公开(公告)号：EP2799526B1

公开(公告)日：2018-12-12

申请号：EP12863066.2

申请日：2012-10-26

Applicant: Wuhan Kaidi Engineering Technology Research Institute Co., Ltd.

Inventor： ZHANG, Yanfeng ,  NIE, Hongtao ,  XIA, Minggui ,  LIU, Wenyan ,  ZHANG, Liang

IPC: C10K1/00 ,  C10K1/02 ,  C10K1/06 ,  C10K1/10 ,  C10K1/04 ,  C01B3/02 ,  C10J3/06

CPC classification number: C01B3/02 ,  C10G2300/1011 ,  C10J3/06 ,  C10J2300/0916 ,  C10J2300/1238 ,  C10K1/02 ,  C10K1/028 ,  C10K1/046 ,  C10K1/06 ,  Y02P20/123 ,  Y02P20/124 ,  Y02P20/129 ,  Y02P20/145 ,  Y02P30/20

Abstract: Provided is a biomass syngas purification process under positive pressure for producing oil and the system thereof. In the process, an oxidation air blower is employed to blast a high-temperature pyrolysis gasifier; a high-temperature syngas extracted from the gasifier enters a water-cooled chilling tower via a water-cooled flue, and the gas is partly chilled to solidify slag by spraying water; the waste heat is recovered by a waste heat boiler of a water-tube type and a waste heat boiler of a heat-tube type in two stages with double pressure; the by-products, middle pressure steam and low pressure steam, are ejected externally; after the heavy tar is condensed and recovered by the waste heat boiler of the heat-tube type, the resulting syngas enters a Venturi scrubber without padding, scrubbing dust extraction, a wet electrostatic precipitator for deep dust extraction, and is purified by removing tar fog; then the acceptable syngas is transported to a wet gas-holder for storage or supplied for use down-stream. The purification aims of cooling of the syngas in stages, gradient recycling of waste heat, stepwise dust extraction and tar removal are achieved and the technical problems of a complex system, long flow, high energy consumption, low efficiency, and poor stability and economy are resolved by optimizing the process and controlling the appropriate process parameters.

公开(公告)号：EP3274303A1

公开(公告)日：2018-01-31

申请号：EP16713832.0

申请日：2016-03-24

Applicant: SCW Systems B.V.

Inventor： ESSING, Gerardus Cornelis Otto Bernard ,  HENDRY, Douglas Scott

IPC: C02F11/08

CPC classification number: C10L3/06 ,  B01J3/008 ,  C01B3/02 ,  C01B2203/0216 ,  C01B2203/0805 ,  C02F11/086 ,  C02F11/125 ,  C02F2103/20 ,  C10L2200/0469 ,  C10L2290/04 ,  C10L2290/06 ,  C10L2290/08

Abstract: The invention relates to a method of and a system (1) for processing a slurry containing organic components, such as biomass, having a water contents of at least 50%, comprising a pump (6) and heater or heat exchanger (7) to bring the liquid in the slurry in a supercritical state, a reactor (8) to convert at least a part of the organic components in the slurry, and a separator (12) to remove gaseous products from the converted slurry, and comprising a mixer (5) for adding fluid from the converted slurry to the slurry upstream from the reactor (8).

公开(公告)号：EP3046997B1

公开(公告)日：2017-12-20

申请号：EP14777502.7

申请日：2014-08-21

Applicant: Recom Patent & License GmbH

Inventor： STREITENBERGER, Hartwig ,  KABIS, André ,  STÖBER, Reinhard ,  ZEPTER, Johannes ,  WILFER, Robert

IPC: C01B3/02 ,  C10J3/72 ,  C10J3/30 ,  C10J3/60 ,  C10J3/26

CPC classification number: C10J3/721 ,  C01B3/02 ,  C10J3/26 ,  C10J3/30 ,  C10J3/60 ,  C10J2200/152 ,  C10J2200/158 ,  C10J2300/0946 ,  C10J2300/1838 ,  C10J2300/1846

公开(公告)号：EP3122450B1

公开(公告)日：2017-10-04

申请号：EP15709935.9

申请日：2015-03-13

Applicant: Clean Fuels B.V.

