CN204717697U - Industry danger castoff burning smoke treatment recycling residual heat system - Google Patents

Industry danger castoff burning smoke treatment recycling residual heat system Download PDF

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Publication number
CN204717697U
CN204717697U CN201520308635.8U CN201520308635U CN204717697U CN 204717697 U CN204717697 U CN 204717697U CN 201520308635 U CN201520308635 U CN 201520308635U CN 204717697 U CN204717697 U CN 204717697U
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tower
waste
residual heat
heat system
smoke treatment
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沈勇
陈宇
胡昌平
许宏
苏柳燕
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Wuxi City Industrial Waste Safe Disposal Co Ltd
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Wuxi City Industrial Waste Safe Disposal Co Ltd
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Abstract

本实用新型涉及工业危废弃物焚烧处理烟气余热循环利用系统,包括依次连接的上料提升机、回转窑、二次燃烧室、余热锅炉、急冷塔、脱酸塔、布袋除尘器、洗涤塔、烟气加热器、引风机及烟囱;所述回转窑及所述二次燃烧室分别安装有燃气燃烧器,所述急冷塔连接有水循环冷却装置,所述脱酸塔连接有物料投加装置,所述洗涤塔连接有碱液中和处理装置。上料提升机用于固体废物及桶装废物的添加,液体废物直接添加到回转窑中进行多种类废弃物的焚烧,同时余热锅炉用于烟气余热的二次利用,同时脱酸塔及洗涤塔的设置,可提高对废气及废液的处理能力。该系统对危废弃物的处置能力较强,同时可节省能耗,节约处理时间。

The utility model relates to an industrial hazardous waste incineration treatment flue gas waste heat recycling system, comprising a feeding hoist, a rotary kiln, a secondary combustion chamber, a waste heat boiler, a rapid cooling tower, a deacidification tower, a bag dust collector, and a washing tower connected in sequence , flue gas heater, induced draft fan and chimney; the rotary kiln and the secondary combustion chamber are respectively equipped with gas burners, the quench tower is connected with a water circulation cooling device, and the deacidification tower is connected with a material dosing device , the washing tower is connected with a lye neutralization treatment device. The feeding hoist is used to add solid waste and barreled waste, and the liquid waste is directly added to the rotary kiln for incineration of various wastes. At the same time, the waste heat boiler is used for the secondary utilization of the waste heat of the flue gas. The setting of the tower can improve the treatment capacity of waste gas and waste liquid. The system has a strong ability to dispose of hazardous waste, while saving energy consumption and processing time.

Description

工业危废弃物焚烧处理烟气余热循环利用系统Industrial hazardous waste incineration treatment flue gas waste heat recycling system

技术领域 technical field

本实用新型涉及工业危废弃物焚烧处理烟气余热循环利用系统,属于环保技术领域。 The utility model relates to a waste heat recycling system for industrial hazardous waste incineration treatment flue gas, which belongs to the technical field of environmental protection.

背景技术 Background technique

随着国家对危废处置工作的重视以及地区经济建设的快速发展,地区的危险废物处置量不断增多,危废类别复杂,如图1所示,传统技术中主处理工艺是废弃物直接进入焚烧炉中焚烧,产生的废烟气经过二次燃烧室的处理后,再进入喷淋洗涤塔中处理,最后废弃排放,废液进行沉淀处理。这种传统的热解焚烧炉及配套技术相对落后,在焚烧处置废弃物的种类上存在一定的局限性,焚烧化工残渣、污泥、胶状废弃物时能耗高、时间长。 With the country's emphasis on hazardous waste disposal and the rapid development of regional economic construction, the amount of hazardous waste disposed of in the region is increasing, and the types of hazardous waste are complex. As shown in Figure 1, the main treatment process in traditional technology is that waste is directly incinerated Incinerated in the furnace, the waste flue gas produced is treated in the secondary combustion chamber, then enters the spray scrubber for treatment, and finally discards and discharges, and the waste liquid is subjected to precipitation treatment. This traditional pyrolysis incinerator and supporting technology are relatively backward, and there are certain limitations in the types of incineration and disposal of waste. The incineration of chemical residues, sludge, and colloidal waste requires high energy consumption and takes a long time.

实用新型内容 Utility model content

本实用新型的目的在于克服上述现有技术的问题,提供一种工业危废弃物焚烧处理烟气余热循环利用系统,其对危废弃物的处置能力较强,同时可节省能耗,节约处理时间。 The purpose of this utility model is to overcome the above-mentioned problems of the prior art, and provide a waste heat recycling system for industrial hazardous waste incineration, which has a strong ability to dispose of hazardous waste, and can save energy consumption and processing time at the same time .

本实用新型的目的是通过以下技术方案来实现: The purpose of this utility model is to realize through the following technical solutions:

工业废弃物焚烧处理烟气余热循环利用系统,包括依次连接的上料提升机、回转窑、二次燃烧室、余热锅炉、急冷塔、脱酸塔、布袋除尘器、洗涤塔、烟气加热器、引风机及烟囱;所述回转窑及所述二次燃烧室分别安装有燃气燃烧器,所述急冷塔连接有水循环冷却装置,所述脱酸塔连接有物料投加装置,所述洗涤塔连接有碱液中和处理装置。 Industrial waste incineration flue gas waste heat recycling system, including sequentially connected feeding hoist, rotary kiln, secondary combustion chamber, waste heat boiler, quenching tower, deacidification tower, bag filter, washing tower, flue gas heater , induced draft fan and chimney; the rotary kiln and the secondary combustion chamber are respectively equipped with gas burners, the quench tower is connected with a water circulation cooling device, the deacidification tower is connected with a material dosing device, and the washing tower It is connected with lye neutralization treatment device.

上料提升机用于固体废物及桶装废物的添加,液体废物直接添加到回转窑中进行多种类废弃物的焚烧,同时余热锅炉用于烟气余热的二次利用,同时脱酸塔及洗涤塔的设置,可提高对废气及废液的处理能力。该系统对危废弃物的处置能力较强,同时可节省能耗,节约处理时间。 The feeding hoist is used to add solid waste and barreled waste, and the liquid waste is directly added to the rotary kiln for incineration of various wastes. At the same time, the waste heat boiler is used for the secondary utilization of the waste heat of the flue gas. The setting of the tower can improve the treatment capacity of waste gas and waste liquid. The system has a strong ability to dispose of hazardous waste, while saving energy consumption and processing time.

进一步地,所述回转窑分别安装连通有一次风机及冷却风机,用于提供氧气供给。 Further, the rotary kiln is respectively installed and communicated with a primary fan and a cooling fan for providing oxygen supply.

进一步地,所述回转窑还连接有出渣机,用于清理炉渣。 Further, the rotary kiln is also connected with a slag extractor for cleaning the slag.

进一步地,所述二次燃烧室安装连通有二次风机。 Further, the secondary combustion chamber is installed and communicated with a secondary fan.

进一步地,所述水循环冷却装置包括与所述急冷塔的循环出水口连接的冷却塔,所述冷却塔连接水箱,所述水箱连接有冷却水泵,所述冷却水泵与所述急冷塔的循环进水口连通。 Further, the water circulation cooling device includes a cooling tower connected to the circulation outlet of the quenching tower, the cooling tower is connected to a water tank, and the water tank is connected to a cooling water pump, and the cooling water pump is connected to the circulation of the quenching tower. The water port is connected.

进一步地,所述物料投加装置包括活性炭投加装置及消石灰投加装置,所述活性碳投加装置连接有活性炭储仓,所述消石灰投加装置包括消石灰储仓。 Further, the material dosing device includes an activated carbon dosing device and a slaked lime dosing device, the activated carbon dosing device is connected with an activated carbon storage bin, and the slaked lime dosing device includes a slaked lime storage bin.

进一步地,所述活性炭储仓、所述消石灰储仓及所述布袋除尘器分别连通有压缩空气。 Further, the activated carbon storage bin, the slaked lime storage bin and the bag filter are respectively communicated with compressed air.

进一步地,所述碱液中和处理装置包括碱液箱,所述碱液箱连接有碱液泵,所述碱液泵连通所述洗涤塔,所述洗涤塔的出液口连通有储水箱,所述储水箱通过循环泵循环连通至所述洗涤塔。 Further, the lye neutralization treatment device includes an lye tank, the lye tank is connected with a lye pump, the lye pump is connected to the washing tower, and the liquid outlet of the washing tower is connected to a water storage tank , the water storage tank is circulated to the washing tower through a circulation pump.

进一步地,所述急冷塔、所述脱酸塔及所述布袋除尘器设有灰渣出口。 Further, the quench tower, the deacidification tower and the bag filter are provided with ash outlets.

