WO2008128466A1 - Unité d'élimination de déchets - Google Patents
Unité d'élimination de déchets Download PDFInfo
- Publication number
- WO2008128466A1 WO2008128466A1 PCT/CN2008/070735 CN2008070735W WO2008128466A1 WO 2008128466 A1 WO2008128466 A1 WO 2008128466A1 CN 2008070735 W CN2008070735 W CN 2008070735W WO 2008128466 A1 WO2008128466 A1 WO 2008128466A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- waste
- reaction vessel
- outer casing
- pressure
- steam injection
- Prior art date
Links
- 239000002699 waste material Substances 0.000 title claims abstract description 55
- 238000003756 stirring Methods 0.000 claims abstract description 19
- 238000006243 chemical reaction Methods 0.000 claims description 46
- 238000010793 Steam injection (oil industry) Methods 0.000 claims description 19
- 230000001105 regulatory effect Effects 0.000 claims description 15
- 230000001276 controlling effect Effects 0.000 claims description 7
- 238000001035 drying Methods 0.000 abstract description 10
- 239000000463 material Substances 0.000 abstract description 6
- 239000010865 sewage Substances 0.000 abstract 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 16
- 239000007787 solid Substances 0.000 description 5
- 239000000446 fuel Substances 0.000 description 4
- 230000007613 environmental effect Effects 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 239000002994 raw material Substances 0.000 description 3
- 238000000926 separation method Methods 0.000 description 3
- 230000009286 beneficial effect Effects 0.000 description 2
- 230000018044 dehydration Effects 0.000 description 2
- 238000006297 dehydration reaction Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000003344 environmental pollutant Substances 0.000 description 2
- 239000003337 fertilizer Substances 0.000 description 2
- 239000002920 hazardous waste Substances 0.000 description 2
- 239000002440 industrial waste Substances 0.000 description 2
- 238000002347 injection Methods 0.000 description 2
- 239000007924 injection Substances 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000002906 medical waste Substances 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 231100000719 pollutant Toxicity 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 238000004065 wastewater treatment Methods 0.000 description 2
- 238000013019 agitation Methods 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000001125 extrusion Methods 0.000 description 1
- 239000010794 food waste Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000010806 kitchen waste Substances 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 239000010813 municipal solid waste Substances 0.000 description 1
- 239000010815 organic waste Substances 0.000 description 1
- 239000000123 paper Substances 0.000 description 1
- 238000004321 preservation Methods 0.000 description 1
- 238000000197 pyrolysis Methods 0.000 description 1
- 239000000376 reactant Substances 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 239000002023 wood Substances 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
- B09B—DISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
- B09B3/00—Destroying solid waste or transforming solid waste into something useful or harmless
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
- B09B—DISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
- B09B3/00—Destroying solid waste or transforming solid waste into something useful or harmless
- B09B3/40—Destroying solid waste or transforming solid waste into something useful or harmless involving thermal treatment, e.g. evaporation
- B09B3/45—Steam treatment, e.g. supercritical water gasification or oxidation
-
- C—CHEMISTRY; METALLURGY
- C05—FERTILISERS; MANUFACTURE THEREOF
- C05F—ORGANIC FERTILISERS NOT COVERED BY SUBCLASSES C05B, C05C, e.g. FERTILISERS FROM WASTE OR REFUSE
- C05F9/00—Fertilisers from household or town refuse
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A40/00—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
- Y02A40/10—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in agriculture
- Y02A40/20—Fertilizers of biological origin, e.g. guano or fertilizers made from animal corpses
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/10—Biofuels, e.g. bio-diesel
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel
Definitions
- the present invention relates to a waste disposal apparatus, and more particularly to an organic waste treatment apparatus.
- the technical problem to be solved by the present invention is that, in view of the drawbacks of the prior art fuel manufacturing apparatus that require additional drying equipment, a waste treatment apparatus is provided which does not require additional drying equipment during waste disposal.
- the technical solution adopted by the present invention to solve the technical problems thereof is: constructing a waste treatment device, comprising: a reaction vessel for containing waste for treatment, a stirring device for stirring waste in the reaction vessel, and a reaction port and a discharge port communicating with the reaction vessel, and a pressure regulating device, the waste treatment device further comprising an outer casing, the reaction vessel being located in the outer casing and having a gap therebetween;
- the outer casing and the reaction vessel are respectively provided with a first steam injection port and a second steam injection port.
- the boiler is further included, and the boiler is connected to the first steam injection port and the second steam injection port.
- an exhaust valve is provided in the reaction vessel, and the exhaust valve is connected to an exhaust gas treatment device.
- an exhaust valve is provided on the outer casing.
- the pressure regulating device includes a first exhaust pipe that communicates with a lumen of the outer casing, and is connected to the first exhaust pipe and disposed outside the outer casing The first pressure regulating valve.
- the pressure regulating device further includes a second exhaust pipe communicating with the inner cavity of the reaction kettle, and being connected to the second exhaust pipe and disposed in the a second pressure regulating valve external to the housing.
- the waste treatment apparatus further includes control means for controlling the stirring means, the pressure adjusting means, and the steam injection.
- a pressure gauge and a thermometer connected to the control device are further included.
- Adding an outer casing which can be filled with water vapor between the outer casing and the reaction kettle, can enhance the heating and heat preservation effect of the reaction kettle, and directly dry the reacted substances in the reaction kettle.
- the extruded water has solid particles, which increases the cost of wastewater treatment, but there is no solid-liquid separation in the waste treatment device of the present invention, thereby saving cost;
- FIG. 1 is a schematic view of a waste treatment apparatus of the present invention.
- Fig. 1 is a schematic view of a waste treatment apparatus of the present invention. As shown in FIG.
- the waste treatment apparatus 100 of the present invention comprises: a casing 1; a reaction vessel 2 located inside the casing 1 and having a gap with the casing 1 for containing various wastes for processing; , for stirring the waste in the reaction vessel 2; a steam injection device 4 for injecting water vapor into the outer casing 1 and the reaction vessel 2; and a pressure regulating device 5 for controlling the pressure in the outer casing 1 and the reaction vessel 2; And a control device 6 for controlling the stirring device 3, the water vapor injecting device 4, and the pressure regulating device 5.
- Both the outer casing 1 and the reaction vessel 2 are composed of a pressure-resistant pressure vessel.
- An input port 21 leading to the inside of the reaction vessel 2 is provided above the outer casing 1 for introducing waste into the reaction vessel 2.
- a feeding funnel can be provided on the inlet port 21.
- the steam injection device 4 includes a boiler 41, a first water vapor injection port 42 and a second water vapor injection port 43 which are respectively disposed on the outer casing 1 and the reaction vessel 2.
- the first and second steam injection ports 42, 43 are all connected to the boiler 41.
- the control device 6 individually controls the opening and closing of the boiler 41 and the first and second steam injection ports 42, 43.
- the boiler 41 may be an external portion that is separated from the waste treatment device, and the first and second steam injection ports 42, 43 on the outer casing 1 and the reaction vessel 2 and the boiler are required when water vapor is injected. Connected to 41, you can inject water vapor.
- the control device 6 individually controls the opening and closing of the first and second steam injection ports 42, 43.
- the water vapor pressure in the boiler 41 is constant, and the pressure inside the casing 1 and the reactor 2 is controlled by the amount of steam injected, thereby controlling the internal temperature.
- the stirring device 3 can uniformly pressurize and heat the waste, and includes a rotating shaft 31 disposed inside the reaction vessel 2 in the longitudinal direction, a stirring blade 32 disposed on the rotating shaft 31, and attached to the rotating shaft 31.
- a motor 33 that drives its forward and reverse rotation.
- the motor 33 is provided on the housing 1 or outside the housing 1.
- the agitating blades 32 are inclined with respect to the vertical direction of the horizontal rotating shaft toward the discharge port 22, so that the input waste is conveyed to the discharge port 22 while stirring.
- the motor 33 can be reversed, and the steering and turning time of the motor 33 can be controlled before the waste is converted into a suitable shape.
- the waste reciprocates in the reaction vessel 2.
- the steam injection port 43 of the reaction vessel 2 is located higher than the rotating shaft 31, and when the waste is stirred, it can be contacted with high-pressure steam to improve the treatment efficiency.
- the pressure regulating device 5 includes a first exhaust pipe 51 communicating with the inner cavity of the outer casing 1, a first pressure regulating valve 52 connected to the first exhaust pipe 51 and disposed outside the outer casing 1, if the outer casing 1 and the reaction kettle 2 When the pressure between the two exceeds the predetermined value, the first pressure regulating valve 52 is opened to release the water vapor therein, thereby maintaining the predetermined pressure.
