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公开(公告)号：US5030338A
公开(公告)日：1991-07-09
申请号：US269087
申请日：1988-11-09
申请人： Mohsen N. Harandi , Hartley Owen
发明人： Mohsen N. Harandi , Hartley Owen
IPC分类号： B01J29/90 , C10G35/095
CPC分类号： B01J29/90 , C10G35/095
摘要： A process and apparatus are disclosed for the catalytic conversion of hydrocarbons in a transport or sub-transport fluidized bed reaction zone. Inert particles are used to transfer heat to the reaction zone. The particles may be heated separately from the catalyst in a combustion zone or together with the catalyst in a regenerator. Fuel is fired to heat the inert particles or a mixture of catalyst and inert particles. Hydrogen deficient fuels such as charcoal or coke are preferred.
摘要翻译： 公开了用于在运输或副输送流化床反应区中的烃的催化转化的方法和装置。 惰性颗粒用于将热量传递到反应区。 颗粒可以在燃烧区中与催化剂分开加热，或者与再生器中的催化剂一起加热。 燃烧燃料以加热惰性颗粒或催化剂和惰性颗粒的混合物。 缺碳燃料如木炭或焦炭是优选的。
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42.发明授权Olefins etherification and conversion to liquid fuels with paraffins dehydrogenation 失效烯烃醚化和转化为具有链烷烃脱氢的液体燃料
公开(公告)号：US5024679A
公开(公告)日：1991-06-18
申请号：US480710
申请日：1990-02-15
申请人： Mohsen N. Harandi , Hartley Owen
发明人： Mohsen N. Harandi , Hartley Owen
CPC分类号： C07C41/06 , C10L1/023 , C10L1/06 , Y02P20/125
摘要： An integrated process for the production of ether-rich liquid fuels containing MTBE and TAME by etherifying a hydrocarbon feedstock containing C.sub.4 + isoalkenes in the presence of a high stoichiometric excess of lower alkyl alcohol. Unreacted alcohol and olefins are passed to a zeolite catalyzed conversion reactor under olefinic and oxygenates conversion condition whereby gasoline and light hydrocarbons are produced. The light hydrocarbon fraction comprising C.sub.4 -C.sub.5 paraffins is dehydrogenated and C.sub.4 -C.sub.5 olefins are recycled to the etherification reactor.
摘要翻译： 一种通过在高化学计量过量的低级烷基醇存在下醚化含有C4 +异烯烃的烃原料来生产含有MTBE和TAME的富含醚的液体燃料的综合方法。 未反应的醇和烯烃在烯烃和含氧化合物转化条件下通入沸石催化转化反应器，由此产生汽油和轻烃。 包含C4-C5链烷烃的轻烃馏分被脱氢，C4-C5烯烃再循环到醚化反应器中。
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公开(公告)号：US5013329A
公开(公告)日：1991-05-07
申请号：US331201
申请日：1989-03-31
摘要： A process is disclosed for converting a light hydrocarbon feedstock that contains a mixture of linear and branched olefins to ether-rich high octane gasoline streams that include tertiary alkyl and isoalkyl ethers such as MTBE, TAME, methyl isopropyl ether (MIPE), and methyl sec-butylether (MSBE). The conversion is achieved by utilizing the differing reactivity of tertiary olefins under selected conditions compared to linear olefins in the catalyzed etherification processes. The discovery has been made that unreacted olefins from the etherification reactions can be converted to gasoline boiling range hydrocarbons by contacting them with zeolite catalyst at elevated temperature. Further, it has been discovered that unreacted paraffins in the integrated process can be dehydrogenated to produce C.sub.3 -C.sub.4 olefins which can be recycled to the etherification process.
