CN1453306A - High-intercluding transparent polypropylene resin composition, sheet made of the composition and its making process - Google Patents
High-intercluding transparent polypropylene resin composition, sheet made of the composition and its making process Download PDFInfo
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- CN1453306A CN1453306A CN 03131317 CN03131317A CN1453306A CN 1453306 A CN1453306 A CN 1453306A CN 03131317 CN03131317 CN 03131317 CN 03131317 A CN03131317 A CN 03131317A CN 1453306 A CN1453306 A CN 1453306A
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Abstract
The high-intercluding transparent polypropylene resin composite includes polypropylene resin, C5-C9 petroleum resin, organic nucleating agent, high-density polyethylene resin and additive. The composite is mixed, extruded, cooled and formed in a three-roller sheet extruding machine to form the high-intercluding transparent polypropylene sheet. The high-intercluding transparent polypropylene sheet is superior to common polypropylene sheet in transparency, intercluding performance, thermal forming performance and modulus, and is used mainly in packing medicine, food, etc.
Description
Technical field
The invention belongs to the processing and the Application Areas of macromolecular material.Particularly, the present invention relates to high-barrier polypropylene (PP) clear sheet resin combination, by the manufacture method of clear sheet and this clear sheet of its manufacturing.
Prior art
Plastic Packaging Materials is used very extensive from industrial goods to the sphere of life, 27% of plastics total amounts have been accounted for, domestic food and drug packaging at present mainly adopted polyvinyl chloride (PVC), polystyrene (PS), polyester materials such as (PET) with high barrier material, but can produce obnoxious flavour after the PVC recycling, cause environmental pollution, be detrimental to health, some western countries have limited even have banned use of PVC at present, and the price of PS and PE is more expensive.Compare with above-mentioned traditional material, polypropylene has tangible performance and price advantage.On performance, polypropylene density is little, high temperature resistant, microwave adaptability is good, chemical-resistant resistance and oil-proofness is good, to the good barrier property of steam, and be easy to machine-shaping, particularly sanitation performance is good, is easy to recycling, and is environmentally friendly, the pp material source is abundant simultaneously, low price, purposes are very extensive, are one of the fastest macromolecular materials of development in recent years.
But polypropylene is high crystalline macromolecular material, and its large diameter spherulitic crystal structure makes its goods poor transparency, and the hot formability of its sheet material is good inadequately simultaneously.Therefore, solve the transparency of polypropylene material, further improve hot formability, suitably improve key technical problems such as barrier, modulus, can constantly enlarge its purposes, strengthen competitive power at packaging field.The existing hard sheet of polypropylene transparent material substitution PVC of the Germany and the U.S. is still useless at home in the production of food and drug packaging usefulness high-barrier polypropylene transparent sheet material at present, does not also work out concerned countries standard or industry standard.
Many people have done a large amount of trials, in the hope of improving Properties of Polypropylene.For example, to cool off melt polypropylene (clear 62-41457, clear 62-42822, clear 60-236719, clear 62-10816) fast be the method that early is used to prepare polypropylene transparent sheet material and film in water-bath.This method is freezed the polypropylene molecule crystallization by quick cooling, generate imperfect crystal, reducing the crystalling propylene degree enhances the transparency, but the modulus of crystalline p p sheet also can descend thereupon, hot formability does not improve yet, in addition, the crystalline p p sheet melt is directly used water cooling, its sheet surface low in glossiness.
Adding nucleator is a kind of method that improves the acrylic resin transparency.Nucleator is a kind of promotion crystalline small-molecule substance, and it can play the effect of nucleus in resin, increases nucleus number in the crystallizing system, and the quantity of crystallite is increased, and the spherocrystal reduced number improves the polypropylene material transparency.The sorbyl alcohol that adopts Shanxi chemical research institute to produce is nucleator DBS-1, or Millad 3988 nucleators (the Plastics Technology of employing MillikenChemical Co.Ltd., 44, in July, 2002) produce common homo-polypropylene clear sheet, its transparency improves, modulus also has increase, but hot formability does not have improvement.