- the pressure regulating device 5 further includes a second exhaust pipe 53 communicating with the inner cavity of the reaction vessel 2, a second pressure regulating valve 54 connected to the second exhaust pipe 53 and disposed outside the outer casing 1. If the pressure inside the reactor 2 exceeds a predetermined value, the second pressure regulating valve 54 is opened to release the water vapor therein, thereby maintaining the predetermined pressure.
- an exhaust valve 23 which can be used to discharge the gas in the chamber and subject the discharged gas to condensation treatment.
- the muffler 24 and the condenser 25 are provided at the outlet of the exhaust valve 23, and if necessary, may be connected to the exhaust gas treatment device for incinerating the discharged gas.
- an exhaust valve, a muffler connected to the exhaust valve, and a condenser are also provided.
- the control unit 6 is electrically connected to the stirring unit 3, the water vapor injecting unit 4, and the pressure adjusting unit 5. By controlling the motor 33 of the stirring device 3, the time and direction of the agitation can be adjusted. By controlling the steam injection device 4, the temperature and pressure between the reaction vessel 2 and the outer casing 1 and the reaction vessel 2 can be adjusted to facilitate the reaction and drying of the waste.
- a pressure gauge and a thermometer are provided on the waste disposal apparatus 100 for sensing the pressure inside the reactor 2 and the pressure and temperature between the outer casing 1 and the reactor 2. Control unit 6 is electrically coupled to the pressure gauge and thermometer to control temperature and pressure.
- the waste treatment apparatus 100 of the present invention has the following characteristics:
- the outer casing 1 is added, and water vapor can be filled between the outer casing 1 and the reaction vessel 2, and the reacted substances in the reaction vessel 2 are directly dried;
- the extruded water has solid particles, which increases the cost of wastewater treatment, but there is no solid-liquid separation in the waste treatment device 100 of the present invention, thereby saving cost;
Landscapes
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Processing Of Solid Wastes (AREA)
- Treatment Of Sludge (AREA)
Abstract
L'invention concerne une unité d'élimination de déchets (100) comprenant une cuve de réaction (2) qui contient des déchets à éliminer, un dispositif d'agitation (3) pour agiter les déchets dans la cuve de réaction (2), une ouverture de réception (21) et une ouverture d'évacuation (22) reliée à la cuve de réaction (2) et un dispositif de réglage de pression (5). L'unité d'élimination de déchets (100) comprend également une enveloppe (1) disposée autour de la cuve de réaction (2), un certain espace étant ménagé entre elles. L'unité d'élimination de déchets (100) est équipée d'une première ouverture d'injection de flux (42) et d'une seconde ouverture d'injection de flux (43) qui sont respectivement situées sur l'enveloppe (1) et la cuve de réaction (2). Les matériaux réactifs placés dans la cuve de réaction (2) sont séchés au moyen du flux injecté entre l'enveloppe (1) et la cuve de réaction (2), un gaz d'échappement étant solidifié sans avoir recours à des équipements de séchage et de déshydratation et de rejet des eaux usées.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2007100740684A CN101288874B (zh) | 2007-04-18 | 2007-04-18 | 废弃物处理装置 |
CN200710074068.4 | 2007-04-18 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2008128466A1 true WO2008128466A1 (fr) | 2008-10-30 |
Family
ID=39875096
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/CN2008/070735 WO2008128466A1 (fr) | 2007-04-18 | 2008-04-17 | Unité d'élimination de déchets |
Country Status (2)
Country | Link |
---|---|
CN (1) | CN101288874B (fr) |
WO (1) | WO2008128466A1 (fr) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107228369A (zh) * | 2016-03-24 | 2017-10-03 | 无锡锡能锅炉有限公司 | 生物质锅炉的料排结构 |
CN107228370A (zh) * | 2016-03-24 | 2017-10-03 | 无锡锡能锅炉有限公司 | 用于生物质锅炉的料排 |
WO2018221215A1 (fr) * | 2017-06-01 | 2018-12-06 | Takase Tech株式会社 | Procédé de production d'un combustible et dispositif de production d'un combustible |
CN113025356A (zh) * | 2021-03-03 | 2021-06-25 | 上海市机电设计研究院有限公司 | 生物质燃料温和热解装置及工艺 |
Families Citing this family (6)
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CN102167491B (zh) * | 2011-01-30 | 2012-12-26 | 北京绿创生态科技有限公司 | 一种污泥处理活化釜 |
CN102615087B (zh) * | 2012-03-15 | 2014-12-10 | 上海泰伍科新能源科技有限公司 | 一种从固体废物中获得高质量固体燃料的方法和设备 |
CN104001708A (zh) * | 2013-02-22 | 2014-08-27 | 聪明太华有限公司 | 由食物垃圾生成碳化固体物及可溶液的方法及其生成装置 |
CN104941986B (zh) * | 2015-06-30 | 2017-08-25 | 华南理工大学 | 一种有机垃圾连续性烘干装置 |
CN106352712A (zh) * | 2016-10-20 | 2017-01-25 | 湖南野森环保科技有限责任公司 | 一种自动化的环保型工业炉 |
CN106520252A (zh) * | 2016-11-25 | 2017-03-22 | 苏州草宝能源科技有限公司 | 一种生活垃圾制作燃料的方法 |
Citations (6)
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CN2241984Y (zh) * | 1994-10-18 | 1996-12-11 | 长春艾达理科技开发有限公司 | 蓄禽废弃物熔炼干燥装置 |
CN2397116Y (zh) * | 1999-07-08 | 2000-09-20 | 邢力 | 一种用废轮胎和或有机废弃物制取烃油的设备 |
JP2003047409A (ja) * | 2001-08-07 | 2003-02-18 | Toshimasa Itakura | 原料加工方法、飼料製造方法、肥料製造方法並びに原料加工装置 |
CN2714184Y (zh) * | 2004-06-23 | 2005-08-03 | 闫振华 | 医疗废弃物无害化处理装置 |
JP2007075659A (ja) * | 2004-03-26 | 2007-03-29 | Nishimuragumi:Kk | 燃料製造装置および燃料製造方法 |
CN201042710Y (zh) * | 2007-05-25 | 2008-04-02 | 无锡市博阳精密机械制造有限公司 | 轴承自动清洗机 |
Family Cites Families (3)
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EP0988900A4 (fr) * | 1998-02-23 | 2006-04-19 | Tlv Co Ltd | Equipement pour traiter par fermentation des dechets organiques |
CN2355824Y (zh) * | 1999-01-22 | 1999-12-29 | 广州企得丰新技术发展有限公司 | 垃圾分解罐 |
CN201042717Y (zh) * | 2007-04-18 | 2008-04-02 | 深圳市环源科技发展有限公司 | 废弃物处理装置 |
-
2007
- 2007-04-18 CN CN2007100740684A patent/CN101288874B/zh active Active
-
2008
- 2008-04-17 WO PCT/CN2008/070735 patent/WO2008128466A1/fr active Application Filing
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
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CN2241984Y (zh) * | 1994-10-18 | 1996-12-11 | 长春艾达理科技开发有限公司 | 蓄禽废弃物熔炼干燥装置 |
CN2397116Y (zh) * | 1999-07-08 | 2000-09-20 | 邢力 | 一种用废轮胎和或有机废弃物制取烃油的设备 |
JP2003047409A (ja) * | 2001-08-07 | 2003-02-18 | Toshimasa Itakura | 原料加工方法、飼料製造方法、肥料製造方法並びに原料加工装置 |
JP2007075659A (ja) * | 2004-03-26 | 2007-03-29 | Nishimuragumi:Kk | 燃料製造装置および燃料製造方法 |
CN2714184Y (zh) * | 2004-06-23 | 2005-08-03 | 闫振华 | 医疗废弃物无害化处理装置 |
CN201042710Y (zh) * | 2007-05-25 | 2008-04-02 | 无锡市博阳精密机械制造有限公司 | 轴承自动清洗机 |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107228369A (zh) * | 2016-03-24 | 2017-10-03 | 无锡锡能锅炉有限公司 | 生物质锅炉的料排结构 |
CN107228370A (zh) * | 2016-03-24 | 2017-10-03 | 无锡锡能锅炉有限公司 | 用于生物质锅炉的料排 |
WO2018221215A1 (fr) * | 2017-06-01 | 2018-12-06 | Takase Tech株式会社 | Procédé de production d'un combustible et dispositif de production d'un combustible |
JP2018203842A (ja) * | 2017-06-01 | 2018-12-27 | Takase Tech株式会社 | 燃料製造方法および燃料製造装置 |
CN113025356A (zh) * | 2021-03-03 | 2021-06-25 | 上海市机电设计研究院有限公司 | 生物质燃料温和热解装置及工艺 |
CN113025356B (zh) * | 2021-03-03 | 2021-12-14 | 上海市机电设计研究院有限公司 | 生物质燃料温和热解装置及工艺 |
Also Published As
Publication number | Publication date |
---|---|
CN101288874B (zh) | 2011-07-20 |
CN101288874A (zh) | 2008-10-22 |
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