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公开(公告)号：US08083931B2
公开(公告)日：2011-12-27
申请号：US11881063
申请日：2007-07-25
CPC分类号： C10G51/023 , C10G55/04
摘要： The invention is directed to a process wherein a feedstock or stream comprising steam cracker tar is passed to a vacuum pipestill. A deasphalted cut of tar is obtained as an overhead (or sidestream) and a heavy tar asphaltenic product is obtained as bottoms. In preferred embodiments, at least a portion of the bottoms product is sent to a partial oxidation unit (POX) wherein syn gas may be obtained as a product, and/or at least a portion of the bottoms product is used to produce a light product stream in a coker unit, such as coker naphtha and/or or coker gas oil. In another preferred embodiment at least a portion of the overheads product is added to refinery fuel oil pools and in yet another preferred embodiment at least a portion of the overheads product is mixed with locally combusted materials to lower soot make. Two or more of the aforementioned preferred embodiments may be combined.
摘要翻译： 本发明涉及一种方法，其中将包含蒸汽裂解焦油的原料或料流送入真空管道。 作为塔顶（或侧流）获得焦油的脱沥青馏分，并且作为底部获得重质焦油沥青产物。 在优选的实施方案中，将底部产物的至少一部分送至部分氧化单元（POX），其中可以获得产物的合成气，和/或至少部分底部产物用于生产轻质产物 在焦化装置中，例如焦化石脑油和/或焦化瓦斯油。 在另一个优选的实施方案中，将至少一部分塔顶馏出产物加入到炼油厂燃料油池中，在另一个优选的实施方案中，塔顶产物的至少一部分与局部燃烧的材料混合以降低烟灰。 上述优选实施例中的两个或更多个可以组合。
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公开(公告)号：US08083930B2
公开(公告)日：2011-12-27
申请号：US11880983
申请日：2007-07-25
CPC分类号： C10G7/06
摘要： A process is described for producing deasphalted steam cracker tar comprising feeding steam cracker tar to a vacuum pipestill (VPS) including a flash zone separated from a zone comprising trays by at least one annular entrainment ring and obtaining as an overheads a deasphalted tar product and as a bottoms an asphaltenic heavy tar product. Also according to the invention, there is a system for the upgrading of tar comprising said VPS with at least one annular entrainment ring.
摘要翻译： 描述了一种用于生产脱沥青蒸汽裂化器焦油的方法，其包括将蒸气裂解焦油加入到真空管道（VPS）中，所述真空管道（VPS）包括通过至少一个环形夹带环从包含塔板的区域分离的闪蒸区域，并获得脱沥青焦油产物和作为塔顶馏出物 一种沥青质焦油产品的底部。 同样根据本发明，存在一种用于使包含所述VPS的焦油升级至少一个环形夹带环的系统。
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公开(公告)号：US07846324B2
公开(公告)日：2010-12-07
申请号：US12023322
申请日：2008-01-31
IPC分类号： C10C3/00
CPC分类号： C10G9/00
摘要： The invention relates to a process for upgrading tar using a heat exchanger in series with a vapor/liquid separator to separate tar into a heavy tar asphaltenic material and a deasphalted tar material.
摘要翻译： 本发明涉及一种使用与蒸汽/液体分离器串联的热交换器来提升焦油的方法，以将焦油分离成焦油沥青质的重质沥青和脱沥青焦油。
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公开(公告)号：US20080210598A1
公开(公告)日：2008-09-04
申请号：US12023322
申请日：2008-01-31
IPC分类号： C10G55/02
CPC分类号： C10G9/00
摘要： The invention relates to a process for upgrading tar using a heat exchanger in series with a vapor/liquid separator to separate tar into a heavy tar asphaltenic material and a deasphalted tar material.
摘要翻译： 本发明涉及一种使用与蒸汽/液体分离器串联的热交换器来提升焦油的方法，以将焦油分离成焦油沥青质的重质沥青和脱沥青焦油。
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公开(公告)号：US07625480B2
公开(公告)日：2009-12-01
申请号：US11432260
申请日：2006-05-11
申请人： David Beattie , Richard Charles Stell , James N. McCoy , Bryan Daniel McVicker , Paul F. Keusenkothen , Alok Srivastava , David Bleckinger
发明人： David Beattie , Richard Charles Stell , James N. McCoy , Bryan Daniel McVicker , Paul F. Keusenkothen , Alok Srivastava , David Bleckinger
摘要： The invention relates to a method for processing asphaltene-containing feed to a pyrolysis furnace by raising the final boiling point of the feed/steam mixture to the pyrolysis furnace to ensure fouling occurs lower in the convection section where the mixture of air and steam can burn off fouling deposits during decoking operations. The final boiling point of the feed stream is increased by adding a heavy essentially asphaltene-free high boiling point hydrocarbon to the feed stream before the feed stream enters the convection section of the pyrolysis furnace, whereby said fouling occurs lower in the convection section.
摘要翻译： 本发明涉及通过将进料/蒸汽混合物的最终沸点提高到热解炉来将沥青质的进料加工成热解炉的方法，以确保在空气和蒸汽的混合物可以燃烧的对流部分中发生较低的结垢 在除焦作业期间污染沉积物。 在进料流进入热解炉的对流段之前，通过向进料流中加入重质基本上不含沥青质的高沸点烃来提高进料流的最终沸点，由此在对流段中发生较低的污垢。
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公开(公告)号：US20080099371A1
公开(公告)日：2008-05-01
申请号：US11589453
申请日：2006-10-30
CPC分类号： C10G55/04 , C10G21/003
摘要： A feedstream comprising tar is feed to a solvent deasphalter wherein it is contacted with a deasphalting solvent or fluid to produce a composition comprising a mixture or slurry of solvent containing a soluble portion of the tar, and a heavy tar fraction comprising the insoluble portion of the tar. These fractions may be separated in the deasphalter apparatus, such as by gravity settling wherein the heavy tar fraction is taken off as bottoms, and the solvent-soluble fraction taken as overflow or overheads with the solvent. The overflow or overheads is sent to a solvent recovery unit, such as a distillation apparatus, wherein solvent is recovered as overheads and a deasphalted tar fraction is taken off as a sidestream or bottoms. The solvent or a portion thereof, recovered as overheads, may be then be recycled to the solvent deasphalter, or in a preferred embodiment, at least a portion of the solvent is steam cracked to produce a product comprising light olefins.
摘要翻译： 将包含焦油的进料流进料到溶剂脱沥青，其中其与脱沥青溶剂或流体接触以产生包含含有可溶部分焦油的溶剂的混合物或浆料的组合物，以及包含不溶部分的重焦油馏分 柏油。 这些级分可以在脱沥青装置中分离，例如通过重力沉降，其中重焦油馏分作为塔底馏分取出，溶剂可溶部分用溶剂作为溢流或塔顶馏出物。 将溢出物或塔顶馏出物送入溶剂回收装置，例如蒸馏装置，其中将溶剂回收为塔顶馏出物，脱沥青焦油馏分作为侧流或塔底馏分脱除。 然后将作为塔顶馏出物回收的溶剂或其一部分再循环到溶剂脱沥青中，或者在一个优选的实施方案中，至少一部分溶剂被蒸汽裂化以产生包含轻质烯烃的产物。
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公开(公告)号：US07744743B2
公开(公告)日：2010-06-29
申请号：US11589453
申请日：2006-10-30
CPC分类号： C10G55/04 , C10G21/003
摘要： A feedstream comprising tar is fed to a solvent deasphalter wherein it is contacted with a deasphalting solvent or fluid to produce a composition comprising a mixture or slurry of solvent containing a soluble portion of the tar, and a heavy tar fraction comprising the insoluble portion of the tar. These fractions may be separated in the deasphalter apparatus, such as by gravity settling wherein the heavy tar fraction is taken off as bottoms, and the solvent-soluble fraction taken as overflow or overheads with the solvent. The overflow or overheads is sent to a solvent recovery unit, such as a distillation apparatus, wherein solvent is recovered as overheads and a deasphalted tar fraction is taken off as a sidestream or bottoms. The solvent or a portion thereof, recovered as overheads, may be then be recycled to the solvent deasphalter, or in a preferred embodiment, at least a portion of the solvent is steam cracked to produce a product comprising light olefins.
摘要翻译： 将包含焦油的进料流进料到溶剂脱沥青器中，其中其与脱沥青溶剂或流体接触以产生包含含有焦油的可溶部分的溶剂的混合物或浆料的组合物，以及包含不溶部分的重焦油馏分 柏油。 这些级分可以在脱沥青装置中分离，例如通过重力沉降，其中重焦油馏分作为塔底馏分取出，溶剂可溶部分用溶剂作为溢流或塔顶馏出物。 将溢出物或塔顶馏出物送入溶剂回收装置，例如蒸馏装置，其中将溶剂回收为塔顶馏出物，脱沥青焦油馏分作为侧流或塔底馏分脱除。 然后将作为塔顶馏出物回收的溶剂或其一部分再循环到溶剂脱沥青中，或者在一个优选的实施方案中，至少一部分溶剂被蒸汽裂化以产生包含轻质烯烃的产物。
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公开(公告)号：US07906010B2
公开(公告)日：2011-03-15
申请号：US11331945
申请日：2006-01-13
IPC分类号： C10C3/00
CPC分类号： C10L1/00 , C10G2400/20
摘要： The invention relates to the use of steam cracked tar with the bottoms product of a flash drum integrated with a pyrolysis furnace. In embodiments, the steam cracked tar is added to fuel oil.
摘要翻译： 本发明涉及使用与热解炉一体的闪蒸罐的底部产物的蒸汽裂化焦油。 在实施方案中，将蒸汽裂化的焦油加入到燃料油中。
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9.发明授权Process and apparatus for upgrading steam cracker tar using hydrogen donor compounds 有权使用氢供体化合物升级蒸汽裂解焦油的方法和设备公开(公告)号：US08197668B2
公开(公告)日：2012-06-12
申请号：US12499999
申请日：2009-07-09
申请人： John D. Y. Ou , Glenn A. Heeter , Paul F. Keusenkothen , James N. McCoy , Judith Hey, legal representative
IPC分类号： C10C3/02
CPC分类号： C10G9/36 , C10G9/007 , C10G47/34 , C10G51/04 , C10G2300/1077 , C10G2300/206 , C10G2300/301 , C10G2300/308 , C10G2300/4056 , C10G2300/4081 , C10G2300/42 , C10G2300/807 , C10G2400/02 , C10G2400/06
摘要： A process and apparatus are provided for upgrading steam cracker tars from steam crackers. The invention also relates to a steam cracking process and apparatus for reducing yields of tars produced from steam cracking while increasing yields of higher value products by heating steam cracker tar, in the presence of hydrogen donor compounds, e.g., tetralin. The hydrogen donor compounds can be provided in a hydrogen donor-rich hydrocarbon stream, e.g., light cycle oils, or low sulfur vacuum tower bottoms. The treated tar can be separated into gas oil, fuel oil and tar streams.
摘要翻译： 提供了一种用于从蒸汽裂解器升级蒸汽裂化器焦油的方法和装置。 本发明还涉及一种蒸汽裂解方法和装置，用于在氢供体化合物例如四氢化萘的存在下，通过加热蒸汽裂化塔焦油来降低由蒸汽裂解产生的焦油的产率，同时通过加热蒸气裂解塔焦油来提高产率。 氢供体化合物可以提供在富氢给体的烃流中，例如轻循环油或低硫真空塔底。 经处理的焦油可分为瓦斯油，燃油和焦油流。
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10.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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