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公开(公告)号：US20230302467A1
公开(公告)日：2023-09-28
申请号：US18188130
申请日：2023-03-22
申请人： Brian W. Hedrick
发明人： Brian W. Hedrick
CPC分类号： B04C3/06 , B04C3/04 , B04C2003/006
摘要： A uniflow cyclone that has multiple inlets, normally achieved via a vane, a barrel length, then a solids collection channel of larger diameter but concentric with the barrel and a tangential solids outlet to either a plenum or a dust hopper. The gas flows past the enlarged channel and continues through additional barrel length to an outlet zone. The cyclone would normally have a concentric center pipe the extends from the vane to the gas outlet of the cyclone.
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52.发明授权公开(公告)号：US10695775B1
公开(公告)日：2020-06-30
申请号：US16696940
申请日：2019-11-26
申请人： Brian W. Hedrick
发明人： Brian W. Hedrick
摘要： A compact dual stage cyclone separation assembly, an efficient dual stage cyclone separator, and a method for utilizing the same, comprising a lower pressure drop across the dual stage separators due to fewer particle-contaminated gas flow directional changes in the particle contaminated gas stream, and method for using same. The dual stage cyclone separator comprises a primary stage cyclone barrel and a second stage cyclone barrel, wherein the second stage cyclone barrel is coaxial with and concentric within the first cyclone separator, a solids extraction port, wherein said sidewall of said main body defines a solids extraction port opening located between said upper end and said lower end for discharging large particles from said cyclone body, and a small particle discharge opening, wherein the small particle discharge opening is located inside the lower end of the main body.
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公开(公告)号：US09238600B2
公开(公告)日：2016-01-19
申请号：US13325292
申请日：2011-12-14
申请人： David A. Wegerer , Brian W. Hedrick , Zhihao Fei , Daniel N. Myers , Vincenza Myers , Paolo Palmas , Laura E. Leonard
发明人： David A. Wegerer , Brian W. Hedrick , Zhihao Fei , Daniel N. Myers , Paolo Palmas , Laura E. Leonard
CPC分类号： C07C4/06 , C07C2521/04 , C07C2521/08 , C07C2521/16 , C07C2529/40 , C07C2529/50 , C07C2529/65 , C10G11/05 , C10G11/18 , C10G51/026 , C10G2400/20 , Y02P20/52 , Y02P20/584 , C07C11/04 , C07C11/06
摘要： A process for improving the yield of ethylene and propylene from a light naphtha feedstock includes obtaining light naphtha feedstock from a primary cracking zone having a cracking catalyst. The light naphtha feedstock is contacted with an olefin catalyst in an olefin producing zone to produce an ethylene- and propylene-rich stream. After reacting with the olefin catalyst, the ethylene- and propylene-rich stream is separated from the olefin catalyst from in a separator zone. At least a portion of the olefin catalyst is regenerated by combusting coke deposited on a surface of the olefin catalyst in an oxygen-containing environment, and at least a portion of the olefin catalyst is heated. These portions could be the same one or they could be different. In some embodiments, at least a portion of the olefin catalyst could be neither regenerated nor heated. The olefin catalyst is returned to the olefin producing zone.
摘要翻译： 从轻石脑油原料提高乙烯和丙烯的产率的方法包括从具有裂化催化剂的一次裂解区获得轻质石脑油原料。 轻质石脑油原料与烯烃生产区中的烯烃催化剂接触以产生富含乙烯和丙烯的料流。 在与烯烃催化剂反应后，将乙烯和富丙烯物流从分离器区域与烯烃催化剂分离。 至少一部分烯烃催化剂通过在含氧环境中燃烧沉积在烯烃催化剂的表面上的焦炭再生，至少部分烯烃催化剂被加热。 这些部分可以是相同的，也可以是不同的。 在一些实施方案中，烯烃催化剂的至少一部分既不能再生也不能加热。 将烯烃催化剂返回到烯烃生产区。
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公开(公告)号：US09157037B2
公开(公告)日：2015-10-13
申请号：US12337728
申请日：2008-12-18
申请人： Brian W. Hedrick , Daniel B. Gillis
发明人： Brian W. Hedrick , Daniel B. Gillis
CPC分类号： C10G69/04 , C10G67/04 , C10G69/126
摘要： A process and apparatus for improving flow properties of crude may include processing a first crude stream, which may in turn include cracking the first crude stream with catalyst to form a cracked stream and spent catalyst, hydrotreating a portion of the cracked stream and then mixing the hydrotreated stream with an unprocessed second crude stream.
