CN105674300A - Gaseous pollutant purification treatment system - Google Patents
Gaseous pollutant purification treatment system Download PDFInfo
- Publication number
- CN105674300A CN105674300A CN201410664432.2A CN201410664432A CN105674300A CN 105674300 A CN105674300 A CN 105674300A CN 201410664432 A CN201410664432 A CN 201410664432A CN 105674300 A CN105674300 A CN 105674300A
- Authority
- CN
- China
- Prior art keywords
- combustion chamber
- treatment system
- pipeline
- gaseous pollutant
- waste gas
- 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.)
- Pending
Links
Landscapes
- Chimneys And Flues (AREA)
- Incineration Of Waste (AREA)
Abstract
The invention relates to a gaseous pollutant purification treatment system. The gaseous pollutant purification treatment system mainly comprises a dust remover, an air feeder, a heat preservation layer, a combustion chamber, a ceramic heat storage body and a reverse blowing air feeder. A gas inlet pipeline is arranged at one end of the dust remover, smoke is conveyed into the dust remover through the gas inlet pipeline, and the air feeder is arranged at the other end of the dust remover. Waste gas is guided into the combustion chamber through a pipeline, and the heat preservation layer is arranged on the outermost periphery of the combustion chamber. The ceramic heat storage body is arranged inside the combustion chamber and made of novel ceramic heat storage materials in the prior art. High-temperature gas generated through oxidization flows though the special ceramic heat storage body, and the temperature of the ceramic heat storage body is increased. The reverse blowing air feeder is arranged on one side of the outside of the combustion chamber and connected with the interior of the combustion chamber through a pipeline. A flame arrester is arranged at a gas outlet pipeline of the combustion chamber. The other side of the combustion chamber is connected with a chimney through a pipeline. The waste gas can be drawn away through the reverse blowing air feeder and exhausted into the atmosphere through the chimney. The gaseous pollutant purification treatment system is an organic waste gas treatment system which is simple in process, small in occupied area and low in operation cost, and the gaseous pollutant purification treatment system is low in heat loss and high in heat exchange efficiency.
Description
Technical field
The present invention relates to the technical field of industrial gaseous waste process, it is specifically related to a kind of gaseous pollutant cleaning treatment system.
Background technology
The industrial development of current China is rapid, the harm that industry produces also is expanding day by day, industrial gaseous waste is an important source of nowadays topsoil, industrial gas emission is various to the pollutant kind in air, wherein dust, nitrogen oxide, organic compound, the objectionable impuritiess such as carbide are quite serious to the pollution of air, carbon monoxide in carbide is that carbon burns insufficient formation, its Thorough combustion must be oxidized, not so directly discharge will cause the severe contamination of air, containing a large amount of carbon monoxide in chemical emission, the general mode that all can adopt directly burning, carbon monoxide etc. is oxidized, entering in air, but this kind of mode makes the heat output of carbon monoxide directly be lost, a large amount of energy has been fallen in waste.
Summary of the invention
For the problem existing for the process of chemical emission in prior art, a kind of gaseous pollutant cleaning treatment system provided by the invention, it is possible to realizing the process that chemical emission rationalizes, the saving of the energy utilizes.
In order to realize above-mentioned purpose, the technical solution used in the present invention is as follows:
A kind of gaseous pollutant cleaning treatment system, mainly comprises fly-ash separator, fan, thermal insulation layer, combustion chamber, pottery thermal store, blowback fan.
Described fly-ash separator one end is provided with intake ducting, fly-ash separator is entered by intake ducting supplied flue gases, dust etc. in waste gas can be filtered out by described fly-ash separator, the fly-ash separator the other end is located at by described fan, by pipeline, waste gas is imported in combustion chamber, combustion chamber outermost is provided with thermal insulation layer, combustion chamber is provided with pottery thermal store, pottery thermal store adopts new ceramics heat accumulating of the prior art, in combustion chamber, waste gas can be heated to more than 700 degree, make the fully oxidized carbonic acid gas that resolve into such as the carbon monoxide in waste gas, the high-temperature gas that oxidation produces flows through pottery thermal store, pottery thermal store is heated up, this storage heat is used for the follow-up organic exhaust gas entered of preheating, thus save the materials consumption that waste gas is heated up, the side that described blowback fan is located at outside combustion chamber, connect in combustion chamber by pipeline, another side connects chimney by pipeline, waste gas can be taken away by blowback fan, entered in air by chimney.
