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    • 1. 发明授权
    • Heat-seal resin and package formed therefrom
    • 热封树脂和由此形成的包装
    • US08173748B1
    • 2012-05-08
    • US12972035
    • 2010-12-17
    • David John LohseThomas Tungshi SunAspy K. MehtaGabor KissRobert Patrick Reynolds, Jr.John W. ChuManika Varma-Nair
    • David John LohseThomas Tungshi SunAspy K. MehtaGabor KissRobert Patrick Reynolds, Jr.John W. ChuManika Varma-Nair
    • C08F8/00C08L23/00C08L23/04C08L23/10
    • C08L23/142C08L2205/025
    • Provided is a heat-seal resin. The resin includes 5 wt % to 95 wt % of a first copolymer and 95 wt % to 5 wt % of a second copolymer based on the total weight of the resin. The first copolymer and the second copolymer together are 90 wt % or more of the total weight of the resin. The first copolymer includes a first monomer of an alphaolefin of 2 to 4 carbon atoms and a second monomer selected from a second monomer of an alphaolefin of 2 to 8 carbon atoms. The first monomer and the second monomer of the first copolymer are different. The first copolymer has an MFR of from 5 to 1000 g/10 minutes and a Tfm of 66° C. to 80° C. The second copolymer includes a first monomer of an alphaolefin of 2 to 4 carbon atoms and a second monomer selected from a second monomer of an alphaolefin of 2 to 8 carbon atoms. The first monomer and the second monomer of the second copolymer are different. The second copolymer has an MFR of from 0.5 to 5 g/10 minutes and a Tfm of 45° C. to 66° C., wherein the first copolymer has an MFR of at least 2 g/10 minutes greater and a Tfm of at least 10° C. greater than the second copolymer. There is also a package formed partly or entirely of the resin.
    • 提供一种热封树脂。 基于树脂的总重量,树脂包含5重量%至95重量%的第一共聚物和95重量%至5重量%的第二共聚物。 第一共聚物和第二共聚物一起是树脂总重量的90重量%以上。 第一共聚物包括2至4个碳原子的α-烯烃的第一单体和选自2至8个碳原子的α-烯烃的第二单体的第二单体。 第一共聚物的第一单体和第二单体是不同的。 第一共聚物的MFR为5至1000g / 10分钟,Tfm为66℃至80℃。第二共聚物包括第一单体,其具有2至4个碳原子的α-烯烃,第二单体选自 2至8个碳原子的α-烯烃的第二单体。 第二共聚物的第一单体和第二单体是不同的。 第二共聚物的MFR为0.5〜5g / 10分钟,Tfm为45〜66℃,其中第一共聚物的MFR为2g / 10分钟以上, 比第二共聚物大至少10℃。 还有一部分或全部由树脂形成的包装。
    • 6. 发明申请
    • Polypropylene ethylene-propylene copolymer blends and in-line process t produce them
    • 聚丙烯乙烯 - 丙烯共聚物共混物和在线工艺生产它们
    • US20090163643A1
    • 2009-06-25
    • US12317045
    • 2008-12-18
    • Gabor KissPatrick BrantRobert Partick Reynolds, JR.Aspy K. MehtaManika Varma-NairJohn W. ChuSteven P. Rucker
    • Gabor KissPatrick BrantRobert Partick Reynolds, JR.Aspy K. MehtaManika Varma-NairJohn W. ChuSteven P. Rucker
    • C08L23/16C08L23/12C08F2/01
    • C08L23/0815C08F110/06C08F210/06C08L23/10C08L2314/02C08L2314/06Y02P20/544C08L2666/06C08F2500/12C08F2500/20C08F2500/03C08F210/16
    • Isotactic polypropylene ethylene-propylene copolymer blends and in-line processes for producing them. The blend of polypropylene and ethylene-propylene copolymer may have between 1 and 50 wt % of isotactic polypropylene with a melt flow rate of between 0.5 and 20,000 g/10 min and a melting peak temperature of 145° C. or higher, and wherein the difference between the DSC peak melting and the peak crystallization temperatures is less than or equal to 0.5333 times the melting peak temperature minus 41.333° C., and between 50 and 99 wt % of ethylene-propylene copolymer including between 10 wt % and 20 wt % randomly distributed ethylene with a melt flow rate of between 0.5 and 20,000 g/10 min, wherein the copolymer is polymerized by a bulk homogeneous polymerization process, and wherein the total regio defects in the continuous propylene segments of the copolymer is between 40 and 150% greater than a copolymer of equivalent melt flow rate and wt % ethylene polymerized by a solution polymerization process. The in-line process for producing the blend includes providing two or more parallel reactor trains and a separator for product blending and product-feed separation; wherein the two or more reactor trains operate under fluid phase bulk homogeneous conditions and at least one of the trains operates under supercritical conditions.
    • 全同立构聚丙烯乙烯 - 丙烯共聚物共混物和在线生产方法。 聚丙烯和乙烯 - 丙烯共聚物的共混物可以具有1至50重量%的全同立构聚丙烯,熔体流动速率在0.5至20,000g / 10min之间,熔融峰温度为145℃或更高,其中 DSC峰值熔融和峰值结晶温度之间的差异小于或等于熔融峰值温度减去41.333℃的0.5333倍,和包含10重量%至20重量%之间的乙烯 - 丙烯共聚物的50至99重量% 熔体流动速率为0.5至20,000g / 10min的随机分布的乙烯,其中共聚物通过本体均相聚合方法聚合,并且其中共聚物的连续丙烯链段中的总区域缺陷为40-150% 大于通过溶液聚合方法聚合的当量熔体流动速率和wt%乙烯的共聚物。 用于生产共混物的在线方法包括提供两个或更多个平行的反应器列和用于产物共混和产物进料分离的分离器; 其中所述两个或多个反应器列车在流体相体积均匀条件下操作,并且所述列车中的至少一个在超临界条件下操作。