Process and system for recursive document retrieval
    31.
    发明授权
    Process and system for recursive document retrieval 失效
    递归文件检索的过程和系统

    公开(公告)号:US5787424A

    公开(公告)日:1998-07-28

    申请号:US565535

    申请日:1995-11-30

    IPC分类号: G06F17/30 G06F17/00

    摘要: A system (10) for recursive document retrieval is provided. An original repository (12) comprises a plurality of documents (14), and a query (16) comprises information by which the original repository (12) can be analyzed to identify relevant documents (14). A retrieval engine (18) is coupled to the original repository (12) and receives the query (16). The retrieval engine (18) is operable to execute an automatic recursive retrieval process with respect to the original repository (12) using the query (16) where the automatic recursive retrieval process comprises a plurality of iterations. The retrieval engine (18) is also operable to provide as system output a retrieved repository (28) comprising a plurality of documents (30) from the original repository (12) identified as sufficiently relevant to the query (16) according to the automatic recursive retrieval process for detection as relevant documents.

    摘要翻译: 提供了用于递归文档检索的系统(10)。 原始存储库(12)包括多个文档(14),并且查询(16)包括可以分析原始存储库(12)以识别相关文档(14)的信息。 检索引擎(18)耦合到原始存储库(12)并接收查询(16)。 检索引擎(18)可操作以使用查询(16)执行关于原始存储库(12)的自动递归检索处理,其中自动递归检索处理包括多个迭代。 检索引擎(18)还可操作以根据自动递归来提供从原始存储库(12)提供被识别为与查询(16)充分相关的多个文档(30)的检索的存储库(28) 检索过程作为相关文件进行检测。

    Method for reducing the temperature in a regeneration zone of a fluid
catalytic cracking process
    32.
    发明授权
    Method for reducing the temperature in a regeneration zone of a fluid catalytic cracking process 失效
    降低流化催化裂化过程再生区温度的方法

    公开(公告)号:US4859313A

    公开(公告)日:1989-08-22

    申请号:US896569

    申请日:1986-08-15

    IPC分类号: C10G11/18

    CPC分类号: C10G11/18

    摘要: A method for operating a fluid catalytic cracking unit comprising a regeneration zone and a reaction zone with a relatively reduced temperature in the regeneration zone while processing a hydrocarbon feedstock having a 50 volume percent distillation temperature greater than about 500.degree. F. which method comprises contacting the feedstock in a reaction zone with a mixture of regenerated fluidizable cracking catalyst and fluidizable low coke make solid particles comprising a refractory inorganic oxide in a ratio of low coke make solid particles to cracking catalyst from about 1:100 to about 10:1, the low coke made solid particles having a surface area of less than about 5 m.sup.2 /g and a coke making capability of less than about 0.2 weight percent coke on the spent low coke make solid particles in the ASTM standard method for testing cracking catalyst by microactivity test (MAT); separating the resulting vaporized hydrocarbon products from the mixture of deactivated fluidizable cracking catalyst and fluidizable low coke made solid particles; recovering the resulting vaporized hydrocarbon products; passing the mixture of cracking catalyst and low coke made solid particles to the regeneration zone for regeneration by removal of coke; and passing the resulting regenerated mixture of cracking catalyst and low coke make solid particles from the regeneration zone to the reaction zone to contact the feedstock as described above whereby the regeneration zone temperature is maintained at a reduced temperature as compared to an equivalent operation without the use of the fluidizable low coke make solid particles while simultaneously not affecting the operation of the reaction zone.

    摘要翻译: 一种用于操作流化催化裂化装置的方法,所述流化催化裂化装置包括再生区和在再生区中具有相对降低的温度的反应区,同时处理具有大于约500°F的50体积%蒸馏温度的烃原料。该方法包括使 在与可再生的可流化裂化催化剂和可流化的低焦炭的混合物的反应区中的原料使固体颗粒包含低焦度的难熔性无机氧化物,使固体颗粒与裂化催化剂的比例为约1:100至约10:1,低 焦炭制成的表面积小于约5m 2 / g的固体颗粒和焦炭制造能力小于约0.2重量%的焦炭在废低焦炭上制成固体颗粒,按照ASTM标准方法通过微活性试验测试裂化催化剂( 垫); 将所得蒸发的烃产物与可失活的可流化裂化催化剂和可流化的低焦炭固体颗粒的混合物分离; 回收所得蒸发的烃产物; 将裂解催化剂和低焦炭固体颗粒的混合物通过除去焦炭再生到再生区; 并将得到的裂解催化剂和低焦炭再生混合物从固体颗粒从再生区制成固体颗粒至反应区,以与上述原料接触,由此与无需使用的等效操作相比,再生区温度保持在降低的温度 的可流化的低焦炭制成固体颗粒,同时不影响反应区的操作。

