公开(公告)号：EP2450101A1

公开(公告)日：2012-05-09

申请号：EP11188225.4

申请日：2011-11-08

Applicant: Sumitomo Chemical Company, Limited

Inventor： Sumida, Masakazu ,  Yamazaki, Kazuhiro ,  Sato, Yoshinori ,  Wake, Takao

IPC: B01J19/18 ,  C08F2/00 ,  C08F2/01 ,  C08F2/02

CPC classification number: B01J19/0066 ,  B01J19/18 ,  B01J2219/0004 ,  B01J2219/00094 ,  B01J2219/00164 ,  B01J2219/002 ,  B01J2219/00202 ,  B01J2219/00204 ,  B01J2219/00213 ,  C08F2/001 ,  C08F2/01

Abstract: The present invention is directed to a novel continuous polymerization apparatus which is able to more efficiently produce a polymer composition suitable for obtaining a resin composition of high quality.
In the continuous polymerization apparatus at least first and second reactors (10, 20) of a complete mixing type are used. Each of the reactors (10, 20) is provided with a supply port (11a, 21a) and an effluent port (11b, 21b) which is located at the reactor's top; the supply port (11a) of the first reactor (10) is connected to a supply source (1, 3) of a raw material monomer and a polymerization initiator; and the effluent port (11b) of the first reactor (10) is connected to the supply port (21a) of the second reactor (20).

Abstract translation: 本发明涉及一种能够更有效地制备适于获得高品质树脂组合物的聚合物组合物的新型连续聚合装置。 在连续聚合装置中，使用完全混合型的至少第一和第二反应器（10,20）。 每个反应器（10,20）设置有供应口（11a，21a）和位于反应器顶部的排出口（11b，21b） 第一反应器（10）的供给口（11a）与原料单体和聚合引发剂的供给源（1,3）连接， 并且第一反应器（10）的排出口（11b）连接到第二反应器（20）的供给口（21a）。

公开(公告)号：EP1642638B1

公开(公告)日：2012-05-09

申请号：EP05256135.4

申请日：2005-09-30

Applicant: Sumitomo Chemical Company, Limited

Inventor： Yamazaki, Kazuhiro ,  Nishitani, Akira

IPC: B01J19/00 ,  B01J19/18 ,  C08F2/00

CPC classification number: B01J19/0013 ,  B01J19/18 ,  B01J2219/00063 ,  B01J2219/00094 ,  B01J2219/00164 ,  B01J2219/002 ,  B01J2219/00213 ,  B01J2219/0022 ,  B01J2219/00231 ,  B01J2219/00254 ,  C08F2/01 ,  C08F2/02 ,  Y10S526/92

公开(公告)号：EP1584120B1

公开(公告)日：2012-04-11

申请号：EP03811914.5

申请日：2003-11-21

Applicant: CASIO COMPUTER CO., LTD.

Inventor： BITOH, Hiroyasu

IPC: B01B1/00 ,  B01J19/00 ,  C01B3/38 ,  C01B3/58 ,  H01M8/02 ,  H01M8/06 ,  H01M8/04

CPC classification number: H01M8/04037 ,  B01B1/005 ,  B01J19/0093 ,  B01J2219/00191 ,  B01J2219/002 ,  B01J2219/00783 ,  B01J2219/00835 ,  B01J2219/00873 ,  B01J2219/00961 ,  C01B3/384 ,  C01B3/583 ,  C01B2203/00 ,  C01B2203/0233 ,  C01B2203/0283 ,  C01B2203/044 ,  C01B2203/047 ,  C01B2203/066 ,  C01B2203/0844 ,  C01B2203/085 ,  C01B2203/0866 ,  C01B2203/107 ,  C01B2203/1076 ,  C01B2203/1082 ,  C01B2203/1223 ,  C01B2203/1288 ,  C01B2203/16 ,  C01B2203/1604 ,  C01B2203/1619 ,  C01B2203/1685 ,  C01B2203/169 ,  C01B2203/1695 ,  H01M8/04007 ,  H01M8/04067 ,  H01M8/04268 ,  H01M8/04373 ,  H01M8/04604 ,  H01M8/04656 ,  H01M8/04686 ,  H01M8/0612

Abstract: A power supply system for producing electric power comprising at least a power generation section for generating power comprises at least one chemical reaction section to which fuel for power generation is supplied; heating sections for heating the chemical reaction section; and comprises a temperature detection section for detecting the temperature of the chemical reaction section that comprises an abnormal judgment means which judges abnormalities in the power supply system are occurring when discriminated that the temperature change of the chemical reaction section is not the proper variation quantity based on the heat of the heating sections.

