CN205939175U - Organic gas burns device - Google Patents
Organic gas burns device Download PDFInfo
- Publication number
- CN205939175U CN205939175U CN201620871414.6U CN201620871414U CN205939175U CN 205939175 U CN205939175 U CN 205939175U CN 201620871414 U CN201620871414 U CN 201620871414U CN 205939175 U CN205939175 U CN 205939175U
- Authority
- CN
- China
- Prior art keywords
- regenerator
- gas
- organic gas
- air inlet
- burning
- 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.)
- Active
Links
Landscapes
- Incineration Of Waste (AREA)
Abstract
The utility model relates to an environmental protection technology field, saying more specifically relates to an organic gas burns device. It is including the at least a set of unit that burns, it includes incineration chamber to burn the unit, the incineration chamber both sides communicate respectively and are provided with the regenerator, the regenerator is provided with air inlet and gas outlet, the regenerator the air inlet communicates through switching -over device and intake stack, another the regenerator the gas outlet is through sweeping device and exhaust pipe intercommunication, the exhaust pipe other end passes through the switching -over device with regenerator air inlet intercommunication, two the regenerator is admitted air in turn. The utility model provides an organic gas burns device of the cross contamination emission of the gas after not having the gaseous of periodic preliminary treatment and handling.
Description
Technical field
This utility model is related to environmental technology field, in particular, is related to a kind of organic gas incinerator.
Background technology
It is a kind of very effective processing means using burning method process organic exhaust gas, hypertoxic gas, foul gass, it is former
Reason is directly the harmful substance oxidation Decomposition in exhaust gas constituents using hyperpyrexia, and such as Organic substance is oxidized to CO2 and H20.For saving
Burning expense, adopts heat accumulating type incineration method more.
At present, as Chinese patent literature CN203517820U in prior art, a kind of heat accumulating type heating power is provided to burn and light
The waste gas pollution control and treatment system of catalytic control, including a heat accumulating type incineration device, a photocatalyst purification plant；Described heat accumulating type burns
Burn device by heater, oxidizing chamber, regenerator, reversing arrangement and the control system matching form；Heater and oxidation
Room phase is connected in it and provides heat energy, and one end of described regenerator is connected with oxidizing chamber by reversing arrangement, and the other end passes through commutation
Device is connected with waste gas intake stack, regenerator waste gas exhaust duct respectively；The air inlet of photocatalyst purification plant respectively with
Waste gas intake stack, regenerator waste gas exhaust duct are connected, the exhaust outlet of photocatalyst purification plant pass through pipeline successively with draw
Blower fan, air draft chimney are connected.
The heat accumulating type incineration device of above-mentioned patent documentation, using regenerator replace switch mode run, complete gas heating,
Burn the process of purification and accumulation of heat.However, the gas in input pretreatment turns with replacing between the pattern of the gas after discharge process
When changing, the gas of the pretreatment of the residual in the regenerator of preheating therefore can have because being discharged by burning purification
The problem of the gas cross disposal of pollutants after the gas of periodic pretreatment and process.
Utility model content
Therefore, the technical problems to be solved in the utility model is to overcome the incinerator of existing product to have periodically
The gas of pretreatment with process after gas cross-contamination discharge problem, provide and a kind of do not have periodic pretreatment
The organic gas incinerator of the cross-contamination discharge of the gas after gas and process.
For solving the above problems, a kind of organic gas incinerator of the present utility model, burn unit including least one set,
Described burning unit include Burning Room, described Burning Room both sides are provided with and respectively communicated with regenerator, described regenerator be provided with into
QI KOU and gas outlet, the described air inlet of described regenerator is connected with intake stack by reversing arrangement, another described regenerator
Described gas outlet connected with exhaust duct by blow device, the described exhaust duct other end pass through described reversing arrangement and institute
State the connection of regenerator air inlet, two described regenerator replace air inlet.
Wherein, described air inlet is overlapped with described gas outlet and is connected with described reversing arrangement.
Wherein, described burning interior is provided with electric heating assembly.
Wherein, described electric heating assembly is electric radiant tube.
Wherein, described reversing arrangement is reversal valve.
Wherein, described intake stack includes oxygen interface and waste gas interface.
Wherein, described Burning Room is provided with and burns, to described, the nozzle that interior sprays into fuel.
Wherein, described burning unit is two groups and is arranged in parallel.
Wherein, described blow device is purging motor.