Atsushi Fujii etc. has introduced crystalline p p sheet cooling steel band calendering process in US-5204037, this method is the best method of the raising crystalline p p sheet transparency seen at present, but owing to produce investment and product cost height, does not see the industry use so far.
Improve main at present the employing in the polypropylene material of crystalline p p sheet thermoforming performance and add polyethylene (PE) material co-blended, the adding of PE material has reduced vicat softening temperature, the heat-drawn wire of polypropylene material; But this method reduces the transparency and the modulus of sheet material, can not be used for the packing of product of transparent requirement.
US-5595827 has reported the method that adopts high degree of isotacticity (degree of isotacticity 98.6%) polypropylene material and petroleum resin blend to produce the polypropylene thermal formed sheet with high water vapor rejection characteristics, this method has been used special polypropylene material, its transparency of products is very bad, and mist degree only is 50%.
In view of above-mentioned prior art situation, the polypropylene transparent sheet material that a kind of transparency, barrier and thermoforming performance excellence still need be developed in this area is used for food and drug packaging.
Summary of the invention
The present inventor has carried out research extensively and profoundly in polypropylene transparent sheet material field, in the hope of developing a kind of food and drug packaging polypropylene transparent sheet material with excellent transparency, barrier and hot formability.Found that by selecting specific polypropylene transparent sheet material resin combination, can use ordinary tablet material forming machine to obtain having the polypropylene transparent sheet material of above-mentioned performance.The present invention is based on this discovery is accomplished.
An object of the present invention is to provide a kind of high-barrier polypropylene transparent sheet material resin combination.
Another object of the present invention provides the high-barrier polypropylene transparent sheet material that a kind of cost is low, performance good, can produce on the plain polypropylene sheet production line.
A further object of the present invention has provided a kind of manufacture method of above-mentioned clear sheet.
One aspect of the present invention provides a kind of high-barrier polypropylene transparent sheet material resin combination, comprises:
1) acrylic resin of 70-95 weight %;
2) C of 2-20 weight %
5-C
9Petroleum resin;
3) organic nucleating agent of 0.1-0.3 weight %;
4) high-density polyethylene resin of 0.1-5 weight %; With
5) additive of 0.01-0.04 weight %.
The present invention provides a kind of high-barrier polypropylene transparent sheet material of being made with resin combination by high-barrier polypropylene transparent sheet material of the present invention on the other hand, and this sheet material is characterised in that steam transmitance＜1g/d.m
2, mist degree＜6%.
Further aspect of the present invention provides a kind of manufacture method of high-barrier polypropylene transparent sheet material, comprise with each component of above-mentioned resin combination mix, heat, extrude, cooling, moulding, can obtain high-barrier polypropylene transparent sheet material.
In resin combination of the present invention, employed acrylic resin is that melting index is 0.1-20g/10min, the homopolymerization of preferred 0.3-10g/10min or the mixture of Co-polypropylene resin or these resins.
In resin combination of the present invention, employed petroleum resin are that global softening temperature is 100-140 ℃ C
5-C
9Olefin polymer or these mixture of polymers.
In resin combination of the present invention, employed organic nucleating agent can be a nucleator commonly used during crystalline p p sheet is produced.The example comprises Sodium Benzoate, sorbyl alcohol dibenzyl ester (DBS), Millad3988 or its mixture.
In resin combination of the present invention, the melting index that employed high-density polyethylene resin has is that 1-100g/10min and density are 0.95-0.97g/cm
3
The additive that can be used for resin combination of the present invention is an additive commonly used in the crystalline p p sheet processing, as static inhibitor, thermal oxidation resistance agent, anti-light aging agent, low-molecular-weight wax lubricant, fluorescent agent etc.
