CN109306120A - 一种共混法高阻隔性聚丙烯包装膜的生产方法 - Google Patents
一种共混法高阻隔性聚丙烯包装膜的生产方法 Download PDFInfo
- Publication number
- CN109306120A CN109306120A CN201811113355.6A CN201811113355A CN109306120A CN 109306120 A CN109306120 A CN 109306120A CN 201811113355 A CN201811113355 A CN 201811113355A CN 109306120 A CN109306120 A CN 109306120A
- Authority
- CN
- China
- Prior art keywords
- polypropylene
- isotactic polypropylene
- polyethylene glycol
- blending
- isotactic
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- 239000004743 Polypropylene Substances 0.000 title claims abstract description 58
- -1 polypropylene Polymers 0.000 title claims abstract description 58
- 229920001155 polypropylene Polymers 0.000 title claims abstract description 55
- 238000000034 method Methods 0.000 title claims abstract description 21
- 229920006280 packaging film Polymers 0.000 title claims abstract description 15
- 239000012785 packaging film Substances 0.000 title claims abstract description 15
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 14
- 239000002202 Polyethylene glycol Substances 0.000 claims abstract description 35
- 229920001223 polyethylene glycol Polymers 0.000 claims abstract description 35
- 238000002156 mixing Methods 0.000 claims abstract description 24
- 230000004888 barrier function Effects 0.000 claims abstract description 21
- 239000004372 Polyvinyl alcohol Substances 0.000 claims abstract description 13
- 229920002451 polyvinyl alcohol Polymers 0.000 claims abstract description 13
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 claims description 48
- 239000003054 catalyst Substances 0.000 claims description 17
- 125000002887 hydroxy group Chemical group [H]O* 0.000 claims description 15
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 12
- IQPQWNKOIGAROB-UHFFFAOYSA-N isocyanate group Chemical group [N-]=C=O IQPQWNKOIGAROB-UHFFFAOYSA-N 0.000 claims description 12
- 239000005058 Isophorone diisocyanate Substances 0.000 claims description 9
- NIMLQBUJDJZYEJ-UHFFFAOYSA-N isophorone diisocyanate Chemical compound CC1(C)CC(N=C=O)CC(C)(CN=C=O)C1 NIMLQBUJDJZYEJ-UHFFFAOYSA-N 0.000 claims description 9
- 239000000463 material Substances 0.000 claims description 9
- TWRXJAOTZQYOKJ-UHFFFAOYSA-L Magnesium chloride Chemical compound [Mg+2].[Cl-].[Cl-] TWRXJAOTZQYOKJ-UHFFFAOYSA-L 0.000 claims description 8
- 238000006116 polymerization reaction Methods 0.000 claims description 8
- UKLDJPRMSDWDSL-UHFFFAOYSA-L [dibutyl(dodecanoyloxy)stannyl] dodecanoate Chemical compound CCCCCCCCCCCC(=O)O[Sn](CCCC)(CCCC)OC(=O)CCCCCCCCCCC UKLDJPRMSDWDSL-UHFFFAOYSA-L 0.000 claims description 7
- 238000006243 chemical reaction Methods 0.000 claims description 7
- 239000003795 chemical substances by application Substances 0.000 claims description 7
- 239000012975 dibutyltin dilaurate Substances 0.000 claims description 7
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 claims description 7
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 claims description 7
- XNWFRZJHXBZDAG-UHFFFAOYSA-N 2-METHOXYETHANOL Chemical compound COCCO XNWFRZJHXBZDAG-UHFFFAOYSA-N 0.000 claims description 6
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 claims description 6
- 229910001882 dioxygen Inorganic materials 0.000 claims description 6
- 239000007788 liquid Substances 0.000 claims description 6
- 229910052757 nitrogen Inorganic materials 0.000 claims description 6
- 239000003960 organic solvent Substances 0.000 claims description 6
- 230000003647 oxidation Effects 0.000 claims description 6
- 238000007254 oxidation reaction Methods 0.000 claims description 6
- 229920000151 polyglycol Polymers 0.000 claims description 6
- 239000010695 polyglycol Substances 0.000 claims description 6
- 230000035484 reaction time Effects 0.000 claims description 6
- 238000010992 reflux Methods 0.000 claims description 6
- 125000005234 alkyl aluminium group Chemical group 0.000 claims description 5
- AYOHIQLKSOJJQH-UHFFFAOYSA-N dibutyltin Chemical compound CCCC[Sn]CCCC AYOHIQLKSOJJQH-UHFFFAOYSA-N 0.000 claims description 5
- 238000002360 preparation method Methods 0.000 claims description 5
- 239000002994 raw material Substances 0.000 claims description 5
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 claims description 4
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical compound CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 claims description 4
- 229910003074 TiCl4 Inorganic materials 0.000 claims description 4
- 239000003426 co-catalyst Substances 0.000 claims description 4
- 238000001125 extrusion Methods 0.000 claims description 4
- 229910001629 magnesium chloride Inorganic materials 0.000 claims description 4
- 238000000926 separation method Methods 0.000 claims description 4
- XJDNKRIXUMDJCW-UHFFFAOYSA-J titanium tetrachloride Chemical compound Cl[Ti](Cl)(Cl)Cl XJDNKRIXUMDJCW-UHFFFAOYSA-J 0.000 claims description 4
- 239000002131 composite material Substances 0.000 claims description 3
- 238000001816 cooling Methods 0.000 claims description 3
- 239000012153 distilled water Substances 0.000 claims description 3
- 230000002779 inactivation Effects 0.000 claims description 3
- 238000005935 nucleophilic addition reaction Methods 0.000 claims description 3
- 230000001590 oxidative effect Effects 0.000 claims description 3
- 230000035945 sensitivity Effects 0.000 claims description 3
- 239000012265 solid product Substances 0.000 claims description 3
- 239000002904 solvent Substances 0.000 claims description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 3
- LCGLNKUTAGEVQW-UHFFFAOYSA-N Dimethyl ether Chemical compound COC LCGLNKUTAGEVQW-UHFFFAOYSA-N 0.000 claims description 2
