-
1.发明授权Alkylation process using co-current downflow reactor with a continuous hydrocarbon phase 失效使用具有连续烃相的并流下流反应器的烷基化方法
公开(公告)号：US5345027A
公开(公告)日：1994-09-06
申请号：US933163
申请日：1992-08-21
申请人： Jonathan E. Child , Kenneth J. Del Rossi , Albin Huss, Jr. , Frederick J. Krambeck , Thomas R. Melli , Sergei Yurchak
发明人： Jonathan E. Child , Kenneth J. Del Rossi , Albin Huss, Jr. , Frederick J. Krambeck , Thomas R. Melli , Sergei Yurchak
CPC分类号： C07C2/62 , B01J27/12 , B01J27/16 , C07C2527/1213 , C07C2527/173
摘要： A continuous alkylation process for the production of high octane gasoline comprising contacting a mixture of an isoparaffin and an olefin with a catalyst complex comprising BF3:H.sub.3 PO.sub.4 in a continuous hydrocarbon downflow reactor.
摘要翻译： 包括用于生产高辛烷值汽油的连续烷基化方法，包括使异链烷烃和烯烃的混合物与包含BF 3 :H 3 PO 4的催化剂络合物在连续的烃下流反应器中接触。
-
公开(公告)号：US5258568A
公开(公告)日：1993-11-02
申请号：US965306
申请日：1992-10-23
CPC分类号： C07C2/62 , C07C2527/054 , C07C2527/1206
摘要： A single path process for alkylating a hydrocarbon feedstock containing an olefin and an isoparaffin is disclosed. The process includes dispersing an acid-based liquid alkylation catalyst into a reaction zone for contact with a continuous hydrocarbon phase. The process further includes separating the hydrocarbon phase from the acid catalyst upon completion of the alkylation reaction and providing a continuous on-line regeneration of the entire volume of catalyst once it has been separated from the hydrocarbon phase.
摘要翻译： 公开了用于烷基化含有烯烃和异链烷烃的烃原料的单程方法。 该方法包括将酸基液体烷基化催化剂分散在与连续烃相接触的反应区中。 该方法还包括在烷基化反应完成时从酸催化剂中分离出烃相，并且一旦将其从烃相中分离出来，就提供了整个体积催化剂的连续在线再生。
-
公开(公告)号：US4973790A
公开(公告)日：1990-11-27
申请号：US437138
申请日：1989-11-16
CPC分类号： C10G69/126 , C07C11/02 , C07C2/12 , C07C7/12 , C07C2529/40
摘要： A process for oligomerizing C2 to C10 olefins obtained by catalytic cracking of heavy crude oil is disclosed. The olefins are oligomerized in the presence of added hydrogen over a shape selective zeolite to gasoline and distillate products. Feed pretreatment, to remove basic nitrogen compounds present in light olefin stream in refinery, with water wash or a guard bed is practiced improves catalyst life.
摘要翻译： 公开了通过重质原油的催化裂化获得的C2至C10烯烃的低聚方法。 在形成选择性沸石的情况下，在加入氢气的情况下，烯烃被低聚化成汽油和馏出物。 进料预处理，以清除精炼厂中轻质烯烃流中存在的碱性氮化合物，用水洗或保护床，可以提高催化剂的使用寿命。
-
公开(公告)号：US4814536A
公开(公告)日：1989-03-21
申请号：US133416
申请日：1987-12-15
申请人： Sergei Yurchak
发明人： Sergei Yurchak
CPC分类号： C10G3/60 , C07C1/20 , C10G3/49 , C10G3/54 , C07C2529/40 , C10G2300/4018 , C10G2400/02 , Y02P20/582 , Y02P30/20
摘要： An improved MTG process for converting lower aliphatic C.sub.1 -C.sub.4 oxygenates, such as methanol, to gasoline boiling range hydrocarbons is disclosed which is capable of obtaining improved cycle average gasoline yields and improved catalyst life by programming the methanol WHSV from high values at essentially quantitative methanol conversion at the start of a cycle to low values at essentially quantitative methanol conversion at the end of a cycle.
摘要翻译： 公开了用于将低级脂族C 1 -C 4含氧化合物如甲醇转化为汽油沸程烃的改进的MTG方法，其能够通过在基本上定量的甲醇中从高值编程甲醇WHSV获得改善的循环平均汽油产率和改善催化剂寿命 在循环开始时转化为在一个循环结束时基本上定量甲醇转化的低值。
-
公开(公告)号：US4404414A
公开(公告)日：1983-09-13
申请号：US425845
申请日：1982-09-28
申请人： Joe E. Penick , Sergei Yurchak , John C. Zahner
发明人： Joe E. Penick , Sergei Yurchak , John C. Zahner
CPC分类号： C10G3/54 , C07C1/20 , C10G3/49 , C07C2529/40 , C10G2300/4006 , C10G2300/4081 , C10G2300/802 , C10G2400/02 , Y02P30/20
摘要： A methanol-to-gasoline conversion process in which the conversion is conducted in a number of reactors which are fed directly by the charge, preferably in equal proportions. A diluent gas, preferably recycled light hydrocarbons separated from the product, is passed in sequence through each of the beds to carry away the heat of reaction. In this way, a high effective recycle ratio is maintained in each bed although the actual recycle ratio for the entire system is low.
摘要翻译： 一种甲醇 - 汽油转化方法，其中转化是在直接通过电荷进料的多个反应器中进行，优选以相等比例进行。 将稀释气体，优选从产物分离出的再循环的轻质烃顺次通过每个床，以携带反应热。 以这种方式，尽管实际的整个系统的再循环比例较低，但是每个床中保持高的有效循环比。
-
公开(公告)号：US5262579A
公开(公告)日：1993-11-16
申请号：US991918
申请日：1992-12-17
IPC分类号： C01B7/19 , C07C2/62 , C07D333/48 , C07C7/10
CPC分类号： C07D333/48 , C01B7/195 , C07C2/62 , C07C2527/1206
摘要： The present invention provides a method for separating sulfolane from a mixture containing conjunct polymers, sulfolane, and hydrofluoric acid comprising the sequential steps of:(a) removing HF from said mixture to provide an intermediate stream containing less than about 30 weight percent HF;(b) contacting said intermediate stream with water;(c) contacting said intermediate stream with an aliphatic hydrocarbon co-solvent having from about 3 to about 20 carbon atoms concurrently with said water-contacting step (b);(d) recovering an extract stream enriched in sulfolane and hydrofluoric acid; and(e) recovering a raffinate stream enriched in conjunct polymers.
摘要翻译： 本发明提供了从含有结合聚合物，环丁砜和氢氟酸的混合物中分离环丁砜的方法，其包括以下顺序步骤：（a）从所述混合物中除去HF以提供含有少于约30重量％HF的中间物流; （b）使所述中间物流与水接触; （c）使所述中间物流与具有约3至约20个碳原子的脂族烃共溶剂与所述水接触步骤（b）同时接触; （d）回收富含环丁砜和氢氟酸的萃取物流; 和（e）回收富含结合聚合物的萃余液流。
-
公开(公告)号：US4966680A
公开(公告)日：1990-10-30
申请号：US200109
申请日：1988-05-31
申请人： Amos A. Avidan , Sergei Yurchak
发明人： Amos A. Avidan , Sergei Yurchak
CPC分类号： C10G57/02
摘要： Process and apparatus for upgrading light olefinic crackate gas from a fluidized catalytic cracking unit having a riser reactor for contacting hot solid cracking catalyst with a heavy hydrocarbon feedstock, said light crackate gas containing ethene, propene and other C.sub.1 -C.sub.4 lower aliphatics, comprising the steps of:reacting the light olefinic gas in contact with a fluidized bed of acid medium pore zeolite catalyst particles under oligomerization and/or aromatization conditions to produce a hydrocarbon effluent stream rich in C.sub.5.sup.+ hydrocarbons and a byproduct light gas rich in C.sub.1 -C.sub.4 saturated hydrocarbons;separating the oligomerization reaction effluent stream to provide a second light gas stream and a condensed liquid hydrocarbon product stream; andrecycling at least a portion of the second gas stream to the fluidized catalytic cracking unit as a lift gas for fluidizing solid cracking catalyst particles in a lower riser portion of said cracking unit.
摘要翻译： 用于从具有用于使热固体裂化催化剂与重质烃原料接触的提升管反应器的流化催化裂化装置升级轻烯烃裂化气体的方法和装置，所述轻质裂化气体含有乙烯，丙烯和其它C1-C4低级脂族烃，其包括步骤 ：在低聚和/或芳构化条件下使轻质烯属气体与酸性介质孔隙沸石催化剂颗粒的流化床接触，以产生富含C5 +烃的烃流出物流和富含C1-C4饱和烃的副产物轻质气体; 分离低聚反应流出物流以提供第二轻质气体流和冷凝液态烃产物流; 以及将所述第二气流的至少一部分再循环到所述流化催化裂化装置，作为用于在所述裂化装置的下部提升管部分中流化固体裂化催化剂颗粒的提升气体。
-
8.发明授权Method for gasoline yield enhancement in the fixed bed methanol-to-gasoline process 失效固定床甲醇对汽油过程中汽油产量提高的方法
公开(公告)号：US4523046A
公开(公告)日：1985-06-11
申请号：US352417
申请日：1982-02-25
申请人： Ronald M. Gould , Sergei Yurchak
发明人： Ronald M. Gould , Sergei Yurchak
CPC分类号： C10G3/49 , C10G2400/02 , Y02P30/20
摘要： Gasoline product yield is enhanced in a fixed bed methanol-to-gasoline process by splitting the conversion reactor into a series of smaller conversion reactors such that the total amount of catalyst normally present in the single conversion reactor is present in equal quantities in the smaller conversion reactors. The smaller conversion reactors operate sequentially with the next conversion reactor beginning operation only when the preceeding conversion reactor is catalytically exhausted. The by-passing of one or more of the catalyst beds prevents premature deactivation of the catalyst beds downstream of the point at which the reaction products are removed.
摘要翻译： 通过将转化反应器分成一系列较小的转化反应器，固定床甲醇 - 汽油过程中汽油产物产率提高，使得单一转化反应器中通常存在的催化剂的总量在较小的转化率中以相等的量存在 反应堆。 只有当先前的转化反应器被催化耗尽时，较小的转化反应器依次操作下一个转化反应器开始操作。 一个或多个催化剂床的旁路可以防止在除去反应产物的点下游的催化剂床的过早失活。
-
公开(公告)号：US5276243A
公开(公告)日：1994-01-04
申请号：US991922
申请日：1992-12-17
申请人： Michael A. Better , Jonathan E. Child , Kenneth J. Del Rossi , Anagha A. Gupte , Tomas R. Melli , Sergei Yurchak
发明人： Michael A. Better , Jonathan E. Child , Kenneth J. Del Rossi , Anagha A. Gupte , Tomas R. Melli , Sergei Yurchak
IPC分类号： C01B7/19 , C07C2/62 , C07D333/48 , C07C7/10
CPC分类号： C07D333/48 , C01B7/195 , C07C2/62 , C07C2527/1206
摘要： The present invention provides a method for separating conjunct polymers and sulfolane from a mixture containing conjunct polymers, sulfolane, and hydrofluoric acid comprising the sequential steps of:(a) separating hydrofluoric acid from said mixture to provide an intermediate stream containing less than about 30 percent hydrofluoric acid by weight;(b) gravitationally separating said intermediate stream into a sulfolane-enriched stream and a conjunct polymer-enriched stream;(c) contacting said sulfolane-enriched stream with a polar extraction solvent to provide an extract stream enriched in sulfolane and a raffinate stream enriched in conjunct polymers;(d) stripping the polar extraction solvent from said sulfolane-enriched extract stream; and(e) recovering sulfolane from said enriched stream of step (d).
摘要翻译： 本发明提供了从含有结合聚合物，环丁砜和氢氟酸的混合物中分离结合聚合物和环丁砜的方法，包括以下顺序步骤：（a）从所述混合物中分离出氢氟酸，以提供含有少于约30％ 氢氟酸; （b）将所述中间物流重力分离成富含环丁砜的物流和富含聚合物的混合物流; （c）使富含环丁砜的料流与极性萃取溶剂接触，以提供富含环丁砜的萃取物流和富含结合聚合物的萃余液流; （d）从所述富含环丁砜的萃取物流中汽提极性萃取溶剂; 和（e）从步骤（d）的富集流中回收环丁砜。
-
公开(公告)号：US5264651A
公开(公告)日：1993-11-23
申请号：US991920
申请日：1992-12-17
IPC分类号： C01B7/19 , C07C2/62 , C07D333/48 , C07C7/10
CPC分类号： C07D333/48 , C01B7/195 , C07C2/62 , C07C2527/1206 , Y02P20/584
摘要： This invention provides a method for separating ASO from a mixture containing ASO, HF and sulfolane comprising the steps of:(a) contacting said mixture with a sorbent to selectively sorb HF and water from said mixture to evolve an intermediate product containing less than 5 weight percent HF;(b) charging said intermediate product to a gravitational separation zone;(c) holding said intermediate product in said gravitational separation zone for time sufficient to evolve two at least partially immiscible liquid phases in said gravitational separation zone; and(d) withdrawing a less-dense phase enriched in ASO and a more-dense phase enriched in sulfolane from said gravitational separation zone.
摘要翻译： 本发明提供了一种从含有ASO，HF和环丁砜的混合物中分离ASO的方法，包括以下步骤：（a）使所述混合物与吸附剂接触以选择性地从所述混合物吸收HF和水，以释放含有小于5重量的中间产物 百分比HF; （b）将所述中间产物装入重力分离区; （c）在所述重力分离区中保持所述中间产物足以在所述重力分离区中放出两个至少部分不混溶的液相的时间; 和（d）从所述重力分离区取出富含ASO的较不密集的相和富含环丁砜的更致密相。
-
-
-
-
-
-
-
-
-
搜索结果
27 条记录 (耗时 0.017 秒)
