公开(公告)号：US08519076B2

公开(公告)日：2013-08-27

申请号：US12733000

申请日：2010-03-26

Applicant: Jessica Erwin ,  Klaus Massow ,  Stephan Zollner

Inventor： Jessica Erwin ,  Klaus Massow ,  Stephan Zollner

IPC: C08F2/48 ,  C08F2/00 ,  C08F2/38 ,  C08F2/46 ,  C08F118/02

CPC classification number: B01J19/0066 ,  B01J4/02 ,  B01J19/1818 ,  B01J19/20 ,  B01J2219/00094 ,  B01J2219/00135 ,  B01J2219/00186 ,  B01J2219/182 ,  B29C47/0021 ,  B29C47/42 ,  B29C47/76 ,  C08F2/02 ,  C08F2/06 ,  C08F20/12 ,  C08F220/12 ,  C08L33/06 ,  C09D133/062 ,  C09D133/066 ,  C09J7/385 ,  Y02P20/582 ,  Y10S526/918 ,  C08L2666/14

Abstract: A UV-crosslinkable polyacrylate pressure-sensitive adhesive composition having a polyacrylate having photoinitiator units incorporated therein by polymerization and being produced by a free-radical solvent-free polymerization process.

Abstract translation: 具有聚丙烯酸酯的紫外线交联性聚丙烯酸酯系粘合剂组合物，其通过聚合并入其中并通过无自由基无溶剂聚合方法制造而具有光引发剂单元。

公开(公告)号：US20120043179A1

公开(公告)日：2012-02-23

申请号：US13287448

申请日：2011-11-02

Applicant: Taishi Kurata

Inventor： Taishi Kurata

IPC: C10G19/02 ,  C10G31/06

CPC classification number: C10G9/00 ,  B01J4/02 ,  B01J19/0013 ,  B01J19/008 ,  B01J2219/00081 ,  B01J2219/00094 ,  B01J2219/00157 ,  C10G9/42 ,  C10G45/00 ,  C10G47/32 ,  C10G49/007

Abstract: Equipment and a process for upgrading oil are provided to produce a refined oil lighter than a material oil by cracking the heavier material oil with the addition of hydrogen under relatively relaxed production conditions. An equipment for upgrading oil according to one aspect of the invention includes an emulsion making portion (10), a refinery tank portion (20), and a heating portion (30), and configured to make an emulsion (E) by emulsifying ionized alkaline water (A) in a material oil (O1) in the emulsion making portion (10), and to drop droplets (D) of the emulsion (E) onto the surface (S) of a heat medium (O2) in the refinery tank portion (20) heated by the heating portion (30).

Abstract translation: 提供设备和升级油的方法，以在相对放松的生产条件下通过加入氢气裂化较重的原料油，生产比材料油更精炼的油。 根据本发明的一个方面的用于升级油的设备包括乳化制造部分（10），炼油罐部分（20）和加热部分（30），并且被构造成通过乳化电离碱 在乳液制备部分（10）中的材料油（O1）中的水（A）和将乳液（E）的液滴（D）滴落到炼油罐中的热介质（O 2）的表面（S）上 由所述加热部（30）加热的部分（20）。

公开(公告)号：US20110301307A1

公开(公告)日：2011-12-08

申请号：US13144492

申请日：2010-01-14

Applicant: Dieter Littmann ,  Andre-Armand Finette ,  Jürgen Peter Mohrbutter ,  Sven George Wolfram

Inventor： Dieter Littmann ,  Andre-Armand Finette ,  Jürgen Peter Mohrbutter ,  Sven George Wolfram

IPC: C08F2/01 ,  B01J19/18

CPC classification number: B01J19/2415 ,  B01J4/008 ,  B01J4/02 ,  B01J2219/00164 ,  B01J2219/00182 ,  B01J2219/00772 ,  C08F10/02 ,  C08F110/02 ,  C08F210/16 ,  Y10S526/919 ,  C08F2/00 ,  C08F2/001 ,  C08F2/01 ,  C08F4/38

Abstract: Process for the preparation of ethylene homopolymers or copolymers in a high pressure reactor with at least two spatially separated initiator injection points by polymerizing ethylene and optionally further monomers in the presence of at least two different mixtures of free-radical polymerization initiators at from 100° C. to 350° C. and pressures in the range of from 160 MPa to 350 MPa, wherein the process comprises the following steps: a) providing at least two different initiators as solution in a suitable solvent or in liquid state, b) mixing the initiators and optionally additional solvent in at least two static mixers and c) feeding each of the mixtures to a different initiator injection point of the high pressure reactor, and apparatus for feeding initiator mixtures to a high pressure reactor with at least two spatially separated initiator injection points.

