CN207356893U - A kind of energy-efficient exhaust gas processor - Google Patents
A kind of energy-efficient exhaust gas processor Download PDFInfo
- Publication number
- CN207356893U CN207356893U CN201721301906.2U CN201721301906U CN207356893U CN 207356893 U CN207356893 U CN 207356893U CN 201721301906 U CN201721301906 U CN 201721301906U CN 207356893 U CN207356893 U CN 207356893U
- Authority
- CN
- China
- Prior art keywords
- heat exchanger
- preheating
- heat
- stage
- high temperature
- 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
- Waste-Gas Treatment And Other Accessory Devices For Furnaces (AREA)
- Treating Waste Gases (AREA)
Abstract
The utility model discloses a kind of energy-efficient exhaust gas processor, including collecting pipe, multi-stage heat exchanger, accumulation of heat high temperature furnace, resisting blower, chimney；The multi-stage heat exchanger is equipped with preheating channel, heat exchanger channels, and the collecting pipe is connected with the preheating entrance of the multi-stage heat exchanger preheating channel, the heat exchange outlet of the chimney and the multi-stage heat exchanger preheating channel；Between the preheating outlet of the multi-stage heat exchanger preheating channel and accumulation of heat high temperature furnace, between the heat exchange outlet of accumulation of heat high temperature furnace and multi-stage heat exchanger heat exchanger channels, pass through preheating pipe respectively, heat exchange pipeline connects；The high-temperature blower is between multi-stage heat exchanger and high temperature furnace；In the case where the resisting blower is pumped, gas passes sequentially through the collecting pipe, the preheating entrance of multi-stage heat exchanger preheating channel, preheating outlet, accumulation of heat high temperature furnace, the heat exchange entrance of multi-stage heat exchanger preheating channel, heat exchange outlet, chimney.
Description
Technical field
It the utility model is related to printing technology field, and in particular, to a kind of organic waste for being used to produce printing
The energy-efficient exhaust gas processor that gas is handled.
Background technology
In printing industry, due to being printed using materials such as organic solvent, film, paper, ink, in process
In, particularly drying course can produce a large amount of organic exhaust gas.To prevent these organic exhaust gas from being polluted to environment, it is obviously desirable to
It could be discharged by exhaust-gas treatment.With the pay attention to day by day that Environmental is protected, the requirement to VOCs treatment is got over
Come higher.It is existing by plasma, active carbon adsorption, RPO ceramics inhale the modes such as heat release processing, inadequate there are treatment effeciency
High, the problems such as degree of purification is not good enough, processing cost is higher.
Utility model content
The purpose of this utility model is to provide a kind of energy-efficient exhaust gas processor, to solve to carry in above-mentioned background technology
The problem of going out.
To achieve the above object, the utility model provides following technical solution：
A kind of energy-efficient exhaust gas processor, including for collect print produce organic exhaust gas collecting pipe, for pair
The multi-stage heat exchanger that low temperature waste gas is preheated, exchanged heat to the high temperature purification gas after processing, carries out organic exhaust gas high
The accumulation of heat high temperature furnace of warm resolution process, for the resisting blower of pumping gas, for the chimney being outwardly vented；The multistage
Heat exchanger is equipped with preheating channel, heat exchanger channels, and the preheating entrance of the collecting pipe and the multi-stage heat exchanger preheating channel connects
It is logical, the heat exchange outlet of the chimney and the multi-stage heat exchanger preheating channel；The multi-stage heat exchanger preheating channel it is pre-
Between heat outlet and accumulation of heat high temperature furnace, between the heat exchange outlet of accumulation of heat high temperature furnace and multi-stage heat exchanger heat exchanger channels, pass through respectively
Preheating pipe, heat exchange pipeline connection；The resisting blower be arranged on chimney and multi-stage heat exchanger heat exchange outlet between pipeline, receive
On pipeline, the preheating pipe and/or heat exchange pipeline between the collecting pipe and multi-stage heat exchanger preheating entrance of collection exhaust gas
One or more；In the case where the resisting blower is pumped, gas passes sequentially through the collecting pipe, multi-stage heat exchanger preheating channel
Preheating entrance, preheating outlet, accumulation of heat high temperature furnace, the heat exchange entrance of multi-stage heat exchanger preheating channel, heat exchange outlet, chimney carries out
Processing.
Here, in the multi-stage heat exchanger, directly using in heat exchange pipeline from accumulation of heat high temperature furnace discharge
High temperature purification gas carries out heat exchange with the low temperature waste gas entered from the collecting pipe in preheating pipe, low temperature waste gas is existed
Temperature increases substantially the operating temperature close to accumulation of heat high temperature furnace in the case of without directly consuming energy, subsequently into accumulation of heat high temperature
Stove carries out pyrolytic, and substantial amounts of heat is produced while decomposition to maintain the high temperature in accumulation of heat high temperature furnace, and after the completion of decomposing
High temperature purification gas arrange to multi-stage heat exchanger；Likewise, multi-stage heat exchanger absorbs the heat of high temperature purification gas by exchanging heat, favorably
In making full use of waste heat, harmful effect of the waste heat to atmospheric environment is prevented.
