CN206803186U - Industrial refuse and incineration fume treatment optimizes device - Google Patents
Industrial refuse and incineration fume treatment optimizes device Download PDFInfo
- Publication number
- CN206803186U CN206803186U CN201720597254.5U CN201720597254U CN206803186U CN 206803186 U CN206803186 U CN 206803186U CN 201720597254 U CN201720597254 U CN 201720597254U CN 206803186 U CN206803186 U CN 206803186U
- Authority
- CN
- China
- Prior art keywords
- cloth bag
- heat exchanger
- chuck
- waste heat
- heat boiler
- 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
Links
Abstract
It the utility model is related to a kind of industrial refuse and incineration fume treatment optimization device, including pyrolysis oven, dual firing chamber, smoke processing system and the heat exchanger being sequentially connected, the smoke processing system includes waste heat boiler, chilling tower, neutralizing tower, cloth bag pulse dust collector, chemical spray tower and the chimney being sequentially connected, the steam outlet of the waste heat boiler is connected by jet chimney with heat exchanger, chuck is provided with the heat exchanger, the chuck connection compressed air supply arrangement connection, the port of export of the chuck are connected by pipeline with cloth bag pulse dust collector.The utility model can be solved the problems, such as in industrial refuse and incineration flue gas pulse dust collector cloth bag deashing process because temperature reduction makes moisture in casing and flying dust condensation causes cloth bag paste bag, extension cloth bag service life, reduction cloth bag replacing production cost；Using waste heat boiler heat, by heat exchanger heated compressed air, so that vapours is utilized caused by waste heat boiler, do not waste.
Description
Technical field
It the utility model is related to the fume treatment dress of industrial refuse processing technology field, more particularly to industrial refuse and incineration
Put.
Background technology
(1) pulsed jet cloth filter is on traditional deduster technical foundation is introduced, and absorbs German deduster technological merit,
With reference to the horizontal high efficiency deduster of the up-to-date technology of the actual national conditions development and production in China.The deduster of this type, set point
The advantages of room blowback and the injection type deduster such as pulse, kinetic energy insufficient strength when overcoming chamber-dividing counter-blowing, pulse jet filtering with
The shortcomings that deashing is carried out simultaneously.Widely applying proves, pulse dust removal technology has high reliability and extremely excellent performance and price
Than；
(2) certain moisture is contained in the industrial solid rubbish burned, and dual firing chamber is sprayed in the liquid solvent and mineral oil fired
Containing substantial amounts of moisture, they enter exhaust treatment system by becoming vapor after burning with incineration flue gas.
(3) pulsed jet cloth filter is used for the dedusting link of incineration flue gas, it is necessary to assure into cloth bag pulse dust collector
Flue-gas temperature maintains 180 DEG C or so, make vapor be not easy to condense in caused on cloth bag cloth bag paste bag；
(4), with the progress of filtering operating mode, the flying dust on filter bag is cumulative, when equipment resistance reaches the Resistance Value of restriction
When, it is necessary to carry out deashing processing to cloth bag, pulsed jet cloth filter increases in filter bag pressure pcl by the injection of compressed air moment,
Flying dust on filter bag is shaken off into ash bucket, discharged by ash exhauster.Because the compression for entering pulsed jet cloth filter is empty
Gas can reduce the temperature in dust-removing box, the moisture in flue gas is easily coagulated together with the flying dust on cloth bag, cause cloth bag
Bag is pasted, shortens the service life of cloth bag.
Utility model content
In consideration of it, the utility model provides a kind of industrial refuse and incineration fume treatment optimization device, sack cleaner deashing
While maintain casing in temperature, eliminate cloth bag paste bag phenomenon, extend cloth bag service life；Waste heat boiler is made full use of to produce
Vapours, it is not necessary to be additionally provided the energy.
In order to solve the above problems, the utility model uses following scheme：
A kind of industrial refuse and incineration fume treatment optimizes device, including pyrolysis oven, dual firing chamber, the fume treatment being sequentially connected
System and heat exchanger, the smoke processing system include be sequentially connected waste heat boiler, chilling tower, neutralizing tower, cloth bag pulse
Deduster, chemical spray tower and chimney, the steam outlet of the waste heat boiler are connected by jet chimney with heat exchanger, institute
State and chuck is provided with heat exchanger, the chuck connection compressed air supply arrangement connection, the port of export of the chuck passes through pipe
Road is connected with cloth bag pulse dust collector.
Further improvement as above-mentioned technical proposal：
Temperature sensor is installed in the chuck and is provided with magnetic valve, the temperature sensor is connected with controller,
The controller controls the open and-shut mode of the magnetic valve according to the temperature signal of temperature sensor.
It is of the present utility model to have technical effect that：
The utility model can be solved in industrial refuse and incineration flue gas pulse dust collector cloth bag deashing process due to casing medium temperature
Degree reduction makes moisture cause cloth bag to paste bag problem with flying dust condensation, extends cloth bag service life, reduces cloth bag and changes production cost；
Using waste heat boiler heat, by heat exchanger heated compressed air, so that vapours is utilized caused by waste heat boiler,
Do not waste；The utility model need not be additionally provided the energy or resource.
Brief description of the drawings
Fig. 1 is structural representation of the present utility model.
In figure：1st, pyrolysis oven；11st, temperature sensor；12nd, controller；2nd, dual firing chamber；3rd, heat exchanger；4th, waste heat boiler；
5th, chilling tower；6th, neutralizing tower；7th, cloth bag pulse dust collector；8th, chemical spray tower；9th, chimney.
Embodiment
Specific embodiment of the present utility model is described further below in conjunction with the accompanying drawings.
As shown in figure 1, the industrial refuse and incineration fume treatment optimization device of the present embodiment, including the pyrolysis oven being sequentially connected
1st, dual firing chamber 2, smoke processing system and heat exchanger 3, smoke processing system include waste heat boiler 4, the chilling tower being sequentially connected
5th, neutralizing tower 6, cloth bag pulse dust collector 7, chemical spray tower 8 and chimney 9, the steam outlet of waste heat boiler 4 pass through steam pipe
Road is connected with heat exchanger 3, and chuck, chuck connection compressed air supply arrangement connection, the outlet of chuck are provided with heat exchanger 3
End is connected by pipeline with cloth bag pulse dust collector 7.
Temperature sensor 11 is installed in chuck and is provided with magnetic valve, temperature sensor 11 is connected with controller 12, control
Device 12 processed controls the open and-shut mode of magnetic valve according to the temperature signal of temperature sensor 11.
Flue gas caused by industrial refuse and incineration comes out temperature from dual firing chamber and can reach 1100 DEG C or so, passes through waste heat boiler 4
600 DEG C or so are reduced to, the heat that waste heat boiler 4 absorbs incineration flue gas produces a large amount of steam, is delivered to by the jet chimney at top
Heat exchanger 3.
Chuck is provided with heat exchanger 3, compressed air is flowed in chuck, and is provided with compressed air inlet and outlet, together
When be provided with steam outlet.The steam heat transmitting and converting that jet chimney conveys to compressed air, is made compression empty by heat exchanger 3
Temperature degree constantly rises.
Temperature sensor 11 is provided with heat exchanger jacket, when compressed air temperature reaches 180 DEG C, compressed air outlet
The pipeline valve at place is opened, and the compressed air after heating enters cloth bag pulse dust collector 7 to cloth bag in dust-removing box by pipeline
On flying dust be blown, the flying dust of injection is discharged into ash bucket.
Using high-temperature steam caused by waste heat boiler 4 by the heated compressed air of heat exchanger 3, make to remove into cloth bag pulse
The compressed air temperature of dirt device 7 is consistent with the temperature in dust-removing box, is caused so as to reduce bag-type dust spin manifold temperature
The flying dust on moisture and cloth bag in flue gas is coagulated together, so as to cause cloth bag to paste bag.Cloth bag is extended in actual production
Service life.
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 industrial refuse and incineration fume treatment optimizes device, it is characterised in that：Including be sequentially connected pyrolysis oven (1), two
Fire room (2), smoke processing system and heat exchanger (3), waste heat boiler (4) that the smoke processing system includes being sequentially connected,
Chilling tower (5), neutralizing tower (6), cloth bag pulse dust collector (7), chemical spray tower (8) and chimney (9), the waste heat boiler (4)
Steam outlet be connected by jet chimney with heat exchanger (3), be provided with chuck, the chuck in the heat exchanger (3)
Compressed air supply arrangement connection is connected, the port of export of the chuck is connected by pipeline with cloth bag pulse dust collector (7).
2. industrial refuse and incineration fume treatment according to claim 1 optimizes device, it is characterised in that：Pacify in the chuck
Equipped with temperature sensor (11) and magnetic valve is provided with, the temperature sensor (11) is connected with controller (12), the control
Device (12) controls the open and-shut mode of the magnetic valve according to the temperature signal of temperature sensor (11).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720597254.5U CN206803186U (en) | 2017-05-26 | 2017-05-26 | Industrial refuse and incineration fume treatment optimizes device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720597254.5U CN206803186U (en) | 2017-05-26 | 2017-05-26 | Industrial refuse and incineration fume treatment optimizes device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206803186U true CN206803186U (en) | 2017-12-26 |
Family
ID=60741889
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720597254.5U Expired - Fee Related CN206803186U (en) | 2017-05-26 | 2017-05-26 | Industrial refuse and incineration fume treatment optimizes device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206803186U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109966900A (en) * | 2019-03-08 | 2019-07-05 | 厦门东江环保科技有限公司 | A kind of flue gas purification system of pyrolysis gasification furnace |
| CN116497167A (en) * | 2023-06-20 | 2023-07-28 | 华北理工大学智能仪器厂 | Blast furnace gas cloth bag dust removing system |
-
2017
- 2017-05-26 CN CN201720597254.5U patent/CN206803186U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109966900A (en) * | 2019-03-08 | 2019-07-05 | 厦门东江环保科技有限公司 | A kind of flue gas purification system of pyrolysis gasification furnace |
| CN109966900B (en) * | 2019-03-08 | 2021-09-03 | 厦门东江环保科技有限公司 | Flue gas purification system of pyrolysis gasifier |
| CN116497167A (en) * | 2023-06-20 | 2023-07-28 | 华北理工大学智能仪器厂 | Blast furnace gas cloth bag dust removing system |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN203938658U (en) | The integrated system of a kind of biomass gas purifying and combustion tail gas residual heat recovery | |
| CN206803186U (en) | Industrial refuse and incineration fume treatment optimizes device | |
| CN110395866A (en) | A kind of sludge at low temperature glows pyrolysis installation | |
| CN208871641U (en) | A kind of adaptive heat accumulating type incineration furnace apparatus of concentration air quantity interlocking | |
| CN101104809B (en) | Coal feeding and coke extracting two-in-one earth station dust removing system for coke oven | |
| CN209431443U (en) | A kind of coal-burning boiler waste-heat recovery device | |
| CN204064005U (en) | Regenerative cycles device in Gas heating furnace high-temperature burns carbon distribution device | |
| CN205991719U (en) | A kind of rotary kiln processes waste gas purification and the residual neat recovering system of mud | |
| CN204593406U (en) | The efficient heat utilization device of a kind of industrial waste gas incineration of liquor | |
| CN201421186Y (en) | High-efficiency energy-saving emission-reducing organic heat carrier boiler of circulating fluidize bed | |
| CN211011443U (en) | Biomass fuel boiler receives dust collector | |
| CN107511030A (en) | A kind of dual firing chamber's formula exhaust treatment system | |
| CN103614509A (en) | Carbon steel converter dry cloth bag dust removal process and device capable of recovering waste heat in whole process | |
| CN107224831A (en) | A kind of spray drying tower waste gas dedusting processing equipment | |
| CN203625414U (en) | Dry cloth-bag dust removal device for carbon steel converter capable of recovering waste heat in whole process | |
| CN104197733B (en) | Regenerative cycles device in Gas heating furnace high-temperature burns carbon distribution device and technique | |
| CN106595041A (en) | Denitration-free biomass/ natural gas double-fuel boiler | |
| CN203758209U (en) | Sealing type hot-blast stove | |
| CN112161505A (en) | High-temperature furnace smoke heat exchange device | |
| CN207085571U (en) | A kind of methanol-to-olefins regenerated flue gas UTILIZATION OF VESIDUAL HEAT IN and dust arrester | |
| CN202328306U (en) | Heat recovery and dust reducing device for boiler smoke | |
| CN204593870U (en) | A kind of biomass boiler | |
| CN206131699U (en) | Use dust collecting equipment in coal drying equipment | |
| CN205014401U (en) | Waste heat, coal tar recovery system for boiler | |
| CN201093179Y (en) | Oil transportation heating furnace air flue waste heat utilization and acquisition air flue dust double-acting vacuum apparatus |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| CP01 | Change in the name or title of a patent holder |
Address after: 215126, Suzhou Industrial Park, Jiangsu, Suzhou Province, 18 Pu Cheng Pu Road Patentee after: Zhongxin Heshun environmental protection (Jiangsu) Co.,Ltd. Address before: 215126, Suzhou Industrial Park, Jiangsu, Suzhou Province, 18 Pu Cheng Pu Road Patentee before: JIANGSU HESHUN ENVIRONMENTAL PROTECTION Co.,Ltd. |
|
| CP01 | Change in the name or title of a patent holder | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20171226 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |