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    Fractionation for full boiling range gasoline desulfurization
    4.
    发明授权
    Fractionation for full boiling range gasoline desulfurization 有权
    全沸点汽油脱硫分馏

    公开(公告)号：US06726835B2

    公开(公告)日：2004-04-27

    申请号：US10321945

    申请日：2002-12-17

    申请人： Gavin P. Towler ,  Michael A. Schultz

    发明人： Gavin P. Towler ,  Michael A. Schultz

    IPC分类号： C10G4500

    CPC分类号： C10G67/16 ,  B01D3/141 ,  C10G2400/02

    摘要： Savings in the processing of a naphtha boiling range feed containing a thiophene are achieved by fractionating the feed stream in a single dividing wall column to yield a C6-minus overhead stream, a side-draw containing the majority of the C6 and C7 paraffins and olefins, and a bottoms stream comprising C7 and heavier hydrocarbons. A dividing wall column provides better control of the concentration of both thiophene and toluene in the side-draw. Less of the valuable naphtha is lost and the amount of thiophene in the overhead product is minimized.

    摘要翻译： 在含有噻吩的石脑油沸程进料加工过程中节省的成本是通过在单分隔壁塔中分馏进料流来获得C6-塔顶馏出物流，含有大部分C6和C7链烷烃和烯烃的侧馏分 ，以及包含C7和较重烃的底部料流。 分隔壁柱可以更好地控制侧吸中噻吩和甲苯的浓度。 少量有价值的石脑油损失，塔顶产物中噻吩的量最小化。

    Modified absorption recovery processing of FCC-produced light olefins
    5.
    发明授权
    Modified absorption recovery processing of FCC-produced light olefins 有权
    FCC生产的轻质烯烃的改性吸收回收处理

    公开(公告)号：US08007661B1

    公开(公告)日：2011-08-30

    申请号：US11643884

    申请日：2006-12-21

    申请人： Michael A. Schultz ,  David A. Wegerer ,  Gavin P. Towler

    发明人： Michael A. Schultz ,  David A. Wegerer ,  Gavin P. Towler

    IPC分类号： C10G11/18

    CPC分类号： C10G11/18

    摘要： Processing schemes and arrangements are provided arrangements are provided for the processing a heavy hydrocarbon feedstock via hydrocarbon cracking processing with selected hydrocarbon fractions being obtained via absorption-based product recovery while minimizing or avoiding loss of light olefins via system purging.

    摘要翻译： 提供的处理方案和布置提供了用于通过烃裂解加工处理重质烃原料的装置，其中所选择的烃馏分通过基于吸收的产物回收获得，同时通过系统吹扫最小化或避免轻质烯烃的损失。

    Fractionation for full boiling range gasoline desulfurization
    6.
    发明授权
    Fractionation for full boiling range gasoline desulfurization 失效
    全沸点汽油脱硫分馏

    公开(公告)号：US06540907B1

    公开(公告)日：2003-04-01

    申请号：US09900941

    申请日：2001-07-09

    申请人： Gavin P. Towler ,  Michael A. Schultz

    发明人： Gavin P. Towler ,  Michael A. Schultz

    IPC分类号： C10G4500

    CPC分类号： C10G67/16 ,  B01D3/141 ,  C10G2400/02

    摘要： Savings in the processing of a naphtha boiling range feed containing a thiophene are achieved by fractionating the feed stream in a single dividing wall column to yield a C6-minus overhead stream, a side-draw containing the majority of the C6 and C7 paraffins and olefins, and a bottoms stream comprising C7 and heavier hydrocarbons. A dividing wall column provides better control of the concentration of both thiophene and toluene in the side-draw. Less of the valuable naphtha is lost and the amount of thiophene in the overhead product is minimized.

    摘要翻译： 在含有噻吩的石脑油沸程进料加工过程中节省的成本是通过在单分隔壁塔中分馏进料流来获得C6-塔顶馏出物流，含有大部分C6和C7链烷烃和烯烃的侧馏分 ，以及包含C7和较重烃的底部料流。 分隔壁柱可以更好地控制侧吸中噻吩和甲苯的浓度。 少量有价值的石脑油损失，塔顶产物中噻吩的量最小化。

    Process for the removal of sulfur-oxidated compounds from a hydrocarbonaceous stream
    7.
    发明授权
    Process for the removal of sulfur-oxidated compounds from a hydrocarbonaceous stream 有权
    从烃流中除去硫氧化化合物的方法

    公开(公告)号：US07452459B2

    公开(公告)日：2008-11-18

    申请号：US10813250

    申请日：2004-03-30

    申请人： Michael A. Schultz ,  John P. Brady

    发明人： Michael A. Schultz ,  John P. Brady

    IPC分类号： C10G25/00 ,  C10G25/12

    CPC分类号： C10G25/003 ,  C10G25/05 ,  C10G25/12

    摘要： A process for the removal of sulfur-oxidated compounds from a hydrocarbonaceous stream containing sulfur-oxidated compounds wherein the hydrocarbonaceous stream containing sulfur-oxidated compounds is contacted with an adsorbent which selectively adsorbs sulfur-oxidated compounds from the hydrocarbonaceous stream to produce an adsorbent having adsorbed sulfur-oxidated compounds. The loaded adsorbent containing sulfur-oxidated compounds is contacted with a desorbent to produce a desorbent containing sulfur-oxidated compounds and an adsorbent having a reduced content of sulfur-oxidated compounds. The regenerated adsorbent is then used to remove additional sulfur-oxidated compounds.

    摘要翻译： 一种从含硫氧化化合物的含烃流中除去硫氧化化合物的方法，其中含有硫氧化化合物的烃物流与选择性吸附来自烃物流的硫氧化化合物以产生吸附剂的吸附剂接触 硫氧化化合物。 负载的含硫氧化化合物的吸附剂与解吸剂接触以产生含硫氧化化合物的解吸剂和具有降低的硫氧化化合物含量的吸附剂。 然后再生的吸附剂用于除去附加的硫氧化化合物。

    Process and system for heating or cooling streams for a divided distillation column
    8.
    发明授权
    Process and system for heating or cooling streams for a divided distillation column 有权
    用于分馏蒸馏塔的加热或冷却流的方法和系统

    公开(公告)号：US08999117B2

    公开(公告)日：2015-04-07

    申请号：US12398070

    申请日：2009-03-04

    申请人： Michael A. Schultz ,  Xin X. Zhu ,  Jibreel A. Qafisheh

    发明人： Michael A. Schultz ,  Xin X. Zhu ,  Jibreel A. Qafisheh

    IPC分类号： B01D3/32 ,  B01D3/14

    CPC分类号： B01D3/14 ,  B01D3/141 ,  C10G2400/02

    摘要： One exemplary embodiment can be a system for separating a plurality of naphtha components. The system can include a column, an overhead condenser, and a side condenser. Generally, the column includes a dividing imperforate wall with one surface facing a feed and another surface facing at least one side stream. Typically, the wall extends a significant portion of the column height to divide the portion into at least two substantially vertical, parallel contacting sections. Typically, the overhead condenser receives an overhead stream including a light naphtha from the column. Usually, a side condenser receives a process stream from the column and returns the stream to the column to facilitate separation. A cooling stream may pass through the overhead condenser and then the side condenser.

    摘要翻译： 一个示例性实施例可以是用于分离多个石脑油组分的系统。 该系统可以包括塔，塔顶冷凝器和侧冷凝器。 通常，柱包括分隔的无孔壁，其一个表面面向进料，另一个表面面向至少一个侧流。 通常，壁延伸柱高度的大部分，以将该部分分成至少两个基本垂直的平行的接触部分。 通常，塔顶冷凝器从塔中接收包括轻石脑油的塔顶流。 通常，侧冷凝器从塔接收工艺流并将流返回到柱以便于分离。 冷却流可以通过顶部冷凝器，然后通过侧冷凝器。

    Selective hydrogenation of unsaturated aliphatic hydrocarbons in predominantly aromatic streams
    9.
    发明授权
    Selective hydrogenation of unsaturated aliphatic hydrocarbons in predominantly aromatic streams 失效
    主要是芳族物流中不饱和脂肪烃的选择性氢化

    公开(公告)号：US08350106B2

    公开(公告)日：2013-01-08

    申请号：US12165291

    申请日：2008-06-30

    申请人： Deng-Yang Jan ,  Michael A. Schultz

    发明人： Deng-Yang Jan ,  Michael A. Schultz

    IPC分类号： C07C5/05

    CPC分类号： C07C15/46 ,  C07C2/66 ,  C07C5/333 ,  C07C7/163 ,  C07C15/073

    摘要： The selective saturation of unsaturated aliphatic hydrocarbons (e.g., diolefins) in a hydrogenation feed stream comprising an aromatic compound (e.g., benzene) and one or more nitrogen compounds renders it beneficial when the stream or a portion thereof is subsequently treated (e.g., with a zeolitic adsorbent) to remove nitrogen. In particular, the selective saturation of, for example, olefins and diolefins prolongs the life of the nitrogen guard bed. In a representative embodiment, the selective hydrogenation is applied to a recycle benzene-containing stream recovered in the separation section (e.g., from the benzene/toluene splitter overhead) of a styrene production process, prior to treatment with a nitrogen guard bed adsorbent.

    摘要翻译： 在包含芳族化合物（例如苯）和一种或多种氮化合物的氢化进料流中，不饱和脂族烃（例如二烯烃）的选择性饱和使其在后续处理流或其一部分时（例如， 沸石吸附剂）去除氮气。 特别地，例如烯烃和二烯烃的选择性饱和延长了氮保护床的寿命。 在代表性的实施方案中，在用氮保护床吸附剂处理之前，将选择性氢化应用于在苯乙烯生产方法的分离段（例如苯/甲苯分离器塔顶馏出物）中回收的再循环含苯物流。