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1. 发明授权

US4203759A Process for the preparation of a vanadium-containing metallic ash concentrate 失效
标题翻译：用于制备含钒金属灰精矿的方法
公开(公告)号：US4203759A
公开(公告)日：1980-05-20
申请号：US901700
申请日：1978-05-01
申请人： William J. Metrailer , David E. Mueller
发明人： William J. Metrailer , David E. Mueller
IPC分类号： C22B1/00 , C22B34/22 , B22F9/00
CPC分类号： C10B55/10 , C10J3/463 , C10J3/482 , C10J3/721 , C10J3/78 , C22B1/005 , C22B34/22 , C10J2300/0943 , C10J2300/0956 , C10J2300/0959 , C10J2300/0976 , C10J2300/0986 , C10J2300/1807 , C10J2300/1846 , Y02P10/212
摘要： A low density particulate vanadium-containing metallic ash concentrate, at least 50 percent of the articles of said concentrate having a diameter not greater than about 1 micron, is produced from a partially gasified coke comprising metallic components including vanadium components by heating the partially gasified coke in an oxidizing atmosphere at a temperataure below the fusion point of the metallic components.
摘要翻译：低密度颗粒状含钒金属灰分浓缩物，所述浓缩物的至少50％的直径不大于约1微米，由部分气化的焦炭产生，所述部分气化焦炭包括包含钒组分的金属组分，通过加热部分气化的焦炭在低于金属组分的熔点的温度的氧化气氛中。

2. 发明授权

US3933445A Process and apparatus for preventing deposits on a gas inlet nozzle 失效
标题翻译：用于防止气体入口喷嘴沉积物的方法和装置
公开(公告)号：US3933445A
公开(公告)日：1976-01-20
申请号：US406219
申请日：1973-10-15
申请人： David E. Mueller , William J. Metrailer
发明人： David E. Mueller , William J. Metrailer
IPC分类号： B01J8/18 , C10J3/56 , C10J3/54
CPC分类号： B01J8/1818 , C10J3/503 , C10J3/56 , C10J3/78 , C10J2300/093 , C10J2300/0946 , C10J2300/0956 , C10J2300/0959 , C10J2300/0976
摘要： An oxidizing gas is injected through a nozzle into a bed of carbonaceous particles in a downward direction at an angle of declination at least as great as the angle of repose of the bed particles and at a gas inlet velocity of about 50 to 500 feet per second to supply the gas needed to fluidize the bed of carbonaceous particles.
摘要翻译：氧化气体通过喷嘴以向下的方向沿着向下的方向注入到至少与床颗粒的休止角一样大的角度并以每秒约50至500英尺的气体入口速度注入到碳质颗粒床中以供应流化碳质颗粒床所需的气体。

3. 发明授权

US4051016A Fluid coking with H.sub.2 S addition 失效
标题翻译：流体焦化与H {HD 2 {B S添加
公开(公告)号：US4051016A
公开(公告)日：1977-09-27
申请号：US652761
申请日：1976-01-27
申请人： William J. Metrailer , Charles Rebick , Richard K. Lyon
发明人： William J. Metrailer , Charles Rebick , Richard K. Lyon
IPC分类号： C10B55/10 , C10G9/00 , C10G9/32
CPC分类号： C10G9/32 , C10B55/10 , C10G9/005 , C10G2400/26
摘要： A fluid coking process is provided in which a relatively large amount of hydrogen sulfide is added to the coker fluidizing gas. A preferred fluidizing gas is a mixture of hydrogen and hydrogen sulfide.
摘要翻译：提供了一种流化焦化方法，其中相对大量的硫化氢被加入到焦化器流化气体中。优选的流化气体是氢和硫化氢的混合物。

