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1. 发明授权

US5639930A Process of producing alkylates 失效
标题翻译：生产烷基化物的方法
公开(公告)号：US5639930A
公开(公告)日：1997-06-17
申请号：US368533
申请日：1995-01-04
申请人： Joe E. Penick
发明人： Joe E. Penick
IPC分类号： C07C2/58 , C07C2/56
CPC分类号： C07C2/58 , C07C2529/06 , C07C2529/08 , C07C2529/12 , C07C2529/18 , C07C2529/22
摘要： Method of producing alkylates in which an isoparaffin, olefin, a diffusing agent and a solid, acid catalyst are combined to form a three phase reaction mixture; a hydrocarbon phase containing primarily isoparaffin, a diffusing agent phase containing the diffusing agent, olefin and diffuse isoparaffin and a solid, acid catalyst phase, the diffusing agent being a polar solvent in which the olefin and aromatics are soluble.
摘要翻译：制备其中将异链烷烃，烯烃，扩散剂和固体酸催化剂合并形成三相反应混合物的烷基化物的方法; 主要含有异链烷烃的烃相，含有扩散剂的扩散剂相，烯烃和扩散异构链烷烃以及固体，酸催化剂相，扩散剂是烯烃和芳族化合物可溶的极性溶剂。

2. 发明授权

US4640675A Method of burning low hydrogen content fuels 失效
标题翻译：燃烧低氢含量燃料的方法
公开(公告)号：US4640675A
公开(公告)日：1987-02-03
申请号：US659124
申请日：1984-10-09
申请人： Gary J. Green , Harry A. McVeigh , Joe E. Penick , Tsoung Y. Yan
发明人： Gary J. Green , Harry A. McVeigh , Joe E. Penick , Tsoung Y. Yan
IPC分类号： C10L1/04 , F23C1/00
CPC分类号： C10L1/04
摘要： Decreasing the viscosity of and improving the atomizing and burning characteristics of a hydrogen deficient fuel by dissolving a light, hydrogen rich hydrocarbon in the fuel.
摘要翻译：通过将轻质富氢烃溶解在燃料中来降低氢气缺乏燃料的雾度和燃烧特性的粘度并提高其燃烧特性。

3. 发明授权

US4597854A Multi-bed hydrodewaxing process 失效
标题翻译：多床加氢脱蜡工艺
公开(公告)号：US4597854A
公开(公告)日：1986-07-01
申请号：US755767
申请日：1985-07-17
申请人： Joe E. Penick
发明人： Joe E. Penick
IPC分类号： C10G45/64 , C10G45/58 , C10G49/00 , C10G65/04 , C10G65/12
CPC分类号： C10G45/58 , C10G49/002 , C10G65/043
摘要： Catalytic dewaxing of hydrocarbon oils is effected with intermediate hydrotreating. A continuous multi-bed technique employs alternating beds of dewaxing and hydrogenation catalysts to improve process performance, whereby partially dewaxed effluent is treated to decrease coke deposits.
摘要翻译：烃油的催化脱蜡通过中间加氢处理进行。连续多床技术使用脱蜡和氢化催化剂的交替床来提高加工性能，从而处理部分脱蜡的流出物以减少焦炭沉积物。