Overall efficiency is pumped to improve gas, obtains more preferable waste gas purification effect, it is preferred that the resisting blower is set
In on the heat exchange pipeline.
During due to carrying out exhaust-gas treatment, exhaust gas can take away heat, to improve accumulation of heat high temperature furnace accumulation of heat effect, shorten it and reach
The time of predetermined temperature, it is preferred that the collecting pipe is equipped with inlet valve, and the inlet valve is used in system warm-up rank
Section closes collecting pipe exhaust gas entrance.
During preheating, to be preheated to whole system, further, the preheating entrance of the multi-stage heat exchanger preheating channel
Snorkel is equipped between being exported with heat exchange, the snorkel is equipped with gas valve, by closing collecting pipe exhaust gas entrance
When, gas valve, operating resisting blower are opened, realizes the preheating to whole systems such as multi-stage heat exchanger, resisting blowers, from
And system is set to reach good exhaust-gas treatment state.
For the utility model is better described, here, its workflow is briefly described below：
In the system warm-up stage, when the accumulation of heat high temperature furnace starts to warm up, by closing the inlet valve, described in opening
Gas valve, resisting blower, make the interior circulation in accumulation of heat high temperature furnace, multi-stage heat exchanger and pipeline of pre- hot wind, energy saving to realize
Be rapidly heated, shorten the heating-up time.After system bulk temperature rises to setting value, circulation in closing, opening inlet valve,
Close gas valve, equipment normal work, into the exhaust-gas treatment stage.
In the exhaust-gas treatment stage, the organic exhaust gas being collected into passes through the preheating entrance entrance from the multi-stage heat exchanger, absorbs
The preheating outlet of multi-stage heat exchanger is reached after enough heats, then enters accumulation of heat high temperature furnace by preheating pipe, further
Heating.In accumulation of heat high temperature furnace, after organic exhaust gas fully decomposes, carbon dioxide, water are converted into, becomes purified gas and enters back into multistage
Heat, is discharged into multi-stage heat exchanger, is finally arranged with relatively low temperature by chimney to air by heat exchanger heat exchange entrance.
Compared with prior art, the beneficial effects of the utility model are：At energy-efficient exhaust gas described in the utility model
Reason machine, by multi-stage heat exchanger, accumulation of heat high temperature furnace, resisting blower and its optimizing and combining, efficiently uses organic exhaust gas feature,
Have the characteristics that treatment effeciency higher, degree of purification be more preferable, processing cost reduces, realize clean and effective, energy saving and cost lowering, have
Good application prospect.
Brief description of the drawings
Fig. 1 is the structure diagram of the utility model embodiment；
Wherein：1. collecting pipe, 2. multi-stage heat exchangers, 3. accumulation of heat high temperature furnaces, 4. resisting blowers, 5. chimneys, A. preheatings
Entrance, B. preheatings outlet, C. heat exchange entrances, D. heat exchange outlet, H. inlet valves, G. gas valves.
Embodiment
The following is a combination of the drawings in the embodiments of the present utility model, and the technical scheme in the embodiment of the utility model is carried out
Clearly and completely describe, it is clear that the described embodiments are only a part of the embodiments of the utility model, rather than whole
Embodiment.Based on the embodiment in the utility model, those of ordinary skill in the art are without making creative work
All other embodiments obtained, shall fall within the protection scope of the present invention.
With reference to shown in Fig. 1, a kind of energy-efficient exhaust gas processor, including print the gas collection for producing organic exhaust gas for collecting
Pipeline 1, the multi-stage heat exchanger 2 to exchange heat for being preheated to low temperature waste gas, to the high temperature purification gas after processing, to having
Machine exhaust gas carries out the accumulation of heat high temperature furnace 3 of pyrolytic processing, for the resisting blower 4 of pumping gas, for being outwardly vented
Chimney 5；The multi-stage heat exchanger 2 is equipped with preheating channel, heat exchanger channels, and the collecting pipe 1 and the multi-stage heat exchanger 2 are pre-
The preheating entrance A connections of the passage of heat, the chimney 5 are connected with the heat exchange outlet D of 2 preheating channel of multi-stage heat exchanger；It is described
The preheating of 2 preheating channel of multi-stage heat exchanger is exported between B and accumulation of heat high temperature furnace 3, accumulation of heat high temperature furnace 3 exchanges heat with multi-stage heat exchanger 2
Between the heat exchange outlet D of passage, connected respectively by preheating pipe, heat exchange pipeline；The resisting blower 4 is arranged on internal pipeline
On；In the case where the resisting blower 4 is pumped, gas pass sequentially through the collecting pipe 1,2 preheating channel of multi-stage heat exchanger it is pre-
Hot entrance A, preheating outlet B, accumulation of heat high temperature furnace 3, heat exchange entrance C, the heat exchange outlet D of 2 preheating channel of multi-stage heat exchanger, chimney 5
Handled.