Technical solutions of the utility model, have the advantage that：
1. incinerator of the present utility model, the gas of pretreatment passes sequentially through described intake stack, described reversing arrangement
It is passed through described accumulation of heat interior with described air inlet, after described accumulation of heat interior preheating, be passed through the indoor burning of described burning, after process
Gas enter another described accumulation of heat interior fast cooling after, a part passes through described gas outlet, described blow device, described row
Wind pipeline, described reversing arrangement and described air inlet return and pass to described accumulation of heat interior, and another part is after described reversing arrangement
Be expelled in purifier purify or air in.When inputting the gas preheating of pretreatment to described regenerator, there is one
The gas of pretreatment rests on described accumulation of heat interior, before replacing and switch in described regenerator, stops indoor logical to described accumulation of heat
Enter the gas of pretreatment, to the indoor gas returning after logical process of described accumulation of heat, the gas after this process is indoor by described accumulation of heat
The gas of pretreatment purges and burns indoor burning to described, then carries out alternately switching of described regenerator, can avoid remaining in
The gas of the pretreatment in described regenerator because purifying and be discharged by burning, cause the gas of periodic pretreatment with
The problem of the cross-contamination discharge of the gas after process.
2. incinerator of the present utility model, described air inlet is overlapped with described gas outlet setting, it is possible to reduce described storage
The manufacturing cost in hot cell, and described regenerator is few with the position of ft connection, it is possible to reduce the machine of leakage in described regenerator
Rate.
3. adopt electric heating assembly that the gas of pretreatment is heated in this utility model, electric energy more cleans, it is possible to reduce
Environmental pollution.
4. with electric radiant tube the heating of the gas of pretreatment is obtained with high temperature in this utility model, the gas of pretreatment be passed through
There is oxidation reaction in the described oxygen burning interior, mode of heating is simple, easy and simple to handle.
5. the described reversal valve in this utility model disclosure satisfy that use requirement, and the purchase of described reversal valve is more convenient
Extensively.
6., in this utility model, burn, to described, G＆O, the gas of pretreatment and the oxygen that interior is passed through pretreatment
Gas burns indoor fully burning described, so that the Organic substance in the gas of pretreatment is burned and thoroughly decomposes.
7., in this utility model, after described Burning Room starts burning, can select to be continuing with electric heating assembly to pre-
The gas processing heats it is also possible to select to be passed through fuel to described burning interior, the heat that fuel is produced with oxygen combustion is to pre-
The gas heating processing, makes the gas of pretreatment occur oxidation reaction to complete the oxidation of described organic gas, can using fuel
To reduce power consumption, save the burning cost of organic gas.
Brief description
In order to be illustrated more clearly that this utility model specific embodiment or technical scheme of the prior art, below will be right
In specific embodiment or description of the prior art the accompanying drawing of required use be briefly described it should be apparent that, below describe
In accompanying drawing be some embodiments of the present utility model, for those of ordinary skill in the art, do not paying creativeness
On the premise of work, other accompanying drawings can also be obtained according to these accompanying drawings.
Fig. 1 is a kind of structural representation of embodiment of this utility model；
Fig. 2 is the structural representation of this utility model another embodiment；
Description of reference numerals：
1- intake stack；2- waste gas interface；3- oxygen interface；4- reversing arrangement；5- regenerator；6- nozzle；7- electrical heating
Assembly；8- Burning Room；9- blow device；10- exhaust duct；11- air inlet；12- gas outlet.
Specific embodiment
Below in conjunction with accompanying drawing, the technical solution of the utility model is clearly and completely described it is clear that described
Embodiment is a part of embodiment of this utility model, rather than whole embodiments.Based on the embodiment in this utility model, this
The every other embodiment that field those of ordinary skill is obtained under the premise of not making creative work, broadly falls into this practicality
Novel protected scope.
As shown in figure 1, a kind of organic gas incinerator of this utility model one embodiment, including one group of burning unit,
Burn unit and include Burning Room 8, regenerator 5, reversing arrangement 4 and blow device 9.
