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1.发明授权Process and apparatus for cracking hydrocarbon feedstock containing resid to improve vapor yield from vapor/liquid separation 有权用于裂化含有渣油的烃原料以提高蒸气/液体分离产物的方法和装置公开(公告)号：US07553460B2
公开(公告)日：2009-06-30
申请号：US11713505
申请日：2007-03-02
申请人： Richard C. Stell , Jennifer L. Bancroft , Arthur R. Dinicolantonio , Subramanian Annamalai , James N. McCoy , Paul F. Keusenkothen , George Stephens , John R. Messinger , James Mitchell Frye , Nick G. Vidonic , George J. Balinsky
发明人： Richard C. Stell , Jennifer L. Bancroft , Arthur R. Dinicolantonio , Subramanian Annamalai , James N. McCoy , Paul F. Keusenkothen , George Stephens , John R. Messinger , James Mitchell Frye , Nick G. Vidonic , George J. Balinsky
CPC分类号： C10G9/00 , C10G2400/20
摘要： A process for cracking hydrocarbon feedstock containing resid comprising: heating the feedstock, mixing the heated 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 which collect as bottoms and removing the liquid phase, separating and cracking the vapor phase, and cooling the product effluent. The process comprises at least two of the following conditions: (1) maintaining the bottoms under conditions to effect at least partial visbreaking; (2) reducing or eliminating partial vapor condensation during flashing by adding a heated vaporous diluent to dilute and superheat the vapor; (3) partially condensing the vapor within said flash/separation vessel by contacting with a condenser; (4) decoking internal surfaces and associated piping of the flash/separation vessel with air and steam; (5) utilizing a flash/separation vessel having an annular, inverted L-shaped baffle; and (6) regulating temperature in furnace tube banks used for heating by utilizing a desuperheater and/or an economizer. An apparatus for carrying out the process is also provided.
摘要翻译： 一种用于裂化含有渣油的烃原料的方法，包括：加热原料，将加热的原料与流体和/或初级稀释蒸汽流混合以形成混合物，使混合物闪蒸形成气相和液相， 并除去液相，分离和裂化气相，并冷却产物流出物。 该方法包括以下条件中的至少两个：（1）在至少部分减粘裂化的条件下保持底部物质; （2）通过添加加热的蒸气稀释剂来稀释和过热蒸气来减少或消除闪蒸过程中的部分蒸气冷凝; （3）通过与冷凝器接触来部分冷凝所述闪蒸/分离容器内的蒸气; （4）用空气和蒸汽去除闪蒸/分离容器的内表面和相关管道; （5）利用具有环形的倒L形挡板的闪光/分离容器; 和（6）通过利用过热降温器和/或节能器来调节用于加热的炉管组中的温度。 还提供了一种用于执行该过程的装置。
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2.发明授权Process and apparatus for cracking hydrocarbon feedstock containing resid to improve vapor yield from vapor/liquid separation 有权用于裂化含有渣油的烃原料以提高蒸气/液体分离产物的方法和装置公开(公告)号：US07193123B2
公开(公告)日：2007-03-20
申请号：US11134148
申请日：2005-05-20
申请人： Richard C. Stell , Jennifer L. Bancroft , Arthur R. DiNicolantonio , Subramanian Annamalai , James N. McCoy , Paul F. Keusenkothen , George Stephens , John R. Messinger , James Mitchell Frye , Nick G. Vidonic , George J. Balinsky
发明人： Richard C. Stell , Jennifer L. Bancroft , Arthur R. DiNicolantonio , Subramanian Annamalai , James N. McCoy , Paul F. Keusenkothen , George Stephens , John R. Messinger , James Mitchell Frye , Nick G. Vidonic , George J. Balinsky
CPC分类号： C10G9/00 , C10G2400/20
摘要： A process for cracking hydrocarbon feedstock containing resid comprising: heating the feedstock, mixing the heated 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 which collect as bottoms and removing the liquid phase, separating and cracking the vapor phase, and cooling the product effluent. The process comprises at least two of the following conditions: (1) maintaining the bottoms under conditions to effect at least partial visbreaking; (2) reducing or eliminating partial vapor condensation during flashing by adding a heated vaporous diluent to dilute and superheat the vapor; (3) partially condensing the vapor within said flash/separation vessel by contacting with a condenser; (4) decoking internal surfaces and associated piping of the flash/separation vessel with air and steam; (5) utilizing a flash/separation vessel having an annular, inverted L-shaped baffle; and (6) regulating temperature in furnace tube banks used for heating by utilizing a desuperheater and/or an economizer. An apparatus for carrying out the process is also provided.
