公开(公告)号：US20120228118A1

公开(公告)日：2012-09-13

申请号：US13505507

申请日：2010-11-02

Applicant: Timo Honkola

Inventor： Timo Honkola

IPC: B01D3/36

CPC classification number: D21C11/00 ,  C10B49/16 ,  C10B49/22 ,  D21C11/12 ,  D21C11/125 ,  F23C2900/99008 ,  F23G5/027 ,  F23G7/04 ,  F23G2201/304 ,  Y02E20/346 ,  Y02P70/24

Abstract: The invention relates to a method and equipment for treating pulp mill black liquor so as to recover the energy in chemicals therein. In the invention the black liquor is pyrolysed in a pyrolysis reactor (4), where causticizing material consisting of metal oxide and sodium oxide and heated in a burning unit (6) is conveyed, and gaseous components formed in pyrolysis are conveyed for utilization and solids are returned to the burning unit.

Abstract translation: 本发明涉及一种处理纸浆黑液的方法和设备，以回收其中的化学物质的能量。 在本发明中，黑液在热解反应器（4）中被热解，其中由燃烧单元（6）加热的由金属氧化物和氧化钠组成的苛化材料被输送，并且在热解中形成的气体组分被输送以供利用和固体 返回到燃烧单元。

公开(公告)号：US20120012039A1

公开(公告)日：2012-01-19

申请号：US12837376

申请日：2010-07-15

Applicant: Paolo Palmas ,  Paul Alvin Sechrist ,  Daniel N. Myers ,  Sid Kulprathipanja ,  Stanley Joseph Frey ,  Barry Freel

Inventor： Paolo Palmas ,  Paul Alvin Sechrist ,  Daniel N. Myers ,  Sid Kulprathipanja ,  Stanley Joseph Frey ,  Barry Freel

IPC: F23G5/027 ,  F23G7/00

CPC classification number: C10B23/00 ,  C10B49/22 ,  C10B53/02 ,  C10C5/00 ,  C10K1/026 ,  F23G5/0273 ,  F23G5/30 ,  F23G5/46 ,  F23G5/50 ,  F23G7/10 ,  F23G2201/303 ,  F23G2201/304 ,  F23G2201/601 ,  F23G2206/10 ,  F23G2900/50205 ,  Y02E50/14 ,  Y02P20/133 ,  Y02P20/145 ,  Y02P30/20

Abstract: Char-handling processes for controlling overall heat balance, ash accumulation, and afterburn in a reheater are provided. Carbonaceous biomass feedstock is pyrolyzed using a heat transfer medium forming pyrolysis products and a spent heat transfer medium. The spent heat transfer medium is separated into segregated char and char-depleted spent heat transfer medium. The char-depleted spent heat transfer medium is introduced into a dense bed of heat transfer medium fluidized by a stream of oxygen-containing regeneration gas. All or a portion of the segregated char is combusted in the dense bed using the stream of oxygen-containing regeneration gas. A portion of the segregated char may be exported out of the pyrolysis system to control the overall heat balance and ash accumulation.

Abstract translation: 提供了用于控制再热器中总体热平衡，灰分积累和再燃烧的焦炭处理过程。 碳质生物质原料使用形成热解产物和废热转移介质的传热介质进行热解。 废弃的传热介质被分离成分离的炭和贫乏的传热介质。 将贫乏的废热转移介质引入通过含氧再生气体流流化的传热介质的致密层中。 所有或部分分离的炭在密实床中使用含氧再生气体气流燃烧。 分离的焦炭的一部分可以从热解系统输出以控制总体热平衡和灰分积累。

