that the raw materials are fully mixed and uniformly dispersed, the problem of local overheating or insufficient mixing is avoided, meanwhile, the standing time of the crude sizing material is carefully set to ensure the full curing and stability of the crude sizing material, and in the open milling step, the open milling rate and the sizing material turning time are controlled, the fluidity and the plasticity of the sizing material are further optimized, and a good foundation is laid for the subsequent forming step;
In the extrusion molding step, a cold feed extruder is used, key parameters such as screw temperature, plasticizing temperature, machine head temperature, extrusion speed and the like are strictly controlled, smooth extrusion and molding of the rubber material are ensured, the production efficiency and the product quality are improved, the extrusion temperature is precisely controlled, the problem of insufficient degradation or crosslinking of the rubber material due to overhigh temperature in the extrusion process is avoided, and meanwhile, the dimensional stability and the surface quality of the rubber tube are ensured by reasonable extrusion speed.
The whole preparation process from banburying, open milling, preforming to extrusion molding is carefully designed and optimized, so that the smoothness and high efficiency of the production flow are ensured, the production efficiency is improved, and the production cost and the energy consumption are reduced.
In summary, the application has the following beneficial technical effects:
1. According to the application, kaolin is introduced into the raw materials for preparing the white food-grade ethylene propylene diene monomer rubber tube, and compared with the traditional white carbon black and calcium carbonate, the kaolin has lower hygroscopicity, so that the moisture absorbed by the rubber material in the preparation and storage processes is reduced, bubbles are avoided in the vulcanization process, and the appearance quality and the internal structural stability of the product are ensured;
2. The comprehensive accelerator in the raw materials for preparing the white food-grade ethylene propylene diene monomer rubber tube is prepared by compounding Altermix BGL-70, HANSUN EG, 6M-80GE and 5-hydroxy-1, 4-naphthoquinone according to a specific proportion, can obviously improve the vulcanization efficiency, shortens the vulcanization time, and widens the vulcanization temperature range after compounding, so that the vulcanization process is more stable and controllable.
Detailed Description
The present application will be described in further detail with reference to examples.
Performance test
The rubber tubes prepared in examples and comparative examples were tested for physical properties according to standard GB/T3512-2014, ISO 188:2011, and the test items were hardness (Shore A), tensile strength, elongation at break (%);
The rubber tubes prepared in examples and comparative examples were subjected to distilled water tests according to standard FDA 21 CFR 177.2600, and the residual amounts of 7 hours before distillation and 2 hours after distillation (residual amounts refer to the contents of distilled water and other unnecessary impurities) were measured, respectively.
Examples 1 to 4
A white food grade ethylene propylene diene monomer rubber tube comprises the following components and the amounts (kg) of the components are shown in the table.
TABLE 1 raw material conditions for preparing white food grade ethylene propylene diene monomer rubber tubes in examples 1-4
The white carbon black is AEROSIL R202 hydrophobic fumed silica, the kaolin is basf Metamax high-activity metakaolin, the silane coupling agent is SG-Si 1589 and Rsi-E, the proportion is 40-60%, the comprehensive accelerator is a mixture prepared by compounding Altermix BGL-70%, HANSUN EG M-80GE and 5-hydroxy-1, 4-naphthoquinone according to the mass percentage of 43-56-1%, the ethylene content of the EPDM rubber is 70.0-70.5wt% and the norbornene content of 0.5-5.0wt%;
the white food-grade ethylene propylene diene monomer rubber tube is prepared by the following preparation steps:
S1, banburying, namely adding a predetermined amount of EDPM rubber, zinc oxide powder and stearic acid, heating and mixing for 1min at a constant rate of 15 ℃ per min, adding white carbon black, kaolin, paraffin oil, a silane coupling agent and titanium dioxide, continuously mixing for 5min until the temperature reaches 115 ℃, discharging the rubber to obtain a crude rubber material, standing the crude rubber material at room temperature for 24h, mixing the rubber material with sulfur, a comprehensive accelerator and calcium oxide powder, mixing for 3min until the temperature reaches 120 ℃, and discharging the rubber to obtain a pre-refined rubber material;
S2, open milling, namely open milling the pre-mixed rubber material at the speed of 35rpm/min, and turning rubber for 5min and then discharging tablets;
S3, preforming, namely cutting the film obtained after the film is discharged from the S2 into strips, hanging the strips, and naturally cooling the strips to below 25 ℃ at room temperature for later use;
And S4, extrusion molding, namely using a cold feed extruder to extrude the normal-temperature adhesive tape obtained after cooling in the step S3, wherein the temperature of a screw is 55 ℃, the plasticizing temperature is 65 ℃, the extrusion temperature is 70 ℃, the temperature of a machine head is 80 ℃, the extrusion speed is 20m/min, so as to obtain a crude rubber pipe product, and then performing microwave vulcanization on the crude rubber pipe product through multiple sections of hot air, so as to obtain the white food-grade ethylene propylene diene monomer rubber pipe.
Examples 5 to 8
The only difference from example 2 is the white food grade ethylene propylene diene monomer hose, the amounts of the components being different, the components and their amounts (kg) being shown in the following table.
TABLE 2 raw materials for the preparation of white food grade ethylene propylene diene monomer rubber tubes of example 1 and examples 5-8
Each performance test was performed on the white food-grade ethylene propylene diene monomer rubber tubes prepared in examples 1 to 8 described above with reference to the aforementioned performance test, and the test results are shown in the following table.
TABLE 3 detection results of the performance of white food-grade ethylene propylene diene monomer rubber tubes of examples 1-8
As can be seen from the test data of the table, the rubber hoses prepared in the examples 1-8 have good physical properties and can meet the daily use requirements, but in the FDA distilled water test, the examples have different performances, wherein the residual quantity of 7 hours before distillation is within 1.6-22.4mg/in 2, only the example 6 fails the test requirement, the residual quantity of 2 hours after distillation is within 0.33-5.4mg/in 2, and only the example 2 passes the test requirement;
It follows that embodiment 2 may be the preferred embodiment among the above-described embodiments.
Examples 9 to 11
The white food grade ethylene propylene diene monomer rubber tube is different from the embodiment 2 only in that,
The white carbon black used in the preparation is different in use condition, and the specific conditions are shown in the table below.
TABLE 4 use cases of raw material white carbon black used for preparing white food grade ethylene propylene diene monomer rubber tubes of examples 9-11
Example 12
The white food grade ethylene propylene diene monomer rubber tube is different from the embodiment 2 only in that,
The kaolin used for preparation is Acti-Min RG.
Examples 13 to 16
The only difference from example 2 is the use of the synthetic accelerator used in the preparation.
TABLE 5 comprehensive promoter use cases in raw materials for preparing white food grade ethylene propylene diene monomer rubber tubes of examples 13-16
Comparative examples 1 to 3
The only difference from example 2 is the white food grade ethylene propylene diene monomer hose, which is prepared from different raw materials, in particular as shown in the following table.
TABLE 6 raw material conditions for preparing white food grade ethylene propylene diene monomer rubber tubes in comparative examples 1-3
The white food-grade ethylene propylene diene rubber hoses prepared in examples 9 to 16 and comparative examples 1 to 3 were subjected to various performance tests with reference to the performance test tests described above, and the test results are shown in the following table.
TABLE 7 results of the performance test of white food-grade ethylene propylene diene monomer rubber tubes of examples 1-8
As can be seen from the above table, the white food grade ethylene propylene diene monomer rubber tube prepared in examples 9-11 has a residual amount of 4.2-30.4mg/in 2 before distillation and a residual amount of 0.54-7.7mg/in 2 after distillation in FDA distilled water test;
In the index which cannot pass the FDA distilled water test in the embodiment 9, as AEROSIL20 hydrophilic fumed silica is adopted as the white carbon black in the embodiment 9, the surface of the white carbon black contains hydrophilic groups such as hydroxyl groups and the like, and the white carbon black is more likely to interact with water molecules;
In example 11, a mixture of two hydrophobic white carbon blacks was used in place of AEROSIL R202 in equal amounts, and there was still a gap in FDA distilled water testing compared to the test results of example 2, although the two hydrophobic white carbon blacks used alone performed well, their mixture may not have the same performance advantage, which may be a compromise or imbalance in performance caused by the interaction of the different types of hydrophobic white carbon blacks in the mixture.
In example 10, WACKER hydrophobic white carbon black HDK H20 was used to replace AEROSIL R202 hydrophobic fumed silica in equal amount, but the test result was still inferior to the white food grade ethylene propylene diene monomer rubber tube prepared in example 2.
In example 12, the 7 hour residue before distillation was 22.7mg/in 2 and the 2 hour residue after distillation was 5.6mg/in 2, an index that could not be calibrated by FDA distilled water test, which is probably that the high activity metakaolin of Pasteur Metamax had unique functional properties that make it perform well in rubber hoses, whereas the Acti-Min RG kaolin, while also being a good quality kaolin, may have properties that differ from Metamax, resulting in failure to achieve equivalent performance after replacement.
In examples 13-16, the residual amount of 7 hours before distillation is 5.4-9.8mg/in 2, the residual amount of 2 hours after distillation is 0.78-1.43mg/in 2, and examples 15 and 16 pass the index calibrated by the FDA distilled water test, when the comprehensive promoter is a mixture prepared by compounding Altermix BGL-70 and HANSUN EG M-80GE according to 50% by mass percent or a mixture prepared by compounding Actmix-75 EG3M-75GEF140, altermix BGL-70 and HANSUN EG M-80GE according to 20% by mass percent and 40% by mass percent, as shown by the performance detection results of examples 13 and 14, the index calibrated by the FDA distilled water test is not passed;
however, when 5-hydroxy-1, 4-naphthoquinone was included in the integrated accelerator, as shown in examples 13 and 14, there was a significant effect on the vulcanization efficiency and whether it could pass the FDA distilled water test, and the properties of the white food grade ethylene propylene diene monomer rubber tube prepared only when the integrated accelerator was a mixture of Altermix BGL-70, HANSUN EG M-80GE and 5-hydroxy-1, 4-naphthoquinone compounded at a mass percentage of 43% to 56% to 1% were optimal.
In addition, in comparative examples 1 to 3, an attempt was made to prepare white food-grade ethylene propylene diene monomer tubes using multiple rubber components instead of single EPDM rubber, and from the test results, although they exhibited good physical properties, they failed to reach the index calibrated by the FDA distilled water test, and there was a large gap from the calibration index.
Therefore, the raw material components are specially selected, so that the rubber material can reach the vulcanization temperature more quickly in the microwave vulcanization process, the vulcanization efficiency is improved, meanwhile, the vulcanization process is more stable and controllable due to the reduction of the adverse effect of moisture on the vulcanization process, the production efficiency and quality of the product are further improved, and all the components are mutually cooperated and matched, so that the prepared white food-grade ethylene propylene diene monomer rubber tube has excellent physical properties and chemical stability.
The above description is provided for the purpose of enabling those skilled in the art to make modifications and obvious technical teaching of the present embodiment without any creative contribution, as required, after reading the present specification, and is protected by patent law within the scope of the claims of the present application.

Claims (7)

1.一种白色食品级三元乙丙橡胶胶管,其特征在于,制备所用原料,按照重量份数计,包括以下:1. A white food-grade EPDM rubber hose, characterized in that the raw materials used for preparation, in parts by weight, include the following: EPDM橡胶 100份EPDM rubber 100 parts 白炭黑 20-40份White carbon black 20-40 parts 高岭土 100-150份Kaolin 100-150 parts 石蜡油 10-30份Paraffin oil 10-30 parts 氧化锌粉末 3-5份Zinc oxide powder 3-5 parts 氧化钙粉末10-15份Calcium oxide powder 10-15 parts 硬脂酸 1-2份Stearic acid 1-2 parts 硅烷偶联剂1-3份Silane coupling agent 1-3 parts 钛白粉5-10份Titanium dioxide 5-10 parts 硫磺 0.5-1.5份Sulfur 0.5-1.5 parts 综合促进剂 3-5份;Comprehensive accelerator 3-5 parts; 所述综合促进剂是由Altermix BGL-70、HANSUN EG6M-80GE以及5-羟基-1,4-萘醌按照质量百分比43%:56%:1%复配而得的混合物。The comprehensive accelerator is a mixture of Altermix BGL-70, HANSUN EG6M-80GE and 5-hydroxy-1,4-naphthoquinone in a mass percentage of 43%:56%:1%. 2.