CN2585051Y - Rotary hearth type municipal waste pyrolysis gasification incineration treatment device - Google Patents
Rotary hearth type municipal waste pyrolysis gasification incineration treatment device Download PDFInfo
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- CN2585051Y CN2585051Y CN 02261678 CN02261678U CN2585051Y CN 2585051 Y CN2585051 Y CN 2585051Y CN 02261678 CN02261678 CN 02261678 CN 02261678 U CN02261678 U CN 02261678U CN 2585051 Y CN2585051 Y CN 2585051Y
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- incineration treatment
- treatment device
- rotary hearth
- pyrolysis gasification
- hearth type
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- 238000002309 gasification Methods 0.000 title claims abstract description 14
- 238000000197 pyrolysis Methods 0.000 title claims abstract description 14
- 239000002699 waste material Substances 0.000 title claims description 8
- 238000002485 combustion reaction Methods 0.000 claims abstract description 24
- 239000002918 waste heat Substances 0.000 claims abstract description 14
- 239000010813 municipal solid waste Substances 0.000 claims abstract description 9
- 229910000831 Steel Inorganic materials 0.000 claims description 3
- 239000012528 membrane Substances 0.000 claims description 3
- 239000010959 steel Substances 0.000 claims description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 3
- 238000010438 heat treatment Methods 0.000 claims 1
- 238000000034 method Methods 0.000 abstract description 14
- 239000007789 gas Substances 0.000 abstract description 4
- 238000010248 power generation Methods 0.000 abstract description 4
- 230000007613 environmental effect Effects 0.000 abstract description 2
- 230000008676 import Effects 0.000 abstract 1
- 239000000779 smoke Substances 0.000 abstract 1
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 6
- 239000003546 flue gas Substances 0.000 description 6
- 238000004056 waste incineration Methods 0.000 description 4
- 238000010586 diagram Methods 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- HGUFODBRKLSHSI-UHFFFAOYSA-N 2,3,7,8-tetrachloro-dibenzo-p-dioxin Chemical compound O1C2=CC(Cl)=C(Cl)C=C2OC2=C1C=C(Cl)C(Cl)=C2 HGUFODBRKLSHSI-UHFFFAOYSA-N 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 230000005611 electricity Effects 0.000 description 2
- 239000010812 mixed waste Substances 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 239000002574 poison Substances 0.000 description 2
- 231100000614 poison Toxicity 0.000 description 2
- 239000011819 refractory material Substances 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 239000003610 charcoal Substances 0.000 description 1
- 238000011038 discontinuous diafiltration by volume reduction Methods 0.000 description 1
- 239000010791 domestic waste Substances 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 239000002440 industrial waste Substances 0.000 description 1
- 230000004807 localization Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 239000002893 slag Substances 0.000 description 1
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Abstract
Description
所属领域Field
本实用新型回转炉床式城市垃圾热解气化焚烧处理装置涉及环保领域。直接应用于中小城市垃圾焚烧处理及余热发电利用,烟气达标排放。The utility model relates to a rotary hearth type municipal garbage pyrolysis gasification incineration treatment device, which relates to the field of environmental protection. It is directly applied to waste incineration treatment and waste heat power generation utilization in small and medium-sized cities, and the flue gas discharge meets the standard.
背景技术Background technique
从全球范围来说,垃圾焚烧处理已成为城市垃圾减容化、无害化和资源化的主要手段之一,特别是像中国这样一个幅员广大,城市众多的大国,在相当长时期内焚烧处理将作为主要处理技术之一而存在。垃圾焚烧处理装置主要有四种方式:活动炉排焚烧炉;回转式焚烧炉;流化床焚烧炉和气化焚烧炉。From a global perspective, waste incineration has become one of the main means of volume reduction, harmlessness and resource utilization of urban waste. Will exist as one of the main processing technologies. There are four main types of waste incinerators: active grate incinerator; rotary incinerator; fluidized bed incinerator and gasification incinerator.
发明内容Contents of the invention
本实用新型的目的是提供一种适合国情的垃圾焚烧彻底、干净,且可利用余热产生蒸汽发电的、国产化造价低、易于推广应用的垃圾焚烧处理装置。The purpose of the utility model is to provide a waste incineration treatment device which is suitable for the national conditions and can be thoroughly and cleanly incinerated, and can generate steam to generate electricity by using waste heat, which is low in localization cost and easy to popularize and apply.
本实用新型可通过下述技术方案实现:一种回转炉床式城市垃圾热解气化焚烧处理装置,有焚烧装置,特点是:焚烧处理装置由回转窑和余热锅炉构成,回转窑经窄式移动炉排与带有一个垂直布置、长流程二燃室的余热锅炉结合。采用回转窑与余热锅炉的有机配合构成了一个新型的垃圾焚烧处理装置。回转窑中垃圾在欠氧中温条件下逐步完成干燥、热解气化及部分燃烧过程后进入窄式移动炉排和二燃室,窄式移动炉排作为回转窑的后燃烧段和带有一个垂直布置、流程较长的二燃室有机结合。The utility model can be realized through the following technical solutions: a rotary hearth type urban waste pyrolysis gasification incineration treatment device, which has an incineration device, and is characterized in that the incineration treatment device is composed of a rotary kiln and a waste heat boiler. The mobile grate is combined with a waste heat boiler with a vertically arranged, long flow secondary combustion chamber. The organic combination of rotary kiln and waste heat boiler constitutes a new type of waste incineration treatment device. The garbage in the rotary kiln gradually completes the drying, pyrolysis gasification and partial combustion process under the condition of insufficient oxygen and medium temperature, and then enters the narrow mobile grate and the second combustion chamber. The narrow mobile grate is used as the post-combustion section of the rotary kiln and has a The secondary combustion chambers arranged vertically and with a long flow are organically combined.
其中,所述余热锅炉由窄式移动炉排、二燃室、膜式水冷壁、过热器、省煤器、汽包构成,采用角管式结构。Wherein, the waste heat boiler is composed of a narrow moving grate, a secondary combustion chamber, a membrane water wall, a superheater, an economizer, and a steam drum, and adopts an angle tube structure.
所述的回转窑为一种慢速回转的由钢制简体制成的炉窑体,内衬耐火材料层,倾斜式布置,包括垃圾进料斗、推料器、一次风口、窑出口与窄式移动炉排连接。The rotary kiln is a slow-rotating kiln body made of steel, lined with a refractory material layer, and arranged in an inclined manner, including a garbage feeding hopper, a pusher, a primary tuyere, a kiln outlet and a narrow kiln. type mobile grate connection.
本实用新型与常规锅炉不同点是带有一水平布置的窄式移动炉排作为回转窑的后燃烧段和带有一个垂直布置、流程较长的二燃室。在适量热空气的配比下,窑口落下的残渣在炉排上继续燃尽。窑内热解气化产生的可燃气在适量的二次风配比下,在二燃室内充分高温燃尽和热交换,同时使形成的二恶英毒物在此高温区内完全分解。高温烟气依次流过过热器、省煤器,完成热交换过程降温后,从出口烟道排入后续工艺流程,最后清洁烟气从烟囱排入大气。The difference between the utility model and the conventional boiler is that it has a horizontally arranged narrow moving grate as the post-combustion section of the rotary kiln and has a vertically arranged secondary combustion chamber with a long process flow. With an appropriate amount of hot air, the residues falling from the kiln mouth continue to burn out on the grate. The combustible gas produced by pyrolysis and gasification in the kiln is fully combusted and heat-exchanged in the secondary combustion chamber at an appropriate amount of secondary air ratio, and at the same time, the formed dioxin poisons are completely decomposed in this high-temperature zone. The high-temperature flue gas flows through the superheater and the economizer in turn. After the heat exchange process is completed and the temperature is lowered, it is discharged into the subsequent process from the outlet flue, and finally the clean flue gas is discharged into the atmosphere from the chimney.