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 2
- IMNFDUFMRHMDMM-UHFFFAOYSA-N N-Heptane Chemical compound CCCCCCC IMNFDUFMRHMDMM-UHFFFAOYSA-N 0.000 claims description 2
- 238000000071 blow moulding Methods 0.000 claims description 2
- 230000000694 effects Effects 0.000 claims description 2
- 238000010534 nucleophilic substitution reaction Methods 0.000 claims description 2
- TVMXDCGIABBOFY-UHFFFAOYSA-N octane Chemical compound CCCCCCCC TVMXDCGIABBOFY-UHFFFAOYSA-N 0.000 claims description 2
- 239000003208 petroleum Substances 0.000 claims description 2
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 claims 3
- 150000001336 alkenes Chemical class 0.000 claims 1
- XLJMAIOERFSOGZ-UHFFFAOYSA-N anhydrous cyanic acid Natural products OC#N XLJMAIOERFSOGZ-UHFFFAOYSA-N 0.000 claims 1
- DKAGJZJALZXOOV-UHFFFAOYSA-N hydrate;hydrochloride Chemical compound O.Cl DKAGJZJALZXOOV-UHFFFAOYSA-N 0.000 claims 1
- 229920005989 resin Polymers 0.000 abstract description 4
- 239000011347 resin Substances 0.000 abstract description 4
- 239000000126 substance Substances 0.000 abstract description 3
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 abstract description 2
- 229910052760 oxygen Inorganic materials 0.000 abstract description 2
- 239000001301 oxygen Substances 0.000 abstract description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 6
- 238000001035 drying Methods 0.000 description 3
- 229920000642 polymer Polymers 0.000 description 3
- 230000007547 defect Effects 0.000 description 2
- 238000007306 functionalization reaction Methods 0.000 description 2
- ZNQVEEAIQZEUHB-UHFFFAOYSA-N 2-ethoxyethanol Chemical compound CCOCCO ZNQVEEAIQZEUHB-UHFFFAOYSA-N 0.000 description 1
- 239000004925 Acrylic resin Substances 0.000 description 1
- 229920000178 Acrylic resin Polymers 0.000 description 1
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 1
- IMROMDMJAWUWLK-UHFFFAOYSA-N Ethenol Chemical group OC=C IMROMDMJAWUWLK-UHFFFAOYSA-N 0.000 description 1
- 239000005977 Ethylene Substances 0.000 description 1
- 229920000219 Ethylene vinyl alcohol Polymers 0.000 description 1
- YCKRFDGAMUMZLT-UHFFFAOYSA-N Fluorine atom Chemical compound [F] YCKRFDGAMUMZLT-UHFFFAOYSA-N 0.000 description 1
- 239000004594 Masterbatch (MB) Substances 0.000 description 1
- 239000004677 Nylon Substances 0.000 description 1
- 239000004698 Polyethylene Substances 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 238000004220 aggregation Methods 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- 150000001335 aliphatic alkanes Chemical class 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 239000004411 aluminium Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 229920001400 block copolymer Polymers 0.000 description 1
- UBAZGMLMVVQSCD-UHFFFAOYSA-N carbon dioxide;molecular oxygen Chemical compound O=O.O=C=O UBAZGMLMVVQSCD-UHFFFAOYSA-N 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 239000007822 coupling agent Substances 0.000 description 1
- 238000005336 cracking Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 238000006073 displacement reaction Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000006353 environmental stress Effects 0.000 description 1
- UFRKOOWSQGXVKV-UHFFFAOYSA-N ethene;ethenol Chemical compound C=C.OC=C UFRKOOWSQGXVKV-UHFFFAOYSA-N 0.000 description 1
- 239000004715 ethylene vinyl alcohol Substances 0.000 description 1
- 229910052731 fluorine Inorganic materials 0.000 description 1
- 239000011737 fluorine Substances 0.000 description 1
- 239000003205 fragrance Substances 0.000 description 1
- 125000000524 functional group Chemical group 0.000 description 1
- 230000007062 hydrolysis Effects 0.000 description 1
- 238000006460 hydrolysis reaction Methods 0.000 description 1
- 239000011159 matrix material Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000000269 nucleophilic effect Effects 0.000 description 1
- 229920001778 nylon Polymers 0.000 description 1
- 239000005022 packaging material Substances 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 238000007747 plating Methods 0.000 description 1
- 229920006112 polar polymer Polymers 0.000 description 1
- 229920000728 polyester Polymers 0.000 description 1
- 229920000573 polyethylene Polymers 0.000 description 1
- 229920001451 polypropylene glycol Polymers 0.000 description 1
- 238000012805 post-processing Methods 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 150000003384 small molecules Chemical class 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- 238000010189 synthetic method Methods 0.000 description 1
- 229920001567 vinyl ester resin Polymers 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J5/00—Manufacture of articles or shaped materials containing macromolecular substances
- C08J5/18—Manufacture of films or sheets
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F110/00—Homopolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond
- C08F110/04—Monomers containing three or four carbon atoms
- C08F110/06—Propene
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F2/00—Processes of polymerisation
- C08F2/38—Polymerisation using regulators, e.g. chain terminating agents, e.g. telomerisation
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F8/00—Chemical modification by after-treatment
- C08F8/12—Hydrolysis
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G18/00—Polymeric products of isocyanates or isothiocyanates
- C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
- C08G18/28—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
- C08G18/40—High-molecular-weight compounds
- C08G18/48—Polyethers
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G18/00—Polymeric products of isocyanates or isothiocyanates
