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1. 发明申请

WO2017025330A1 PROCESS FOR THE POLYMERIZATION OF OLEFINS 审中-公开
标题翻译：烯烃聚合方法
公开(公告)号：WO2017025330A1
公开(公告)日：2017-02-16
申请号：PCT/EP2016/067901
申请日：2016-07-27
申请人： SABIC GLOBAL TECHNOLOGIES B.V.
发明人： BANAT, Yahya , ALSHAIBAN, Ahmad, Abdullah , AL-HUMAIDAN, Osamah
IPC分类号： C08F2/01 , B01J8/08 , C08F110/06 , C08F210/06 , C08F2/34 , C08F10/06 , C08F10/00 , C08F110/02 , C08F210/02 , C08F10/02
CPC分类号： C08F2/01 , B01J8/08 , B01J8/1818 , B01J8/1827 , B01J8/1836 , B01J2208/00176 , B01J2208/00274 , B01J2208/00991 , C08F2/34 , C08F10/00 , C08F10/02 , C08F10/06 , C08F110/02 , C08F110/06 , C08F210/02 , C08F210/06 , C08F210/16
摘要： The present invention relates to a process for the continuous preparation of a polyolefin in a reactor from one or more α-olefin monomers of which at least one is ethylene or propylene, wherein the reactor comprises a fluidized bed, an expanded section located at or near the top of the reactor, a distribution plate located at the lower part of the reactor and an inlet for a recycle stream located under the distribution plate wherein the process comprises - feeding a polymerization catalyst to the fluidized bed in the area above the distribution plate - feeding the one or more α-olefin monomers to the reactor - withdrawing the polyolefin from the reactor - circulating fluids from the top of the reactor to the bottom of the reactor, wherein the circulating fluids are compressed using a compressor and subsequently cooled using a heat exchanger to form a cooled recycle stream comprising liquid, and wherein the cooled recycle stream is introduced into the reactor using the inlet for the recycle stream wherein a part of the cooled recycle stream is drawn to form a liquid comprising stream, wherein the liquid comprising stream is introduced into the expanded section during at least part of the polymerization process, and wherein the liquid comprising stream is brought into contact with at least part of the interior surface of the expanded section.
摘要翻译：本发明涉及一种在反应器中从一种或多种α-烯烃单体连续制备聚烯烃的方法，其中至少一种是乙烯或丙烯，其中反应器包括流化床，位于或接近反应器的顶部，位于反应器下部的分配板和位于分配板下方的再循环流的入口，其中该方法包括 - 将聚合催化剂供给到分配板上方的流化床中 - 将一种或多种α-烯烃单体进料到反应器中 - 从反应器中回收聚烯烃 - 将反应器的顶部循环流体循环到反应器底部，其中使用压缩机压缩循环流体，随后使用热量交换器以形成包含液体的冷却循环流，并且其中使用r的入口将冷却的循环流引入反应器循环流，其中将一部分冷却的再循环料流抽吸以形成包含料流的液体，其中在聚合过程的至少部分期间将包含流体的液体引入膨胀部分，并且其中将包含流体的液体与膨胀部分的内表面的至少一部分。

2. 发明申请

WO2013162623A1 METHOD FOR ALKYLATION OF TOLUENE TO FORM STYRENE AND ETHYLBENZENE UTILIZING A MOVING BED REACTOR 审中-公开
标题翻译：氧化苯甲酸形成苯乙烯的方法和利用移动床反应器的乙烯苯
公开(公告)号：WO2013162623A1
公开(公告)日：2013-10-31
申请号：PCT/US2012/037693
申请日：2012-05-14
申请人： FINA TECHNOLOGY, INC. , PELATI, Joseph, E.
发明人： PELATI, Joseph, E.
IPC分类号： B01J29/08 , B01J29/00 , C07C2/86
CPC分类号： B01J8/12 , B01J8/08 , B01J8/085 , B01J8/10 , B01J8/125 , B01J8/24 , B01J29/068 , B01J29/072 , B01J29/076 , B01J29/08 , B01J29/082 , B01J29/084 , B01J29/085 , B01J29/087 , B01J29/10 , B01J29/103 , B01J29/16 , B01J29/163 , B01J29/40 , B01J29/60 , B01J29/7003 , B01J29/7007 , B01J29/7038 , B01J29/90 , B01J2208/00557 , B01J2219/0004 , B01J2229/186 , C07C2/862 , C07C2529/08 , C07C2529/10 , C07C2529/16 , Y02P20/584 , C07C15/46
摘要： A method is disclosed for making styrene and/or ethylbenzene by reacting toluene with a Ci source in the presence of a catalyst in a reactor sized and configured to provide for a moving catalyst bed therethrough to form a product stream including styrene and/or ethylbenzene.
摘要翻译：公开了一种通过在反应器中在催化剂存在下使甲苯与C 1 C反应来制备苯乙烯和/或乙苯的方法，其尺寸和构造为提供通过其移动的催化剂床以形成包含苯乙烯和/或乙苯的产物流。

