公开(公告)号：EP2489444A1

公开(公告)日：2012-08-22

申请号：EP10823430.3

申请日：2010-10-14

Applicant: Urayasu Densetsu K.K.

Inventor： KOBAYASHI, Takaitsu

IPC: B09B3/00 ,  A01G9/18 ,  A01G9/24 ,  C02F11/02 ,  C02F11/06 ,  C02F11/12 ,  C05F7/00 ,  C05F9/02 ,  C05F17/02

CPC classification number: B09B3/00 ,  B01D53/343 ,  B01D53/78 ,  B01D2257/90 ,  B01D2258/05 ,  C05F7/00 ,  C12M21/04 ,  C12M47/14 ,  F23G7/001 ,  F23G2900/50208 ,  Y02A40/213 ,  Y02P20/152 ,  Y02P20/59 ,  Y02P60/24 ,  Y02W10/40 ,  Y02W30/20 ,  Y02W30/43

Abstract: Provided is a treatment system whereby a wet organic waste can be effectively treated and CO 2 produced in the course of the treatment can be immobilized to thereby contribute to the reduction of CO 2 . The treatment system is characterized by including microbiologically fermenting a wet organic waste in a fermentation device, combusting in a combustion furnace a fermented material obtained from the fermentation device and, at the same time, supplying to the combustion furnace a fermentation gas produced by the microbiological fermentation treatment in the fermentation device, and then recovering and immobilizing CO 2 in a hot exhaust gas produced by the combustion treatment in the combustion furnace.

Abstract translation: 提供了可以有效地处理湿有机废物并且可以固定在处理过程中产生的CO 2从而有助于还原CO 2的处理系统。 处理系统的特征在于在发酵装置中微生物发酵湿有机废物，在燃烧炉中燃烧由发酵装置获得的发酵材料，同时向燃烧炉供给由微生物产生的发酵气体 在发酵装置中发酵处理，然后在燃烧炉中通过燃烧处理产生的热废气中回收和固定CO 2。

公开(公告)号：EP2379206A4

公开(公告)日：2012-07-04

申请号：EP09838563

申请日：2009-12-14

Applicant: UOP LLC

Inventor： HUANG RICHARD ,  DAVIS LAMAR A ,  LECHNICK WILLIAM J ,  ZHU XIN X

IPC: B01D53/75 ,  B01D53/14 ,  B01D53/26 ,  B01D53/34 ,  B01D53/40 ,  C10L3/10

CPC classification number: B01D53/1425 ,  B01D53/1456 ,  B01D53/343 ,  B01D53/77 ,  B01D53/78 ,  B01D2257/304 ,  B01D2257/308 ,  B01D2257/504

公开(公告)号：EP2109491A4

公开(公告)日：2012-04-04

申请号：EP08728818

申请日：2008-02-01

Applicant: CHEVRON USA INC

Inventor： BUCKLES JOHN J ,  EATON ANTHONY P ,  CHAN KAMAN I

IPC: B01D53/14 ,  B01D53/34

CPC classification number: B01D53/1425 ,  B01D53/1462 ,  B01D53/343 ,  C10L3/10 ,  C10L3/102

公开(公告)号：EP2401052A2

公开(公告)日：2012-01-04

申请号：EP09717231.6

申请日：2009-02-24

Applicant: Timmins, Cyril ,  Mayer, Ruth Elizabeth ,  Fisher, Jacqueline Anne ,  Timmins, Robert John ,  Timmins, Bryan Christopher

Inventor： Timmins, Cyril ,  Mayer, Ruth Elizabeth ,  Fisher, Jacqueline Anne ,  Timmins, Robert John ,  Timmins, Bryan Christopher

IPC: B01D53/00 ,  B01D53/14 ,  C01B31/20 ,  F23J15/04

CPC classification number: B01D53/002 ,  B01D53/0462 ,  B01D53/1475 ,  B01D53/343 ,  B01D53/62 ,  B01D53/75 ,  B01D2256/16 ,  B01D2256/22 ,  B01D2257/502 ,  C01B3/34 ,  C01B3/506 ,  C01B3/52 ,  C01B3/56 ,  C01B31/20 ,  C01B32/50 ,  C01B2203/0233 ,  C01B2203/025 ,  C01B2203/0283 ,  C01B2203/0405 ,  C01B2203/0415 ,  C01B2203/043 ,  C01B2203/0445 ,  C01B2203/0475 ,  C01B2203/0485 ,  C01B2203/06 ,  C01B2203/1241 ,  C01B2203/1258 ,  C01B2203/146 ,  C01B2203/84 ,  C10J3/46 ,  C10J2300/1612 ,  C10J2300/1653 ,  C10J2300/1662 ,  C10K1/005 ,  C10K1/08 ,  C10K3/04 ,  F02C3/28 ,  F02C6/08 ,  F05D2220/722 ,  F05D2220/75 ,  F23J15/06 ,  F23J2900/15061 ,  F25J3/061 ,  F25J3/0625 ,  F25J3/0635 ,  F25J3/0655 ,  F25J3/066 ,  F25J3/067 ,  F25J2205/40 ,  F25J2205/50 ,  F25J2210/70 ,  F25J2235/80 ,  F25J2240/12 ,  F25J2260/80 ,  F25J2270/12 ,  Y02C10/04 ,  Y02C10/06 ,  Y02C10/08 ,  Y02C10/12 ,  Y02E20/16 ,  Y02E20/18 ,  Y02E20/185 ,  Y02E20/326 ,  Y02E50/12 ,  Y02P20/129 ,  Y02P20/152 ,  Y02P30/30

Abstract: An energy conversion process that exports by-product CO2 at elevated pressure where a fuel gas feed stream is mixed with a reactant stream and additional CO2 is added to at least part of, the fuel gas feed stream, the reactant stream or both through desorption by contacting with a CO2-rich solvent stream in a first stage contactor to produce a mixed feed gas stream and a CO2-lean solvent stream; passing said mixed feed gas stream to a chemical conversion step, where further CO2 is produced; chilling at least part of the products of said chemical conversion step and thereby produce a CO2-lean gas stream; and passing at least part of said CO2-lean gas stream said to a second stage contactor where further CO2 is removed, by absorption, to produce a product gas stream and a solvent stream rich in CO2 from which said CO2-rich solvent stream is subsequently derived.

公开(公告)号：EP1827656B1

公开(公告)日：2011-05-04

申请号：EP05800552.1

申请日：2005-10-12

Applicant: NORSK HYDRO ASA

Inventor： ÅSEN, Knut, Ingvar ,  EIMER, Dag, Arne

IPC: B01D53/62 ,  B01D53/14

CPC classification number: B01D53/62 ,  B01D53/1475 ,  B01D53/343 ,  Y02A50/2342 ,  Y02C10/04 ,  Y02C10/06 ,  Y02E20/16 ,  Y02E20/18

Abstract: The present invention relates to a method for removing and recovering CO 2 from exhaust gas from a gas turbine based electric power and heat generation process (a main power process) by chemical absorption and desorption for deposition of CO 2 as convenient at the location. The exhaust gas from said main power process is cooled before being fed to a secondary gas turbine based power and heat generation process (a secondary power process) where said exhaust gas is compressed to elevated pressure and used as oxidant in a secondary gas turbine combustion chamber in said secondary power process. The resulting hot exhaust gas from said secondary process is further fed to a turbine connected to an electric power generator where the exhaust gas is depressurised to close to ambient pressure before entering a heat recovery process where the exhaust gas is cooled and further fed to a CO 2 separation process for capturing of CO 2 .

公开(公告)号：EP2276552A1

公开(公告)日：2011-01-26

申请号：EP09745308.8

申请日：2009-05-15

Applicant: Calix Limited

Inventor： SCEATS, Mark, Geoffrey

IPC: B01D53/62 ,  B01D53/02 ,  B01D53/14 ,  B01D53/73 ,  C01B31/20

CPC classification number: B01D53/62 ,  B01D53/04 ,  B01D53/08 ,  B01D53/343 ,  B01D53/346 ,  B01D2251/404 ,  B01D2251/606 ,  B01D2257/504 ,  B01D2259/128 ,  B01D2259/40098 ,  B01D2259/65 ,  Y02A50/2342 ,  Y02C10/04 ,  Y02C10/06 ,  Y02C10/08

Abstract: A system and System for removing CO2 from an input gas stream. The system comprises a carboniser segment configured such that a solid sorbent reacts therein with the input gas stream to remove CO2 from the input gas stream; a calciner segment configured such that the solid sorbent from the carboniser segment reacts therein to release the CO2 into a substantially pure gas stream; a heat exchanger unit for exchanging heat between the carboniser and calciner segments; a first conditioning unit for controlling a CO2 partial pressure in the carboniser segment; and a second conditioning unit for controlling a CO2 partial pressure in the calciner segment; wherein the first and second conditioning units are configured such that a difference between the CO2 partial pressures in the carboniser and calciner segments respectively is controlled such that heat is provided from the carboniser to the calciner through the heat exchanging unit.

公开(公告)号：EP2262875A2

公开(公告)日：2010-12-22

申请号：EP09718359.4

申请日：2009-02-27

Applicant: Uhde GmbH

Inventor： KOWOLL, Johannes

IPC: C10J3/52 ,  C10J3/86 ,  B01D53/14 ,  B01D5/00

CPC classification number: C10J3/86 ,  B01D53/343 ,  B01D53/78 ,  C10J3/485 ,  C10J3/845 ,  C10J2300/0959 ,  C10J2300/1675 ,  C10J2300/1687 ,  C10J2300/169 ,  C10K1/101 ,  C10K1/12

Abstract: The invention relates to a method and a device for treating fluid streams produced during the combustion of carbon- and ash-containing fuels. The aim of the invention is to optimally utilize the heat content present in the system as well as the amount of water for cooling and condensation required during the recirculation of the latter. The method according to the invention is characterized in that the suspension (6) withdrawn from the mixing vessel is expanded in at least one subsequent stage (7a)-(7d) during the evaporation of at least part of the water and reduction of the temperature and in that the vapor produced is cooled by direct contact with water and at least partially condensed out. The device according to the invention is characterized in that a line (6) between a lower section of the mixing vessel (1b) leads to a first expansion vessel that is designed as a scrubber tower (7a), the scrubber tower being provided with a condensate collection bottom (8a) and a recirculation line (10a) towards the mixing vessel (1b) for the forming condensate, which mixing vessel is equipped with spray heads.

公开(公告)号：EP1508360A2

公开(公告)日：2005-02-23

申请号：EP04013305.0

申请日：2004-06-05

Applicant: Donau Carbon GmbH & Co. KG

Inventor： Reichert, Bernd, Dipl.-Ing. ,  Röder, Herbert, Dipl.-Ing.

IPC: B01D53/34

CPC classification number: B01D53/343 ,  F25B27/02 ,  F28D21/0012 ,  F28D2021/0019 ,  Y02A30/274

Abstract: Die Erfindung betrifft ein Verfahren zur Kaltwassererzeugung unter Nutzung von Desorbatwärme, die bspw. in einer Lösemittelrückgewinnungsanlage (1) anfällt. Hierzu wird in einem Desorbatwärmetauscher (12) ein Heiz- oder Kühlmedium erwärmt und dessen Wärmeenergie in einem Puffersystem (25) gespeichert, aus welchen mittels eines weiteren Heiz- oder Kühlmediums Wärmeenergie bspw. zum Heizen von Räumen abgeführt wird. Die Nutzung von Desorbatwärme zur Kaltwassererzeugung kann dadurch erreicht werden, dass das weitere Heiz- oder Kühlmedium vor der Nutzung seiner Wärmeenergie bspw. zum Heizen von Räumen in einem Temperaturgleichrichter (28) auf ein im Wesentlichen konstantes Temperaturniveau zwischen 85° C und 110° C gebracht und die Wärmeenergie des Heiz- oder Kühlmediums in einer dem Temperaturgleichrichter (28) nachgeschalteten Kaltwassererzeugungsanlage (30) zur Kühlung eines Kühlmediums eingesetzt wird. Weiter betrifft die Erfindung eine Anlage zur Kaltwassererzeugung unter Nutzung von Desorbatwärme.

Abstract translation: 在轮转凹版印刷过程中，借助于热交换器（12）缓冲单元（25）解热的热也从溶剂回收组件（1）中回收冷水，也使用辅助加热或冷却介质。 在其引入系统之前，补充介质通过温度调节单元（28），其在85至100摄氏度之间的稳定温度下投降。然后将温度调节的辅助介质放回冷水 回收系统（30），其中冷却另外的介质。 进一步的介质达到约95℃的温度。还要求的是相应的组件。

公开(公告)号：EP1161980A1

公开(公告)日：2001-12-12

申请号：EP01304829.3

申请日：2001-05-31

Applicant: Nippon Shokubai Co., Ltd.

Inventor： Okazaki, Kazuto ,  Nishimura, Takeshi ,  Sakamoto, Kazuhiko ,  Dodo, Osamu

IPC: B01D53/34 ,  F23G7/06

CPC classification number: F23G7/07 ,  B01D53/343 ,  B01D53/346 ,  B01D53/8678 ,  F23G7/066 ,  F23G2207/101 ,  F23G2207/113 ,  F23G2207/30

Abstract: An apparatus for the treatment of a waste gas that is capable of recovering the heat generated by the catalytic oxidation of a waste gas to the largest possible extent and allowing the temperature of the treated gas in a first waste gas pre-heater to be adjusted to an arbitrary level incapable of condensing moisture and/or corrosive gas is provided. The apparatus for the treatment of the waste gas includes a molecular oxygen-containing gas supplying device (207), second to n'th waste gas pre-heaters (202,203), a heat-recovering device (204), and a reactor (201).

Abstract translation: 一种用于处理废气的装置，其能够以最大可能的程度回收由废气的催化氧化产生的热量，并允许将第一废气预热器中的处理气体的温度调节至 提供了不能冷凝水分和/或腐蚀性气体的任意水平。 用于处理废气的装置包括分子氧气体供应装置（207），第二至第n废气预热器（202,203），热回收装置（204）和反应器（201） ）。

公开(公告)号：EP0562278B2

公开(公告)日：1999-08-25

申请号：EP93102596.9

申请日：1993-02-19

Applicant: BDAG Balcke-Dürr Aktiengesellschaft

Inventor： Kienböck, Martin ,  Kehr, Manfred, Dr.

IPC: B01D53/34

CPC classification number: B01D53/343