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    • 1. 发明授权
    • Heterogeneous in-reactor polymer blends
    • 不均匀的反应器内聚合物共混物
    • US08106127B2
    • 2012-01-31
    • US12638861
    • 2009-12-15
    • Carlos U. De GraciaKevin R. SquirePeijun JiangArmenag H. DekmezianBeverly J. PooleCesar A. Garcia-Franco
    • Carlos U. De GraciaKevin R. SquirePeijun JiangArmenag H. DekmezianBeverly J. PooleCesar A. Garcia-Franco
    • C08F8/00C08L23/04C08L23/10C08K5/00
    • C08L23/16C08L23/12C08L2314/06C08L2666/06
    • An in-reactor polymer blend comprises (a) a propylene-containing first polymer; and (b) an ethylene-containing second polymer such that the polymer blend comprises between about 50 wt % and about 80 wt % units derived from ethylene and between about 50 wt % and about 20 wt % units derived from propylene. The blend is substantially free of dienes and the content of ethylene in the second polymer in the form of ethylene-ethylene-ethylene triads is at least 40%. The second polymer contains at least 0.1 branch having 8 or more carbon atoms per 10,000 carbons. In addition, the blend has a strain hardening index of at least 1.8, a shear thinning slope in the plot of log(dynamic viscosity) versus log(frequency) of less than −0.2 and exhibits at least two peaks when subjected to Differential Scanning Calorimetry (first melt) corresponding to a first melting point of at least 150° C. and a second melting point of at least 40° C. such that the difference between the first and second melting temperatures is at least 20° C.
    • 反应器内聚合物共混物包含(a)含丙烯的第一聚合物; 和(b)含乙烯的第二聚合物,使得聚合物共混物包含衍生自乙烯的约50重量%至约80重量%的单元和衍生自丙烯的约50重量%至约20重量%的单元。 共混物基本上不含二烯,乙烯 - 乙烯 - 乙烯三单元组形式的第二聚合物中的乙烯含量至少为40%。 第二聚合物含有至少0.1个分支,每10,000个碳原子具有8个或更多个碳原子。 此外,共混物的应变硬化指数为至少1.8,对数(动态粘度)对log(频率)的曲线图中的剪切变稀斜率小于-0.2,并且当进行差示扫描量热法时显示出至少两个峰 (第一熔体),其对应于至少150℃的第一熔点和至少40℃的第二熔点,使得第一和第二熔融温度之间的差异为至少20℃。
    • 2. 发明申请
    • Heterogeneous In-Reactor Polymer Blends
    • 非均相反应器聚合物共混物
    • US20100152390A1
    • 2010-06-17
    • US12638861
    • 2009-12-15
    • Carlos U. De GraciaKevin R. SquirePeijun JiangArmenag H. DekmezianBeverly J. PooleCesar A. Garcia-Franco
    • Carlos U. De GraciaKevin R. SquirePeijun JiangArmenag H. DekmezianBeverly J. PooleCesar A. Garcia-Franco
    • C08L23/06
    • C08L23/16C08L23/12C08L2314/06C08L2666/06
    • An in-reactor polymer blend comprises (a) a propylene-containing first polymer; and (b) an ethylene-containing second polymer such that the polymer blend comprises between about 50 wt % and about 80 wt % units derived from ethylene and between about 50 wt % and about 20 wt % units derived from propylene. The blend is substantially free of dienes and the content of ethylene in the second polymer in the form of ethylene-ethylene-ethylene triads is at least 40%. The second polymer contains at least 0.1 branch having 8 or more carbon atoms per 10,000 carbons. In addition, the blend has a strain hardening index of at least 1.8, a shear thinning slope in the plot of log(dynamic viscosity) versus log(frequency) of less than −0.2 and exhibits at least two peaks when subjected to Differential Scanning Calorimetry (first melt) corresponding to a first melting point of at least 150° C. and a second melting point of at least 40° C. such that the difference between the first and second melting temperatures is at least 20° C.
    • 反应器内聚合物共混物包含(a)含丙烯的第一聚合物; 和(b)含乙烯的第二聚合物,使得聚合物共混物包含衍生自乙烯的约50重量%至约80重量%的单元和衍生自丙烯的约50重量%至约20重量%的单元。 共混物基本上不含二烯,乙烯 - 乙烯 - 乙烯三单元组形式的第二聚合物中的乙烯含量至少为40%。 第二聚合物含有至少0.1个分支,每10,000个碳原子具有8个或更多个碳原子。 此外,共混物的应变硬化指数为至少1.8,对数(动态粘度)对log(频率)的曲线图中的剪切变稀斜率小于-0.2,并且当进行差示扫描量热法时显示出至少两个峰 (第一熔体),其对应于至少150℃的第一熔点和至少40℃的第二熔点,使得第一和第二熔融温度之间的差异为至少20℃。
    • 7. 发明申请
    • Thermoplastic Elastomer Polyolefin In-Reactor Blends And Molded Articles Therefrom
    • 热塑性弹性体聚烯烃反应器共混物和成型制品
    • US20100152383A1
    • 2010-06-17
    • US12638916
    • 2009-12-15
    • Peijun JiangArmenag H. DekmezianKevin R. SquireCesar A. Garcia-Franco
    • Peijun JiangArmenag H. DekmezianKevin R. SquireCesar A. Garcia-Franco
    • C08L23/04
    • C08L23/06C08L23/08C08L2205/02C08L2314/06C08L2666/06
    • This invention relates to an in-reactor polymer blend comprising: (a) a first ethylene-containing polymer having a density of greater than 0.90 g/cm3 and a Mw of more than 20,000 g/mol and (b) a second ethylene-containing polymer having a density of less than 0.90 g/cm3, wherein the polymer blend has a Tm of at least 90° C. (DSC second melt), a density of less than 0.92 g/cm3, and the densities of the first and second polymers differ by at least 1%. Specifically this invention relates to an in-reactor polymer blend comprising: (a) a first ethylene polymer comprising 90 to 100 wt % ethylene and from 0 to less than 10 wt % comonomer, said first ethylene polymer component having density of greater than 0.920 g/cm3, an Mw of 20,000 g/mol or more; and (b) a second ethylene polymer comprising from 70 to 90 wt % ethylene and 30 to 10 wt % comonomer, said second ethylene polymer having a density of 0.910 g/cm3 or less, wherein the polymer blend has: (a) a Tm of at least 100° C. over a density ranging from 0.84 to 0.92 g/cm3; (b) a elongation at break of 300% or more; (c) a strain hardening index M300/M100 of at least 1.2; (d) a ratio of complex viscosity at 0.01 rad/s to the viscosity at 100 rad/s is of at least 30; and (e) a shear thinning slope of the plot of log(dynamic viscosity) versus log(frequency) less than −0.2.