公开(公告)号：EP1812352B1

公开(公告)日：2012-01-18

申请号：EP05800932.5

申请日：2005-11-11

Applicant: Hollingford Limited

Inventor： GIDNER, Anders

IPC: C02F11/08 ,  B01J3/00

CPC classification number: C02F11/086 ,  B01J3/008 ,  B01J19/2415 ,  B01J2208/00044 ,  B01J2208/00362 ,  B01J2208/0053 ,  B01J2208/00548 ,  B01J2219/00063 ,  B01J2219/00121 ,  B01J2219/00159 ,  B01J2219/00164 ,  B01J2219/002 ,  B01J2219/00231 ,  Y02P20/544

公开(公告)号：EP1098005B1

公开(公告)日：2011-05-11

申请号：EP00127181.6

申请日：1996-03-07

Applicant: Pressure Biosciences, Inc.

Inventor： Laugharn, James A., Jr. ,  Dreier, Gustav H. ,  Rudd, Edwin A. ,  Green, David J.

IPC: C07K1/04 ,  C12M1/40 ,  C07H21/00

CPC classification number: C12N9/00 ,  B01J3/00 ,  B01J19/185 ,  B01J2219/00162 ,  B01J2219/002 ,  B01J2219/00211 ,  B01J2219/00229 ,  Y10T436/143333

公开(公告)号：EP2249945A1

公开(公告)日：2010-11-17

申请号：EP08872812.6

申请日：2008-12-08

Applicant: Korea Research Institute Of Chemical Technology ,  Daelim Industrial Co., Ltd. ,  Doosan Mecatec Co., Ltd. ,  Korea National Oil Corporation ,  Hyundai Engineering Co., Ltd ,  SK Energy Co., Ltd.

Inventor： WOO, Kwang Jae ,  JUN, Ki-won ,  KANG, Suk-Hwan ,  KIM, Seung-Moon ,  BAE, Jong-Wook

IPC: B01D53/00

CPC classification number: B01J8/22 ,  B01J8/006 ,  B01J8/1809 ,  B01J2208/00061 ,  B01J2208/0007 ,  B01J2208/0061 ,  B01J2219/002 ,  B01J2219/00213 ,  B01J2219/00236 ,  C10G2/342 ,  C10G2300/4056 ,  C10G2300/4081

Abstract: The present invention relates to a continuous separation and discharge apparatus and method of solid catalysts and liquid products for Fischer-Tropsch synthesis reactions, and more particularly, to a continuous separation and discharge apparatus and method of solid catalysts and products for Fischer-Tropsch synthesis reactions involving the conversion of synthetic gas into synthetic oil, by which products of the Fischer-Tropsch synthesis including wax, as a long-chain hydrocarbon, can be stably obtained by continuously separating the products from a slurry comprising solid catalyst particles and the products using periodic pulses of a feeding gas and discharging the products through a lower portion of a reactor. Provided is a continuous separation and discharge apparatus of solid catalysts and products for Fischer-Tropsch synthesis reactions including: a level sensing device which is installed at an upper portion of a reactor and detects the slurry-level of reactants; a solid catalyst/ product separation device and a discharge device which are installed at a lower portion of the reactor and separate and discharge liquid products from a mixed slurry in the reactor; and a control unit which receives a signal from the level sensing device to open and close the discharge device, wherein the separation device filters the solid catalysts, and the discharge device continuously discharges the products separated from the solid catalysts through the lower portion of the reactor by the amount of the synthesized products measured by a level sensing device.