- C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
- C08G18/28—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
- C08G18/40—High-molecular-weight compounds
- C08G18/62—Polymers of compounds having carbon-to-carbon double bonds
- C08G18/6204—Polymers of olefins
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G18/00—Polymeric products of isocyanates or isothiocyanates
- C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
- C08G18/70—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the isocyanates or isothiocyanates used
- C08G18/72—Polyisocyanates or polyisothiocyanates
- C08G18/74—Polyisocyanates or polyisothiocyanates cyclic
- C08G18/75—Polyisocyanates or polyisothiocyanates cyclic cycloaliphatic
- C08G18/751—Polyisocyanates or polyisothiocyanates cyclic cycloaliphatic containing only one cycloaliphatic ring
- C08G18/752—Polyisocyanates or polyisothiocyanates cyclic cycloaliphatic containing only one cycloaliphatic ring containing at least one isocyanate or isothiocyanate group linked to the cycloaliphatic ring by means of an aliphatic group
- C08G18/753—Polyisocyanates or polyisothiocyanates cyclic cycloaliphatic containing only one cycloaliphatic ring containing at least one isocyanate or isothiocyanate group linked to the cycloaliphatic ring by means of an aliphatic group containing one isocyanate or isothiocyanate group linked to the cycloaliphatic ring by means of an aliphatic group having a primary carbon atom next to the isocyanate or isothiocyanate group
- C08G18/755—Polyisocyanates or polyisothiocyanates cyclic cycloaliphatic containing only one cycloaliphatic ring containing at least one isocyanate or isothiocyanate group linked to the cycloaliphatic ring by means of an aliphatic group containing one isocyanate or isothiocyanate group linked to the cycloaliphatic ring by means of an aliphatic group having a primary carbon atom next to the isocyanate or isothiocyanate group and at least one isocyanate or isothiocyanate group linked to a secondary carbon atom of the cycloaliphatic ring, e.g. isophorone diisocyanate
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J2323/00—Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers
- C08J2323/02—Characterised 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
- C08J2323/10—Homopolymers or copolymers of propene
- C08J2323/12—Polypropene
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J2429/00—Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by an alcohol, ether, aldehydo, ketonic, acetal, or ketal radical; Hydrolysed polymers of esters of unsaturated alcohols with saturated carboxylic acids; Derivatives of such polymer
- C08J2429/02—Homopolymers or copolymers of unsaturated alcohols
