CN204911110U - Be used for fashioned dust collecting device of living beings granule - Google Patents
Be used for fashioned dust collecting device of living beings granule Download PDFInfo
- Publication number
- CN204911110U CN204911110U CN201520525522.3U CN201520525522U CN204911110U CN 204911110 U CN204911110 U CN 204911110U CN 201520525522 U CN201520525522 U CN 201520525522U CN 204911110 U CN204911110 U CN 204911110U
- Authority
- CN
- China
- Prior art keywords
- air
- deduster
- cyclone separator
- collect plant
- dust collect
- 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
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Classifications
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/10—Biofuels, e.g. bio-diesel
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel
Abstract
The utility model discloses a be used for fashioned dust collecting device of living beings granule, including cyclone, dust remover and feed bin, cyclone is connected with the wind channel so that contain in the gaseous cyclone of entering of timber, the cyclone top is equipped with the air outlet, the air outlet passes through the pipeline and is connected with the air inlet of dust remover, the dust remover is equipped with the filter bag, and the gas outlet intercommunication of export of filter bag top and dust remover, the bottom of cyclone and dust remover all is connected with the feed bin. Adopt the utility model discloses, inhalable particle concentration in the low air of degradable, the security of improving production.
Description
Technical field
The utility model relates to grain forming field, particularly relates to a kind of dust collect plant for biomass grain forming.
Background technology
Along with the minimizing day by day of oil and coal resources, the whole world is also more and more paid attention to the development and utilization of new forms of energy, and utilize discarded stalk, the produced biomass granule fuel such as wood leftover material also starts to widely use.Timber cuts into Powdered, then is involved in air channel by blower fan and is transported to feed bin, inevitably causes a large amount of molecules to scatter in atmosphere, not only causes air pollution, and there is the potential safety hazard of dust explosion.Therefore need a kind of new dust collect plant for solving the dust that in biomass grain forming, timber transport produces.
Utility model content
Technical problem to be solved in the utility model is, provides a kind of dust collect plant for biomass grain forming, can reduce Inhalable Particulate concentration, improves the security of producing.
In order to solve the problems of the technologies described above, the utility model provides a kind of dust collect plant for biomass grain forming, comprise cyclone separator, deduster and feed bin, described cyclone separator is connected with air channel to make the gas containing timber enter in cyclone separator, described cyclone separator top is provided with air outlet, and described air outlet is connected with the air inlet of deduster by pipeline; Described deduster is provided with filter bag, and above filter bag, outlet is communicated with the gas outlet of deduster, and described cyclone separator is all connected with feed bin with the bottom of deduster.
As the improvement of such scheme, described cyclone separator is provided with cylindrical shell, comprises cylindrical tube and conic tube, and described cylindrical tube is located at above conic tube.
As the improvement of such scheme, described cyclone separator also comprises the air inlet being located at cylindrical tube sidewall.
As the improvement of such scheme, the air inlet of described cyclone separator is arc-shape wind pipe to make the gas containing timber be input to inner chamber along the inner core tangential direction of cylindrical tube.
As the improvement of such scheme, described deduster top is provided with air-purifying chamber, and described air-purifying chamber is provided with gas outlet, and described gas outlet is connected with air exhauster.
As the improvement of such scheme, described air-purifying chamber is provided with pulse blowing valve, injection tube and shower nozzle, and described injection tube is distributed in the top of filter bag, and the end of injection tube is provided with shower nozzle, and each filter bag correspondence arranges a shower nozzle;
Described pulse blowing valve is located in injection tube to control compressed-air actuated air inflow.
As the improvement of such scheme, described deduster is provided with 100 ~ 200 filter bags.
As the improvement of such scheme, the bottom of described cyclone separator is provided with the first discharge rotary valve.
As the improvement of such scheme, the bottom of described deduster is provided with the second discharge rotary valve.
Implement the utility model, there is following beneficial effect:
The sedimentation that dust collect plant described in the utility model adopts the combination of cyclopneumatic separator and deduster to process non-powder timber and powdery timber is collected, can realize adopting wind to send mode to transport the object of timber arrival feed bin, also can reduce dust in transportation to scatter in atmosphere, significantly reduce Inhalable Particulate concentration, ensure that the health of field personnel also reduces the air pollution to environment, reduce the risk that dust explosion produces.
Accompanying drawing explanation
Fig. 1 is the structural representation of the utility model for the dust collect plant of biomass grain forming.
Detailed description of the invention
For making the purpose of this utility model, technical scheme and advantage clearly, below in conjunction with accompanying drawing, the utility model is described in further detail.
As shown in Figure 1, the utility model provides a kind of dust collect plant for biomass grain forming, comprise cyclone separator 1, deduster 2 and feed bin 3, described cyclone separator 1 is connected with air channel to make the gas containing timber enter in cyclone separator 1, described cyclone separator 1 top is provided with air outlet 13, and described air outlet 13 is connected with the air inlet 23 of deduster 2 by pipeline; Described deduster 2 is provided with filter bag 24, and above filter bag 24, outlet is communicated with the gas outlet 22 of deduster 2, and described cyclone separator 1 is all connected with feed bin 3 with the bottom of deduster 2.
The object of dust collect plant described in the utility model to make timber be settled down to feed bin 3 by air channel the gas of timber after co-grinding, and control of dust purified gas is discharged, and realizes being separated of solid and gas.Wherein, be transported to feed bin 3 by blower fan and can cause being studded with a large amount of powdery timber (dust) in feed bin 3 in air, powdery timber is due to lightweight, be difficult to sedimentation, not only cause the waste of timber, powdery timber is pellet simultaneously, easily causes the disease of human body respiration aspect.Therefore, the timber that the utility model adopts wind to send is delivered to cyclone separator 1 and is separated with non-powder timber by powdery timber.
Preferably, cyclone separator 1 described in the utility model is provided with cylindrical shell, comprises cylindrical tube 11 and conic tube 12, and described cylindrical tube 11 is located at above conic tube 12.
Preferably, described cyclone separator 1 also comprises the air inlet 14 being located at cylindrical tube 11 sidewall.
Preferably, the air inlet 14 of described cyclone separator 1 is arc-shape wind pipe to make the gas containing timber be input to inner chamber along the inner core tangential direction of cylindrical tube 11.
Cyclone separator 1 cylindrical shell described in the utility model comprises cylindrical tube 11 and conic tube 12, and air inlet 14 is located at the sidewall of cylindrical tube 11, enter from air inlet 14 containing timber air-flow, and be input to inner chamber along the inner core tangential direction of cylindrical tube 11, in cylindrical tube 11, form spiral helicine whirlwind.The larger non-powder timber of particle diameter and the less powdery timber of particle diameter is comprised containing timber air-flow.Non-powder timber in whirlwind is thrown toward barrel under centrifugal action, and under gravity, the barrel along conic tube 12 glides, and concentrates on the bottom of conic tube 12.And the bottom of cyclone separator 1 is provided with the first discharge rotary valve 15, the non-powder timber at the bottom of cylinder can be expelled to feed bin 3, realizes the transfer of non-powder timber.On the other hand, powdery timber discharges cyclone separator 1 along air-flow by the air outlet 13 above cylindrical tube 11.Powdery timber is little due to particle diameter, if discharge extraneous along with air-flow, can produce a large amount of dusts, therefore need further to the process of powdery timber.
Through the dust that cyclone separator 1 air outlet 13 is discharged, enter the air inlet 23 of deduster 2.Be provided with 100 ~ 200 filter bags 24 in deduster 2, more preferably, in deduster 2, be provided with 150 ~ 180 filter bags 24.Air-flow containing powdery timber is passed into air-purifying chamber 21 above deduster 2 from filter bag 24, is discharged outside deduster 2 by the air exhauster (not marking air exhauster in figure) be connected with gas outlet 22.
It should be noted that, when deduster 2 described in the utility model works, comprise pure qi (oxygen) and deashing two duties.Pure qi (oxygen) process, air exhauster is utilized inwardly to bleed, at this moment from the air-flow containing powdery timber that cyclone separator 1 input is come in, the air-purifying chamber 21 on deduster 2 top can only be entered from filter bag 24, discharge deduster 2 from air-purifying chamber 21 again, and air-flow can make dust amass the outer surface being attached to filter bag 24 through filter bag 24.But along with dust amasss attached thicker, the resistance of deduster 2 air-breathing constantly rises, and for making equipment resistance be no more than 1200Pa, deduster 2 can normally work, need the dust regularly removed on filter bag 24.
Preferably, described air-purifying chamber 21 is provided with pulse blowing valve 25, injection tube 26 and shower nozzle 27, and described injection tube 26 is distributed in the top of filter bag 24, and the end of injection tube 26 is provided with shower nozzle 27, and each filter bag 24 correspondence arranges a shower nozzle 27;
Described pulse blowing valve 25 is located in injection tube 26 to control compressed-air actuated air inflow.