公开(公告)号：EP1812352A4

公开(公告)日：2010-10-06

申请号：EP05800932

申请日：2005-11-11

Applicant: HOLLINGFORD LTD

Inventor： GIDNER ANDERS

IPC: C02F11/08 ,  B01J20060101 ,  B01J3/00 ,  B01J19/24

CPC classification number: C02F11/086 ,  B01J3/008 ,  B01J19/2415 ,  B01J2208/00044 ,  B01J2208/00362 ,  B01J2208/0053 ,  B01J2208/00548 ,  B01J2219/00063 ,  B01J2219/00121 ,  B01J2219/00159 ,  B01J2219/00164 ,  B01J2219/002 ,  B01J2219/00231 ,  Y02P20/544

公开(公告)号：EP2201146A1

公开(公告)日：2010-06-30

申请号：EP08798767.3

申请日：2008-08-27

Applicant: Innovative Energy Solution

Inventor： Innovative Energy Solution

IPC: C22B7/00

CPC classification number: C01B3/36 ,  B01J8/001 ,  B01J8/0221 ,  B01J8/025 ,  B01J8/0278 ,  B01J8/0285 ,  B01J19/0013 ,  B01J2208/00088 ,  B01J2208/00176 ,  B01J2208/0053 ,  B01J2208/00548 ,  B01J2208/025 ,  B01J2219/002 ,  B01J2219/00231 ,  B01J2219/00236 ,  C01B3/02 ,  C01B3/48 ,  C01B17/046 ,  C01B2203/0244 ,  C01B2203/0261 ,  C01B2203/0283 ,  C01B2203/04 ,  C01B2203/0405 ,  C01B2203/042 ,  C01B2203/0883 ,  C01B2203/1235 ,  C01B2203/169

Abstract: The invention discloses an apparatus and process for the reformation of hydrogen containing fluids in a cyclic flow inert porous media reactor. The hydrogen containing fluid can be hydrogen sulfide. The cyclic flow reactor comprises a reaction chamber filled with a porous media matrix containing an unconstrained reaction zone located in any portion of the reactor chamber. This reactor system employs valves to canalize the reactant mixture and product mixture during flow cycling channeling the reactant mixture through the porous media matrix, and reacting the reactant mixture. In another embodiment, the reactor system may further comprise at least one aperture along the axial length of the reactor casing to enable mounting of an external energy source and /or at least one heat exchanger to' provide a source of heat transfer to the inlet pipe and outlet pipe as well as the reactant mixture and product mixtures.

公开(公告)号：EP2199369A1

公开(公告)日：2010-06-23

申请号：EP08834246.4

申请日：2008-09-26

Applicant: Nippon Steel Engineering Co., Ltd ,  Japan Oil Gas and Metals National Corporation ,  INPEX Corporation ,  Nippon Oil Corporation ,  Japan Petroleum Exploration Co. Ltd. ,  Cosmo Oil Co., Ltd.

Inventor： ONISHI, Yasuhiro ,  KATO, Yuzuru ,  YAMADA, Eiichi

IPC: C10G2/00 ,  B01J8/22 ,  G01F23/14

CPC classification number: G01F23/168 ,  B01J8/1809 ,  B01J8/1818 ,  B01J8/226 ,  B01J2208/00132 ,  B01J2208/00539 ,  B01J2208/00584 ,  B01J2208/0061 ,  B01J2219/002 ,  B01J2219/0022 ,  B01J2219/00234 ,  C10G2/342 ,  G01F23/18 ,  G01F23/185

Abstract: There is provided a bubble column type hydrocarbon synthesis reactor which synthesizes a hydrocarbon compound by a chemical reaction of a synthesis gas including hydrogen and carbon monoxide as main components, and a slurry having solid catalyst particles suspended in liquid. The hydrocarbon synthesis reactor includes a reactor main body which accommodates the slurry, a synthesis gas supplying section which supplies the synthesis gas to the slurry; one pressure sensor which is arranged higher than the liquid level of the slurry to measure the pressure of the synthesis gas above the liquid level, another pressure sensor which is arranged lower than the liquid level of the slurry to measure the pressure of the slurry, and a liquid level detecting device which detects a liquid level position of the slurry on the basis of measurement results of the pressure sensors. A plurality of the other pressure sensors are provided at arbitrary intervals in an axial direction of the reactor main body.

Abstract translation: 提供了通过包含氢和一氧化碳作为主要成分的合成气的化学反应合成烃化合物的气泡塔型烃合成反应器和悬浮在液体中的固体催化剂颗粒的浆料。 烃合成反应器包括容纳浆料的反应器主体，向浆料供给合成气的合成气供给部; 一个压力传感器被布置成高于浆液的液面以测量液面以上的合成气的压力，另一个压力传感器布置成低于浆液的液面以测量浆料的压力，以及 液位检测装置，其基于压力传感器的测量结果检测浆料的液面位置。 多个其它压力传感器以反应器主体的轴向任意间隔设置。

公开(公告)号：EP2192085A2

公开(公告)日：2010-06-02

申请号：EP09013185.5

申请日：2009-10-20

Applicant: Adensis GmbH

Inventor： Acker, Jörg, Prof. Dr. ,  Rietig, Anja ,  Meinel, Birgit, Dipl.-Chem.