- C08J2429/04—Polyvinyl alcohol; Partially hydrolysed homopolymers or copolymers of esters of unsaturated alcohols with saturated carboxylic acids
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J2475/00—Characterised by the use of polyureas or polyurethanes; Derivatives of such polymers
- C08J2475/04—Polyurethanes
- C08J2475/08—Polyurethanes from polyethers
Landscapes
- Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- General Chemical & Material Sciences (AREA)
- Wrappers (AREA)
Abstract
本发明公开了一种共混法高阻隔性聚丙烯包装膜的生产方法,以等规聚丙烯‑b‑聚乙二醇两嵌段物作为等规聚丙烯和聚乙烯醇的相容剂,聚乙烯醇具有优秀的阻氧性能,等规聚丙烯‑b‑聚乙二醇两嵌段物作为相容剂后,使规聚丙烯和聚乙烯醇之间具有良好的相容性,使得聚乙烯醇相在聚丙烯树脂中能均匀分散,形成次连续相或片层状结构,从而显著提高共混膜的阻隔性能。
Description
技术领域
本发明涉及包装材料技术领域,具体讲是一种共混法高阻隔性聚丙烯包装膜的生产方法。
背景技术
现有技术的聚丙烯包装膜的阻隔性能不佳,氧气、二氧化碳、水蒸气、香气及有机小分子等物质易透过聚丙烯膜而影响到被包装物的性能与寿命。目前,制备高阻隔聚丙烯膜主要有四种方法:多层复合、表面镀膜、纳米复合改性及共混改性,这四种方法均存在各自的缺陷和不足,例如多层复合膜存在溶剂残留、废弃物分离及后处理困难等问题;表面镀膜设备昂贵、成本高、膜层不均匀;纳米复合易产生粒子团聚现象,导致透明性下降等诸多问题。共混改性是这些方法中工艺最简单、操作最方便、成本最低的制备方法,但现有的改性剂对提高聚丙烯的阻隔性效果不明显。
目前,通过共混的方法提高聚丙烯膜的阻隔性能通常是将聚丙烯与尼龙、聚酯、聚乙烯酵(PVA)或乙烯-酸般乙烯酯共聚物的部分水解物(EVOH)共混,生产出具有优异抗冲、射环境应力、开裂性能和阻隔性能优良的专用料或母料,再经适当配混后进行成型加工。由于所使用的阻隔性树脂均为极性聚合物,而聚丙烯为缺少功能性基团的非扱性聚合物,再加上其半结品性的特性,并且隔性树脂和聚丙烯的相容性很差,无法在聚丙烯基体中均匀分散,大大减弱了其阻隔作用。因此,需要对阻隔性树脂进行改性,提高其与聚丙烯的相容性。
发明内容
鉴于上述现有技术的缺陷,本发明的目的在于:提供一种共混法高阻隔性聚丙烯包装膜的生产方法。
为解决上述问题,本发明的技术解决方案是:一种共混法高阻隔性聚丙烯包装膜的生产方法,包括以下步骤:
(1)用MgCl2负载的TiCl4作为主催化剂,用烷基铝作为副催化剂,催化丙烯聚合,以C-donor为外给电子体,ZnEt2为链转移剂,制备等规聚丙烯;
(2)用干燥的氧气氧化等规聚丙烯,等规聚丙烯用盐酸水解并得到端羟基等规聚丙烯;
(3)将聚乙二醇单甲醚的甲苯溶液加到异佛尔酮二异氰酸酯的甲苯溶液中,制备端异氰酸酯基聚乙二醇;
(4)将端异氰酸酯基聚乙二醇添加到端羟基等规聚丙烯的甲苯溶液中,制备等规聚丙烯-b-聚乙二醇两嵌段物;
(5)以等规聚丙烯-b-聚乙二醇两嵌段物为相容剂,将基等规聚丙烯、等规聚丙烯-b-聚乙二醇两嵌段物、聚乙烯醇共混,共混后在螺杆挤出机中进行充分的熔融共混,再进行挤出、吹塑和双向拉伸,制备聚丙烯复合材料膜。
进一步地,步骤(1)具体为:在无水无氧的条件下,将有机溶剂、作为助催化剂的烷基铝、C-donor外给电子体以及链转移剂ZnEt2加入到Schlenk瓶中,最后加入主催化剂TiCl4/MgCl2,通入压力为0.1~1.1Mpa的丙烯,控制聚合温度为40~80℃,聚合时间为0.5~3h,制得等规聚丙烯。
进一步地,步骤(2)具体为:用干燥的氧气氧化等规聚丙烯,氧化温度为80~120℃,用1mol/L的盐酸水溶液进行淬灭,使催化剂失活,搅拌5-10min后用分液漏斗静置分液,除去上、中层清液;除去固体产物中的溶剂,再用蒸馏水和有机溶剂反复洗涤后真空干燥,制得端羟基等规聚丙烯。
进一步地,所述有机溶剂为甲苯、二甲苯、正庚烷、正辛烷或石油醚中的一种。
进一步地,步骤(3)具体为:在装有回流冷凝管的、干燥且经氮气抽排3次的Schlenk瓶中,加入聚乙二醇单甲醚、异佛尔酮二异氰酸酯、二月桂酸二丁基锡和甲苯,反应温度为25℃~60℃,反应时间为4~24h,聚乙二醇单甲醚与异佛尔酮二异氰酸酯在催化剂二月桂酸二丁基锡的作用下发生亲核取代反应,得到端异氰酸酯基聚乙二醇。
进一步地,步骤(4)具体为:在装有回流冷凝管的、干燥且经氮气抽排3次的Schlenk瓶中,加入端羟基等规聚丙烯、端异氰酸酯基聚乙二醇、甲苯和二月桂酸二丁基锡,端异氰酸酯基聚乙二醇与端羟基功能化等规聚丙烯在催化剂二月桂酸二丁基锡的作用下发生亲核加成反应,得到等规聚丙烯-b-聚乙二醇两嵌段物,反应温度为90℃~130℃,反应时间为4~24h。
进一步地,步骤(5)具体为:以等规聚丙烯-b-聚乙二醇两嵌段物为相容剂,将等规聚丙烯、等规聚丙烯-b-聚乙二醇两嵌段物、聚乙烯醇共混,混合后的原料经双螺杆挤出机塑化,将熔融态熔体送入模头,并在模头口挤出熔融态片材,挤出的片材置于对开模中,闭模后立即在型坯内通入压缩空气,冷却脱模后得到铸片,铸片再分别经过纵拉机和横向拉伸机,将片材拉制成薄膜,薄膜经厚度检测后进行冷却并收卷。
本发明的有益效果是:
(1)以TiCl4/MgCl2作为主催化剂,烷基铝作为助催化剂,ZnEt2为链转移剂制备分子量可控的等规聚丙烯,再将聚合物用干燥的氧气氧化,用盐酸水溶液水解制备端羟基等规聚丙烯,该合成方法合成的聚合物分子量可控,易于实现工业化;
(2)以异佛尔酮二异氰酸酯为偶联剂将端羟基等规聚丙烯与聚乙二醇单甲醚偶联起来,制备等规聚丙烯-b-聚乙二醇两嵌段物,该合成技术方法实施方便,成本较低,并且效率高,所使用的原料简单易得,价格低廉,可通过调节两种链段的长度,调控嵌段共聚物的性能,制备的等规聚丙烯-b-聚乙二醇两嵌段物中等规聚丙烯链段保持了很高的等规度;
(3)以等规聚丙烯-b-聚乙二醇两嵌段物作为等规聚丙烯和聚乙烯醇的相容剂,聚乙烯醇具有优秀的阻氧性能,等规聚丙烯-b-聚乙二醇两嵌段物作为相容剂后,使规聚丙烯和聚乙烯醇之间具有良好的相容性,使得聚乙烯醇相在聚丙烯树脂中能均匀分散,形成次连续相或片层状结构,从而显著提高共混膜的阻隔性能。