Inventor： SIEMONS, Roland

IPC: B01J19/26 ,  B01J4/00 ,  F23D7/00 ,  F23D9/00

CPC classification number: B01J4/002 ,  B01J19/0026 ,  B01J2219/00247 ,  C01B3/02 ,  C01B3/22 ,  C01B2203/0266 ,  C01B2203/0272 ,  C10J3/48 ,  C10J3/485 ,  C10J2200/152 ,  C10J2300/0916 ,  C10J2300/0956 ,  C10J2300/0976 ,  C10J2300/1637 ,  F23D7/00 ,  F23D9/00 ,  F23D2900/00016

公开(公告)号：EP3214155A2

公开(公告)日：2017-09-06

申请号：EP17155870.3

申请日：2017-02-13

Applicant: KOPF SynGas GmbH & Co. KG

Inventor： Dr. Judex, Johannes

IPC: C10B47/44 ,  C10J3/48 ,  C10J3/66 ,  C10J3/72 ,  C10K1/08 ,  C10K1/32

CPC classification number: C10J3/66 ,  C01B3/02 ,  C10B47/44 ,  C10J3/466 ,  C10J3/485 ,  C10J3/723 ,  C10J3/82 ,  C10J2300/094 ,  C10J2300/0956 ,  C10J2300/1643 ,  C10K1/08 ,  C10K1/32 ,  F02B43/08

Abstract: Ein Produktionsverfahren von Synthesegas zum Betreiben eines Verbrennungsmotors (19) aus organischem Festbrennstoff, welcher in einem Pyrolyse-Reaktor (4) ohne Sauerstoffzufuhr in Pyrolyse-Produkte aufgespalten wird, wobei anschließend sämtliche Pyrolyse-Produkte aus dem Pyrolyse-Reaktor von unten her einem weiteren Reaktor zugeführt werden, wobei ein im weiteren Reaktor erzeugtes Synthesegas dem weiteren Reaktor als Produktgas entnommen und direkt oder indirekt dem Verbrennungsmotor zugeführt wird, und wobei der Pyrolyse-Reaktor mit mindestens einer Pyrolyse-Schnecke (5) zur Förderung des Festbrennstoffs betrieben wird, ist dadurch gekennzeichnet, dass der weitere Reaktor als Wirbelschicht-Reaktor (7) ausgebildet ist, welcher mittels Luftzufuhr mit einer Geschwindigkeit oberhalb der minimalen Lockerungsgeschwindigkeit des Bettmaterials der Wirbelschicht (9) des Wirbelschicht-Reaktors fluidisiert wird, dass dem Pyrolyse-Reaktor als organischer Festbrennstoff ein biogener Abfallstoff mit einem Aschegehalt von mindestens 20% der Feststoffmasse des Festbrennstoffs zugeführt wird, und dass der organische Festbrennstoff im Pyrolyse-Reaktor in Pyrolyse-Öl, Pyrolyse-Koks und Pyrolyse-Gas aufgespalten wird. Damit können organische Festbrennstoffe wie biogene Abfallstoffe, Klärschlamm, Papierschlamm, Trester, Spelzen, Mist, Schalen oder dergleichen in einem stabilen Prozess besonders kostengünstig zu einem Synthesegas vergast werden, welches zur motorischen Nutzung mittels einer Gasturbine geeignet ist.

