公开(公告)号：US20110020187A1

公开(公告)日：2011-01-27

申请号：US12921305

申请日：2008-03-06

Applicant: Jiro Hiraiwa ,  Hitoshi Takebayashi ,  Osamu Yoshimoto ,  Noriyuki Tanaka ,  Ichiro Fujita ,  Hiroyoshi Sasaki ,  Kazutaka Mori

Inventor： Jiro Hiraiwa ,  Hitoshi Takebayashi ,  Osamu Yoshimoto ,  Noriyuki Tanaka ,  Ichiro Fujita ,  Hiroyoshi Sasaki ,  Kazutaka Mori

IPC: B01D53/34 ,  B01J19/00

CPC classification number: H01L21/6719 ,  B01J4/008 ,  H01L21/67017 ,  H01L21/67109

Abstract: A surface treatment apparatus 100 includes a diluent gas supplier 1, a fluorine gas supplier 2, a mixer 5 which mixes a diluent gas with a fluorine gas, and a reactor 6 which treats a treatment target by using a mixed gas generated by the mixer 5. A diluent gas supplied from a diluent gas supplier is heated by a heater 8, and the heated diluent gas is mixed with a fluorine gas supplied from a fluorine gas supplier, in the mixer 5. The mixed gas is supplied to the reactor 6. The gas in the reactor 6 is supplied from the reactor 6 to flow paths 219, 220, 221, and 222 by an exhauster 207. The valves 223, 224, 225, and 226 are serially opened, so that the gas in the reactor 6 is supplied to a harm removal apparatus 208 while the gas flow rate is being adjusted by the flow paths 219, 220, 221, and 222.

Abstract translation: 表面处理装置100包括稀释气体供给体1，氟气供给体2，将稀释气体与氟气混合的混合器5以及通过使用由混合器5产生的混合气体来处理处理对象物的反应器6 从稀释气体供给装置供给的稀释气体由加热器8加热，加热后的稀释气体与从氟气供给体供给的氟气混合在混合器5中。混合气体供给反应器6。 反应器6中的气体通过排气器207从反应器6供应到流动路径219,220,221和222.阀223,224,225和226串联打开，使得反应器6中的气体 在通过流路219,220,221和222调节气体流量的同时，供给到危害消除装置208。

公开(公告)号：US20100243082A1

公开(公告)日：2010-09-30

申请号：US11980743

申请日：2007-10-31

Applicant: Wuu-Jyh Lin ,  Mao-Hsung Chang ,  Kuo-Yuan Chu ,  Dow-chi Chen ,  Ping-Yen Huang ,  Jenn-Tzong Chen ,  Ting-shien Duh

Inventor： Wuu-Jyh Lin ,  Mao-Hsung Chang ,  Kuo-Yuan Chu ,  Dow-chi Chen ,  Ping-Yen Huang ,  Jenn-Tzong Chen ,  Ting-shien Duh

IPC: F16K15/00

CPC classification number: B01J4/008 ,  Y10T137/7838

Abstract: A liquid isotope delivery system includes a pressure-controlling unit, an input unit, a target chamber, a proton-radiating unit and a storage unit. The pressure-controlling unit includes a first regulating valve, a second regulating valve connected to the first regulating valve and a third regulating valve connected to the first regulating valve. The input unit is connected to the second regulating valve. The target chamber is connected to the third regulating valve and the input unit. The proton-radiating unit is located near the target chamber. The storage unit is connected to the target chamber.

Abstract translation: 液体同位素输送系统包括压力控制单元，输入单元，目标室，质子辐射单元和存储单元。 压力控制单元包括第一调节阀，连接到第一调节阀的第二调节阀和连接到第一调节阀的第三调节阀。 输入单元连接到第二调节阀。 目标腔室连接到第三调节阀和输入单元。 质子辐射单元位于目标室附近。 存储单元连接到目标室。

公开(公告)号：US20100063206A1

公开(公告)日：2010-03-11

申请号：US12282290

申请日：2007-03-13

Applicant: Rolf Van Bonn ,  Joachim Barbe

Inventor： Rolf Van Bonn ,  Joachim Barbe

IPC: C08F289/00 ,  B01J19/00

CPC classification number: B01J4/008 ,  B01J4/002 ,  B01J19/26 ,  B01J2219/00135 ,  B01J2219/00162 ,  B01J2219/00164 ,  B01J2219/00166 ,  B01J2219/00186 ,  C08J7/126

Abstract: The gas-phase fluorination of plastic articles is effected in a reaction chamber 1 into which the plastic articles to be fluorinated are introduced. The gas-phase fluorination is effected at normal or atmospheric ambient pressure of about 1 kPa in the reaction chamber. The gas-phase fluorination can be carried out statically or dynamically. The flushing carried out before the gas-phase fluorination for complete or partial removal of atmospheric oxygen from the reaction chamber 1 can also be effected at atmospheric pressure in the reaction chamber. The reaction chamber 1 is equipped with a cover 2 and metering valves V0, V1, V2 for air, inert gas and gas mixture comprising fluorine and one or more inert gases are present on the entrance side of the reaction chamber, which is not vacuum-tight and hence also cannot be evacuated. The metering valves are connected to the reaction chamber 1 via a flow meter 4. A release valve V3 and a flow-through/shut-off valve V4 are arranged in an exhaust gas line 8 of the reaction chamber 1.

Abstract translation: 塑料制品的气相氟化在其中引入待氟化的塑料制品的反应室1中进行。 气相氟化在反应室中在约1kPa的正常或大气环境压力下进行。 气相氟化可以静态或动态地进行。 在气相氟化之前进行的冲洗完全或部分地从反应室1中除去大气中的氧也可以在大气压下在反应室中进行。 反应室1配备有盖2，空气的计量阀V0，V1，V2，包含氟和一种或多种惰性气体的惰性气体和气体混合物存在于反应室的入口侧， 因此也不能疏散。 计量阀经由流量计4连接到反应室1.释放阀V3和流通/截止阀V4布置在反应室1的废气管线8中。

公开(公告)号：US20100037963A1

公开(公告)日：2010-02-18

申请号：US12593996

申请日：2008-09-22

Applicant: Shu Yamamoto

Inventor： Shu Yamamoto

IPC: B01J4/00 ,  B67D7/78 ,  G01F23/00

CPC classification number: G01F23/00 ,  B01J4/008 ,  Y10T137/0324 ,  Y10T137/7303

Abstract: A process-liquid supply part includes: a supply tank configured to contain a process liquid; a level gauge pipe connected to the supply tank, the level gauge pipe being provided with level sensors for detecting a remaining amount of the process liquid contained in the supply tank; and a measuring part configured to measure a remaining amount of the process liquid based on signals from the level sensors provided on the level gauge pipe. Connected to the supply tank are a process-liquid supply pipe configured to drain the process liquid contained in the supply tank, and a process-liquid return pipe configured to introduce the process liquid drained through the process-liquid supply pipe to the supply tank. A connection pipe, in which an openable and closable valve is provided, disposed between the process-liquid supply pipe or the process-liquid return pipe and the level gauge pipe.

Abstract translation: 处理液供给部包括：供给槽，其配置成容纳处理液; 液位计管连接到供应罐，液位计管设有液位传感器，用于检测包含在供应罐中的处理液的剩余量; 以及测量部，其被配置为基于来自设置在液位计管上的液位传感器的信号来测量处理液的剩余量。 与供给罐连接的是处理液供给管，其配置为排出供给槽中所含有的处理液，以及处理液返回管，其配置为将通过处理液供给管排出的处理液引入供给槽。 设置在处理液供给管或处理液返回管与液位计管之间的连接管，其中设置有可开闭阀。

公开(公告)号：US20090263257A1

公开(公告)日：2009-10-22

申请号：US12301589

申请日：2007-05-25

Applicant: Guillaume Rameau ,  Valere Laurent ,  Jean-Marc Girard

Inventor： Guillaume Rameau ,  Valere Laurent ,  Jean-Marc Girard

IPC: F04F9/00

CPC classification number: B01J4/008 ,  B01J4/001 ,  B01J4/002 ,  B01J19/26 ,  B01J2219/00094 ,  B01J2219/00119 ,  B01J2219/185 ,  B01J2219/1944 ,  C23C16/4402 ,  C23C16/4482 ,  F28D2021/0022 ,  F28D2021/0033

Abstract: The present invention relates to a method for distributing products, in particular pyrophoric, from a storage point to a use point.According to the invention, an inert gas is bubbled through the product, in particular pyrophoric, to be purified in the liquid state in order to generate a mixture, the mixture is preferably routed close to the use point, the product, in particular pyrophoric, is separated from the inert gas and from some light impurities, to generate a purified final product, in particular pyrophoric, in liquid or solid form. The purified product is supplied in a quantity just necessary to the use point, particularly when it is solidified in the heat exchanger after the transport of the mixture.

Abstract translation: 本发明涉及一种从储存点到使用点分配产品，特别是发火的方法。 根据本发明，惰性气体鼓泡通过产品，特别是自燃的，以液态纯化，以便产生混合物，该混合物优选地靠近使用点，产物，特别是发火的， 与惰性气体和一些轻质杂质分离，以液体或固体形式产生纯化的最终产物，特别是发火的。 纯化产物以使用点所需的量提供，特别是在混合物输送之后在热交换器中固化时。

公开(公告)号：US20090183789A1

公开(公告)日：2009-07-23

申请号：US12280624

申请日：2007-02-21

Applicant: Andre Lewalle ,  Denis Mignon ,  Sandra Davidts

Inventor： Andre Lewalle ,  Denis Mignon ,  Sandra Davidts

IPC: F16L41/00

CPC classification number: B01J8/0015 ,  B01J4/008 ,  B01J19/2435 ,  B01J2219/0004 ,  B01J2219/00166 ,  B01J2219/00184 ,  B01J2219/00254 ,  C08F110/02 ,  C08F210/16 ,  F16L41/023 ,  F16L41/03 ,  F16L47/32 ,  Y10S526/918 ,  Y10S526/92 ,  Y10T137/85938 ,  C08F210/06

Abstract: The present system discloses a transfer system devised in order to produce optimal flow from the first to the second loop reactor, by connecting the transfer lines to a by-pass line and by separating the connecting points of the transfer lines into the by-pass line by at least 70 cm.

Abstract translation: 本系统公开了一种设计用于通过将传输线连接到旁路线并通过将传输线的连接点分离成旁路线而产生从第一到第二环路反应器的最佳流量的传输系统 至少70厘米。

公开(公告)号：US07470293B2

公开(公告)日：2008-12-30

申请号：US11096827

申请日：2005-03-31

Applicant: David J. Edlund ,  R. Todd Studebaker

Inventor： David J. Edlund ,  R. Todd Studebaker

IPC: B01J7/00 ,  B65B1/04 ,  F17D1/04 ,  G05D16/00

CPC classification number: B01J4/001 ,  B01J3/03 ,  B01J4/008 ,  C01B3/34 ,  C01B2203/0205 ,  C01B2203/0405 ,  C01B2203/042 ,  C01B2203/12 ,  H01M8/0612

Abstract: Feedstock delivery systems for hydrogen generation assemblies having a hydrogen-producing region and a heating assembly. The delivery system provides a hydrogen-production fluid to the hydrogen-producing region and provides a heating fuel to the heating assembly. The delivery system includes a pressure vessel having an interior cavity containing the heating fuel and the hydrogen-production fluid, which are disposed in the pressure vessel in a pressurizing—pressurized relationship, in which the heating fuel is discharged from the pressure vessel under it own pressure and the hydrogen-production fluid is discharged under pressure applied by the heating fuel. The feedstock delivery system may separately discharge the hydrogen-production fluid and the heating fuel and may include a pressure transmitter disposed between the hydrogen-production fluid and the heating fuel. The heating fuel may be a condensable fluid and the hydrogen-production fluid may be a liquid at the operating conditions of the feedstock delivery system.

Abstract translation: 用于具有产氢区和加热组件的氢产生组件的原料输送系统。 输送系统向产氢区域提供氢气生产流体并向加热组件提供加热燃料。 输送系统包括压力容器，该压力容器具有包含加热燃料和氢气产生流体的内部空腔，所述内部空腔以加压关系设置在压力容器中，其中加热燃料在其自身下面从压力容器排出 压力，并且在由加热燃料施加的压力下排出产氢流体。 原料输送系统可以单独排出产氢流体和加热燃料，并且可以包括设置在氢气产生流体和加热燃料之间的压力变送器。 加热燃料可以是可冷凝流体，并且在原料输送系统的操作条件下，氢气产生流体可以是液体。

公开(公告)号：US20070129512A1

公开(公告)日：2007-06-07

申请号：US10581689

申请日：2004-11-04

Applicant: Hans-Dieter Blitz ,  Norbert Suetterlin

Inventor： Hans-Dieter Blitz ,  Norbert Suetterlin

IPC: C08F2/00 ,  B01J19/18

CPC classification number: B01J19/1818 ,  B01J4/008 ,  B01J2219/00094 ,  B01J2219/00779 ,  C08F20/12

Abstract: The invention relates to a process for the continuous free-radical homogeneous solution polymerization or melt polymerization of (meth)acrylate monomer mixtures.

Abstract translation: 本发明涉及（甲基）丙烯酸酯单体混合物的连续自由基均相溶液聚合或熔融聚合的方法。

公开(公告)号：US20050008554A1

公开(公告)日：2005-01-13

申请号：US10794557

申请日：2004-03-05

Applicant: Marek Nowosielski-Slepowron ,  Brian Krafton

Inventor： Marek Nowosielski-Slepowron ,  Brian Krafton

IPC: A01K7/02 ,  B01F3/08 ,  B01F15/00 ,  B01F15/04 ,  B01J4/00 ,  C01B11/02 ,  C01B11/08 ,  C01B11/10 ,  C02F1/66 ,  C02F1/68 ,  C02F1/76 ,  C01G43/025

CPC classification number: C01B11/08 ,  A01K7/02 ,  B01F3/08 ,  B01F15/005 ,  B01F15/0416 ,  B01J4/008 ,  C01B11/024 ,  C01B11/026 ,  C01B11/10 ,  C02F1/66 ,  C02F1/685 ,  C02F1/76 ,  C02F2103/026 ,  C02F2209/40

Abstract: An apparatus that can be used for producing chlorine dioxide is provided. The apparatus comprises a single fluid proportioning device, which comprises three or more fluid transferring devices, a conduit to the inlet of each fluid transferring device, a conduit to the outlet of each fluid transferring device, a water inlet to the device, and a water outlet from the device in which the fluid transferring device is proportionally actuated by the flow of water through the device. Also provided is a process that can be used to produce chlorine dioxide. The process comprises flowing water through the fluid proportioning device to create a downstream water and to actuate the fluid transferring devices; drawing three or more precursor compounds each from a separate source and flowing each compound separately through one of the fluid transferring devices; and injecting the precursor compounds into the downstream water.

Abstract translation: 提供了可用于生产二氧化氯的装置。 该装置包括单个流体分配装置，其包括三个或更多个流体输送装置，每个流体输送装置的入口的导管，每个流体输送装置的出口的导管，该装置的进水口和水 来自装置的出口，其中流体输送装置由水流通过装置成比例地致动。 还提供了可用于生产二氧化氯的方法。 该过程包括使水流过流体分配装置以产生下游水并致动流体转移装置; 从分离的源中抽出三种或更多种前体化合物，并通过其中一种流体转移装置分别流动每种化合物; 并将前体化合物注入下游水中。

公开(公告)号：US20040192860A1

公开(公告)日：2004-09-30

申请号：US10849393

申请日：2004-05-19

Inventor： John D. Hottovy ,  Harvey D. Hensley ,  David J. Przelomski ,  Teddy H. Cymbaluk ,  Robert K. Franklin III ,  Ethelwoldo P. Perez

IPC: C08G085/00 ,  C08F002/00

CPC classification number: B01J8/007 ,  B01J4/008 ,  B01J8/0055 ,  B01J19/1837 ,  B01J2219/00006 ,  C08F6/003 ,  C08F10/00 ,  C08F10/02 ,  C08F210/16 ,  C08F2/14 ,  C08F210/14

Abstract: An olefin polymerization process wherein monomer, diluent and catalyst are circulated in a continuous loop reactor and product slurry is recovered by means of a continuous product take off. The continuous product allows operating the reaction at significantly higher solids content in the circulating slurry. In a preferred embodiment, the slurry is heated in a flash line heater and passed to a high pressure flash where a majority of the diluent is separated and thereafter condensed by simple heat exchange, without compression, and thereafter recycled. Also an olefin polymerization process operating at higher reactor solids by virtue of more aggressive circulation.

Abstract translation: 其中单体，稀释剂和催化剂在连续环管反应器中循环并通过连续产物脱除回收产物浆料的烯烃聚合方法。 连续产品允许在循环浆液中以显着更高的固体含量操作反应。 在优选的实施方案中，将浆料在闪光线加​​热器中加热并通过高压闪蒸，其中大部分稀释剂被分离，然后通过简单的热交换而不压缩，然后再循环。 还有一种通过更积极的循环在更高反应堆固体运行的烯烃聚合方法。