摘要翻译： 用于改善粗品流动性质的方法和设备可包括加工第一原油流，其还可包括用催化剂裂化第一原油流以形成裂化料流和废催化剂，加氢处理裂化物流的一部分，然后将 加氢处理的流与未加工的第二原油流。
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公开(公告)号：US08747504B2
公开(公告)日：2014-06-10
申请号：US13328528
申请日：2011-12-16
IPC分类号： A47L5/36
CPC分类号： B01D45/16 , B04C3/04 , B04C3/06 , B04C2003/006 , Y10T137/0402
摘要： Embodiments of a gas-solids separation unit and embodiments of a method for manufacturing a separation unit are provided. In one embodiment, the separation unit includes a cyclonic separator and a vessel having a flue gas chamber, a clean gas chamber, and an entrained solids chamber between the flue gas chamber and the clean gas chamber. The cyclonic separator includes, in turn, a cyclone barrel extending from the flue gas chamber toward the clean gas chamber, a swirl vane positioned across the cyclone barrel, a gas outlet tube fluidly coupling the cyclone barrel to the clean gas chamber, and a first check valve opening formed through the barrel sidewall upstream of the gas outlet tube. The check valve opening fluidly couples the cyclone barrel to the entrained solids chamber to permit the centrifugal separation of the particulate matter from the gas stream during operation of the gas-solids separation unit.
摘要翻译： 提供气固分离单元的实施例和制造分离单元的方法的实施例。 在一个实施方案中，分离单元包括旋风分离器和具有烟道气室，清洁气体室和在烟道气室和清洁气体室之间的夹带固体室的容器。 旋风分离器又包括从烟道气室朝向清洁气体室延伸的旋风筒，旋转叶片定位在旋风筒上，将气旋出口管流体地连接到清洁气体室，第一 止回阀开口通过气体出口管上游的桶壁侧壁形成。 止回阀打开将旋风筒流体地连接到夹带的固体室，以允许在气固分离单元的操作期间颗粒物质与气流的离心分离。
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公开(公告)号：US08263008B2
公开(公告)日：2012-09-11
申请号：US12337734
申请日：2008-12-18
申请人： Brian W. Hedrick , Daniel B. Gillis
发明人： Brian W. Hedrick , Daniel B. Gillis
CPC分类号： C10G11/18 , C10G45/32 , C10G69/04 , C10G2300/1033
摘要： A process and apparatus for improving flow properties of crude may include processing a first crude stream, which may in turn include cracking the first crude stream with catalyst to form a cracked stream and spent catalyst, hydrotreating a portion of the cracked stream and then mixing the hydrotreated stream with an unprocessed second crude stream.
摘要翻译： 用于改善粗品流动性质的方法和设备可包括加工第一原油流，其还可包括用催化剂裂化第一原油流以形成裂化料流和废催化剂，加氢处理裂化物流的一部分，然后将 加氢处理的流与未加工的第二原油流。
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公开(公告)号：US08246914B2
公开(公告)日：2012-08-21
申请号：US12340945
申请日：2008-12-22
CPC分类号： C10G11/18 , C10G2300/1044 , C10G2300/1088 , C10G2300/301 , C10G2400/02 , C10G2400/20
摘要： One exemplary embodiment can be a fluid catalytic cracking system. The system can include a reaction zone operating at conditions to facilitate olefin production and including at least one riser. The at least one riser can receive a first feed having a boiling point of about 180-about 800° C., and a second feed having more than about 70%, by weight, of one or more C4+ olefins.
摘要翻译： 一个示例性实施方案可以是流化催化裂化系统。 该系统可以包括在促进烯烃生产的条件下操作并包括至少一个提升管的反应区。 所述至少一个提升管可以接收沸点为约180-约800℃的第一进料，以及具有大于约70重量％的一种或多种C 4 +烯烃的第二进料。
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公开(公告)号：US07799287B2
公开(公告)日：2010-09-21
申请号：US11950886
申请日：2007-12-05
IPC分类号： F27B15/08
CPC分类号： C10G11/182
摘要： Disclosed is an apparatus and process for disengaging regenerated catalyst from flue gas in a catalyst regenerator so as to avoid re-entrainment of catalyst that has settled into a bed in the catalyst regenerator using a disengaging device. A disengaging arm of the disengaging device has an outer shell that encloses the arm, an inner shell with a slot for allowing catalyst and flue gas to exit the arm and an outer baffle having a lower edge located below the opening in the outer wall. The baffle directs the catalyst and flue gas downwardly and limits radial flow. Catalyst and flue gas enter the disengaging arm through an opening in an outer wall of a riser section at a first superficial velocity and exits through a slot in a bottom of the disengaging arm at no more than 1.33 the first superficial velocity.
