公开(公告)号：US20060117386A1

公开(公告)日：2006-06-01

申请号：US11331730

申请日：2006-01-13

Applicant: Ramesh Gupta ,  Parveen Jain ,  Keith Amidon ,  Fengmin Gong ,  Srikant Vissamsetti ,  Steve Haeffele ,  Ananth Raman

Inventor： Ramesh Gupta ,  Parveen Jain ,  Keith Amidon ,  Fengmin Gong ,  Srikant Vissamsetti ,  Steve Haeffele ,  Ananth Raman

IPC: G06F12/14 ,  H04L9/00 ,  G06F11/36 ,  G06F11/00 ,  G06F11/22 ,  G06F11/30 ,  G06F11/32 ,  G06F11/34 ,  G06F12/16 ,  G06F15/18 ,  G08B23/00

CPC classification number: H04L63/1408 ,  G06F21/55 ,  H04L63/1416 ,  H04L63/1441 ,  H04L63/1458

Abstract: A method of detecting intrusions on a computer includes the step of identifying an internet protocol field range describing fields within internet protocol packets received by a computer. A connectivity range is also established which describes a distribution of network traffic received by the computer. An internet protocol field threshold and a connectivity threshold are then determined from the internet protocol field range and connectivity range, respectively. During the operation of the computer, values are calculated for the internet protocol field range and connectivity range. These values are compared to the internet protocol metric threshold and connectivity metric threshold so as to identify an intrusion on the computer.

公开(公告)号：US06846469B1

公开(公告)日：2005-01-25

申请号：US09712654

申请日：2000-11-14

Applicant: Ramesh Gupta ,  Salvatore Joseph Rossetti ,  David Charles Dankworth ,  Jeffrey L. Kaufman ,  David Lee Vannauker ,  James Philip Bailor

Inventor： Ramesh Gupta ,  Salvatore Joseph Rossetti ,  David Charles Dankworth ,  Jeffrey L. Kaufman ,  David Lee Vannauker ,  James Philip Bailor

IPC: B01J8/00 ,  B01J8/02 ,  C10G49/00 ,  B01J35/02

CPC classification number: B01J8/008 ,  B01J8/025 ,  B01J8/0278 ,  B01J2208/00707 ,  C10G49/002

Abstract: A method for extending the operating life of a fixed bed reactor for reacting a feedstock in which a feedstock is contacted with a fixed bed of catalytic material contained in the reactor.

Abstract translation: 一种用于延长固定床反应器的工作寿命的方法，用于使原料与反应器中包含的催化材料的固定床接触的原料反应。

公开(公告)号：US06692705B2

公开(公告)日：2004-02-17

申请号：US09933939

申请日：2001-08-22

Applicant: Ramesh Gupta ,  Salvatore Joseph Rossetti

Inventor： Ramesh Gupta ,  Salvatore Joseph Rossetti

IPC: B01J804

CPC classification number: C10G49/002 ,  B01J8/008 ,  B01J8/025 ,  B01J8/0278 ,  B01J2208/00707

Abstract: The invention is directed to a multi-tier bypass apparatus for extending the operating life of fixed bed reactors. The multi-tier bypass may be disposed within a fixed catalyst bed to allow any fluid feedstock to bypass successive layers of the fixed catalyst bed as they foul. The invention also relates to an improved fixed bed reactor comprising the inventive multi-tier bypass and a method for extending the operating life of a fixed bed reactor.

Abstract translation: 本发明涉及一种用于延长固定床反应器的使用寿命的多层旁路装置。 多层旁路可以设置在固定的催化剂床内，以允许任何流体原料在它们弄脏时绕过固定催化剂床的连续层。 本发明还涉及一种改进的固定床反应器，其包括本发明的多层旁路和延长固定床反应器的使用寿命的方法。

公开(公告)号：US06632350B2

公开(公告)日：2003-10-14

申请号：US09960014

申请日：2001-09-21

Applicant: Ramesh Gupta

Inventor： Ramesh Gupta

IPC: C10G6502

CPC classification number: C10G65/02

Abstract: A hydrocarbonaceous feed is hydroprocessed in a single vessel containing two reaction stages and a stripping stage. The feed is fed into the first reaction stage to produce a vapor and liquid effluent which are separated, and the liquid stripped. The stripped liquid is passed as feed into the second stage, in which it meets with fresh hydrogen to produce a hydroprocessed liquid product and a hydrogen-rich vapor. The vapor is passed into the first stage, to provide the hydrogen for that stage. The use of a single vessel provides an efficient and economical addition to, or replacement for, a vessel for an existing hydroprocessing facility.

Abstract translation: 烃类进料在含有两个反应阶段和汽提阶段的单个容器中进行加氢处理。 将进料进料到第一反应阶段以产生蒸汽和液体流出物，将其分离，并将液体汽提。 汽提的液体作为进料通入第二阶段，其中它与新鲜的氢气接触以产生加氢处理液体产物和富氢蒸气。 蒸汽进入第一阶段，为该阶段提供氢气。 使用单个容器为现有的加氢处理设备提供有效和经济的补充或代替船只。

公开(公告)号：US06579443B1

公开(公告)日：2003-06-17

申请号：US09456139

申请日：1999-12-07

Applicant: Larry L. Iaccino ,  Edward S. Ellis ,  Ramesh Gupta ,  Brenda A. Raich

Inventor： Larry L. Iaccino ,  Edward S. Ellis ,  Ramesh Gupta ,  Brenda A. Raich

IPC: C10G4500

CPC classification number: C10G49/002 ,  C10G45/00

Abstract: A process for upgrading a liquid petroleum or chemical stream wherein said feedstream flows countercurrent to the flow of a treat gas, such as a hydrogen-containing gas, in at least one reaction zone. The feedstream is treated so that it is substantially free of particulate matter and foulant precursors.

Abstract translation: 一种用于升级液体石油或化学物流的方法，其中所述原料流在至少一个反应区中与处理气体（例如含氢气体）的流动逆流流动。 处理进料流使其基本上不含颗粒物质和污垢前体。

公开(公告)号：US6054041A

公开(公告)日：2000-04-25

申请号：US73412

申请日：1998-05-06

Applicant: Edward S. Ellis ,  William Ernest Lewis ,  David C. Dankworth ,  Ramesh Gupta

Inventor： Edward S. Ellis ,  William Ernest Lewis ,  David C. Dankworth ,  Ramesh Gupta

IPC: C10G65/04 ,  C10G45/02 ,  C10G65/00 ,  C10G65/02 ,  C10G45/00

CPC classification number: C10G65/00

Abstract: A hydroprocessing process includes two cocurrent flow liquid reaction stages and one vapor stage, in which feed components are catalytically hydroprocessed by reacting with hydrogen. The liquid stages both produce a liquid and a hydrogen-rich vapor effluent, with most of the hydroprocessing accomplished in the first stage. The first stage vapor is also hydroprocessed. The hydroprocessed vapor and second stage vapor are cooled to condense and recover additional product liquid and produce an uncondensed hydrogen-rich vapor. After cleanup to remove contaminants, the hydrogen-rich vapor is recycled back into the first stage as treat gas. Fresh hydrogen is introduced into the second stage. This is useful for hydrotreating heteroatom-containing hydrocarbons.

Abstract translation: 加氢处理方法包括两个并流流动液体反应阶段和一个蒸气阶段，其中进料组分通过与氢反应催化加氢处理。 液相都产生液体和富氢蒸汽流出物，大部分加氢处理在第一阶段完成。 第一级蒸气也被加氢处理。 将加氢蒸气和第二级蒸气冷却以冷凝并回收另外的产物液体并产生未冷凝的富氢蒸汽。 净化后清除污染物，富氢蒸汽再循环回第一阶段作为处理气体。 新鲜氢气被引入第二阶段。 这对于加氢处理含杂原子的烃是有用的。

公开(公告)号：US5942197A

公开(公告)日：1999-08-24

申请号：US885788

申请日：1997-06-30

Applicant: Ramesh Gupta ,  Jeffrey W. Frederick ,  Edward S. Ellis ,  David C. Dankworth ,  Dimitrios M. Tsangaris

Inventor： Ramesh Gupta ,  Jeffrey W. Frederick ,  Edward S. Ellis ,  David C. Dankworth ,  Dimitrios M. Tsangaris

IPC: B01D3/16 ,  B01J8/04 ,  B01J19/24 ,  C10G45/00 ,  C10G45/44 ,  C10G47/00 ,  C10G49/00 ,  C10G65/02

CPC classification number: B01D3/16 ,  B01J8/0453 ,  B01J8/0492 ,  C10G49/002

Abstract: A reactor is provided for reacting a liquid with a treat gas in the presence of a catalyst, the reactor comprising a continuous wall enclosing a first reaction zone, wherein the first reaction zone includes a catalyst for causing a desired reaction between the liquid and the treat gas; a liquid inlet above the first reaction zone for allowing a portion of the liquid to enter the reactor; a gas inlet below the first reaction zone for allowing a portion of the treat gas to enter the reactor; a liquid outlet below the first reaction zone for allowing a reacted portion of the liquid to exit the reactor; a gas outlet above the first reaction zone for allowing a portion of the treat gas to exit the reactor; and a gas bypass device in the first reaction zone for allowing a portion of the treat gas to bypass a portion of the first reaction zone, the gas bypass device including a gas bypass regulating device for regulating the amount of treat gas which bypasses the first reaction zone. In a preferred embodiment, a plurality of reaction zones are present, and a liquid distribution tray is disposed above each reaction zone. Preferably, the gas bypass device creates a hydrostatic seal with the liquid accumulating in the distribution tray so that the timing and extent of gas bypass is self-regulating based on predefined flooding conditions.

Abstract translation: 提供反应器用于在催化剂存在下使液体与处理气体反应，所述反应器包括包围第一反应区的连续壁，其中第一反应区包括用于在液体和处理之间引起所需反应的催化剂 加油站; 在第一反应区上方的液体入口，用于使一部分液体进入反应器; 位于第一反应区下方的气体入口，用于使一部分处理气体进入反应器; 位于第一反应区下方的液体出口，用于允许液体的反应部分离开反应器; 在第一反应区上方的气体出口，用于允许一部分处理气体离开反应器; 以及在所述第一反应区域中的气体旁通装置，用于允许所述处理气体的一部分绕过所述第一反应区域的一部分，所述气体旁通装置包括用于调节绕过所述第一反应的处理气体的量的气体旁路调节装置 区。 在优选的实施方案中，存在多个反应区，并且在每个反应区上方设置液体分配塔。 优选地，气体旁通装置产生液体密封，液体积聚在分配盘中，使得基于预定的淹水条件，气体旁路的时间和程度是自调节的。

公开(公告)号：US5871635A

公开(公告)日：1999-02-16

申请号：US753857

申请日：1996-12-03

Applicant: Ramesh Gupta ,  Edward S. Ellis ,  William Ernest Lewis

Inventor： Ramesh Gupta ,  Edward S. Ellis ,  William Ernest Lewis

IPC: C10G45/00 ,  C10G45/04 ,  C10G45/12 ,  C10G47/00 ,  C10G47/16

CPC classification number: C10G45/12 ,  C10G45/00 ,  C10G45/04 ,  C10G47/00 ,  C10G47/16

Abstract: Hydrocarbonaceous feedstocks admixed with a flow-through catalyst and hydrogen are hydroprocessed in a hydroprocessing reactor containing a captive hydroprocessing catalyst. The flow-through catalyst is continually withdrawn with the hydroprocessed feed from the hydroprocessing reactor. The flow-through catalyst may be an FCC, hydrocracking, isomerization or ring-opening catalyst. In a preferred embodiment, the captive hydroprocessing catalyst contains Co, Ni and/or Mo on an alumina base and the flow-through catalyst is an FCC zeolitic catalyst which is withdrawn with the hydroprocessed feed from the hydroprocessing reactor and then sent to an FCC unit.

Abstract translation: 与流通催化剂和氢气混合的烃类原料在含有捕获加氢处理催化剂的加氢处理反应器中进行加氢处理。 使用加氢处理反应器的加氢进料连续抽出流通催化剂。 流通催化剂可以是FCC，加氢裂化，异构化或开环催化剂。 在优选的实施方案中，捕获加氢处理催化剂在氧化铝基底上含有Co，Ni和/或Mo，并且流通催化剂是FCC沸石催化剂，其由来自加氢处理反应器的加氢处理进料排出，然后送至FCC装置 。

公开(公告)号：US5770044A

公开(公告)日：1998-06-23

申请号：US702347

申请日：1996-08-23

Applicant: Edward S. Ellis ,  Ramesh Gupta ,  Martin G. Bienstock

Inventor： Edward S. Ellis ,  Ramesh Gupta ,  Martin G. Bienstock

IPC: C10G7/00 ,  C10G11/05 ,  C10G11/18 ,  C10G35/04 ,  C10G45/00 ,  C10G49/04 ,  C10G69/00 ,  C10G69/04 ,  C10G69/06 ,  C10G69/08 ,  C10G51/02

CPC classification number: C10G69/00 ,  C10G69/04 ,  C10G69/06

Abstract: Disclosed is a catalytic cracking process which includes more than one catalytic cracking reaction step. The process integrates a hydroprocessing step between the catalytic cracking reaction steps in order to maximize olefins production, distillate quality and octane level of the overall cracked product. Preferably, the hydroprocessing step is included between the reaction stages, and a portion of the hydroprocessed products, i.e., a naphtha and mid distillate fraction, is combined with cracked product for further separation and hydroprocessing. It is also preferred that the first catalytic cracking reaction step be a short contact time reaction step.

Abstract translation: 公开了一种催化裂解方法，其包括多于一个催化裂化反应步骤。 该方法将催化裂化反应步骤之间的加氢处理步骤整合，以使烯烃的产生最大化，馏出物质量和整个裂解产物的辛烷值达到最大。 优选地，加氢处理步骤包括在反应阶段之间，并且一部分加氢处理产物，即石脑油和中间馏分馏分与裂化产物组合用于进一步分离和加氢处理。 还优选的是，第一催化裂化反应步骤是短接触时间反应步骤。

公开(公告)号：US5720872A

公开(公告)日：1998-02-24

申请号：US775638

申请日：1996-12-31

Applicant: Ramesh Gupta

Inventor： Ramesh Gupta

IPC: C10G65/02 ,  C10G45/04 ,  C10G45/08 ,  C10G45/10 ,  C10G45/52 ,  C10G47/16 ,  C10G47/18 ,  C10G65/04 ,  C10G51/02

CPC classification number: C10G65/04

Abstract: A process for hydroprocessing liquid petroleum and chemical streams in two or more hydroprocessing stages, which stages are in separate reaction vessels and wherein each reaction stage contains a bed of hydroprocessing catalyst. The liquid product from the first reaction stage is sent to a stripping stage and stripped of H.sub.2 S, NH.sub.3 and other dissolved gases. The stripped product stream is then sent to the next downstream reaction stage, the product from which is also stripped of dissolved gases and sent to the next downstream reaction stage until the last reaction stage, the liquid product of which is stripped of dissolved gases and collected or passed on for further processing. The flow of treat gas is in a direction opposite the direction in which the reaction stages are staged for the flow of liquid. Each stripping stage is a separate stage, but all stages are contained in the same stripper vessel.

Abstract translation: 一种用于在两个或多个加氢处理阶段中加氢处理液体石油和化学物流的方法，这些阶段在单独的反应容器中，并且其中每个反应阶段包含加氢处理催化剂床。 将来自第一反应阶段的液体产物送至汽提阶段并汽提H2S，NH3和其他溶解气体。 然后将汽提的产物流送至下一个下游反应阶段，将产物从其中除去溶解的气体，并送至下一个下游反应阶段，直到最后一个反应阶段，其液体产物被汽提出溶解的气体并收集 或转交进一步处理。 处理气体的流动方向与反应级分为液体流动方向相反。 每个汽提阶段是一个单独的阶段，但是所有阶段都包含在相同的汽提塔中。