具体实施方式
为比较直观、完整地理解本发明的技术方案,现进行非限制性的特征说明如下:
实施例一:
一种共混法高阻隔性聚丙烯包装膜的生产方法,包括以下步骤:
(1)在无水无氧的条件下,将甲苯、作为助催化剂的烷基铝、C-donor外给电子体以及链转移剂ZnEt2加入到Schlenk瓶中,最后加入主催化剂TiCl4/MgCl2,通入压力为0.1~1.1Mpa的丙烯,控制聚合温度为50℃,聚合时间为1h,制得等规聚丙烯。
(2)用干燥的氧气氧化等规聚丙烯,在氧化温度为100℃环境下反应0.5h,用1mol/L的盐酸水溶液进行淬灭,使催化剂失活,搅拌10min后用分液漏斗静置分液,除去上、中层清液;除去固体产物中的溶剂,再用蒸馏水和甲苯反复洗涤后真空干燥,制得端羟基等规聚丙烯。
(3)在装有回流冷凝管的、干燥且经氮气抽排3次的Schlenk瓶中,加入聚乙二醇单甲醚、异佛尔酮二异氰酸酯、二月桂酸二丁基锡和甲苯,反应温度为30℃,反应时间为6h,聚乙二醇单甲醚与异佛尔酮二异氰酸酯在催化剂二月桂酸二丁基锡的作用下发生亲核取代反应,得到端异氰酸酯基聚乙二醇。
(4)在装有回流冷凝管的、干燥且经氮气抽排3次的Schlenk瓶中,加入端羟基等规聚丙烯、端异氰酸酯基聚乙二醇、甲苯和二月桂酸二丁基锡,端异氰酸酯基聚乙二醇与端羟基功能化等规聚丙烯在催化剂二月桂酸二丁基锡的作用下发生亲核加成反应,得到等规聚丙烯-b-聚乙二醇两嵌段物,反应温度为100℃,反应时间为6h。
(5)按以下质量百分比称取原料:等规聚丙烯60%、等规聚丙烯-b-聚乙二醇两嵌段物15%、聚乙烯醇25%;以等规聚丙烯-b-聚乙二醇两嵌段物为相容剂,将等规聚丙烯、等规聚丙烯-b-聚乙二醇两嵌段物、聚乙烯醇共混,混合后的原料经双螺杆挤出机塑化,将熔融态熔体送入模头,并在模头口挤出熔融态片材,挤出的片材置于对开模中,闭模后立即在型坯内通入压缩空气,冷却脱模后得到铸片,铸片再分别经过纵拉机和横向拉伸机,将片材拉制成薄膜,薄膜经厚度检测后进行冷却并收卷。
Claims (7)
1.一种共混法高阻隔性聚丙烯包装膜的生产方法,其特征在于包括以下步骤:
(1)用MgCl2负载的TiCl4作为主催化剂,用烷基铝作为副催化剂,催化丙烯聚合,以C-donor为外给电子体,ZnEt2为链转移剂,制备等规聚丙烯;
(2)用干燥的氧气氧化等规聚丙烯,等规聚丙烯用盐酸水解并得到端羟基等规聚丙烯;
(3)将聚乙二醇单甲醚的甲苯溶液加到异佛尔酮二异氰酸酯的甲苯溶液中,制备端异氰酸酯基聚乙二醇;
(4)将端异氰酸酯基聚乙二醇添加到端羟基等规聚丙烯的甲苯溶液中,制备等规聚丙烯-b-聚乙二醇两嵌段物;
(5)以等规聚丙烯-b-聚乙二醇两嵌段物为相容剂,将基等规聚丙烯、等规聚丙烯-b-聚乙二醇两嵌段物、聚乙烯醇共混,共混后在螺杆挤出机中进行充分的熔融共混,再进行挤出、吹塑和双向拉伸,制备聚丙烯复合材料膜。
2.根据权利要求1所述的一种共混法高阻隔性聚丙烯包装膜的生产方法,其特征在于步骤(1)具体为:在无水无氧的条件下,将有机溶剂、作为助催化剂的烷基铝、C-donor外给电子体以及链转移剂ZnEt2加入到Schlenk瓶中,最后加入主催化剂TiCl4/MgCl2,通入压力为0.1~1.1Mpa的丙烯,控制聚合温度为40~80℃,聚合时间为0.5~3h,制得等规聚丙烯。
3.根据权利要求2所述的一种共混法高阻隔性聚丙烯包装膜的生产方法,其特征在于步骤(2)具体为:用干燥的氧气氧化等规聚丙烯,氧化温度为80~120℃,用1mol/L的盐酸水溶液进行淬灭,使催化剂失活,搅拌5-10min后用分液漏斗静置分液,除去上、中层清液;除去固体产物中的溶剂,再用蒸馏水和有机溶剂反复洗涤后真空干燥,制得端羟基等规聚丙烯。
4.根据权利要求3所述的一种共混法高阻隔性聚丙烯包装膜的生产方法,其特征在于:所述有机溶剂为甲苯、二甲苯、正庚烷、正辛烷或石油醚中的一种。
5.根据权利要求1所述的一种共混法高阻隔性聚丙烯包装膜的生产方法,其特征在于步骤(3)具体为:在装有回流冷凝管的、干燥且经氮气抽排3次的Schlenk瓶中,加入聚乙二醇单甲醚、异佛尔酮二异氰酸酯、二月桂酸二丁基锡和甲苯,反应温度为25℃~60℃,反应时间为4~24h,聚乙二醇单甲醚与异佛尔酮二异氰酸酯在催化剂二月桂酸二丁基锡的作用下发生亲核取代反应,得到端异氰酸酯基聚乙二醇。
6.根据权利要求5述的一种共混法高阻隔性聚丙烯包装膜的生产方法,其特征在于步骤(4)具体为:在装有回流冷凝管的、干燥且经氮气抽排3次的Schlenk瓶中,加入端羟基等规聚丙烯、端异氰酸酯基聚乙二醇、甲苯和二月桂酸二丁基锡,端异氰酸酯基聚乙二醇与端羟基功能化等规聚丙烯在催化剂二月桂酸二丁基锡的作用下发生亲核加成反应,得到等规聚丙烯-b-聚乙二醇两嵌段物,反应温度为90℃~130℃,反应时间为4~24h。
7.根据权利要求1的一种共混法高阻隔性聚丙烯包装膜的生产方法,其特征在于步骤(5)具体为:以等规聚丙烯-b-聚乙二醇两嵌段物为相容剂,将等规聚丙烯、等规聚丙烯-b-聚乙二醇两嵌段物、聚乙烯醇共混,混合后的原料经双螺杆挤出机塑化,将熔融态熔体送入模头,并在模头口挤出熔融态片材,挤出的片材置于对开模中,闭模后立即在型坯内通入压缩空气,冷却脱模后得到铸片,铸片再分别经过纵拉机和横向拉伸机,将片材拉制成薄膜,薄膜经厚度检测后进行冷却并收卷。
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201811113355.6A CN109306120B (zh) | 2018-09-25 | 2018-09-25 | 一种共混法高阻隔性聚丙烯包装膜的生产方法 |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201811113355.6A CN109306120B (zh) | 2018-09-25 | 2018-09-25 | 一种共混法高阻隔性聚丙烯包装膜的生产方法 |
Publications (2)
Publication Number | Publication Date |
---|---|
CN109306120A true CN109306120A (zh) | 2019-02-05 |
CN109306120B CN109306120B (zh) | 2021-06-25 |
Family
ID=65224714