3. 发明申请

WO2013142026A1 PROCESS AND APPARATUS FOR FLUID CATALYTIC CRACKING 审中-公开
标题翻译：流体催化裂化的工艺和装置
公开(公告)号：WO2013142026A1
公开(公告)日：2013-09-26
申请号：PCT/US2013/028497
申请日：2013-03-01
申请人： UOP LLC
发明人： PALMAS, Paolo
IPC分类号： C10G11/18
CPC分类号： C10G11/182 , B01J8/0055 , B01J8/08 , B01J8/26 , B01J21/20 , B01J29/90 , B01J38/06 , C10G11/00
摘要： One exemplary embodiment can be a process for fluid catalytic cracking. The process can include sending a first catalyst from a first riser reactor and a second catalyst from a second riser reactor to a regeneration vessel having a first stage and a second stage. The first catalyst may be sent to the first stage and the second catalyst may be sent to the second stage of the regeneration vessel. Generally, the first stage is positioned above the second stage.
摘要翻译：一个示例性实施方案可以是流化催化裂化的方法。该方法可以包括将第一催化剂从第一提升管反应器和第二催化剂从第二提升管反应器送到具有第一阶段和第二阶段的再生容器。可将第一催化剂送至第一阶段，第二催化剂可送至再生容器的第二阶段。通常，第一阶段位于第二阶段之上。

4. 发明申请

WO2009124034A1 LAYERS DURABLY BONDED TO SURFACES 审中-公开
标题翻译：层数与表面贴合
公开(公告)号：WO2009124034A1
公开(公告)日：2009-10-08
申请号：PCT/US2009/038931
申请日：2009-03-31
申请人： THE GOVERNMENT OF THE UNITED STATES OF AMERICA, AS REPRESENTED BY THE SECRETARY OF THE AIR FORCE , TRIBOLOGIX, INC., LICENSEE , ZABINSKI, Jeffrey S.
发明人： ZABINSKI, Jeffrey S.
IPC分类号： B42C11/00
CPC分类号： B05D5/086 , B01J8/08 , B01J8/10 , B01J8/38 , B05D1/24 , B05D1/36 , B05D5/00 , B05D5/08 , B05D5/083 , B05D5/12 , B05D7/52 , B05D2401/32 , B32B9/00 , B32B9/04 , B32B9/041 , B32B15/00 , B32B15/04 , B32B2250/02 , B32B2250/20 , B32B2264/10 , B32B2264/102 , B32B2264/104 , B32B2264/105 , B32B2264/107 , B32B2264/108 , B32B2264/12 , B32B2307/30 , B32B2307/40 , B32B2307/714 , B32B2307/746 , B32B2307/752 , C23C28/042 , C23C28/044 , F16N15/00 , Y10T428/12493 , Y10T428/30 , Y10T428/31678
摘要： A method and class of bond coat is provided herein that physically and chemically bonds solid layer lubricants and other functional coatings to a substrate by burnishing, for example, selected soft materials, including oxides such as antimony trioxide which is seen as a major improvement over conventional bonding or coating methods. The process is non-vacuum at ambient temperatures, no binders, adhesives, curing or baking. Lubricant performance can be enhanced by orders of magnitude compared to when the bond coat and burnishing process are not applied. The method is inexpensive, environmentally friendly, applicable to any substrate material, and scalable.
摘要翻译：本文提供了一种方法和类型的粘合涂层，其通过抛光例如选择的软材料（例如氧化物，例如三氧化锑）将固体层润滑剂和其它功能性涂层物理和化学键合到基底上，其被认为是比常规的主要改进粘合或涂布方法。该过程在环境温度下是非真空的，没有粘合剂，粘合剂，固化或烘烤。与不施加粘合涂层和抛光工艺相比，润滑剂性能可以提高数量级。该方法廉价，环保，适用于任何基材，并具有可扩展性。