IPC: C01B33/02

CPC classification number: C01B33/037 ,  B01J19/0086 ,  B01J19/18 ,  B01J2219/00006 ,  B01J2219/00177 ,  B01J2219/00182 ,  B01J2219/002 ,  B01J2219/00213 ,  B01J2219/00225 ,  B01J2219/00231 ,  B01J2219/0027 ,  C01B3/06 ,  Y02E60/36

Abstract: Dies Verfahren dient zum Entfernen von feinteiligem Silizium-Material, insbesondere mit Korngrößen kleiner als 1 µm, aus einem Silizium-Mahlgut (Si) mit Korngrößen kleiner als 500 µm. Das in einem Reaktionsbehälter (22) befindliche Silizium-Mahlgut (Si) wird mit einer wässrigen oder wasserenthaltenden Lösung einer Base (NaOH, KOH) aus einem Vorratsbehälter (26, 28) unter Rühren versetzt. Es erfolgen dabei eine Suspendierung und ein Aufschäumen. Hierbei findet ein Ätzprozess statt, bei dem die feine Fraktion mit Korngrößen kleiner als 1 µm chemisch entfernt wird. Diese Fraktion geht in Lösung. Nach einer gewünschten Zeit, nämlich sobald die feine Fraktion praktisch vollständig in Lösung gegangen ist, wird der Ätzprozess abgebrochen. Dies kann durch Zugabe einer Säure (HCl) aus einem weiteren Vorratsbehälter (30) geschehen. Alternativ kann dies auch durch Zugabe von viel Wasser aus einem zusätzlichen Vorratsbehälter (28) bewirkt werden. Der Zeitpunkt für das Abbrechen wird z. B. an einem Zeitgeber (86) eingestellt oder aber während des Ätzprozesses mit einem Messgerät (88, 90) ermittelt. Das zurückgebliebene grobkörnige Festgut (10) kann nun nach Sedimentierung für die weitere Verwendung oder Bearbeitung bereitgestellt werden.

Abstract translation: 除去细晶粒硅材料包括：选择地硅酮材料; 提供接地硅材料到反应容器中; 加入wässrige或水含有碱到地面硅材料的溶液; 加入酸或水，以终止蚀刻和引起悬浮快速沉降在相对粗粒度固体的形式; 以及提供所述沉降相对粗粒度的固体用于进一步处理或回抽相对粗粒度的固体，或两者上方形成的溶液中。 除去细晶粒硅材料与来自具有小于500微米的晶粒尺寸地面硅材料的小于1微米的晶粒尺寸包括：选择地面硅材料做展品主要为褐色在wässrige悬浮液，表明没有相当一部分 接地硅材料具有小于0:25微米的颗粒尺寸; 提供接地硅材料到反应容器中; 加入wässrige或碱到地面硅材料的溶液，从而导致蚀刻工艺产生的泡沫体积显著和化学移除具有小于约1微米的颗粒尺寸的细颗粒部分含水; 加入酸或水，以终止蚀刻和引起悬浮快速沉降在相对粗粒度固体的形式; 以及提供所述沉降相对粗粒度的固体用于进一步处理或回抽相对粗粒度的固体，或两者上方形成的溶液中。 一个独立的claimsoft是用于从地面硅材料具有小于500微米，包括晶粒尺寸去除具有小于1微米的晶粒尺寸细粒硅材料的装置：由储存容器用于接地硅氧烷互连构建的反应容器 材料，碱或储存容器一个wässrige或碱的溶液中，并在酸的储存容器含有水的; 用于可控地提供接地硅材料，碱或碱和酸到反应容器中的溶液的控制器; 用于搅拌反应容器中的内容的装置; 在由计时器或通过测量装置开采确定性一个预定时间的时刻中断酸到反应容器中的任一个供给单元; 安装在反应容器中用于除去相对粗粒固体的沉淀级分的第一抽出装置; 和安装在所述反应容器中的第二抽出装置用于除去驻留在沉淀级分以上的液体。