CN202733916U - Burning dregs fluidized bed boiler - Google Patents
Burning dregs fluidized bed boiler Download PDFInfo
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- CN202733916U CN202733916U CN201220402609.8U CN201220402609U CN202733916U CN 202733916 U CN202733916 U CN 202733916U CN 201220402609 U CN201220402609 U CN 201220402609U CN 202733916 U CN202733916 U CN 202733916U
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- flue
- combustion chamber
- chamber
- combustion
- dregs
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- 238000002485 combustion reaction Methods 0.000 claims abstract description 49
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 7
- 239000000428 dust Substances 0.000 claims abstract description 6
- 238000001816 cooling Methods 0.000 claims abstract description 4
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims description 7
- 239000003546 flue gas Substances 0.000 claims description 7
- 238000007599 discharging Methods 0.000 claims 1
- 239000012530 fluid Substances 0.000 claims 1
- 230000010358 mechanical oscillation Effects 0.000 claims 1
- 238000000034 method Methods 0.000 abstract description 6
- 229910000831 Steel Inorganic materials 0.000 abstract description 4
- 239000010959 steel Substances 0.000 abstract description 4
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 abstract description 2
- 229910052799 carbon Inorganic materials 0.000 abstract description 2
- 239000010881 fly ash Substances 0.000 abstract description 2
- 238000005299 abrasion Methods 0.000 abstract 1
- 230000008030 elimination Effects 0.000 abstract 1
- 238000003379 elimination reaction Methods 0.000 abstract 1
- 239000002956 ash Substances 0.000 description 10
- 239000000446 fuel Substances 0.000 description 7
- 239000002893 slag Substances 0.000 description 6
- 239000003814 drug Substances 0.000 description 5
- 229940079593 drug Drugs 0.000 description 4
- 239000010438 granite Substances 0.000 description 3
- 239000003245 coal Substances 0.000 description 2
- 239000003640 drug residue Substances 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 239000002028 Biomass Substances 0.000 description 1
- 240000007594 Oryza sativa Species 0.000 description 1
- 235000007164 Oryza sativa Nutrition 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000010903 husk Substances 0.000 description 1
- 239000003077 lignite Substances 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000003415 peat Substances 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 235000009566 rice Nutrition 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Images
Classifications
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- 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
- Y02E20/00—Combustion technologies with mitigation potential
- Y02E20/34—Indirect CO2mitigation, i.e. by acting on non CO2directly related matters of the process, e.g. pre-heating or heat recovery
Landscapes
- Fluidized-Bed Combustion And Resonant Combustion (AREA)
Abstract
Description
技术领域 technical field
本实用新型涉及一种流化床锅炉,具体讲的是一种以药渣为燃料的燃药渣流化床锅炉。 The utility model relates to a fluidized bed boiler, in particular to a drug slag burning fluidized bed boiler which uses drug slag as fuel.
背景技术 Background technique
现有技术中的流化床锅炉,主要以燃劣质煤(如泥煤、褐煤、煤矸石等)为主的锅炉,也有用于燃稻壳的。国内对于燃煤流化床锅炉技术都较成熟,但对于其他燃料,特别是以药渣为燃料的流化床锅炉目前还没有出现。随着国际和国家一方面对环保的重视,另一方面对开发新能源、可再生能源的提倡,因此锅炉行业需要开发一种高效、环保、节能的新型换代锅炉产品以供应市场需求。 The fluidized bed boilers in the prior art are mainly boilers that burn low-quality coal (such as peat, lignite, coal gangue, etc.), and are also used to burn rice husks. Domestic coal-fired fluidized bed boiler technology is relatively mature, but for other fuels, especially fluidized bed boilers fueled by medicinal residues, there has not yet appeared. With the international and national emphasis on environmental protection on the one hand, and the promotion of the development of new energy and renewable energy on the other hand, the boiler industry needs to develop a new type of boiler product that is efficient, environmentally friendly, and energy-saving to supply market demand.
现有的流化床锅炉的典型结构为燃烧室和传热体为一整体,形成一个较高大的炉型;此炉型既耗料又不便于操作维修;因此急需要开发的一种新的既能以药渣为燃料,又能克服现有流化床锅炉存在的不足的燃药渣的锅炉。 The typical structure of the existing fluidized bed boiler is that the combustion chamber and the heat transfer body are integrated to form a relatively large furnace type; this furnace type is both material-consuming and inconvenient to operate and maintain; therefore, it is urgent to develop a new The utility model relates to a boiler that can use medicine dregs as a fuel and overcome the shortcomings of existing fluidized bed boilers.
