会员体验
专利管家(专利管理)
工作空间(专利管理)
风险监控(情报监控)
数据分析(专利分析)
侵权分析(诉讼无效)
联系我们
交流群
官方交流:
QQ群: 891211   
微信请扫码    >>>
现在联系顾问~
热词
    • 4. 发明申请
    • Process for reducing the VOC content of a polyolefin composition
    • WO2023006423A1
    • 2023-02-02
    • PCT/EP2022/069569
    • 2022-07-13
    • BOREALIS AG
    • WANG, JingboGAHLEITNER, MarkusBERNREITNER, KlausLESKINEN, PauliPOTTER, Elisabeth
    • C08F6/00C08L23/14
    • 31 ABSTRACT The present invention relates to a process for reducing the volatile organic compound (VOC, VDA 278 October 2011) content of a polyolefin composition, the polyolefin composition including a polypropylene homopolymer, a polypropylene copolymer, a polyethylene homopolymer, and/or a polyethylene copolymer, the process comprising the steps of a) subjecting the polyolefin composition having a VOC (VOC, VDA 278 October 2011) content, which is contained in an aeration vessel, to an aeration gas flow, and maintaining said aeration gas flow for an aeration time of 15 hours or less the aeration gas having a minimum temperature of at least 20°C measured at an inlet of the aeration gas of the aeration vessel, and a maximum temperature of 99°C measured at an inlet for aeration gas of the aeration vessel; the aeration vessel having - at least one inlet for aeration gas, - at least one outlet for aeration gas, - an inlet for the polyolefin composition having a VOC content, - an outlet for an aerated polyolefin composition at the bottom of the aeration vessel; wherein the polyolefin composition contains 20 to 55 pieces/g (pellet size 3-5 mm) as measured according to the specification; and wherein the polyolefin composition is present in the aeration vessel as a packed bed; and b) withdrawing the aerated polyolefin composition from the aeration vessel having a VOC content (VOC, VDA 278 October 2011) of not greater than 600 µg/g.
    • 6. 发明申请
    • HETEROPHASIC POLYOLEFIN COMPOSITION HAVING IMPROVED FLOWABILITY AND IMPACT STRENGTH
    • 具有改善流动性和冲击强度的异种聚烯烃组合物
    • WO2012116718A1
    • 2012-09-07
    • PCT/EP2011/005656
    • 2011-11-10
    • BOREALIS AGKOCK, CorneliaGREIN, ChristellePOTTER, Elisabeth
    • KOCK, CorneliaGREIN, ChristellePOTTER, Elisabeth
    • C08L23/10
    • C08L23/10C08L23/0815C08L23/16C08L2666/06
    • The invention relates to a heterophasic polyolefin composition having improved flowability and impact strength but also an excellent impact/stiffness balance and a low amount of a hexane extractable fraction, to a process for the preparation of such a heterophasic polyolefin composition, to articles made therefrom and uses of the heterophasic polyolefin composition. The heterophasic polyolefin composition, comprises a matrix comprising a heterophasic propylene base polymer, comprising a matrix comprising a propylene homo- and/or copolymer, an elastomeric ethylene/ alpha-olefin phase dispersed in the matrix, and an ethylene polymer component having an MFR (2.16 kg/ 190 °C) of 15 to 300 g/10 min. and a density of 0.915 g/cm3 or more, wherein the heterophasic polyolefin composition comprising monomer units derived from an oligomeric diene compound, and having a hexane extractable fraction in an amount of not more than 6 wt.%, measured from extruded cast films of 100μm thickness at 50 °C and 2 h extraction time and an MFR (2.16 kg, 230 °C, ISO 1133) of 8 to 80 g/10 min. The heterophasic propylene polymer composition may be used for extrusion, injection moulding, blow moulding, injection stretch blow moulding, cast film extrusion or thermoforming.