公开(公告)号：US20110062013A1

公开(公告)日：2011-03-17

申请号：US12919729

申请日：2008-02-27

Applicant: Andreas Tsangaris ,  Mare Bacon

Inventor： Andreas Tsangaris ,  Mare Bacon

IPC: F23G5/027

CPC classification number: F23G5/0276 ,  C10J3/18 ,  C10J3/60 ,  C10J3/721 ,  C10J3/74 ,  C10J3/84 ,  C10J2200/36 ,  C10J2300/094 ,  C10J2300/0956 ,  C10J2300/1238 ,  C10J2300/1634 ,  C10K3/001 ,  F23G5/085 ,  F23G5/165 ,  F23G5/46 ,  F23G5/50 ,  F23G2201/301 ,  F23G2201/304 ,  F23G2202/104 ,  F23J2900/01002

Abstract: A multi-zone carbon converter for converting processed feedstock to syngas and slag is provided comprising a chamber comprising a carbon conversion zone in communication with a slag zone for melting ash into molten slag and/or for maintaining slag in a molten state by the application of plasma heat. The carbon conversion zone and the slag zone are separated by the inter-zonal region that comprises an impediment for restricting or limiting the movement of material between the two zones. The inter-zonal region may also provide for the initial melting of the ash into molten slag by affecting the transfer of plasma heat from the slag zone.

Abstract translation: 提供了一种用于将加工的原料转化为合成气和炉渣的多区碳转化器，其包括一个室，该室包括与炉渣区连通的碳转化区，用于将灰分熔化成熔融炉渣和/或通过施加 等离子体热。 碳转化区和炉渣区由区间区域分开，区域区域包括限制或限制两个区域之间材料运动的障碍物。 区域间区域还可以通过影响来自熔渣区域的等离子体热的传递来提供灰分熔融熔渣的初始熔融。

公开(公告)号：US20110027132A1

公开(公告)日：2011-02-03

申请号：US12921802

申请日：2009-03-18

Applicant: Hisanori Nukumi ,  Toshiyuki Suda ,  Tomoya Muramoto

Inventor： Hisanori Nukumi ,  Toshiyuki Suda ,  Tomoya Muramoto

IPC: F27B15/14

CPC classification number: C10J3/482 ,  C10J2300/0916 ,  C10J2300/093 ,  C10J2300/0946 ,  C10J2300/0976 ,  C10J2300/0993 ,  C10J2300/1637 ,  C10J2300/1807 ,  C10J2300/1853 ,  C10K1/026 ,  F23G5/0276 ,  F23G5/30 ,  F23G7/12 ,  F23G2201/304 ,  F23G2201/40 ,  F23G2203/501 ,  F23G2203/503 ,  F23G2209/281

Abstract: A gasification furnace 2 is divided into a plurality of gasification furnace units 2a and 2b each of which has an inlet 15a, 15b on a lower portion at a longitudinally upstream end in a direction of travel of raw and bed materials and has an outlet 16a, 16b on an upper portion at a longitudinally downstream end in the direction of travel. The outlet 16a is connected to the inlet 15b. The inlet 15a is fed with a raw material and a hot bed material from a materials separator 8. The inlet 15b is also fed with the hot bed material from the material separator 8. The outlet 16b is connected to a combustion furnace 5.

Abstract translation: 气化炉2分为多个气化炉单元2a和2b，每个气化炉单元2a和2b在原料和床料的行进方向上的纵向上游端的下部具有入口15a，15b，并具有出口16a， 16b在行进方向上的纵向下游端的上部。 出口16a连接到入口15b。 入口15a从材料分离器8供给原料和热床材料。入口15b还从材料分离器8送入热床材料。出口16b连接到燃烧炉5。

公开(公告)号：US20110020145A1

公开(公告)日：2011-01-27

申请号：US12934546

申请日：2009-03-11

Applicant: Tomoyuki Katagiri ,  Hisanori Nukumi ,  Kenichiro Kondo

Inventor： Tomoyuki Katagiri ,  Hisanori Nukumi ,  Kenichiro Kondo

IPC: F04F5/44

CPC classification number: C10J3/463 ,  C10J3/728 ,  C10J2300/0976 ,  C10J2300/0993 ,  C10J2300/1637 ,  C10J2300/1807 ,  F23G5/0276 ,  F23G5/30 ,  F23G2201/304 ,  F23G2201/40 ,  F23G2203/501 ,  F23G2203/503 ,  F23G2208/10

Abstract: A fluidized bed gasification furnace has a fluidized bed formed and a freeboard section F above a bed material so as to produce a produced gas by a reaction of raw material with a gasifying agent and take out the produced gas through the freeboard section. Upon shutdown of the furnace, inert gas is fed from below to the furnace for purging of gas in the fluidized bed with inert gas while steam is supplied to a freeboard section above the fluidized bed to purge a gas in the freeboard section with steam.