4. 发明授权

US4678645A Conversion of LPG hydrocarbons to distillate fuels or lubes using integration of LPG dehydrogenation and MOGDL 失效
标题翻译：使用LPG脱氢和MOGDL的整合将LPG烃转化为馏出燃料或润滑油
公开(公告)号：US4678645A
公开(公告)日：1987-07-07
申请号：US739407
申请日：1985-05-30
申请人： Clarence D. Chang , Joe E. Penick , Richard F. Socha
发明人： Clarence D. Chang , Joe E. Penick , Richard F. Socha
IPC分类号： C10G50/00 , C10G50/02 , B01J8/04 , C07C2/12 , C07C2/74
CPC分类号： C10G50/02 , C10G50/00
摘要： A method and apparatus for producing distillate and/or lubes employs integrating catalytic (or thermal) dehydrogenation of paraffins with MOGDL. The process feeds the product from a low temperature propane and/or butane dehydrogenation zone into a first catalytic reactor zone, which operates at low pressure and contains zeolite oligomerization catalysts, where the low molecular weight olefins are reacted to primarily gasoline range materials. These gasoline range materials can then be pressurized to the pressure required for reacting to distillate in a second catalytic reactor zone operating at high pressure and containing a zeolite oligomerization catalyst. The distillate is subsequently sent to a hydrotreating unit and product separation zone to form lubes and other finished products.
摘要翻译：用于生产馏出物和/或润滑剂的方法和装置将石蜡的催化（或热）脱氢与MOGDL整合。该方法将产物从低温丙烷和/或丁烷脱氢区进料到第一催化反应器区，其在低压下操作并含有沸石低聚催化剂，其中低分子量烯烃主要与汽油范围材料反应。然后可以将这些汽油范围材料加压至在高压下操作并含有沸石低聚催化剂的第二催化反应器区域中与馏出物反应所需的压力。随后将馏出物送至加氢处理装置和产品分离区以形成润滑剂和其它成品。

5. 发明授权

US4523987A Feed mixing techique for fluidized catalytic cracking of hydrocarbon oil 失效
标题翻译：用于烃油流化催化裂化的饲料混合技术
公开(公告)号：US4523987A
公开(公告)日：1985-06-18
申请号：US665333
申请日：1984-10-26
申请人： Joe E. Penick
发明人： Joe E. Penick
IPC分类号： C10G11/00 , B01J8/08 , C10G11/18
CPC分类号： C10G11/18 , B01J8/085
摘要： In a fluid catalytic cracking process comprising admixing a hydrocarbon oil feed with hot regenerated catalyst in the bottom section of a reactor riser, passing the mixture of the hydrocarbon oil feed and the catalyst through the riser, thereby at least partially volatilizing the oil feed and effecting cracking thereof at the process temperature under endothermic process conditions and deactivating the catalyst by deposition of carbonaceous deposits thereon, separating the deactivated catalyst from the cracked hydrocarbonaceous feed, passing the deactivated catalyst to a regenerator vessel wherein the carbonaceous deposits are removed from the deactivated catalyst under exothermic process conditions by means of a regenerating medium introduced into the regenerator vessel, and passing the regenerated hot catalyst substantially above process cracking temperature to the bottom section of the reactor riser; the improvement comprisingcontinuously injecting liquid oil feed into a primary mixing zone in a venturi tube mixer spaced inwardly from the reactor riser wall at the bottom portion therein adjacent a regenerated catalyst return conduit;continuously passing a first portion of the hot regenerated catalyst into the venturi tube mixer sufficient to vaporize a major amount of oil feed without substantial cracking thereof; andpassing a remaining second hot regenerated catalyst portion into the reactor riser through a passage between the venturi tube mixer and reactor riser wall, thereby mixing additional hot catalyst with vaporized oil feed to crack the oil feed in the reactor riser above the venturi tube mixer.
摘要翻译：在流化催化裂解方法中，包括将碳氢化合物油进料与热再生催化剂混合在反应器提升管的底部，使烃油进料和催化剂的混合物通过提升管，从而至少部分挥发油进料并实现在吸热过程条件下在工艺温度下开裂，并在其上沉积碳沉积物使催化剂失活，将失活的催化剂与裂化的烃类进料分离，使失活的催化剂通过再生器容器，其中将碳沉积物从失活的催化剂中除去通过引入再生器容器的再生介质，并将再生的热催化剂大大高于工艺开裂温度，使其进入反应器提升管的底部; 改进包括将液体油进料连续地喷射到文丘里管混合器中的文丘里管混合器中，该文丘里管混合器在其邻近再生催化剂返回导管的底部处与反应器提升管壁向内间隔开; 将热再生催化剂的第一部分连续地通入文氏管混合器中，足以蒸发大量的油进料而没有实质的裂化; 并将剩余的第二热再生催化剂部分通过文丘里管混合器和反应器提升管壁之间的通道传送到反应器提升管中，由此将附加的热催化剂与汽化的进料混合物裂解在文丘里管混合器上方的反应器提升管中的油进料。

6. 发明授权

US4064039A Fluid catalytic cracking 失效
标题翻译：流体催化裂化
公开(公告)号：US4064039A
公开(公告)日：1977-12-20
申请号：US653167
申请日：1976-01-28
申请人： Joe E. Penick
发明人： Joe E. Penick
IPC分类号： C10G11/02 , C10G11/18
CPC分类号： C10G11/18 , C10G11/02
摘要： Modifying a heat balanced operating fluid catalytic cracking (FCC) system to utilize a platinum group metal modified cracking catalyst, whereby increasing the heat generated in the exothermic regeneration of coked catalyst, and to provide a regenerated catalyst heat exchange cooler to permit adjustment of cracking conditions independent of the extra heat produced in the regeneration of catalyst.
摘要翻译：修改热平衡工作流体催化裂化（FCC）系统以利用铂族金属改性裂化催化剂，由此增加在焦化催化剂的放热再生中产生的热量，并提供再生催化剂热交换冷却器以允许调节裂化条件独立于催化剂再生产生的额外热量。

7. 发明授权

US4755281A Countercurrent process with froth control for treating heavy hydrocarbons 失效
标题翻译：用于处理重质烃的泡沫控制的逆流过程
公开(公告)号：US4755281A
公开(公告)日：1988-07-05
申请号：US789219
申请日：1985-10-18
申请人： Joe E. Penick
发明人： Joe E. Penick
IPC分类号： B01J8/00 , B01J8/02 , B01J19/00 , C10G49/00 , C10G49/26 , C10G13/10 , C10G13/06
CPC分类号： C10G49/002 , B01J19/0006 , B01J8/001 , B01J8/02 , C10G49/00 , C10G49/26 , B01J2208/0007 , B01J2208/00079 , B01J2208/0053 , B01J2208/00539 , B01J2208/00548 , B01J2208/0061 , Y10S208/01
摘要： A countercurrent technique is disclosed for contacting liquid and gas reactants in a fixed porous catalyst bed. The reactants are maintained as a multiphase mixture in the catalyst bed. Upwardly flowing dispersed gas is disengaged from liquid feedstock above the catalyst bed, while controlling froth level.
摘要翻译：公开了用于使液体和气体反应物在固定的多孔催化剂床中接触的逆流技术。反应物在催化剂床中作为多相混合物维持。向上流动的分散气体与催化剂床上方的液体原料脱开，同时控制泡沫水平。

8. 发明授权

US4705621A Catalytic reactor system with crosscurrent liquid and gasflow 失效
标题翻译：具有交叉流动和气流的催化反应器系统
公开(公告)号：US4705621A
公开(公告)日：1987-11-10
申请号：US714776
申请日：1985-03-22
申请人： Joe E. Penick
发明人： Joe E. Penick
IPC分类号： B01J8/02 , C10G45/64 , C10G49/00 , B01J8/08
CPC分类号： C10G49/002 , B01J8/0207 , B01J8/0242 , B01J8/0278 , C10G45/64
摘要： A crossflow reactor and operating technique provides a porous body of contact solids, such as a fixed catalyst bed, contained in a sloping configuration. Liquid, such as hydrocarbon oil, to be treated is applied to the bed surface and flows by gravity through the porous solid. Reactant gas flows transverse to the liquid, providing a horizontal component to the liquid to improve contact efficiency.
摘要翻译：交叉流反应器和操作技术提供包含在倾斜构造中的多孔接触固体，例如固定的催化剂床。待处理的液体如烃油被施加到床表面并通过重力流过多孔固体。反应物气体横向于液体流动，为液体提供水平分量以提高接触效率。

