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公开(公告)号：US07972482B2
公开(公告)日：2011-07-05
申请号：US12785758
申请日：2010-05-24
Applicant: Robert David Strack , John R. Messinger
Inventor： Robert David Strack , John R. Messinger
IPC: C10B27/00
Abstract: A method is disclosed for treating the effluent from a hydrocarbon pyrolysis unit without employing a primary fractionator. The method comprises passing the gaseous effluent to at least one primary heat exchanger, thereby cooling the gaseous effluent and generating high pressure steam, and then cooling the gaseous effluent to a temperature at which tar, formed by reactions among constituents of the effluent, condenses. The gaseous effluent and the condensed tar are fed to at least one knock-out drum, whereby the tar is separated from the gaseous effluent. The gaseous effluent is then further cooled to condense a pyrolysis gasoline fraction from the effluent and to reduce the temperature of the effluent to a point at which it can be compressed efficiently. The condensed pyrolysis gasoline fraction is separated from the effluent and then distilled so as to reduce its final boiling point.
Abstract translation: 公开了一种用于处理来自烃热解单元的流出物而不使用初级分馏器的方法。 该方法包括将气态流出物通入至少一个主要热交换器，从而冷却气态流出物并产生高压蒸汽，然后将气态流出物冷却至通过流出物组分之间的反应形成的焦油冷凝的温度。 将气态流出物和冷凝的焦油进料至至少一个分离鼓，由此将焦油与气态流出物分离。 然后气态流出物被进一步冷却以从流出物中冷凝裂解汽油馏分，并将流出物的温度降低到有效压缩的点。 将冷凝的热解汽油馏分与流出物分离，然后蒸馏，以降低其最终沸点。
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公开(公告)号：US07780843B2
公开(公告)日：2010-08-24
申请号：US11178025
申请日：2005-07-08
Applicant: Robert David Strack , David R. Spicer , George Stephens , James Mitchell Frye
Inventor： Robert David Strack , David R. Spicer , George Stephens , James Mitchell Frye
CPC classification number: C10G9/002 , C10G2300/1033 , C10G2300/1044 , C10G2300/1051 , C10G2300/1074 , C10G2300/44
Abstract: A method is provided for treating the effluent from a hydrocarbon pyrolysis unit processing heavier than naphtha feeds to recover heat and remove tar therefrom. The method comprises passing the gaseous effluent to at least one primary transfer line heat exchanger, thereby cooling the gaseous effluent and generating superheated steam. Thereafter, the gaseous effluent is passed through at least one secondary transfer line heat exchanger having a heat exchange surface with a liquid coating on said surface, thereby further cooling the remainder of the gaseous effluent to a temperature at which tar, formed by the pyrolysis process, condenses. The condensed tar is then removed from the gaseous effluent in at least one knock-out drum. An apparatus for carrying out the method is also provided.
Abstract translation: 提供一种处理来自比石脑油进料重的烃热解单元的流出物的方法以回收热量并从其中除去焦油。 该方法包括将气态流出物送至至少一个一次传输线热交换器，从而冷却气态流出物并产生过热蒸汽。 此后，气态流出物通过至少一个具有在所述表面上具有液体涂层的热交换表面的二次传输线热交换器，从而进一步将剩余的气态流出物冷却至通过热解过程形成的焦油的温度 ，冷凝。 然后在至少一个分离鼓中从气态流出物中除去冷凝的焦油。 还提供了一种用于执行该方法的装置。
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公开(公告)号：US07578929B2
公开(公告)日：2009-08-25
申请号：US11487780
申请日：2006-07-17
Applicant: Richard C. Stell , Arthur R. Dinicolantonio , James Mitchell Frye , David B. Spicer , James N. McCoy , Robert David Strack
Inventor： Richard C. Stell , Arthur R. Dinicolantonio , James Mitchell Frye , David B. Spicer , James N. McCoy , Robert David Strack
IPC: C10G9/36
Abstract: A process for feeding or cracking heavy hydrocarbon feedstock containing non-volatile hydrocarbons comprising: heating the heavy hydrocarbon feedstock, mixing the heavy hydrocarbon feedstock with a fluid and/or a primary dilution steam stream to form a mixture, flashing the mixture to form a vapor phase and a liquid phase, and varying the amount of the fluid and/or the primary dilution steam stream mixed with the heavy hydrocarbon feedstock in accordance with at least one selected operating parameter of the process, such as the temperature of the flash stream before entering the flash drum.
Abstract translation: 一种用于进料或裂解含有非挥发性烃的重质烃原料的方法，包括：加热重质烃原料，将重质烃原料与流体和/或初级稀释蒸汽流混合以形成混合物，使混合物闪蒸以形成蒸汽 相和液相，并根据过程的至少一个选定的操作参数，例如在进入之前的闪蒸流的温度，改变与重质烃原料混合的流体和/或初级稀释蒸汽流的量 闪光鼓。
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公开(公告)号：US07465388B2
公开(公告)日：2008-12-16
申请号：US11178158
申请日：2005-07-08
Applicant: Robert David Strack , John R. Messinger
Inventor： Robert David Strack , John R. Messinger
IPC: C10G9/36
CPC classification number: C10G9/002 , C10G2300/301 , C10G2400/02
Abstract: A method is disclosed for treating the effluent from a hydrocarbon pyrolysis process unit to recover heat and remove tar therefrom. The method comprises passing the gaseous effluent to at least one primary heat exchanger, thereby cooling the gaseous effluent and generating high pressure steam. Thereafter, the gaseous effluent is passed through at least one secondary heat exchanger having a heat exchange surface maintained at a temperature such that part of the gaseous effluent condenses to form in situ a liquid coating on said surface, thereby further cooling the remainder of the gaseous effluent to a temperature at which tar, formed by the pyrolysis process, condenses. The condensed tar is then removed from the gaseous effluent in at least one knock-out drum.
Abstract translation: 公开了一种用于处理来自烃热解过程单元的流出物以回收热量并从其中除去焦油的方法。 该方法包括将气态流出物通入至少一个主要热交换器，从而冷却气态流出物并产生高压蒸汽。 此后，气态流出物通过至少一个二次热交换器，其具有保持在一定温度下的热交换表面，使得部分气态流出物冷凝以在所述表面上原位形成液体涂层，从而进一步冷却气态的其余部分 流出物达到通过热解过程形成的焦油的温度。 然后在至少一个分离鼓中从气态流出物中除去冷凝的焦油。
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公开(公告)号：US07138047B2
公开(公告)日：2006-11-21
申请号：US10188461
申请日：2002-07-03
Applicant: Richard C. Stell , Arthur R. DiNicolantonio , James Mitchell Frye , David B. Spicer , James N. McCoy , Robert David Strack
Inventor： Richard C. Stell , Arthur R. DiNicolantonio , James Mitchell Frye , David B. Spicer , James N. McCoy , Robert David Strack
IPC: C10G9/36
Abstract: A process for feeding or cracking heavy hydrocarbon feedstock containing non-volatile hydrocarbons comprising: heating the heavy hydrocarbon feedstock, mixing the heavy hydrocarbon feedstock with a fluid and/or a primary dilution steam stream to form a mixture, flashing the mixture to form a vapor phase and a liquid phase, and varying the amount of the fluid and/or the primary dilution steam stream mixed with the heavy hydrocarbon feedstock in accordance with at least one selected operating parameter of the process, such as the temperature of the flash stream before entering the flash drum.
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Patent Agency Ranking
公开(公告)号：US07981374B2
公开(公告)日：2011-07-19
申请号：US12272292
申请日：2008-11-17
Applicant: Robert David Strack , John R. Messinger
Inventor： Robert David Strack , John R. Messinger
CPC classification number: C10G9/002 , C10G2300/301 , C10G2400/02
Abstract: A method is disclosed for treating the effluent from a hydrocarbon pyrolysis process unit to recover heat and remove tar therefrom. The method comprises passing the gaseous effluent to at least one primary heat exchanger, thereby cooling the gaseous effluent and generating high pressure steam. Thereafter, the gaseous effluent is passed through at least one secondary heat exchanger having a heat exchange surface maintained at a temperature such that part of the gaseous effluent condenses to form in situ a liquid coating on said surface, thereby further cooling the remainder of the gaseous effluent to a temperature at which tar, formed by the pyrolysis process, condenses. The condensed tar is then removed from the gaseous effluent in at least one knock-out drum.
Abstract translation: 公开了一种用于处理来自烃热解过程单元的流出物以回收热量并从其中除去焦油的方法。 该方法包括将气态流出物通入至少一个主要热交换器，从而冷却气态流出物并产生高压蒸汽。 此后，气态流出物通过至少一个二次热交换器，其具有保持在一定温度下的热交换表面，使得部分气态流出物冷凝以在所述表面上原位形成液体涂层，从而进一步冷却气态的其余部分 流出物达到通过热解过程形成的焦油的温度。 然后在至少一个分离鼓中从气态流出物中除去冷凝的焦油。
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公开(公告)号：US07763162B2
公开(公告)日：2010-07-27
申请号：US11177075
申请日：2005-07-08
Applicant: Robert David Strack
Inventor： Robert David Strack
CPC classification number: C10G9/002
Abstract: A method is disclosed for treating the effluent from a hydrocarbon pyrolysis unit processing heavier than naphtha feeds to recover heat and remove tar therefrom. The method comprises passing the gaseous effluent to at least one primary heat exchanger, thereby cooling the gaseous effluent and generating superheated steam. Thereafter, the gaseous effluent is passed through at least one secondary heat exchanger having a heat exchange surface maintained at a temperature such that part of the gaseous effluent condenses to form a liquid coating on said surface, thereby further cooling the remainder of the gaseous effluent to a temperature at which tar, formed by the pyrolysis process, condenses. The condensed tar is then removed from the gaseous effluent in at least one knock-out drum. An apparatus for carrying out this method is also provided.
Abstract translation: 公开了一种处理来自比石脑油进料重的烃热解单元的流出物回收热量并从其中除去焦油的方法。 该方法包括将气态流出物送至至少一个主要热交换器，从而冷却气态流出物并产生过热蒸汽。 此后，气态流出物通过至少一个二次热交换器，其具有保持在一定温度下的热交换表面，使得部分气态流出物冷凝以在所述表面上形成液体涂层，从而进一步将其余的气态流出物冷却至 通过热解过程形成的焦油的冷凝温度。 然后在至少一个分离鼓中从气态流出物中除去冷凝的焦油。 还提供了一种用于执行该方法的装置。
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公开(公告)号：US6107533A
公开(公告)日：2000-08-22
申请号：US871859
申请日：1997-06-09
Applicant: Rimas Virgilijus Vebeliunas , David Alan Bamford , Neil James Drummond , Sheri Renee Snider , Robert David Strack , Roy Thomas Halle
Inventor： Rimas Virgilijus Vebeliunas , David Alan Bamford , Neil James Drummond , Sheri Renee Snider , Robert David Strack , Roy Thomas Halle
CPC classification number: C10G70/02 , C10G45/32 , Y10S585/95
Abstract: Process flow sequences for the reduction of equipment fouling in the fractional distillation of light end hydrocarbon components, such as those produced by pyrolysis or steam cracking, wherein conventional multiple hydrogenation unit configurations are replaced with upstream hydrogenation unit configurations. The upstream hydrogenation units of the invention are located at either side draws or in the reboiler circuit of deethanizers, in front-end demethanizer and front-end deethanizer sequences, or depropanizers, in front-end depropanizer sequences and obviate the need for most of the conventionally used hydrogenation units downstream.
Abstract translation: 用于减少轻馏分烃组分（例如通过热解或蒸汽裂化产生的那些）的分馏中的设备污染的工艺流程序列，其中常规多个加氢单元配置被上游氢化单元构型替代。 本发明的上游氢化单元位于脱乙烷塔的任一侧或再沸器回路中，在前端脱丙烷塔序列中的前端脱甲烷塔和前端脱乙烷塔系统或脱丙烷化器中，并且不需要大部分 常规使用的氢化装置在下游。
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公开(公告)号：US08092671B2
公开(公告)日：2012-01-10
申请号：US12643470
申请日：2009-12-21
Applicant: Robert David Strack , Richard C. Stell , John R. Messinger , Dane C. Grenoble , John E. Asplin
Inventor： Robert David Strack , Richard C. Stell , John R. Messinger , Dane C. Grenoble , John E. Asplin
CPC classification number: C10G9/00 , C10G9/002 , C10G2300/1033 , C10G2300/1044 , C10G2300/1051 , C10G2300/1059 , C10G2300/107 , C10G2300/1077 , C10G2300/206
Abstract: A method is disclosed for treating gaseous effluent from a hydrocarbon pyrolysis unit to provide steam cracked tar of reduced asphaltene and toluene insolubles content. The method is suitable for preparing reduced viscosity tar useful as a fuel blending stock, or feedstock for producing carbon black, while reducing or eliminating the need for externally sourced lighter aromatics additives to meet viscosity specifications. The method comprises drawing steam cracked tar from a separation vessel, e.g., a primary fractionator or tar knock-out drum, cooling the tar, and returning it to the separation vessel to effect lower overall tar temperatures within the separation vessel, in order to reduce viscosity increasing condensation reactions. An apparatus for carrying out the method is also provided.
Abstract translation: 公开了一种用于处理来自烃热解单元的气态流出物以提供减少的沥青质和甲苯不溶物含量的蒸汽裂化焦油的方法。 该方法适用于制备用作燃料混合原料的还原粘度焦油或用于生产炭黑的原料，同时减少或消除对来自外部的较轻芳烃添加剂以满足粘度规格的需要。 该方法包括从分离容器（例如主分馏器或焦油脱除鼓）中抽出蒸汽裂解焦油，冷却焦油，并将其返回到分离容器中以降低分离容器内的总焦油温度，以便减少 粘度增加缩合反应。 还提供了一种用于执行该方法的装置。
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公开(公告)号：US08074707B2
公开(公告)日：2011-12-13
申请号：US12835899
申请日：2010-07-14
Applicant: Robert David Strack , David B. Spicer , George Stephens , James Mitchell Frye
Inventor： Robert David Strack , David B. Spicer , George Stephens , James Mitchell Frye
IPC: F28F19/00
CPC classification number: C10G9/002 , C10G2300/1033 , C10G2300/1044 , C10G2300/1051 , C10G2300/1074 , C10G2300/44
Abstract: A method is provided for treating the effluent from a hydrocarbon pyrolysis unit processing heavier than naphtha feeds to recover heat and remove tar therefrom. The method comprises passing the gaseous effluent to at least one primary transfer line heat exchanger, thereby cooling the gaseous effluent and generating superheated steam. Thereafter, the gaseous effluent is passed through at least one secondary transfer line heat exchanger having a heat exchange surface with a liquid coating on said surface, thereby further cooling the remainder of the gaseous effluent to a temperature at which tar, formed by the pyrolysis process, condenses. The condensed tar is then removed from the gaseous effluent in at least one knock-out drum. An apparatus for carrying out the method is also provided.
Abstract translation: 提供一种处理来自比石脑油进料重的烃热解单元的流出物的方法以回收热量并从其中除去焦油。 该方法包括将气态流出物送至至少一个一次传输线热交换器，从而冷却气态流出物并产生过热蒸汽。 此后，气态流出物通过至少一个具有在所述表面上具有液体涂层的热交换表面的二次传输线热交换器，从而进一步将剩余的气态流出物冷却至通过热解过程形成的焦油的温度 ，冷凝。 然后在至少一个分离鼓中从气态流出物中除去冷凝的焦油。 还提供了一种用于执行该方法的装置。
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