Alkylation and catalyst regenerative process
    101.
    发明授权
    Alkylation and catalyst regenerative process 有权
    烷基化和催化剂再生过程

    公开(公告)号:US07259283B2

    公开(公告)日:2007-08-21

    申请号:US11256803

    申请日:2005-10-24

    IPC分类号: C07C2/68 B01J20/34

    摘要: A process for the regeneration of a deactivated zeolite beta catalyst such as rare earth promoted zeolite beta catalyst deactivated in the course of an aromatic alkylation reaction. A zeolite beta conversion catalyst deactivated with the deposition of coke is heated to a temperature in excess of 300° C. in an oxygen-free environment. An oxidative regeneration gas is supplied to the catalyst bed with oxidation of a portion of a relatively porous coke component to produce an exotherm moving through the catalyst bed. At least one of the temperature and oxygen content of the gas is progressively increased to oxidize a porous component of the coke. Regeneration gas is supplied having at least one of an increased oxygen content or increased temperature to oxidize a less porous refractory component of the coke. The regeneration process is completed by passing an inert gas through the catalyst bed at a reduced temperature.

    摘要翻译: 在芳族烷基化反应过程中,再生失活的沸石β催化剂如稀土促进沸石β催化剂失活的方法。 在无氧环境中将焦炭沉积失活的沸石β转化催化剂加热至超过300℃的温度。 氧化再生气体被一部分相对多孔的焦炭组分的氧化提供给催化剂床,以产生通过催化剂床移动的放热。 气体的温度和氧气含量中的至少一个逐渐增加以氧化焦炭的多孔组分。 提供再生气体,其具有增加的氧含量或升高的温度中的至少一种以氧化焦炭的较少多孔的耐火成分。 通过使惰性气体在降低的温度下通过催化剂床完成再生过程。

    Method for preparation of stable bitumen polymer compositions
    102.
    发明授权
    Method for preparation of stable bitumen polymer compositions 失效
    稳定沥青聚合物组合物的制备方法

    公开(公告)号:US07186765B2

    公开(公告)日:2007-03-06

    申请号:US10888563

    申请日:2004-07-09

    IPC分类号: C08L95/00

    摘要: The present invention provides a method for preparing an asphalt and thermoplastic elastomer composition. The process comprises heating an asphalt cut in a stirred tank to a temperature sufficient to allow the stirring of the asphalt in the tank. A thermoplastic elastomer or rubber is added to the asphalt while continuing to stir the asphalt. The mixture is stirred at a speed and for a period of time sufficient to increase the distribution of the elastomer into the asphalt. The stirring speed is reduced and the temperature is increased to add crosslinking agents to the tank. Stirring is continued for a period of time sufficient to improve the distribution of the crosslinking agent dispersion in the asphalt. Crosslinking agents include compositions of mercaptobenzothiazole, zinc oxide and elemental sulfur; compositions of mercaptobenzothiazole, zinc oxide, and mixed polythiomorpholine; and compositions of zinc 2-mercaptobenzothiazole and dithiodimorpholine.

    摘要翻译: 本发明提供一种制备沥青和热塑性弹性体组合物的方法。 该方法包括将在搅拌槽中切割的沥青加热到足以允许在罐中搅拌沥青的温度。 在沥青中继续搅拌沥青时,加入热塑性弹性体或橡胶。 将混合物以足以增加弹性体分配到沥青中的速度搅拌一段时间。 搅拌速度降低,温度升高,向罐中加入交联剂。 搅拌持续一段时间,足以改善沥青中交联剂分散体的分布。 交联剂包括巯基苯并噻唑,氧化锌和元素硫的组合物; 巯基苯并噻唑,氧化锌和混合多硫代吗啉的组成; 和2-巯基苯并噻唑锌和二硫代二吗啉的组合物。

    Dispersing agent and method for the delivery of cross-linking agent to polymer modified asphalt compositions
    103.
    发明授权
    Dispersing agent and method for the delivery of cross-linking agent to polymer modified asphalt compositions 失效
    用于将交联剂递送到聚合物改性沥青组合物的分散剂和方法

    公开(公告)号:US06927245B2

    公开(公告)日:2005-08-09

    申请号:US10454001

    申请日:2003-06-04

    IPC分类号: C08J3/00 C08L95/00

    摘要: The present invention provides a dispersing agent that facilitates the delivery of a cross-linking agent to polymer modified asphalt. The present invention further includes a composition comprising a liquid hydrocarbon, the dispersant and cross-linking agent, and methods of preparing the composition and of preparing cross-linked polymer modified asphalt composition.