4. 发明授权

US4295956A Fluid coking process 失效
标题翻译：流体焦化工艺
公开(公告)号：US4295956A
公开(公告)日：1981-10-20
申请号：US126400
申请日：1980-03-03
申请人： William J. Metrailer
发明人： William J. Metrailer
IPC分类号： C10B55/10 , C10G9/00 , C10G9/32
CPC分类号： C10G9/005 , C10B55/10 , C10G9/32
摘要： A fluid coking process is provided in which the recycling of coke particles of less than about 44 microns in diameter to the coking reactor is minimized by passing the stream of coke withdrawn from the coking reactor to a vessel comprising a fluidized bed of solids separated into two zones. The coke withdrawn from the coker is passed into one zone where seed generation for the process is performed. Coke recycled to the coker is withdrawn from the second zone which is operated as an elutriation zone. The solid fines of less than 44 microns are removed overhead from the vessel with the gaseous effluent of the vessel. This improvement is particularly suitable for once-through fluid coking to minimize small fines being present in the coker liquid product.
摘要翻译：提供了一种流体焦化方法，其中通过使从焦化反应器中排出的焦炭流通过包含分离成两部分的固体流化床的容器将直径小于约44微米的焦炭颗粒再循环至焦化反应器被最小化区域。从焦化器中取出的焦炭进入一个进行该过程的种子生成的区域。再循环到焦化器的焦炭从作为淘汰区域运行的第二区域排出。小于44微米的固体细粉从容器的顶部除去容器的气态流出物。这种改进特别适用于直接流体焦化以使焦化液体产品中存在的小细屑最小化。

5. 发明授权

US4366048A Fluid coking with the addition of solids 失效
标题翻译：流体焦化，加入固体
公开(公告)号：US4366048A
公开(公告)日：1982-12-28
申请号：US281918
申请日：1981-07-09
申请人： William J. Metrailer , Steven Wiechert
发明人： William J. Metrailer , Steven Wiechert
IPC分类号： C10G9/32 , C10G9/00
CPC分类号： C10G9/32
摘要： A fluid coking process is provided in which inert particles, such as coke, are added to the coker feed, in a specified amount.
摘要翻译：提供了一种流体焦化方法，其中将惰性颗粒如焦炭以指定量加入焦化器进料中。

6. 发明授权

US4169038A Combination hydroconversion, fluid coking and gasification 失效
标题翻译：组合加氢转化，流化焦化和气化
公开(公告)号：US4169038A
公开(公告)日：1979-09-25
申请号：US889744
申请日：1978-03-24
申请人： William J. Metrailer , Roby Bearden, Jr. , Clyde L. Aldridge
发明人： William J. Metrailer , Roby Bearden, Jr. , Clyde L. Aldridge
IPC分类号： C10B55/10 , C10G1/00 , C10G1/06 , C10G1/08 , C10G69/06 , C10J3/54 , C10G9/32
CPC分类号： C10J3/54 , C10B55/10 , C10G1/002 , C10G1/08 , C10G1/086 , C10G69/06 , C10J3/503 , C10J3/66 , C10J3/78 , C10J3/84 , C10J2300/0906 , C10J2300/093 , C10J2300/0946 , C10J2300/0956 , C10J2300/0959 , C10J2300/0976 , C10J2300/0986 , C10J2300/1807 , C10J2300/1884 , Y10S208/951
摘要： A combination slurry hydroconversion, coking and coke gasification process is provided wherein solid fines having an average particle size of less than 10 microns in diameter or the ashes thereof recovered from a gaseous product derived from the coke gasification are used as a catalyst in the hydroconversion stage.
摘要翻译：提供了一种组合浆料加氢转化，焦化和焦炭气化方法，其中直径小于10微米的固体细粉或其衍生自焦炭气化的气态产物回收的灰分在加氢转化阶段用作催化剂。

7. 发明授权

US4426277A Low severity fluid coking process 失效
标题翻译：低浓度流体焦化工艺
公开(公告)号：US4426277A
公开(公告)日：1984-01-17
申请号：US378211
申请日：1982-05-14
申请人： William J. Metrailer
发明人： William J. Metrailer
IPC分类号： C10B57/04 , B01J8/38 , C10B49/20 , C10B55/08 , C10G9/00 , C10G9/32 , C10G51/02
CPC分类号： C10G51/023 , B01J8/384 , C10B49/20 , C10B55/08 , C10G9/005 , C10G9/32
摘要： A fluid coking process is provided in which a carbonaceous feed is first coked in a dense fluidized bed first coking zone and the effluent of the dense bed is passed as a suspension through a transferline second coking zone. A major portion of the solids is separated from the effluent of the upper end of the transferline and passed to a third coking zone which is operated at a higher temperature than the other coking zones and in which the first and second coking zones are positioned.
摘要翻译：提供了一种流体焦化方法，其中碳质进料首先在致密的流化床第一焦化区中焦化，并且致密床的流出物作为悬浮液通过传输线第二焦化区。固体的主要部分与传输线上端的流出物分离，并通过第三焦化区，其在比其它焦化区更高的温度下操作，其中第一和第二焦化区位于该第三焦化区。

