公开(公告)号：EP1256375B1

公开(公告)日：2011-01-19

申请号：EP01904514.5

申请日：2001-02-16

Applicant: Kaneka Corporation

Inventor： SHINOBUDANI, Koji, c/o The Japan Steel Works, Ltd ,  SHINOMIYA, Tetsuo, c/o The Japan Steel Works, Ltd ,  NAGAI, Mitsuo, c/o The Japan Steel Works, Ltd ,  HARAMOTO, Nobuhiro, c/o The Japan Steel Works, Ltd ,  MIYAHARA, Hiroshi, c/o The Japan Steel Works, Ltd ,  NINOMIYA, Toshiyuki, c/o The Japan Steel Works Ltd ,  NOSHO, Yasuharu, c/o Kaneka Corporation ,  HASHIMOTO, Shinichi, c/o Kaneka Corporation ,  KATO, Masakazu, c/o Kaneka Corporation ,  UESHIMA, Kazuhiro, c/o Kaneka Corporation

IPC: B01J3/02 ,  A23L1/00 ,  F15B15/22 ,  F16L55/02

CPC classification number: B01J3/00 ,  A23L3/0155 ,  B01J3/02 ,  B01J2219/00033 ,  G05D16/2066 ,  G05D16/2073

Abstract: A device and a method for continuous high-pressure treatment; the method, comprising the steps of increasing the pressure of raw material (25) in a feed tank (9) by a pressurizing pump (1) so as to continuously feed the raw material to treatment containers (6) and (6a) and increasing the flow rate of the pressurizing pump (1) over that of a depressurizing pump (2) or continuously exhausting the raw material from the treatment containers (6) and (6a) through a pressure regulating flow path resistance (59) while depressurizing; the device, comprising pressure releasing bypass circuits (55) disposed in the flow path resistance (59) in parallel with each other, wherein the insides of the treatment containers (6) and (6a) are kept in a specified high-pressure state during the continuous processing.

公开(公告)号：EP1238946B1

公开(公告)日：2009-01-21

申请号：EP00974863.3

申请日：2000-11-09

Applicant: Phild Co., Ltd.

Inventor： HIRATA, Yoshihiro, Phild Co. Ltd, Kawamoto Bldg. ,  UEDA, Yoshio ,  TAKASE, Hiroaki, Phild Co. Ltd., Kawamoto Bldg.

IPC: A23L1/30 ,  A23L2/52 ,  C01B5/00 ,  B01J8/22 ,  B01J3/04 ,  C02F1/68

CPC classification number: B22F1/0022 ,  A23L33/16 ,  A23V2002/00 ,  A61K33/24 ,  B01J3/00 ,  B01J3/02 ,  B01J10/002 ,  B01J19/0066 ,  B01J19/24 ,  B22F1/0018 ,  B22F9/06 ,  B22F2009/045 ,  B22F2998/00 ,  B82Y30/00 ,  C01B5/00 ,  C02F1/68 ,  A23V2250/1568

Abstract: A production method of water in which ultrafine gold particles on a 1- to 2-digit micron order in size, obtained by subdividing a normal gold fine particle size, are dissolved and which is excellent in physiologically active function such as health promotion; and its applications. A device comprising a pressure vessel provided with a high-pressure water storing tank, an oxygen/hydrogen mixing gas jetting nozzle, an ignition device and a combustion chamber is used to burn an oxygen/hydrogen mixing gas in a high-pressure water in which gold foils are floated, and to heat and melt the gold foils with the mixing gas to thereby produce ultrafine gold particle-dissolved water.

公开(公告)号：EP0853608B1

公开(公告)日：2001-07-18

申请号：EP96926517.2

申请日：1996-08-23

Applicant: METHANOL CASALE S.A.

Inventor： FILIPPI, Ermanno

IPC: C07C29/151 ,  C07C31/04 ,  C01C1/04 ,  B01J3/04

CPC classification number: C01B3/34 ,  B01J3/00 ,  B01J10/00 ,  C01B3/025 ,  C01B2203/0288 ,  C01B2203/0475 ,  C01B2203/0495 ,  C01B2203/061 ,  C01B2203/068 ,  C01B2203/0883 ,  C01B2203/1241 ,  C01B2203/141 ,  C07C29/1518 ,  C07C31/04

Abstract: A process for ammonia and methanol co-production in a plant comprising a secondary reformer section, a high-temperature CO conversion section and a low-temperature CO conversion section, arranged in series, and an ammonia synthesis section, is distinguished by the fact that the unreacted gas flow coming from a methanol synthesis section, before being fed to the low-temperature CO conversion section, is advantageously saturated with a liquid flow comprising H2O appropriately heated by indirect heat exchange with a gaseous flow coming from the secondary reformer section.

