公开(公告)号：US20110081282A1

公开(公告)日：2011-04-07

申请号：US12575334

申请日：2009-10-07

Applicant: Krishniah Parimi ,  Steven X. Song ,  Ralph E. Killen ,  Ronald K. Meeker ,  Steven A. Souers

Inventor： Krishniah Parimi ,  Steven X. Song ,  Ralph E. Killen ,  Ronald K. Meeker ,  Steven A. Souers

IPC: B01J8/04 ,  B01F3/04

CPC classification number: B01F3/0446 ,  B01F5/0646 ,  B01F5/0652 ,  B01J8/008 ,  B01J8/0453 ,  B01J8/0492 ,  B01J2208/00849 ,  B01J2219/00024

Abstract: The invention is a fluid distribution device for coupling with a fluid distribution conduit or chimney for improving the distribution of downwardly flowing poly-phase mixture including at least one gas phase and at least one liquid phase, above at least one catalyst bed of granular solid catalytic material. The fluid distribution device for receiving the liquid and gas phases has one or more openings in the top and/or upper portion of its height through which a gas phase can enter and has a gas conduit that opens to a mixing cavity within the device. The fluid distribution device further comprises one or more lateral openings for liquid ingress. The lateral opening or openings allow the liquid to enter a liquid conduit that opens to the internal mixing cavity. The mixing cavity allows intimate contact between the liquid and gas phases. Therefore the flow distribution device of the invention provides improved tolerance for tray out of levelness.

Abstract translation: 本发明是用于与流体分配导管或烟囱耦合的流体分配装置，用于改善向下流动的多相混合物的分布，包括至少一个气相和至少一个液相，至少一个颗粒状固体催化剂催化剂床上方 材料。 用于接收液相和气相的流体分配装置在其高度的顶部和/或上部具有一个或多个开口，气相可通过该开口进入，并具有通向装置内的混合腔的气体导管。 流体分配装置还包括用于液体进入的一个或多个横向开口。 侧向开口或开口允许液体进入通向内部混合腔的液体导管。 混合腔允许液相和气相之间的紧密接触。 因此，本发明的流量分配装置提供了提高盘的平坦度的容限。

公开(公告)号：US20100130800A1

公开(公告)日：2010-05-27

申请号：US12324601

申请日：2008-11-26

Applicant: Huping Luo ,  Moinuddin Ahmed ,  Krishniah Parimi ,  Bong-Kyu Chang

Inventor： Huping Luo ,  Moinuddin Ahmed ,  Krishniah Parimi ,  Bong-Kyu Chang

IPC: C07C2/64 ,  C07C7/144 ,  B01J38/56

CPC classification number: C07C7/00 ,  B01D17/045 ,  B01J31/0277 ,  B01J31/40 ,  Y02P20/584

Abstract: A process for separating an ionic liquid from hydrocarbons employs a coalescer material having a stronger affinity for the ionic liquid than the hydrocarbons. The coalescer material can be a high surface area material having a large amount of contact area to which ionic liquid droplets dispersed in the hydrocarbons may adhere. The process includes feeding a mixture comprising ionic liquid droplets dispersed in hydrocarbons to a coalescer comprising the coalescer material. The process further includes a capture step involving adhering at least a portion of the ionic liquid droplets to the coalescer material to provide captured droplets and a coalescing step involving coalescing captured droplets into coalesced droplets. After the capture and coalescence steps, the coalesced droplets are allowed to fall from the coalescer material to separate the ionic liquid from the hydrocarbons and provide a hydrocarbon effluent.

Abstract translation: 从烃中分离出离子液体的方法采用了比烃类对离子液体具有更强亲合力的聚结剂材料。 聚结器材料可以是具有大量接触面积的高表面积材料，其中分散在烃中的离子液滴可以粘附到该表面积材料上。 该方法包括将包含分散在烃中的离子液滴的混合物进料到包括聚结器材料的聚结器。 该方法还包括捕获步骤，其包括将离子液滴的至少一部分粘附到聚结器材料以提供捕获的液滴，以及聚集步骤，其将捕获的液滴聚结成聚结的液滴。 在捕获和聚结步骤之后，使聚结的液滴从聚结器材料中落下，以将离子液体与烃分离并提供烃流出物。

公开(公告)号：US20090171133A1

公开(公告)日：2009-07-02

申请号：US12003576

申请日：2007-12-28

Applicant: Huping Luo ,  Abdenour Kemoun ,  Krishniah Parimi ,  Moinuddin Ahmed ,  Bong-Kyu Chang ,  Hye-Kyung Timken

Inventor： Huping Luo ,  Abdenour Kemoun ,  Krishniah Parimi ,  Moinuddin Ahmed ,  Bong-Kyu Chang ,  Hye-Kyung Timken

IPC: C10L1/04

CPC classification number: C10G29/205 ,  B01J4/002 ,  B01J19/2465 ,  B01J2219/00047 ,  B01J2219/0011 ,  C10G50/00 ,  C10G2300/1081 ,  C10G2300/1088 ,  C10G2300/1092 ,  C10G2400/02

Abstract: Provided is a process for producing low volatility, high quality gasoline blending components which comprises recirculation of at least a portion of a recovered stream comprising primarily isoparaffins. Recirculation of the stream allows for an enhanced I/O ratio and a more cost effective process.

Abstract translation: 提供了一种生产低挥发性，高质量汽油调和组分的方法，其包括至少部分回流的主要包含异构烷烃的流的再循环。 流的再循环允许增强的I / O比和更具成本效益的过程。

公开(公告)号：US20090170688A1

公开(公告)日：2009-07-02

申请号：US12003578

申请日：2007-12-28

Applicant: Bong-Kyu Chang ,  Huping Luo ,  Moinuddin Ahmed ,  Krishniah Parimi ,  Saleh Elomari

Inventor： Bong-Kyu Chang ,  Huping Luo ,  Moinuddin Ahmed ,  Krishniah Parimi ,  Saleh Elomari

IPC: B01J38/54

CPC classification number: B01J38/56 ,  B01J31/0278 ,  B01J31/40 ,  C10G21/14 ,  C10G29/205

Abstract: A regeneration process for re-activating an ionic liquid catalyst, which is useful in a variety of reactions, especially alkylation reactions, and which has been deactivated by conjunct polymers. The process includes a reaction step and a solvent extraction step. The process comprises (a) providing the ionic liquid catalyst, wherein at least a portion of the ionic liquid catalyst is bound to conjunct polymers; and (b) reacting the ionic liquid catalyst with aluminum metal to free the conjunct polymers from the ionic liquid catalyst in a stirred reactor or a fixed reactor. The conjunct polymer is then separated from the catalyst phase by solvent extraction in a stirred extraction or packed column.

Abstract translation: 用于重新活化离子液体催化剂的再生方法，其可用于各种反应，特别是烷基化反应，并且已经通过结合聚合物失活。 该方法包括反应步骤和溶剂萃取步骤。 该方法包括（a）提供离子液体催化剂，其中至少一部分离子液体催化剂与结合聚合物结合; 和（b）使离子液体催化剂与铝金属反应，以在搅拌反应器或固定反应器中从离子液体催化剂中释放结合的聚合物。 然后在搅拌的萃取或填充柱中通过溶剂萃取将结合的聚合物与催化剂相分离。

公开(公告)号：US06589415B2

公开(公告)日：2003-07-08

申请号：US09826534

申请日：2001-04-04

Applicant: Ben D. Smith ,  Krishniah Parimi ,  Richard O. Moore, Jr.

Inventor： Ben D. Smith ,  Krishniah Parimi ,  Richard O. Moore, Jr.

IPC: C10G6510

CPC classification number: C10G65/12 ,  Y10S208/95

Abstract: The present invention is directed to a method for hydroprocessing Fischer-Tropsch products. The invention in particular relates to an integrated method for producing liquid fuels from a hydrocarbon stream provided by Fischer-Tropsch synthesis. The method involves separating the Fischer-Tropsch products into a light fraction with normal boiling points below 700° F. and including predominantly C5-20 components and a heavy fraction with normal boiling points above 650° F. and including predominantly C20+ components. The heavy fraction is subjected to hydrocracking conditions, preferably through multiple catalyst beds, to reduce the chain length. The light fraction is used as all or part of a quench fluid between each catalyst bed.

Abstract translation: 本发明涉及一种加氢处理费 - 托产品的方法。 本发明特别涉及由费 - 托合成提供的烃流产生液体燃料的综合方法。 该方法包括将费 - 托产物分离成具有低于700°F的正常沸点的轻馏分，并且主要包括C5-20组分和具有标准沸点高于650°F的重馏分，并且主要包括C20 +组分。 重馏分经受加氢裂化条件，优选通过多个催化剂床，以减少链长度。 轻馏分用作每个催化剂床之间的骤冷流体的全部或部分。

公开(公告)号：US5603904A

公开(公告)日：1997-02-18

申请号：US624195

申请日：1996-03-28

Applicant: Robert W. Bachtel ,  Yoshitomo Ohara ,  Toshio Ishizuka ,  Tsunehiko Hiraga ,  Krishniah Parimi ,  David E. Earls

Inventor： Robert W. Bachtel ,  Yoshitomo Ohara ,  Toshio Ishizuka ,  Tsunehiko Hiraga ,  Krishniah Parimi ,  David E. Earls

IPC: B01J8/00 ,  B01J8/12 ,  B01J8/44 ,  B01J19/30 ,  C10G49/00 ,  C10G49/12 ,  C10G49/14 ,  B01J8/18

CPC classification number: C10G49/14 ,  B01J19/305 ,  B01J8/008 ,  B01J8/12 ,  B01J8/44 ,  C10G49/002 ,  C10G49/12 ,  B01J2208/00884

Abstract: A light-weight and easily manufacturable catalyst support structure is provided, which allows fluid flow into a catalyst bed in uniform distribution. The support structure is formed in a cone-like shape in which the diameter enlarges upward. The support structure comprises a shell-like support member, a first mesh layer comprising thick mesh elements, and a second mesh layer having a mesh size which does not allow catalytic particulates to pass through. The first mesh layer overlays the support member, and the second mesh layer overlays the first mesh layer. The shell-like support member includes a circular bottom plate extending perpendicular to the center line of the reactor, and a side wall having a truncated cone shape which extends upward from the edge of the bottom plate. The bottom plate and the side wall are primarily made of perforated plates through which the fluid passes. A plurality of cylindrical flow guides of different diameters are provided underneath the shell-like support member.

Abstract translation: 提供了一种重量轻且容易制造的催化剂载体结构，其允许流体以均匀分布流入催化剂床。 支撑结构形成为锥形，其中直径向上扩大。 支撑结构包括壳状支撑构件，包括厚网状元件的第一网格层和具有不允许催化剂颗粒通过的网孔大小的第二网格层。 第一网格层覆盖支撑构件，并且第二网格层覆盖第一网格层。 壳状支撑构件包括垂直于反应器的中心线延伸的圆形底板，以及具有从底板的边缘向上延伸的截头圆锥形状的侧壁。 底板和侧壁主要由多孔板制成，液体通过该板。 在壳状支撑构件的下方设置有多个不同直径的圆柱形流动引导件。