公开(公告)号：EP3075820A4

公开(公告)日：2017-08-02

申请号：EP14864396

申请日：2014-11-21

Applicant: CHANGZHENG ENG CO LTD

Inventor： JIANG CONGBIN ,  XIN WEI ,  LI HONGHAI ,  GAO RUIHENG ,  CHEN YONGJIN ,  LI XIAOFEI ,  ZHANG YAN ,  ZHANG LI

IPC: C10J3/48 ,  C10J3/04 ,  C10J3/52

CPC classification number: C10J3/86 ,  C01B3/02 ,  C01B3/50 ,  C01B2203/04 ,  C01B2203/0877 ,  C10J3/485 ,  C10J3/506 ,  C10J3/84 ,  C10J2300/093 ,  C10J2300/0976 ,  C10J2300/1853

Abstract: A carbonaceous substance dry powder gasification device and method, the device comprising from bottom to top a lower cooling and purification section (1), a gasification reaction section (2), a cooling reaction section (3) and an upper cooling and purification section (4); an initial cooling device is disposed at the connection between the cooling reaction section and the gasification reaction section; and a plurality of nozzles are circumferentially arranged in the gasification reaction section. The method comprises: a gasification reaction is conducted between a carbonaceous substance and an oxygenated gasifying agent to generate crude synthesis gas and ash; part of the crude synthesis gas and most of the ash go downstream for cooling and gasification, and the cooled and ash removed crude synthesis gas is transferred to subsequent processes, and the quenched ash is discharged through an ash outlet; the remaining crude synthesis gas and fly ash go upstream to mix with a cooling substance for cooling, and then are transferred to the cooling reaction section for reacting with the incompletely reacted carbon and added gasification agent; the crude synthesis gas and the fly ash are cooled and purified to remove the fly ash, and the clean low-temperature crude synthesis gas is transferred to subsequent processes. The method avoids ash blocking at an ash outlet in an upstream air-exhaust method, and also avoids overheating at the top in a downstream air-exhaust method, thus improving the carbon conversion rate.

Abstract translation: 一种含碳物质干粉气化装置和方法，该装置从下到上包括下部冷却和净化部分（1），气化反应部分（2），冷却反应部分（3）和上部冷却和净化部分（ 4）; 初始冷却装置设置在冷却反应段和气化反应段之间的连接处; 在气化反应部中沿周向排列有多个喷嘴。 该方法包括：在含碳物质和含氧气化剂之间进行气化反应，生成粗合成气和灰分; 部分粗合成气和大部分灰分下游用于冷却和气化，并且将经冷却并除去灰分的粗合成气转移至随后的工艺中，并且将经骤冷的灰分通过灰出口排​​出; 剩余的粗合成气和粉煤灰上游与冷却物质混合冷却，然后转移到冷却反应区，与未反应不完全的碳和添加的气化剂反应; 粗合成气和飞灰被冷却和纯化以去除飞灰，并且清洁的低温粗合成气被转移到后续工艺中。 该方法避免了采用上游排气方式在出灰口堵灰，也避免了下游排气方式顶部过热，提高了碳转化率。

公开(公告)号：EP3181665A1

公开(公告)日：2017-06-21

申请号：EP16206883.7

申请日：2009-06-25

Applicant: Accordant Energy, LLC

Inventor： BAI, Dingrong ,  CALABRESE, Paula A. , 

IPC: C10L5/40

CPC classification number: C10J3/72 ,  C01B3/02 ,  C10J3/463 ,  C10J2300/0903 ,  C10J2300/0906 ,  C10J2300/0909 ,  C10J2300/0916 ,  C10J2300/092 ,  C10J2300/0946 ,  C10L5/08 ,  C10L5/36 ,  C10L5/363 ,  C10L5/366 ,  C10L5/40 ,  C10L5/403 ,  C10L5/406 ,  C10L5/445 ,  C10L5/46 ,  C10L2200/0469 ,  C10L2250/04 ,  C10L2290/24 ,  C10L2290/28 ,  C10L2290/30 ,  Y02E50/10 ,  Y02E50/30 ,  Y02P20/145

Abstract: Disclosed are novel engineered fuel feed stocks, feed stocks produced by the described processes, and methods of making the fuel feed stocks. Components derived from processed MSW waste streams can be used to make such feed stocks which are substantially free of glass, metals, grit and noncombustibles. These feed stocks are useful for a variety of purposes including as gasification and combustion fuels.

Abstract translation: 公开了新颖的工程燃料原料，通过所描述的工艺生产的原料和制造燃料原料的方法。 衍生于加工垃圾废物流的组分可用于制造基本上不含玻璃，金属，砂砾和不可燃物的此类原料。 这些原料可用于各种用途，包括气化和燃烧燃料。

公开(公告)号：EP2789582B1

公开(公告)日：2017-03-01

申请号：EP13858269.7

申请日：2013-10-10

Applicant: Panasonic Intellectual Property Management Co., Ltd.

Inventor： TAMURA, Yoshio ,  KUSUMURA, Koichi ,  NAKAMURA, Akinari ,  OGURA, Hiroki

IPC: H01M8/0662 ,  C01B3/38 ,  C01B3/36 ,  H01M8/04 ,  H01M8/0612 ,  H01M8/0606 ,  H01M8/04701 ,  C01B3/02

CPC classification number: H01M8/0606 ,  C01B3/02 ,  C01B3/38 ,  C01B2203/0233 ,  C01B2203/0244 ,  C01B2203/025 ,  C01B2203/066 ,  C01B2203/127 ,  C01B2203/148 ,  H01M8/04738 ,  H01M8/0612 ,  H01M8/0675 ,  Y02E60/50

公开(公告)号：EP2953893A4

公开(公告)日：2017-01-25

申请号：EP14779083

申请日：2014-03-12

Applicant: POWERDYNE INC

Inventor： HIRSON GEOFFREY ,  SHOUSE GUS F

IPC: C01B3/00 ,  C01B13/00 ,  C01B32/40 ,  C01B32/50

CPC classification number: C07C1/04 ,  B01J8/02 ,  B01J19/088 ,  B01J2208/00539 ,  B01J2208/00628 ,  B01J2219/0004 ,  B01J2219/00058 ,  B01J2219/00162 ,  B01J2219/00186 ,  B01J2219/0809 ,  B01J2219/0875 ,  B01J2219/0877 ,  C01B3/02 ,  C01B3/042 ,  C01B13/0207 ,  C01B2203/062 ,  C10G2/32 ,  C10G2400/02 ,  C10G2400/04 ,  C10G2400/08 ,  C10G2400/10 ,  Y02E60/324 ,  Y02E60/364 ,  Y02P20/13

Abstract: Systems and methods for fabricating syngas mixtures or fuels are disclosed. A system may include parallel processing chambers, each processing chamber configured to produce one component of a syngas mixture. Each chamber may include at least one plasma torch having a source of a working gas. In one embodiment, a first processing chamber may be optimized to produce hydrogen gas, and a second processing chamber may be optimized to produce carbon monoxide gas. The system may include a mixing component configured to mix the hydrogen gas and the carbon monoxide gas. The system may also include a reaction system to receive the hydrogen gas and the carbon monoxide gas and produce a fuel therefrom. The parallel processing chamber system may be used in methods for producing a syngas mixture or a fuel.

公开(公告)号：EP3080516A1

公开(公告)日：2016-10-19

申请号：EP14869847.5

申请日：2014-11-24

Applicant: Reed, Frank

Inventor： Reed, Frank

IPC: F23G5/027

CPC classification number: C10B53/07 ,  C01B3/02 ,  C10B7/10 ,  C10B21/12 ,  C10B27/06 ,  C10B47/44 ,  C10K3/06 ,  F01K5/02 ,  F23G5/0276 ,  F23G7/12 ,  F23G2201/301 ,  F23G2201/303 ,  F23G2203/8013 ,  F23G2209/281 ,  F23J1/06 ,  Y02P20/143

Abstract: Systems and methods are disclosed for pyrolysis of waste feed material. Some systems include a main retort and a secondary retort. Syngas is produced by pyrolysis in the main retort, and is then mixed with combustion air and ignited, in some cases to produce energy. Carbon char travels to the secondary retort and is exhausted from the system through an airlock.

Abstract translation: 公开了用于废料进料的热解的系统和方法。 一些系统包括主蒸煮器和次蒸馏器。 合成气通过主蒸馏器中的热解产生，然后与燃烧空气混合并点燃，在某些情况下产生能量。 碳炭运送到二级蒸馏器，并通过气闸从系统中排出。