公开(公告)号：US07282616B2

公开(公告)日：2007-10-16

申请号：US10450949

申请日：2001-12-19

申请人： Jouko Nikkonen ,  Jyrki Hiltunen ,  Jaana Makkonen ,  Marja Tiitta ,  Isto Eilos ,  Pasi Hagelberg

发明人： Jouko Nikkonen ,  Jyrki Hiltunen ,  Jaana Makkonen ,  Marja Tiitta ,  Isto Eilos ,  Pasi Hagelberg

IPC分类号： C07C2/54 ,  C07C2/66

CPC分类号： C07C5/2775 ,  C07C2521/04 ,  C07C2521/12 ,  C07C2529/04 ,  C07C2529/85 ,  Y02P20/584 ,  Y10S585/922 ,  C07C11/02

摘要： A process for converting an olefin feed to hydrocarbons suitable for fuel components or their feedstock. According to the process, an olefin feed, possibly together with another hydrocarbon feed, is contacted in a reactor with a catalyst in order to produce a hydrocarbon having at least one alkyl side chain. In the invention, the olefin feed is contacted with a particle-form fluidized catalyst in a circulating-bed reactor, wherein the catalyst forms the circulating bed of the reactor. When the operation is carried out in a circulating-bed reactor, the retention time of the feedstock is short. In this case, iso-olefins are formed quite selectively from n-olefins in isomerization. Since the useful life of the catalyst lengthens while the catalytic activity of the bed remains high for a long time, the conversion level also remains high. A long useful life of the catalyst is an economically highly significant advantage. In a circulating-bed reactor the regeneration of the catalyst can be carried out quite flexibly, and the operation of the reactor need not be interrupted for the duration of regeneration.

摘要翻译： 将烯烃进料转化为适用于燃料组分或其原料的烃的方法。 根据该方法，烯烃进料可能与另一种烃进料一起在反应器中与催化剂接触，以便产生具有至少一个烷基侧链的烃。 在本发明中，烯烃进料在循环床反应器中与颗粒形式的流化催化剂接触，其中催化剂形成反应器的循环床。 当在循环床反应器中进行操作时，原料的停留时间短。 在这种情况下，异构烯烃在异构化中非常选择性地从正构烯烃形成。 由于催化剂的使用寿命延长，而床的催化活性长时间保持较高，转化率也保持较高。 催化剂的长期使用寿命是经济上显着的优势。 在循环床反应器中，可以相当灵活地进行催化剂的再生，并且在再生持续期间不需要中断反应器的操作。

公开(公告)号：US06533844B1

公开(公告)日：2003-03-18

申请号：US09762683

申请日：2001-04-11

申请人： Jyrki Hiltunen ,  Isto Eilos ,  Vesa Niemi

发明人： Jyrki Hiltunen ,  Isto Eilos ,  Vesa Niemi

IPC分类号： B01D4512

CPC分类号： B01D45/16 ,  B01D21/267 ,  B04C5/02 ,  B04C5/103 ,  B04C5/26 ,  C10G11/18 ,  F23C10/08 ,  F23J15/027 ,  F23J2217/40

摘要： The invention relates to a method for separating materials of two different phases from one another and an assembly for implementing the method. According to one embodiment of the invention, the second phase having the material in suspended or dispersed form is separated from the first phase by centrifugal force. At least one separator comprises a multiport cyclone into which the material flow is passed via an infeed nozzle having an annular cross section.

摘要翻译： 本发明涉及一种用于分离两个不同相的材料的方法以及用于实施该方法的组件。 根据本发明的一个实施方案，具有悬浮或分散形式的材料的第二相通过离心力与第一相分离。 至少一个分离器包括多孔旋风分离器，材料流经其具有环形横截面的进料喷嘴通过。