根据权利要求1所述的白色食品级三元乙丙橡胶胶管,其特征在于,制备所用原料,按照重量份数计,包括以下:2. The white food-grade EPDM rubber hose according to claim 1, characterized in that the raw materials used in its preparation, in parts by weight, include the following: EPDM橡胶 100份EPDM rubber 100 parts 白炭黑 30-40份White carbon black 30-40 parts 高岭土 130-150份Kaolin 130-150 parts 石蜡油 20-30份Paraffin oil 20-30 parts 氧化锌粉末 3-5份Zinc oxide powder 3-5 parts 氧化钙粉末10-15份Calcium oxide powder 10-15 parts 硬脂酸 1-2份Stearic acid 1-2 parts 硅烷偶联剂 1-3份Silane coupling agent 1-3 parts 钛白粉 5-8份Titanium dioxide 5-8 parts 硫磺 0.5-1.5份Sulfur 0.5-1.5 parts 综合促进剂 3-5份。Comprehensive accelerator 3-5 parts. 3.根据权利要求2所述的白色食品级三元乙丙橡胶胶管,其特征在于,制备所用原料,按照重量份数计,由以下组分制得:3. The white food-grade EPDM rubber hose according to claim 2 is characterized in that the raw materials used for preparation are prepared from the following components in parts by weight: EPDM橡胶 100份EPDM rubber 100 parts 白炭黑 30份White carbon black 30 parts 高岭土 130份Kaolin 130 parts 石蜡油 20份Paraffin oil 20 parts 氧化锌粉末 5份Zinc oxide powder 5 parts 氧化钙粉末 10份Calcium oxide powder 10 parts 硬脂酸 1份1 part stearic acid 硅烷偶联剂 3份Silane coupling agent 3 parts 钛白粉 8份Titanium dioxide 8 parts 硫磺 0.5份Sulfur 0.5 parts 综合促进剂 5份。Comprehensive accelerator 5 parts. 4.根据权利要求1所述的白色食品级三元乙丙橡胶胶管,其特征在于,所述硅烷偶联剂选自双(三乙氧基硅基丙基)二硫化物、双-(γ-三乙氧基硅基丙基)四硫化物、双-(γ-三乙氧基硅基丙基)四硫化物蜡状物中的一种或多种。4. The white food-grade EPDM rubber hose according to claim 1, characterized in that the silane coupling agent is selected from one or more of bis(triethoxysilylpropyl) disulfide, bis-(γ-triethoxysilylpropyl) tetrasulfide, and bis-(γ-triethoxysilylpropyl) tetrasulfide wax. 5.根据权利要求1所述的白色食品级三元乙丙橡胶胶管,其特征在于,所述EPDM橡胶的乙烯含量为70.0-70.5wt%,降冰片烯含量为0.5-5.0wt%。5. The white food-grade EPDM rubber hose according to claim 1, characterized in that the EPDM rubber has an ethylene content of 70.0-70.5wt% and a norbornene content of 0.5-5.0wt%. 6.权利要求1-5中任一所述的白色食品级三元乙丙橡胶胶管的制备方法,其特征在于,包括以下制备步骤:6. The method for preparing the white food-grade EPDM rubber hose according to any one of claims 1 to 5, characterized in that it comprises the following preparation steps: S1、密炼:投入EDPM橡胶、氧化锌粉末、硬脂酸,以10-20℃/min的恒定速率升温混炼1-2min后,再加入白炭黑、高岭土、石蜡油、硅烷偶联剂以及钛白粉,继续混炼5-8min,直至温度达到110-120℃,然后排胶得到粗胶料,粗胶料室温静置24h后,再将胶料与硫磺、综合促进剂、氧化钙粉末混合进行混炼2-3min,直至温度达到110-120℃后排胶,得到预炼胶料;S1, banburying: adding EDPM rubber, zinc oxide powder, and stearic acid, heating and mixing at a constant rate of 10-20°C/min for 1-2min, then adding white carbon black, kaolin, paraffin oil, silane coupling agent, and titanium dioxide, and continuing to mix for 5-8min until the temperature reaches 110-120°C, then removing the glue to obtain a coarse rubber material, after the coarse rubber material is left to stand at room temperature for 24h, the rubber material is mixed with sulfur, a comprehensive accelerator, and calcium oxide powder for mixing for 2-3min, until the temperature reaches 110-120°C, and then removing the glue to obtain a pre-refined rubber material; S2、开炼:以30-40rpm/min速率对预炼胶料进行开炼,翻胶3-7min后出片;S2, refining: refining the pre-refined rubber material at a rate of 30-40 rpm/min, and discharging the sheet after 3-7 minutes of refining; S3、预成型:将S2出片后得到的胶片进行切条挂杆,室温放置自然冷却至25℃以下,待用;S3, preforming: the film obtained after S2 is cut into strips and hung on a rod, and is left to cool naturally to below 25° C. at room temperature for standby use; S4、挤出成型:将S3中冷却后得到的常温胶条进行挤出成型,即得产品。S4, extrusion molding: the room temperature rubber strip obtained after cooling in S3 is extruded to obtain a product. 7.根据权利要求6所述的白色食品级三元乙丙橡胶胶管的制备方法,其特征在于,挤出成型的具体工艺为:使用冷喂料挤出机进行挤出成型,螺杆温度为50-60℃,塑化温度为65-75℃,机头温度为75-85℃,挤出速度为15-25m/min。7. The preparation method of the white food-grade EPDM rubber hose according to claim 6 is characterized in that the specific process of extrusion molding is: using a cold feed extruder for extrusion molding, the screw temperature is 50-60°C, the plasticizing temperature is 65-75°C, the head temperature is 75-85°C, and the extrusion speed is 15-25m/min.
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