实用新型内容 Utility model content
针对上述现有技术存在的不足,本实用新型提供一种燃药渣流化床锅炉,它既能适应药渣燃料的特性,又能克服现有流化床锅炉所存在的不足,达到废物利用、节能环保的目的。 Aiming at the deficiencies of the above-mentioned prior art, the utility model provides a fluidized bed boiler for burning drug residue, which can not only adapt to the characteristics of the fuel of drug residue, but also overcome the existing shortcomings of the existing fluidized bed boiler, and achieve waste utilization , The purpose of energy saving and environmental protection.
本实用新型的技术方案是:一种燃药渣流化床锅炉,包括锅筒、燃烧室、烟道,所述燃烧室、烟道安装在钢架平台上,烟道的上方安装有锅筒,所述烟道内根据烟气流向依次设置有对流管束、省煤器、空气预热器,其特征在于:在所述燃烧室上设有螺旋绞龙给料装置,在所述燃烧室和烟道之间还设置有转向室;燃烧室和转向室内都设置有用于热交换的水冷壁。 The technical scheme of the utility model is: a fluidized bed boiler for burning powder slag, including a drum, a combustion chamber, and a flue. The combustion chamber and the flue are installed on a steel frame platform, and a drum is installed above the flue. , the flue is provided with a convection tube bundle, an economizer, and an air preheater in sequence according to the flue gas flow direction, and it is characterized in that: an auger feeding device is provided on the combustion chamber, There is also a turning chamber between the channels; both the combustion chamber and the turning chamber are equipped with water-cooled walls for heat exchange.
所述燃烧室内底部的流化床炉排下面设有一次风管,燃烧室中部设置二次风管。 A primary air duct is provided under the fluidized bed grate at the bottom of the combustion chamber, and a secondary air duct is provided in the middle of the combustion chamber.
所述燃烧室、转向室及烟道底部都设有出灰装置。 The combustion chamber, the steering chamber and the bottom of the flue are all equipped with ash discharge devices.
所述烟道的尾部设置有麻石水膜除尘器。 The tail of the flue is provided with a granite water film dust collector.
所述对流管束上设计有机械振动除灰装置。 A mechanical vibration ash removal device is designed on the convection tube bundle.
本实用新型的优点:①设计合理,在众多的锅炉设计经验的基础上,专门针对药渣含水率高的特点进行设计,采取流化床燃烧和燃烬室及烟道式对流段组合方案,各部分热量计算分配合理,热利用率高;②给料方式采用特制螺旋绞龙,变节距、变叶片角度螺旋绞龙在输送过程中料的体积逐渐变大、松疏,压力变小,有效防止给料阻塞;③配合二次风分级燃烧,采用流化床炉膛+燃烬室双燃烧室结构,保证将飞灰粒子含碳燃烬;④炉气入口段即转向室设计空间大,烟气流速低,形成自然沉降段,达到防磨和除尘两个目的;⑤排灰采用水冷螺旋绞龙连续出灰,除灰过程中密封不泄漏,环境好;⑥锅炉蒸发对流管均设计有机械振打除灰装置,保证受热面传热效率,同时保证了锅炉热效率。 The advantages of the utility model: ① The design is reasonable. On the basis of numerous boiler design experiences, it is specially designed for the characteristics of high moisture content of the dregs, and adopts the combination scheme of fluidized bed combustion, ember chamber and flue type convection section, The heat calculation and distribution of each part is reasonable, and the heat utilization rate is high; ②The feeding method adopts a special screw auger, and the screw auger with variable pitch and blade angle gradually becomes larger and looser during the conveying process, and the pressure becomes smaller, effectively To prevent feeding blockage; ③Combined with the secondary air staged combustion, the double combustion chamber structure of fluidized bed furnace and ember chamber is adopted to ensure that the carbon-containing fly ash particles are burned; The air flow rate is low, forming a natural sedimentation section to achieve the two purposes of anti-wear and dust removal; ⑤The ash discharge adopts a water-cooled screw auger for continuous ash removal, and the seal does not leak during the ash removal process, and the environment is good; ⑥Boiler evaporation and convection pipes are designed with mechanical The rapping ash removal device ensures the heat transfer efficiency of the heating surface and the boiler thermal efficiency at the same time.
附图说明 Description of drawings
图1为本实用新型的结构示意图。 Fig. 1 is the structural representation of the utility model.