In the manufacture method of high-barrier polypropylene transparent sheet material of the present invention, at first adopt twin screw extruder to extrude used each component of resin combination, screw diameter D=75mm wherein, screw slenderness ratio L/D=36, screw speed=150 commentaries on classics/min; The extruding pelletization temperature is controlled to be 190-240 ℃.Obtain resin combination thus.Then the gained resin combination is sent in the common multi-layer co-extruded three roller sheet material machines and carried out moulding, extrusion temperature is 200-260 ℃, and chill-roll temperature is 15-80 ℃.It is 0.15-0.4mm that resulting sheet can manufacture thickness, and width is 600-1250mm.
Consider the difference of each component proterties of material, for the homogeneity that improves the gained resin combination and make it be easy to carry out sheet material processing, preferably mix in the invention process process, melt extrude granulation with twin screw extruder and make polypropylene resin composite by its compositing formula; Also can polypropylene segment resin and other component be mixed by its compositing formula, melt extrude granulation with twin screw extruder and make the composition masterbatch, all the other acrylic resins and masterbatch are mixed obtain the production that polypropylene resin composite is used for the PP sheet material then.
The present invention is by the mixture and the C of acrylic resin or Co-polypropylene resin or acrylic resin and copolymerization acrylic resin
5-C
9After the material blend such as petroleum resin, organic nucleating agent, high-density polyethylene resin, resulting composition has unique crystallization mechanism.Polypropylene is a kind of high crystalline macromolecular material, and melt crystallization speed is slow, easily forms big spherocrystal, and its diameter is greater than visible wavelength, and incident light is absorbed by crystal, has reduced the material transparency.Nucleator in the polypropylene resin composite of the present invention is a kind of promotion crystalline small-molecule substance.Add nucleator in polypropylene, promote heterogeneous nucleation, increase the crystal growth point, improved crystallization velocity, changed crystallization path, the quantity of crystallite is increased, the spherocrystal reduced number has reduced the mean sizes of spherocrystal; Along with the insertion of PE, the PP spherocrystal is divided into wafer by PE, the crystal refinement simultaneously.Prove by experiment, compare with the general purpose polypropylene resin, the acrylic resin that contains nucleator has higher Tc and crystallization velocity, and polypropylene resin composite of the present invention has lower Tc and higher crystallization velocity, thereby improved the transparency of material, improved every performance.Sheet material mist degree by polypropylene resin composite manufacturing of the present invention has been reduced to below 6%.
Because polypropylene, high density polyethylene(HDPE) and petroleum resin also have good consistency, filled up the lattice imperfection of polypropylene molecule pars amorpha, intermolecular degree of compactness is increased, effectively hindered passing through of small molecules liquid, gas, thereby make the barrier property of clear sheet of the present invention improve greatly, for example steam transmitance＜1g/d.m
2, preferred＜0.8g/d.m
2
The plain polypropylene sheet forming is difficulty relatively, polyethylene and C
5-C
9Petroleum resin can be regulated the melting index of polypropylene resin composite, reduce heat-drawn wire, the vicat softening temperature of polypropylene resin composite.The polypropylene resin composite melting index that will be suitable for sheet production in the present invention is controlled at 1-10g/10min (2.16Kg, 230 ℃), vicat softening temperature≤155 ℃ (polypropylene is 160 ℃), heat-drawn wire≤105 ℃ (polypropylene is 110 ℃), thereby can increase the processing temperature scope, improve thermoforming performance, processing characteristics.In addition, polypropylene resin composite also has higher modulus, for example＞1400Mpa, thus make sheet material have deflection preferably.
