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1. 发明授权

US5059302A Method and apparatus for the fluid catalytic cracking of hydrocarbon feed employing a separable mixture of catalyst and sorbent particles 失效
标题翻译：使用催化剂和吸附剂颗粒的可分离混合物进行烃进料的流化催化裂化的方法和装置
公开(公告)号：US5059302A
公开(公告)日：1991-10-22
申请号：US515540
申请日：1990-04-26
申请人： Harold N. Weinberg , W. Benedict Johnson , Michael F. Raterman , Barry K. Speronello , William J. Reagan , Larry G. Sherman
发明人： Harold N. Weinberg , W. Benedict Johnson , Michael F. Raterman , Barry K. Speronello , William J. Reagan , Larry G. Sherman
IPC分类号： C10G11/18
CPC分类号： C10G11/18
摘要： The present invention features the use of a particulate sorbent and a particulate FCC catalyst, which are physically separable, sequentially in the same FCC riser, followed by separation of commingled spent catalyst and sorbent particles from vapors, and the subsequent primary partial regeneration and heat up of spent sorbent particles and catalysts particles in an oxygen deficient burning zone, followed by physical separation of partially regenerated catalyst and sorbent particles, preferably using a cyclonic classifier to effect the separation. This is followed by secondary regeneration of the resulting segregated partially regenerated sorbent and catalyst streams in oxygen rich combustion zones to fully regenerate sorbent and catalyst particles.
摘要翻译：本发明的特征在于使用颗粒状吸附剂和颗粒FCC催化剂，其在相同的FCC提升管中依次物理分离，然后从蒸气中分离混合的废催化剂和吸附剂颗粒，随后的主要部分再生和加热的废吸附剂颗粒和催化剂颗粒在缺氧燃烧区中，然后物理分离部分再生的催化剂和吸附剂颗粒，优选使用旋风分级器来实现分离。随后在富氧燃烧区中二次再生生成的偏析的部分再生的吸附剂和催化剂流，以完全再生吸附剂和催化剂颗粒。

2. 发明授权

US5196172A Apparatus for the fluid catalytic cracking of hydrocarbon feed employing a separable mixture of catalyst and sorbent particles 失效
标题翻译：使用催化剂和吸附剂颗粒的可分离混合物进行烃进料流化催化裂化的装置
公开(公告)号：US5196172A
公开(公告)日：1993-03-23
申请号：US724235
申请日：1991-07-01
申请人： Harold N. Weinberg , W. Benedict Johnson , Michael F. Raterman , Barry K. Speronello , William J. Reagan , Larry G. Sherman
发明人： Harold N. Weinberg , W. Benedict Johnson , Michael F. Raterman , Barry K. Speronello , William J. Reagan , Larry G. Sherman
IPC分类号： C10G11/18
CPC分类号： C10G11/18
摘要： The present invention features the use of a particulate sorbent and a particulate FCC catalyst, which are physically separable, sequentially in the same FCC riser, followed by separation of commingled spent catalyst and sorbent particles from vapors, and the subsequent primary partial regeneration and heat up of spent sorbent particles and catalysts particles in an oxygen deficient burning zone, followed by physical separation of partially regenerated catalyst and sorbent particles, preferably using a cyclonic classifier to effect the separation. This is followed by secondary regeneration of the resulting segregated partially regenerated sorbent and catalyst streams in oxygen rich combustion zones to fully regenerate sorbent and catalyst particles.
摘要翻译：本发明的特征在于使用颗粒状吸附剂和颗粒FCC催化剂，其在相同的FCC提升管中依次物理分离，然后从蒸气中分离混合的废催化剂和吸附剂颗粒，随后的主要部分再生和加热的废吸附剂颗粒和催化剂颗粒在缺氧燃烧区中，然后物理分离部分再生的催化剂和吸附剂颗粒，优选使用旋风分级器来实现分离。其次是在富氧燃烧区域中所产生的分离的部分再生的吸附剂和催化剂流的二次再生，以完全再生吸附剂和催化剂颗粒。

3. 发明授权

US08951315B2 Method of injecting fuel into a gasifier via pressurization 有权
标题翻译：通过加压将燃料喷入气化器的方法
公开(公告)号：US08951315B2
公开(公告)日：2015-02-10
申请号：US12590158
申请日：2009-11-03
申请人： Michael F. Raterman
发明人： Michael F. Raterman
IPC分类号： C01B3/36 , C10J3/50 , B01J8/00 , B01J8/06 , C10J3/72
CPC分类号： C10J3/506 , B01J8/002 , B01J8/0035 , B01J8/062 , B01J2208/00752 , C10J3/723 , C10J2200/152 , C10J2300/0916 , C10J2300/093 , C10J2300/0933 , C10J2300/0936 , C10J2300/0943 , C10J2300/1693
摘要： The present invention relates to an improved gasifier injection system. In particular, the present invention provides an improved apparatus and operating scheme to improve the control flow of solid particulates in a multi-burner gasifier. The system also provides for integrated flow control and emergency shutoff in the case of abnormal operating conditions or unexpected backflow of the process burners. This improved design simplifies the mechanical systems required for large multi-burner gasifiers thus providing a more reliable and compact gasifier feed system. In preferred embodiments, the gasifier hydrocarbon feed is substantially in a solid particulate state and is preferably comprised of coal, petrochemical coke, and/or solid biomass.
摘要翻译：本发明涉及一种改进的气化器喷射系统。特别地，本发明提供改进的设备和操作方案，以改善多燃烧器气化器中的固体微粒的控制流程。在异常操作条件或过程燃烧器意外回流的情况下，该系统还提供集成流量控制和紧急关闭。这种改进的设计简化了大型多燃烧器气化器所需的机械系统，从而提供了更可靠和更紧凑的气化器进料系统。在优选的实施方案中，气化器烃进料基本上是固体颗粒状态，优选由煤，石化焦炭和/或固体生物质组成。

4. 发明申请

US20120279824A1 Optimizing Feed Mixer Performance In A Paraffinic Froth Treatment Process 有权
标题翻译：优化饲料混合器在石蜡泡沫处理过程中的性能
公开(公告)号：US20120279824A1
公开(公告)日：2012-11-08
申请号：US13554792
申请日：2012-07-20
申请人： Arun K. Sharma , Michael F. Raterman
发明人： Arun K. Sharma , Michael F. Raterman
IPC分类号： C10C3/08 , G06F19/00
CPC分类号： C10G1/045 , C10G1/047
摘要： The invention relates to improved bitumen recovery processes and systems. One process provides for operation of a bitumen froth treatment plant at optimum shear rates in the feed pipe carrying the bitumen froth to the froth settling unit. Another process provides for optimizing the design of a bitumen froth treatment plant by optimizing the diameter of the feed pipe to impart an optimum shear rate to the bitumen froth mixture and further optimizing the volume of the feed pipe to impart an optimum residence time for the bitumen froth stream in the feed pipe. An optimal plant design is also disclosed, the plant including optimal diameter and volume of the feed pipe.
摘要翻译：本发明涉及改进的沥青回收方法和系统。一个方法提供了在将沥青泡沫运送到泡沫沉降装置的进料管中以最佳剪切速率操作沥青泡沫处理装置。另一个方法通过优化进料管的直径来优化沥青泡沫处理设备的设计，以赋予沥青混合物最佳的剪切速率并且进一步优化进料管的体积以赋予沥青最佳的停留时间进料管中的泡沫流。还公开了最佳设备设计，该设备包括进料管的最佳直径和体积。

5. 发明申请

US20090321323A1 Optimizing Heavy Oil Recovery Processes Using Electrostatic Desalters 有权
标题翻译：使用静电脱盐剂优化重油回收过程
公开(公告)号：US20090321323A1
公开(公告)日：2009-12-31
申请号：US12464724
申请日：2009-05-12
申请人： Arun K. Sharma , Michael F. Raterman
发明人： Arun K. Sharma , Michael F. Raterman
IPC分类号： C10G1/04 , C10C3/08
CPC分类号： C10G1/047 , C10G1/002 , C10G1/045 , C10G33/02 , C10G2300/206 , C10G2300/4081 , C10G2300/44 , C10G2300/805
摘要： The invention relates to improved bitumen recovery processes and systems. The process may include providing a bitumen froth feed stream, separating the stream in a froth separation unit to produce a diluted bitumen stream, treating the diluted bitumen stream in an electrostatic desalter to produce a treated bitumen stream, and separating the treated bitumen stream into a solvent recycle stream and a bitumen product stream. The system may include a combined AC/DC desalter with a control unit for optimizing the treatment process to produce a product bitumen stream using less solvent and smaller separators than conventional bitumen froth treatment plants and processes.
摘要翻译：本发明涉及改进的沥青回收方法和系统。该方法可以包括提供沥青泡沫进料流，将泡沫分离单元中的物流分离以产生稀释的沥青料流，在静电脱盐器中处理稀释的沥青料流以产生经处理的沥青料流，并将处理的沥青料流分离成溶剂循环流和沥青产物流。该系统可以包括具有控制单元的组合AC / DC脱盐器，其用于优化处理过程以使用比常规沥青处理装置和工艺更少的溶剂和更小的分离器产生产物沥青流。

6. 发明授权

US5198397A Two-stage fluid bed regeneration of catalyst with shared dilute phase 失效
标题翻译：具有共同稀释相的催化剂的两阶段流化床再生
公开(公告)号：US5198397A
公开(公告)日：1993-03-30
申请号：US797678
申请日：1991-11-25
申请人： Michael F. Raterman
发明人： Michael F. Raterman
IPC分类号： B01J8/26 , C10G11/18
CPC分类号： B01J8/26 , C10G11/182
摘要： A process and apparatus for multi-stage fluidized bed regeneration of spent FCC catalyst in a single vessel. At least two isolated relatively dense phase fluidized beds are disposed beneath a common dilute phase region. Spent catalyst discharged into a primary regeneration stage is regenerated to produce flue gas and partially regenerated catalyst, which preferably overflows into the second stage. Flue gas and entrained catalyst from each fluidized bed are processed in two trains of separation means, preferably cyclones. The inlets of each train are disposed above the isolated fluidized beds, and are effectively separated although sharing an open dilute phase region.
摘要翻译：用于在单个容器中废催化裂化催化剂多阶段流化床再生的方法和装置。至少两个分离的相对致密的相流化床设置在公共稀相区域的下方。排出到初级再生阶段的废催化剂被再生，以产生烟气和部分再生的催化剂，其优选地溢出到第二阶段。来自每个流化床的烟气和夹带的催化剂在两个分离装置的列车中进行处理，优选旋风分离器。每个列车的入口设置在分离的流化床之上，并且有效地分离，尽管共享开放的稀相区。

7. 发明授权

US5183480A Apparatus and method for collecting particulates by electrostatic precipitation 失效
标题翻译：通过静电沉淀收集颗粒的装置和方法
公开(公告)号：US5183480A
公开(公告)日：1993-02-02
申请号：US783472
申请日：1991-10-28
申请人： Michael F. Raterman , Michael D. Thiel
发明人： Michael F. Raterman , Michael D. Thiel
IPC分类号： B03C3/51
CPC分类号： B03C3/51
摘要： An electrostatic precipitator apparatus and method which minimizes reentrainment of collected particles during their removal from the collecting electrode by use of a collecting system including concentric semi-tubes which are configurable from a position exposed to gas flow to one protected therefrom.
摘要翻译：一种静电除尘器装置和方法，其使收集的颗粒在从收集电极移除期间的再吸入最小化，所述收集系统包括可从暴露于气流的位置配置到其中的一个被保护的同心半管。

8. 发明申请

US20110289842A1 Corrosion Resistant Gasifier Components 有权
标题翻译：耐腐蚀气化器组件
公开(公告)号：US20110289842A1
公开(公告)日：2011-12-01
申请号：US13053986
申请日：2011-03-22
申请人： Paul D. Oldenburg , Michael F. Raterman
发明人： Paul D. Oldenburg , Michael F. Raterman
IPC分类号： B01J7/00
CPC分类号： C10J3/485 , C10J3/506 , C10J3/74 , C10J3/76 , C10J2300/0916 , C10J2300/093 , C10J2300/0956 , C10J2300/0959
摘要： The present invention relates to an improved gasifier reactor design. In particular, the present invention relates to improved design of gasifier reactor faceplates, gasifier reactor walls, gasifier reactor cooling tubes, and gasifier reactor walls with integrated cooling channels. The present invention utilizes aluminum nitride and/or aluminum nitride/metal composite materials which promote many benefits to the present design herein, including improved corrosion and erosion resistively as compared to high alloy metal materials.
摘要翻译：本发明涉及一种改进的气化器反应器设计。特别地，本发明涉及气化器反应器面板，气化器反应器壁，气化器反应器冷却管和具有集成冷却通道的气化器反应器壁的改进设计。本发明使用氮化铝和/或氮化铝/金属复合材料，其对本文的本设计有很多益处，包括与高合金金属材料相比可以改善腐蚀和侵蚀性。

9. 发明申请

US20100155298A1 Process for producing a high stability desulfurized heavy oils stream 有权
标题翻译：生产高稳定性脱硫重油料流的方法
公开(公告)号：US20100155298A1
公开(公告)日：2010-06-24
申请号：US12590157
申请日：2009-11-03
申请人： Michael F. Raterman , Daniel P. Leta , Walter D. Vann , Roby Bearden, JR.
发明人： Michael F. Raterman , Daniel P. Leta , Walter D. Vann , Roby Bearden, JR.
IPC分类号： C10G67/00
CPC分类号： C10G19/00 , C10G29/04 , C10G29/06 , C10G29/16 , C10G45/02
摘要： The present invention relates to a process for desulfurizing heavy oil feedstreams with alkali metal compounds and improving the compatibility of the to stream components in either the feed stream, an intermediate product stream, and/or the reaction product stream in the desulfurization process. The present invention utilizes a high stability aromatic-containing stream that is preferably added to the heavy oil prior to reaction with the alkali metal compounds. The resulting stream resists precipitation of reaction solids in the desulfurization reactors. Even more preferably, the desulfurization system employs at least two desulfurization reactors in series flow wherein the high stability aromatic-containing stream is contacted with the reaction product from the first reactor prior to the second reactor, wherein the first reactor can be operated at a higher severity than without the use of the high stability aromatic-containing component stream.
摘要翻译：本发明涉及一种使用碱金属化合物脱硫重油进料流并提高脱硫过程中进料流，中间产物流和/或反应产物流中的流组分的相容性的方法。本发明利用在与碱金属化合物反应之前优选加入到重油中的高稳定性含芳族物流。所得流阻止脱硫反应器中反应固体的沉淀。甚至更优选地，脱硫系统使用至少两个串联流量的脱硫反应器，其中高稳定性含芳族物流与第二反应器之前的来自第一反应器的反应产物接触，其中第一反应器可以在较高严重程度高于不使用高稳定性的含芳烃的组分流。

10. 发明授权

US5643537A FCC process and apparatus with contained vortex third stage separator 失效
标题翻译： FCC工艺和装置含有涡流第三级分离器
公开(公告)号：US5643537A
公开(公告)日：1997-07-01
申请号：US533135
申请日：1995-09-26
申请人： Michael F. Raterman , Christopher G. Smalley
发明人： Michael F. Raterman , Christopher G. Smalley
IPC分类号： B04C9/00 , B01D45/12 , B01J8/00 , B04C5/00 , B04C5/081 , B04C5/14 , B04C5/187 , B04C5/28 , C10G11/18 , F27D17/00 , F27B15/09
CPC分类号： B01D45/12 , B01J8/0055 , B04C5/081 , B04C5/14 , B04C5/187 , B04C5/28 , C10G11/18
摘要： Vertical, small diameter cyclones are disclosed. Gas and fines are added tangentially or axially around a clean vapor outlet tube in a cylindrical cyclone. A vortex of solids and some gas passes into a contiguous and axially aligned cylindrical vortex containment means from which solids are withdrawn via a vertical slot in a sidewall of the containment means. 0-5 micron particle removal is enhanced. An FCC process uses the cyclones as a third stage separator.
摘要翻译：公开了垂直的，小直径的旋风分离器。气体和细屑在圆柱形旋风分离器中的干净蒸气出口管周围切向或轴向加入。固体和一些气体的涡流进入连续和轴向对准的圆柱形涡流容纳装置，固体通过容器装置的侧壁中的垂直槽排出。 0-5微米颗粒去除增强。 FCC工艺使用旋风分离器作为第三级分离器。

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