公开(公告)号：WO2017095042A1

公开(公告)日：2017-06-08

申请号：PCT/KR2016/013094

申请日：2016-11-14

Applicant: KOREA RESEARCH INSTITUTE OF CHEMICAL TECHNOLOGY

Inventor： YU, Ju-Hyun ,  EOM, In-Yong ,  JEGAL, Jong-Geon ,  KOO, Myung-Hoi

IPC: B01J4/00 ,  B01J19/24 ,  B01J19/00 ,  B01F7/08 ,  C12P1/00 ,  B01J3/00 ,  B01J3/02 ,  B65G33/18 ,  B02C19/22 ,  B02C7/02

CPC classification number: B02C23/24 ,  B01F7/00866 ,  B01F7/085 ,  B01F7/086 ,  B01J3/00 ,  B01J3/02 ,  B01J4/00 ,  B01J19/00 ,  B01J19/24 ,  B02C7/02 ,  B02C7/04 ,  B02C19/22 ,  B65G33/18 ,  C12P1/00

Abstract: The present disclosure relates to a high-pressure reactor for continuous hydrolysis of lignocellulosic biomass and a method for continuous high-pressure pretreatment. The present disclosure is very useful in continuous high-temperature, high-pressure steam explosion and hydrolysis of biomass because the surface area can be increased and the aspect ratio (fiber width/fiber length) can be decreased through quick hydration and abrasion and various crushed lignocellulosic biomass having different properties can be continuously injected into the high-pressure reactor, regardless of the kind of biomass.

Abstract translation: 本公开涉及用于木质纤维素生物质的连续水解的高压反应器和用于连续高压预处理的方法。 本公开在连续高温，高压蒸汽爆炸和生物质水解中非常有用，因为可以增加表面积并且通过快速水化和磨损以及各种压碎可以降低纵横比（纤维宽度/纤维长度） 无论生物质的种类如何，具有不同特性的木质纤维素生物质都可以连续地注入高压反应器中。

公开(公告)号：WO2016063399A1

公开(公告)日：2016-04-28

申请号：PCT/JP2014/078209

申请日：2014-10-23

Applicant: 中国電力株式会社 ,  国立大学法人広島大学 ,  中電プラント株式会社 ,  株式会社東洋高圧

Inventor： 松村　幸彦 ,  和田　泰孝 ,  久保田　晴仁 ,  中村　昭史 ,  尾山　圭二 ,  川井　良文 ,  野口　琢史

IPC: C10J3/78 ,  B01J3/00

CPC classification number: B01J3/00 ,  C10J3/78 ,  Y02P20/544

Abstract: 　本発明の課題は、ガス化原料を含む水を加熱及び加圧して超臨界状態とし、このガス化原料を分解処理して燃料ガスを得るに際し、高温域でのタールの生成を抑制することにある。　本発明は、高分子化合物を含むガス化原料から原料スラリーを作製し、前記ガス化原料を含む水を加熱及び加圧して超臨界状態とすることで前記ガス化原料を分解処理し、燃料ガスを得るガス化装置であって、原料スラリーにラジカル捕捉剤を添加する捕捉剤添加部４１と、ラジカル捕捉剤が添加された原料スラリーにおけるガス化原料を含む水を、超臨界状態まで加熱及び加圧するガス化処理部４０とを有することを特徴とする。

Abstract translation: 本发明解决了在对包含气化原料的水进行加热加压使得水处于超临界状态并使气化原料劣化以获得燃料气体时，在高温范围内抑制焦油的产生的问题。 本发明是一种气化器，其从包括高分子化合物的气化原料产生原料浆料，通过对包括气化原料的水进行加热和加压来使气化原料降解，使得水处于超临界状态，并获得燃料气体 。 气化器的特征在于包括向原料淤浆中添加自由基清除剂的清除剂添加单元41和将自由基清除剂加入到原料浆中的包含气化原料的水加热和加压的气化单元40， 水处于超临界状态。

公开(公告)号：WO2016058229A1

公开(公告)日：2016-04-21

申请号：PCT/CN2014/090361

申请日：2014-11-05

Applicant: 彭碳科技有限公司

Inventor： 彭雁 ,  杜桂香

IPC: C01B31/06 ,  C01B31/02 ,  B01J3/00

CPC classification number: B01J3/00 ,  C01B32/05 ,  C01B32/25

Abstract: 提供了制备三维石墨烯包覆单粒子纳米金刚石材料的配方及方法；采用三硝基甲苯、黑索金或奥克托金、以及金属作为配方原料，并将配方原料制备成含能材料，从而利用高能量来合成三维石墨烯包覆单粒子纳米金刚石材料；配方应用于含能材料反应法，相对于传统制备过程没有导致成本的大幅度增加，并且可以为三维石墨烯包覆单粒子纳米金刚石材料的形成提供足够的高能量，得到纯度较高的三维石墨烯包覆单粒子纳米金刚石材料。

公开(公告)号：WO2015184285A1

公开(公告)日：2015-12-03

申请号：PCT/US2015/033223

申请日：2015-05-29

Applicant: BAKER HUGHES INCORPORATED

Inventor： BIRD, Marc, W.

IPC: B22F3/12 ,  B22F7/06 ,  E21B10/42

CPC classification number: E21B10/567 ,  B01J3/00 ,  B01J2203/062 ,  B01J2203/0655 ,  B01J2203/0685 ,  B24D18/0009 ,  B24D99/005 ,  E21B10/55

Abstract: A method of forming polycrystalline diamond includes encapsulating diamond particles, carbon monoxide, and carbon dioxide in a container. The encapsulated diamond particles, carbon monoxide, and carbon dioxide are subjected to a pressure of at least 4.5 GPa and a temperature of at least 1400°C to form inter-granular bonds between the diamond particles. A cutting element includes polycrystalline diamond material comprising inter-bonded grains of diamond. The polycrystalline diamond material is substantially free of graphitic carbon and metallic compounds. The polycrystalline diamond material exhibits a density of at least about 3.49 g/cm 3 and a modulus of at least about 1000 GPa. An earth-boring tool may include such a cutting element secured to a body.

Abstract translation: 形成多晶金刚石的方法包括将金刚石颗粒，一氧化碳和二氧化碳包封在容器中。 将包封的金刚石颗粒，一氧化碳和二氧化碳经受至少4.5GPa的压力和至少1400℃的温度以在金刚石颗粒之间形成颗粒间结合。 切割元件包括多晶金刚石材料，其包含金刚石的互相结合的颗粒。 多晶金刚石材料基本上不含石墨碳和金属化合物。 多晶金刚石材料表现出至少约3.49g / cm 3的密度和至少约1000GPa的模量。 钻孔工具可以包括固定到主体上的这种切割元件。

公开(公告)号：WO2008092102A3

公开(公告)日：2008-10-16

申请号：PCT/US2008052089

申请日：2008-01-25

Applicant: PRESSURE BIOSCIENCES INC ,  TING EDMUND Y

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: 压力循环系统包括配置成接收样品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朝向电荷泵的流动。 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。 控制器被配置为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操作压力增加器来在第二压力和第三压力之间波动反应室中的压力。

公开(公告)号：WO2008092102A2

公开(公告)日：2008-07-31

申请号：PCT/US2008/052089

申请日：2008-01-25

Applicant: PRESSURE BIOSCIENCES INC. ,  TING, Edmund, Y.

Inventor： TING, Edmund, Y.

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: 压力循环系统包括配置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。 该控制器还被配置为通过所述增压器的操作，以在波动第二压力和第三压力之间的反应室中的压力。

公开(公告)号：WO00061275A2

公开(公告)日：2000-10-19

申请号：PCT/DE2000/001061

申请日：2000-04-07

IPC: B01F3/08 ,  B01F5/02 ,  B01F13/00 ,  B01F15/06 ,  B01J3/00 ,  B01J3/02 ,  B01J3/04 ,  B01J3/06 ,  B01J19/00 ,  B01J19/24 ,  B01J19/26

CPC classification number: B01J3/06 ,  B01F5/0256 ,  B01F13/0059 ,  B01F15/06 ,  B01F2215/0036 ,  B01J3/00 ,  B01J19/0093 ,  B01J19/2405 ,  B01J19/26 ,  B01J2219/00123 ,  B01J2219/0015 ,  B01J2219/00162 ,  B01J2219/00835

Abstract: The invention relates to a method and a device for carrying out chemical and physical processes. The aim of the invention is to be able to carry out such processes with better results and in the same apparatus. To this end, for the initiation of chemical or physical processes the invention provides for at least two liquid media to be injected by means of pumps, preferably high-pressure pumps, into a reactor chamber (5) enclosed by a reactor housing (53) and on to a shared collision point (25), each medium being injected through one nozzle (1). Through an opening (3a) in the reactor chamber a gas, an evaporating liquid, a cooling liquid or a cooling gas is introduced so as to maintain the gas atmosphere in the reactor interior, notably in the collision point (25) of the liquid jets, and to cool the resulting products. The resulting products and excess gas are removed from the reactor housing (53) via a further opening (3) by positive pressure on the gas input side or negative pressure on the product and gas discharge side.

Abstract translation: 本发明涉及一种方法和用于实施化学和物理过程的装置。 为了具有更好的结果，并且在相同的装置根据本发明进行这些处理中提出，以引发的化学或物理过程的泵中的至少两种液体介质，优选高压泵，通过一个喷嘴各自（1）到（一个反应器壳体53的 ）封闭反应室（5）（到公共碰撞点25）被注入，其在碰撞点的开口（3a）的到反应器腔室中的气体，挥发的液体中，冷却液体或冷却气体，以保持反应器内的气体气氛下，特别是 （25）的液体射流，或对于所得到的产品的冷却被启动，并且所述产品，并将所得的过量气体通过过压的气体入口侧或负压的产品和气体出口侧的方式从反应器壳体（53）的另一开口（3） 我们走 RDEN。

公开(公告)号：WO99028023A1

公开(公告)日：1999-06-10

申请号：PCT/JP1998/005335

申请日：1998-11-27

IPC: B01D53/46 ,  B01D53/00 ,  B01J3/00 ,  C01B23/00 ,  C23C16/44 ,  B01J3/02 ,  H01L21/285 ,  H01L21/205 ,  H01L21/203 ,  C23C16/50 ,  C23F4/00

CPC classification number: C01B23/001 ,  B01D53/00 ,  B01D2256/18 ,  B01D2258/0216 ,  B01J3/00 ,  C23C16/4412 ,  Y02C20/30

Abstract: A method of and an apparatus for recovering a rare gas, capable of efficiently recovering a rare gas discharged from equipment using the rare gas, stably supplying the rare gas of a predetermined purity to the same equipment and reducing the consumption of the rare gas, wherein, when the rare gas in an exhaust gas discharged from the rare gas-using equipment operated under vacuum is recovered, the introducing of the exhaust gas into a recovery system is switched to/from the discharging of the same gas to an exhaust system under a vacuum condition, this switching operation being carried out in accordance with the concentration of the impurity components contained in the exhaust gas and the operational condition of the rare gas-using equipment.

Abstract translation: 一种用于回收稀有气体的方法和装置，其能够有效地回收使用稀有气体从设备排出的稀有气体，将相同设备稳定地供给预定纯度的稀有气体并减少稀有气体的消耗，其中 当回收从在真空下运行的稀有气体使用设备排出的废气中的稀有气体时，将废气引入回收系统中，从同一气体向排气系统的排放切换到 真空条件下，根据废气中所含的杂质成分的浓度和稀有气体使用设备的运转状况进行切换。

公开(公告)号：WO1997023283A1

公开(公告)日：1997-07-03

申请号：PCT/NZ1996000141

申请日：1996-12-16

Applicant: CONVERTECH GROUP LIMITED ,  SCOTT, Kenneth, Eli ,  ARNOUX, Louis, Auguste, Raymond ,  ORANGE, Paul, Anthony

Inventor： CONVERTECH GROUP LIMITED

IPC: B01J03/00

CPC classification number: C08H99/00 ,  B01J3/00 ,  B01J19/10 ,  B01J19/26 ,  B01J2219/00119 ,  B01J2219/00123 ,  B01J2219/00162 ,  B01J2219/00166 ,  C07G17/004 ,  C10G1/02 ,  C13B50/00 ,  C13K1/02 ,  D21C11/06

Abstract: A method of producing carbohydrate complexes and/or hydrocarbon complexes from organic material(s) which comprises the steps of (i) preparing a dense mixed phase of organic particulate materials entrained with a gas (such as steam) [the entraining gas being preferably less than 1 % by weight of the total dense mixed phase and the entraining gas preferably not reacting with the organic particulate materials under the chosen operating conditions]; (ii) mixing the organic material(s) as dense mixed phased entrained particulate material(s) with a (preferably gaseous) heat transfer medium which is at an elevated temperature and allowing pyrolytic and/or thermochemical conversion to occur at elevated pressure(s) and temperature(s) to produce and oil/gas phase, and (iii) rapidly reducing the temperature of the oil/gas phase from step (ii) without any substantial mixing with a coolant to produce the carbohydrate complex(es) and/or hydrocarbon complex(es). The steps (ii) and (iii) are performed in a total time of less than or equal to 10 seconds (preferably less than 4 seconds).

Abstract translation: 一种从有机材料制备碳水化合物络合物和/或烃络合物的方法，其包括以下步骤：（i）制备夹带有气体（例如蒸汽）的有机颗粒物质的致密混合相[引入气体优选较少 超过1％重量的总致密混合相，并且夹带气体优选在选择的操作条件下不与有机颗粒材料反应]; （ii）将有机材料作为致密的混合带状夹带的颗粒材料与处于升高的温度的（优选气态的）传热介质混合，并允许在高压下发生热解和/或热化学转化 ）和产生的温度和油/气相，和（iii）快速降低来自步骤（ii）的油/气相的温度，而没有与冷却剂的任何实质混合以产生碳水化合物复合物和/ 或烃络合物。 步骤（ii）和（iii）在小于或等于10秒（优选小于4秒）的总时间内进行。

公开(公告)号：WO1997010194A1

公开(公告)日：1997-03-20

申请号：PCT/IB1996000830

申请日：1996-08-23

Applicant: METHANOL CASALE S.A. ,  FILIPPI, Ermanno

Inventor： METHANOL CASALE S.A.

IPC: C07C29/151

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.

Abstract translation: 在包括二次重整器部分，高温CO转化部分和低温CO转化部分串联布置的设备中的氨和甲醇共同生产的方法和氨合成部分的特征在于以下事实： 来自甲醇合成段的未反应气流在被供给到低温CO转化段之前有利地被包含通过与来自二级重整器部分的气流的间接热交换适当加热的H 2 O的液体流饱和。