公开(公告)号：WO1997009277A1

公开(公告)日：1997-03-13

申请号：PCT/RU1995000192

申请日：1995-09-04

Applicant: NEVALINE CO. LTD. ,  KONONOV, Viktor Evgenievich ,  TROFIMOV, Valery Afanasievich ,  SHIPOV, Valery Pavlovich

Inventor： NEVALINE CO. LTD.

IPC: C02F11/08

CPC classification number: C02F11/08 ,  B01J3/00 ,  B01J19/0086 ,  B09B3/00

Abstract: The proposed method of reprocessing biogenic waste sediment involves heat treatment of a suspension of sediments (15) at a temperature of 150-220 DEG C and pressure of 0.5-3.0 mPa for 10-120 minutes; alkalization of the suspension thus treated to produce a pH of more than 10 (17); and subsequent treatment with an oxygen-containing gas (18) at a temperature of 150-220 DEG C and pressure of 1.5-5.0 mPa for between 20 and 180 minutes. Once the pressure has fallen to atmospheric pressure and the temperature has dropped below 100 DEG C, the reaction material is divided (2) into a liquid-phase organo-mineral complex and an insoluble sediment component. Treatment with oxygen-containing gas is carried out in a device for reprocessing biogenic waste sediments (gas lift apparatus) (18) which facilitates mass-exchange processes in three-phase systems (liquid-gas-solid). The insoluble sediment component contains heavy metal salts and organic substances chemically bonded to those salts and can be used as raw material in the production of construction materials. The liquid product is a solution of organo-mineral complex containing water-soluble salts of high-molecular carboxylic acids with the properties of humic substances. The organo-mineral complex can be used in various areas of technology and agriculture.

Abstract translation: 提出的生物源废弃物后处理方法涉及在150-220℃的温度和0.5-3.0mPa的压力下对沉淀物（15）的悬浮液进行10-120分钟的热处理; 如此处理的悬浮液碱化以产生大于10（17）的pH; 随后在150-220℃的温度和1.5-5.0mPa的压力下用含氧气体（18）处理20至180分钟。 一旦压力降至大气压，温度降至100℃以下，将反应物料分为液相有机 - 无机复合物和不溶性沉淀成分。 含氧气体的处理是在三相系统（液气固体）中有利于质量交换过程的生物废物沉积物（气提设备）（18）的后处理装置中进行的。 不溶性沉淀成分含有与这些盐化学键合的重金属盐和有机物，可用作建筑材料生产中的原料。 液体产物是含有高分子量羧酸的水溶性盐的有机 - 矿物复合物与腐殖质的性质的溶液。 有机矿物复合体可用于各种技术和农业领域。

公开(公告)号：WO1996029143A1

公开(公告)日：1996-09-26

申请号：PCT/EP1995001031

申请日：1995-03-20

Applicant: SCHMIDT, Hermann ,  ZETTNER, Michael, L.

Inventor： SCHMIDT, Hermann

IPC: B01J12/00

CPC classification number: B01J12/005 ,  B01J3/00 ,  F23G7/008 ,  F23G7/065

Abstract: A process for thermochemically converting fluid or fluidisable compounds (charge), in particular organic or complex toxic compounds, into low-molecular organic or inorganic compounds, has a preliminary step, during which the energy required for the conversion reaction is generated, and at least one subsequent main step during which the conversion reaction takes place. In the preliminary step, the reaction partners that are subjected to an overpressure and form an exothermic mixture are completely mixed during a mixing phase without being able to react during the mixing phase. Only at the end of the mixing phase both reaction partners react with a high reaction speed and energy density that depend on the overpressure. During the main step of the process, a second mixture to be reacted that consists of the charge and of a reactive receives the energy required for the reaction by being mixed with the reaction products from the first partial reaction that are in a high temperature and pressure state.

Abstract translation: 一种用于热化学转化可流动的或该过程可被转换成可流动状态的化合物（起始原料），特别是有机的或复杂的有毒化合物，成由用于产生能量的转化反应和至少一个在与所述转换反应主方法步骤a预审步骤的低分子量有机或无机化合物。 发生在初始步骤发生在混合相的下过量压力的完全混合和放热物质混合物形成的反应物没有这种混合物可以在混合相反应。 仅在混合阶段的最后，两个反应伙伴反应以对应于高反应率和能量密度的压力。 在主处理步骤通过与设在第一反应步骤的高温和高压状态的反应产物混合接收第二待反应混合物组成的原料和转换物质的，用于该反应所需的能量。

公开(公告)号：WO1996017680A1

公开(公告)日：1996-06-13

申请号：PCT/FR1995001600

申请日：1995-12-05

Applicant: L'ELECTROLYSE ,  SENTAGNES, Dominique ,  BERDEU, Bernard ,  DEMAZEAU, Gérard ,  GARRABOS, Yves ,  LARGETEAU, Alain

Inventor： L'ELECTROLYSE

IPC: B01J19/00

CPC classification number: A62D3/37 ,  A62D2101/20 ,  A62D2101/24 ,  A62D2101/28 ,  B01J3/00 ,  B01J3/008 ,  C02F11/086 ,  Y02P20/544 ,  Y10S208/952

Abstract: A method for the chemical conversion of complex chemical structures in a supercritical medium is disclosed. One or more chemical structures (20) may be converted by means of a reduction reaction in a supercritical solvent (22). The method is useful for destroying hazardous products, processing industrial effluents and natural products, and altering molecular structures.

Abstract translation: 公开了一种用于超临界介质中复合化学结构化学转化的方法。 可以通过在超临界溶剂（22）中的还原反应转化一种或多种化学结构（20）。 该方法可用于破坏危险品，加工工业废水和天然产物，改变分子结构。

公开(公告)号：EP4357014A1

公开(公告)日：2024-04-24

申请号：EP21945726.4

申请日：2021-09-29

Applicant: China Petroleum & Chemical Corporation ,  Sinopec Exploration & Production Research Institute

Inventor： HU, Zongquan ,  MA, Zhongliang ,  ZHENG, Lunju ,  ZHAO, Yongqiang ,  WANG, Qiang ,  NI, Chunhua ,  YU, Lingjie ,  DU, Wei ,  HE, Chuan ,  MA, Jianfei ,  LIU, Zhongbao ,  BIAN, Ruikang ,  SHEN, Baojian

IPC: B01J3/04 ,  G09B25/06

CPC classification number: B01J3/03 ,  B01J3/04 ,  G01N1/28 ,  B01J3/00 ,  G09B25/06

Abstract: The present invention provides an experimental device and method for simulating dynamics of hydrocarbon generation and expulsion in geological process. The experimental device comprises a reaction system. The reaction system comprises a reactor having a sample chamber formed therein for placing a sample, a sample sleeve being arranged within the sample chamber for receiving the sample. The sample sleeve comprises a cylindrical body enclosing the sample in a circumferential direction, an outer side wall of the cylindrical body being in engagement with an inner side wall of the reactor, and the cylindrical body being perforated to form a channel for product circulation between an outer side wall of the sample and the inner side wall of the reactor.

公开(公告)号：EP3095772A4

公开(公告)日：2017-07-26

申请号：EP15834747

申请日：2015-10-20

Applicant: LG CHEMICAL LTD

Inventor： HAN SANG JIN ,  KANG JUN HAN ,  KO DONG HYUN ,  NAM HYUN SEOK ,  LEE JOO HYUCK ,  HAN JUN KYU ,  SUH MYUNG JI ,  CHA KYONG YONG ,  CHOI DAE HEUNG ,  HWANG YE SEUL

IPC: C07C2/40 ,  B01J3/00 ,  C07C2/08 ,  C07C5/333 ,  C07C11/167

CPC classification number: C07C5/48 ,  B01J3/00 ,  C07C5/3332 ,  C07C11/167

Abstract: Disclosed are a method of preparing conjugated diene and a device therefor. More particularly, disclosed a method of preparing conjugated diene, wherein generated gas including butadiene is cooled and then water discharged at a lower part is not directly treated as waste water and subjected to byproduct removal and steam-extraction to utilize converted steam, and an installation issue of an existing biological waste water disposal equipment due to an excessive amount of byproducts can be resolved, and a device therefor are disclosed.

Abstract translation: 公开了一种制备共轭二烯的方法及其装置。 更具体地说，公开了一种制备共轭二烯的方法，其中包含丁二烯的生成气体被冷却，然后在下部排出的水不被直接作为废水处理并且经受副产物去除和蒸汽提取以利用转化的蒸汽， 可以解决由于过量的副产物引起的现有生物废水处理设备的问题，并且公开了其装置。

公开(公告)号：EP3148732A1

公开(公告)日：2017-04-05

申请号：EP15799358.5

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/cm3 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，包括封装的金刚石颗粒，一氧化碳，和在容器中的二氧化碳。 包封的金刚石颗粒，一氧化碳，和二氧化碳经受至少4.5 GPa的压力以及至少1400℃的温度以形成金刚石颗粒之间的晶粒间键。 的切削元件包括多晶金刚石材料包含金刚石的相互键合的晶粒。 多晶金刚石材料基本上不含石墨碳和金属的化合物。 多晶金刚石材料表现出至少约3:49克/厘米3的密度和至少约1000 GPa的弹性模量。 钻地工具可包括寻求固定到主体上的切割元件。

公开(公告)号：EP3061726A1

公开(公告)日：2016-08-31

申请号：EP16000407.3

申请日：2016-02-18

Applicant: TerraNova Energy GmbH

Inventor： Buttmann, Marc ,  Yalcin, Erkan ,  Schneider, Claudia ,  Decker, Andreas

IPC: C01B25/00 ,  B01D11/02 ,  B01D21/01 ,  B01J3/00 ,  B09B3/00 ,  C01B25/28 ,  C01B25/32

CPC classification number: C01B25/003 ,  B01D11/0257 ,  B01D21/01 ,  B01J3/00 ,  B09B3/00 ,  B09B3/0016 ,  B09B3/0083 ,  C01B25/28 ,  C01B25/32

Abstract: Offenbart wird ein Verfahren zur Abtrennung von Phosphor aus Biomasse, insbesondere aus Klärschlamm, wobei zunächst eine hydrothermale Karbonisierung durchgeführt wird, dann der entstandene Kohleschlamm ohne eine vorausgehende Fest-Flüssigtrennung im pH-Wert abgesenkt wird, anschließend nur eine Fest-Flüssigtrennung zur Abscheidung der Flüssigphase vorgenommen wird und schließlich die Flüssigphase einer Phosphoreliminierung unterzogen wird. Sowie eine Vorrichtung, insbesondere zur Durchführung des vorbeschriebenen Verfahrens umfassend ein durchbeaufschlagtes Reaktionsvolumen zur Durchführung der hydrothermalen Karbonisierung 1 ein Reaktionsgefäß mit Rührwerk und Säurezufuhr 2, 3 in direkter Verbindung mit 1 oder mit einer Einrichtung zur gravimetrischen Eindickung, eine Fest-Flüssig-Trenneinrichtung 4 ein Behältnis zur Phosphoreliminierung durch Abscheidung mittels Fällung / Kristallisation 7 bzw. durch Wasserverdampfung einen Auslass für den phosphorhaltigen Feststoff 8 / das phosphorhaltige wässrige Konzentrat, ggf. unter Weiterverarbeitung durch Entwässerung und/oder Trocknung und/oder Granulierung,einen Auslass für Kohle 5.

Abstract translation: 公开了一种用于由生物质为液相的分离分离磷，尤其是污水污泥，其中第一水热碳化进行，然后将所得煤浆被降低，而不在所述pH值的前述固 - 液分离，然后仅一个固 - 液分离的过程 进行，最后，磷消除液相进行。 和包含durchbeaufschlagtes反应体积进行水热碳化1与1或与重力增稠的装置的固 - 液分离装置4是一种设备，特别是用于执行上述方法搅拌器和酸进料2，3直接连通的反应容器 容器为除磷通过沉积通过沉淀/结晶7或通过蒸发水的含磷固体8 /含磷水性浓缩物的出口，任选地与进一步的处理通过脱水和/或干燥和/或粒化，对于碳的出口。5

公开(公告)号：EP2627659B1

公开(公告)日：2016-04-20

申请号：EP11832197.5

申请日：2011-10-14

Applicant: UPM-Kymmene Corporation

Inventor： MIETTINEN, Mauno

IPC: C07G1/00 ,  D21C11/00 ,  D21C11/04

CPC classification number: D21C11/10 ,  B01J3/00 ,  B01J3/02 ,  B01J3/042 ,  C07G1/00 ,  D21C11/0007 ,  D21C11/04

Abstract: In a method for the continuous precipitation of lignin from black liquor black liquor is provided so as to flow as a pressurized flow in a reactor (2) with a dwell time of less than 300s,—an acidifying agent selected from the group of carbon dioxide, acid and their combinations is led to the flow at one or more feeding sites (2a) to lower the pH of black liquor,—the pH is allowed to decrease by the effect of the acidifying agent in the pressurized flow to the precipitation point of lignin, the pressure of the pressurized flow is abruptly released, and lignin particles are separated from black liquor.

公开(公告)号：EP2894192A2

公开(公告)日：2015-07-15

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: 一种用于生产原料的再生树脂组合物的系统，包括（1）： - 用于分解热固性树脂，其包括分解反应装置（2）：导入部（222），用于将含有热固性树脂的树脂组合物和 含热固性树脂或单体组分的衍生物的单体组分的溶剂; 用于获得第一处理回收产品含有生成具有降低的分子量，固体残余物和低沸点成分含有溶剂的热固化性树脂的再生树脂，通过加热和加压所述树脂的分解反应部（221） 组合物和溶剂，使溶剂达到超临界状态或亚临界状态，并且在分解反应部（221）被包括一个管式反应器（22），所有这些是angepasst与树脂组合物和进行分解处理的 毕业，和用于排出第一处理回收产品，worin分解反应装置（2）是angepasst以连续地执行引入树脂组合物和溶剂导入部（222），分解处理的排出部（223） 在分解反应部的热固化性树脂（221）和所述第一恢复治疗PROD的放电的 从排出部（223），用作固 - 液分离器，worin第一分离单元的第一分离单元（51）UCT（51）被设计用于分离和从第一处理回收产物中除去固体残余物，第二 分离单元（52）作为气体 - 液体分离器，worin第二分离单元（52）被设计用于分离和提取与所述降低的分子量的再生树脂，以及作为低沸点组分含有来自溶剂 从该固体残留物已被除去的第一处理回收产品，worin第一分离单元（51）和所述第二分离单元（52）指定的序列中被连接到分解反应装置（2）的放电部（223） ，

公开(公告)号：EP1098005B1

公开(公告)日：2011-05-11

申请号：EP00127181.6

申请日：1996-03-07

Applicant: Pressure Biosciences, Inc.

Inventor： Laugharn, James A., Jr. ,  Dreier, Gustav H. ,  Rudd, Edwin A. ,  Green, David J.

IPC: C07K1/04 ,  C12M1/40 ,  C07H21/00

CPC classification number: C12N9/00 ,  B01J3/00 ,  B01J19/185 ,  B01J2219/00162 ,  B01J2219/002 ,  B01J2219/00211 ,  B01J2219/00229 ,  Y10T436/143333