Burning Room 8 is the main burning place of the gas of pretreatment, and the gas of oxygen and pretreatment occurs in Burning Room 8
Oxidation reaction, the oxidation operation in the gas of pretreatment is decomposed.It is provided with electric heating assembly 7, electric heating assembly in Burning Room 8
7 make the G＆O that the temperature in Burning Room 8 is increased to pretreatment that oxidation reaction, in the present embodiment, electrical heating can occur
Assembly 7 is electric radiant tube.It is additionally provided with the nozzle 6 spraying into fuel into Burning Room 8, Burning Room 8 starts burning, electricity in Burning Room 8
Temperature in Burning Room 8 is increased to heating assembly 7 gas of pretreatment and oxygen can occur oxidation reaction, now to burning
Fuel is sprayed into, fuel and oxygen occur oxidation reaction to discharge substantial amounts of heat, and the heat of release be enough to maintain pretreatment in room 8
When gas occurs oxidation reaction with oxygen, the power of electric heating assembly 7 or the work stopping electric heating assembly 7 can be reduced,
Only maintain heating mode with fuel, the consumption to electric energy can be reduced, save organic gas and burn cost.Electric heating assembly 7 He
The setting number of nozzle 6 can be arranged according to requirements, in the present embodiment, as shown in figure 1, being respectively arranged with 2.
In the present embodiment, can be according to the use condition of organic gas incinerator or the demand of client, using electricity
Heating assembly 7 is to heating in Burning Room 8, or the combination interior heating to Burning Room 8 using electric heating assembly 7 and fuel.As warp
The gas of the pretreatment after Burning Room 8 burning enters in air, can select two ways to heating in Burning Room 8, but to warp
When the gas of the pretreatment after Burning Room 8 burning needs to reclaim, preferably only select to add in Burning Room 8 using electric heating assembly 7
Heat, it is to avoid the flue gas introducing fuel with dioxygen oxidation generation reduces the content reclaiming material, improves organic efficiency.
Regenerator 5 is arranged on the both sides of Burning Room 8 and is connected with Burning Room 8, and regenerator 5 is provided with air inlet 11 and gives vent to anger
Mouth 12, the air inlet 11 of regenerator 5 is connected with intake stack 1 by reversing arrangement 4, and the gas outlet 12 of another regenerator 5 is passed through
Blow device 9 is connected with exhaust duct 10, and exhaust duct 10 other end is connected with regenerator 5 air inlet 11 by reversing arrangement 4,
Replace air inlet between two regenerator 5.Include oxygen interface 3 and waste gas interface 2 on intake stack 1, think that incinerator carries
G＆O for pretreatment.
The present embodiment is with the difference of above-described embodiment, replaces oxygen with air, but, in the air contains substantial amounts of nitrogen
After the gas mixing of gas, air and pretreatment, the concentration of the Organic substance in the gas of the pretreatment in Burning Room 8 can be reduced, go out
The now inadequate thoroughly problem of organic compound combustion, the effect using oxygen is not good.
The present embodiment is with the difference of above-described embodiment, and air inlet 11 is overlapped with gas outlet 12 and connected with reversing arrangement 4
Logical.Such setting, it is possible to reduce the manufacturing cost of regenerator 5, and reduce the position of regenerator 5 and ft connection, can drop
The probability of leakage in low regenerator 5.
In the present embodiment, reversing arrangement 4 uses reversal valve, and blow device 9 uses purging motor.
The present embodiment is with the difference of above-described embodiment, as shown in Fig. 2 burn unit and being two groups and be arranged in parallel, burns
The group number burning unit can set according to use demand.
The flow process that the gas of pretreatment burns is as follows：
The G＆O of pretreatment passes sequentially through intake stack 1, reversing arrangement 4 after mixing at intake stack 1 and enters
QI KOU 11 is passed through in regenerator 5, after preheating, is passed through in Burning Room 8 and burns, the gas after process enters another in regenerator 5
After fast cooling in regenerator 5, a part when needing regenerator 5 is purged, by gas outlet 12, blow device 9, exhaust duct
Road 10, reversing arrangement 4 and air inlet pass to purging in regenerator 5 for 11 times, after another part passes through gas outlet 12 and reversing arrangement 4
It is expelled in purifier purification or air.
Obviously, above-described embodiment is only intended to clearly illustrate example, and the not restriction to embodiment.Right
For those of ordinary skill in the art, can also make on the basis of the above description other multi-forms change or
Change.There is no need to be exhaustive to all of embodiment.And the obvious change thus extended out or
Change among the protection domain created still in this utility model.
Claims (9)
1. a kind of organic gas incinerator, burns unit including least one set, and described burning unit includes Burning Room (8), institute
State Burning Room (8) both sides and be provided with and respectively communicated with regenerator (5) it is characterised in that described regenerator (5) is provided with air inlet
(11) and gas outlet (12), the described air inlet (11) of described regenerator (5) passes through reversing arrangement (4) with intake stack (1) even
Logical, the described gas outlet (12) of another described regenerator (5) is connected with exhaust duct (10) by blow device (9), described row
Wind pipeline (10) other end is connected with described regenerator (5) air inlet (11) by described reversing arrangement (4), two described accumulation of heats
Room (5) replaces air inlet.