本实用新型的优越性在于:本装置是根据我国国情开发的新型工艺设备,采用回转炉床结构形式和分级燃烧技术来实现垃圾热解气化、清洁燃烧的工艺过程,工程造价仅相当于进口价格的1/3~1/4,完全适合在我国推广应用。The advantage of the utility model lies in that the device is a new type of process equipment developed according to my country's national conditions, and adopts the structure of the rotary hearth and the staged combustion technology to realize the technological process of pyrolysis gasification and clean combustion of garbage, and the project cost is only equivalent to imported 1/3 to 1/4 of the price, completely suitable for popularization and application in our country.
附图说明Description of drawings
附图1,本实用新型结构示意图。Accompanying drawing 1, the structural representation of the utility model.
附图2,本实用新型工作原理图。Accompanying
具体实施方式:Detailed ways:
如图1本实用新型结构示意图所示,其中,回转窑4为一钢板焊制的筒体,内衬耐火材料,倾斜式布置,慢速回转,城市混合垃圾经垃圾进料斗1,由推料器2推送入窑内,随窑回转搅拌翻动,由一次风口3控制进入风量,在欠氧中温条件下逐步完成干燥、热解气化及部分燃烧过程。窑出口处以炭为主的固体残渣落入后燃烧段的窄式移动炉排5。As shown in Fig. 1, the structural diagram of the utility model, wherein, the rotary kiln 4 is a cylinder body welded by a steel plate, lined with refractory material, arranged in an inclined manner, and rotates at a slow speed. The
窄式移动炉排5、二燃室8、膜式水冷壁9、过热器10、省煤器11、汽包12构成余热锅炉,采用角管式结构。它与常规锅炉不同点是带有一(1×6m)水平布置的窄炉排作为回转窑的后燃烧段和带有一个垂直布置、流程较长的二燃室8。在适量热空气的配比下,窑口落下的残渣在炉排上继续燃尽。窑内热解气化产生的可燃气在适量的二次风7配比下,在二燃室内充分高温燃尽和热交换,同时使形成的二恶英毒物在此高温区内完全分解。高温烟气依次流过过热器10、省煤器11,完成热交换过程降温至200℃左右后,从出口烟道13排入后续工艺流程,最后清洁烟气从烟囱排入大气。Narrow
本实施例装置是根据我国国情开发的新型工艺设备,采用回转炉床结构形式和分级燃烧技术来实现垃圾热解气的余热发电。The device in this embodiment is a new type of process equipment developed according to my country's national conditions. It adopts the rotary hearth structure and staged combustion technology to realize waste heat power generation of waste pyrolysis gas.
应用例,利用本实用新型,可实现垃圾余热发电。其规模及主要参数为:As an application example, the utility model can realize waste heat power generation. Its scale and main parameters are:
垃圾处理生产线:2条Garbage treatment production line: 2
日处理城市混合垃圾:2×150吨/日Daily processing of urban mixed waste: 2×150 tons/day
回转窑:2条,外径3.32米,长15米Rotary kiln: 2, outer diameter 3.32 meters, length 15 meters
锅炉窄式移动炉排:2条,1×6mBoiler narrow mobile grate: 2 pieces, 1×6m
锅炉蒸汽参数:2.5Mpa,350℃Boiler steam parameters: 2.5Mpa, 350°C
蒸发量:2×28吨/小时Evaporation capacity: 2×28 tons/hour
发电功率:2×3000kWGenerating power: 2×3000kW
如图2本实用新型工作原理图所示,先将工业垃圾进行粗选破碎后与生活垃圾一同进入混合垃圾库,从推料器2进入回转窑4,初步燃烧处理后进入余热锅炉的二燃室8和炉排5上,灰渣自出渣机6排出后填埋,蒸汽用于汽轮发电机组发电,对烟气用半干法净化塔净化后经布袋除尘器从出口烟道13排出,对固体灰份进行固化处理。As shown in Fig. 2, the working principle diagram of the utility model, the industrial waste is first roughed and crushed, and then enters the mixed waste storage together with domestic waste, enters the rotary kiln 4 from the
Claims (3)
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 02261678 CN2585051Y (en) | 2002-11-19 | 2002-11-19 | Rotary hearth type municipal waste pyrolysis gasification incineration treatment device |
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| Application Number | Priority Date | Filing Date | Title |
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| CN 02261678 CN2585051Y (en) | 2002-11-19 | 2002-11-19 | Rotary hearth type municipal waste pyrolysis gasification incineration treatment device |