    • 本发明涉及一种反应器内聚合物共混物,其包含:(a)密度大于0.90g / cm 3,Mw大于20,000g / mol的第一含乙烯聚合物和(b)第二含乙烯的聚合物 聚合物的密度小于0.90g / cm 3,其中聚合物共混物具有至少90℃的Tm(DSC第二熔体),密度小于0.92g / cm 3,第一和第二密度 聚合物的差异至少为1%。 具体而言,本发明涉及一种反应器内聚合物共混物,其包含:(a)包含90至100重量%乙烯和0至小于10重量%共聚单体的第一乙烯聚合物,所述第一乙烯聚合物组分的密度大于0.920g / cm3,Mw为20,000g / mol以上; 和(b)包含70-90wt%乙烯和30-10wt%共聚单体的第二乙烯聚合物,所述第二乙烯聚合物的密度为0.910g / cm 3或更低,其中所述聚合物共混物具有:(a)Tm 至少100℃,密度范围为0.84至0.92g / cm 3; (b)断裂伸长率在300%以上; (c)至少为1.2的应变硬化指数M300 / M100; (d)0.01rad / s下的复数粘度与100rad / s下的粘度之比至少为30; 和(e)对数(动态粘度)对log(频率)小于-0.2的曲线的剪切变薄斜率。
    • 9. 发明授权
    • Thermoplastic elastomer polyolefin in-reactor blends and molded articles therefrom
    • 热塑性弹性体聚烯烃反应器内共混物及其模塑制品
    • US08101685B2
    • 2012-01-24
    • US12638916
    • 2009-12-15
    • Peijun JiangArmenag H. DekmezianKevin R. SquireCesar A. Garcia-Franco
    • Peijun JiangArmenag H. DekmezianKevin R. SquireCesar A. Garcia-Franco
    • C08F8/00C08L23/04C08L23/10
    • C08L23/06C08L23/08C08L2205/02C08L2314/06C08L2666/06
    • This invention relates to an in-reactor polymer blend comprising: (a) a first ethylene-containing polymer having a density of greater than 0.90 g/cm3 and a Mw of more than 20,000 g/mol and (b) a second ethylene-containing polymer having a density of less than 0.90 g/cm3, wherein the polymer blend has a Tm of at least 90° C. (DSC second melt), a density of less than 0.92 g/cm3, and the densities of the first and second polymers differ by at least 1%. Specifically this invention relates to an in-reactor polymer blend comprising: (a) a first ethylene polymer comprising 90 to 100 wt % ethylene and from 0 to less than 10 wt % comonomer, said first ethylene polymer component having density of greater than 0.920 g/cm3, an Mw of 20,000 g/mol or more; and (b) a second ethylene polymer comprising from 70 to 90 wt % ethylene and 30 to 10 wt % comonomer, said second ethylene polymer having a density of 0.910 g/cm3 or less, wherein the polymer blend has: (a) a Tm of at least 100° C. over a density ranging from 0.84 to 0.92 g/cm3; (b) a elongation at break of 300% or more; (c) a strain hardening index M300/M100 of at least 1.2; (d) a ratio of complex viscosity at 0.01 rad/s to the viscosity at 100 rad/s is of at least 30; and (e) a shear thinning slope of the plot of log(dynamic viscosity) versus log(frequency) less than −0.2.
    • 本发明涉及一种反应器内聚合物共混物,其包含:(a)密度大于0.90g / cm 3,Mw大于20,000g / mol的第一含乙烯聚合物和(b)第二含乙烯的聚合物 聚合物的密度小于0.90g / cm 3,其中聚合物共混物具有至少90℃的Tm(DSC第二熔体),密度小于0.92g / cm 3,第一和第二密度 聚合物的差异至少为1%。 具体而言,本发明涉及一种反应器内聚合物共混物,其包含:(a)包含90至100重量%乙烯和0至小于10重量%共聚单体的第一乙烯聚合物,所述第一乙烯聚合物组分的密度大于0.920g / cm3,Mw为20,000g / mol以上; 和(b)包含70-90wt%乙烯和30-10wt%共聚单体的第二乙烯聚合物,所述第二乙烯聚合物的密度为0.910g / cm 3或更低,其中所述聚合物共混物具有:(a)Tm 至少100℃,密度范围为0.84至0.92g / cm 3; (b)断裂伸长率在300%以上; (c)至少为1.2的应变硬化指数M300 / M100; (d)0.01rad / s下的复数粘度与100rad / s下的粘度之比至少为30; 和(e)对数(动态粘度)对log(频率)小于-0.2的曲线的剪切变薄斜率。