公开(公告)号：EP1007234A1

公开(公告)日：2000-06-14

申请号：EP96940549.7

申请日：1996-11-20

Applicant: CLEVELAND STATE UNIVERSITY

Inventor： GRAHAM, Edgar, E. ,  KOEBERLE, Roger, M. ,  CONEGLIO, Thomas, C. ,  BEDI, Raj, D.

IPC: B21B45/00 ,  B21B45/02

CPC classification number: B21J3/00 ,  B01J3/00 ,  C10M129/40 ,  C10M129/60 ,  C10M133/08 ,  C10M137/04 ,  C10M145/30 ,  C10M145/38 ,  C10M145/40 ,  C10M173/02 ,  C10M2207/125 ,  C10M2207/126 ,  C10M2207/129 ,  C10M2207/18 ,  C10M2209/104 ,  C10M2209/105 ,  C10M2209/109 ,  C10M2209/12 ,  C10M2215/042 ,  C10M2223/04 ,  C10M2223/041 ,  C10M2223/042 ,  C10M2225/00 ,  C10M2225/02 ,  C10N2240/402 ,  C10N2240/403 ,  C10N2240/404 ,  C10N2240/405 ,  C10N2240/406 ,  C10N2240/407 ,  C10N2240/408 ,  C10N2240/409 ,  C10N2250/02 ,  C10N2250/121

Abstract: An improved method to lubricate a metal workpiece at elevated working temperatures is described employing a novel liquid lubricant preparation which includes a vaporizable and polymerizable alkyl aromatic phosphate ester in combination with a die release agent selected from the group consisting of an organic binder and a fatty acid soap, to include mixtures thereof. The applied preparation forms a solid polymer lubricant in the forming die at the elevated working temperatures enabling lower applied pressures to be employed while producing superior workpieces.

公开(公告)号：EP0909261A1

公开(公告)日：1999-04-21

申请号：EP97936026.0

申请日：1997-06-06

Applicant: RPC Waste Management Services Inc., doing business as Eco Waste Technologies

Inventor： McBRAYER, Roy, N., Jr. ,  ELLER, James, M. ,  STANTON, Walter, H. ,  APPLEGATH, Fred ,  BARBER, John, S. ,  PEACOCK, Richard, D. ,  LOVETT, Gordon, H.

IPC: B01J3 ,  B01J19 ,  C02F1 ,  C02F11

CPC classification number: C02F11/086 ,  B01J3/00 ,  B01J3/008 ,  B01J3/044 ,  B01J19/2435 ,  B01J2219/00051 ,  B01J2219/00058 ,  B01J2219/00103 ,  B01J2219/00105 ,  B01J2219/00162 ,  C02F1/72 ,  Y02P20/544

Abstract: Systems and methods for heating, reacting, and/or treating a stream containing oxidizable matter, particularly reactor systems and methods utilizing oxidation reactions at or near supercritical conditions for water. Such systems and methods may be particularly useful to treat organic waste in aqueous-organic waste streams. Recycle reactor (100) is used alone or in conjunction with plug-flow reactor. Density differences in the recycle reactor facilitate flow within the recycle reactor without subtantial external heat exchange.

公开(公告)号：EP0814061A3

公开(公告)日：1998-07-22

申请号：EP97109058

申请日：1997-06-04

Applicant: EBARA CORP

Inventor： HIGO TSUTOMU ,  SERIKAWA ROBERTO MASAHIRO ,  KONDO KAZUHIRO

IPC: B09B3/00 ,  B01J3/00 ,  B01J3/04 ,  B01J19/00 ,  C02F1/72 ,  C02F1/78 ,  C02F3/08 ,  C02F11/08 ,  C02F11/10 ,  C02F11/18 ,  F23K1/02

CPC classification number: B01J3/00 ,  B01J3/04 ,  B01J2219/00087 ,  B01J2219/00162 ,  B01J2219/00182 ,  C02F1/025 ,  C02F1/722 ,  C02F1/78 ,  C02F11/08 ,  C02F11/083 ,  C02F11/18 ,  F23K1/02 ,  Y10S210/908

Abstract: A hydrothermal reaction is performed on an aqueous medium without adding an oxidizing agent, and then another hydrothermal reaction is performed in the presence of an oxidizing agent, thereby reducing a chemical oxygen demand of the aqueous medium. An apparatus for performing a hydrothermal reaction has a fluid inlet being capable of introducing an oxidizing agent in a fluid form during a hydrothermal reaction.

公开(公告)号：EP0832852A2

公开(公告)日：1998-04-01

申请号：EP97116376.1

申请日：1997-09-19

Applicant: Peroxid-Chemie GmbH

Inventor： Meichelböck, Wilfried ,  Gutewort, Sven, Dr. ,  Gnann, Michael, Dr.

IPC: C02F1/72

CPC classification number: B01J3/00 ,  B01J19/0013 ,  B01J2219/00067 ,  B01J2219/00094 ,  B01J2219/00108 ,  B01J2219/00155 ,  B01J2219/00159 ,  B01J2219/00177 ,  C02F1/302 ,  C02F1/32 ,  C02F1/36 ,  C02F1/722 ,  C02F1/725

Abstract: Zum Abbau von Schadstoffen in Abwässern, Prozeßlösungen und Trinkwasser unter Verwendung von Persulfat wird der Abbau bei mindestens 130 °C, vorzugweise 130 bis 140 °C und einem Druck größer als 1 bar durchgeführt. Zur Durchführung des Verfahrens eignet sich eine Einrichtung mit einem ersten Behälterteil zur Aufnahme der wässrigen Lösung, welcher einen Einlauf und einen Auslauf aufweist und einen Reaktionsraum bildet, wobei eine Heizvorrichtung zum Beheizen der wässrigen Lösung vorgesehen ist, wobei weiter Wärmeübergangsmittel vorgesehen sind, die einen Wärmeübergang zwischen der Heizvorrichtung und der wässrigen Lösung gestatten, und wobei wenigstens ein Druckerzeugungsmittel vorgesehen ist.

Abstract translation: 使用过硫酸盐除去流出物，工艺溶液或饮用水中的有害物质的方法包括在至少130（130-140）℃的温度和大于1巴的压力下进行消除步骤。用于该方法的装置 也声称。

公开(公告)号：EP0783921A2

公开(公告)日：1997-07-16

申请号：EP97100283.7

申请日：1997-01-09

Applicant: Yamasaki, Nakamichi ,  YKK CORPORATION

Inventor： Yamasaki, Nakamichi ,  Mochida, Tsuneaki ,  Maeda, Akihiro ,  Fukuda, Takeshi ,  Morimura, Tsuyoshi

IPC: B01J3/00

CPC classification number: B01J3/008 ,  B01F3/022 ,  B01F2013/1091 ,  B01J3/00 ,  B01J8/20 ,  B01J2208/00398 ,  B01J2208/00415 ,  B01J2208/0053 ,  B01J2219/00006

Abstract: A continuous hydrothermal synthesis method which comprises pressurizing and heating a material slurry below a saturated vapor temperature or pressurizing a material slurry at normal temperature, pressurizing and heating an aqueous liquid above the saturated vapor temperature, atomizing and mixing the slurry and the aqueous liquid, effecting hydrothermal synthesis in a reaction section above the saturated vapor temperature, cooling the reaction product and taking out the product while retaining the pressurized state in the system by alternately opening and closing shut-off valves provided above and below a product discharging section or through a thin pipe provided in the product discharging section. The method is performed using an apparatus comprising heating-pressurizing sections respectively connected to a material slurry feeding section and an aqueous liquid feeding section, an atomizing-mixing section and a reaction section provided after these feeding sections, and a product discharging section.

Abstract translation: 一种连续的水热合成方法，其包括在饱和蒸汽温度以下加压和加热材料浆料或在常温下加压材料浆料，将饱和蒸汽温度以上的水性液体加压和加热，使浆料和水性液体雾化和混合， 在高于饱和蒸汽温度的反应段中进行水热合成，冷却反应产物并取出产品，同时通过交替地打开和关闭设置在产品排放部分上方和下方的截止阀，或通过薄的 产品放置部分设有管。 该方法使用包括分别连接到材料浆料供给部分和水性液体供给部分的加热加压部分，设置在这些进料部分之后的雾化混合部分和反应部分的装置以及产物排出部分进行。

公开(公告)号：EP0733401A2

公开(公告)日：1996-09-25

申请号：EP96104305.6

申请日：1996-03-19

Applicant: BASF AKTIENGESELLSCHAFT

Inventor： Bittins, Klaus, Dr. ,  Heider, Marc, Dr. ,  Schmidt-Radde, Martin, Dr. ,  Kellenbenz, Jochen, Dr. ,  Wagner, Kurt Josef ,  Zehner, Peter, Dr. ,  Berg, Stefan, Dr.

IPC: B01J10/00 ,  B01J3/00

CPC classification number: C07D233/54 ,  B01J3/00 ,  B01J10/002 ,  B01J2219/00162 ,  C07C29/36 ,  C07C29/44 ,  C07C41/08 ,  C07C51/235 ,  C07C2601/14 ,  Y10S585/951 ,  C07C53/122 ,  C07C43/16 ,  C07C43/188 ,  C07C43/178 ,  C07C43/1785 ,  C07C43/162 ,  C07C43/1781 ,  C07C31/12 ,  C07C35/08 ,  C07C31/202 ,  C07C31/207 ,  C07C31/276

Abstract: Verfahren zur Durchführung von Gas/Flüssigreaktionen bei Temperaturen von (-50) bis 300°C und einem Druck von 0,1 bis 100 bar, indem man in Abwesenheit einer zusammenhängenden Gasphase arbeitet, sowie als Spezialfall ein Verfahren zur diskontinuierlichen Umsetzung von Acetylen in flüssiger Phase bei Temperaturen von 0 bis 300°C und Drücken von 2 bis 30 bar, in dem man in Abwesenheit einer a) zusammenhängenden Gasphase Acetylen und b) isobar bis zu einem Sättigungsgrad von 5 bis 100% einleitet.

Abstract translation: 一种用于在从（-50）至300℃，0.1〜100巴的压力下的温度下进行气/液反应过程中，通过在不存在连续气相的工作，和作为用于在液体中乙炔的不连续反应的方法的一种特殊情况 在0的温度至300℃和2至30巴，其中一个）的压力相以引发在不存在的）气相乙炔和b等压线得到5〜100％的饱和度连续。

公开(公告)号：WO2017048705A2

公开(公告)日：2017-03-23

申请号：PCT/US2016/051501

申请日：2016-09-13

Applicant: CHEVRON PHILLIPS CHEMICAL COMPANY LP

Inventor： KREISCHER, Bruce

IPC: C07C2/08 ,  C07C2/22 ,  C07C2/32

CPC classification number: C07C2/22 ,  B01J3/00 ,  C07C2/32 ,  C07C11/08 ,  C07C11/107 ,  C07C11/02

Abstract: A process includes periodically or continuously introducing an olefin monomer and periodically or continuously introducing a catalyst system or catalyst system components into a reaction mixture within a reaction system, oligomerizing the olefin monomer within the reaction mixture to form an oligomer product, and periodically or continuously discharging a reaction system effluent comprising the oligomer product from the reaction system. The reaction system includes a total reaction mixture volume and a heat exchanged portion of the reaction system comprising a heat exchanged reaction mixture volume and a total heat exchanged surface area providing indirect contact between the reaction mixture and a heat exchange medium. A ratio of the total heat exchanged surface area to the total reaction mixture volume within the reaction system is in a range from 0.75 in -1 to 5 in -1 , and an oligomer product discharge rate from the reaction system is between 1.0 (lb)(hr -1 )(gal -1 ) to 6.0 (lb)(hr -1 )(gal -1 ).

Abstract translation: 一种方法包括定期或连续地引入烯烃单体并且周期性或连续地将催化剂体系或催化剂体系组分引入反应体系内的反应混合物中，使反应混合物内的烯烃单体低聚以形成低聚物产物，并周期性或连续地排出 包含来自反应体系的低聚物产物的反应体系流出物。 反应体系包括总反应混合物体积和反应体系的热交换部分，其包含热交换反应混合物体积和提供反应混合物与热交换介质之间的间接接触的总热交换表面积。 反应体系中总热交换表面积与总反应混合物体积之比在0.75-1-1 5 in-1的范围内，来自反应体系的低聚物产物排出速率为1.0（lb） （hr-1）（gal-1）至6.0（lb）（hr-1）（gal-1）。