    Fluid particle cooling process and apparatus
    33.
    发明授权
    Fluid particle cooling process and apparatus 失效
    流体颗粒冷却过程和装置

    公开(公告)号:US4434245A

    公开(公告)日:1984-02-28

    申请号:US413047

    申请日:1982-08-30

    摘要: A process and associated apparatus for the cooling of hot fluidized solid particles. The particles flow from a dense phase fluidized bed into the shell side of a vertically oriented shell and tube heat exchanger where cooling occurs via indirect heat exchange with a cooling media circulating in the tubes. The extent of cooling is controlled by the varying of the heat transfer coefficient between the tubes and particles in the heat exchanger which are maintained as a dense phase fluidized bed. The coefficient is varied by varying a combination of the variables comprising the quantity of fluidizing gas to the fluidized bed in the heat exchanger and the quantity of particle flow through that bed. The process has particular applicability to a combustive regeneration process and most particular applicability to the FCC process.

    摘要翻译: 一种用于冷却热流化固体颗粒的方法和相关设备。 颗粒从密相流化床流入垂直取向的壳管式热交换器的壳侧,其中冷却通过与在管中循环的冷却介质的间接热交换而发生。 冷却的程度通过保持为致密相流化床的热交换器中的管和颗粒之间的传热系数的变化来控制。 通过将包含流化气体的量的变量与热交换器中的流化床的变量和通过该床的颗粒流量的组合变化来改变系数。 该方法特别适用于燃烧再生过程以及对FCC方法的最特别的适用性。

    Fluid catalyst regeneration apparatus
    34.
    发明授权
    Fluid catalyst regeneration apparatus 失效
    流体催化剂再生装置

    公开(公告)号:US4424192A

    公开(公告)日:1984-01-03

    申请号:US389790

    申请日:1982-06-18

    摘要: A catalyst regeneration process and apparatus for the oxidative removal of coke from a coke contaminated fluid catalyst. The process comprises a high temperature coke combustion zone, a catalyst disengagement zone and an external heat removal zone comprising a shell and tube heat exchanger. Catalyst is cooled by passing it through the shell side of the heat exchanger with a cooling medium through the tube side. A mixture of coke contaminated catalyst, oxygen containing gas, and cool regenerated catalyst from the heat removal zone are contacted in the high temperature combustion zone, the temperature of which is controlled by adjusting the rate at which fluidizing gas is passed to the bottom portion of the shell of the heat exchanger which varies the degree of turbulence of the fluidized bed in the shell side and thus the heat transfer coefficient at the outside surface of the tubes which in turn varies the quantity of heat transferred to the cooling medium in the tubes.

    摘要翻译: 用于从焦炭污染的流体催化剂氧化除去焦炭的催化剂再生方法和装置。 该方法包括高温焦炭燃烧区,催化剂分离区和包括管壳式热交换器的外部除热区。 通过将冷却介质穿过管侧通过热交换器的外壳侧来冷却催化剂。 来自除热区域的焦炭污染催化剂,含氧气体和冷再生催化剂的混合物在高温燃烧区接触,其温度通过调节流化气体通过到底部的速率来控制 热交换器的壳体,其改变了壳侧中的流化床的湍流程度,因此改变了管的外表面处的传热系数,这又改变了传递到管中的冷却介质的热量。

    Catalyst regeneration process
    35.
    发明授权
    Catalyst regeneration process 失效
    催化剂再生过程

    公开(公告)号:US4197189A

    公开(公告)日:1980-04-08

    申请号:US908301

    申请日:1978-05-22

    摘要: A catalyst regeneration process and apparatus for the oxidation of coke from a spent catalyst, said coke being converted to CO, and for the conversion of the CO to CO.sub.2. Hot regenerated catalyst is recycled from a dense bed in the regeneration zone to mix with incoming spent catalyst in a riser-mixer. The riser-mixer operates in dense phase and is supplied with a relatively small amount of a fluidizing medium, preferably air. After the mixing of spent and fresh catalyst is substantially completed, a relatively large amount of a regenerating gas, preferably air, is admixed with the catalyst mixture, and some coke oxidation occurs. The balance of coke oxidation takes place in a downstream-situated regeneration zone of substantially conventional design. The regenerating gas addition is preferably made at the base of a cone-shaped combustor in order to provide a venturi effect which ensures good air-catalyst mixing.

    摘要翻译: 用于从废催化剂氧化焦炭的催化剂再生方法和装置,所述焦炭转化为CO,并将CO转化为CO 2。 热再生催化剂从再生区中的致密床再循环,与提升管混合器中的输入的废催化剂混合。 提升混合器以密相工作,并且供应相对少量的流化介质,优选空气。 在废旧催化剂的混合基本上完成之后,将相当大量的再生气体,优选空气与催化剂混合物混合,并发生一些焦炭氧化。 焦炭氧化的平衡发生在基本上常规设计的位于下游的再生区中。 再生气体添加优选在锥形燃烧器的基部制成,以提供确保良好的空气 - 催化剂混合的文氏管效应。

    Gas distribution apparatus for use with fluidized beds
    36.
    发明授权
    Gas distribution apparatus for use with fluidized beds 失效
    用于流化床的气体分配设备

    公开(公告)号:US4170626A

    公开(公告)日:1979-10-09

    申请号:US922461

    申请日:1978-07-06

    IPC分类号: B01J8/44 B01J8/18 B01J8/00

    CPC分类号: B01J8/1818

    摘要: Apparatus for distributing the flow of gas, usually air, in a fluidized bed includes a plurality of vertically upstanding distributor members extending upwardly from a manifold member to which they are threadedly engaged. The members are of closed end, generally tubular shape and have a helical slotted opening extending along their length. The width of the slotted openings is less than the diameter of the majority of particles utilized in the associated fluidized bed.

    摘要翻译: 用于将气体流(通常为空气)分配在流化床中的装置包括从歧管构件向上延伸的多个垂直竖立的分配器构件,它们与它们相啮合。 这些构件是封闭端的,大致为管状,并且具有沿其长度延伸的螺旋形槽口。 开槽开口的宽度小于在相关流化床中使用的大部分颗粒的直径。

    Fiber-containing composite and method for making the same
    38.
    发明授权
    Fiber-containing composite and method for making the same 有权
    含纤维复合材料及其制造方法

    公开(公告)号:US07651964B2

    公开(公告)日:2010-01-26

    申请号:US11205688

    申请日:2005-08-17

    IPC分类号: D04H1/00 B32B5/24

    摘要: A unitary, fiber-containing composite comprises (a) a first region comprising a plurality of first binder fibers and a plurality of bast fibers, (b) a second region disposed above the first region, the second region comprising a plurality of second binder fibers and a plurality of bast fibers, and (c) a transitional region disposed between the first region and the second region. The transitional region comprises concentrations of the first binder fiber, the second binder fiber, and the bast fiber. The concentration of the first binder fiber in the first transitional region is greatest proximate to the first region and least proximate to the second region, and the concentration of the second binder fiber and the bast fiber in the first transitional region is greatest proximate to the second region and least proximate to the first region. A method for producing a unitary, fiber-containing composite is also described.

    摘要翻译: 单一的含纤维复合材料包括(a)包含多个第一粘合纤维和多个韧皮纤维的第一区域,(b)设置在第一区域上方的第二区域,第二区域包括多个第二粘合纤维 和多个韧皮纤维,(c)设置在第一区域和第二区域之间的过渡区域。 过渡区域包括第一粘合纤维,第二粘合纤维和韧皮纤维的浓度。 第一过渡区域中的第一粘合纤维的浓度最接近于第一区域并且最接近于第二区域,并且第一过渡区域中的第二粘合纤维和韧皮纤维的浓度最接近于第二区域 区域并且最靠近第一区域。 还描述了用于生产单一的含纤维复合材料的方法。

    VOC-absorbing nonwoven composites
    40.
    发明申请
    VOC-absorbing nonwoven composites 失效
    吸收VOC的非织造复合材料

    公开(公告)号:US20080153375A1

    公开(公告)日:2008-06-26

    申请号:US11890214

    申请日:2007-08-03

    IPC分类号: D04H13/00 B29C65/10 B29C70/44

    摘要: A nonwoven composite has a first surface, a second surface, and a thickness extending between the first and second surfaces. The nonwoven composite comprises a plurality of natural fibers, a plurality of binder fibers, and a VOC-absorbing material. The binder fibers are bonded to or interlocked with the natural fibers. The VOC-absorbing material is dispersed within the nonwoven composite in such a manner that the density of the VOC-absorbing material in the nonwoven composite is greatest adjacent to the second surface of the nonwoven composite. A method for producing a nonwoven composite is also described.

    摘要翻译: 非织造复合材料具有第一表面,第二表面和在第一和第二表面之间延伸的厚度。 非织造复合材料包括多种天然纤维,多种粘合纤维和VOC吸收材料。 粘合剂纤维与天然纤维结合或互锁。 吸收VOC的材料以非织造复合材料中的VOC吸收材料的密度与非织造复合材料的第二表面相邻最大的方式分散在非织造复合材料中。 还描述了一种生产非织造复合材料的方法。