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201811113355.6A Active CN109306120B (zh) | 2018-09-25 | 2018-09-25 | 一种共混法高阻隔性聚丙烯包装膜的生产方法 |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN109306120B (zh) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN112358571A (zh) * | 2020-11-10 | 2021-02-12 | 熊烈祥 | 一种改性pp助剂及其制备方法 |
JP7405642B2 (ja) | 2019-03-12 | 2023-12-26 | 三洋化成工業株式会社 | 樹脂用相溶化剤 |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103214605A (zh) * | 2013-04-17 | 2013-07-24 | 浙江大学 | 一种端羟基功能化的等规聚丙烯及其制备方法 |
CN103509192A (zh) * | 2013-09-14 | 2014-01-15 | 浙江大学 | 一种等规聚丙烯-b-聚乙二醇两嵌段物及其制备方法 |
CN106315009A (zh) * | 2016-08-19 | 2017-01-11 | 湖北富思特材料科技集团有限公司 | 一种耐磨花烟膜及其制备方法 |
CN108559174A (zh) * | 2018-03-27 | 2018-09-21 | 贵州省材料产业技术研究院 | 一种相形态与界面结晶调控制备高阻隔聚丙烯材料的方法 |
-
2018
- 2018-09-25 CN CN201811113355.6A patent/CN109306120B/zh active Active
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103214605A (zh) * | 2013-04-17 | 2013-07-24 | 浙江大学 | 一种端羟基功能化的等规聚丙烯及其制备方法 |
CN103509192A (zh) * | 2013-09-14 | 2014-01-15 | 浙江大学 | 一种等规聚丙烯-b-聚乙二醇两嵌段物及其制备方法 |
CN106315009A (zh) * | 2016-08-19 | 2017-01-11 | 湖北富思特材料科技集团有限公司 | 一种耐磨花烟膜及其制备方法 |
CN108559174A (zh) * | 2018-03-27 | 2018-09-21 | 贵州省材料产业技术研究院 | 一种相形态与界面结晶调控制备高阻隔聚丙烯材料的方法 |
Non-Patent Citations (2)
Title |
---|
徐百平主编: "《塑料挤出成型技术》", 31 August 2011, 北京:中国轻工业出版社 * |
李振昊、荔栓红、陈超、张勇杰、李化毅: ""聚烯烃-极性聚合物嵌段共聚物最新研究进展"", 《高分子通报》 * |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP7405642B2 (ja) | 2019-03-12 | 2023-12-26 | 三洋化成工業株式会社 | 樹脂用相溶化剤 |
CN112358571A (zh) * | 2020-11-10 | 2021-02-12 | 熊烈祥 | 一种改性pp助剂及其制备方法 |
Also Published As
Publication number | Publication date |
---|---|
CN109306120B (zh) | 2021-06-25 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
Ronca | Polyethylene | |
CN104109262B (zh) | 一种热塑性淀粉-聚乙烯醇复合塑料薄膜 | |
CN106397974B (zh) | 一种高阻隔抗老化的水杯及其制备方法 | |
CN104334630B (zh) | 一种加工性能改善的交联聚乙烯组合物 | |
CN104802482A (zh) | 一种三层共挤聚丙烯/聚乙烯/聚丙烯上吹薄膜及其制备方法 | |
CN111040277A (zh) | 高强度聚乙烯双壁波纹管内壁用填充母料及其制造方法 | |
CN101293982A (zh) | 一种高密度聚乙烯土工膜及其制作工艺 | |
CN109293958A (zh) | 一种低雾度高阻隔性聚丙烯膜的生产方法 | |
CN109306120A (zh) | 一种共混法高阻隔性聚丙烯包装膜的生产方法 | |
CN110452525B (zh) | 一种石墨烯改性抗静电tpu膜 | |
CN109093978A (zh) | 一种高拉伸倍数的薄膜及其生产方法 | |
CN109280270A (zh) | 一种耐高温高阻隔性聚丙烯膜的生产方法 | |
WO2018205326A1 (zh) | 一种免粘合剂的瓶盖垫片和/或衬垫及其制备方法 | |
CN109233105A (zh) | 一种抗拉伸高阻隔性聚丙烯膜的生产方法 | |
CN108250371B (zh) | 键合型聚合物/二氧化硅杂化材料及其制备方法 | |
CN105367874B (zh) | 药用托盘专用的生物质复合材料及其制备方法 | |
CN107011563A (zh) | 一种环保聚乙烯塑料袋及其制备方法 | |
CN103991246A (zh) | 一种聚烯烃母料制备三层共挤管材的方法 | |
CN109401227A (zh) | 采用扩链剂制备的pla/pbat共混改性生物降解树脂及其制备方法 | |
CN101717553A (zh) | 一种高阻隔复合材料及其制备工艺 | |
CN111269481A (zh) | 一种高阻隔抗菌pe膜及其生产工艺 | |
CN114921069B (zh) | 一种高热封强度的全生物降解薄膜及其制备方法和应用 | |
CN100487054C (zh) | 低弯曲强度尼龙6/聚乙烯合金的制备方法 | |
CN110964339A (zh) | 一种气密性良好的生物基复合材料薄膜制备方法 | |
CN109233106A (zh) | 一种低成本高阻隔性聚丙烯膜的生产方法 |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
GR01 | Patent grant | ||
GR01 | Patent grant |