CN206793380U - Double layers of sprinkling tower for waste incineration - Google Patents

Double layers of sprinkling tower for waste incineration Download PDF

Info

Publication number
CN206793380U
CN206793380U CN201720563631.3U CN201720563631U CN206793380U CN 206793380 U CN206793380 U CN 206793380U CN 201720563631 U CN201720563631 U CN 201720563631U CN 206793380 U CN206793380 U CN 206793380U
Authority
CN
China
Prior art keywords
flue gas
lye
alkali lye
pump
gas pipe
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
CN201720563631.3U
Other languages
Chinese (zh)
Inventor
崔晓峰
马忠贺
白利涛
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Zhongxin Heshun Environmental Protection Jiangsu Co ltd
Original Assignee
JIANGSU HESHUN ENVIRONMENTAL PROTECTION CO Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by JIANGSU HESHUN ENVIRONMENTAL PROTECTION CO Ltd filed Critical JIANGSU HESHUN ENVIRONMENTAL PROTECTION CO Ltd
Priority to CN201720563631.3U priority Critical patent/CN206793380U/en
Application granted granted Critical
Publication of CN206793380U publication Critical patent/CN206793380U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Treating Waste Gases (AREA)

Abstract

It the utility model is related to a kind of double layers of sprinkling tower for waste incineration, spray column is divided into two layers of spray region, top is alkali lye spraying zone, bottom is running water spraying zone, two regions are connected by air channel, thermal-collecting tube goes out positioned at air inlet, and pass through pipeline communication with flue gas pipe, flue gas pipe is located at tower body top, flue gas pipe top is provided with smoke sampling device, smoke sampling device connecting detection instrument, detector connects controller, flue gas pipe bottom is alkali lye spraying zone, alkali lye atomizer simultaneously and lye pump, air compressor machine is connected, lye pump is connected with alkali lye circulatory pool;Smoke sampling device extracts fume sample after depickling, is sent into detector and detects acid gas in flue gas and smoke content, and controls water pump, lye pump, pneumatics acc power by controller, adjusts running water and alkali lye spray flux.

Description

Double layers of sprinkling tower for waste incineration
Technical field
It the utility model is related to environment protection garbage incineration tower, more particularly to the double layers of sprinkling tower for waste incineration.
Background technology
In waste incineration industry, there are the following problems for existing alkali lye spray column:1) flue dust in alkali liquid washing flue gas, makes Contain a large amount of suspensions, easy plug nozzle and packing area salt crust into alkali lye;2) lye pump can not be according to pollutant concentration in flue gas Alkali lye dosage is adjusted, causes the waste of electric energy;3) defogging effect is bad low with flue-gas temperature, causes chimney to emit white cigarette, influences to feel See.
Utility model content
The applicant is directed to the disadvantages mentioned above of prior art, studied and improved, there is provided a kind of for waste incineration Double layers of sprinkling tower.
In order to solve the above problems, the utility model uses following scheme:
A kind of double layers of sprinkling tower for waste incineration, spray column are divided into two layers of spray region, and top is alkali lye spraying zone, Bottom is running water spraying zone, and two regions are connected by air channel, and thermal-collecting tube goes out positioned at air inlet, and are led to flue gas pipe Piping connects, and flue gas pipe is located at tower body top, and flue gas pipe top is provided with smoke sampling device, the connection of smoke sampling device Detector, detector connection controller, flue gas pipe bottom is alkali lye spraying zone, alkali lye atomizer simultaneously with lye pump, Air compressor machine is connected, and lye pump is connected with alkali lye circulatory pool;Smoke sampling device extracts fume sample after depickling, is sent into detector and examines Acid gas in flue gas and smoke content are surveyed, and water pump, lye pump, pneumatics acc power are controlled by controller, adjusts running water With alkali lye spray flux.
Further improvement as above-mentioned technical proposal:
Thermal-collecting tube is connected with flue gas pipe by pipeline and circulating pump, filling conduction oil wherein in pipeline.
It is of the present utility model to have technical effect that:
The utility model can automatically adjust running water and the spray column of alkali lye spray flux according to pollutant concentration in flue gas, can Sodium hydroxide concentration and energy consumption are effectively reduced, emits white cigarette prevented also from filler salt crust and chimney;It can be polluted according in exiting flue gas Thing concentration self-control running water and alkali lye spray flux, sour gas and flue dust in flue gas are efficiently removed, inside anti-locking apparatus Salt crust, and collect heat exiting flue gas in air inlet flue gas, prevent chimney from emitting white cigarette and protect in tower facility from high temperature Infringement.
Brief description of the drawings
Fig. 1 is structural representation of the present utility model.
In figure:10th, circulating pump;11st, thermal-collecting tube;12nd, air inlet;13rd, flue gas pipe;14th, alkali lye atomizer;17、 Air channel;19th, alkali lye circulatory pool;2nd, smoke sampling device;21st, water pump;3rd, detector;4th, controller;5th, lye pump;6th, pneumatics Machine.
Embodiment
Specific embodiment of the present utility model is described further below in conjunction with the accompanying drawings.
As shown in figure 1, the double layers of sprinkling tower for waste incineration of the present embodiment, spray column are divided into two layers of spray region, Top is alkali lye spraying zone, and bottom is running water spraying zone, and two regions are connected by air channel 17, and thermal-collecting tube 11 is located at air inlet Mouth 12 goes out, and with flue gas pipe 13 by pipeline communication, flue gas pipe 13 is located at tower body top, the top of flue gas pipe 13 Provided with smoke sampling device 2, the connecting detection instrument 3 of smoke sampling device 2, detector 3 connects controller 4, and the bottom of flue gas pipe 13 is Alkali lye spraying zone, alkali lye atomizer 14 are connected with lye pump 5, air compressor machine 6 simultaneously, and lye pump 5 is connected with alkali lye circulatory pool 19; Smoke sampling device 2 extracts fume sample after depickling, is sent into detector 3 and detects acid gas in flue gas and smoke content, and leads to Cross controller 4 and control water pump 21, lye pump 5, the power of air compressor machine 6, adjust running water and alkali lye spray flux.
Further, thermal-collecting tube 11 is connected with flue gas pipe 13 by pipeline and circulating pump 10, is wherein filled in pipeline Conduction oil.Alkali lye memory block is liquid separatnig plate 15 thereon, and bottom is connected by pipeline with lye pump 5, the outlet of lye pump 5 connection alkali lye Atomizer 14, and mutually converged with compressed air at alkali lye atomizer 14.Alkali lye atomizer 14 is peripheral hardware nozzle, is easy to pacify Dress and maintenance.A kind of alkali lye spray equipment for incineration flue gas processing according to claim 1, it is characterised in that running water Spraying zone sprays flue dust and sour gas in originally water elution flue gas by originally (operating) water nozzle 9, and water outlet is sunk through originally water circulation tank Drop Posterior circle to use, originally water consumption can be reduced.Described smoke sampling device 2 extracts fume sample after depickling, is sent into detector 3 Middle detection acid gas in flue gas and smoke content, and water pump 21, lye pump 5, the power of air compressor machine 6 are controlled by controller 4, adjust Save running water and alkali lye spray flux;When working off one's feeling vent one's spleen 1 acid gas in flue gas and dust concentration is less than a, a unlatching water pump 21, root According to sour gas and the dust concentration regulation power of water pump 21, when sour gas and dust concentration are between a and b, water pump 21 is completely negative Lotus is run, and opens lye pump 5 and air compressor machine 6, and its power is adjusted according to sour gas and dust concentration.Thermal-collecting tube 11 and flue gas Heating tube 13 is connected by pipeline with circulating pump 10, wherein filling conduction oil, thermal-collecting tube 11 collects the heat in the flue gas of air inlet 12 Amount, heat exchange occurs with the flue gas after depickling at flue gas pipe 13, improves the flue-gas temperature of exit 1, it is white to prevent that chimney from emitting Cigarette.
Embodiment provided above is better embodiment of the present utility model, is only used for convenient explanation the utility model, and It is non-to make any formal limitation, any those of ordinary skill in the art to the utility model, if not departing from In the range of the utility model carries technical characteristic, locally change or repair using made by the utility model disclosed technology content The equivalent embodiment of decorations, and without departing from the technical characteristics of the utility model content, still fall within the utility model technical characteristic In the range of.

Claims (2)

  1. A kind of 1. double layers of sprinkling tower for waste incineration, it is characterised in that:Spray column is divided into two layers of spray region, and top is alkali Liquid spraying zone, bottom are running water spraying zone, and two regions are connected by air channel (17), and thermal-collecting tube (11) is located at air inlet (12) go out, and tower body top, flue gas pipe are located at by pipeline communication, flue gas pipe (13) with flue gas pipe (13) (13) top is provided with smoke sampling device (2), smoke sampling device (2) connecting detection instrument (3), and detector (3) connects controller (4), Flue gas pipe (13) bottom is alkali lye spraying zone, alkali lye atomizer (14) while is connected with lye pump (5), air compressor machine (6), Lye pump (5) is connected with alkali lye circulatory pool (19);Smoke sampling device (2) extracts fume sample after depickling, is sent into detector (3) Acid gas in flue gas and smoke content are detected, and water pump (21), lye pump (5), air compressor machine (6) are controlled by controller (4) Power, adjust running water and alkali lye spray flux.
  2. 2. it is used for the double layers of sprinkling tower of waste incineration according to claim 1, it is characterised in that:Thermal-collecting tube (11) adds with flue gas Heat pipe (13) is connected by pipeline with circulating pump (10), filling conduction oil wherein in pipeline.
CN201720563631.3U 2017-05-19 2017-05-19 Double layers of sprinkling tower for waste incineration Expired - Fee Related CN206793380U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201720563631.3U CN206793380U (en) 2017-05-19 2017-05-19 Double layers of sprinkling tower for waste incineration

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201720563631.3U CN206793380U (en) 2017-05-19 2017-05-19 Double layers of sprinkling tower for waste incineration

Publications (1)

Publication Number Publication Date
CN206793380U true CN206793380U (en) 2017-12-26

Family

ID=60741431

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201720563631.3U Expired - Fee Related CN206793380U (en) 2017-05-19 2017-05-19 Double layers of sprinkling tower for waste incineration

Country Status (1)

Country Link
CN (1) CN206793380U (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108744794A (en) * 2018-05-03 2018-11-06 浙江利欧环保科技有限公司 A kind of processing unit and method for distributing flue gas of refuse burning
CN108905572A (en) * 2018-06-05 2018-11-30 江苏和顺环保有限公司 Automatic clear saline solution spray equipment for fume treatment
CN112827330A (en) * 2021-01-08 2021-05-25 深圳市水务科技有限公司 Odor linkage processing method, system and storage medium
CN114383902A (en) * 2021-11-26 2022-04-22 国家能源集团新能源技术研究院有限公司 Tower gas sampling device and tower

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108744794A (en) * 2018-05-03 2018-11-06 浙江利欧环保科技有限公司 A kind of processing unit and method for distributing flue gas of refuse burning
CN108744794B (en) * 2018-05-03 2021-06-15 浙江利欧环保科技有限公司 Treatment device and method for distributed waste incineration flue gas
CN108905572A (en) * 2018-06-05 2018-11-30 江苏和顺环保有限公司 Automatic clear saline solution spray equipment for fume treatment
CN112827330A (en) * 2021-01-08 2021-05-25 深圳市水务科技有限公司 Odor linkage processing method, system and storage medium
CN114383902A (en) * 2021-11-26 2022-04-22 国家能源集团新能源技术研究院有限公司 Tower gas sampling device and tower

Similar Documents

Publication Publication Date Title
CN206793380U (en) Double layers of sprinkling tower for waste incineration
CN205109380U (en) Forced air cooling SOx/NOx control dust removal deodorization environment -friendly device
CN203469768U (en) Novel high-efficiency and energy-saving air treatment device with two-stage spraying and absorbing system for organic waste gas
CN207153427U (en) Waste incinerated smoke purification system
CN106582237A (en) Incineration flue gas purification and cyclic treatment system
CN208302509U (en) Efficiency of waste gas spray column
CN205042354U (en) Waste gas purifying equipment
CN206566746U (en) Water spray vent cabinet
CN109092033A (en) A kind of washing desulfurization integrated device
CN206325383U (en) A kind of decontamination cycle processing system of incineration flue gas
CN206463762U (en) A kind of flue gas recirculation carrying out washing treatment system
CN208449038U (en) A kind of plasmatorch test platform smoke processing system
CN203719244U (en) Mine air return waste heat recovery device
CN207085657U (en) A kind of desulfurizing tower
CN206008449U (en) A kind of desulphurization denitration combined system
CN209393017U (en) A kind of spray equipment handling mercury fume
CN209254433U (en) Absorption tower structure in hydrochloric acid process
CN104941365B (en) Purifier for exhaust gas of industrial boiler
CN203175650U (en) Tail gas treatment device of generator set
CN203715294U (en) Automatic coking, desulfurating and salt-extracting device
CN206762565U (en) One kind welding waste gas treatment equipment
CN203852611U (en) Edible mushroom steam sterilization device
CN208407380U (en) A kind of nanometer of mist generation device
CN207645799U (en) A kind of energy saving bromine production system
CN207922175U (en) Efficient flue gas waste heat utilizes steam boiler

Legal Events

Date Code Title Description
GR01 Patent grant
CP01 Change in the name or title of a patent holder
CP01 Change in the name or title of a patent holder

Address after: 215126 Chengpu Road, Sheng Pu town, Suzhou Industrial Park, Suzhou, Jiangsu 18

Patentee after: Zhongxin Heshun environmental protection (Jiangsu) Co.,Ltd.

Address before: 215126 Chengpu Road, Sheng Pu town, Suzhou Industrial Park, Suzhou, Jiangsu 18

Patentee before: JIANGSU HESHUN ENVIRONMENTAL PROTECTION Co.,Ltd.

CF01 Termination of patent right due to non-payment of annual fee
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20171226