摘要翻译： 一种用于裂化含有渣油的烃原料的方法，包括：加热原料，将加热的原料与流体和/或初级稀释蒸汽流混合以形成混合物，使混合物闪蒸形成气相和液相， 并除去液相，分离和裂化气相，并冷却产物流出物。 该方法包括以下条件中的至少两个：（1）在至少部分减粘裂化的条件下保持底部物质; （2）通过添加加热的蒸气稀释剂来稀释和过热蒸气来减少或消除闪蒸过程中的部分蒸气冷凝; （3）通过与冷凝器接触来部分冷凝所述闪蒸/分离容器内的蒸气; （4）用空气和蒸汽去除闪蒸/分离容器的内表面和相关管道; （5）利用具有环形的倒L形挡板的闪光/分离容器; 和（6）通过利用过热降温器和/或节能器来调节用于加热的炉管组中的温度。 还提供了一种用于执行该过程的装置。
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公开(公告)号：US07097758B2
公开(公告)日：2006-08-29
申请号：US10189618
申请日：2002-07-03
IPC分类号： C10G9/16
CPC分类号： C10G9/00
摘要： A process to increase the non-volatile removal efficiency in a flash drum in the steam cracking system. The gas flow from the convection section is converted from mist flow to annular flow before entering the flash drum to increase the removal efficiency. The conversion of gas flow from mist flow to annular flow is accomplished by subjecting the gas flow first to at least one expander and then to bends of various degrees and force the flow to change directions at least once. The change of gas flow from mist to annular helps coalesce fine liquid droplets and thus being removed from the vapor phase.
摘要翻译： 在蒸汽裂解系统中提高闪蒸桶中的非挥发性去除效率的方法。 在进入闪蒸鼓之前，来自对流部分的气体流从雾流转换成环形流，以提高去除效率。 气流从气流到环流的转化是通过首先将气流首先流到至少一个膨胀器，然后使各种程度弯曲并迫使流动至少改变方向来实现的。 从烟雾到气体的气流的变化有助于凝结细液滴，从气相中除去。
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4.发明授权Cracking hydrocarbon feedstock containing resid utilizing partial condensation of vapor phase from vapor/liquid separation to mitigate fouling in a flash/separation vessel 有权使用蒸气/液体分离的气相部分冷凝来破碎含有残留物的烃原料，以减轻闪蒸/分离容器中的结垢公开(公告)号：US07767170B2
公开(公告)日：2010-08-03
申请号：US11454779
申请日：2006-06-16
CPC分类号： C10G9/00 , B01D3/06 , B01D5/003 , B01D5/0069 , B01D19/0036 , C10G9/20
摘要： A process is provided for cracking hydrocarbon feedstock containing resid comprising: heating the feedstock, mixing the heated feedstock with a fluid and/or a primary dilution steam stream to form a mixture, optionally further heating the mixture, flashing the mixture within a flash/separation vessel to form a vapor phase and a liquid phase, partially condensing the vapor phase by contacting with a condenser within the vessel, to condense at least some coke precursors within the vapor while providing condensates which add to the liquid phase, removing the vapor phase of reduced coke precursors content as overhead and the liquid phase as bottoms, heating the vapor phase, cracking the vapor phase in a radiant section of a pyrolysis furnace to produce an effluent comprising olefins, and quenching the effluent and recovering cracked product therefrom. An apparatus for carrying out the process is also provided.
摘要翻译： 提供了一种用于裂化含有渣油的烃原料的方法，包括：加热原料，将加热的原料与流体和/或初级稀释蒸汽流混合以形成混合物，任选地进一步加热混合物，在闪蒸/分离 容器以形成气相和液相，通过与容器内的冷凝器接触来部分地冷凝气相，以在蒸汽内冷凝至少一些焦炭前体，同时提供冷凝物，其加入液相，除去气相 将焦炭前体含量降低为塔顶馏出物，液相作为塔底馏分，加热气相，裂解热解炉的辐射段中的气相以产生包含烯烃的流出物，并淬灭流出物并从其中回收裂化产物。 还提供了一种用于执行该过程的装置。
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5.发明授权Cracking hydrocarbon feedstock containing resid utilizing partial condensation of vapor phase from vapor/liquid separation to mitigate fouling in a flash/separation vessel 有权使用蒸气/液体分离的气相部分冷凝来破碎含有残留物的烃原料，以减轻闪蒸/分离容器中的结垢公开(公告)号：US07419584B2
公开(公告)日：2008-09-02
申请号：US11454338
申请日：2006-06-16
CPC分类号： C10G9/00 , B01D3/06 , B01D5/003 , B01D5/0069 , B01D19/0036 , C10G9/20
摘要： A process is provided for cracking hydrocarbon feedstock containing resid comprising: heating the feedstock, mixing the heated feedstock with a fluid and/or a primary dilution steam stream to form a mixture, optionally further heating the mixture, flashing the mixture within a flash/separation vessel to form a vapor phase and a liquid phase, partially condensing the vapor phase by contacting with a condenser within the vessel, to condense at least some coke precursors within the vapor while providing condensates which add to the liquid phase, removing the vapor phase of reduced coke precursors content as overhead and the liquid phase as bottoms, heating the vapor phase, cracking the vapor phase in a radiant section of a pyrolysis furnace to produce an effluent comprising olefins, and quenching the effluent and recovering cracked product therefrom. An apparatus for carrying out the process is also provided.
摘要翻译： 提供了一种用于裂化含有渣油的烃原料的方法，包括：加热原料，将加热的原料与流体和/或初级稀释蒸汽流混合以形成混合物，任选地进一步加热混合物，在闪蒸/分离 容器以形成气相和液相，通过与容器内的冷凝器接触来部分地冷凝气相，以在蒸汽内冷凝至少一些焦炭前体，同时提供冷凝物，其加入液相，除去气相 将焦炭前体含量降低为塔顶馏出物，液相作为塔底馏分，加热气相，裂解热解炉的辐射段中的气相以产生包含烯烃的流出物，并淬灭流出物并从其中回收裂化产物。 还提供了一种用于执行该过程的装置。
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6.发明授权Cracking hydrocarbon feedstock containing resid utilizing partial condensation of vapor phase from vapor/liquid separation to mitigate fouling in a flash/separation vessel 有权使用蒸气/液体分离的气相部分冷凝来破碎含有残留物的烃原料，以减轻闪蒸/分离容器中的结垢公开(公告)号：US07247765B2
公开(公告)日：2007-07-24
申请号：US10851494
申请日：2004-05-21
CPC分类号： C10G9/00 , B01D3/06 , B01D5/003 , B01D5/0069 , B01D19/0036 , C10G9/20
摘要： A process is provided for cracking hydrocarbon feedstock containing resid comprising: heating the feedstock, mixing the heated feedstock with a fluid and/or a primary dilution steam stream to form a mixture, optionally further heating the mixture, flashing the mixture within a flash/separation vessel to form a vapor phase and a liquid phase, partially condensing the vapor phase by contacting with a condenser within the vessel, to condense at least some coke precursors within the vapor while providing condensates which add to the liquid phase, removing the vapor phase of reduced coke precursors content as overhead and the liquid phase as bottoms, heating the vapor phase, cracking the vapor phase in a radiant section of a pyrolysis furnace to produce an effluent comprising olefins, and quenching the effluent and recovering cracked product therefrom. An apparatus for carrying out the process is also provided.
摘要翻译： 提供了一种用于裂化含有渣油的烃原料的方法，包括：加热原料，将加热的原料与流体和/或初级稀释蒸汽流混合以形成混合物，任选地进一步加热混合物，在闪蒸/分离 容器以形成气相和液相，通过与容器内的冷凝器接触来部分地冷凝气相，以在蒸汽内冷凝至少一些焦炭前体，同时提供冷凝物，其加入液相，除去气相 将焦炭前体含量降低为塔顶馏出物，液相作为塔底馏分，加热气相，裂解热解炉的辐射段中的气相以产生包含烯烃的流出物，并淬灭流出物并从其中回收裂化产物。 还提供了一种用于执行该过程的装置。
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7.发明授权公开(公告)号：US08882991B2
公开(公告)日：2014-11-11
申请号：US12545470
申请日：2009-08-21
CPC分类号： C10G69/06 , C10G9/38 , C10G45/00 , C10G2300/1059 , C10G2300/107 , C10G2300/301 , C10G2300/42
摘要： In one aspect, the invention includes in a process for cracking a hydrocarbon feedstock comprising: a) feeding a hydrocarbon feedstock containing at least 1 wt % of resid components having boiling points of at least 500° C. to a furnace convection section to heat the feedstock; b) flashing the heated feedstock in a first flash separation vessel to create a first overhead stream and a first bottoms liquid stream; c) hydrogenating at least a portion of the first bottoms liquid stream to create a hydrogenated bottoms stream; d) flashing the hydrogenated bottoms stream in a second flash separation vessel to create a second overhead stream and a second bottoms liquid stream; e) cracking the first overhead stream and the second overhead stream in a cracking furnace to produce a pyrolysis effluent stream. In other embodiments, the process further comprises heating the hydrocarbon feedstock in step a) to a temperature within a range of from 315° C. to 705° C.
摘要翻译： 在一个方面，本发明包括在烃原料裂化的方法中，包括：a）将含有至少1重量％沸点至少为500℃的至少1重量％残渣组分的烃原料进料到炉对流部分，以加热 原料; b）在第一快速分离容器中使加热的原料闪烁以产生第一塔顶流和第一塔底液流; c）将至少一部分第一底部液体流氢化以产生氢化底部物流; d）在第二快速分离容器中使氢化塔底物流闪蒸，以产生第二塔顶流和第二塔底液流; e）在裂解炉中裂化第一塔顶馏出物流和第二塔顶馏出物以产生热解流出物流。 在其它实施方案中，该方法还包括将步骤a）中的烃原料加热至315℃至705℃的温度
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8.发明申请公开(公告)号：US20110042269A1
公开(公告)日：2011-02-24
申请号：US12545470
申请日：2009-08-21
CPC分类号： C10G69/06 , C10G9/38 , C10G45/00 , C10G2300/1059 , C10G2300/107 , C10G2300/301 , C10G2300/42
摘要： In one aspect, the invention includes in a process for cracking a hydrocarbon feedstock comprising: a) feeding a hydrocarbon feedstock containing at least 1 wt % of resid components having boiling points of at least 500° C. to a furnace convection section to heat the feedstock; b) flashing the heated feedstock in a first flash separation vessel to create a first overhead stream and a first bottoms liquid stream; c) hydrogenating at least a portion of the first bottoms liquid stream to create a hydrogenated bottoms stream; d) flashing the hydrogenated bottoms stream in a second flash separation vessel to create a second overhead stream and a second bottoms liquid stream; e) cracking the first overhead stream and the second overhead stream in a cracking furnace to produce a pyrolysis effluent stream. In other embodiments, the process further comprises heating the hydrocarbon feedstock in step a) to a temperature within a range of from 315° C. to 705° C.
摘要翻译： 在一个方面，本发明包括在烃原料裂化的方法中，包括：a）将含有至少1重量％沸点至少为500℃的至少1重量％的残渣组分的烃原料进料到炉对流段以加热 原料; b）在第一快速分离容器中使加热的原料闪烁以产生第一塔顶流和第一塔底液流; c）将至少一部分第一底部液体流氢化以产生氢化底部物流; d）在第二快速分离容器中使氢化塔底物流闪蒸，以产生第二塔顶流和第二塔底液流; e）在裂解炉中裂化第一塔顶馏出物流和第二塔顶馏出物以产生热解流出物流。 在其它实施方案中，该方法还包括将步骤a）中的烃原料加热至315℃至705℃的温度
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公开(公告)号：US09296955B2
公开(公告)日：2016-03-29
申请号：US13219397
申请日：2011-08-26
CPC分类号： C10G7/00 , C10G7/06 , C10G7/12 , C10G9/00 , C10G9/20 , C10G2300/1074 , C10G2400/20 , F01K3/20 , F02C3/00
摘要： A method and system are disclosed for co-production of olefins and electric power. The method includes determining a separation level, separating a hydrocarbon feed into a light fraction stream and a heavy fraction stream based on the determined separation level; generating electric power from the heavy fraction stream; and cracking the light fraction stream in a pyrolysis unit to produce an effluent comprising olefins. The separation level may be based on olefin production requirements and electric power requirements or specific split of the hydrocarbon feed to be utilized for power generation and olefin production.
摘要翻译： 公开了用于共同生产烯烃和电力的方法和系统。 该方法包括确定分离水平，基于所确定的分离水平将烃进料分离成轻馏分料流和重馏分料流; 从重馏分流产生电力; 并在热解单元中裂解轻馏分流以产生包含烯烃的流出物。 分离水平可以基于烯烃生产要求和用于发电和烯烃生产的碳氢化合物进料的电力需求或特定裂缝。
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公开(公告)号：US20120067058A1
公开(公告)日：2012-03-22
申请号：US13219397
申请日：2011-08-26
CPC分类号： C10G7/00 , C10G7/06 , C10G7/12 , C10G9/00 , C10G9/20 , C10G2300/1074 , C10G2400/20 , F01K3/20 , F02C3/00
摘要： A method and system are disclosed for co-production of olefins and electric power. The method includes determining a separation level, separating a hydrocarbon feed into a light fraction stream and a heavy fraction stream based on the determined separation level; generating electric power from the heavy fraction stream; and cracking the light fraction stream in a pyrolysis unit to produce an effluent comprising olefins. The separation level may be based on olefin production requirements and electric power requirements or specific split of the hydrocarbon feed to be utilized for power generation and olefin production.
摘要翻译： 公开了用于共同生产烯烃和电力的方法和系统。 该方法包括确定分离水平，基于所确定的分离水平将烃进料分离成轻馏分料流和重馏分料流; 从重馏分流产生电力; 并在热解单元中裂解轻馏分流以产生包含烯烃的流出物。 分离水平可以基于烯烃生产要求和用于发电和烯烃生产的碳氢化合物进料的电力需求或特定裂缝。
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