Here, in the multi-stage heat exchanger 2, being discharged from the accumulation of heat high temperature furnace 3 in heat exchange pipeline is directly utilized
High temperature purification gas carry out heat exchange with the low temperature waste gas entered in preheating pipe from the collecting pipe 1, low temperature is given up
Gas temperature in the case of without directly consuming energy increases substantially the operating temperature close to accumulation of heat high temperature furnace 3, subsequently into storage
Hot high temperature furnace 3 carries out pyrolytic, and decomposition while produces substantial amounts of heat to maintain the high temperature in accumulation of heat high temperature furnace 3, and will point
High temperature purification gas after the completion of solution is arranged to multi-stage heat exchanger 2；Likewise, multi-stage heat exchanger 2 absorbs high temperature purification gas by exchanging heat
Heat, be conducive to make full use of waste heat, prevent harmful effect of the waste heat to atmospheric environment.
Here, the resisting blower 4 is arranged on the heat exchange pipeline.
During due to carrying out exhaust-gas treatment, exhaust gas can take away heat, to improve 3 accumulation of heat effect of accumulation of heat high temperature furnace, shorten it and reach
To the time of predetermined temperature, the collecting pipe 1 is equipped with inlet valve H, the inlet valve H in the system warm-up stage
Close 1 exhaust gas entrance of collecting pipe.
During preheating, to be preheated to whole system, further, the preheating of 2 preheating channel of multi-stage heat exchanger enters
Snorkel is equipped between mouth A and heat exchange outlet D, the snorkel is equipped with gas valve G, by useless in closing collecting pipe 1
During gas entrance, gas valve G, operating resisting blower 4 are opened, is realized to the whole system such as multi-stage heat exchanger 2, resisting blower 4
The preheating of system, so that system reaches good exhaust-gas treatment state.
After snorkel and gas valve G are set, hanker in advance, acted on by battle array pressure, the extraneous air outside chimney 5, which will not enter, is
In system, the heat in system outwards will not excessively scatter and disappear.Experiment shows, under the same terms of control other factors, uses
The system of the present embodiment rises to the time needed for 800-900 DEG C compared with homogeneous system, by the temperature of accumulation of heat high temperature furnace 3, from same
The 4 of class system shorten to when small the present embodiment 2 it is small when.
For the utility model is better described, here, its workflow is briefly described below：
In the system warm-up stage, when the accumulation of heat high temperature furnace 3 starts to warm up, by closing the inlet valve H, institute is opened
Gas valve G, resisting blower 4 are stated, makes the interior circulation in accumulation of heat high temperature furnace 3, multi-stage heat exchanger 2 and pipeline of pre- hot wind, with reality
Show energy saving and be rapidly heated, shorten the heating-up time.After system bulk temperature rises to setting value, close in circulation, open into
Mouth valve H, close gas valve G, equipment normal work, into the exhaust-gas treatment stage.
In the exhaust-gas treatment stage, the organic exhaust gas being collected into passes through the preheating entrance A entrance from the multi-stage heat exchanger 2, inhales
The preheating outlet B that multi-stage heat exchanger 2 is reached after enough heats has been received, has then entered accumulation of heat high temperature furnace 3 by preheating pipe, into
One step heats.In accumulation of heat high temperature furnace 3, after organic exhaust gas fully decomposes, be converted into carbon dioxide, water, become purified gas again into
Enter multi-stage heat exchanger 2 exchange heat entrance C, heat is discharged into multi-stage heat exchanger 2, finally with relatively low temperature by 5 row of chimney to
Air.
While there has been shown and described that the embodiment of the utility model, for the ordinary skill in the art,
It is appreciated that these embodiments can be carried out with a variety of changes in the case where not departing from the principle of the utility model and spirit, repaiied
Change, replace and modification, the scope of the utility model are defined by the appended claims and the equivalents thereof.