5. 发明申请

WO2005104752A3 EBULLATED BED HYDROPROCESSING METHODS AND SYSTEMS AND METHODS OF UPGRADING AN EXISTING EBULLATED BED SYSTEM 审中-公开
标题翻译： EBULLED BED HYDROPROCESSING METHODS AND SYSTEMS AND METHODS OF UPGRADING AEDING EBULLED BED SYSTEM
公开(公告)号：WO2005104752A3
公开(公告)日：2006-04-06
申请号：PCT/US2005014435
申请日：2005-04-28
申请人： HEADWATERS HEAVY OIL LLC
发明人： LOTT ROGER K , LEE LAP-KEUNG
IPC分类号： C10G45/00 , C10G47/00 , C10G47/26 , C10G47/02 , B01J8/18 , C10G65/02 , C10G65/10
CPC分类号： C10G47/06 , B01J8/08 , B01J8/22 , B01J8/226 , C10G45/04 , C10G45/16 , C10G45/34 , C10G45/46 , C10G45/56 , C10G47/26 , C10G49/005 , C10G49/12 , C10G65/00 , C10G65/02 , C10G67/08 , C10G2300/1033 , C10G2300/107 , C10G2300/1077 , C10G2300/202 , C10G2300/206 , C10G2300/4056 , C10G2300/70 , C10G2300/703 , C10G2300/802
摘要： An ebullated bed hydroprocessing system, and also a method for upgrading a pre-existing ebullated bed hydroprocessing system, involves introducing a colloidal or molecular catalyst, or a precursor composition capable of forming the colloidal or molecular catalyst, into an ebullated bed reactor. The colloidal or molecular catalyst is formed by intimately mixing a catalyst precursor composition into a heavy oil feedstock and raising the temperature of the feedstock to above the decomposition temperature of the precursor composition to form the colloidal or molecular catalyst in situ. The improved ebullated bed hydroprocessing system includes at least one ebullated bed reactor that employs both a porous supported catalyst and the colloidal or molecular catalyst to catalyze hydroprocessing reactions involving the feedstock and hydrogen. The colloidal or molecular catalyst provides catalyst in what would otherwise constitute catalyst free zones within the ebullated bed hydroprocessing system. Asphaltene or other hydrocarbon molecules too large to diffuse into the pores of the supported catalyst can be upgraded by the colloidal or molecular catalyst. A slurry phase reactor may be positioned upstream from one or more ebullated bed reactors or converted from a pre-existing ebullated bed reactor.
摘要翻译：沸腾床加氢处理系统以及用于升级预先存在的沸腾床加氢处理系统的方法包括将能形成胶体或分子催化剂的胶体或分子催化剂或前体组合物引入沸腾床反应器中。胶体或分子催化剂通过将催化剂前体组合物紧密地混合到重油原料中并将原料的温度升高到高于前体组合物的分解温度以形成原位形成胶态或分子催化剂而形成。改进的沸腾床加氢处理系统包括至少一个沸腾床反应器，其使用多孔负载催化剂和胶体或分子催化剂催化涉及原料和氢的加氢反应。胶体或分子催化剂提供催化剂，否则将在沸腾床加氢处理系统内构成催化剂自由区。太大而不能扩散到负载型催化剂的孔中的沥青质或其他烃类分子可以通过胶体或分子催化剂来提升。浆料相反应器可以位于一个或多个沸腾床反应器的上游，或从预先存在的沸腾床反应器中转化。

6. 发明申请

WO00042372A1 AGITATED BED COOLING, DRYING, OR HEATING APPARATUS 审中-公开
标题翻译：干燥或加热装置
公开(公告)号：WO00042372A1
公开(公告)日：2000-07-20
申请号：PCT/US2000/000767
申请日：2000-01-12
IPC分类号： B01J8/08 , B01J8/10 , B01J8/36 , F26B3/28 , F26B3/30 , F26B17/02 , F26B17/04 , F26B17/24 , F26B19/00 , B07B1/00 , B07B1/04 , B65G35/00 , B65G37/00 , B65G47/10 , F26B3/34 , F26B5/14 , F26B7/00 , F26B9/00 , F26B17/12
CPC分类号： F26B3/30 , B01J8/08 , B01J8/10 , B01J8/36 , B01J2208/00203 , F26B3/283 , F26B3/305 , F26B17/02 , F26B17/045 , F26B17/24
摘要： An agitated bed apparatus (20) for heating, cooling and/or drying particulate material (152) is provided which includes a housing (22) having an elongated flexible bed (24) therein adapted to receive the material (152). An agitator assembly (26) made up of a series of rotatable beater bar units (70) is located below the bed (24) and oriented for repeatedly impacting the bed (24) to establish an undulating bed movement for elevation and tumbling of the particulate material (152). A material conditioning unit (156) such as an infrared heating unit array (28) is located above the bed (24) so as to expose the particulate material (152) to hot, cool, or ambient air for heating, drying, or cooling thereof. In another embodiment, the apparatus (20) includes a plurality of units (156) which are slidably removable from the housing (22) of the apparatus (20).
摘要翻译：提供了一种用于加热，冷却和/或干燥颗粒材料（152）的搅拌床装置（20），其包括其中适于接纳材料（152）的细长柔性床（24）的壳体（22）。由一系列可旋转的搅拌棒单元（70）组成的搅拌器组件（26）位于床（24）下方并且被定向成反复冲击床（24）以建立起伏的床运动，以提高和翻转颗粒材料（152）。诸如红外加热单元阵列（28）的材料调节单元（156）位于床（24）上方，以将颗粒材料（152）暴露于热，冷或环境空气中用于加热，干燥或冷却它们。在另一个实施例中，装置（20）包括可从装置（20）的壳体（22）可滑动地移除的多个单元（156）。

7. 发明申请

WO1988006201A1 PROCESS FOR PRODUCTION OF CELLULOSE PULP AND/OR DELIGNIFICATION OF SECONDARY FIBERS 审中-公开
标题翻译：生产纤维素浆的方法和/或二次纤维的修饰
公开(公告)号：WO1988006201A1
公开(公告)日：1988-08-25
申请号：PCT/NO1988000011
申请日：1988-02-11
申请人： FONGEN, Sigurd
IPC分类号： D21C03/00
CPC分类号： D21C9/00 , B01J8/005 , B01J8/08 , D21C7/00
摘要： In a process for digesting plant and wood fibers or for delignification, optinally with preceding deinking, of fibers from chemical or mechanical pulps, optionally with succeeding bleaching, the fibrous raw material is digested or delignified in an alkaline pumpable slurry in a pressurized tube system and conducted therethrough by the use of pulp pumps. On its way through the pressurized tube system the pulp is repeatedly dewatered and after each dewatering, save the last one, is rediluted with pressed out process liquor recycled from a downstream dewatering step and/or from a downstream pumping stage of the process. While being conducted through the pressurized tube system the pulp is subjected to stepwise increasing pressure, the pressure increase being caused by the pulp pumps. An apparatus for use in carrying out the process comprises an inner perforated tube (83) surrounded by an outer tube (85) which at its ends is sealed against the inner tube (83). The outer tube (85) which is capable of enduring high pressures is provided with one or more tubes (86) for receiving process liquor pressed out from the pulp through the perforations of the inner tube (83).

8. 发明申请

WO2017087187A1 MULTIPHASE SEPARATOR AND METHODS OF USE THEREOF FOR PRODUCING HYDROCARBONS FROM OXYGENATES AND OLEFINS 审中-公开
标题翻译：多相分离器及其用于从氧化物和烯烃生产烃的方法
公开(公告)号：WO2017087187A1
公开(公告)日：2017-05-26
申请号：PCT/US2016/060518
申请日：2016-11-04
申请人： EXXONMOBIL RESEARCH AND ENGINEERING COMPANY
发明人： BEHKISH, Arsam , RATERMAN, Michael Francis , KARRI, Surya Bhaskara Reddy
IPC分类号： B01J8/00 , C10G11/16 , C10G3/00 , B01J8/12 , B01J8/44
CPC分类号： C07C1/20 , B01J8/005 , B01J8/08 , B01J8/125 , B01J8/44 , B01J19/24 , B01J2219/24 , C10G3/54 , C10G11/16
摘要： Multiphase separators, processes and systems for converting an oxygenate and/or olefin feedstock to a hydrocarbon product are described herein.
摘要翻译：本文描述了用于将含氧化合物和/或烯烃原料转化成烃产物的多相分离器，方法和系统。

9. 发明申请

WO2017032683A1 PROCESS FOR CONTINUOUS POLYMERIZATION OF OLEFIN MONOMERS IN A REACTOR 审中-公开
标题翻译：烯烃单体在反应器中连续聚合的方法
公开(公告)号：WO2017032683A1
公开(公告)日：2017-03-02
申请号：PCT/EP2016/069591
申请日：2016-08-18
申请人： SABIC GLOBAL TECHNOLOGIES B.V.
发明人： BANAT, Yahya , WAJEEH, Moughrabiah
IPC分类号： C08F2/01 , B01J8/08 , B01J8/18 , B01J8/24 , C08F2/34
CPC分类号： C08F2/01 , B01J8/08 , B01J8/18 , B01J8/24 , C08F2/34 , C08F210/16 , C08F210/06 , C08F2/00
摘要： The invention relates to a process and system for the continuous polymerization of one or more α-olefin monomers comprising the steps of: (a) withdrawing fluids from a reactor (b) cooling fluids comprising the withdrawn fluids with a cooling unit (c) introducing the cooled fluids to a separator to separate at least part of the liquid from these fluids to form a liquid phase and a gas/liquid phase (d) introducing the gas/liquid phase below to the reactor below a distribution plate (e) introducing the liquid phase to a settling tank to separate liquid from fines that settle down in the settling tank (f) introducing liquid from the settling tank upstream of the cooling unit.
摘要翻译：本发明涉及用于连续聚合一种或多种α-烯烃单体的方法和系统，包括以下步骤：（a）从反应器中取出流体（b）用冷却单元冷却包含排出的流体的流体（c）引入将冷却的流体输送到分离器以将至少部分液体与这些流体分离以形成液相和气/液相（d）将下面的气/液相引入到分布板下方的反应器（e）液相到沉淀池，以将液体与沉降在沉淀池中的细粉分离（f）将来自沉淀槽的液体从冷却单元的上游引入。

10. 发明申请

WO2015199605A1 A STEAM SEPARATION UNIT FOR A SYSTEM FOR HYDROLYSIS OF LIGNOCELLULOSIC BIOMASS MATERIAL 审中-公开
标题翻译：用于水解生物质生物质材料的系统的蒸汽分离装置
公开(公告)号：WO2015199605A1
公开(公告)日：2015-12-30
申请号：PCT/SE2015/050732
申请日：2015-06-24
申请人： VALMET AB
发明人： THYR, Anders , AHLGREN, Örjan , SJÖBLOM, Krister
IPC分类号： B04C5/18 , B01D45/02 , B01D45/12 , C13K1/02
CPC分类号： B01D45/12 , B01D45/02 , B01J8/08 , B04C5/18 , B04C5/22 , C12M45/20 , C13K1/02
摘要： A steam separation unit for separation of steam from lignocellulosic biomass material in a hydrolysis process comprising a treatment vessel including a separation section and a biomass collection section. The separation section is arranged with at least one inlet for receiving at least partly hydrolyzed biomass material mixed with steam and at least one control outlet for discharging the steam from the vessel. A biomass collection section arranged to be filled at least partly with liquid during operation and coupled to the separation section to collect the biomass material after separation from steam, wherein the biomass collection section includes a mixing element for mixing the biomass material with liquid and at least one control valve for discharging biomass material mixed with liquid. A system for hydrolysis of lignocellulosic biomass material including such a separation unit is also presented.
摘要翻译：一种蒸汽分离单元，用于在水解过程中从木质纤维素生物质材料中分离蒸汽，所述水解方法包括包括分离部分和生物质收集部分的处理容器。分离段布置有至少一个入口，用于接收与蒸汽混合的至少部分水解的生物质材料和用于从容器排出蒸汽的至少一个控制出口。一种生物质收集部分，其布置成在操作期间至少部分地用液体填充并且与分离部分相连，以在与蒸汽分离之后收集生物质材料，其中生物质收集部分包括用于将生物质材料与液体混合的混合元件一个用于排放与液体混合的生物质材料的控制阀。还提出了包括这种分离单元的木质纤维素生物质材料的水解系统。

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