The performance of PP sheet material of the present invention is also closely related with sheet production equipment and technology.Find in the test that too high temperature can make polypropylene resin composite decompose when extruding, degradation production influences the sheet material outward appearance, and low excessively temperature is unfavorable for that the fusion plastification of polypropylene resin composite, sheet material produce brilliant point.The control of rolling chill-roll temperature in addition can guarantee the good bond between crystalline p p sheet and the roller, eliminate crystalline p p sheet surface water wave, the stack cooling temperature is the important method that reduces and eliminate the crystalline p p sheet orientation with reasonable cooperation of production rate simultaneously.The present invention adopts common three roller sheet production equipment, control polypropylene resin composite extrusion temperature at 200-260 ℃, three roller stack chill-roll temperature be 15-80 ℃ (top roll 55-80 ℃, central roll 40-60 ℃, lower roll 15-50 ℃), sheet production speed 5-20m/min.
Polypropylene resin composite of the present invention and crystalline p p sheet performance detection method and standard are as follows:
PP melting index: GB 3682-1983 thermoplastics melt flow rate (MFR) test method, 2.16Kg, 230 ℃
PE melting index: GB 3682-1983 thermoplastics melt flow rate (MFR) test method, 2.16Kg, 190 ℃
PP degree of isotacticity: GB 2412-1980 polypropylene isotactic index testing method
Sheet material transmittance and mist degree: GB 2410-1983 transparent plastics transmittance and mist degree test method
The steam transmitance: GB 1037-1988 plastics film and sheet material water vapor permeability can test methods (cup type method)
Thermal distortion: ASTM D648-00
Softening temperature: the mensuration of GB1633-2000 thermoplastics vicat softening temperature (VST)
Tensile property: GB 1040-1992 plastic tensile method for testing performance
Embodiment
Further describe the present invention below in conjunction with embodiment, but the present invention is not limited to these embodiment.
Embodiment 1
With 100 parts of (weight part, as follows) acrylic resins (1002 of Yanshan Petrochemical production, melting index 3g/10min, degree of isotacticity 96.7,165 ℃ of DSC melt temperatures), 10 parts of C
5-C
9Petroleum resin (P125 of Japanese deserted mountain petrochemical industry, 115 ℃ of global softening temperatures), 2 parts of high density polyethylene(HDPE)s (K81 of Liaoyang petrochemical industry, melting index 15g/10min, density 0.95g/cm
3), 0.3 part of sorbyl alcohol is that nucleator (DBS-1 of Shanxi chemical institute, fusing point 215-217 ℃), 0.2 part of stearic acid monoglycerides (fusing point 63-64 ℃) and 0.1 part of additive HALS Tin 944 (Ciba-Geigy) mix and adopt twin screw extruder to melt extrude granulation in plastics mixer to obtain polypropylene resin composite.
The twin screw extruder screw diameter D=75mm of Cai Yonging here, screw slenderness ratio L/D=36, screw speed=150 commentaries on classics/min; The extruding pelletization temperature is controlled to be 190-240 ℃.The melting index of gained polypropylene resin composite is 6g/10min, and vicat softening temperature is 148 ℃, and heat-drawn wire is 100 ℃; The pp material resin of this polypropylene resin composite and use relatively has the Tc of reduction and the crystallization velocity of raising.
Above-mentioned polypropylene resin composite is used to produce sheet material, and sheet production equipment is single screw extrusion machine, the screw diameter D=90mm of this forcing machine, and screw slenderness ratio L/D=33, sheet die width are 1300mm, the die orifice width is 1mm.The processing condition of sheet production are: extruder temperature: 170,180,195,210,230,240,230 ℃; Die head temperature: 220,225,230,225,220 ℃; Stack temperature: 70 ℃ of top rolls, 50 ℃ of central rolls, 20 ℃ of lower rolls; Thermoforming bubble-cap temperature: 130 ℃.
Adopt above-mentioned polypropylene resin composite and sheet production condition production articles of sheet material of the present invention, stable production process, articles of sheet material does not have brilliant point, any surface finish.Other performance index of present embodiment see Table 2.