Deashing process is the gas outlet 22 first cutting off air-purifying chamber 21, the state making the filter bag 24 in deduster 2 be in airless to pass through.Start by set date pulse blowing valve 25, make compressed air be delivered to the shower nozzle 27 above each filter bag 24 by injection tube 26, sprayed by shower nozzle 27 and enter filter bag 24, filter bag 24 was sharply expanded in moment, powdery timber is shaken off in opposite direction effect along with air-flow, reaches the object of deashing.It should be noted that, enough durations are closed to ensure after winding-up from the dust settling of filter bag 24 stripping to ash bucket after break impulse blowing valve 25, avoid dust disengaging filter bag 24 surface after again with the phenomenon of the attached collection of air-flow to adjacent filter bag 24 surface, make filter bag 24 deashing thorough.Finally, powdery timber is collected in bottom deduster 2 after filter bag 24 falls, and makes powdery timber drain into feed bin 3 by the second discharge rotary valve 28, significantly can reduce dust degree of scatter in transportation, reduce the air pollution to environment.
The sedimentation that dust collect plant described in the utility model adopts the combination of cyclopneumatic separator and deduster 2 to process non-powder timber and powdery timber is collected, can realize adopting wind to send mode to transport the object of timber arrival feed bin 3, also can reduce dust in transportation to scatter in atmosphere, significantly reduce Inhalable Particulate concentration, ensure that the health of field personnel also reduces the air pollution to environment, reduce the risk that dust explosion produces.
Above disclosedly be only a kind of preferred embodiment of the utility model, certainly can not limit the interest field of the utility model with this, therefore according to the equivalent variations that the utility model claim is done, still belong to the scope that the utility model is contained.
Claims (9)
1. for the dust collect plant of biomass grain forming, it is characterized in that, comprise cyclone separator, deduster and feed bin, described cyclone separator is connected with air channel to make the gas containing timber enter in cyclone separator, described cyclone separator top is provided with air outlet, and described air outlet is connected with the air inlet of deduster by pipeline; Described deduster is provided with filter bag, and above filter bag, outlet is communicated with the gas outlet of deduster, and described cyclone separator is all connected with feed bin with the bottom of deduster.
2. as claimed in claim 1 for the dust collect plant of biomass grain forming, it is characterized in that, described cyclone separator is provided with cylindrical shell, comprises cylindrical tube and conic tube, and described cylindrical tube is located at above conic tube.
3. as claimed in claim 2 for the dust collect plant of biomass grain forming, it is characterized in that, described cyclone separator also comprises the air inlet being located at cylindrical tube sidewall.
4. as claimed in claim 3 for the dust collect plant of biomass grain forming, it is characterized in that, the air inlet of described cyclone separator is arc-shape wind pipe to make the gas containing timber be input to inner chamber along the inner core tangential direction of cylindrical tube.
5. as claimed in claim 1 for the dust collect plant of biomass grain forming, it is characterized in that, described deduster top is provided with air-purifying chamber, and described air-purifying chamber is provided with gas outlet, and described gas outlet is connected with air exhauster.
6. as claimed in claim 5 for the dust collect plant of biomass grain forming, it is characterized in that, described air-purifying chamber is provided with pulse blowing valve, injection tube and shower nozzle, and described injection tube is distributed in the top of filter bag, and the end of injection tube is provided with shower nozzle, each filter bag correspondence arranges a shower nozzle;
Described pulse blowing valve is located in injection tube to control compressed-air actuated air inflow.
7. as claimed in claim 1 for the dust collect plant of biomass grain forming, it is characterized in that, described deduster is provided with 100 ~ 200 filter bags.
8. as claimed in claim 1 for the dust collect plant of biomass grain forming, it is characterized in that, the bottom of described cyclone separator is provided with the first discharge rotary valve.
9. as claimed in claim 1 for the dust collect plant of biomass grain forming, it is characterized in that, the bottom of described deduster is provided with the second discharge rotary valve.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520525522.3U CN204911110U (en) | 2015-07-20 | 2015-07-20 | Be used for fashioned dust collecting device of living beings granule |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520525522.3U CN204911110U (en) | 2015-07-20 | 2015-07-20 | Be used for fashioned dust collecting device of living beings granule |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204911110U true CN204911110U (en) | 2015-12-30 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520525522.3U Expired - Fee Related CN204911110U (en) | 2015-07-20 | 2015-07-20 | Be used for fashioned dust collecting device of living beings granule |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204911110U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106139809A (en) * | 2016-08-22 | 2016-11-23 | 李志伟 | A kind of dust separation device |
-
2015
- 2015-07-20 CN CN201520525522.3U patent/CN204911110U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106139809A (en) * | 2016-08-22 | 2016-11-23 | 李志伟 | A kind of dust separation device |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20151230 Termination date: 20170720 |
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| CF01 | Termination of patent right due to non-payment of annual fee |