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公开(公告)号：US07622620B2
公开(公告)日：2009-11-24
申请号：US11615254
申请日：2006-12-22
IPC分类号： C10G65/02
CPC分类号： C10G29/205 , C10G11/10 , C10G11/16 , C10G35/12 , C10G49/002 , C10G49/14 , C10G51/026 , C10G59/02 , C10G65/02
摘要： One exemplary embodiment can include a hydrocarbon conversion process. Generally, the process includes passing a hydrocarbon stream through a hydrocarbon conversion zone comprising a series of reaction zones. Typically, the hydrocarbon conversion zone includes a staggered-bypass reaction system having a first, second, third, and fourth reaction zones, which are staggered-bypass reaction zones, and a fifth reaction zone, which can be a non-staggered-bypass reaction zone, subsequent to the staggered-bypass reaction system.
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22.发明申请公开(公告)号：US20090054712A1
公开(公告)日：2009-02-26
申请号：US12260312
申请日：2008-10-29
IPC分类号： C07C2/00
CPC分类号： C10G29/205 , C10G11/10 , C10G11/16 , C10G35/12 , C10G49/002 , C10G49/14 , C10G51/026 , C10G59/02 , C10G65/02
摘要： One exemplary embodiment can include a hydrocarbon conversion process. Generally, the process includes passing a hydrocarbon stream through a hydrocarbon conversion zone comprising a series of reaction zones. Typically, the hydrocarbon conversion zone includes a staggered-bypass reaction system having a first, second, third, and fourth reaction zones, which are staggered-bypass reaction zones, and a fifth reaction zone, which can be a non-staggered-bypass reaction zone, subsequent to the staggered-bypass reaction system.
摘要翻译： 一个示例性实施方案可以包括烃转化方法。 通常，该方法包括使烃流通过包含一系列反应区的烃转化区。 通常，烃转化区包括具有交错旁路反应区的第一，第二，第三和第四反应区的交错旁路反应系统，以及可以是非交错旁路反应的第五反应区 在交错旁路反应系统之后。
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23.发明申请公开(公告)号：US20080154076A1
公开(公告)日：2008-06-26
申请号：US11615254
申请日：2006-12-22
IPC分类号： C10G65/02
CPC分类号： C10G29/205 , C10G11/10 , C10G11/16 , C10G35/12 , C10G49/002 , C10G49/14 , C10G51/026 , C10G59/02 , C10G65/02
摘要： One exemplary embodiment can include a hydrocarbon conversion process. Generally, the process includes passing a hydrocarbon stream through a hydrocarbon conversion zone comprising a series of reaction zones. Typically, the hydrocarbon conversion zone includes a staggered-bypass reaction system having a first, second, third, and fourth reaction zones, which are staggered-bypass reaction zones, and a fifth reaction zone, which can be a non-staggered-bypass reaction zone, subsequent to the staggered-bypass reaction system.
摘要翻译： 一个示例性实施方案可以包括烃转化方法。 通常，该方法包括使烃流通过包含一系列反应区的烃转化区。 通常，烃转化区包括具有交错旁路反应区的第一，第二，第三和第四反应区的交错旁路反应系统，以及可以是非交错旁路反应的第五反应区 在交错旁路反应系统之后。
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公开(公告)号：US5613622A
公开(公告)日：1997-03-25
申请号：US490079
申请日：1995-06-13
CPC分类号： B65D90/046 , B65D2590/046
摘要： A container for containing flowable material comprises a rigid tank having a top opening therein for filling the tank with flowable material. A bottom opening in the lowermost portion of the tank for evacuating the flowable material. A cap seals the top opening in the tank and a piping assembly is connected to the bottom opening. A collapsible bladder inside the tank prevents the flowable material from coming into contact with the tank. A mating top cover and bottom base assembly are shaped to receive and enclose the tank. The piping assembly includes a dispensing spout which utilizes a spout, a dry-lock or a spring valve.
摘要翻译： 用于容纳可流动材料的容器包括刚性罐，其中具有顶部开口，用于将罐装满可流动材料。 在罐的最下部分的底部开口用于抽空可流动的材料。 盖子密封罐中的顶部开口，并且管道组件连接到底部开口。 罐内的可折叠的气囊防止可流动的材料与罐接触。 配合的顶盖和底部基座组件成形为容纳和封闭罐。 管道组件包括使用喷口，干式锁或弹簧阀的分配喷口。
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公开(公告)号：US5366704A
公开(公告)日：1994-11-22
申请号：US992342
申请日：1992-12-17
CPC分类号： B01J8/003 , B01J8/0085 , B01J8/12 , C10G35/12
摘要： A fluid solid-contacting device eliminates the accumulation of deposits behind distribution collection conduits, reduces the differential expansion between the conduits and a containment vessel, and improves fluid distribution by extending the perforations into a back side of a distribution conduit that abuts the vessel. This apparatus has greatest application to scallop-shaped conduits that are commonly used in radial flow reactors. The perforations, extended into the back side of the scallop, ventilate the area between the scallop and the vessel holding the scallops.
摘要翻译： 流体固体接触装置消除了分布收集管道后面的沉积物的累积，减少了管道和容器之间的差异膨胀，并且通过将穿孔延伸到与容器邻接的分配导管的后侧来改善流体分布。 该设备对通常用于径向流反应器的扇形管道具有最大的应用。 穿过扇形物，延伸到扇贝的背面，使扇贝和容纳扇贝的容器之间的区域通风。
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公开(公告)号：US5209908A
公开(公告)日：1993-05-11
申请号：US729977
申请日：1991-07-15
CPC分类号： B01J8/12 , B01J8/003 , B01J8/0085 , C10G35/12
摘要： A fluid solid-contacting device eliminates the accumulation of deposits behind distribution collection conduits, reduces the differential expansion between the conduits and a containment vessel, and improves fluid distribution by extending the perforations into a back side of a distribution conduit that abuts the vessel. This apparatus has greatest application to scallop-shaped conduits that are commonly used in radial flow reactors. The perforations, extended into the back side of the scallop, ventilate the area between the scallop and the vessel holding the scallops.
摘要翻译： 流体固体接触装置消除了分布收集管道后面的沉积物的累积，减少了管道和容器之间的差异膨胀，并且通过将穿孔延伸到与容器邻接的分配导管的后侧来改善流体分布。 该设备对通常用于径向流反应器的扇形管道具有最大的应用。 穿过扇形物，延伸到扇贝的背面，使扇贝和容纳扇贝的容器之间的区域通风。
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公开(公告)号：US4250018A
公开(公告)日：1981-02-10
申请号：US73168
申请日：1979-09-06
申请人： Kenneth D. Peters
发明人： Kenneth D. Peters
摘要： A multiple stage hydrocarbon conversion system wherein a hydrogen-hydrocarbonaceous feedstock reaction mixture is processed serially through a plurality of reaction zones, each of which contains a particulate catalyst disposed as an annular-form bed movable downwardly through the reaction zone, and wherein said reaction mixture is processed in radial flow through said annular-form bed. Pinning of the catalyst particles within the annular-form bed is substantially obviated by the combined effect of charging only a portion of the total hydrogen to the first reaction zone, charging the balance of the total hydrogen to a subsequent reaction zone, and restricting the effluent flow of at least one reaction zone.
摘要翻译： 一种多级烃转化系统，其中氢 - 烃类原料反应混合物通过多个反应区串联加工，其中每个反应区含有设置成可向下移动通过反应区的环形床的颗粒催化剂，并且其中所述反应混合物 在通过所述环形床的径向流中被加工。 催化剂颗粒在环形床内的固定基本上被仅将一部分总氢充入第一反应区，将总氢平衡装入后续反应区和限制流出物 至少一个反应区的流动。
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