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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：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：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：US08524070B2
公开(公告)日：2013-09-03
申请号：US11178037
申请日：2005-07-08
Applicant: Robert David Strack , John R. Messinger
Inventor： Robert David Strack , John R. Messinger
IPC: C10G9/00
CPC classification number: C10G9/002 , C10G2300/301 , C10G2300/4081 , C10G2300/805 , C10G2400/02
Abstract: A method and apparatus are disclosed for treating the effluent from a hydrocarbon pyrolysis unit employing a small primary fractionator, i.e., a rectifier. The method comprises cooling the gaseous effluent, e.g., by direct quench and/or at least one primary heat exchanger, and then cooling the gaseous effluent to a temperature at which tar, formed by reactions among constituents of the effluent, condenses, e.g., in a secondary exchanger. The resulting mixed gaseous and liquid effluent is passed through a rectifier, to cleanly separate quench oil from the gaseous effluent comprising a pyrolysis gasoline fraction, whose boiling point can be lowered as a result of the rectifier treatment. The effluent is then cooled to condense a liquid effluent comprising pyrolysis gasoline and water condensed from steam, which fractions are separated in a distillate drum. The cooled gaseous effluent is directed to a recovery train to recover light olefins. At least a portion of the pyrolysis gasoline-containing fraction can be recycled to the rectifier to enhance separation of the quench oil from the pyrolysis gasoline fraction.
Abstract translation: 公开了一种用于处理来自使用小型主分馏器，即整流器的烃热解单元的流出物的方法和装置。 该方法包括例如通过直接淬火和/或至少一个主要热交换器冷却气态流出物，然后将气态流出物冷却至通过流出物的组分之间的反应形成的焦油冷凝的温度，例如在 二次换热器。 所得到的混合气体和液体流出物通过整流器，以将来自包含热解汽油馏分的气态流出物的骤冷油干净地分离，其沸点可以通过整流器处理而降低。 然后将流出物冷却以冷凝包含热解汽油和从蒸汽冷凝的水的液体流出物，该馏分在蒸馏塔中分离。 将冷却的气态流出物导向回收系统以回收轻质烯烃。 含裂解汽油馏分的至少一部分可以再循环到整流器中以增强急冷油与热解汽油馏分的分离。
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公开(公告)号：US20100230235A1
公开(公告)日：2010-09-16
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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Patent Agency Ranking
公开(公告)号：US07749372B2
公开(公告)日：2010-07-06
申请号：US11177975
申请日：2005-07-08
Applicant: Robert David Strack , John R. Messinger
Inventor： Robert David Strack , John R. Messinger
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：US07718049B2
公开(公告)日：2010-05-18
申请号：US11177076
申请日：2005-07-08
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：US07674366B2
公开(公告)日：2010-03-09
申请号：US11177125
申请日：2005-07-08
Applicant: Robert David Strack , John R. Messinger
Inventor： Robert David Strack , John R. Messinger
Abstract: A method is disclosed for treating the effluent from a hydrocarbon pyrolysis unit without employing a primary fractionator. The method comprises cooling the gaseous effluent, e.g., by direct quench and/or at least one primary heat exchanger, thereby 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 resulting mixed gaseous and liquid effluent is passed through a quench oil knock-out drum, to separate quench oil from the gaseous effluent which is then cooled to condense a liquid effluent comprising pyrolysis gasoline and water condensed from steam, which fractions are separated in a distillate drum. The cooled gaseous effluent is directed to a recovery train, to recover light olefins. The pyrolysis gasoline-containing fraction passes to a tailing tower which provides an overhead stream rich in pyrolysis gasoline and a bottoms stream rich in gas oil.
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。 该方法包括例如通过直接淬火和/或至少一个主要热交换器冷却气态流出物，由此产生高压蒸汽，然后将气态流出物冷却至通过流出物的组分之间的反应形成的焦油的温度 ，冷凝。 将所得混合的气态和液态流出物通过骤冷油分离鼓，以将来自气态流出物的骤冷油分离，然后将其冷却以冷凝包含热解汽油和从蒸汽中冷凝的水的液体流出物，该馏分在一 蒸馏桶。 将冷却的气态流出物导向回收馏分，以回收轻质烯烃。 含裂解汽油的馏分通过尾矿塔，其提供富含裂解汽油的塔顶馏出物和富含瓦斯油的塔底物流。
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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：US20100096296A1
公开(公告)日：2010-04-22
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
IPC: C10L1/04
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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