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    • 32. 发明授权
    • Process for making alkylated polycyclic aromatics
    • 制备烷基化多环芳烃的方法
    • US5302769A
    • 1994-04-12
    • US986187
    • 1992-12-07
    • David O. MarlerDominick N. MazzoneL. Deane Rollmann
    • David O. MarlerDominick N. MazzoneL. Deane Rollmann
    • C07C6/12C10G29/20C07C2/66C07C15/24C07C15/27
    • C07C6/126C10G29/205
    • A polycyclic aromatic is contacted with an alkyl-substituted single ring aromatic, such as toluene, o-, m- or p-xylene or mesitylene, over a catalyst comprising a zeolite, such as zeolite beta, USY or ZSM-5 to alkylate the polycyclic aromatic. The polycyclic aromatic can be a fused polynuclear aromatic, e.g. phenanthrene, or an assembly of two or more cyclic systems, e.g. biphenyl. The polycyclic aromatic can also include carbocyclic systems such as fluorene and naphthalene or heterocyclic systems such as benzothiophene and dibenzothiophene. The polycyclic aromatic can be derived from a cycle oil, coker gas oil, extract of lubricant solvent refining or crude distillate fraction. The transalkylating agent can be derived from a reformate, pyrolysis gasoline or coker naphtha.
    • 使多环芳族化合物与烷基取代的单环芳族化合物如甲苯,邻 - ,间 - 或对 - 二甲苯或均三甲苯在包含沸石如β沸石,USY或ZSM-5沸石的催化剂上接触,将 多环芳香族。 多环芳族化合物可以是稠合多核芳族化合物。 菲或两个或更多个环状体系的组合,例如。 联苯。 多环芳族还可以包括碳环体系如芴和萘,或杂环体系如苯并噻吩和二苯并噻吩。 多环芳烃可以衍生自循环油,焦化瓦斯油,润滑剂溶剂精制或粗馏分馏提取物。 烷基转移剂可以由重整油,热解汽油或焦化石脑油衍生而来。
    • 40. 发明授权
    • Integration of steam reforming unit and cogeneration power plant
    • 蒸汽重整单元和热电联产电站的整合
    • US5624964A
    • 1997-04-29
    • US471976
    • 1995-06-06
    • Ronald J. CiminiDavid O. MarlerReuel ShinnarGerald J. Teitman
    • Ronald J. CiminiDavid O. MarlerReuel ShinnarGerald J. Teitman
    • C01B3/44C07C27/06
    • C01B3/44Y02E20/16Y02P20/584
    • A process for integration of a steam reforming unit and a cogeneration power plant in which said steam reforming unit comprises two communicating fluid beds; the first fluid bed comprising a reformer containing catalyst and which is used to react steam and light hydrocarbons at conditions sufficient to produce a mixture comprising synthesis gas hydrogen, carbon monoxide, and carbon dioxide, the second fluid bed comprising a combustor-regenerator which receives spent catalyst from the first fluid bed and which provides heat to heat the catalyst and balance the reaction endotherm, by combusting fuel gas in direct contact with the catalyst producing hot flue gas; said cogeneration power plant comprises a gas turbine equipped with an air compressor and a combustor; said integration which comprises drawing off a portion of compressed air from the power plant gas turbine air compressor leaving remainder compressed air; introducing the drawn off compressed air to the combustor-regenerator; mixing the hot flue gas from the combustor-regenerator with the remainder of the compressed air to produce a recombined gas stream and feeding this recombined gas stream to the combustor of the cogeneration gas turbine power plant.
    • 一种用于整合蒸汽重整单元和热电联产电厂的方法,其中所述蒸汽重整单元包括两个连通流体床; 所述第一流化床包括含有重整器的催化剂,其用于在足以产生包含合成气氢,一氧化碳和二氧化碳的混合物的条件下反应蒸汽和轻质烃,所述第二流化床包括燃烧器再生器 催化剂,其提供热量以加热催化剂并平衡反应吸热,通过燃烧与产生热烟道气的催化剂直接接触的燃料气体; 所述热电联产电厂包括配备有空气压缩机和燃烧器的燃气轮机; 所述集成包括从发电厂燃气轮机空气压缩机中取出一部分压缩空气,留下剩余的压缩空气; 将抽出的压缩空气引入燃烧器 - 再生器; 将来自燃烧器 - 再生器的热烟气与剩余的压缩空气混合以产生重组气流,并将该重组气流送入热电联产燃气轮机发电厂的燃烧器。