摘要翻译： 公开了一种用于使再生催化剂与催化剂再生器中的烟道气脱离的装置和方法，以避免使用分离装置将催化剂重新夹带在催化剂再生器中的床中。 分离装置的分离臂具有包围臂的外壳，具有用于允许催化剂和烟道气离开臂的槽的内壳和具有位于外壁中的开口下方的下边缘的外挡板。 挡板将催化剂和烟道气向下引导并限制径向流动。 催化剂和烟气以第一表面速度通过提升管部分的外壁中的开口进入分离臂，并且以不超过第一表面速度的1.33离开分离臂的底部中的狭槽。
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公开(公告)号：US20100158767A1
公开(公告)日：2010-06-24
申请号：US12340945
申请日：2008-12-22
IPC分类号： B01J8/24
CPC分类号： C10G11/18 , C10G2300/1044 , C10G2300/1088 , C10G2300/301 , C10G2400/02 , C10G2400/20
摘要： One exemplary embodiment can be a fluid catalytic cracking system. The system can include a reaction zone operating at conditions to facilitate olefin production and including at least one riser. The at least one riser can receive a first feed having a boiling point of about 180-about 800° C., and a second feed having more than about 70%, by weight, of one or more C4+ olefins.
摘要翻译： 一个示例性实施方案可以是流化催化裂化系统。 该系统可以包括在促进烯烃生产的条件下操作并包括至少一个提升管的反应区。 所述至少一个提升管可以接收沸点为约180-约800℃的第一进料，以及具有大于约70重量％的一种或多种C 4 +烯烃的第二进料。
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60.发明授权Method and system of heating a fluid catalytic cracking unit for overall CO2 reduction 有权加热流化催化裂化装置以减少总体CO2的方法和系统公开(公告)号：US07699975B2
公开(公告)日：2010-04-20
申请号：US11962810
申请日：2007-12-21
申请人： Brian W. Hedrick
发明人： Brian W. Hedrick
IPC分类号： C10G51/04
CPC分类号： C10G11/182 , B01J29/90 , B01J38/30 , C01B3/26 , C01B3/30 , C01B2203/0277 , C01B2203/0283 , C01B2203/0415 , C01B2203/043 , C01B2203/0465 , C01B2203/0475 , C01B2203/0485 , C01B2203/0811 , C01B2203/0822 , C01B2203/0883 , C10G11/185 , C10J3/482 , C10J2300/16 , C10J2300/1618 , C10J2300/1671 , F01K13/00 , Y02E20/344 , Y02P20/128 , Y02P20/52 , Y02P20/584 , Y02P30/30 , Y02P30/446
摘要： In at least one embodiment of the present invention, a method of heating a FCC unit having a regenerator and a reactor for over CO2 reduction is provided. The method comprises compressing syngas to define compressed syngas. CO2 is separated from the compressed syngas to provide a first stream of gas comprising CO2. The first stream of gas is expanded with a second stream of gas comprising O2 to define a feed gas. The feed gas and an injected hydrocarbon feed are introduced to the regenerator having spent catalyst from the reactor. The regenerator is at gasification conditions to burn the injected hydrocarbon feed and coke from the spent catalyst producing the syngas and heat for operating the reactor at reaction temperatures.
摘要翻译： 在本发明的至少一个实施方案中，提供了一种加热具有再生器的FCC单元和用于二氧化碳还原的反应器的方法。 该方法包括压缩合成气以限定压缩的合成气。 CO 2与压缩的合成气分离以提供包含CO 2的第一气体流。 第一气体气体用包含O 2的第二气体气流扩张以限定进料气体。 将进料气体和注入的烃进料从反应器引入到具有废催化剂的再生器中。 再生器在气化条件下燃烧注入的烃进料和来自废催化剂的焦炭，产生合成气，并在反应温度下操作反应器的热量。
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