Abstract translation: 流化床气化炉具有形成的流化床和在床材料上方的干舷部分F，以便通过原料与气化剂的反应产生产生的气体，并通过干舷段取出产生的气体。 关闭炉后，将惰性气体从下方进料到炉中，用惰性气体吹送流化床中的气体，同时将蒸汽供应到流化床上方的干舷部分，以用蒸汽吹扫干舷段中的气体。

公开(公告)号：US20100115961A1

公开(公告)日：2010-05-13

申请号：US12689932

申请日：2010-01-19

Applicant: Chris Chapman ,  David Ovens ,  David Deegan ,  Saeed Ismail

Inventor： Chris Chapman ,  David Ovens ,  David Deegan ,  Saeed Ismail

IPC: F02C3/28 ,  C10B57/00

CPC classification number: F23G5/027 ,  F23G5/006 ,  F23G5/02 ,  F23G5/085 ,  F23G5/30 ,  F23G5/46 ,  F23G2201/303 ,  F23G2201/304 ,  F23G2201/40 ,  F23G2203/50 ,  F23G2204/201 ,  F23G2206/203 ,  F23G2900/50208 ,  Y02E20/12

Abstract: A process for the treatment of waste, the process comprising either a gasification step or a pyrolysis step to produce an offgas and a non-airborne, solid char material; followed by a plasma treatment step. An associated apparatus having a plasma treatment unit which is separate from the gasification unit or pyrolysis unit.

Abstract translation: 用于处理废物的方法，该方法包括气化步骤或热解步骤以产生废气和非空气传播的固体炭材料; 随后进行等离子体处理步骤。 具有与气化单元或热解单元分离的等离子体处理单元的相关装置。

公开(公告)号：US07465372B2

公开(公告)日：2008-12-16

申请号：US10519350

申请日：2002-07-04

Applicant: Kari Sundman ,  Markku Raiko ,  Mika Repka ,  Jari Sutinen

Inventor： Kari Sundman ,  Markku Raiko ,  Mika Repka ,  Jari Sutinen

IPC: D21C11/12

CPC classification number: D21C11/127 ,  D21C11/125 ,  F23G7/04 ,  F23G2201/304 ,  F23G2209/101

Abstract: Method for treatment of spent liquor at a pulp mill, in which method at least a part of the spent liquor flow arriving from the evaporation plant is taken to a pyrolysis reactor, wherein it is pyrolysed at a temperature of 300-800° C. in order to separate evaporable compounds from the coke remaining in a solid state. The pyrolysis products, which are gases or liquids, may be used as fuel or they may be processed further. The coke resulting from the pyrolysis is burnt in a soda recovery boiler or in a gasification reactor to regenerate cooking chemicals. The method is suitable for recovery of chemicals and energy both in sulphate and sulphite processes and also in cooking methods based on organic solvents.

Abstract translation: 在纸浆厂处理废液的方法，其中将从蒸发装置到达的至少一部分废液流送入热解反应器，其中将其在300-800℃的温度下热解， 将可蒸发化合物与残留在固态的焦炭分开。 作为气体或液体的热解产物可以用作燃料，或者可以进一步加工。 由热解产生的焦炭在苏打水回收锅炉或气化反应器中燃烧以再生烹饪化学品。 该方法适用于在硫酸盐和亚硫酸盐过程中以及基于有机溶剂的烹饪方法中回收化学品和能量。

公开(公告)号：US07390337B2

公开(公告)日：2008-06-24

申请号：US11073688

申请日：2005-03-08

Applicant: Norihisa Miyoshi ,  Seiichiro Toyoda ,  Shugo Hosoda ,  Nobutaka Kashima ,  Katsutoshi Naruse ,  Katsuyuki Aoki ,  Shinji Sekikawa ,  Shuichi Nagato ,  Hiroshi Hashimoto

Inventor： Norihisa Miyoshi ,  Seiichiro Toyoda ,  Shugo Hosoda ,  Nobutaka Kashima ,  Katsutoshi Naruse ,  Katsuyuki Aoki ,  Shinji Sekikawa ,  Shuichi Nagato ,  Hiroshi Hashimoto

IPC: B01J8/00 ,  B01J8/18

CPC classification number: C10J3/482 ,  C10J3/54 ,  C10J3/56 ,  C10J2300/0916 ,  C10J2300/0946 ,  C10J2300/095 ,  C10J2300/0956 ,  C10J2300/0996 ,  C10J2300/1215 ,  C10J2300/1628 ,  C10J2300/1634 ,  C10J2300/1637 ,  C10J2300/165 ,  C10J2300/1675 ,  C10J2300/1687 ,  C10J2300/1876 ,  C10J2300/1892 ,  F23G5/0276 ,  F23G5/16 ,  F23G5/30 ,  F23G2201/303 ,  F23G2201/304 ,  F23G2201/40 ,  F23G2202/30 ,  F23G2203/502 ,  F23G2206/202 ,  Y02E20/18 ,  Y02P20/124 ,  Y02P20/129

Abstract: The present invention provides a fuel gasification furnace including a gasification chamber (1) for fluidizing a high-temperature fluidizing medium therein to form a gasification chamber fluidized bed having an interface, and for gasifying a fuel in the gasification chamber fluidized bed, a char combustion chamber (2) for fluidizing a high-temperature fluidizing medium therein to form a char combustion chamber fluidized bed having an interface, and for combusting char generated by gasification in the gasification chamber (1) in the char combustion chamber fluidized bed to heat the fluidizing medium, and a first energy recovery device (109) for using gases generated by the gasification chamber (1) as a fuel. The gasification chamber (1) and the char combustion chamber (2) are integrated with each other. The gasification chamber (1) and the char combustion chamber (2) are divided from each other by a first partition wall (15) for preventing gases from flowing therebetween, and which extends vertically upward from the interfaces of the respective fluidized beds. The first partition wall (15) has a first opening (25) provided in a lower portion thereof, and the first opening (25) serves as a communication between the gasification chamber (1) and the char combustion chamber (2), for allowing the fluidizing medium heated in the char combustion chamber (2) to move from the char combustion chamber (2) via the first opening (25) into the gasification chamber (1).

公开(公告)号：US07318382B2

公开(公告)日：2008-01-15

申请号：US10344242

申请日：2001-06-07

Applicant: Masamoto Kaneko

Inventor： Masamoto Kaneko

IPC: F23G5/02

CPC classification number: F23G5/16 ,  F23G5/0276 ,  F23G5/50 ,  F23G2201/303 ,  F23G2201/304 ,  F23G2202/20 ,  F23G2206/10 ,  F23G2209/281

Abstract: There is provided a method of incinerating a waste material to process incineration residues produced in a gasification furnace easily with existing equipment. A combustible gas generated when a waste material A is dry-distilled in a gasification furnace 1 is introduced into a combustion furnace 3 and combusted therein. The combustible gas is generated in the gasification furnace 1 in order to keep the temperature in the combustion furnace 3 at a temperature capable of melting incineration residues. The incineration residues are charged into the combustion furnace 3 while the combustible gas is being combusted therein, and melted into a melted material B that is discharged from an outlet 3 of the combustion furnace 3 into a receptacle 33 in which the melted material B is solidified. Air supplied to an air jacket 6 and oxygen supplied to the gasification furnace 1 and the combustion furnace 3 are heated by a heat exchange with waste gases from the combustion furnace 3. The heat exchange is carried out by providing a heat exchanger 36 with a conduit 8 disposed therein in a passage of the waste gases from the combustion furnace 4, and passing air or oxygen through the conduit 8 upstream in the passage of the waste gases.

Abstract translation: 提供了一种焚化废物以便在现有设备中容易地处理在气化炉中产生的焚化残渣的方法。 在气化炉1中将废料A干馏时产生的可燃气体引入燃烧炉3并在其中燃烧。 在气化炉1中产生可燃气体，以将燃烧炉3中的温度保持在能够熔化焚烧残渣的温度。 将焚烧残渣装入燃烧炉3中，同时在其中燃烧可燃气体，并熔化成从燃烧炉3的出口3排出的熔融材料B到其中熔化的材料B固化的容器33中 。 供给空气套6的空气和供给到气化炉1和燃烧炉3的氧气通过与来自燃烧炉3的废气的热交换而被加热。热交换通过向热交换器36提供导管 8设置在来自燃烧炉4的废气的通道中，并且使空气或氧气通过导管8在废气通道中的上游。

公开(公告)号：US20070251433A1

公开(公告)日：2007-11-01

申请号：US11393195

申请日：2006-03-30

Applicant: Yuriy Rabiner

Inventor： Yuriy Rabiner

IPC: F23G5/00

CPC classification number: F23G5/006 ,  B09B3/00 ,  C10B47/30 ,  C10B53/00 ,  C10J3/00 ,  C10J3/84 ,  C10J2300/0906 ,  C10J2300/0996 ,  F23G5/027 ,  F23G5/04 ,  F23G5/16 ,  F23G5/46 ,  F23G2201/303 ,  F23G2201/304 ,  F23G2201/602 ,  F23G2201/701 ,  F23G2202/104 ,  F23G2206/10 ,  F23G2900/00001 ,  F23G2900/50205 ,  F23G2900/50401 ,  Y02E20/12 ,  Y02P20/129

Abstract: A municipal or like refuse is crushing, mixing with crushed limestone, dry up in two stages—by hot air and by part of solid products of pyrolysis which other part goes on washing out and filtration. Pyrolysis is carried out in two stages—due to heat of the specified part of solid products of pyrolysis and simultaneous neutralization of allocated hydrogen chloride by limestone with reception of calcium chloride, and then due to heat of final chimney gases of the combustion chamber, where in three stages the washed solid products of pyrolysis preliminary drained by a part of combustion chamber slag are burnt together with liquid and gaseous products of pyrolysis. Gas allocated at pyrolysis condense and divide on organic, which is liquid fuel and water phases. Air after a dryer moves to blowing away of light organic substances from the specified water phase, is heated up due to heat of slag and moves in combustion chamber. Washing water goes on allocation of salts of heavy metals and calcium chloride, and slag after molding of a concrete mixture goes to the chamber of thermohumid processing of the slag concrete by a part of damp chimney gases after drying calcium chloride, other part of gases moves to manufacture of liquid carbon dioxide.

Abstract translation: 市政或类似的垃圾粉碎，与粉碎的石灰石混合，分两个阶段干燥 - 热空气和部分热解固体产物，其他部分进行清洗和过滤。 热分解由两个阶段进行 - 由于特定部分的热解固体产物的热量，并且由接收氯化钙的石灰石同时中和所分配的氯化氢，然后由于燃烧室的最终烟囱气体的热量，其中 在三个阶段中，通过一部分燃烧室炉渣预先排出的经过热分解的洗涤固体产物与热解的液体和气体产物一起燃烧。 在热解过程中分配的气体有机分解，分为液体燃料和水相。 干燥器之后的空气移动以从指定的水相吹走轻质有机物质，由于炉渣的热量而被加热并在燃烧室中移动。 洗涤水分配重金属和氯化钙的盐，混凝土混合物成型后的炉渣在干燥氯化钙后，通过一部分潮湿的烟囱气体进入炉渣混合物的热湿机加工室，其他部分气体移动 制造液态二氧化碳。