Claims (4)
1. a kind of energy-efficient exhaust gas processor, it is characterised in that including printing the gas collecting tube for producing organic exhaust gas for collecting
Road, the multi-stage heat exchanger to exchange heat for being preheated to low temperature waste gas, to the high temperature purification gas after processing, to organic waste
Gas carries out the accumulation of heat high temperature furnace of pyrolytic processing, for the resisting blower of pumping gas, for the chimney being outwardly vented；
The multi-stage heat exchanger is equipped with preheating channel, heat exchanger channels, and the collecting pipe is pre- with the multi-stage heat exchanger preheating channel
Hot entrance connection, the heat exchange outlet of the chimney and the multi-stage heat exchanger preheating channel；The multi-stage heat exchanger preheating
Between the preheating outlet of passage and accumulation of heat high temperature furnace, between the heat exchange outlet of accumulation of heat high temperature furnace and multi-stage heat exchanger heat exchanger channels,
Connected respectively by preheating pipe, heat exchange pipeline；The resisting blower is arranged on internal pipeline；Taken out in the resisting blower
Send down, gas passes sequentially through the collecting pipe, the preheating entrance of multi-stage heat exchanger preheating channel, preheating outlet, accumulation of heat high temperature
Stove, the heat exchange entrance of multi-stage heat exchanger preheating channel, heat exchange outlet, chimney.
2. energy-efficient exhaust gas processor according to claim 1, it is characterised in that the resisting blower is arranged on described
On heat exchange pipeline.
3. energy-efficient exhaust gas processor according to claim 1 or 2, it is characterised in that the collecting pipe is equipped with
Inlet valve, the inlet valve are used to close collecting pipe exhaust gas entrance in the system warm-up stage.
4. energy-efficient exhaust gas processor according to claim 3, it is characterised in that the multi-stage heat exchanger preheating channel
Preheating entrance and heat exchange outlet between be equipped with snorkel, the snorkel is equipped with gas valve.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721301906.2U CN207356893U (en) | 2017-10-11 | 2017-10-11 | A kind of energy-efficient exhaust gas processor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721301906.2U CN207356893U (en) | 2017-10-11 | 2017-10-11 | A kind of energy-efficient exhaust gas processor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207356893U true CN207356893U (en) | 2018-05-15 |
Family
ID=62346947
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201721301906.2U Active CN207356893U (en) | 2017-10-11 | 2017-10-11 | A kind of energy-efficient exhaust gas processor |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207356893U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109925841A (en) * | 2019-04-17 | 2019-06-25 | 惠州市溶科环保科技有限公司 | A kind of energy-efficient organic exhaust gas purifying system |
-
2017
- 2017-10-11 CN CN201721301906.2U patent/CN207356893U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109925841A (en) * | 2019-04-17 | 2019-06-25 | 惠州市溶科环保科技有限公司 | A kind of energy-efficient organic exhaust gas purifying system |
| CN109925841B (en) * | 2019-04-17 | 2021-04-06 | 惠州市溶科环保科技有限公司 | Energy-efficient organic waste gas purification system |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN104654815A (en) | Mosaic ceramic kiln waste heat power generation comprehensive utilization system | |
| CN106196125B (en) | A kind of exhaust-gas treatment structure applied to incinerator | |
| CN207356893U (en) | A kind of energy-efficient exhaust gas processor | |
| CN205316352U (en) | RTO system with tail gas waste heat recovery function | |
| CN206377678U (en) | A kind of chlorobenzene exhaust gas processing device | |
| CN101929095A (en) | Air supplying and exhausting system for dryer hood of paper machine | |
| CN205373043U (en) | Grain drying tower heating system's surplus heat energy -saving processing system | |
| CN208253609U (en) | A kind of printing machine VOCs concentration paddy electricity balance RTO processing system | |
| CN204421052U (en) | A kind of waste heat recovery furnace | |
| CN104515402B (en) | A kind of residual-heat utilization method of sintering system and device | |
| CN206131029U (en) | Automobile coating radiation area heating furnace waste heat recovery device | |
| CN206563304U (en) | A kind of heat accumulating type incineration device with cleaning function | |
| CN207907269U (en) | A kind of gas cooler and steam air heater association system | |
| CN107830720A (en) | One kind is provided multiple forms of energy to complement each other wind and water combined drying device and method | |
| CN208398093U (en) | A kind of Adsorption Concentration runner RTO/RCO combustion furnace | |
| CN207180441U (en) | A kind of heating furnace heat pipe type waste heat reclaiming device | |
| CN201915293U (en) | Ventilating system for paper making | |
| CN207046878U (en) | Hot-blast stove fume comprehensive utilization device in a kind of aluminium polychloride production | |
| CN205807437U (en) | Combustion furnace recycling residual heat system | |
| CN205014801U (en) | Heat recovery unit of cleaning machine | |
| CN204460849U (en) | Building air exhaust waste heat reclaiming type air source heat pump system | |
| CN213556398U (en) | High-efficient mixing arrangement of RTO waste gas | |
| CN205066393U (en) | Special hot -blast furnace of grain drying tower | |
| CN204306034U (en) | A kind of tobacco dense barn waste heat of chimney recycle device | |
| CN108452605A (en) | A kind of flue gas dust collecting system technique and its flue device of application |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |