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    • 3. 发明授权
    • Magnetic particle integrated adhesive and associated method of repairing
a composite material product
    • 磁性颗粒一体化粘合剂及相关方法修复复合材料制品
    • US5833795A
    • 1998-11-10
    • US718192
    • 1996-09-19
    • Michael Roy SmithKevin Dale Walters
    • Michael Roy SmithKevin Dale Walters
    • B29C35/08B29C65/36B29C73/02B29C73/32C09J5/06C09J9/00C09J11/04B32B31/28
    • B64F5/0081B29C65/3612B29C66/91221B29C66/91411B29C66/91431B29C66/91641B29C73/02C09J11/04C09J5/06C09J9/00B29C2035/0811B29C2035/0855B29C66/5326B29C66/71B29C66/7212B29C66/7392B29C66/7394B29C66/961B29C73/32B29K2063/00B29L2031/3085
    • A method of repairing a composite material product by adhering a repair patch to the composite material product with an adhesive or epoxy resin that includes magnetic particles. Thus, the adhesive or epoxy resin can be cured by electromagnetically exciting the magnetic particles, such as by microwave heating. The electromagnetically excited magnetic particles internally heat the adhesive or epoxy resin to the predetermined Curie Point temperature of the magnetic particles such that the adhesive or epoxy resin cures in a uniform and inspectable fashion. The magnetic particles can be mixed into an adhesive, such as a paste adhesive, a film adhesive or a foam adhesive, to create a magnetic particle integrated adhesive. The magnetic particle integrated adhesive can then be applied between a precured repair patch and the underlying composite material product. Alternatively, the magnetic particles can be distributed within the organic resin of an uncured repair patch such that the repair patch can be simultaneously cured and adhered to the composite material product by electromagnetically exciting the magnetic particles. In either embodiment, the adhesive or the epoxy resin is adapted to cure within a predetermined range of cure temperatures. Thus, the magnetic particles, such as Ferrous Silicide, should have a predetermined Curie Point temperature within the predetermined range of cure temperatures.
    • 一种通过用包括磁性颗粒的粘合剂或环氧树脂将修复贴片粘附到复合材料产品上来修复复合材料产品的方法。 因此,粘合剂或环氧树脂可以通过电磁激励磁性颗粒例如通过微波加热来固化。 电磁激发的磁性颗粒将粘合剂或环氧树脂内部加热到磁性颗粒的预定居里点温度,使得粘合剂或环氧树脂以均匀且可检查的方式固化。 磁性颗粒可以混合成粘合剂,例如糊状粘合剂,薄膜粘合剂或泡沫粘合剂,以产生磁性颗粒整合的粘合剂。 然后可以将磁性颗粒整合的粘合剂施加在预固化的修补贴片和下面的复合材料产品之间。 或者,磁性颗粒可以分布在未固化的修补贴片的有机树脂内,使得修复贴片可以通过电磁激励磁性颗粒同时固化并粘附到复合材料产品上。 在任一实施方案中,粘合剂或环氧树脂适于在预定固化温度范围内固化。 因此,诸如硫化亚铁之类的磁性颗粒在预定的固化温度范围内应具有预定的居里点温度。
    • 4. 发明授权
    • Hydrocarbon conversion process to decrease polyaromatics
    • 烃转化过程减少多芳族化合物
    • US07794588B2
    • 2010-09-14
    • US11872140
    • 2007-10-15
    • Peter KokayeffLaura Elise LeonardMichael Roy Smith
    • Peter KokayeffLaura Elise LeonardMichael Roy Smith
    • C10G45/44C10G65/02
    • C10G65/12C10G2400/04
    • A process is provided for producing low sulfur diesel having a reduced poly-aromatic level where at least a portion of the poly-aromatics are converted to mono-aromatics. In one aspect, the process separates the temperature and pressure requirements for obtaining low levels of sulfur from the temperature and pressure requirements to saturate poly-aromatics to mono-aromatics. By one approach, the process first converts a diesel boiling range hydrocarbon stream in a hydrotreating zone at conditions effective to produce a hydrotreating zone effluent having a reduced concentration of sulfur with minimal saturation of poly-aromatics. Hydrogen is then admixed in the hydrotreating zone effluent or at least a portion thereof, which is then reacted in a substantially liquid-phase continuous reaction zone to effect saturation of poly-aromatics to provide a liquid-phase continuous reaction zone effluent having a reduced level of poly-aromatics relative to the diesel feed.
    • 提供了一种制备具有降低的聚芳族水平的低硫柴油的方法,其中至少一部分多芳族化合物转化为单芳族化合物。 在一个方面,该方法将温度和压力要求从温度和压力要求中分离出来以获得低水平的硫,从而将多芳族化合物饱和至单芳族化合物。 通过一种方法,该方法首先将加氢处理区中的柴油沸程烃流转化成有效地产生具有降低的硫浓度并且具有最小的多芳族化合物饱和度的加氢处理区流出物的条件。 然后将氢混合在加氢处理区流出物或其至少一部分中,然后将其在基本上液相的连续反应区中反应以实现多芳族化合物的饱和,以提供具有降低水平的液相连续反应区流出物 的多芳烃相对于柴油进料。
    • 5. 发明授权
    • Hydrocarbon conversion process
    • 烃转化过程
    • US07794585B2
    • 2010-09-14
    • US11872084
    • 2007-10-15
    • Laura Elise LeonardPeter KokayeffMichael Roy Smith
    • Laura Elise LeonardPeter KokayeffMichael Roy Smith
    • C10G65/02
    • C10G65/12
    • Methods of hydroprocessing hydrocarbon streams are provided that employ substantially liquid-phase hydroprocessing conditions. In one aspect, the method includes directing a hydrocarbonaceous feed stock to a first substantially liquid-phase hydroprocessing zone wherein an effluent from the first substantially liquid-phase hydroprocessing zone is directed to a second substantially liquid-phase hydroprocessing zone generally undiluted with other hydrocarbon streams. In another aspect, the method recycles a liquid portion of a liquid hydrocarbonaceous effluent from the second substantially liquid-phase hydroprocessing zone, which preferably includes an amount of hydrogen dissolved therein, to the hydrocarbonaceous feed stock so that the feed to the first substantially liquid-phase hydroprocessing zone has a relatively larger concentration of dissolved hydrogen relative to the hydrocarbonaceous feed stock.
    • 提供加氢处理烃流的方法,其采用基本上液相加氢处理条件。 一方面,该方法包括将烃类原料引导至第一基本上液相加氢处理区,其中来自第一基本上液相加氢处理区的流出物被引导至通常未与其它烃流稀释的第二基本上液相加氢处理区 。 在另一方面,该方法将来自第二基本上液相加氢处理区的液体烃流出物的液体部分再循环到烃原料中,所述第二基本液相加氢处理区优选包含一定量的溶解在其中的氢, 相加氢处理区相对于含烃原料具有相对较大的溶解氢浓度。
    • 6. 发明申请
    • Hydrocarbon Conversion Process To Decrease Polyaromatics
    • 烃转化过程降低多元芳烃
    • US20090095652A1
    • 2009-04-16
    • US11872140
    • 2007-10-15
    • Peter KokayeffLaura Elise LeonardMichael Roy Smith
    • Peter KokayeffLaura Elise LeonardMichael Roy Smith
    • C10G69/02
    • C10G65/12C10G2400/04
    • A process is provided for producing low sulfur diesel having a reduced poly-aromatic level where at least a portion of the poly-aromatics are converted to mono-aromatics. In one aspect, the process separates the temperature and pressure requirements for obtaining low levels of sulfur from the temperature and pressure requirements to saturate poly-aromatics to mono-aromatics. By one approach, the process first converts a diesel boiling range hydrocarbon stream in a hydrotreating zone at conditions effective to produce a hydrotreating zone effluent having a reduced concentration of sulfur with minimal saturation of poly-aromatics. Hydrogen is then admixed in the hydrotreating zone effluent or at least a portion thereof, which is then reacted in a substantially liquid-phase continuous reaction zone to effect saturation of poly-aromatics to provide a liquid-phase continuous reaction zone effluent having a reduced level of poly-aromatics relative to the diesel feed.
    • 提供了一种制备具有降低的聚芳族水平的低硫柴油的方法,其中至少一部分多芳族化合物转化为单芳族化合物。 在一个方面,该方法将温度和压力要求从温度和压力要求中分离出来以获得低水平的硫,从而将多芳族化合物饱和至单芳族化合物。 通过一种方法,该方法首先将加氢处理区中的柴油沸程烃流转化成有效地产生具有降低的硫浓度并且具有最小的多芳族化合物饱和度的加氢处理区流出物的条件。 然后将氢混合在加氢处理区流出物或其至少一部分中,然后将其在基本上液相的连续反应区中反应以实现多芳族化合物的饱和,以提供具有降低水平的液相连续反应区流出物 的多芳烃相对于柴油进料。
    • 8. 发明授权
    • Hydrocarbon conversion process to improve cetane number
    • 烃转化过程提高十六烷值
    • US07790020B2
    • 2010-09-07
    • US11872102
    • 2007-10-15
    • Peter KokayeffLaura Elise LeonardMichael Roy Smith
    • Peter KokayeffLaura Elise LeonardMichael Roy Smith
    • C10G45/44C10G65/02
    • C10G45/02C10G2400/04
    • A process is provided for producing low sulfur diesel having a high cetane number where the temperature and pressure requirements for obtaining low levels of sulfur is separated from the temperature and pressure requirements for improving cetane. In one aspect, a low pressure hydrodesulfurization zone and a high pressure aromatic saturation zone are employed to sequentially achieve the desired sulfur and cetane levels. In another aspect, the process first converts a diesel boiling range hydrocarbonaceous stream in a hydrotreating zone at conditions effective to produce a hydrotreating zone effluent having a reduced concentration of sulfur with minimal saturation of aromatics. Hydrogen is then admixed with the hydrotreating zone effluent, which is then reacted in a substantially liquid-phase continuous reaction zone substantially undiluted with other streams to effect saturation of aromatics to provide a liquid-phase continuous reaction zone effluent having an improved cetane number.
    • 提供了一种生产具有高十六烷值的低硫柴油的方法,其中获得低水平硫的温度和压力要求与用于改善十六烷的温度和压力要求分离。 一方面,使用低压加氢脱硫区和高压芳族饱和区来顺序地获得所需的硫和十六烷值。 在另一方面,该方法首先在加氢处理区中转化柴油沸程烃流,其条件是有效地产生具有降低的硫浓度并且具有最小芳烃饱和度的加氢处理区流出物。 然后将氢气与加氢处理区流出物混合,然后将其在基本上液相连续的反应区中与基本上未稀释的其它流反应,以实现芳族化合物的饱和,以提供具有改进的十六烷值的液相连续反应区流出物。
    • 9. 发明申请
    • Hydrocarbon Conversion Process To Improve Cetane Number
    • 碳氢转化方法提高十六烷值
    • US20090095656A1
    • 2009-04-16
    • US11872102
    • 2007-10-15
    • Peter KokayeffLaura Elise LeonardMichael Roy Smith
    • Peter KokayeffLaura Elise LeonardMichael Roy Smith
    • C10G69/02
    • C10G45/02C10G2400/04
    • A process is provided for producing low sulfur diesel having a high cetane number where the temperature and pressure requirements for obtaining low levels of sulfur is separated from the temperature and pressure requirements for improving cetane. In one aspect, a low pressure hydrodesulfurization zone and a high pressure aromatic saturation zone are employed to sequentially achieve the desired sulfur and cetane levels. In another aspect, the process first converts a diesel boiling range hydrocarbonaceous stream in a hydrotreating zone at conditions effective to produce a hydrotreating zone effluent having a reduced concentration of sulfur with minimal saturation of aromatics. Hydrogen is then admixed with the hydrotreating zone effluent, which is then reacted in a substantially liquid-phase continuous reaction zone substantially undiluted with other streams to effect saturation of aromatics to provide a liquid-phase continuous reaction zone effluent having an improved cetane number.
    • 提供了一种生产具有高十六烷值的低硫柴油的方法,其中获得低水平硫的温度和压力要求与用于改善十六烷的温度和压力要求分离。 一方面,使用低压加氢脱硫区和高压芳族饱和区来顺序地获得所需的硫和十六烷值。 在另一方面,该方法首先在加氢处理区中转化柴油沸程烃流,其条件是有效地产生具有降低的硫浓度并且具有最小芳烃饱和度的加氢处理区流出物。 然后将氢气与加氢处理区流出物混合,然后将其在基本上液相连续的反应区中与基本上未稀释的其它流反应,以实现芳族化合物的饱和,以提供具有改进的十六烷值的液相连续反应区流出物。
    • 10. 发明申请
    • Hydrocarbon Conversion Process
    • 烃转化过程
    • US20090095651A1
    • 2009-04-16
    • US11872084
    • 2007-10-15
    • Laura Elise LeonardPeter KokayeffMichael Roy Smith
    • Laura Elise LeonardPeter KokayeffMichael Roy Smith
    • C10G65/02
    • C10G65/12
    • Methods of hydroprocessing hydrocarbon streams are provided that employ substantially liquid-phase hydroprocessing conditions. In one aspect, the method includes directing a hydrocarbonaceous feed stock to a first substantially liquid-phase hydroprocessing zone wherein an effluent from the first substantially liquid-phase hydroprocessing zone is directed to a second substantially liquid-phase hydroprocessing zone generally undiluted with other hydrocarbon streams. In another aspect, the method recycles a liquid portion of a liquid hydrocarbonaceous effluent from the second substantially liquid-phase hydroprocessing zone, which preferably includes an amount of hydrogen dissolved therein, to the hydrocarbonaceous feed stock so that the feed to the first substantially liquid-phase hydroprocessing zone has a relatively larger concentration of dissolved hydrogen relative to the hydrocarbonaceous feed stock.
    • 提供加氢处理烃流的方法,其采用基本上液相加氢处理条件。 一方面,该方法包括将烃类原料引导至第一基本上液相加氢处理区,其中来自第一基本上液相加氢处理区的流出物被引导至通常未与其它烃流稀释的第二基本上液相加氢处理区 。 在另一方面,该方法将来自第二基本上液相加氢处理区的液体烃流出物的液体部分再循环到烃原料中,所述第二基本液相加氢处理区优选包含一定量的溶解在其中的氢, 相加氢处理区相对于含烃原料具有相对较大的溶解氢浓度。