本实用新型所述的工业废弃物焚烧处理烟气余热循环利用系统,包括依次连接的上料提升机、回转窑、二次燃烧室、余热锅炉、急冷塔、脱酸塔、布袋除尘器、洗涤塔、烟气加热器、引风机及烟囱;所述回转窑及所述二次燃烧室分别安装有燃气燃烧器,所述急冷塔连接有水循环冷却装置,所述脱酸塔连接有物料投加装置,所述洗涤塔连接有碱液中和处理装置。上料提升机用于固体废物及桶装废物的添加,液体废物直接添加到回转窑中进行多种类废弃物的焚烧,同时余热锅炉用于烟气余热的二次利用,同时脱酸塔及洗涤塔的设置,可提高对废气及废液的处理能力。该系统对危废弃物的处置能力较强,同时可节省能耗,节约处理时间。 The industrial waste incineration treatment flue gas waste heat recycling system described in the utility model includes a feeding hoist, a rotary kiln, a secondary combustion chamber, a waste heat boiler, a rapid cooling tower, a deacidification tower, a bag filter, and a washing machine connected in sequence. Tower, flue gas heater, induced draft fan and chimney; the rotary kiln and the secondary combustion chamber are respectively equipped with gas burners, the quench tower is connected with a water circulation cooling device, and the deacidification tower is connected with a material feeding device, and the washing tower is connected with a lye neutralization treatment device. The feeding hoist is used to add solid waste and barreled waste, and the liquid waste is directly added to the rotary kiln for incineration of various wastes. At the same time, the waste heat boiler is used for the secondary utilization of the waste heat of the flue gas. The setting of the tower can improve the treatment capacity of waste gas and waste liquid. The system has a strong ability to dispose of hazardous waste, while saving energy consumption and processing time.

附图说明 Description of drawings

图1为传统的的工业废弃物焚烧处理的系统流程结构图; Fig. 1 is a system flow diagram of traditional industrial waste incineration treatment;

图2为本实用新型所述的工业危废弃物焚烧处理烟气余热循环利用系统的系统流程图。 Fig. 2 is a system flow chart of the waste heat recycling system for industrial hazardous waste incineration treatment flue gas according to the utility model.

具体实施方式 Detailed ways

下面根据附图和实施例对本实用新型作进一步详细说明。 The utility model will be described in further detail below according to the accompanying drawings and embodiments.

如图2所示,本实用新型实施例所述的工业废弃物焚烧处理烟气余热循环利用系统,包括依次连接的上料提升机、回转窑、二次燃烧室、余热锅炉、急冷塔、脱酸塔、布袋除尘器、洗涤塔、烟气加热器、引风机及烟囱;回转窑及二次燃烧室分别安装有燃气燃烧器,急冷塔连接有水循环冷却装置,脱酸塔连接有物料投加装置,洗涤塔连接有碱液中和处理装置。 As shown in Figure 2, the industrial waste incineration treatment flue gas waste heat recycling system described in the embodiment of the utility model includes a feeding hoist, a rotary kiln, a secondary combustion chamber, a waste heat boiler, a quenching tower, a degassing Acid tower, bag filter, washing tower, flue gas heater, induced draft fan and chimney; rotary kiln and secondary combustion chamber are respectively equipped with gas burners, quenching tower is connected with water circulation cooling device, and deacidification tower is connected with material feeding device, and the washing tower is connected with a lye neutralization treatment device.

回转窑分别安装连通有一次风机及冷却风机,用于提供氧气供给。回转窑还连接有出渣机,用于清理炉渣。二次燃烧室安装连通有二次风机。 The rotary kiln is respectively installed and communicated with a primary fan and a cooling fan to provide oxygen supply. The rotary kiln is also connected with a slag discharger for cleaning the slag. The secondary combustion chamber is installed and communicated with a secondary fan.

水循环冷却装置包括与急冷塔的循环出水口连接的冷却塔,冷却塔连接水箱,水箱连接有冷却水泵,冷却水泵与急冷塔的循环进水口连通。 The water circulation cooling device includes a cooling tower connected to the circulation outlet of the quenching tower, the cooling tower is connected to a water tank, the water tank is connected to a cooling water pump, and the cooling water pump is communicated with the circulation inlet of the quenching tower.

物料投加装置包括活性炭投加装置及消石灰投加装置,活性碳投加装置连接有活性炭储仓,消石灰投加装置包括消石灰储仓。活性炭储仓、消石灰储仓及布袋除尘器分别连通有压缩空气。 The material dosing device includes an activated carbon dosing device and a slaked lime dosing device, the activated carbon dosing device is connected to an activated carbon storage bin, and the slaked lime dosing device includes a slaked lime storage bin. The activated carbon storage bin, the slaked lime storage bin and the bag filter are respectively connected with compressed air.

碱液中和处理装置包括碱液箱,碱液箱连接有碱液泵,碱液泵连通洗涤塔,洗涤塔的出液口连通有储水箱,储水箱通过循环泵循环连通至洗涤塔。急冷塔、脱酸塔及布袋除尘器设有灰渣出口。 The lye neutralization treatment device includes an lye tank, which is connected with a lye pump, which is connected to a washing tower, and the liquid outlet of the washing tower is connected to a water storage tank, and the water storage tank is circulated to the washing tower through a circulation pump. The quench tower, deacidification tower and bag filter are equipped with ash outlets.

以上所述仅为说明本实用新型的实施方式,并不用于限制本实用新型,对于本领域的技术人员来说,凡在本实用新型的精神和原则之内,所作的任何修改、等同替换、改进等,均应包含在本实用新型的保护范围之内。 The above is only to illustrate the implementation of the utility model, and is not intended to limit the utility model. For those skilled in the art, any modification, equivalent replacement, Improvements and the like should all be included within the protection scope of the present utility model.

Claims (9)

1. industry danger castoff burning smoke treatment recycling residual heat system, it is characterized in that, comprise the charging hoister, rotary kiln, secondary combustion chamber, waste heat boiler, quench tower, extracting tower, sack cleaner, scrubbing tower, flue gas heater, air-introduced machine and the chimney that connect successively; Described rotary kiln and described secondary combustion chamber are separately installed with gas burner, and described quench tower is connected with water circulation cooling device, and described extracting tower is connected with material throwing device, and described scrubbing tower is connected with alkali lye neutralisation treatment device.
2. industry danger castoff burning smoke treatment recycling residual heat system as claimed in claim 1, it is characterized in that, described rotary kiln is installed respectively and is communicated with primary air fan and cooling blower, supplies for providing oxygen.
3. industry danger castoff burning smoke treatment recycling residual heat system as claimed in claim 1, it is characterized in that, described rotary kiln is also connected with mucking machine, for clearing up slag.
4. industry danger castoff burning smoke treatment recycling residual heat system as claimed in claim 1, it is characterized in that, described secondary combustion chamber is installed and is communicated with overfire air fan.
5. industry danger castoff burning smoke treatment recycling residual heat system as claimed in claim 1, it is characterized in that, described water circulation cooling device comprises the cooling tower be connected with the circulating outlet of described quench tower, described cooling tower connects water tank, described water tank is connected with cooling water pump, and described cooling water pump is communicated with the circulation water inlet of described quench tower.
6. industry danger castoff burning smoke treatment recycling residual heat system as claimed in claim 1, it is characterized in that, described material throwing device comprises activated charcoal adding apparatus and calcium hydroxide throwing device, described activated carbon throwing device is connected with active carbon warehouse, and described calcium hydroxide throwing device comprises calcium hydroxide warehouse.
7. industry danger castoff burning smoke treatment recycling residual heat system as claimed in claim 6, it is characterized in that, described active carbon warehouse, described calcium hydroxide warehouse and described sack cleaner are communicated with compressed air respectively.
8. industry danger castoff burning smoke treatment recycling residual heat system as claimed in claim 1, it is characterized in that, described alkali lye neutralisation treatment device comprises lye tank, described lye tank is connected with lye pump, described lye pump is communicated with described scrubbing tower, the liquid outlet of described scrubbing tower is communicated with storage tank, and described storage tank is communicated to described scrubbing tower by circulating pump circulation.
9. industry danger castoff burning smoke treatment recycling residual heat system as claimed in claim 1, it is characterized in that, described quench tower, described extracting tower and described sack cleaner are provided with lime-ash outlet.
CN201520308635.8U 2015-05-14 2015-05-14 Industry danger castoff burning smoke treatment recycling residual heat system Expired - Fee Related CN204717697U (en)

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107120657A (en) * 2017-06-11 2017-09-01 无锡绿麦环保科技有限公司 Solid waste incineration system and its technique
CN107998868A (en) * 2018-01-16 2018-05-08 斐控环境工程(上海)有限公司 A kind of white lime dry-process deacidification technique
CN108662596A (en) * 2018-04-27 2018-10-16 江苏和顺环保有限公司 A kind of low-flash organic solvent and high concentrated organic waste liquid mixed processing method

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107120657A (en) * 2017-06-11 2017-09-01 无锡绿麦环保科技有限公司 Solid waste incineration system and its technique
CN107998868A (en) * 2018-01-16 2018-05-08 斐控环境工程(上海)有限公司 A kind of white lime dry-process deacidification technique
CN108662596A (en) * 2018-04-27 2018-10-16 江苏和顺环保有限公司 A kind of low-flash organic solvent and high concentrated organic waste liquid mixed processing method
CN108662596B (en) * 2018-04-27 2019-12-13 江苏和顺环保有限公司 Mixed treatment method of low-flash-point organic solvent and high-concentration organic waste liquid

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Granted publication date: 20151021