摘要翻译： 公开了一种将包含直链和支链烯烃的混合物的轻质烃原料转化成富含高级辛烷值汽油的方法，其中包括叔烷基和异烷基醚如MTBE，TAME，甲基异丙醚（MIPE）和甲基sec 丁基醚（MSBE）。 通过在催化醚化过程中与线性烯烃相比，在选择的条件下利用三级烯烃的不同反应性来实现转化。 已经发现，来自醚化反应的未反应的烯烃可以通过在升高的温度下与沸石催化剂接触而转化为汽油沸程烃。 此外，已经发现，一体化方法中的未反应的链烷烃可以脱氢生产可以再循环到醚化过程的C 3 -C 4烯烃。
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公开(公告)号：US4975097A
公开(公告)日：1990-12-04
申请号：US454473
申请日：1989-12-21
申请人： Mohsen N. Harandi , Hartley Owen
发明人： Mohsen N. Harandi , Hartley Owen
摘要： A technique for converting olefinic light hydrocarbons to ether-rich liquid fuels and olefinic gasoline including etherification, olefin upgrading and transhydrogenation operations. The preferred process includes: reacting a fresh hydrocarbon stream containing C.sub.4 + iso-alkene with lower aliphatic alcohol in an etherification zone in contact with an acidic etherification catalyst under etherification conditions whereby an effluent stream containing C5+ tertiary-alkyl ether is produced; separating the etherification effluent stream to provide a first liquid stream comprising C5+ ether and a second stream comprising unreacted alcohol and C4+ hydrocarbons; contacting the second stream with acidic metallosilicate catalyst for conversion of oxygenates and olefins under olefin oligomerization and isomerization conditions at elevated temperature; separating oligomerization effluent to recover an intermediate hydrocarbon stream rich in C.sub.4 + paraffinic hydrocarbon, a light gas stream, and a liquid product stream comprising C.sub.6 + olefinic gasoline; contacting the C.sub.4 + intermediate hydrocarbon stream with lower alkene in the presence of transhydrogenation catalyst whereby C.sub.4 + paraffin is converted to C4+ olefin, including iso-alkene; separating transhydrogenation effluent to recover C4+ olefin containing iso-alkene; and passing at least a portion of iso-alkene to the etherification zone for co-conversion with fresh hydrocarbon and alcohol to produce tertiary-alkyl ether.
摘要翻译： 一种将烯烃轻质烃转化为富醚液体燃料和烯烃汽油的技术，包括醚化，烯烃提质和转氢操作。 优选的方法包括：在醚化条件下使与C4-异烯烃的低级脂族醇与酸性醚化催化剂接触的醚化区反应，由此产生含有C5 +叔烷基醚的流出物流; 分离醚化流出物流以提供包含C5 +醚的第一液流和包含未反应的醇和C 4 +烃的第二料流; 使第二流与酸性金属硅酸盐催化剂接触，以在烯烃低聚和异构化条件下在升高的温度下转化含氧化合物和烯烃; 分离低聚流出物以回收富含C 4 +链烷烃，轻质气体流和包含C6 +烯烃汽油的液体产物流的中间烃流; 在转氢催化剂存在下使C4 +中间烃物流与低级烯烃接触，由此将C4 +链烷烃转化为C4 +烯烃，包括异烯烃; 分离反氢化流出液以回收含有异烯烃的C4 +烯烃; 并将至少一部分异烯烃通入醚化区，以与新鲜的烃和醇共转化生成叔烷基醚。
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公开(公告)号：US4950823A
公开(公告)日：1990-08-21
申请号：US375172
申请日：1989-07-03
申请人： Mohsen N. Harandi , Hartley Owen
发明人： Mohsen N. Harandi , Hartley Owen
CPC分类号： C10G63/00 , C07C2/66 , C07C2529/40 , Y10S203/09
摘要： A process and apparatus are disclosed for the production of gasoline from a C.sub.4.sup.- fuel gas containing ethene and propene and catalytic reformate containing C.sub.6 to C.sub.8 aromatics. The C.sub.4.sup.- fuel gas is contacted with debutanized catalytic reformate over a zeolite catalyst under process conditions to convert ethene and propene in the C.sub.4.sup.- fuel gas to C.sub.5.sup.+ aliphatic and aromatic hydrocarbon gasoline and to convert C.sub.6 to C.sub.8 aromatics in the reformate to C.sub.7 to C.sub.11 aromatic hydrocarbon gasoline. Reformer fractionation system containing debutanizer column and separator stabilizes effluent gasoline and recycles unconverted light aromatics.
摘要翻译： 公开了用于从含有乙烯和丙烯的C4-燃料气体以及含有C6至C8芳族化合物的催化重整油生产汽油的方法和装置。 在工艺条件下，C4-燃料气体通过沸石催化剂与脱丁烷催化重整产物接触，以将C4-燃料气体中的乙烯和丙烯转化为C5 +脂族和芳族烃汽油，并将重整产品中的C6至C8芳族化合物转化为C7至C11 芳烃汽油。 含有脱丁烷塔和分离器的重整器分馏系统稳定流出汽油并回收未转化的轻质芳烃。
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46.发明授权Single zone oligomerization of olefins in a super-dense phase turbulent fluid bed 失效在超密相湍流流化床中烯烃的单区低聚
公开(公告)号：US4877921A
公开(公告)日：1989-10-31
申请号：US184465
申请日：1988-04-20
申请人： Mohsen N. Harandi , Hartley Owen
发明人： Mohsen N. Harandi , Hartley Owen
CPC分类号： C07C2/00 , B01J8/24 , B01J8/26 , C07C2529/40 , C07C2529/65 , C07C2529/70
摘要： A turbulent super-dense fluid-bed of a medium pore zeolite metallosilicate catalyst is operated at low WHSV, outside a critical region in the phase diagram of the hydrocarbon mixture in the reactor, at or above conditions of pressure P.sub.max and temperature T.sub.max at which a liquid phase may not form. The result is oligomerization of a "light gas" predominantly C.sub.3 -C.sub.5 olefin feed, the remainder being mainly C.sub.3 -C.sub.5 lower alkanes. The oligomerized product is a "heavies" stream, namely, distillate and lube oil range hydrocarbons, with a minor proportion by weight of gasoline range hydrocarbons. The reactor may be operated in either a C.sub.1.sup.+ distillate mode, or, a C.sub.22.sup.+ lubes mode. The superdense fluid bed with a density, measured at the bottom of the reaction zone, greater than 500 kg/m.sup.3, and operates at a temperature in the range from about 204.degree. C. (400.degree. F.) to about 371.degree. C. (700.degree. F.), and a pressure in the range from about 2857 kPa (400 psig) to about 13880 kPa (2000 psig) or even higher. This unique process provides per pass conversion of olefins, and selectively to C.sub.5.sup.+ hydrocarbons, each in excess of 80%.
摘要翻译： 中等孔沸石金属硅酸盐催化剂的湍流超稠密流化床在反应器中的烃混合物的相图中的临界区域外的低WHSV下操作，在压力Pmax和温度Tmax或更高的条件下， 液相不能形成。 结果是“轻质气体”主要是C3-C5烯烃进料的低聚，其余的主要是C3-C5低级烷烃。 低聚产物是“重质”流，即馏出物和润滑油范围的烃，其重量比小于汽油范围的烃。 反应器可以以C1 +馏出模式或C22 +润滑油模式操作。 在反应区底部测量的具有密度的超密度流化床大于500kg / m 3，并且在约204℃（约400℃）至约371℃的温度下操作。 （700°F），压力范围为约2857kPa（400psig）至约13880kPa（2000psig）或甚至更高。 这种独特的方法提供了烯烃的全程转化，并且选择性地提供了每个超过80％的C5 +烃。
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47.发明授权System for conversion of crude oxygenate to gasoline with feedstock extraction 失效用原料提取将粗含氧化合物转化为汽油的系统
公开(公告)号：US4857667A
公开(公告)日：1989-08-15
申请号：US105425
申请日：1987-10-07
申请人： Mohsen N. Harandi , Hartley Owen
发明人： Mohsen N. Harandi , Hartley Owen
CPC分类号： C07C1/20 , C10L1/023 , C07C2529/40 , Y10S585/92 , Y10S585/921
摘要： Apparatus for converting crude aqueous oxygenate feedstock, such methanol or the like, to liquid hydrocarbons in contact with a medium pore shape selective crystalline acid zeolite catalyst, such as HZSM-5. In a preferred embodiment, the novel technique comprises means for: (a) contacting a crude methanol feedstock containing a minor amount of water with a liquid hydrocarbon extraction stream under extraction conditions favorable to selective extraction of the methanol, thereby providing an extract liquid stream rich in methanol and an aqueous raffinate stream lean in methanol; (b) charging the extracted methanol substantially free of water to said reaction zone under process conditions to convert substantially all methanol to hydrocarbons; (c) cooling reaction effluent to recover aqueous liquid byproduct stream, gas rich in C.sub.2.sup.- hydrocarbons, liquid rich in C.sub.3 -C.sub.4 hydrocarbons and C.sub.5.sup.+ liquid hydrocarbons; and (d) contacting crude methanol feedstock with at least a portion of the liquid hydrocarbons employed as extraction liquid.
摘要翻译： 用于将粗含水含氧化合物原料（例如甲醇等）转化成与中等孔形状的选择性结晶酸沸石催化剂如HZSM-5接触的液体烃的装置。 在一个优选的实施方案中，新技术包括用于：（a）在有利于选择性提取甲醇的萃取条件下，使含有少量水的粗甲醇原料与液体烃萃取物流接触，从而提供富含萃取液流 在甲醇和贫甲醇水溶液中; （b）在工艺条件下将基本上不含水的提取的甲醇装入所述反应区，以将基本上所有的甲醇转化成烃; （c）冷却反应流出液以回收含水液体副产物流，富含C2-烃的气体，富含C3-C4烃和C5 +液体烃的液体; 和（d）使粗甲醇原料与用作萃取液体的至少一部分液体烃接触。
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公开(公告)号：US4854939A
公开(公告)日：1989-08-08
申请号：US130260
申请日：1987-12-08
申请人： Mohsen N. Harandi , Hartley Owen
发明人： Mohsen N. Harandi , Hartley Owen
IPC分类号： C10G3/00 , C10G35/095 , C10L1/02
CPC分类号： C10L1/1852 , C10G3/45 , C10G3/49 , C10L1/023 , C10G2300/1088 , C10G2300/4006 , C10G2300/4012 , C10G2400/02 , Y02P30/20
摘要： An integrated process for the production of aromatics rich an MTBE and TAME rich high octane gasoline fractions is described. Etherifications of iso-olefins is conducted in the presence of excess methanol. Unreacted methanol is passed to a fixed, fluid or moving bed aromatization zone in contact with ZSM-5 catalyst and olefin and paraffin feedstream to produce high octane gasoline.
摘要翻译： 描述了富含MTBE和TAME富含高辛烷值汽油馏分的芳烃生产的综合方法。 异烯烃的醚化在过量甲醇的存在下进行。 将未反应的甲醇通入与ZSM-5催化剂和烯烃和链烷烃进料流接触的固定的，流动的或移动的床芳构化区以产生高辛烷值汽油。
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公开(公告)号：US4822480A
公开(公告)日：1989-04-18
申请号：US137113
申请日：1987-12-22
CPC分类号： C10G49/22
摘要： Improved product stripping in a catalytic hydrodesulfurization (CHD) product stream is obtained by employing off-gas from the unit as a stripping medium. The compressed off-gas is introduced into the stripper below the stripper feed level. The stripper may be operated at pressures higher than those previously employed in CHD product strippers and this permits LPG recovery to be maximized with lower product sulfur levels and reduced load in the off-gas compressor.
摘要翻译： 通过使用来自该单元的废气作为汽提介质来获得催化加氢脱硫（CHD）产物流中的改进的产物汽提。 压缩的废气在汽提器进料液位下方引入汽提器。 汽提器可以在高于CHD产品汽提器中以前使用的压力下操作，并且这允许LPG回收率随着废气压缩机中较低的产品硫含量和减少的负荷而最大化。
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50.发明授权Production of heavier hydrocarbons from light olefins in multistage catalytic reactors 失效在多级催化反应器中从轻质烯烃生产较重的烃
公开(公告)号：US4788366A
公开(公告)日：1988-11-29
申请号：US137913
申请日：1987-12-28
申请人： Mohsen N. Harandi , Hartley Owen , Samuel A. Tabak
发明人： Mohsen N. Harandi , Hartley Owen , Samuel A. Tabak
CPC分类号： C07C2/00 , C07C2/12 , C10G50/00 , C10L1/06 , C07C2529/40
摘要： A multi-stage catalytic olefin upgrading technique for converting lower olefinic feedstock to heavier liquid hydrocarbon product. The invention provides a fluid bed continuous primary stage reaction zone with shape selective medium pore zeolite oligomerization catalyst particles to convert at least a portion of the lower olefinic components to intermediate olefinic hydrocarbons containing olefinic and aromatic components; cooling primary stage reaction effluent to condense at least a portion of the intermediate hydrocarbons; feeding a second olefinic stream to a serially arranged multi-reactor secondary stage for upgrading lower olefins; quenching partially upgraded secondary stage olefins with primary stage liquid; and further contacting the quenched mixture including aromatics from the primary stage with shape selective medium pore zeolite olgiomerization catalyst in a high pressure fix bed secondary stage distillate mode catalytic reactor at elevated temperature and high prssure to provide a heavier hydrocarbon effluent stream comprising distillate hydrocarbons.
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