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    分解反応装置、再生樹脂組成物原料製造システム、再生樹脂組成物原料製造方法、再生樹脂組成物原料、および成形体
    162.
    发明申请
    分解反応装置、再生樹脂組成物原料製造システム、再生樹脂組成物原料製造方法、再生樹脂組成物原料、および成形体 审中-公开
    分解反应装置，用于生产用于回收树脂组合物的原料的系统，用于生产用于回收树脂组合物的原料的方法，用于回收树脂组合物的原料和形成的物品

    公开(公告)号：WO2006051663A1

    公开(公告)日：2006-05-18

    申请号：PCT/JP2005/018643

    申请日：2005-10-07

    Applicant: 住友ベークライト株式会社 ,  後藤 純也 ,  三宅 澄也 ,  石川 真毅 ,  下谷地 一徳

    Inventor： 後藤 純也 ,  三宅 澄也 ,  石川 真毅 ,  下谷地 一徳

    IPC: C08J11/18

    CPC classification number: C08J11/18 ,  B01J3/00 ,  B01J3/008 ,  B01J4/008 ,  B01J19/20 ,  B01J19/243 ,  B01J2219/00033 ,  B01J2219/0009 ,  B01J2219/00135 ,  B01J2219/00162 ,  B01J2219/00164 ,  B01J2219/00166 ,  B01J2219/00168 ,  B01J2219/00184 ,  B01J2219/00252 ,  B01J2219/185 ,  B01J2219/1944 ,  Y02P20/544 ,  Y02P20/582 ,  Y02W30/706

    Abstract: 　分解反応装置は、熱硬化性樹脂を分解処理する。この分解反応装置は、熱硬化性樹脂を含む樹脂組成物と、熱硬化性樹脂のモノマー成分またはこのモノマー成分に類する成分を含む溶媒とを導入する導入部と、樹脂組成物および溶媒を加熱・加圧して、溶媒を超臨界状態または亜臨界状態とすることにより、熱硬化性樹脂を低分子量化した再生樹脂を含有する処理回収物を得る分解反応部と、処理回収物を排出する排出部とを備える反応装置を有する。この反応装置は、導入部への樹脂組成物および溶媒の導入と、分解反応部での熱硬化性樹脂の分解処理と、排出部からの処理回収物の排出とは、いずれも連続的に行われるため、熱硬化性樹脂を含む産業廃棄物や一般廃棄物などを樹脂組成物とし再生樹脂組成物原料を連続的に製造することができる。

    Abstract translation: 一种用于热塑性树脂分解处理的分解反应装置，其包括反应装置，该反应装置包括用于引入含有热塑性树脂的树脂组合物的引入部分和含有热塑性树脂的单体组分的溶剂或类似于单体组分的组分 ，用于对树脂组合物和上述溶剂进行加压和加压以使溶剂具有超临界状态或亚临界状态的分解反应部分，从而制备含有通过还原分子形成的再循环树脂的处理和回收产物 上述热塑性树脂的重量，以及用于排出处理和回收的产品的排出部分。 在上述反应装置中，引入树脂组合物和溶剂，分解反应部分中的热塑性树脂的分解处理和从排出部排出的处理和回收的产物全部连续进行，因此， 可以连续地制造使用含有热塑性树脂的工业或一般废物作为上述树脂组合物的回收树脂组合物的原料。

    ENHANCED ADSORBENT AND ROOM TEMPERATURE CATALYST PARTICLE AND METHOD OF MAKING AND USING THEREFOR
    166.
    发明申请
    ENHANCED ADSORBENT AND ROOM TEMPERATURE CATALYST PARTICLE AND METHOD OF MAKING AND USING THEREFOR 审中-公开
    增强吸附和室温催化剂颗粒及其制备和使用方法

    公开(公告)号：WO9633013A3

    公开(公告)日：1996-12-05

    申请号：PCT/US9605303

    申请日：1996-04-17

    Applicant: M & K PATENT CO INC ,  MOSKOVITZ MARK L ,  KEPNER BRYAN E

    Inventor： MOSKOVITZ MARK L ,  KEPNER BRYAN E

    IPC: A61L9/00 ,  B01D53/02 ,  B01D53/86 ,  B01D53/94 ,  B01J3/00 ,  B01J3/02 ,  B01J19/08 ,  B01J19/24 ,  B01J20/30 ,  B01J20/34 ,  B01J21/04 ,  B01J23/34 ,  B01J37/34 ,  C01B31/08 ,  C02F1/28

    CPC classification number: B01J20/3441 ,  B01D53/02 ,  B01J3/00 ,  B01J3/02 ,  B01J19/085 ,  B01J19/24 ,  B01J37/34 ,  B01J37/344 ,  B01J37/347 ,  B01J2219/00112 ,  B01J2219/00162 ,  B01J2219/00177 ,  C01B32/366

    Abstract: A method for producing an enhanced adsorbent and/or enhanced catalytic particle and/or for producing a catalytic particle, comprising the steps of: (a) removing an effective amount of air from a closed chamber containing an adsorbent and/or catalytic particle, wherein the resultant chamber pressure is less than one atmosphere; (b) raising the chamber pressure with an inert gas to at least one atmosphere; (c) contacting the particle with an energy beam of sufficient energy for a sufficient time to thereby enhance the adsorbent and/or catalytic properties of the particle and/or produce catalytic properties in the particle. A continuous process directed to step (c) alone is also provided. Also disclosed are adsorbent and/or catalytic particles, methods of contaminant reduction or elimination, including room temperature catalysis, particle binders, apparatuses of the present invention, and methods of increasing the surface area of adsorbent and/or catalytic particles.

    Abstract translation: 一种用于生产增强的吸附剂和/或增强的催化颗粒和/或用于生产催化剂颗粒的方法，包括以下步骤：（a）从含有吸附剂和/或催化颗粒的封闭室除去有效量的空气，其中 所产生的室压力小于一个大气压; （b）将惰性气体的室压力升至至少一个大气压; （c）使颗粒与足够能量的能量束接触足够的时间，从而增强颗粒的吸附剂和/或催化性质和/或在颗粒中产生催化性能。 还提供了仅针对步骤（c）的连续方法。 还公开了吸附剂和/或催化颗粒，减少或消除污染物的方法，包括室温催化，颗粒粘合剂，本发明的装置以及增加吸附剂和/或催化颗粒的表面积的方法。

    Decomposition Reaction Apparatus, System for Producing Raw Material for Recycled Resin Composition, Method for Producing Raw Material for Recycled Resin Composition, Raw Material for Recycled Resin Composition, and Formed Article
    168.
    发明公开
    Decomposition Reaction Apparatus, System for Producing Raw Material for Recycled Resin Composition, Method for Producing Raw Material for Recycled Resin Composition, Raw Material for Recycled Resin Composition, and Formed Article 有权
    用于制造的原料再循环树脂组合物的分解反应装置的系统，用于制备起始原料为再生树脂组合物原料的再生树脂组合物和模制品

    公开(公告)号：EP2894192A3

    公开(公告)日：2015-08-12

    申请号：EP15155799.8

    申请日：2005-10-07

    Applicant: Sumitomo Bakelite Company Limited

    Inventor： Goto, Junya ,  Miyake, Sumiya ,  Ishikawa, Masaki ,  Shimoyachi, Kazunori

    IPC: C08J11/18 ,  B01J3/00 ,  B01J19/20 ,  B01J19/24 ,  C08J11/10 ,  B01J4/00

    CPC classification number: C08J11/18 ,  B01J3/00 ,  B01J3/008 ,  B01J4/008 ,  B01J19/20 ,  B01J19/243 ,  B01J2219/00033 ,  B01J2219/0009 ,  B01J2219/00135 ,  B01J2219/00162 ,  B01J2219/00164 ,  B01J2219/00166 ,  B01J2219/00168 ,  B01J2219/00184 ,  B01J2219/00252 ,  B01J2219/185 ,  B01J2219/1944 ,  Y02P20/544 ,  Y02P20/582 ,  Y02W30/706

    Abstract: A system (1) for producing a raw material for a recycled resin composition, comprising:
    - a decomposition reaction apparatus (2) for decomposing a thermosetting resin, comprising:
    an introduction section (222) for introducing a resin composition containing the thermosetting resin and a solvent containing a monomer component of the thermosetting resin or a derivative of the monomer component;
    a decomposition reaction section (221) for obtaining a first treated recovery product containing a recycled resin formed of the thermosetting resin having a reduced molecular weight, a solid residue and a low-boiling-point component containing the solvent, by heating and pressurizing the resin composition and the solvent and bringing the solvent into a supercritical state or a subcritical state, and the decomposition reaction section (221) being comprised of a tube-type reactor (22) which is adapted to perform the decomposition treatment with the resin composition and the solvent,
    and
    a discharge section (223) for discharging the first treated recovery product,
    wherein the decomposition reaction apparatus (2) is adapted to continuously perform the introduction of the resin composition and the solvent into the introduction section (222), the decomposition treatment of the thermosetting resin in the decomposition reaction section (221) and the discharge of the first treated recovery product from the discharge section (223),
    a first separating unit (51) serving as a solid-liquid separator, wherein the first separating unit (51) is designed for separating and removing the solid residue from the first treated recovery product,
    a second separating unit (52) serving as a gas-liquid separator, wherein the second separating unit (52) is designed for separating and extracting the recycled resin with the reduced molecular weight as well as the low-boiling-point component containing the solvent from the first treated recovery product from which the solid residue has been removed,
    wherein the first separating unit (51) and the second separating unit (52) are connected to the discharge section (223) of the decomposition reaction apparatus (2) in the named sequence.

    Abstract translation: 用于热固性树脂的分解处理，其包括反应装置，包括一个导入部导入含有热固性树脂和含有热固性树脂的或单体成分的成分类似单体成分的溶剂中的树脂组合物A的分解反应装置 用于加热和加压的树脂组合物和上述溶剂，从而为溶剂，具有超临界状态或亚临界状态，从而制备治疗和回收的产物含有由分子的还原形成的再生树脂的分解反应部 重量的上述热固性树脂，以及用于排出处理过的和回收的产物的排出部。 在上述反应装置中，在引入树脂组合物和溶剂的，在分解反应部的热固性树脂的分解处理和经处理的排放和回收的产物从排出部都连续进行，因此， 使用在工业或一般废弃物含有热固性树脂作为上述树脂组合物的原料的再生树脂组合物可以连续地制造。

    PRESSURE CYCLING SYSTEMS AND RELATED METHOD
    170.
    发明公开
    PRESSURE CYCLING SYSTEMS AND RELATED METHOD 审中-公开
    压力循环系统及相关方法

    公开(公告)号：EP2129456A2

    公开(公告)日：2009-12-09

    申请号：EP08728313.1

    申请日：2008-01-25

    Applicant: Pressure Biosciences Inc.

    Inventor： TING, Edmund, Y.

    IPC: B01J3/00 ,  B01J3/03 ,  C12M1/00

    CPC classification number: B01J3/00 ,  B01J3/03 ,  B01J2219/00065 ,  B01J2219/00162 ,  B01J2219/002 ,  B01J2219/00213 ,  B01J2219/00231

    Abstract: A pressure cycling system includes a reaction chamber configured to receive a sample and a charge pump in fluid communication with the reaction chamber. The charge pump is operable to convey a fluid from a fluid source toward the reaction chamber. The system also includes a check valve disposed between the charge pump and the reaction chamber. The check valve is operable to inhibit the flow of fluid from the reaction chamber toward the charge pump. A pressure intensifier is in fluid communication with the reaction chamber. The pressure intensifier is pneumatically operable to adjust a pressure in the reaction chamber. A controller is configured to control operation of the charge pump and the pressure intensifier. The controller is configured to pressurize the reaction chamber to a first pressure through operation of the charge pump. The controller is also configured to fluctuate the pressure in the reaction chamber between a second pressure and a third pressure through operation of the pressure intensifier.

    Abstract translation: 压力循环系统包括构造成接收样本的反应室和与反应室流体连通的电荷泵。 电荷泵可操作以将流体从流体源传送到反应室。 该系统还包括设置在电荷泵和反应室之间的止回阀。 止回阀可操作以阻止流体从反应室流向电荷泵。 增压器与反应室流体连通。 增压器可气动地操作以调节反应室中的压力。 控制器被配置为控制电荷泵和增压器的操作。 控制器构造成通过操作电荷泵将反应室加压至第一压力。 控制器还被配置为通过增压器的操作使反应室中的压力在第二压力和第三压力之间波动。

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