Abstract translation: 在具有至少两个空间分离的引发剂注入点的高压反应器中制备乙烯均聚物或共聚物的方法，其通过在100℃下在至少两种不同的自由基聚合引发剂混合物存在下聚合乙烯和任选的其它单体 至350℃，压力范围为160MPa至350MPa，其中该方法包括以下步骤：a）在合适的溶剂中或以液态提供至少两种不同的引发剂作为溶液，b）将 引发剂和任选地在至少两种静态混合器中的另外的溶剂，以及c）将每种混合物进料到高压反应器的不同引发剂注入点，以及用于将引发剂混合物供入具有至少两个空间分离的引发剂注入的高压反应器的装置 积分

公开(公告)号：US20110053758A1

公开(公告)日：2011-03-03

申请号：US12714537

申请日：2010-02-28

Applicant: Richard D. Weir ,  Carl W. Nelson

Inventor： Richard D. Weir ,  Carl W. Nelson

IPC: C04B35/00

CPC classification number: C01B13/363 ,  B01J4/02 ,  B01J19/1812 ,  B01J19/2405 ,  B01J2219/00065 ,  B01J2219/00162 ,  B01J2219/00166 ,  C01B13/366 ,  C01G23/006 ,  C01P2002/34 ,  C01P2002/52 ,  C01P2002/72 ,  C01P2004/52 ,  C01P2004/61 ,  C01P2004/62 ,  C01P2006/40 ,  C01P2006/42 ,  H01B3/10

Abstract: A reactor for the wet-chemical co-precipitation of oxide powders includes a cylindrical structure having first and second ends and a lumen extending the length of the tube. A central axis extends through the lumen. The first end is closed. The reactor also includes a first inlet port disposed proximal to the first end of the cylindrical structure and providing access through the cylindrical structure to inject a first reactant solution. The reactor further includes a second inlet port disposed proximal to the first end of the cylindrical structure and providing access through the cylindrical structure to inject a second reactant solution. The first and second inlet ports are disposed on opposite sides of the cylindrical structure and are coaxial relative to the central axis.

Abstract translation: 用于氧化物粉末的湿化学共沉淀的反应器包括具有第一和第二端以及延伸管的长度的内腔的圆柱形结构。 中心轴线延伸穿过管腔。 第一个关闭。 反应器还包括设置在圆柱形结构的第一端附近的第一入口端口，并提供通过圆柱形结构的入口以注入第一反应物溶液。 反应器还包括靠近圆柱形结构的第一端设置的第二入口端口，并提供通过圆柱形结构的通路以注入第二反应物溶液。 第一和第二入口端口设置在圆柱形结构的相对侧上并且相对于中心轴线是同轴的。

公开(公告)号：US07820119B2

公开(公告)日：2010-10-26

申请号：US11074034

申请日：2005-03-07

Applicant: Dennis E. Rutkowski ,  Andy M. Yaksic

Inventor： Dennis E. Rutkowski ,  Andy M. Yaksic

IPC: B01J19/00 ,  B01J19/18 ,  C01G49/10

CPC classification number: B01J4/02 ,  B01J19/006 ,  B01J19/0066 ,  B01J19/1806 ,  B01J2219/00029 ,  B01J2219/00063 ,  B01J2219/00186 ,  B01J2219/00189 ,  B01J2219/00768 ,  C01G49/10

Abstract: The present invention involves a system and method of making ferric chloride with reduced amounts of hydrochloric acid for water treatment. The method comprises preparing a reactant batch comprising ferric oxide and hydrochloric acid at a predetermined molar ratio. The method further includes mixing the reactant batch with an impeller rotating between about 60 and 150 revolutions per minute. The method further includes maintaining the reactant batch at a temperature between about 70° Fahrenheit and 180° Fahrenheit. The method forms a reaction product including ferric chloride and a reduced amount of hydrochloric acid.

Abstract translation: 本发明涉及一种制备和制备氯化铁与减少量的盐酸进行水处理的方法。 该方法包括以预定的摩尔比制备包含氧化铁和盐酸的反应物批料。 该方法还包括将反应物批料与约60至150转/分钟之间旋转的叶轮进行混合。 该方法还包括将反应物批料保持在约70华氏​​度和180华氏度之间的温度。 该方法形成包括氯化铁和减少量的盐酸的反应产物。

公开(公告)号：US07534341B2

公开(公告)日：2009-05-19

申请号：US10552853

申请日：2004-04-15

Applicant: Rainer Karer ,  Kaspar Evertz ,  Peter Kölle ,  Hans-Jacob Feindt

Inventor： Rainer Karer ,  Kaspar Evertz ,  Peter Kölle ,  Hans-Jacob Feindt

IPC: C10G35/00 ,  C10G35/10

CPC classification number: B01J4/002 ,  B01J4/007 ,  B01J4/02 ,  B01J8/0035 ,  B01J8/004 ,  B01J8/1872 ,  B01J2208/00752 ,  C08F10/00 ,  C08F110/02 ,  C08F210/16 ,  C08F2/00 ,  C08F2/01 ,  C08F2/34 ,  C08F2500/07 ,  C08F2500/12

Abstract: Method of metering at least one solid, particulate catalyst into a reactor containing a fluidized bed (11) of particles in an at least partly gaseous medium, in which the catalyst is metered discontinuously at prescribed time intervals into the fluidized bed (11) at at least one metering point (10). According to the present invention, a fluid stream is firstly introduced into the reactor (5) so that a region having a reduced particle density is formed in the fluidized bed (11) around the metering point (10) and the catalyst is subsequently metered into this region. As a result of the prior introduction of a fluid stream (“preblowing”) before the actual introduction of the catalyst, the catalyst can penetrate significantly deeper into the fluidized bed from the metering point due to the reduced particle density and is dispersed better.

Abstract translation: 将至少一种固体颗粒催化剂计量到含有至少部分气体介质中的颗粒流化床（11）的反应器的方法，其中催化剂以规定的时间间隔不连续地计量加入流化床（11）中 至少一个计量点（10）。 根据本发明，首先将流体流引入反应器（5），使得在流化床（11）周围形成具有减小的颗粒密度的区域，并将催化剂随后计量加入 这个地区。 由于在实际引入催化剂之前先前引入流体物流（“预吹扫”），由于颗粒密度降低，催化剂可以从计量点深入到流化床中，并且分散得更好。

公开(公告)号：US20090050210A1

公开(公告)日：2009-02-26

申请号：US12258818

申请日：2008-10-27

Applicant: Han-Mei Choi ,  Thomas Jongwon Kwon ,  Jae-Soon Lim ,  Ki-Chul Kim ,  Sung-Tae Kim ,  Young-Sun Kim

Inventor： Han-Mei Choi ,  Thomas Jongwon Kwon ,  Jae-Soon Lim ,  Ki-Chul Kim ,  Sung-Tae Kim ,  Young-Sun Kim

IPC: G05D7/06 ,  B01F3/04 ,  G05D11/00

CPC classification number: C23C16/448 ,  B01B1/005 ,  B01J4/02 ,  B01J2219/0011 ,  B01J2219/00164 ,  C23C16/45561 ,  Y10T137/0329 ,  Y10T436/2575

Abstract: Liquid chemical delivery systems are provided which include a liquid chemical storage canister, a pressurized gas source that feeds a pressurized gas into the storage canister, a vaporizer that may be used to vaporize the liquid chemical supplied from the storage canister, a delivery line that connects the storage canister to the vaporizer, a liquid mass flow controller that controls the flow rate of the liquid chemical through the delivery line, a reaction chamber that is connected to the vaporizer, and a liquid chemical recycling element that collects at least some of the chemical flowing through the system during periods when the liquid chemical delivery system is isolated from the reaction chamber.

Abstract translation: 提供了液体化学输送系统，其包括液体化学品储存罐，将加压气体进料到储存罐中的加压气体源，可用于蒸发从储存罐供应的液体化学品的蒸发器，连接 储存罐到蒸发器，液体质量流量控制器，其通过输送管线控制液体化学品的流速;连接到蒸发器的反应室;以及液体化学品循环元件，其收集至少一些化学物质 在液体化学品输送系统与反应室隔离的期间流经系统。

公开(公告)号：US20090004512A1

公开(公告)日：2009-01-01

申请号：US12280703

申请日：2007-02-27

Applicant: Masakazu Sugimoto ,  Masaya Yano ,  Taiichi Sugita

Inventor： Masakazu Sugimoto ,  Masaya Yano ,  Taiichi Sugita

IPC: H01M8/00

CPC classification number: C01B3/065 ,  B01J4/008 ,  B01J4/02 ,  H01M8/04179 ,  H01M8/04186 ,  H01M8/06 ,  H01M8/0662 ,  Y02E60/362

Abstract: (EN) A liquid constant-rate emitting apparatus that in the event of delivering a liquid, such as water, from a liquid accommodating container, even when the amount thereof is small, is capable of constant-rate delivery thereof. There is provided an apparatus comprising liquid accommodating container (2) for water accommodation; water lead-out pipe (11) for water emission from the liquid accommodating container (2); gas accommodating container (1) for compressed air accommodation; and introduction pipe (6) for feeding of the compressed air within the gas accommodating container (1) into the liquid accommodating container (2), so that constant-rate water emission from the water lead-out pipe (11) is attained by application of the compressed air to the liquid within the liquid accommodating container (2).

Abstract translation: （EN）一种液体恒定速率发射装置，即使在液体容纳容器的量少的情况下也能从液体容纳容器中输送水等液体的情况下，能够恒定速度地输送。 提供了一种包括用于水容纳的液体容纳容器（2）的装置; 用于从液体容纳容器（2）排出水的出水管（11）; 用于压缩空气容纳的气体容纳容器（1） 以及用于将气体容纳容器（1）内的压缩空气供给到液体容纳容器（2）中的引入管（6），从而通过应用获得来自引水管（11）的恒定的水排放 的压缩空气流到液体容纳容器（2）内的液体。

公开(公告)号：US07465428B2

公开(公告)日：2008-12-16

申请号：US11158763

申请日：2005-06-22

Applicant: Julian Ross

Inventor： Julian Ross

IPC: A62B7/08

CPC classification number: B01J7/02 ,  A62B21/00 ,  B01J4/001 ,  B01J4/02 ,  B01J19/2445 ,  B01J2219/00029 ,  B01J2219/00038 ,  C01B13/0203 ,  C01B13/0207 ,  C01B13/0211

Abstract: An apparatus is provided to generate a gas by mixing chemicals with water. Typically, the production of gas, particularly oxygen, by combining water with powders and other dry chemicals has not been widely employed. There have existed a number of preexisting barriers such as undesirable flow rates and yields. However, by utilizing multiple reaction chambers the flow rates and yields can be more precisely tailored for a variety of situations that may call for particular flow rates and yields. Additionally, the use of the dry chemicals would allow for a long self-life allowing the apparatus to be particularly useful in emergency situations.

Abstract translation: 提供了一种通过将化学品与水混合来产生气体的装置。 通常，通过将水与粉末和其它干燥化学品结合来生产气体，特别是氧气，尚未得到广泛应用。 存在一些先前存在的障碍，例如不良流量和产量。 然而，通过利用多个反应室，可以针对可能需要特定流速和产率的各种情况更精确地定制流速和产率。 另外，干燥化学品的使用可以延长使用寿命，从而使设备在紧急情况下特别有用。

公开(公告)号：US07381837B2

公开(公告)日：2008-06-03

申请号：US10503303

申请日：2003-02-26

Applicant: Hidehiko Nakajima ,  Yoshiyuki Harano ,  Manabu Yamada

Inventor： Hidehiko Nakajima ,  Yoshiyuki Harano ,  Manabu Yamada

IPC: C07C51/12 ,  C07C51/14

CPC classification number: B01J19/0006 ,  B01J4/02 ,  B01J10/002 ,  B01J2219/00006 ,  B01J2219/00065 ,  B01J2219/00162 ,  B01J2219/00164 ,  B01J2219/002 ,  B01J2219/00207 ,  B01J2219/00216 ,  B01J2219/0022 ,  B01J2219/00231 ,  B01J2219/0024 ,  C07C51/12 ,  Y02P20/142 ,  C07C53/08

Abstract: A method comprises continuously supplying an alcohol to a pressurized reaction system, pressurizing carbon monoxide with a compressor 8 attached to a first feed line 22, for continuously supplying carbon monoxide to the reaction system via a second feed line 23 with a reference flow rate F, and converging excess carbon monoxide in the reaction system in the first feed line via a branched circulation line 24 for allowing to react alcohol with carbon monoxide. The reference flow rate F in the second feed line 23 is a total rate of a reference consumption flow rate Fcs in the reaction and a flow rate F1 in excess rate over a fluctuation consumption flow rate ΔFcv in the reaction system (F=Fcs+F1, F1>ΔFcv). According to the pressure fluctuation of the gaseous phase in the reaction system, the flow rate in the circulation line 24 is controlled to a flow rate Fr=F1−ΔFcv and the feed flow rate in the first feed line 22 is controlled to a flow rate Fsu=Fcs+ΔFcv, for compensating a consumption rate variation in the reaction system with the feed flow rate of carbon monoxide. This ensures discharge inhibition of the gaseous reactant in a liquid phase pressurized reaction system (such as carbonylation reaction system) and effective utilization of the reactant for the reaction.

Abstract translation: 一种方法包括向加压反应系统连续供应醇，用连接到第一进料管线22的压缩机8加压一氧化碳，用于经由第二进料管线23以参考流量F连续向反应系统供应一氧化碳， 并且通过分支循环管线24在第一进料管线中的反应体系中过量的一氧化碳收敛，以允许醇与一氧化碳反应。 第二进料管线23中的参考流量F是反应中的参考消耗流量Fcs和超过反应体系中的波动消耗流量DeltaFcv的流量F 1的总速率（F = Fcs + F 1，F 1> DeltaFcv）。 根据反应体系中的气相的压力波动，将循环管线24的流量控制为流量Fr = F 1 -DeltaFcv，将第一进料管线22中的进料流量控制为流量 速率Fsu = Fcs +ΔFcv，用于补偿反应体系中一氧化碳进料流量的消耗速率变化。 这确保液相加压反应体系（如羰基化反应体系）中的气态反应物的排放抑制和反应物的有效利用。