9. 发明授权

US4550012A Multi-phase countercurrent reactor system 失效
标题翻译：多相逆流反应堆系统
公开(公告)号：US4550012A
公开(公告)日：1985-10-29
申请号：US605740
申请日：1984-05-01
申请人： Joe E. Penick
发明人： Joe E. Penick
IPC分类号： B01J8/00 , B01J8/02 , B01J19/00 , C10G49/00 , C10G49/26 , B01J8/10 , B01D19/02
CPC分类号： B01J8/02 , B01J19/0006 , B01J8/001 , C10G49/00 , C10G49/002 , C10G49/26 , B01J2208/0007 , B01J2208/00079 , B01J2208/0053 , B01J2208/00539 , B01J2208/00548 , B01J2208/0061
摘要： A countercurrent continuous catalytic reactor system for treating a liquid phase, such as oil, with a gaseous reactant.An enclosed reactor shell contains a fixed porous bed of solid catalyst, upper liquid inlet device for introducing a stream of liquid substantially above the catalyst bed for downward gravity flow through the bed, and lower liquid outlet device for withdrawing treated liquid from the reactor shell. A gaseous reactant is dispersed through the liquid phase in intimate contact with the solid catalyst, and withdrawn above the catalyst bed.Level detector apparatus is disposed in a froth zone above the catalyst bed for detecting level of a mixed gas-liquid froth.Fluid handling control apparatus responsive to a level signal controls fluid stream flow for regulating froth level above the catalyst bed.
摘要翻译：一种用气态反应物处理液相如油的逆流连续催化反应器系统。封闭的反应器壳体包含固定催化剂的固定多孔床，用于引入基本上在催化剂床上方的液体流以用于向下重力流过床的上部液体入口装置，以及用于从反应器壳体中抽出经处理的液体的下部液体出口装置。气态反应物通过液相分散，与固体催化剂紧密接触，并在催化剂床上取出。液位检测装置设置在催化剂床上方的泡沫区中，用于检测混合气液泡沫的水平。响应于液位信号的流体处理控制装置控制用于调节催化剂床上方的泡沫水平的流体流动流。

10. 发明授权

US4542247A Conversion of LPG hydrocarbons to distillate fuels or lubes using integration of LPG dehydrogenation and MOGDL 失效
标题翻译：使用LPG脱氢和MOGDL的整合将LPG烃转化为馏出燃料或润滑油
公开(公告)号：US4542247A
公开(公告)日：1985-09-17
申请号：US650473
申请日：1984-09-14
申请人： Clarence D. Chang , Joe E. Penick , Richard F. Socha
发明人： Clarence D. Chang , Joe E. Penick , Richard F. Socha
IPC分类号： C10G50/00 , C10G50/02 , C07C5/00 , C07C1/00
CPC分类号： C10G50/00 , C10G50/02
摘要： Disclosed is a method and apparatus for producing distillate and/or lubes which employ integrating catalytic (or thermal) dehydrogenation of paraffins with MOGDL. The process feeds the product from a low temperature propane and/or butane dehydrogenation zone into a first catalytic reactor zone, which operates at low pressure and contains zeolite oligomerization catalysts, where the low molecular weight olefins are reacted to primarily gasoline range materials. These gasoline range materials can then be pressurized to the pressure required for reacting to distillate in a second catalytic reactor zone operating at high pressure and containing a zeolite oligomerization catalyst. The distillate is subsequently sent to a hydrotreating unit and product separation zone to form lubes and other finished products.
摘要翻译：公开了一种用于生产馏出物和/或润滑剂的方法和装置，其使用与MOGDL一起催化（或热）脱氢石蜡的方法和装置。该方法将产物从低温丙烷和/或丁烷脱氢区进料到第一催化反应器区，其在低压下操作并含有沸石低聚催化剂，其中低分子量烯烃主要与汽油范围材料反应。然后可以将这些汽油范围材料加压至在高压下操作并含有沸石低聚催化剂的第二催化反应器区域中与馏出物反应所需的压力。随后将馏出物送至加氢处理装置和产品分离区以形成润滑剂和其它成品。

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