公开(公告)号：WO2003064833A1

公开(公告)日：2003-08-07

申请号：PCT/US2002/040434

申请日：2002-12-18

Applicant: ARVIN TECHNOLOGIES, INC.

Inventor： DANIEL, Michael, J. ,  SMALING, Rudolph, M. ,  TYLER, Kurt, S. ,  BAUER, Shawn, D.

IPC: F02B43/10

CPC classification number: F01N3/2066 ,  B01D53/9431 ,  B01D53/9495 ,  B01J19/088 ,  B01J2219/00063 ,  B01J2219/0883 ,  B01J2219/0884 ,  B01J2219/0892 ,  B01J2219/0894 ,  C01B3/342 ,  C01B2203/0205 ,  C01B2203/0861 ,  F01N3/0253 ,  F01N3/032 ,  F01N3/035 ,  F01N3/0821 ,  F01N3/0842 ,  F01N3/0871 ,  F01N3/0878 ,  F01N3/0892 ,  F01N13/009 ,  F01N13/0097 ,  F01N13/011 ,  F01N2240/28 ,  F01N2240/30 ,  F01N2610/03 ,  F02B43/10 ,  F02M21/0206 ,  F02M21/0227 ,  F02M21/06 ,  F02M25/12 ,  F02M27/02 ,  F02M27/042 ,  H01M8/04014 ,  H01M8/0618 ,  H01M8/0668 ,  H01M2250/20 ,  Y02A50/2325 ,  Y02T10/121 ,  Y02T10/24 ,  Y02T10/32 ,  Y02T90/32

Abstract: A power system has a fuel reformer, an emission abatement device, and a fuel cell. The fuel reformer reforms hydrocarbons fuels so as to produce a reformate gas which is supplied to both the emission abatement device and the fuel cell. A method of operating a fuel reformer so as to generate and supply a reformate gas to both an emission abatement device and a fuel cell is also disclosed.

Abstract translation: 电力系统具有燃料重整器，排放减排装置和燃料电池。 燃料重整器改性碳氢化合物燃料，以生产供应给排放减排装置和燃料电池两者的重整气体。 还公开了一种操作燃料重整器以便向排放减排装置和燃料电池两者产生并提供重整气体的方法。

公开(公告)号：WO2003044607A1

公开(公告)日：2003-05-30

申请号：PCT/US2002/026406

申请日：2002-08-20

Applicant: BASF CORPORATION ,  TAYLOR, Michael ,  ANTONUCCI, Jonathan ,  RACZ, Robert

Inventor： TAYLOR, Michael ,  ANTONUCCI, Jonathan ,  RACZ, Robert

IPC: G05B17/02

CPC classification number: C08F2/22 ,  B01J19/0006 ,  B01J19/24 ,  B01J19/2445 ,  B01J2219/00006 ,  B01J2219/00063 ,  B01J2219/00069 ,  B01J2219/00081 ,  B01J2219/00164 ,  B01J2219/00198 ,  B01J2219/00213 ,  B01J2219/00231 ,  C08F2400/02 ,  G01N33/442 ,  G05B13/048 ,  G05B17/02

Abstract: The present invention is a method for predicting polymer latex properties for an emulsion polymer latex based on statistical relationships between the polymer latex properties and process parameters for the emulsion polymerization process. The method for predicting one or more polymer latex properties for an emulsion polymer latex according to the invention includes conducting an emulsion polymerization process in a reactor including one or more reactor inputs to produce an emulsion polymer latex, measuring a set of process parameters for the emulsion polymerization process, performing a heat balance and a mass balance across the reactor based on the set of measured process parameters to determine a set of calculated polymer latex properties for the emulsion polymerization process, and determining one or more predicted polymer latex properties for the emulsion polymer being prepared in the emulsion polymerization process using the measured process parameters, the calculated polymer latex properties, and a set of predetermined statistical relationships between the process parameters and the polymer latex properties to be predicted. The present inventionalso includes an apparatus and a computer program product for predicting the polymer latex properties of an emulsion polymer latex.