    • 本发明涉及具有改进的流动性和冲击强度的异相聚烯烃组合物,而且具有优异的冲击/刚度平衡和少量的己烷可萃取部分,用于制备这种多相聚烯烃组合物的方法制备的制品和 多相聚烯烃组合物的用途。 多相聚烯烃组合物包含包含多相丙烯基聚合物的基质,其包含基体,其包含丙烯均聚物和/或共聚物,分散在基质中的弹性体乙烯/α-烯烃相和具有MFR( 2.16kg / 190℃)为15-300g / 10min。 并且密度为0.915g / cm 3以上,其中所述多相聚烯烃组合物包含衍生自低聚二烯化合物的单体单元,并且具有不超过6重量%的己烷可萃取组分,其量由 在50℃下的100μm厚度和2小时提取时间和8至80g / 10min的MFR(2.16kg,230℃,ISO 1133)。 异相丙烯聚合物组合物可用于挤出,注射成型,吹塑,注射拉伸吹塑,流延膜挤出或热成型。
    • 10. 发明申请
    • RANDOM PROPYLENE COPOLYMER WITH HIGH STIFFNESS AND LOW HAZE
    • 随机丙烯共聚物,具有高刚度和低湿度
    • WO2012159927A1
    • 2012-11-29
    • PCT/EP2012/058985
    • 2012-05-15
    • BOREALIS AGPOTTER, ElisabethDOSHEW, PetarKHEIRANDISH, SaeidLESKINEN, PauliGAHLEITNER, Markus
    • POTTER, ElisabethDOSHEW, PetarKHEIRANDISH, SaeidLESKINEN, PauliGAHLEITNER, Markus
    • F01D5/02F01D5/34C08L23/14
    • C08L23/142C08F210/06C08F210/16C08F2500/12C08F2/34C08F2/14C08F2/001
    • Process for the preparation of a propylene copolymer, said process is a sequential polymerization process comprising at least two reactors connected in series, wherein said process comprises the steps of (A) polymerizing in a first reactor propylene and optionally ethylene and /or a C 4 to C 12 a-olefin, obtaining a polypropylene fraction (A), (B) transferring said polypropylene fraction (A) and unreacted comonomers from the first reactor into a second reactor, (C) feeding to said second reactor propylene and ethylene and /or a C4 to C12 a-olefin, (D) polymerizing in said second reactor and in the presence of said polypropylene fraction (A) propylene and ethylene and /or a C 4 to C 12 a-olefin, obtaining a propylene copolymer fraction (B), said polypropylene fraction (A) and said propylene copolymer fraction (B) form the propylene copolymer, wherein further the temperature in the first reactor (R-1) is of more than 70 °C to equal or below 90 °C, the temperature in the second reactor (R-2) is of equal or more than 80 °C to equal or below 95 °C, in the first reactor (R-1) and second reactor (R-2) the polymerization takes place in the presence of a solid catalyst system (SCS) having a surface area measured according to ASTM D 3662 of less than 30 m 2 /g and/or a pore volume measured according to ASTM 4641 of less than 1.0 ml/g, wherein further said solid catalyst system comprises a transition metal selected from one of the groups 4 to 6 of the periodic table (IUPAC), a metal which is selected from one of the groups 1 to 3 of the periodic table (IUPAC), and an internal electron donor (ID), and said propylene copolymer has a melt flow rate MFR 2 (230 °C) of equal or more than 65 to equal or below 200 g/lOmin, and a comonomer content in the range of equal or more than 1.5 to equal or below 8.0 wt.-%.
    • 制备丙烯共聚物的方法,所述方法是包含至少两个串联连接的反应器的顺序聚合方法,其中所述方法包括以下步骤:(A)在第一反应器中聚合丙烯和任选的乙烯和/或C 4至 得到聚丙烯馏分(A),(B)将所述聚丙烯馏分(A)和未反应的共聚单体从第一反应器转移到第二反应器中,(C)向第二反应器进料丙烯和乙烯和/或 (D)在所述第二反应器中和在所述聚丙烯级分(A)丙烯和乙烯和/或C 4至C 12α-烯烃存在下聚合,得到丙烯共聚物部分(B),所述 聚丙烯馏分(A)和所述丙烯共聚物部分(B)形成丙烯共聚物,其中第一反应器(R-1)中的温度进一步高于70℃至等于或低于90℃, 第二反应器(R-2 )等于或大于80℃至等于或低于95℃,在第一反应器(R-1)和第二反应器(R-2)中,聚合在固体催化剂体系(SCS)存在下进行, 具有根据ASTM D 3662测量的表面积小于30m 2 / g和/或根据ASTM 4641测量的孔体积小于1.0ml / g,其中所述固体催化剂体系还包含选自以下之一的过渡金属: 元素周期表(IUPAC)的第4至6族,选自元素周期表(IUPAC)中的1至3族之一的金属和内部电子给体(ID),所述丙烯共聚物具有熔体 等于或大于65的流量MFR 2(230℃)等于或低于200g / 10min,共聚单体含量在等于或大于1.5至等于或低于8.0重量%的范围内。