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    • 1. 发明授权
    • Method for converting waste plastic to lower-molecular weight hydrocarbons, particularly hydrocarbon fuel materials, and the hydrocarbon material produced thereby
    • 将废塑料转化为低分子量烃,特别是烃燃料材料的方法以及由此生产的烃材料
    • US08927797B2
    • 2015-01-06
    • US13019725
    • 2011-02-02
    • Moinuddin Sarker
    • Moinuddin Sarker
    • C10G1/10
    • C10G1/10C10L1/04C10L2200/0461C10L2270/023C10L2270/026C10L2290/543C10L2290/547
    • The method produces a hydrocarbonaceous fluid (a liquid mixture of hydrocarbons, or in other words a mixture of hydrocarbons which is liquid at ambient room temperature and atmospheric pressure), which functionally is a liquid hydrocarbon fuel, from a feed of waste plastic. The method can comprise the steps of: (step 1) melting a feed of substantially solid waste plastic in an aerobic atmosphere (for instance, air) whereby a waste-plastic melt is produced; (step 2) distilling at least a portion of the waste-plastic melt whereby a hydrocarbonaceous distillate is produced; and (step 3) collecting the hydrocarbonaceous distillate. That distillate is generally referred to above as a condensate. The method can include the step of comminuting the feed of substantially solid waste plastic into pieces substantially no greater than about 1.5 cm2 prior to step 1. The method can also include the step of adding an effective amount of a cracking catalyst to the waste plastic prior to step 2.
    • 该方法从废塑料的进料产生烃流体(烃的液体混合物,或换句话说是在室温和大气压下为液体的烃的混合物),其功能上是液体烃燃料。 该方法可以包括以下步骤:(步骤1)在有氧气氛(例如空气)中熔化基本上固体废塑料的进料,由此产生废塑料熔体; (步骤2)蒸馏至少一部分废塑料熔体,由此产生含烃馏出物; 和(步骤3)收集含烃馏出物。 该馏出物通常称为冷凝物。 该方法可以包括在步骤1之前将基本上固体废塑料的进料粉碎成几乎不大于约1.5cm 2的步骤。该方法还可以包括以下步骤:将有效量的裂化催化剂加入废塑料中 到步骤2。
    • 2. 发明申请
    • METHODS AND SYSTEMS FOR CONVERTING PLASTIC TO FUEL
    • 将塑料转化为燃料的方法和系统
    • US20130118885A1
    • 2013-05-16
    • US13671484
    • 2012-11-07
    • Moinuddin Sarker
    • Moinuddin Sarker
    • C10B53/07
    • C10B53/07C10B47/18C10G1/10Y02P20/143
    • A method for producing a vapor stream from waste plastic comprises providing a waste plastic feedstock into a reactor containing one or more residues produced from a previously heated source of waste plastic, and heating the waste plastic feedstock in the reactor to a temperature from about 125° C. to 500° C. to generate a vapor containing one or more hydrocarbons. The waste plastic feedstock can be heated in the reactor without any added external catalyst. The waste plastic feedstock can have a calcium to sodium mass ratio from about 0.0001 to 400 as measured by inductively-coupled plasma (ICP) spectrometry. The catalytic activity in the reactor may be provided through one or more constituent elements in the waste plastic feedstock or the one or more residues produced from the previously heated source of waste plastic.
    • 用于从废塑料制造蒸汽流的方法包括将废塑料原料提供到含有由先前加热的废塑料源产生的一种或多种残余物的反应器中,并将反应器中的废塑料原料加热至约125℃ 在500℃下生成含有一种或多种烃的蒸气。 废塑料原料可以在反应器中加热,无需任何添加的外部催化剂。 通过电感耦合等离子体(ICP)光谱测定,废塑料原料可以具有约0.0001至400的钙与钠质量比。 反应器中的催化活性可以通过废塑料原料中的一种或多种构成元素或由先前加热的废塑料源生产的一种或多种残余物提供。
    • 3. 发明申请
    • Method for Converting Waste Plastic to Lower-Molecular Weight Hydrocarbons, Particularly Hydrocarbon Fuel Materials, and the Hydrocarbon Material Produced Thereby
    • 将废塑料转化为低分子量烃,特别是烃燃料材料的方法和由此生产的烃材料
    • US20090299110A1
    • 2009-12-03
    • US12471717
    • 2009-05-26
    • Moinuddin Sarker
    • Moinuddin Sarker
    • C10L1/04C10G55/00
    • C10G1/10C10L1/04C10L2200/0461C10L2270/023C10L2270/026C10L2290/543C10L2290/547
    • A method produces a hydrocarbonaceous fluid (a liquid mixture of hydrocarbons, or in other words a mixture of hydrocarbons which is liquid at ambient room temperature and atmospheric pressure), which functionally is a liquid hydrocarbon fuel, from a feed of waste plastic. The method comprises in broad embodiments the steps of: (step 1) melting a feed of substantially solid waste plastic in an aerobic atmosphere (for instance, air) whereby a waste-plastic melt is produced; (step 2) distilling at least a portion of the waste-plastic melt whereby a hydrocarbonaceous distillate is produced; and (step 3) collecting the hydrocarbonaceous distillate. That distillate is generally referred to above as a condensate. In some preferred embodiments, the method includes the step of commutating the feed of substantially solid waste plastic into pieces substantially no greater than about 1.5 cm2 prior to step 1. In preferred embodiments, the method includes the step of adding an effective amount of a cracking catalyst to the waste plastic prior to step 2.
    • 方法从废塑料的进料中产生烃流体(烃的液体混合物,或换句话说是在室温和大气压下为液体的烃的混合物),功能上是液体烃燃料。 该方法在广泛的实施方案中包括以下步骤:(步骤1)在有氧气氛(例如空气)中熔化基本上固体废塑料的进料,由此产生废塑料熔体; (步骤2)蒸馏至少一部分废塑料熔体,由此产生含烃馏出物; 和(步骤3)收集含烃馏出物。 该馏出物通常称为冷凝物。 在一些优选的实施方案中,该方法包括在步骤1之前将基本上固体的废塑料的进料换成基本不大于约1.5cm 2的片的步骤。在优选的实施方案中,该方法包括以下步骤:加入有效量的裂化 在步骤2之前对废塑料的催化剂。
    • 4. 发明申请
    • METHOD FOR CONVERTING WASTE PLASTIC TO LOWER-MOLECULAR WEIGHT HYDROCARBONS, PARTICULARLY HYDROCARBON FUEL MATERIALS, AND THE HYDROCARBON MATERIAL PRODUCED THEREBY
    • 将废塑料转化为较低分子量烃,特别是烃类燃料材料的方法,以及生产的碳氢化合物
    • US20110124932A1
    • 2011-05-26
    • US13019725
    • 2011-02-02
    • Moinuddin Sarker
    • Moinuddin Sarker
    • C10G99/00
    • C10G1/10C10L1/04C10L2200/0461C10L2270/023C10L2270/026C10L2290/543C10L2290/547
    • A method produces a hydrocarbonaceous fluid (a liquid mixture of hydrocarbons, or in other words a mixture of hydrocarbons which is liquid at ambient room temperature and atmospheric pressure), which functionally is a liquid hydrocarbon fuel, from a feed of waste plastic. The method comprises in broad embodiments the steps of: (step 1) melting a feed of substantially solid waste plastic in an aerobic atmosphere (for instance, air) whereby a waste-plastic melt is produced; (step 2) distilling at least a portion of the waste-plastic melt whereby a hydrocarbonaceous distillate is produced; and (step 3) collecting the hydrocarbonaceous distillate. That distillate is generally referred to above as a condensate. In some preferred embodiments, the method includes the step of commutating the feed of substantially solid waste plastic into pieces substantially no greater than about 1.5 cm2 prior to step 1. In preferred embodiments, the method includes the step of adding an effective amount of a cracking catalyst to the waste plastic prior to step 2.
    • 方法从废塑料的进料中产生烃流体(烃的液体混合物,或换句话说是在室温和大气压下为液体的烃的混合物),功能上是液体烃燃料。 该方法在广泛的实施方案中包括以下步骤:(步骤1)在有氧气氛(例如空气)中熔化基本上固体废塑料的进料,由此产生废塑料熔体; (步骤2)蒸馏至少一部分废塑料熔体,由此产生含烃馏出物; 和(步骤3)收集含烃馏出物。 该馏出物通常称为冷凝物。 在一些优选的实施方案中,该方法包括在步骤1之前将基本上固体的废塑料的进料换成基本不大于约1.5cm 2的片的步骤。在优选的实施方案中,该方法包括以下步骤:加入有效量的裂化 在步骤2之前对废塑料的催化剂。