2. organic gas incinerator according to claim 1 is it is characterised in that described air inlet (11) is given vent to anger with described
Mouth (12) is overlapped and is connected with described reversing arrangement (4).
3. organic gas incinerator according to claim 1 and 2 is it is characterised in that be provided with electricity in described Burning Room (8)
Heating assembly (7).
4. organic gas incinerator according to claim 3 is it is characterised in that described electric heating assembly (7) is electric spoke
Penetrate pipe.
5. the organic gas incinerator according to claim 1 or 2 or 4 is it is characterised in that described reversing arrangement (4) is
Reversal valve.
6. organic gas incinerator according to claim 5 includes oxygen it is characterised in that described intake stack (1) is upper
Gas interface (3) and waste gas interface (2).
7. the organic gas incinerator according to claim 1 or 2 or 4 or 6 is it is characterised in that on described Burning Room (8)
It is provided with the nozzle (6) spraying into fuel into described Burning Room (8).
8. organic gas incinerator according to claim 7 is it is characterised in that described burning unit is two groups and parallel connection
Setting.
9. the organic gas incinerator according to claim 1 or 2 or 4 or 6 or 8 is it is characterised in that described blow device
(9) it is purging motor.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620871414.6U CN205939175U (en) | 2016-08-11 | 2016-08-11 | Organic gas burns device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620871414.6U CN205939175U (en) | 2016-08-11 | 2016-08-11 | Organic gas burns device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205939175U true CN205939175U (en) | 2017-02-08 |
Family
ID=57920829
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620871414.6U Active CN205939175U (en) | 2016-08-11 | 2016-08-11 | Organic gas burns device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205939175U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107044646A (en) * | 2017-03-24 | 2017-08-15 | 马鞍山市人智能环保科技有限公司 | A kind of liquid waste treatment system and its processing method |
-
2016
- 2016-08-11 CN CN201620871414.6U patent/CN205939175U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107044646A (en) * | 2017-03-24 | 2017-08-15 | 马鞍山市人智能环保科技有限公司 | A kind of liquid waste treatment system and its processing method |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN203501187U (en) | Device for treating waste gas with high-concentration organic pollutants | |
| CN202478779U (en) | System device for treating organic waste gas by adsorption-catalytic combustion | |
| CN208139289U (en) | A kind of organic exhaust gas organic liquid waste collaboration processing heat accumulating type oxidation furnace | |
| CN202868649U (en) | Heat accumulating type catalytic oxidation device | |
| CN104344409A (en) | Method for processing exhaust gas containing high-concentration organic pollutant | |
| CN109966812A (en) | A kind of cement kiln end denitrating flue gas and system, the process of waste heat recycling | |
| CN105757688A (en) | Method and system for treating VOCs gas in sewage treatment plant | |
| CN109631056A (en) | A kind of technique of propylene oxide chlorohydrination tail gas and trichloro ethylene house exhaust combined governance | |
| CN101352639B (en) | Organic waste gas treatment system | |
| CN209985157U (en) | Single-runner system with high-temperature desorption function | |
| CN101435580A (en) | Pressure-accumulating and purifying heat-accumulating incinerator | |
| CN108844085A (en) | A kind of multi-stage heat exchanger point builds formula catalytic oxidation system and its processing method | |
| CN101561145A (en) | External air-removing type heat-storage incinerator | |
| CN203517820U (en) | Waste gas treatment system for regenerative thermal incineration and photocatalyst purification | |
| CN208536008U (en) | Novel heat-storing incinerator | |
| CN110094745B (en) | Energy-saving and emission-reducing method for treating gravure organic waste gas through double channels | |
| CN102519049A (en) | Low energy consumption system for purifying and incinerating harmful gases | |
| CN102072495B (en) | Organic waste gas catalytic combustion device | |
| CN208253609U (en) | A kind of printing machine VOCs concentration paddy electricity balance RTO processing system | |
| CN205939175U (en) | Organic gas burns device | |
| CN221062202U (en) | VOCs exhaust treatment system | |
| CN208687743U (en) | Liquid waste incineration processing unit | |
| CN208504416U (en) | A kind of multi-stage heat exchanger point builds formula catalytic oxidation system | |
| CN106237800A (en) | Volatile organic compounds melting salt oxidation system | |
| CN217843886U (en) | Petrochemical industry minimum discharge exhaust gas treatment system |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant |