CN108636044A - Cleaner and dust pelletizing system - Google Patents
Cleaner and dust pelletizing system Download PDFInfo
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- CN108636044A CN108636044A CN201810597625.9A CN201810597625A CN108636044A CN 108636044 A CN108636044 A CN 108636044A CN 201810597625 A CN201810597625 A CN 201810597625A CN 108636044 A CN108636044 A CN 108636044A
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- transferring medium
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D50/00—Combinations of methods or devices for separating particles from gases or vapours
- B01D50/40—Combinations of devices covered by groups B01D45/00 and B01D47/00
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Abstract
The present invention relates to smoke eliminator technical fields, more particularly, to a kind of cleaner and dust pelletizing system.Cleaner, including air-intake device, cyclone dust collectors, cooling cylinder, the first heat transferring medium pipeline, absorption type heat pump assembly and steam generation facility；Air-intake device is provided with the gas inlet for entering for flue gas, and air-intake device is connected to the air inlet of cyclone dust collectors；Cyclone dust collectors are located at the inside of cooling cylinder, first heat transferring medium pipeline is passed through from cooling cylinder, for cooling down to cyclone dust collectors, one end of first heat transferring medium pipeline is connected to the generator of absorption type heat pump assembly, and the other end of the first heat transferring medium pipeline is connected to the evaporator of absorption type heat pump assembly；Steam generation facility is connected to the condenser of absorption type heat pump assembly and absorber, and steam generation facility is for generating the water vapour that can be mixed with flue gas.The present invention alleviates particulate matter and exports the phenomenon that being discharged from the purifying smoke of cyclone dust collectors, improves efficiency of dust collection.
Description
Technical field
The present invention relates to smoke eliminator technical fields, more particularly, to a kind of cleaner and dust pelletizing system.
Background technology
In industrial operations, often will produce a large amount of dusty gas, for example, solid matter machine cut or crushing or
The polishing process of abrasive machine, the life in the workshops such as ore dressing, sintering, refractory material, casting, cement, glass in coal, steel, chemical industry
During production, especially when producing ceramic product (such as ceramic tile), the Spraying Dryer of Ceramics meeting a large amount of dusty gas of output, this
A little dusty gases are flown upward everywhere, are not only polluted workshop air and outside atmosphere, also the worker of long-term work can be made to suffer from pneumoconiosis, sternly
The health of worker is endangered again, therefore is dusted processing to dusty gas to have prodigious necessity.
Cyclone dust collectors are a kind of widely used cleaners.It is low with simple in structure, operating cost and initial cost, remove
The advantages that dirt is efficient, and operational management adaptable to polluted gas is simple.But cyclone dust collectors are by centrifugal force general
A kind of cleaner of grain object separation, the particulate matter larger to grain size has good efficiency of dust collection, to micron or submicron order
Particle removal efficiency it is relatively low.
In order to overcome drawbacks described above, wet scrubber and cyclone dust collectors are combined by existing cleaner, wet
Drop is sprayed at formula deduster end, and the particulate matter in gas is captured, and then centrifuges force effect dedusting to passing through in cyclone dust collectors
And dehydration, this mode can cause water mist to carry partial particulate object from the purifying smoke of cyclone dust collectors outlet discharge, therefore, remove
Dirt is less efficient.
Invention content
The purpose of the present invention is to provide a kind of cleaners, existing in the prior art because water mist can carry portion to solve
Divide particulate matter from the low technical problem of efficiency of dust collection caused by the purifying smoke of cyclone dust collectors outlet discharge.
It is existing in the prior art because water mist can carry to solve the present invention also aims to provide a kind of dust pelletizing system
The low technical problem of efficiency of dust collection caused by partial particulate object is discharged from the outlet of the purifying smoke of cyclone dust collectors.
Based on above-mentioned first purpose, the present invention provides a kind of cleaner, including it is air-intake device, cyclone dust collectors, cold
Solidifying case, the first heat transferring medium pipeline, absorption type heat pump assembly and steam generation facility；
The air-intake device is provided with the gas inlet for entering for flue gas, the air-intake device and the cyclone dust removal
The air inlet of device is connected to；
The cyclone dust collectors are located at the inside of the cooling cylinder, and the first heat transferring medium pipeline is from the cooling cylinder
It passes through, for cooling down to the cyclone dust collectors, one end of the first heat transferring medium pipeline and the absorption type heat pump assembly
Generator connection, the other end of the first heat transferring medium pipeline is connected to the evaporator of the absorption type heat pump assembly；
The steam generation facility is connected to the condenser of the absorption type heat pump assembly and absorber, the steam generation
Device is for generating the water vapour that can be mixed with the flue gas.
In some embodiments, the air-intake device includes plenum chamber and blast pipe, the gas inlet with it is described quiet
The air inlet connection of case, the air outlet of the plenum chamber is pressed to be connected to one end of the blast pipe, the other end of the blast pipe
It is connected to the air inlet of the cyclone dust collectors.
In some embodiments, the steam generation facility includes the second heat transferring medium pipeline and sparge pipe；
One end of the second heat transferring medium pipeline is connected to the condenser of the absorption type heat pump assembly, and described second changes
The other end of heat medium pipeline is connected to the absorber of the absorption type heat pump assembly；
The sparge pipe is used for the second heat transferring medium pipeline water spray, to generate water vapour.
In some embodiments, the steam generation facility includes the second heat transferring medium pipeline and steam generator；
The steam generator and the second heat transferring medium pipeline connection, the steam (vapor) outlet of the steam generator and institute
State air-intake device connection.
In some embodiments, further include water tank, one end of the sparge pipe is connected to the water tank, the spray
The other end of water pipe is located at the inside of the plenum chamber.
In some embodiments, the other end of the sparge pipe is provided with nozzle.
In some embodiments, further include return pipe, one end of the return pipe is connected to the plenum chamber, described time
The other end of water pipe is connected to the water tank.
In some embodiments, further include discharge pipe, the purifying smoke of the discharge pipe and the cyclone dust collectors goes out
Mouth connection.
In some embodiments, the discharge pipe is provided with exhaust fan.
Based on above-mentioned second purpose, the present invention also provides a kind of dust pelletizing systems, including multiple cleaners.
Compared with prior art, beneficial effects of the present invention are：
Cleaner provided by the invention, including air-intake device, cyclone dust collectors, cooling cylinder, the first heat transferring medium pipeline,
Absorption type heat pump assembly and steam generation facility；The air-intake device is provided with the gas inlet for entering for flue gas, described
Air-intake device is connected to the air inlet of the cyclone dust collectors；The cyclone dust collectors are located at the inside of the cooling cylinder, described
First heat transferring medium pipeline is passed through from the cooling cylinder, for cooling down to the cyclone dust collectors, first heat transferring medium
One end of pipeline is connected to the generator of the absorption type heat pump assembly, the other end of the first heat transferring medium pipeline with it is described
The evaporator of absorption type heat pump assembly is connected to；Condenser and absorption of the steam generation facility with the absorption type heat pump assembly
Device is connected to, and the steam generation facility is for generating the water vapour that can be mixed with the flue gas.
Based on the structure, cleaner provided by the invention is mixed using water vapour with flue gas, and to cyclone dust collectors into
Row cooling so that steam is condensed to form the drop of bigger, and under the influence of centrifugal force, the particulate matter in flue gas is with drop quilt
It separates, exports the phenomenon that being discharged from the purifying smoke of cyclone dust collectors to effectively alleviate particulate matter, improve and remove
Dirt efficiency.When implementing, flue gas is passed through air-intake device from gas inlet, starts cyclone dust collectors, the first heat transferring medium pipeline
In heat transferring medium absorption condensation case inside heat, cyclone dust collectors are cooled down, in the effect of absorption type heat pump assembly
Under, steam generation facility generates the water vapour that can be mixed with flue gas, and water vapour is mixed with flue gas, and captures the particle in flue gas
The mixture of object, flue gas and water vapour enters from air inlet in cyclone dust collectors, is centrifuged, due to the first heat transferring medium
The heat inside heat transferring medium absorption condensation case in pipeline, cools down cyclone dust collectors, so that steam is condensed
The drop of bigger is formed, under the influence of centrifugal force, particulate matter in flue gas is separated with drop.
Further, the air-intake device includes plenum chamber and blast pipe, the gas inlet and the plenum chamber into
Air port is connected to, and the air outlet of the plenum chamber is connected to one end of the blast pipe, the other end of the blast pipe and the rotation
The air inlet of wind deduster is connected to.
By the way that plenum chamber is arranged so that the intake of flue gas evenly distributes, and helps to improve efficiency of dust collection.In addition, passing through
Plenum chamber is set, additionally it is possible to reduce noise, improve the overall performance of cleaner.
Further, the steam generation facility includes the second heat transferring medium pipeline and sparge pipe；
One end of the second heat transferring medium pipeline is connected to the condenser of the absorption type heat pump assembly, and described second changes
The other end of heat medium pipeline is connected to the absorber of the absorption type heat pump assembly；
The sparge pipe is used for the second heat transferring medium pipeline water spray, to generate water vapour.
Under the action of absorption type heat pump assembly, the temperature of the second heat transferring medium pipeline increases, and sparge pipe sprays to water mist
When the second heat transferring medium pipeline, water mist can vaporize, and generate water vapour, water vapour can be mixed with flue gas, and be captured in flue gas
Particulate matter, the mixture of flue gas and water vapour enters in cyclone dust collectors from air inlet, is centrifuged, and changes due to first
The heat inside heat transferring medium absorption condensation case in heat medium pipeline, cools down cyclone dust collectors, so that steam
It is condensed to form the drop of bigger, under the influence of centrifugal force, particulate matter in flue gas is separated with drop.
Further, the steam generation facility includes the second heat transferring medium pipeline and steam generator；
The steam generator and the second heat transferring medium pipeline connection, the steam (vapor) outlet of the steam generator and institute
State air-intake device connection.
It is passed through water source to steam generator, after water and the second heat transferring medium pipeline contact, vaporization forms water vapour, water vapour
Plenum chamber is entered by steam (vapor) outlet, is mixed with flue gas, and captures the particulate matter in flue gas, the mixture of flue gas and water vapour from into
Gas port enters in cyclone dust collectors, is centrifuged, due to the heat transferring medium absorption condensation case in the first heat transferring medium pipeline
Internal heat, cools down cyclone dust collectors, so that steam is condensed to form the drop of bigger, in the work of centrifugal force
Under, particulate matter in flue gas is separated with drop.
Further, further include water tank, one end of the sparge pipe is connected to the water tank, the sparge pipe it is another
One end is located at the inside of the plenum chamber.
By the way that water tank is arranged, it is capable of providing water source, is sprayed to the outer surface of the second heat transferring medium pipeline convenient for sparge pipe
Water mist, and form water vapour.
Further, the other end of the sparge pipe is provided with nozzle.
By the way that nozzle is arranged, the contact area of water mist and the second heat transferring medium pipeline can be increased, cooling effect is more preferable.
Further, further include return pipe, one end of the return pipe is connected to the plenum chamber, the return pipe it is another
One end is connected to the water tank.
By the way that return pipe is arranged, the mixture of condensed water and water and flue gas particle in plenum chamber can be discharged into
In water tank, water is recycled.
Further, further include discharge pipe, the purifying smoke outlet of the discharge pipe and the cyclone dust collectors.
Further, the discharge pipe is provided with exhaust fan.
By the way that discharge pipe and exhaust fan is arranged, such mode improves net convenient for purified flue gas emission is gone out
Change efficiency.
Dust pelletizing system provided by the invention can effectively be delayed due to the use of multiple cleaners provided by the invention
It solves particulate matter and exports the phenomenon that being discharged from the purifying smoke of cyclone dust collectors, improve efficiency of dust collection.
In conclusion the present invention has the advantages that above-mentioned many and practical value, and there are no in similar product similar
Method publish or use and really belong to innovation, produce the effect of preferable practicality, and there is extensive industrial value.
Attached drawing will be coordinated below, elaborated.
Description of the drawings
It, below will be to specific in order to illustrate more clearly of the specific embodiment of the invention or technical solution in the prior art
Embodiment or attached drawing needed to be used in the description of the prior art are briefly described, it should be apparent that, in being described below
Attached drawing is some embodiments of the present invention, for those of ordinary skill in the art, before not making the creative labor
It puts, other drawings may also be obtained based on these drawings.
Fig. 1 is the structural schematic diagram for the cleaner that the embodiment of the present invention one provides；
Fig. 2 is the structural schematic diagram of cleaner provided by Embodiment 2 of the present invention；
Fig. 3 is the structural schematic diagram for the cleaner that the embodiment of the present invention three provides；
Fig. 4 is the structural schematic diagram for the cleaner that the embodiment of the present invention four provides.
Icon：101- the first heat transferring medium pipelines；102- the second heat transferring medium pipelines；103- cooling cylinders；104- whirlwind removes
Dirt device；105- absorption type heat pump assemblys；106- plenum chambers；107- blast pipes；108- sparge pipes；109- water tanks；110- nozzles；
111- return pipes；112- steam generators；113- discharge pipes；114- exhaust fans.
Specific implementation mode
Technical scheme of the present invention is clearly and completely described below in conjunction with attached drawing, it is clear that described implementation
Example is a part of the embodiment of the present invention, instead of all the embodiments.Based on the embodiments of the present invention, ordinary skill
The every other embodiment that personnel are obtained without making creative work, shall fall within the protection scope of the present invention.
In the description of the present invention, it should be noted that such as occur term "center", "upper", "lower", "left", "right",
The orientation or positional relationship of "vertical", "horizontal", "inner", "outside" etc., instruction is that orientation based on ... shown in the drawings or position are closed
System, is merely for convenience of description of the present invention and simplification of the description, not indicating or implying the indicated device or element must have
Specific orientation, with specific azimuth configuration and operation, therefore be not considered as limiting the invention.In addition, such as there is art
Language " first ", " second ", " third " are used for description purposes only, and are not understood to indicate or imply relative importance.
In the description of the present invention, it should be noted that unless otherwise clearly defined and limited, term " peace such as occur
Dress ", " connected ", " connection " shall be understood in a broad sense, for example, it may be being fixedly connected, may be a detachable connection, or integrally
Connection；It can be mechanical connection, can also be electrical connection；Can be directly connected, can also indirectly connected through an intermediary,
It can be the connection inside two elements.For the ordinary skill in the art, it can understand above-mentioned art with concrete condition
The concrete meaning of language in the present invention.
Embodiment one
Shown in Figure 1, arrow direction indicates the direction that flue gas enters in Fig. 1.A kind of dedusting is present embodiments provided to set
It is standby, including air-intake device, cyclone dust collectors 104, cooling cylinder 103, the first heat transferring medium pipeline 101, absorption type heat pump assembly 105
And steam generation facility；Air-intake device is provided with the gas inlet for entering for flue gas, air-intake device and cyclone dust collectors 104
Air inlet connection；Cyclone dust collectors 104 are located at the inside of cooling cylinder 103, and the first heat transferring medium pipeline 101 is from cooling cylinder 103
In pass through, for cooling down to cyclone dust collectors 104, one end of the first heat transferring medium pipeline 101 and absorption type heat pump assembly 105
Generator is connected to, and the other end of the first heat transferring medium pipeline 101 is connected to the evaporator of absorption type heat pump assembly 105；Steam is sent out
Generating apparatus is connected to the condenser of absorption type heat pump assembly 105 and absorber, and steam generation facility can be with flue gas for generating
Mixed water vapour.
Based on the structure, cleaner provided in this embodiment is mixed using water vapour with flue gas, and to cyclone dust collectors
104 are cooled down so that steam is condensed to form the drop of bigger, under the influence of centrifugal force, particulate matter in flue gas with
Drop is separated, and the phenomenon that being discharged is exported from the purifying smoke of cyclone dust collectors 104 to effectively alleviate particulate matter,
Improve efficiency of dust collection.When implementing, flue gas is passed through air-intake device from gas inlet, starts cyclone dust collectors 104, first changes
The heat inside heat transferring medium absorption condensation case 103 in heat medium pipeline 101, cools down cyclone dust collectors 104, is inhaling
Under the action of receipts formula heat pump unit 105, steam generation facility generates the water vapour that can be mixed with flue gas, and water vapour is mixed with flue gas
It closes, and captures the particulate matter in flue gas, the mixture of flue gas and water vapour enters from air inlet in cyclone dust collectors 104, carries out
It centrifuges, due to the heat inside the heat transferring medium absorption condensation case 103 in the first heat transferring medium pipeline 101, whirlwind is removed
Dirt device 104 is cooled down, so that steam is condensed to form the drop of bigger, under the influence of centrifugal force, in flue gas
Grain object is separated with drop.
It should be noted that the first heat transferring medium in the first heat transferring medium pipeline 101 is refrigerating medium common at present, example
Such as：The aqueous solution etc. of the organic compounds such as water, sodium chloride or calcium chloride salt aqueous solution, ethylene glycol or glycerine.
In certain embodiments, air-intake device includes plenum chamber 106 and blast pipe 107, gas inlet and plenum chamber 106
Air inlet is connected to, and the air outlet of plenum chamber 106 is connected to one end of blast pipe 107, the other end of blast pipe 107 and cyclone dust removal
The air inlet of device 104 is connected to.
By the way that plenum chamber 106 is arranged so that the intake of flue gas evenly distributes, and helps to improve efficiency of dust collection.In addition, logical
Cross setting plenum chamber 106, additionally it is possible to reduce noise, improve the overall performance of cleaner.
In certain embodiments, steam generation facility includes the second heat transferring medium pipeline 102 and sparge pipe 108；Second changes
One end of heat medium pipeline 102 is connected to the condenser of absorption type heat pump assembly 105, the second heat transferring medium pipeline 102 it is another
End is connected to the absorber of absorption type heat pump assembly 105；Sparge pipe 108 is used for 102 water spray of the second heat transferring medium pipeline,
To generate water vapour.
Under the action of absorption type heat pump assembly 105, the temperature of the second heat transferring medium pipeline 102 increases, and sparge pipe 108 will
When water mist sprays to the second heat transferring medium pipeline 102, water mist can vaporize, and generate water vapour, and water vapour can be mixed with flue gas, and
The mixture of particulate matter in capture flue gas, flue gas and water vapour enters from air inlet in cyclone dust collectors 104, carries out centrifugation point
From due to the heat inside the heat transferring medium absorption condensation case 103 in the first heat transferring medium pipeline 101, to cyclone dust collectors 104
Cooled down so that steam is condensed to form the drop of bigger, under the influence of centrifugal force, particulate matter in flue gas with
Drop is separated.
It should be noted that the second heat transferring medium in the second heat transferring medium pipeline 102 is refrigerating medium common at present, example
Such as：The aqueous solution etc. of the organic compounds such as water, sodium chloride or calcium chloride salt aqueous solution, ethylene glycol or glycerine.
In certain embodiments, further include water tank 109, one end of sparge pipe 108 is connected to water tank 109, sparge pipe
108 other end is located at the inside of plenum chamber 106.
By the way that water tank 109 is arranged, it is capable of providing water source, convenient for sparge pipe 108 to outside the second heat transferring medium pipeline 102
Surface water spray, and form water vapour.
In certain embodiments, the other end of sparge pipe 108 is provided with nozzle 110.
By the way that nozzle 110 is arranged, the contact of water mist and 102 cyclone dust collectors 104 of the second heat transferring medium pipeline can be increased
Area, cooling effect are more preferable.
In certain embodiments, further include return pipe 111, one end of return pipe 111 is connected to plenum chamber 106, return pipe
111 other end is connected to water tank 109.
It, can be by the mixture of condensed water and water and flue gas particle in plenum chamber 106 by the way that return pipe 111 is arranged
It is discharged into water tank 109, water is recycled.
Embodiment two
Shown in Figure 2, the present embodiment also provides a kind of cleaner, and the cleaner of the present embodiment describes steam
The technical solution of another implementation of generating means, embodiment one in addition to this also belongs to the embodiment, herein no longer
Repeated description.Identical parts use reference numeral identical with embodiment one, herein with reference to the description to embodiment one.
In the present embodiment, steam generation facility includes the second heat transferring medium pipeline 102 and steam generator 112；Steam is sent out
Raw device 112 is connected to the second heat transferring medium pipeline 102, and the steam (vapor) outlet of steam generator 112 is connected to air-intake device.
It is passed through water source to steam generator 112, after water is contacted with the second heat transferring medium pipeline 102, vaporization forms water vapour,
Water vapour enters plenum chamber 106 by steam (vapor) outlet, is mixed with flue gas, and captures the particulate matter in flue gas, flue gas and water vapour
Mixture enters from air inlet in cyclone dust collectors 104, is centrifuged, due to changing in the first heat transferring medium pipeline 101
Heat inside thermal medium absorption condensation case 103, cools down cyclone dust collectors 104, so that steam is condensed to be formed
The drop of bigger, under the influence of centrifugal force, particulate matter in flue gas are separated with drop.
Embodiment three
Shown in Figure 3, the present embodiment also provides a kind of cleaner, and the cleaner of the present embodiment is in embodiment
The technical solution of improvement on the basis of one, embodiment one in addition to this also belongs to the embodiment, is not repeated to describe herein.
Identical parts use reference numeral identical with embodiment one, herein with reference to the description to embodiment one.
Further include discharge pipe 113 in the present embodiment, discharge pipe 113 and the purifying smoke outlet of cyclone dust collectors 104 connect
It is logical.
In the alternative of the present embodiment, discharge pipe 113 is provided with exhaust fan 114.
By the way that discharge pipe 113 and exhaust fan 114 is arranged, such mode carries convenient for purified flue gas emission is gone out
High purification efficiency.
Example IV
Shown in Figure 4, the present embodiment also provides a kind of cleaner, and the cleaner of the present embodiment is in embodiment
The technical solution of improvement on the basis of two, embodiment two in addition to this also belongs to the embodiment, is not repeated to describe herein.
Identical parts use reference numeral identical with embodiment two, herein with reference to the description to embodiment two.
Further include discharge pipe 113 in the present embodiment, discharge pipe 113 and the purifying smoke outlet of cyclone dust collectors 104 connect
It is logical.
In the alternative of the present embodiment, discharge pipe 113 is provided with exhaust fan 114.
By the way that discharge pipe 113 and exhaust fan 114 is arranged, such mode carries convenient for purified flue gas emission is gone out
High purification efficiency.
Embodiment five
A kind of dust pelletizing system is present embodiments provided, including the cleaner that multiple embodiment of the present invention one provide.
Dust pelletizing system provided in this embodiment, due to the use of the cleaner that multiple embodiment of the present invention one provide, energy
Enough particulate matters of effectively alleviating export the phenomenon that being discharged from the purifying smoke of cyclone dust collectors 104, improve efficiency of dust collection.
It should be noted that dust pelletizing system provided in this embodiment, can also use the embodiment of the present invention two to four to provide
Cleaner.
Finally it should be noted that：The above embodiments are only used to illustrate the technical solution of the present invention., rather than its limitations；To the greatest extent
Present invention has been described in detail with reference to the aforementioned embodiments for pipe, it will be understood by those of ordinary skill in the art that：Its according to
So can with technical scheme described in the above embodiments is modified, either to which part or all technical features into
Row equivalent replacement；And these modifications or replacements, various embodiments of the present invention technology that it does not separate the essence of the corresponding technical solution
The range of scheme.
Claims (10)
1. a kind of cleaner, which is characterized in that including air-intake device, cyclone dust collectors, cooling cylinder, the first heat transferring medium pipe
Road, absorption type heat pump assembly and steam generation facility；
The air-intake device is provided with the gas inlet for entering for flue gas, the air-intake device and the cyclone dust collectors
Air inlet is connected to；
The cyclone dust collectors are located at the inside of the cooling cylinder, and the first heat transferring medium pipeline is worn from the cooling cylinder
It crosses, for cooling down to the cyclone dust collectors, one end of the first heat transferring medium pipeline and the absorption type heat pump assembly
Generator is connected to, and the other end of the first heat transferring medium pipeline is connected to the evaporator of the absorption type heat pump assembly；
The steam generation facility is connected to the condenser of the absorption type heat pump assembly and absorber, the steam generation facility
For generating the water vapour that can be mixed with the flue gas.
2. cleaner according to claim 1, which is characterized in that the air-intake device includes plenum chamber and blast pipe,
The gas inlet is connected to the air inlet of the plenum chamber, and the air outlet of the plenum chamber and one end of the blast pipe connect
Logical, the other end of the blast pipe is connected to the air inlet of the cyclone dust collectors.
3. cleaner according to claim 2, which is characterized in that the steam generation facility includes the second heat transferring medium
Pipeline and sparge pipe；
One end of the second heat transferring medium pipeline is connected to the condenser of the absorption type heat pump assembly, and second heat exchange is situated between
The other end of matter pipeline is connected to the absorber of the absorption type heat pump assembly；
The sparge pipe is used for the second heat transferring medium pipeline water spray, to generate water vapour.
4. cleaner according to claim 2, which is characterized in that the steam generation facility includes the second heat transferring medium
Pipeline and steam generator；
The steam generator and the second heat transferring medium pipeline connection, the steam (vapor) outlet of the steam generator with it is described into
Wind apparatus is connected to.
5. cleaner according to claim 3, which is characterized in that further include water tank, one end of the sparge pipe with
The water tank connection, the other end of the sparge pipe are located at the inside of the plenum chamber.
6. cleaner according to claim 5, which is characterized in that the other end of the sparge pipe is provided with nozzle.
7. cleaner according to claim 5, which is characterized in that further include return pipe, one end of the return pipe with
The plenum chamber connection, the other end of the return pipe are connected to the water tank.
8. cleaner according to any one of claim 1 to 7, which is characterized in that further include discharge pipe, the outlet air
The purifying smoke outlet of pipe and the cyclone dust collectors.
9. cleaner according to claim 8, which is characterized in that the discharge pipe is provided with exhaust fan.
10. a kind of dust pelletizing system, which is characterized in that including multiple cleaners as claimed in any one of claims 1-9 wherein.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810597625.9A CN108636044A (en) | 2018-06-11 | 2018-06-11 | Cleaner and dust pelletizing system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810597625.9A CN108636044A (en) | 2018-06-11 | 2018-06-11 | Cleaner and dust pelletizing system |
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| CN108636044A true CN108636044A (en) | 2018-10-12 |
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| CN201810597625.9A Pending CN108636044A (en) | 2018-06-11 | 2018-06-11 | Cleaner and dust pelletizing system |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109621597A (en) * | 2019-01-25 | 2019-04-16 | 江苏师范大学 | Dedusting and purifying air system |
| CN109745800A (en) * | 2019-01-25 | 2019-05-14 | 江苏师范大学 | Dedusting system |
| CN109939515A (en) * | 2019-01-25 | 2019-06-28 | 江苏师范大学 | Gas cooling container |
| CN113198278A (en) * | 2021-04-21 | 2021-08-03 | 江苏科技大学 | Steam dust removal system and working method thereof |
Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2008023511A (en) * | 2006-07-20 | 2008-02-07 | Ogura Tekko Kk | Waste gas treatment apparatus for steam cleaning apparatus |
| CN201722345U (en) * | 2010-06-08 | 2011-01-26 | 山东万丰煤化工设备制造有限公司 | Cyclone dust removal heat exchanger used for gas producer |
| CN102287841A (en) * | 2011-06-26 | 2011-12-21 | 华北电力大学（保定） | Method for smoke discharge, condensation and dust removal of supercharged oxygen-enriched coal-fired boiler |
| CN204769207U (en) * | 2015-07-01 | 2015-11-18 | 浙江诸暨利达环保设备有限公司 | Novel cyclone |
| CN105546564A (en) * | 2016-01-06 | 2016-05-04 | 浙江浙能节能科技有限公司 | Energy-saving recycling system for low-grade heat energy in smoke pollutant treatment of thermal power plant |
| CN106091212A (en) * | 2016-06-23 | 2016-11-09 | 山东大学 | New wind air cleaning system and the method for PM2.5 is removed based on flocculation core |
| CN206771587U (en) * | 2016-11-17 | 2017-12-19 | 吴庆民 | A kind of heating cooling heat pump with function of purifying indoor air |
| CN107726337A (en) * | 2017-11-17 | 2018-02-23 | 林庆樵 | A kind of smoke processing system of garbage disposal furnace |
| CN208482202U (en) * | 2018-06-11 | 2019-02-12 | 兰州大学 | Cleaner and dust pelletizing system |
-
2018
- 2018-06-11 CN CN201810597625.9A patent/CN108636044A/en active Pending
Patent Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2008023511A (en) * | 2006-07-20 | 2008-02-07 | Ogura Tekko Kk | Waste gas treatment apparatus for steam cleaning apparatus |
| CN201722345U (en) * | 2010-06-08 | 2011-01-26 | 山东万丰煤化工设备制造有限公司 | Cyclone dust removal heat exchanger used for gas producer |
| CN102287841A (en) * | 2011-06-26 | 2011-12-21 | 华北电力大学（保定） | Method for smoke discharge, condensation and dust removal of supercharged oxygen-enriched coal-fired boiler |
| CN204769207U (en) * | 2015-07-01 | 2015-11-18 | 浙江诸暨利达环保设备有限公司 | Novel cyclone |
| CN105546564A (en) * | 2016-01-06 | 2016-05-04 | 浙江浙能节能科技有限公司 | Energy-saving recycling system for low-grade heat energy in smoke pollutant treatment of thermal power plant |
| CN106091212A (en) * | 2016-06-23 | 2016-11-09 | 山东大学 | New wind air cleaning system and the method for PM2.5 is removed based on flocculation core |
| CN206771587U (en) * | 2016-11-17 | 2017-12-19 | 吴庆民 | A kind of heating cooling heat pump with function of purifying indoor air |
| CN107726337A (en) * | 2017-11-17 | 2018-02-23 | 林庆樵 | A kind of smoke processing system of garbage disposal furnace |
| CN208482202U (en) * | 2018-06-11 | 2019-02-12 | 兰州大学 | Cleaner and dust pelletizing system |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109621597A (en) * | 2019-01-25 | 2019-04-16 | 江苏师范大学 | Dedusting and purifying air system |
| CN109745800A (en) * | 2019-01-25 | 2019-05-14 | 江苏师范大学 | Dedusting system |
| CN109939515A (en) * | 2019-01-25 | 2019-06-28 | 江苏师范大学 | Gas cooling container |
| CN109745800B (en) * | 2019-01-25 | 2021-06-18 | 江苏师范大学 | Gas dust removal system |
| CN109939515B (en) * | 2019-01-25 | 2021-06-18 | 江苏师范大学 | Mechanical rotation type bubble generator and environment-friendly gas dust removal device |
| CN113198278A (en) * | 2021-04-21 | 2021-08-03 | 江苏科技大学 | Steam dust removal system and working method thereof |
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