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| CN2585051Y true CN2585051Y (en) | 2003-11-05 |
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Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100458285C (en) * | 2004-03-09 | 2009-02-04 | 江苏正昌集团有限公司 | Process for burning medical refuse |
| CN102425787A (en) * | 2011-12-02 | 2012-04-25 | 沈阳汇丰生物能源发展有限公司 | Liquid slag trapping biomass combustion device and method |
| CN105509065A (en) * | 2015-12-11 | 2016-04-20 | 苏州华周胶带有限公司 | Environment-friendly incineration device of waste garbage |
| CN106705069A (en) * | 2015-11-12 | 2017-05-24 | 衡阳衡锅锅炉有限公司 | Garbage incineration boiler |
| CN107178786A (en) * | 2017-07-03 | 2017-09-19 | 天津市美好生活科技有限公司 | A kind of incinerating method and combinations thereof formula incinerator |
| CN107490008A (en) * | 2017-09-12 | 2017-12-19 | 许志英 | A kind of domestic garbage pyrolysis gasification process of scale |
| CN110440265A (en) * | 2019-08-26 | 2019-11-12 | 同济大学 | A kind of trash burning furnace having hot-fluid tissue |
-
2002
- 2002-11-19 CN CN 02261678 patent/CN2585051Y/en not_active Expired - Fee Related
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100458285C (en) * | 2004-03-09 | 2009-02-04 | 江苏正昌集团有限公司 | Process for burning medical refuse |
| CN102425787A (en) * | 2011-12-02 | 2012-04-25 | 沈阳汇丰生物能源发展有限公司 | Liquid slag trapping biomass combustion device and method |
| CN102425787B (en) * | 2011-12-02 | 2014-05-07 | 沈阳汇丰生物能源发展有限公司 | Liquid slag trapping biomass combustion device and method |
| CN106705069A (en) * | 2015-11-12 | 2017-05-24 | 衡阳衡锅锅炉有限公司 | Garbage incineration boiler |
| CN105509065A (en) * | 2015-12-11 | 2016-04-20 | 苏州华周胶带有限公司 | Environment-friendly incineration device of waste garbage |
| CN107178786A (en) * | 2017-07-03 | 2017-09-19 | 天津市美好生活科技有限公司 | A kind of incinerating method and combinations thereof formula incinerator |
| CN107490008A (en) * | 2017-09-12 | 2017-12-19 | 许志英 | A kind of domestic garbage pyrolysis gasification process of scale |
| CN110440265A (en) * | 2019-08-26 | 2019-11-12 | 同济大学 | A kind of trash burning furnace having hot-fluid tissue |
| CN110440265B (en) * | 2019-08-26 | 2021-07-23 | 同济大学 | A waste burning furnace with heat flow organization |
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| Date | Code | Title | Description |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| ASS | Succession or assignment of patent right |
Owner name: ZHINENG RE-USABLE RESOURCE CO., LTD., DONGGUAN CI Free format text: FORMER OWNER: SHANGHAI KAINENG NEW-TECHNOLOGY ENGINEERING CO., LTD. Effective date: 20061201 |
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| C41 | Transfer of patent application or patent right or utility model | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20061201 Address after: 523961, No. 78, Houjie Avenue, Houjie Town, Guangdong, Dongguan Patentee after: Dongguan Zhi Hui Renewable Resources Power Generation Co., Ltd. Address before: 200233 No. 219, Shanghai, Tianlin Road Patentee before: Shanghai Kaineng New Technology Engineering Co.,Ltd. |
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| C19 | Lapse of patent right due to non-payment of the annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |