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公开(公告)号：EP1913118A1
公开(公告)日：2008-04-23
申请号：EP06774114.0
申请日：2006-06-27
IPC分类号： C10G9/00
CPC分类号： C10G9/002 , C10G2300/1033 , C10G2300/1044 , C10G2300/1051 , C10G2300/1074 , C10G2300/44
摘要： 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 comprisea 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.
摘要翻译： 提供了一种处理来自烃重质分解单元的流出物的方法，其处理比石脑油原料更重的原料以回收热量并从其中除去焦油。 该方法包括将气体流出物传送到至少一个主输送管线热交换器，由此冷却气体流出物并产生过热蒸汽。 此后，气体流出物通过至少一个二级输送管线热交换器，该热交换器具有在所述表面上具有液体涂层的热交换表面，由此进一步将剩余的气体流出物冷却至通过热解过程形成的焦油 ，浓缩。 然后将冷凝的焦油从至少一个分离罐中的气态流出物中除去。 还提供了用于执行该方法的设备。
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公开(公告)号：EP1934307B1
公开(公告)日：2017-12-13
申请号：EP06785654.2
申请日：2006-06-27
发明人： STRACK, Robert, D. , MESSINGER, John, R. , STELL, Richard, C. , GRENOBLE, Dane, C. , ASPLIN, John E.
IPC分类号： C10G9/00
CPC分类号： C10G9/00 , C10G9/002 , C10G2300/1033 , C10G2300/1044 , C10G2300/1051 , C10G2300/1059 , C10G2300/107 , C10G2300/1077 , C10G2300/206
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公开(公告)号：EP1922387A1
公开(公告)日：2008-05-21
申请号：EP06785618.7
申请日：2006-06-27
IPC分类号： C10G9/00
CPC分类号： C10G9/002 , C10G2300/301 , C10G2400/02
摘要： 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.
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公开(公告)号：EP2201085B1
公开(公告)日：2015-03-04
申请号：EP08797349.1
申请日：2008-08-07
CPC分类号： F28D7/106 , C10G9/00 , F28C3/06 , F28D7/0066 , F28D2021/0075
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公开(公告)号：EP1931749A2
公开(公告)日：2008-06-18
申请号：EP06785655.9
申请日：2006-06-27
IPC分类号： C10G9/00
CPC分类号： C10G9/002 , C10G2300/301 , C10G2300/4081 , C10G2300/805 , C10G2400/02
摘要： 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.
摘要翻译： 公开了一种使用小型主分馏器，即精馏器处理来自烃热解装置的流出物的方法和设备。 该方法包括例如通过直接骤冷和/或至少一个主换热器冷却气态流出物，然后将气态流出物冷却至由流出物的成分之间的反应形成的焦油例如在 二级交换器。 所得到的混合气态和液态流出物通过精馏器，从包含裂解汽油馏分的气态流出物中干净地分离骤冷油，其沸点可由于精馏处理而降低。 然后将流出物冷却以冷凝包含裂解汽油和从蒸汽冷凝的水的液体流出物，所述流出物在蒸馏罐中分离。 将冷却的气态流出物导入回收装置以回收轻质烯烃。 至少一部分含裂解汽油的馏分可循环到精馏器中以增强骤冷油与裂解汽油馏分的分离。
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6.发明授权STEAM CRACKING OF HYDROCARBON FEEDSTOCKS CONTAINING NON-VOLATILE COMPONENTS AND/OR COKE PRECURSORS 有权非挥发性组分和/或焦炭前体包含碳氢化合物的申请材料进行蒸汽裂解
公开(公告)号：EP1769054B1
公开(公告)日：2011-06-22
申请号：EP05749874.3
申请日：2005-05-19
发明人： STELL,Richard, C. , STRACK, Robert, D. , FRYE, James, M. , SRIVASTAVA, Alok , ANNAMALAI, Subramanian 4300 Bay Area Boulevard , MCCOY, James, N.
IPC分类号： C10G9/00
CPC分类号： C10G9/206 , C10G9/16 , C10G9/20 , C10G2300/1033 , C10G2300/1044 , C10G2300/1055 , C10G2300/107 , C10G2300/805 , C10G2300/807 , C10G2400/20 , Y02P30/40
摘要： A process for cracking a heavy hydrocarbon feedstock containing non-volatile components and/or coke precursors, wherein a stripping agent is added to the feedstock to form an enhanced hydrocarbon blend which is thereafter separated into a vapor phase and a liquid phase by flashing in a flash/separation vessel, separating and cracking the vapor phase, and recovering cracked product. The stripping agent increases vaporization of the volatile fraction of the heavy hydrocarbon increasing the maximum feedrate capacity of the furnace.
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7.发明公开STEAM CRACKING OF HYDROCARBON FEEDSTOCKS CONTAINING NON-VOLATILE COMPONENTS AND/OR COKE PRECURSORS 有权非挥发性组分和/或焦炭前体包含碳氢化合物的申请材料进行蒸汽裂解
公开(公告)号：EP1769054A2
公开(公告)日：2007-04-04
申请号：EP05749874.3
申请日：2005-05-19
发明人： STELL,Richard, C. , STRACK, Robert, D. , FRYE, James, M. , SRIVASTAVA, Alok , ANNAMALAI, Subramanian 4300 Bay Area Boulevard , MCCOY, James, N.
IPC分类号： C10G9/00
CPC分类号： C10G9/206 , C10G9/16 , C10G9/20 , C10G2300/1033 , C10G2300/1044 , C10G2300/1055 , C10G2300/107 , C10G2300/805 , C10G2300/807 , C10G2400/20 , Y02P30/40
摘要： A process for cracking a heavy hydrocarbon feedstock containing non-volatile components and/or coke precursors, wherein a stripping agent is added to the feedstock to form an enhanced hydrocarbon blend which is thereafter separated into a vapor phase and a liquid phase by flashing in a flash/separation vessel, separating and cracking the vapor phase, and recovering cracked product. The stripping agent increases vaporization of the volatile fraction of the heavy hydrocarbon increasing the maximum feedrate capacity of the furnace.
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公开(公告)号：EP1527151A1
公开(公告)日：2005-05-04
申请号：EP03763037.3
申请日：2003-06-27
发明人： STELL, Richard C. , DINICOLANTONIO, Arthur R. , FRYE, James Mitchell , SPICER, David, B. , MCCOY, James, N. , STRACK, Robert, D.
IPC分类号： C10G9/00
CPC分类号： F28F9/0265 , C10G9/00 , C10G9/36 , C10G2300/1022 , C10G2300/1033 , C10G2300/104 , C10G2300/1044 , C10G2300/1051 , C10G2300/1055 , C10G2300/1059 , C10G2300/107 , C10G2300/1074 , C10G2300/1077 , C10G2300/301 , C10G2300/807 , C10G2400/20
摘要： 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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公开(公告)号：EP1527151B1
公开(公告)日：2018-07-18
申请号：EP03763037.3
申请日：2003-06-27
发明人： STELL, Richard C. , DINICOLANTONIO, Arthur R. , FRYE, James Mitchell , SPICER, David, B. , MCCOY, James, N. , STRACK, Robert, D.
IPC分类号： C10G9/00
CPC分类号： F28F9/0265 , C10G9/00 , C10G9/36 , C10G2300/1022 , C10G2300/1033 , C10G2300/104 , C10G2300/1044 , C10G2300/1051 , C10G2300/1055 , C10G2300/1059 , C10G2300/107 , C10G2300/1074 , C10G2300/1077 , C10G2300/301 , C10G2300/807 , C10G2400/20
摘要： 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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公开(公告)号：EP2201085A2
公开(公告)日：2010-06-30
申请号：EP08797349.1
申请日：2008-08-07
IPC分类号： C10G9/00
CPC分类号： F28D7/106 , C10G9/00 , F28C3/06 , F28D7/0066 , F28D2021/0075
摘要： A process and apparatus are provided for cooling gaseous effluent from a hydrocarbon pyrolysis furnace, the cooling conduit apparatus comprising: (i) an inner wall for contacting the effluent, the inner wall defining a bore extending a length of the cooling conduit, the inner wall including a perimeter opening along the bore; (ii) an outer wall external to the inner wall and substantially coaxial to the inner wall; (iii) a substantially annular cavity external to the inner wall and including at least a portion of the outer wall, the annular cavity fluidly and remotely connected to the perimeter opening, the annular cavity externally surrounding a perimeter of the inner wall, the annular cavity including at least a portion of the outer wall; and (iv) a peripheral channel extending around a perimeter of the inner wall, the peripheral channel providing a channel flow path that fluidly connects the annular cavity with the remotely connected perimeter opening along the perimeter of the inner wall.
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