Reference examples 1-3
According to the PP sheet material production technology of embodiment 1, use the listed composition of table 1, obtain the PP sheet material that is used to contrast, its performance sees Table 2.
Table 1. polypropylene reference examples is formed
| Component | Polypropylene | Nucleator DBS | Petroleum resin (P125) |
| Reference examples 1 | ??100 | ??0.3 | ????- |
| Reference examples 2 | ??100 | ??- | ????10 |
| Reference examples 3 | ??100 | ??- | ????- |
The crystalline p p sheet performance of table 2. embodiment 1 and reference examples 1-3
Embodiment 2
| Performance | Embodiment | Reference examples 1 | Reference examples 2 | Reference examples 3 |
| Sheet thickness, mm | ??0.32 | ?0.32 | ??0.35 | ??0.32 |
| Transmittance, % | ??89.6 | ?82.6 | ??75 | ??70 |
| Mist degree, % | ??3.5 | ?8.6 | ??20.5 | ??25 |
| Draw refreshing intensity, MPa | ??37.9 | ?36.7 | ??32.3 | |
| Tensile modulus, MPa | ??1657 | ?1257 | ??1135 | |
| The steam transit dose | ??0.57 | ?- | ??- | ??2.3 |
| The thermoforming bubble-cap | Shallow bubble | Softening being clamminess |
With (1002 of the Yanshan Petrochemical production of 50 parts of acrylic resins, melting index 3g/10min, degree of isotacticity 96.7,165 ℃ of DSC melt temperatures), 50 parts of acrylic resins (PP1300 that Yanshan Petrochemical is produced, melting index be 1.4g/10min, degree of isotacticity be 97.5 and the DSC melt temperature be 165 ℃), 10 parts of C
5-C
9Petroleum resin (P125 of Japanese deserted mountain petrochemical industry, 115 ℃ of global softening temperatures), 5 parts of high density polyethylene(HDPE)s (K81 of Liaoyang petrochemical industry, melting index 15g/10min, density 0.95g/cm
3), 0.3 part of sorbyl alcohol is that nucleator (DBS-1 of Shanxi chemical institute, fusing point 215-217 ℃), 0.2 part of stearic acid monoglycerides (fusing point 63-64 ℃) and 0.1 part of additive HALS Tin 944 (Ciba-Geigy) mix and adopt twin screw extruder to melt extrude granulation in plastics mixer to obtain polypropylene resin composite.The twin screw extruder screw diameter D=75mm of Cai Yonging here, screw slenderness ratio L/D=36; The extruding pelletization temperature is controlled to be 190-240 ℃, screw speed=150 commentaries on classics/min.The melting index of the polypropylene resin composite that obtains is 4g/10min, and vicat softening temperature is 150 ℃, and heat-drawn wire is 102 ℃.The pp material resin of this polypropylene resin composite and use relatively has the Tc of reduction and the crystallization velocity of raising.
Adopt above-mentioned polypropylene resin composite to produce sheet material, sheet production equipment is single screw extrusion machine, the screw diameter D=90mm of this forcing machine, and screw slenderness ratio L/D=33, sheet die width are 1300mm, the die orifice width is 1mm.The processing condition of sheet production are: extruder temperature: 170,180,195,210,230,240,230 ℃; Die head temperature: 220,225,230,225,220 ℃; Stack temperature: 70 ℃ of top rolls, 50 ℃ of central rolls, 20 ℃ of lower rolls.
Adopt above-mentioned polypropylene resin composite and sheet production condition production articles of sheet material of the present invention, stable production process, articles of sheet material does not have brilliant point, any surface finish.Other performance index of present embodiment see Table 3.
Table 3. sheet properties
| Performance | Embodiment 2 |
| Sheet thickness, mm | ??0.36 |
| Transmittance, % | ??87 |
| Mist degree, % | ??5.1 |
| Tensile strength, MPa | ??36.2 |
| Tensile modulus, MPa | ??1520 |
| The thermoforming bubble-cap | Middle bubble |
Claims (10)
1, a kind of high-barrier polypropylene (PP) clear sheet resin combination comprises the acrylic resin of 70-95 weight %, the C of 2-20 weight %
5-C
9The additive of the high-density polyethylene resin of the organic nucleating agent of petroleum resin, 0.1-0.3 weight %, 0.1-5 weight % and 0.01-0.04 weight %.
2, resin combination as claimed in claim 1 is characterized in that it is 0.1-20g/10min that described acrylic resin is selected from melting index, the homopolymerization of preferred 0.3-10g/10min or the mixture of Co-polypropylene resin and these resins.
3, resin combination as claimed in claim 1 is characterized in that it is 100-140 ℃ C that described petroleum resin are selected from global softening temperature
5-C
9Olefin polymer and these mixture of polymers.
4, resin combination as claimed in claim 1 is characterized in that described organic nucleating agent is selected from Sodium Benzoate, sorbyl alcohol dibenzyl ester (DBS), Millad 3988 and composition thereof.
5, resin combination as claimed in claim 1 is characterized in that it is that 1.0-100g/10min and density are 0.95-0.97g/cm that described high-density polyethylene resin is selected from melting index
3High-density polyethylene resin.
6, resin combination as claimed in claim 1 is characterized in that described additive is selected from static inhibitor, thermal oxidation resistance agent, anti-light aging agent, low-molecular-weight wax lubricant and fluorescent agent.
7, a kind of method for preparing high-barrier polypropylene transparent sheet material comprises the steps:
1) each component of resin combination as claimed in claim 1 is mixed, heats, extrudes and is cooled off, obtain polypropylene resin composite and
2), can obtain high-barrier polypropylene transparent sheet material with the moulding of step 1) resulting composition.
8, method as claimed in claim 7 is characterized in that described resin combination is sent into common multi-layer co-extruded three roller sheet material machines, and extrusion temperature is 200-260 ℃, and chill-roll temperature is 15-80 ℃.
9, method as claimed in claim 7, it is characterized in that the acrylic resin that part is used and other components mix, melt extrude granulation with twin screw extruder and make masterbatch, all the other acrylic resins and masterbatch are mixed obtain polypropylene resin composite then.
10, a kind of high-barrier polypropylene transparent sheet material of being made by each described method among the claim 7-9 is characterized in that the steam transit dose＜0.8g/d.m of sheet material
2, mist degree＜6%.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 03131317 CN1207337C (en) | 2003-05-13 | 2003-05-13 | High-intercluding transparent polypropylene resin composition, sheet made of the composition and its making process |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 03131317 CN1207337C (en) | 2003-05-13 | 2003-05-13 | High-intercluding transparent polypropylene resin composition, sheet made of the composition and its making process |
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| Publication Number | Publication Date |
|---|---|
| CN1453306A true CN1453306A (en) | 2003-11-05 |
| CN1207337C CN1207337C (en) | 2005-06-22 |
Family
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|---|---|---|---|
| CN 03131317 Expired - Fee Related CN1207337C (en) | 2003-05-13 | 2003-05-13 | High-intercluding transparent polypropylene resin composition, sheet made of the composition and its making process |
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Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN102286169A (en) * | 2010-06-18 | 2011-12-21 | 中国石油化工股份有限公司 | Polypropylene composition and preparation method thereof |
| CN102304248A (en) * | 2011-08-31 | 2012-01-04 | 湖北工业大学 | Expandable high-melt-strength polypropylene resin and preparation method thereof |
| CN103066141A (en) * | 2012-12-28 | 2013-04-24 | 苏州度辰新材料有限公司 | Modified polypropylene resin composition and solar energy rear panel made of the same |
| CN103442889A (en) * | 2010-12-28 | 2013-12-11 | 出光统一科技株式会社 | Transparent multilayer sheet and molded product thereof |
| CN112538230A (en) * | 2019-09-20 | 2021-03-23 | 茂名骐锋新材料有限公司 | Additive composition and application thereof in high-transparency high-strength polypropylene plastic |
| CN114456499A (en) * | 2021-12-30 | 2022-05-10 | 安徽志诚机电零部件有限公司 | Polypropylene material for anti-seepage expansion kettle and preparation method thereof |
| CN114891299A (en) * | 2022-05-26 | 2022-08-12 | 浙江新天力容器科技有限公司 | Weight-reduced high-transparency plastic and preparation method and application thereof |
| CN115011029A (en) * | 2022-04-16 | 2022-09-06 | 浙江新天力容器科技有限公司 | Barrier transparent polypropylene material for plastic uptake and preparation method thereof |
| CN115368670A (en) * | 2022-07-01 | 2022-11-22 | 中国石油化工股份有限公司 | High-barrier polypropylene composite material and preparation method thereof |
| CN115926321A (en) * | 2022-12-28 | 2023-04-07 | 金发科技股份有限公司 | High-fuel-vapor-barrier polypropylene composition and preparation method and application thereof |
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2003
- 2003-05-13 CN CN 03131317 patent/CN1207337C/en not_active Expired - Fee Related
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102286169B (en) * | 2010-06-18 | 2015-04-15 | 中国石油化工股份有限公司 | Polypropylene composition and preparation method thereof |
| CN102286169A (en) * | 2010-06-18 | 2011-12-21 | 中国石油化工股份有限公司 | Polypropylene composition and preparation method thereof |
| CN103442889B (en) * | 2010-12-28 | 2017-02-08 | 出光统一科技株式会社 | Transparent multilayer sheet and molded product thereof |
| CN103442889A (en) * | 2010-12-28 | 2013-12-11 | 出光统一科技株式会社 | Transparent multilayer sheet and molded product thereof |
| CN102304248A (en) * | 2011-08-31 | 2012-01-04 | 湖北工业大学 | Expandable high-melt-strength polypropylene resin and preparation method thereof |
| CN103066141A (en) * | 2012-12-28 | 2013-04-24 | 苏州度辰新材料有限公司 | Modified polypropylene resin composition and solar energy rear panel made of the same |
| CN103066141B (en) * | 2012-12-28 | 2015-07-15 | 苏州度辰新材料有限公司 | Modified polypropylene resin composition and solar energy rear panel made of the same |
| CN112538230A (en) * | 2019-09-20 | 2021-03-23 | 茂名骐锋新材料有限公司 | Additive composition and application thereof in high-transparency high-strength polypropylene plastic |
| CN114456499A (en) * | 2021-12-30 | 2022-05-10 | 安徽志诚机电零部件有限公司 | Polypropylene material for anti-seepage expansion kettle and preparation method thereof |
| CN115011029A (en) * | 2022-04-16 | 2022-09-06 | 浙江新天力容器科技有限公司 | Barrier transparent polypropylene material for plastic uptake and preparation method thereof |
| CN114891299A (en) * | 2022-05-26 | 2022-08-12 | 浙江新天力容器科技有限公司 | Weight-reduced high-transparency plastic and preparation method and application thereof |
| CN115368670A (en) * | 2022-07-01 | 2022-11-22 | 中国石油化工股份有限公司 | High-barrier polypropylene composite material and preparation method thereof |
| CN115926321A (en) * | 2022-12-28 | 2023-04-07 | 金发科技股份有限公司 | High-fuel-vapor-barrier polypropylene composition and preparation method and application thereof |
| CN115926321B (en) * | 2022-12-28 | 2023-09-26 | 金发科技股份有限公司 | Polypropylene composition with high fuel vapor barrier and preparation method and application thereof |
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| Publication number | Publication date |
|---|---|
| CN1207337C (en) | 2005-06-22 |
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