具体实施方式 Detailed ways
在图1中,燃药渣流化床锅炉,采取重型炉墙布置,外包钢板,它包括锅筒2、燃烧室3、烟道4,燃烧室3及烟道4安装在钢架平台1上,烟道4的上方安装有锅筒2,烟道4内根据烟气流向依次设置有对流管束5、省煤器6、空气预热器7,省煤器6内的热水进入锅筒2内,在燃烧室3上设有螺旋绞龙给料装置8,在燃烧室3和烟道4之间还设置有转向室9;燃烧室3和转向室9内都设置有用于热交换的水冷壁。燃烧室3内底部的流化床炉排下面设有一次风管10,燃烧室3中部设置二次风管11,一次风和二次风均来自空气预热器7。燃烧室3、转向室9及烟道4底部都设有出灰装置12。烟道4的尾部设置有麻石水膜除尘器。对流管束5上设计有机械振动除灰装置。
In Fig. 1, the fuel-fired slag fluidized bed boiler adopts a heavy-duty furnace wall layout and is covered with steel plates. It includes a drum 2, a combustion chamber 3, and a flue 4. The combustion chamber 3 and the flue 4 are installed on a steel frame platform 1. A drum 2 is installed above the flue 4, and a convection tube bundle 5, an economizer 6, and an air preheater 7 are arranged in the flue 4 in sequence according to the flue gas flow direction, and the hot water in the economizer 6 enters the drum 2 Inside, the auger feeding device 8 is provided on the combustion chamber 3, and a diversion chamber 9 is also provided between the combustion chamber 3 and the flue 4; both the combustion chamber 3 and the diversion chamber 9 are provided with water cooling for heat exchange. wall. A primary air duct 10 is provided below the fluidized bed grate at the inner bottom of the combustion chamber 3 , and a
燃药渣流化床锅炉的工作流程是:生物质和药渣燃料分别从上下两个螺旋绞龙给料装置8进入燃烧室(即炉膛)3中的流化床上进行燃烧,燃料燃烧所产生的高温烟气首先对燃烧室3内布置的水冷壁(即冷却换热面)进行辐射换热,然后经过初步降温的高温烟气进入转向室(也可称燃烬室)9对室内布置的水冷壁进行热交换,这时烟气转向进入烟道4,对烟道4内布置的多组对流管束5进行对流换热,最后低温烟气通过省煤器6和空气预热器7进入麻石水膜除尘器,由引风机抽至烟囱排出。燃料燃烧后所产生的灰渣分别由燃烧室(即炉膛)3、转向室9及烟道4底部的多个出灰装置12排出。 The working process of the fueled drug slag fluidized bed boiler is: biomass and drug slag fuel enter the fluidized bed in the combustion chamber (that is, the furnace) 3 from the upper and lower screw auger feeding devices 8 for combustion, and the combustion of the fuel The generated high-temperature flue gas first performs radiative heat exchange on the water-cooled wall (that is, the cooling heat exchange surface) arranged in the combustion chamber 3, and then the high-temperature flue gas that has been initially cooled enters the steering chamber (also called the ember chamber) 9 pairs of indoor arrangements At this time, the flue gas turns to enter the flue 4, and performs convective heat exchange on the multiple groups of convective tube bundles 5 arranged in the flue 4, and finally the low-temperature flue gas enters through the economizer 6 and the air preheater 7 Granite water film dust collector is drawn to the chimney by the induced draft fan. The ash generated after fuel combustion is respectively discharged from the combustion chamber (ie, the furnace) 3 , the steering chamber 9 and a plurality of ash discharge devices 12 at the bottom of the flue 4 .
Claims (5)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201220402609.8U CN202733916U (en) | 2012-08-15 | 2012-08-15 | Burning dregs fluidized bed boiler |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201220402609.8U CN202733916U (en) | 2012-08-15 | 2012-08-15 | Burning dregs fluidized bed boiler |
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| CN202733916U true CN202733916U (en) | 2013-02-13 |
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| CN201220402609.8U Expired - Fee Related CN202733916U (en) | 2012-08-15 | 2012-08-15 | Burning dregs fluidized bed boiler |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103512029A (en) * | 2013-10-14 | 2014-01-15 | 上海交通大学 | Organic working medium boiler for combustion of coal-fired fluidized bed |
| CN106016970A (en) * | 2016-07-18 | 2016-10-12 | 周伟初 | Drying treatment system used after squeezing of soaked medicine residues |
| CN106765189A (en) * | 2017-01-13 | 2017-05-31 | 安徽未名鼎和环保有限公司 | A kind of environment-friendly type quickly processes garbage apparatus |
-
2012
- 2012-08-15 CN CN201220402609.8U patent/CN202733916U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103512029A (en) * | 2013-10-14 | 2014-01-15 | 上海交通大学 | Organic working medium boiler for combustion of coal-fired fluidized bed |
| CN106016970A (en) * | 2016-07-18 | 2016-10-12 | 周伟初 | Drying treatment system used after squeezing of soaked medicine residues |
| CN106765189A (en) * | 2017-01-13 | 2017-05-31 | 安徽未名鼎和环保有限公司 | A kind of environment-friendly type quickly processes garbage apparatus |
| CN106765189B (en) * | 2017-01-13 | 2018-12-07 | 安徽未名鼎和环保有限公司 | A kind of environment-friendly type quickly handles garbage apparatus |
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| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20130213 Termination date: 20130815 |