Abstract translation: 本发明是基于聚合物胶乳性质和乳液聚合方法的工艺参数之间的统计关系来预测乳液聚合物胶乳的聚合物胶乳性质的方法。 用于预测根据本发明的乳液聚合物胶乳的一种或多种聚合物胶乳性质的方法包括在包括一个或多个反应器输入的反应器中进行乳液聚合方法以产生乳液聚合物胶乳，测量乳液的一组工艺参数 聚合过程，基于所述一组测量的工艺参数在整个反应器中进行热平衡和质量平衡以确定用于乳液聚合方法的一组计算的聚合物胶乳性质，以及确定乳液聚合物的一种或多种预测的聚合物胶乳性质 在乳液聚合方法中使用测量的工艺参数，计算的聚合物胶乳性质以及工艺参数和要预测的聚合物胶乳性质之间的一组预定的统计关系来制备。 本发明还包括用于预测乳液聚合物胶乳的聚合物胶乳性质的装置和计算机程序产品。

公开(公告)号：WO02062104A3

公开(公告)日：2003-02-06

申请号：PCT/US0202072

申请日：2002-01-24

Applicant: CEM CORP ,  JENNINGS WILLIAM EDWARD

Inventor： JENNINGS WILLIAM EDWARD

IPC: H05B6/68 ,  B01J19/12 ,  H01P7/06 ,  H05B6/64 ,  H05B6/70 ,  H05B6/80 ,  H05B6/74

CPC classification number: H05B6/806 ,  B01J19/126 ,  B01J2219/00058 ,  B01J2219/00063 ,  B01J2219/00065 ,  B01J2219/00094 ,  B01J2219/002 ,  B01J2219/0024 ,  B01J2219/1209 ,  B01J2219/1233 ,  B01J2219/1269 ,  B01J2219/1275 ,  H01P7/06

Abstract: An instrument is disclosed fro microwave-assisted chemical processes that avoids tuning discrepancies that otherwise result based upon the materials being heated. The instrument includes a source of microwave radiation, a waveguide in communication with the source, with at least a portion of the waveguide forming a cylindrical arc, a cylindrical cavity inmediately surrounded by the cylindrical arc portions of the waveguide, and at least three slotted openings in the circumference of the circular waveguide that provide microwave communication between the waveguide and the cavity.

Abstract translation: 通过微波辅助化学过程公开了一种仪器，避免了因加热材料而导致的调谐差异。 仪器包括微波辐射源，与源极连通的波导，波导的至少一部分形成圆柱形圆弧，立即被波导的圆柱形圆弧部分包围的圆柱形空腔，以及至少三个开槽开口 在波导和腔之间提供微波连通的圆形波导的周边。

公开(公告)号：WO2002068374A1

公开(公告)日：2002-09-06

申请号：PCT/JP2002/001333

申请日：2002-02-15

Applicant: ダイセル化学工業株式会社 ,  中島 英彦 ,  原野 嘉行

Inventor： 中島 英彦 ,  原野 嘉行

IPC: C07C51/44

CPC classification number: C07B39/00 ,  B01J19/0013 ,  B01J2219/00006 ,  B01J2219/00063 ,  B01J2219/00065 ,  B01J2219/00067 ,  B01J2219/00069 ,  B01J2219/00164 ,  B01J2219/00182 ,  B01J2219/00202 ,  B01J2219/00204 ,  B01J2219/00213 ,  B01J2219/0022 ,  B01J2219/00231 ,  B01J2219/00238 ,  C07C51/12 ,  C07C51/44 ,  Y02P20/582 ,  C07C53/08

Abstract: Methanol and carbon monoxide are fed to a liquid reaction system (3) containing a carbonylation catalyst system through feeding lines (17) and (19), respectively, a part of the reaction mixture containing the resulting acetic acid is withdrawn from the reaction system and is fed to a flash distillation column (4) while maintaining the liquid surface of the reaction system at a constant level, and a high boiling point fraction containing the carbonylation catalyst system is separated by the flash distillation and recycled to the reaction system (3) through a recycle line (21). In the recycle line (21), flow rate and temperature are measured by means of a flow sensor (F3) and a temperature sensor (T2), respectively. The temperature of the high boiling point fraction to be recycled is controlled by a temperature adjusting unit (6) utilizing a controlling unit (8) on the basis of the data measured above, so as to suppress the variation of the temperature and pressure of the above reaction system.

Abstract translation: 甲醇和一氧化碳分别通过进料管线（17）和（19）进料到含有羰基化催化剂体系的液体反应体系（3）中，从反应体系中取出一部分含有所得乙酸的反应混合物， 在将反应体系的液面维持在恒定水平的同时将其送入闪蒸塔（4），通过闪蒸将含有羰基化催化剂体系的高沸点馏分分离并再循环至反应体系（3） 通过再循环管线（21）。 在循环管线（21）中，通过流量传感器（F3）和温度传感器（T2）分别测量流量和温度。 基于上述数据，利用控制单元（8）的温度调节单元（6）控制待回收的高沸点馏分的温度，以便抑制温度和压力的变化 以上反应体系。

公开(公告)号：WO02026620A1

公开(公告)日：2002-04-04

申请号：PCT/JP2001/008345

申请日：2001-09-26

IPC: B01D53/86 ,  B01J8/04 ,  B01J19/24 ,  B01J23/63 ,  B01J37/02 ,  C01B3/48 ,  C01B3/32 ,  H01M8/06

CPC classification number: B01J19/2485 ,  B01D53/864 ,  B01J8/0496 ,  B01J23/63 ,  B01J37/0215 ,  B01J2208/00061 ,  B01J2208/00407 ,  B01J2208/00415 ,  B01J2208/00504 ,  B01J2208/00548 ,  B01J2219/00063 ,  B01J2219/00164 ,  B01J2219/002 ,  B01J2219/00213 ,  B01J2219/00236 ,  C01B3/48 ,  C01B2203/0233 ,  C01B2203/0283 ,  C01B2203/066 ,  C01B2203/0811 ,  C01B2203/085 ,  C01B2203/1023 ,  C01B2203/1041 ,  C01B2203/1064 ,  C01B2203/107 ,  C01B2203/1082 ,  C01B2203/1235 ,  C01B2203/1604 ,  C01B2203/1614 ,  C01B2203/1619 ,  C01B2203/1623 ,  C01B2203/1647 ,  C01B2203/1661 ,  C01B2203/169 ,  C01B2203/1695 ,  H01M8/0612 ,  H01M8/0662

Abstract: Since steam-reforming reaction is attended by formation of carbon monoxide as a by-product, a converter for causing water and carbon monoxide to shift-react is often used additionally. Generally, in stabilized operation, almost no increase in carbon monoxide concentration is observed. However, conditions for using a catalyst in the converter will vary owing to some external cause or other, presenting a problem that carbon monoxide concentration increases. In a device for feeding hydrogen gas from a gas feeder (1) to a converter, which comprises a reformer (1) including carbon monoxide and steam, and a converter (3) provided with a conversion catalyst (3a), the hydrogen gas outlet port of the converter is provided with a carbon monoxide concentration detecting means (6), so that when the detected value of carbon monoxide concentration in the carbon monoxide concentration detecting means (6) becomes larger than a preset value, the amount of steam in the gas feeder (1) is increased.

Abstract translation: 由于通过形成作为副产物的一氧化碳来进行蒸汽重整反应，因此经常使用用于使水和一氧化碳发生移位反应的转化器。 一般来说，在稳定运行中，一氧化碳浓度几乎没有增加。 然而，在转化器中使用催化剂的条件将由于一些外部原因或其它原因而变化，存在一氧化碳浓度增加的问题。 在用于将气体从气体供给器（1）供给到包括一氧化碳和蒸汽的重整器（1）的转化器的装置和具有转化催化剂（3a）的转化器（3）的装置中，氢气出口 转换器的端口设置有一氧化碳浓度检测装置（6），使得当一氧化碳浓度检测装置（6）中的一氧化碳浓度的检测值变得大于预设值时，蒸汽量 气体供给器（1）增加。

公开(公告)号：WO02001919A1

公开(公告)日：2002-01-03

申请号：PCT/US2001/018231

申请日：2001-06-04

IPC: G01N1/28 ,  B01F1/00 ,  B01J19/00 ,  B01L7/00 ,  G01N13/00 ,  G01N33/15 ,  H05B3/00 ,  H05B3/10 ,  H05B3/20 ,  H05B3/34 ,  H05B3/54 ,  H05B1/02 ,  H05B3/36 ,  H05B3/84

CPC classification number: G01N13/00 ,  B01F1/00 ,  B01F1/0011 ,  B01F2215/0037 ,  B01J19/0013 ,  B01J2219/00011 ,  B01J2219/00038 ,  B01J2219/00063 ,  B01J2219/00135 ,  B01J2219/002 ,  B01J2219/00213 ,  B01J2219/00238 ,  B01L7/00 ,  B01L2300/1805 ,  G01N33/15 ,  G01N2013/006 ,  H05B3/00 ,  H05B3/34 ,  H05B3/54 ,  H05B2203/005 ,  H05B2203/014 ,  H05B2203/017 ,  H05B2203/037

Abstract: A dissolution testing system comprises a vessel plate on which a plurality of vessels are mounted. Each vessel including a lateral wall having an outer surface around which a plurality of flexible heater elements are attached. Each heater element includes a transparent surface area, a heat conductive element extending along the transparent surface area, a temperature sensing element extending along the transparent surface area, and an electrical contact element connected to the heat conductive element and the temperature sensing element. The transparent heater element allows unobstructed view into the interior of its vessel, and reduces the time required to achieve a stabilized set point temperature in the vessel. A heater control system communicates with each heat conductive element and each temperature sensing element through a corresponding one of the electrical contact elements. The heater control system permits each vessel to be controlled independently of the other vessels.

Abstract translation: 溶解测试系统包括其上安装有多个容器的容器板。 每个容器包括具有附接有多个柔性加热器元件的外表面的侧壁。 每个加热器元件包括透明表面区域，沿着透明表面区域延伸的导热元件，沿着透明表面区域延伸的温度感测元件以及连接到导热元件和温度检测元件的电接触元件。 透明加热器元件允许在其容器的内部看不到障碍物，并且减少在容器中达到稳定的设定点温度所需的时间。 加热器控制系统通过相应的一个电接触元件与每个导热元件和每个温度感测元件连通。 加热器控制系统允许每个容器独立于其他容器进行控制。

公开(公告)号：WO01038402A1

公开(公告)日：2001-05-31

申请号：PCT/EP2000/011098

申请日：2000-11-10

IPC: B01J14/00 ,  B01J19/00 ,  B01J19/20 ,  C08F2/01 ,  C08F2/10 ,  C08F220/00

CPC classification number: C08F2/01 ,  B01J14/00 ,  B01J19/0013 ,  B01J19/20 ,  B01J2219/00033 ,  B01J2219/00063 ,  B01J2219/00085 ,  B01J2219/00094 ,  B01J2219/00123 ,  B01J2219/00128 ,  B01J2219/00162 ,  B01J2219/00166 ,  C08F2/10

Abstract: The invention relates to a method for continuously producing cross-linked, fine-particle geleous polymerizates by copolymerizing: a) water-soluble, monoethylenically unsaturated monomers; b) 0.001 to 5 mol %, with regard to monomers (a), of monomers containing at least two ethylenically unsaturated double bonds, and; (c) 0 to 20 mol %, with regard to monomers (a), of water-insoluble monoethylenically unsaturated monomers in 20 to 80 wt. % of an aqueous solution in the presence of an initiator and at temperatures ranging from 0 to 140 DEG C, whereby the aqueous solution of the monomers, together with the initiator and an inert gas, are continuously fed to a kneader-mixer having at least two shafts which rotate parallel to the axis. A number of kneading and transport elements are situated on the shafts and deliver the substances, which are added at the entry to the kneader-mixer, in an axial direction to the end of the mixer. The inventive method is characterized in that the proportion of the heat dissipation effected by evaporating water out of the reaction mixture equals at least 5 % of the reaction heat, and the proportion of the heat dissipation effected by product discharge equals at least 25 % of the reaction heat, and the remaining heat dissipation is effected by cooling the reactor walls.

Abstract translation: 基于从0单体（a），至少两个烯属不饱和双键的单体和c）以％ - 的方法，kontrinuierlichen通过共聚制备交联的，细碎的聚合物凝胶）的水溶性单烯属不饱和单体，b）由0.001至5摩尔 20摩尔 - ％，基于单体（a）含有20〜80重量的水不溶性monethylenixh Dopplebindungen不饱和单体。 - 在Initialtor的存在下，在温度为0至140℃下，连续地得到混合捏和机与引发剂和惰性气体与至少两个轴向一起供给的单体的水溶液％水溶液平行的旋转轴，其中所述轴几个KNET - 和是输送元件，其导致促进在朝向混合器的端部在轴向方向上混合捏和机物质的开头所添加的，其特征在于的，在热从反应混合物中通过水的蒸发除去部分是反应热和热通过除去部分的至少5％ 产物排放是热Reaktins的至少25％，残余的热去除需要在反应器壁上的冷却。

公开(公告)号：WO01021302A1

公开(公告)日：2001-03-29

申请号：PCT/US2000/024537

申请日：2000-09-08

IPC: B01J19/00 ,  B01J19/02 ,  B01J19/18 ,  C08G64/20 ,  C40B40/14 ,  C40B60/14 ,  G01N21/33

CPC classification number: C08G64/205 ,  B01J19/0006 ,  B01J19/002 ,  B01J19/0046 ,  B01J19/0066 ,  B01J19/0073 ,  B01J19/02 ,  B01J19/18 ,  B01J2219/00063 ,  B01J2219/00083 ,  B01J2219/00094 ,  B01J2219/00132 ,  B01J2219/00155 ,  B01J2219/00162 ,  B01J2219/00186 ,  B01J2219/00252 ,  B01J2219/00283 ,  B01J2219/00308 ,  B01J2219/00481 ,  B01J2219/00495 ,  B01J2219/00585 ,  B01J2219/00693 ,  B01J2219/00698 ,  B01J2219/00722 ,  C40B40/14 ,  C40B60/14 ,  Y02P20/149

Abstract: In an exemplary embodiment, the apparatus includes a reaction vessel (2) having an interior portion adapted to receive a reaction mixture. An agitator (10) is disposed relative to the reaction vessel (2) such that the agitator (10) is capable of agitating the reaction mixture. A conduit (11) is placed in fluid communication with the interior portion of the reaction vessel (2). A temperature probe (13) is placed in thermal communication with the reaction vessel (2), and an optical analyzer (20) adapted to perform real-time in situ analysis of the reaction mixture is placed proximate or within the reaction vessel (2). In operation, the reaction is monitored and reaction conditions are adjusted, if necessary, to maintain the reaction within pre-determined parameters. The reactor can be used for parallel screening of potential reactants and process conditions.

Abstract translation: 在示例性实施例中，该装置包括具有适于接收反应混合物的内部的反应容器（2）。 搅拌器（10）相对于反应容器（2）设置，使得搅拌器（10）能够搅拌反应混合物。 导管（11）被放置成与反应容器（2）的内部流体连通。 将温度探头（13）放置成与反应容器（2）热连通，并且适于对反应混合物进行实时原位分析的光学分析仪（20）放置在反应容器（2）的近处或内部， 。 在操作中，监测反应并根据需要调整反应条件以将反应维持在预先确定的参数内。 反应器可用于平行筛选潜在的反应物和工艺条件。

公开(公告)号：WO01017915A1

公开(公告)日：2001-03-15

申请号：PCT/SE2000/001675

申请日：2000-08-31

IPC: C02F1/74 ,  B01F5/04 ,  B01F5/06 ,  B01F13/10 ,  B01F15/06 ,  B01J3/00 ,  B01J3/02 ,  B01J3/04 ,  B01J19/02 ,  B01J19/26 ,  C02F1/72 ,  C02F1/76 ,  C02F11/08 ,  B01J19/00

CPC classification number: B01F5/0646 ,  B01F5/045 ,  B01F15/063 ,  B01F2013/1091 ,  B01J3/008 ,  B01J3/02 ,  B01J19/02 ,  B01J19/26 ,  B01J2219/00063 ,  B01J2219/00247 ,  B01J2219/0218 ,  B01J2219/0236 ,  B01J2219/0277 ,  C02F1/72 ,  C02F1/76 ,  C02F11/086 ,  Y02P20/544

Abstract: In a high pressure and high temperature reaction system suitable for oxidative waste treatment, particularly a reaction system for supercritical water oxidation (SCWO), a method is disclosed for injecting a first fluid of a first temperature at a first flow rate into a second fluid of a second temperature at a second flow rate, mixing the first and the second fluids within a mixing length (115, 215), and wherein the first and second temperatures and the first and second flow rates are selected such that a temperature of the mixed fluids downstream of said mixing length (115, 215) is obtained, at which said first fluid being substantially non-corrosive.

Abstract translation: 在适用于氧化废物处理的高压和高温反应体系中，特别是超临界水氧化反应系统（SCWO）中，公开了一种将第一流体的第一温度以第一流速注入第一流体的第二流体 第二流量的第二温度，在混合长度（115,215）内混合第一和第二流体，并且其中选择第一和第二温度以及第一和第二流速使得混合流体的温度 获得所述混合长度（115,215）的下游，所述第一流体基本上是非腐蚀性的。

公开(公告)号：WO00047519A1

公开(公告)日：2000-08-17

申请号：PCT/JP2000/000743

申请日：2000-02-10

IPC: B01D53/32 ,  B01D53/77 ,  B01J3/04 ,  B01J10/00 ,  B01J19/00 ,  B01J19/18 ,  B01J19/26 ,  C02F1/02 ,  C02F1/461 ,  C02F1/467 ,  C02F1/74 ,  B01J3/00 ,  B01J3/02 ,  C25B3/02 ,  C25B9/00

CPC classification number: C02F1/4672 ,  B01D53/32 ,  B01D53/77 ,  B01J3/04 ,  B01J10/00 ,  B01J19/18 ,  B01J19/26 ,  B01J2219/00054 ,  B01J2219/00058 ,  B01J2219/00063 ,  B01J2219/00069 ,  B01J2219/00087 ,  B01J2219/00099 ,  B01J2219/00103 ,  B01J2219/00132 ,  B01J2219/00135 ,  B01J2219/00155 ,  B01J2219/00157 ,  B01J2219/00159 ,  B01J2219/00162 ,  B01J2219/00164 ,  B01J2219/00182 ,  B01J2219/083 ,  B01J2219/0884 ,  B01J2219/185 ,  B01J2219/30207 ,  B01J2219/30223 ,  C02F1/02 ,  C02F1/025 ,  C02F1/461 ,  C02F1/46104 ,  C02F1/46114 ,  C02F1/467 ,  C02F1/74 ,  C02F2001/46133 ,  C02F2101/36 ,  C02F2103/18 ,  C02F2103/28 ,  C02F2201/4612 ,  C02F2201/46155 ,  C02F2301/066 ,  C02F2301/08

Abstract: A method for treating an aqueous medium which comprises a first step treatment wherein an aqueous medium to be treated is subjected to an ordinary hydrothermal reaction or an ordinary electrolysis, to thereby decompose easily decomposable substances, ammonia or organic compounds capable of being decomposed by electrolysis alone, and a second step treatment wherein the resulting aqueous medium is subjected to a hydrothermal electrolysis reaction, to thereby decompose remaining organic substances. The employment of the method results in marked decrease of the electric power consumption in the second step of hydrothermal electrolysis. The method can be used for providing an apparatus and a method for treating an aqueous medium at a reduced running cost through decreasing the electric power consumption required for hydrothermal electrolysis reaction.

Abstract translation: 一种处理水性介质的方法，其包括第一步处理，其中待处理的水性介质经受普通的水热反应或普通电解，从而分解容易分解的物质，氨或能够通过电解单独分解的有机化合物 ，以及第二步处理，其中使得到的水介质进行水热电解反应，从而分解剩余的有机物质。 该方法的使用导致水热电解的第二步中的电力消耗的显着降低。 该方法可以通过降低水热电解反应所需的电力消耗来提供以降低的运行成本来处理水性介质的装置和方法。