    摘要翻译: 本发明提供一种促进交联剂向聚合物改性沥青输送的分散剂。 本发明还包括包含液体烃,分散剂和交联剂的组合物,以及制备该组合物和制备交联聚合物改性沥青组合物的方法。

    Method of conversion of heavy aromatics
    104.
    发明授权
    Method of conversion of heavy aromatics 有权
    重质芳烃转化方法

    公开(公告)号:US06846964B2

    公开(公告)日:2005-01-25

    申请号:US10285736

    申请日:2002-11-01

    摘要: A method is provided for conversion of heavy alkylaromatic compounds, particularly those in the C8-C12 range, into more valuable aromatics of benzene, toluene and xylene utilizing a toluene disproportionation unit containing a nickel, palladium or platinum-modified mordenite catalyst. The method allows large amounts of these heavy alkylaromatic compounds to be processed without adversely affecting catalyst activity or catalyst life. This is accomplished by introducing the heavy alkylaromatic compounds into the reactor at constant reaction severity conditions and maintaining those conditions during conversion.

    摘要翻译: 提供了一种使用含有镍,钯或铂改性的丝光沸石催化剂的甲苯歧化单元将重质烷基芳族化合物,特别是C8-C12范围内的重质烷基芳族化合物转化为更有价值的苯,甲苯和二甲苯的芳族化合物的方法。 该方法允许大量这些重质烷基芳族化合物被加工而不会不利地影响催化剂活性或催化剂寿命。 这是通过将重质烷基芳族化合物以恒定的反应苛刻度条件引入反应器中并在转化期间维持这些条件来实现的。

    Method of conversion of heavy aromatics
    105.
    发明授权
    Method of conversion of heavy aromatics 失效
    重质芳烃转化方法

    公开(公告)号:US06504076B1

    公开(公告)日:2003-01-07

    申请号:US09860755

    申请日:2001-05-18

    IPC分类号: C07C552

    摘要: A method is provided for conversion of heavy alkylaromatic compounds, particularly those in the C8-C12 range, into more valuable aromatics of benzene, toluene and xylene utilizing a toluene disproportionation unit containing a nickel, palladium or platinum-modified mordenite catalyst. The method allows large amounts of these heavy alkylaromatic compounds to be processed without adversely affecting catalyst activity or catalyst life. This is accomplished by introducing the heavy alkylaromatic compounds into the reactor at constant reaction severity conditions and maintaining those conditions during conversion.

    摘要翻译: 提供了一种使用含有镍,钯或铂改性的丝光沸石催化剂的甲苯歧化单元将重质烷基芳族化合物,特别是C8-C12范围内的重质烷基芳族化合物转化为更有价值的苯,甲苯和二甲苯的芳族化合物的方法。 该方法允许大量这些重质烷基芳族化合物被加工而不会不利地影响催化剂活性或催化剂寿命。 这是通过将重质烷基芳族化合物以恒定的反应苛刻度条件引入反应器中并在转化期间维持这些条件来实现的。

    Multistage reaction system with interstage sparger systems
    106.
    发明授权
    Multistage reaction system with interstage sparger systems 失效
    具有级间分布器系统的多级反应系统

    公开(公告)号:US06486371B1

    公开(公告)日:2002-11-26

    申请号:US09723650

    申请日:2000-11-28

    IPC分类号: C07C266

    摘要: Vapor phase alkylation of an aromatic substrate in a multi-stage alkylation reaction zone having a plurality of series-connected catalyst beds providing mixing zones between adjacent catalyst beds. An aromatic substrate and a C2-C4 alkylating agent is supplied to an inlet side of a gas phase reaction zone causing vapor phase alkylation of the aromatic substrate as the aromatic substrate and the alkylating agent flow through the reaction zone from one catalyst bed to the next. A quench fluid comprising one or both of the aromatic substrate and the alkylating agent is supplied into the interior of the mixing zone through a plurality of flow paths. One portion of the flow paths is directed upwardly and another portion downwardly within the mixing zone. The quench fluid is supplied to the mixing zone through a plurality of dispersion channels spaced laterally from one another.

    摘要翻译: 在具有多个串联连接的催化剂床的多级烷基化反应区中芳族底物的气相烷基化提供相邻催化剂床之间的混合区。 将芳香族基质和C 2〜C 4烷基化剂供给到气相反应区的入口侧,引起作为芳香族底物的芳香族基质的气相烷基化,烷基化剂从一个催化剂床流到下一个催化剂床 。 包含芳族底物和烷基化剂中的一种或两种的骤冷流体通过多个流动路径被供给到混合区的内部。 流动路径的一部分向上引导,另一部分在混合区域内向下引导。 骤冷流体通过彼此横向隔开的多个分散通道供应到混合区域。

    Catalysts with low concentration of weak acid sites
    107.
    发明授权
    Catalysts with low concentration of weak acid sites 失效
    具有低浓度弱酸性位点的催化剂

    公开(公告)号:US06268305B1

    公开(公告)日:2001-07-31

    申请号:US09544581

    申请日:2000-04-06

    IPC分类号: B01J2100

    摘要: Ethylbenzene is produced by alkylation over monoclinic silicalite catalysts having a weak acid site concentration of less than 50 micromoles per gram. A Feed stock containing benzene and ethylene is applied to an alkylation reaction zone having at least one catalyst bed containing a monoclinic silicalite catalyst having a weak acid site concentration of less than 50 micromoles per gram. The alkylation reaction zone is operated at temperature and pressure conditions in which the benzene is in a gaseous phase to cause gas-phase alkylation of the aromatic substrate in the presence of the silicalite catalysts to produce an alkylation product. The alkylation product is then withdrawn from the reaction zone for separation and recovery.

    摘要翻译: 通过在弱酸性位点浓度小于50微摩尔/克的单斜硅沸石催化剂上烷基化生产乙苯。 将含有苯和乙烯的原料储存在具有至少一个含有弱酸性位点浓度小于50微摩尔/克的单斜硅沸石催化剂的催化剂床的烷基化反应区。 烷基化反应区在其中苯处于气相的温度和压力条件下运行,以在硅沸石催化剂存在下引起芳族底物的气相烷基化以产生烷基化产物。 然后将烷基化产物从反应区取出以进行分离和回收。

    System for purifying styrene monomer feedstock using ethylbenzene
dehydrogenation waste gas
    110.
    发明授权
    System for purifying styrene monomer feedstock using ethylbenzene dehydrogenation waste gas 失效
    使用乙苯脱氢废气净化苯乙烯单体原料的系统

    公开(公告)号:US5156816A

    公开(公告)日:1992-10-20

    申请号:US787175

    申请日:1991-11-04

    IPC分类号: C07C5/09 C07C7/167 C07C15/46

    摘要: Processes and apparatus are disclosed for the catalytic purification of styrene monomer by hydrogenating the phenylacetylene contaminant therein to styrene in a catalytic bed using multiple hydrogen injection; dilution of the hydrogen by a diluent such as nitrogen; mixing the hydrogen with a catalyst-selectivity improver such as carbon monoxide; using ethylbenzene dehydrogenation ventgas to supply hydrogen; and, using a multiple-catalyst-bed-reactor, or multiple reactors, each with a single catalyst bed. One preferred phenylacetylene reduction catalyst used is palladium on an alumina carrier.

    摘要翻译: 公开了通过使用多个氢气注入在催化床中将苯乙炔污染物氢化为苯乙烯来进行苯乙烯单体的催化净化的方法和装置; 通过稀释剂如氮气稀释氢; 将氢气与催化剂选择性改进剂如一氧化碳混合; 使用乙苯脱氢气体供应氢气; 并使用多催化剂床反应器或多个反应器,每个反应器具有单个催化剂床。 使用的一种优选的苯乙炔还原催化剂是氧化铝载体上的钯。