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    • 1. 发明申请
    • POLYPROPYLENE COMPOSITIONS
    • 聚丙烯组合物
    • WO2016078974A1
    • 2016-05-26
    • PCT/EP2015/076246
    • 2015-11-10
    • SABIC GLOBAL TECHNOLOGIES B.V.
    • FELLAHI, SaidKIOUL, Azzedine
    • C08L23/10C08L77/00C08L59/02
    • C08L23/10C08K7/14C08L59/02C08L77/02C08L2201/10C08L77/00
    • The invention relates to a composition comprising (a) polypropylene having a melt mass flow rate as measured in accordance with ISO 1133 using a 2.16 kg weight and at a temperature of 230 °C in the range from 10 to 40 g/10min and (b) a polymer preferably chosen from the group consisting of polyoxymethylene, polyamide and mixture thereof, wherein the amount of component (b) is from 0.005 to 5 wt% based on the total weight of the components (a) and (b) and wherein the polypropylene has a melt temperature TmPP and a crystallization temperature TcPP, the polymer has a melt temperature TmP and a crystallization temperature TcP, wherein the TcP is 5-40 °C higher than TcPP, wherein the T m and T c are determined using Differential Scanning Calorimetry according to ASTM D 3418-08 using a scan rate of 10°C/min on a sample of 10mg and using the second heating cycle.
    • 本发明涉及一种组合物,其包含(a)具有根据ISO 1133测量的熔体质量流量的聚丙烯,其使用2.16kg重量,在230℃的温度下在10至40g / 10min的范围内和(b )优选选自聚甲醛,聚酰胺及其混合物的聚合物,其中组分(b)的量基于组分(a)和(b)的总重量为0.005-5重量%,其中 聚丙烯具有熔融温度TmPP和结晶温度TcPP,聚合物具有熔融温度TmP和结晶温度TcP,其中TcP比TcPP高5-40℃,其中Tm和Tc使用差示扫描量热法测定,根据 至ASTM D 3418-08,使用10℃/ min的扫描速率对10mg样品并使用第二加热循环。
    • 4. 发明申请
    • PROCESS FOR TRANSITIONING BETWEEN INCOMPATIBLE CATALYSTS
    • 不相容催化剂之间的过渡过程
    • WO2017108347A1
    • 2017-06-29
    • PCT/EP2016/079099
    • 2016-11-29
    • SABIC GLOBAL TECHNOLOGIES B.V.
    • BANAT, YahyaHUMYDI-AL, AbdulazizFELLAHI, Said
    • C08F2/00C08F2/01C08F2/34C08F4/6592
    • C08F2/34C08F2/001C08F2/01C08F4/6592C08F2410/05
    • The invention relates to a process for transitioning from a first continuous polymerization in a gas phase reactor conducted in the presence of a metallocene catalyst to a second polymerization conducted in the presence of a Ziegler-Natta catalyst in the gas phase reactor wherein the metallocene catalyst and the Ziegler-Natta catalysts are incompatible, the process comprising: (a) discontinuing the introduction of the metallocene catalyst into the gas phase reactor; (b) introducing an effective amount of cyclohexylamine into the reactor to at least partially deactivate the metallocene catalyst; (c) introducing an organometallic compound into the reactor and reacting the organometallic compound with cyclohexylamine; (d) degas the gas composition of the reactor and build up a new composition inside the reactor for the second polymerization with the Ziegler-Natta catalyst (e) introducing the Ziegler-Natta catalyst into the reactor.
    • 本发明涉及一种从在茂金属催化剂存在下进行的气相反应器中的第一次连续聚合转变为在Ziegler-Natta催化剂存在下进行的第二次聚合的方法, 气相反应器,其中茂金属催化剂和齐格勒 - 纳塔催化剂不相容,所述方法包括:(a)中止将茂金属催化剂引入气相反应器; (b)将有效量的环己胺引入反应器中以至少部分钝化茂金属催化剂; (c)将有机金属化合物引入反应器中并使有机金属化合物与环己胺反应; (d)使反应器的气体组合物脱气并在反应器内用Ziegler-Natta催化剂在第二次聚合反应中形成新组合物(e)将齐格勒 - 纳塔催化剂引入反应器中。
    • 5. 发明申请
    • COMPOSITION COMPRISING HETEROPHASIC PROPYLENE COPOLYMER
    • 包含异构丙烯共聚物的组合物
    • WO2017009193A1
    • 2017-01-19
    • PCT/EP2016/066192
    • 2016-07-07
    • SABIC GLOBAL TECHNOLOGIES B.V.
    • FELLAHI, SaidKIOUL, AzzedineAHMED, Syed MehmoodAL-OTAIBI, Abdullah, Shamroukh
    • C08L23/12B29C45/00C08L23/10
    • C08L23/12C08K5/0083C08L23/10C08L23/16C08L59/04C08L2207/02C08L77/00
    • The invention relates to a composition comprising (a) a heterophasic propylene copolymer consisting of 5 (i) a propylene-based matrix, wherein the propylene-based matrix consists of a propylene homopolymer and/or a propylene- α-olefin copolymer consisting of at least 70 wt% of propylene and at most 30 wt% of α-olefin, based on the total weight of the propylene-based matrix and wherein the propylene-based matrix is present in an amount of 60 to 95 wt% based on the total heterophasic propylene copolymer and (ii) a dispersed ethylene-α-olefin copolymer, wherein the dispersed ethylene-α-olefin copolymer is present in an amount of 40 to 5 wt% based on the total heterophasic propylene copolymer and wherein the sum of the total amount of propylene-based matrix and total amount of the dispersed ethylene-α-olefin copolymer in the heterophasic propylene copolymer is 100 wt% and (b) a polymer preferably chosen from the group consisting of polyoxymethylene, polyamide and mixtures thereof, wherein the amount of component (b) is from 0.005 to 5 wt% based on the total weight of the components (a) and (b) and wherein the heterophasic propylene copolymer (a) has a melt temperature TmPP and a crystallization temperature TcPP, the polymer (b) has a melt temperature TmP and a crystallization temperature TcP, wherein the TcP is 5-40 ºC higher than TcPP, wherein the T m and T c are determined using Differential Scanning Calorimetry according to ASTM D 3418-08 using a scan rate of 10°C/min on a sample of 10mg and using the second heating cycle.
    • 本发明涉及一种组合物,其包含(a)由5(i)丙烯基基体组成的多相丙烯共聚物,其中丙烯基基体由丙烯均聚物和/或丙烯-α-烯烃共聚物组成,丙烯-α-烯烃共聚物由 至少70重量%的丙烯和至多30重量%的α-烯烃,基于丙烯基基体的总重量,其中基于丙烯的基体的总量为60至95重量% 异相丙烯共聚物和(ii)分散的乙烯-α-烯烃共聚物,其中分散的乙烯-α-烯烃共聚物的存在量相对于总多相丙烯共聚物为40-5重量%,其中总和 丙烯类基质的量和多相丙烯共聚物中分散的乙烯-α-烯烃共聚物的总量为100重量%,(b)优选选自聚甲醛,聚酰胺及其混合物的聚合物, 组分(b)的量基于组分(a)和(b)的总重量为0.005-5重量%,其中异相丙烯共聚物(a)具有熔融温度TmPP和结晶温度TcPP, 聚合物(b)具有熔融温度TmP和结晶温度TcP,其中TcP比TcPP高5-40℃,其中使用差示扫描量热法根据ASTM D 3418-08使用扫描速率测定Tm和Tc 在10℃的样品上使用10℃/分钟,并使用第二加热循环。