Preferably, outlet pipe place, described combustion chamber is provided with spark arrester, after high exhaust temperatures is burnt by described combustion chamber, absorb heat recovery and utilization again, expellant gas temperature is too high, unavoidably leaking out naked light in combustion processes, spark arrester effectively prevent the leakage of flame combustion chamber, has more completely cut off the loss of temperature.
The useful effect of the present invention shows: the present invention is the organic waste gas treatment system that a kind of technique is simple, floor space is little, working cost is low, its efficient heat-exchange system ensure that the efficient recovery of heat output, the cleaning solving tradition storage hot mode such as sweeps at the problem, adopt new ceramics heat-exchange system, making heat exchange efficiency up to 95%, burning, consumption is little does not even need fuel, and system self-adaption is strong, stable operation, the level of automation height of system.
Accompanying drawing explanation
Fig. 1 is the structural representation of a kind of gaseous pollutant cleaning treatment system of the present invention;
1-intake ducting, 2-fly-ash separator, 3-fan, 4-thermal insulation layer, 5-combustion chamber, 6-pottery thermal store, 7-blowback fan, 8-chimney, 9-spark arrester in figure.
Embodiment
For the ease of it is understood by those skilled in the art that the present invention is further illustrated below in conjunction with accompanying drawing 1.
A kind of gaseous pollutant cleaning treatment system according to Fig. 1, mainly comprises fly-ash separator 2, fan 3, thermal insulation layer 4, combustion chamber 5, pottery thermal store 6, blowback fan 7; Described fly-ash separator 2 one end is provided with intake ducting 1, fly-ash separator 2 is entered by intake ducting 1 supplied flue gases, fly-ash separator 2 the other end is located at by described fan 3, combustion chamber 5 below is connected by pipeline, combustion chamber 5 outermost is provided with thermal insulation layer 4, inside, combustion chamber 5 is provided with pottery thermal store 6, pottery thermal store 6 adopts new ceramics heat accumulating of the prior art, the side that described blowback fan 7 is located at outside combustion chamber 5, connect in combustion chamber 5 by pipeline, outlet pipe place, described combustion chamber 5 is provided with spark arrester 9, and another side connects chimney 8 by pipeline.
Workflow: intake ducting is connected in fly-ash separator, the flue dust in waste gas is filtered out by fly-ash separator, by fan, flue gas is taken away in feeding combustion chamber again, waste gas after Thorough combustion, flows through pottery thermal store in combustion chamber, carries out heat exchange and makes heat stored in pottery thermal store, thermal insulation layer it is arranged with outside combustion chamber, prevent calorific loss, finally flow through spark arrester and by reverse fan, waste gas is taken away again, through smoke stack emission.
Above content is only the structure example to the present invention and explanation; described specific embodiment is made various amendment or supplements or adopt similar mode to substitute by affiliated those skilled in the art; as long as not deviateing the structure of invention or surmounting this scope as defined in the claims, protection scope of the present invention all should be belonged to.
Claims (2)
1. a gaseous pollutant cleaning treatment system, mainly comprises fly-ash separator, fan, thermal insulation layer, combustion chamber, pottery thermal store, blowback fan; It is characterized in that described fly-ash separator one end is provided with intake ducting, fly-ash separator is entered by intake ducting supplied flue gases, dust etc. in waste gas can be filtered out by described fly-ash separator, the fly-ash separator the other end is located at by described fan, by pipeline, waste gas is imported in combustion chamber, combustion chamber outermost is provided with thermal insulation layer, combustion chamber is provided with pottery thermal store, the side that described blowback fan is located at outside combustion chamber, connect in combustion chamber by pipeline, another side connects chimney by pipeline, can be taken away by waste gas by blowback fan, be entered in air by chimney.
2. a kind of gaseous pollutant cleaning treatment system according to claim 1, it is characterised in that outlet pipe place, described combustion chamber is provided with spark arrester.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410664432.2A CN105674300A (en) | 2014-11-19 | 2014-11-19 | Gaseous pollutant purification treatment system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410664432.2A CN105674300A (en) | 2014-11-19 | 2014-11-19 | Gaseous pollutant purification treatment system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN105674300A true CN105674300A (en) | 2016-06-15 |
Family
ID=56945028
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201410664432.2A Pending CN105674300A (en) | 2014-11-19 | 2014-11-19 | Gaseous pollutant purification treatment system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN105674300A (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108980864A (en) * | 2018-07-26 | 2018-12-11 | 吴江市贝灵电机有限公司 | A kind of coating waste gas heat utilization method |
| CN109099444A (en) * | 2018-08-24 | 2018-12-28 | 合肥费舍罗热工装备有限公司 | A kind of vent gas treatment cracker |
| CN112539537A (en) * | 2020-12-08 | 2021-03-23 | 苏州惠林节能材料有限公司 | Heat energy recovery device for novel efficient total heat exchange type fresh air exchange system |
| CN112825695A (en) * | 2021-02-19 | 2021-05-25 | 刘生记 | Carbon dioxide air fertilizer machine |
-
2014
- 2014-11-19 CN CN201410664432.2A patent/CN105674300A/en active Pending
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108980864A (en) * | 2018-07-26 | 2018-12-11 | 吴江市贝灵电机有限公司 | A kind of coating waste gas heat utilization method |
| CN109099444A (en) * | 2018-08-24 | 2018-12-28 | 合肥费舍罗热工装备有限公司 | A kind of vent gas treatment cracker |
| CN112539537A (en) * | 2020-12-08 | 2021-03-23 | 苏州惠林节能材料有限公司 | Heat energy recovery device for novel efficient total heat exchange type fresh air exchange system |
| CN112825695A (en) * | 2021-02-19 | 2021-05-25 | 刘生记 | Carbon dioxide air fertilizer machine |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN203980300U (en) | Adopt the off-gas oxidizing device of heat exchanger tube | |
| CN105674300A (en) | Gaseous pollutant purification treatment system | |
| CN108036665A (en) | Carbon baking furnace flue gas pollutant thermal accumulating incinerator and its processing method | |
| CN103331026A (en) | Automatic inertia type spray drying system | |
| CN201517894U (en) | Industrial furnace combustion smoke waste heat recycling system suitable for fuel oil work conditions | |
| CN209279177U (en) | A kind of heat accumulating type Catalytic oxidation furnace | |
| CN107702107A (en) | A kind of waste incinerator and Large-scale fire-electricity unit fume side coupled system | |
| CN204943508U (en) | A kind of rotary accumulation of heat incinerator | |
| CN201517893U (en) | Industrial furnace combustion smoke waste heat recycling system suitable for fuel gas work conditions | |
| CN209840118U (en) | Energy-conserving RTO heat accumulation formula burns burning furnace | |
| CN204114968U (en) | A kind of gaseous contaminant cleaning treatment system | |
| CN103994449B (en) | A kind of compound emission-control equipment | |
| CN103453751A (en) | High heat waste gas energy source utilization system | |
| CN203431936U (en) | Furnace with secondary combustion chamber | |
| CN104595912A (en) | Heat accumulating type high-temperature oxidation treatment device | |
| CN201437987U (en) | Waste gas incinerator | |
| CN211450931U (en) | Flameless energy-saving heat accumulating type incinerator system | |
| CN205192263U (en) | Smelting furnace waste heat recovery system for aluminum ingot production | |
| CN201209854Y (en) | Thermal storage type oxygen-enriched combustion apparatus | |
| CN208091280U (en) | Carbon baking furnace flue gas pollutant thermal accumulating incinerator | |
| CN204678354U (en) | A kind of heat-accumulating type high-temperature oxidation treatment device | |
| CN2926824Y (en) | Smokeless secondary combustion environment-friendly energy-saving hot blast stove | |
| CN201396750Y (en) | Boiler fume-recycling energy-saving emission-reducing system | |
| CN206905011U (en) | Low NOx afterburnings, the efficient eliminating equipments of VOC based on RTO equipment | |
| CN201155799Y (en) | Plaster board organic heat carrier heating stove residual heat utilization device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| WD01 | Invention patent application deemed withdrawn after publication | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20160615 |