公开(公告)号：US6045688A

公开(公告)日：2000-04-04

申请号：US921384

申请日：1997-08-29

申请人： Seppo Ruottu ,  Kari Kaariainen ,  Jyrki Hiltunen

发明人： Seppo Ruottu ,  Kari Kaariainen ,  Jyrki Hiltunen

IPC分类号： B01J8/00 ,  B01J8/18 ,  B01J8/26 ,  C07C5/333 ,  C07C11/02 ,  C10G11/18 ,  C07C2/00 ,  C10G9/32

CPC分类号： C10G11/18 ,  B01J8/0055 ,  B01J8/1854 ,  B01J8/26 ,  C07C5/333 ,  Y02P20/584 ,  Y02P30/446 ,  Y10S585/924

摘要： The invention relates ro a method of converting hydrocarbons. According to the method, a gaseous or liquid hydrocarbon feed is passed into a circulating fluidized-bed reactor, wherein the feed is converted at a high temperatue under the influence of particulate matter kept in a fluidized state, and the converted hydrocarbon products are removed from the reactor in a gaseous phase. According to the invention, a circulating fluidized-bed reactor (1-3; 41-43) is used having an axially annular cross section and being equipped with a multiport cyclone (14,17; 52,63) for the separation of the particulate matter from the gas-phase reaction products. The reaction space comprises an intershell riser space (13; 50) formed between two concentrically located cylindrical and/or conical envelope surfaces. The separation of particulate matter from the gas-phase reaction products is performed by means of a multiport cyclone equipped with louvered vanes (14; 63).

摘要翻译： 本发明涉及转化烃的方法。 根据该方法，将气态或液态烃进料通入循环流化床反应器，其中在保持流化状态的颗粒物质的影响下，进料在高温下转化，并将转化的烃产物从 反应器处于气相。 根据本发明，使用循环流化床反应器（1-3; 41-43），其具有轴向环形横截面并且装备有用于分离颗粒物的多端口旋风器（14,17; 52,63） 物质来自气相反应产物。 反应空间包括在两个同心位置的圆柱形和/或圆锥形包络表面之间形成的壳体上升空间（13; 50）。 颗粒物质与气相反应产物的分离是通过装有百叶窗（14; 63）的多口旋风分离器进行的。

公开(公告)号：US07070645B2

公开(公告)日：2006-07-04

申请号：US10472506

申请日：2002-03-20

申请人： Jyrki Hiltunen ,  Kauko Suppola

发明人： Jyrki Hiltunen ,  Kauko Suppola

IPC分类号： B01D45/12

CPC分类号： B01D45/12 ,  B04C3/04 ,  B04C3/06 ,  B04C5/04 ,  B04C5/28 ,  F23J15/027 ,  F23J2217/40

摘要： The invention relates to a method and apparatus for separating two phases from each other. According to the invention, a stream made up of at least two phases is directed to a separation apparatus, which comprises a separation container (25) and cyclones (26) arranged in the flow direction in parallel and in succession, the cyclones having each an elongate separation chamber wherein the phases are separated from each other. According to the invention, the cyclones used are multi-inlet cyclones (26), the total number of which is at least 10. The stream to be treated is directed to each multi-inlet cyclone (26) in a substantially radial direction. Through the placement of a large number of multi-inlet cyclones in parallel, a purification element resembling a filter is obtained. In comparison to a filter, continuous regeneration takes place in the element, in which case the pressure loss does not increase during operation, since solids do not reduce the cross-sectional area of the flow conduit inside the element.

摘要翻译： 本发明涉及一种将两相分离的方法和装置。 根据本发明，由至少两相组成的料流被引导到分离装置，该分离装置包括分离容器（25）和沿流动方向平行并连续布置的旋风分离器（26），所述旋风分离器具有每个 细长分离室，其中相分离。 根据本发明，使用的旋风分离器是多入口旋风分离器（26），其总数至少为10.待处理的流在大致径向方向上被引导到每个多入口旋风分离器（26）。 通过平行放置大量多入口旋风分离器，可获得类似过滤器的净化元件。 与过滤器相比，在元件中发生连续再生，在这种情况下，在操作过程中压力损失不会增加，因为固体不会减小元件内的流动管道的横截面积。

公开(公告)号：US06858130B2

公开(公告)日：2005-02-22

申请号：US09778922

申请日：2001-02-08

申请人： Jyrki Hiltunen

发明人： Jyrki Hiltunen

IPC分类号： F23C10/18 ,  B01D45/16 ,  B01J8/00 ,  B04C5/26 ,  B04C5/28 ,  B04C9/00 ,  C10G11/18 ,  F23C10/08 ,  F23J15/00 ,  C10G11/00 ,  B01D45/12 ,  F27B15/12

CPC分类号： B04C5/28 ,  B01D45/16 ,  B01J8/0055 ,  C10G11/18 ,  F23C10/08

摘要： The present invention relates to a method and apparatus for separating particulate matter from a gaseous stream. According to the method, the gaseous stream containing the suspended particulates is passed into a separator apparatus which includes at least two multiple-inlet-multicyclones (16-16C), wherein the particulates are separated from the gas by centrifugal force. According to the invention, a separator apparatus is employed wherein at least two (16-16C) of the multiple-inlet cyclones are adapted to operate in parallel so as to form a multiple-inlet-multicyclone apparatus. The cyclone assembly according to the invention may be used as, e.g., the primary separator of an FCC unit, but more advantageously it serves as the secondary or tertiary separator of an FCC unit to remove “fines” from the flue gases of the preceding separation stages.

摘要翻译： 本发明涉及从气流中分离颗粒物质的方法和装置。 根据该方法，将含有悬浮颗粒的气流送入包括至少两个多入口 - 多气旋（16-16C）的分离器装置中，其中颗粒通过离心力与气体分离。 根据本发明，采用分离器装置，其中至少两个（16-16℃）的多入口旋风分离器适于并联操作，以形成多入口多气旋装置。 根据本发明的旋风组件可以用作例如FCC单元的主分离器，但更有利地，其用作FCC单元的二次或三次分离器以从前述分离的烟道气中除去“细粒” 阶段

公开(公告)号：US06814940B1

公开(公告)日：2004-11-09

申请号：US09623018

申请日：2000-10-30

申请人： Jyrki Hiltunen ,  Steven Gust ,  Jukka-Pekka Nieminen

发明人： Jyrki Hiltunen ,  Steven Gust ,  Jukka-Pekka Nieminen

IPC分类号： B01J818

CPC分类号： B01J8/0055 ,  B01J8/1854 ,  B01J8/26 ,  C10B49/22 ,  C10B53/00 ,  C10B53/02 ,  Y02E50/14 ,  Y02P20/145

摘要： The present invention concerns a process and an apparatus for thermal conversion of biomass and organic wastes. According to the invention, the feedstock is fed into a fluidized-bed reactor, wherein the feed is converted at an elevated temperature under the influence of particulate matter kept in a fluidized state by a fluidizing gas, the particulate matter is transferred from the reactor to a regenerator for regeneration and then recirculated to the reactor after the regeneration, and the converted hydrocarbon products are recovered from the reactor. Both the reactor and the regenerator comprise risers having an axially annular cross section and being equipped with multi-inlet cyclones for the separation of particulate matter. By means of the invention, it is possible to producer pyrolysis oil, the quality of which is higher than that of oil produced with the processes of the prior art. The incorporation of multi-inlet cyclones into the reactor configuration reduces gas velocities, reduces the physical size of the cyclone and shortens the residence time of gases in the cyclone.

摘要翻译： 本发明涉及用于生物质和有机废物的热转化的方法和装置。 根据本发明，将原料进料到流化床反应器中，其中进料在升高的温度下在流化气体保持在流化状态的颗粒物质的影响下转化，颗粒物质从反应器转移到 用于再生的再生器，然后在再生之后再循环到反应器中，并且将转化的烃产物从反应器中回收。 反应器和再生器都包括具有轴向环形横截面并具有用于分离颗粒物质的多入口旋风分离器的提升管。 通过本发明，可以生产热解油，其质量高于用现有技术方法生产的油的质量。 将多入口旋风分离器并入反应器构型可降低气体速度，减小旋风分离器的物理尺寸并缩短气体在旋风分离器中的停留时间。