8. 发明授权

US4235700A Two-stage coking for the production of low metals coke 失效
标题翻译：两阶段焦化生产低金属焦炭
公开(公告)号：US4235700A
公开(公告)日：1980-11-25
申请号：US84511
申请日：1979-10-12
申请人： William J. Metrailer
发明人： William J. Metrailer
IPC分类号： C10B55/00 , C10G51/02
CPC分类号： C10B55/00 , C10G51/023
摘要： A low metals coke is produced in a two-stage coking process in which the first coking stage is once-through fluid coking, and the heavy oil separated from the fluid coking zone effluent is coked in a second coking stage, which is delayed coking.
摘要翻译：在两阶段焦化工艺中生产低金属焦炭，其中第一焦化阶段是一次性流化焦化，并且从流体焦化区流出物中分离出的重油在第二焦化阶段焦化，这是延迟焦化。

9. 发明授权

US4204943A Combination hydroconversion, coking and gasification 失效
标题翻译：组合加氢转化，焦化和气化
公开(公告)号：US4204943A
公开(公告)日：1980-05-27
申请号：US942689
申请日：1978-09-15
申请人： William J. Metrailer , Roby Bearden, Jr. , Clyde L. Aldridge
发明人： William J. Metrailer , Roby Bearden, Jr. , Clyde L. Aldridge
IPC分类号： C10B55/10 , C10G1/00 , C10G1/08 , C10G47/26 , C10G69/06 , C10J3/54 , C10G37/06
CPC分类号： C10G1/086 , C10B55/10 , C10G1/002 , C10G1/08 , C10G1/083 , C10G47/26 , C10G69/06 , C10J3/482 , C10J3/54 , C10J3/721 , C10J3/78 , C10J3/84 , C10J2300/0906 , C10J2300/093 , C10J2300/0943 , C10J2300/0956 , C10J2300/0959 , C10J2300/0976 , C10J2300/0986 , C10J2300/1807 , C10J2300/1884 , C10J2300/1892
摘要： A combination slurry hydroconversion, coking and coke gasification process is provided wherein carbonaceous solids having an average particle size of less than 10 microns in diameter or the ashes thereof are used as a catalyst in the hydroconversion stage.
摘要翻译：提供了组合浆料加氢转化，焦化和焦炭气化方法，其中平均粒度小于10微米的碳质固体或其灰分在加氢转化阶段用作催化剂。

10. 发明授权

US4057487A Fluid coking process 失效
标题翻译：流体焦化工艺
公开(公告)号：US4057487A
公开(公告)日：1977-11-08
申请号：US706218
申请日：1976-07-19
申请人： William J. Metrailer , Joseph P. Matula
发明人： William J. Metrailer , Joseph P. Matula
IPC分类号： C10B55/10 , C10G9/32
CPC分类号： C10B55/10
摘要： A hydrocarbonaceous oil is introduced to a quench and scrubbing zone mounted on a fluid coking reactor. Heat from the coker vapor product vaporizes a portion of the hydrocarbonaceous oil. The unvaporized portion of the oil is used to quench and scrub the coker vapor product. The bottoms fraction of the quench and scrubbing zone is passed to a vacuum distillation zone to recover a heavy oil fraction and to produce a vacuum residuum for use as coker feed.
摘要翻译：将烃油引入安装在流化焦化反应器上的骤冷和洗涤区。来自焦化蒸气产物的热量蒸发出一部分含烃油。油的未蒸发部分用于淬火和洗涤焦化蒸气产物。骤冷和洗涤区的底部馏分通入真空蒸馏区，以回收重油馏分，并产生用作焦化器进料的真空渣油。

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