CN109045918A - A kind of air cleaning and wet flue gas dehumidification device - Google Patents
A kind of air cleaning and wet flue gas dehumidification device Download PDFInfo
- Publication number
- CN109045918A CN109045918A CN201811093414.8A CN201811093414A CN109045918A CN 109045918 A CN109045918 A CN 109045918A CN 201811093414 A CN201811093414 A CN 201811093414A CN 109045918 A CN109045918 A CN 109045918A
- Authority
- CN
- China
- Prior art keywords
- flue gas
- wet flue
- unit
- air
- storehouse
- 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.)
- Granted
Links
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 title claims abstract description 82
- 239000003546 flue gas Substances 0.000 title claims abstract description 82
- 238000007791 dehumidification Methods 0.000 title claims abstract description 60
- 238000004140 cleaning Methods 0.000 title claims abstract description 39
- 239000007921 spray Substances 0.000 claims abstract description 45
- 238000011044 inertial separation Methods 0.000 claims abstract description 41
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 32
- 238000009833 condensation Methods 0.000 claims abstract description 30
- 230000005494 condensation Effects 0.000 claims abstract description 30
- 238000001816 cooling Methods 0.000 claims description 7
- 230000008676 import Effects 0.000 claims description 7
- 238000005507 spraying Methods 0.000 claims description 4
- 238000000889 atomisation Methods 0.000 claims 1
- 239000011799 hole material Substances 0.000 claims 1
- 238000000034 method Methods 0.000 abstract description 12
- 238000000746 purification Methods 0.000 abstract description 12
- 239000003595 mist Substances 0.000 abstract description 9
- 238000000926 separation method Methods 0.000 abstract description 8
- 230000008569 process Effects 0.000 abstract description 7
- 230000018044 dehydration Effects 0.000 abstract description 3
- 238000006297 dehydration reaction Methods 0.000 abstract description 3
- 239000008398 formation water Substances 0.000 abstract 1
- 239000000428 dust Substances 0.000 description 7
- 238000005516 engineering process Methods 0.000 description 7
- 239000007789 gas Substances 0.000 description 7
- 239000002245 particle Substances 0.000 description 7
- 230000000694 effects Effects 0.000 description 6
- 238000010586 diagram Methods 0.000 description 5
- 238000001914 filtration Methods 0.000 description 4
- 238000002156 mixing Methods 0.000 description 4
- 238000005201 scrubbing Methods 0.000 description 4
- 239000007787 solid Substances 0.000 description 4
- 238000004887 air purification Methods 0.000 description 3
- 239000011148 porous material Substances 0.000 description 3
- 238000010521 absorption reaction Methods 0.000 description 2
- 235000019504 cigarettes Nutrition 0.000 description 2
- 238000009792 diffusion process Methods 0.000 description 2
- 239000003344 environmental pollutant Substances 0.000 description 2
- 230000007246 mechanism Effects 0.000 description 2
- 231100000719 pollutant Toxicity 0.000 description 2
- 238000005406 washing Methods 0.000 description 2
- 230000009471 action Effects 0.000 description 1
- 238000003915 air pollution Methods 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 238000006477 desulfuration reaction Methods 0.000 description 1
- 230000023556 desulfurization Effects 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 230000002708 enhancing effect Effects 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 230000001939 inductive effect Effects 0.000 description 1
- 239000002440 industrial waste Substances 0.000 description 1
- 238000002955 isolation Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 239000013618 particulate matter Substances 0.000 description 1
- FGIUAXJPYTZDNR-UHFFFAOYSA-N potassium nitrate Chemical compound [K+].[O-][N+]([O-])=O FGIUAXJPYTZDNR-UHFFFAOYSA-N 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 239000000779 smoke Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Classifications
-
- 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
- B01D50/10—Combinations of devices covered by groups B01D45/00, B01D46/00 and B01D47/00
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/002—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by condensation
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2258/00—Sources of waste gases
- B01D2258/06—Polluted air
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Treating Waste Gases (AREA)
- Separating Particles In Gases By Inertia (AREA)
- Separation Of Particles Using Liquids (AREA)
Abstract
The present invention discloses a kind of air cleaning and wet flue gas dehumidification device, wet flue gas initially enters spray mixed cell, cool down after spray head sprays and is sufficiently mixed with spray water mist, mixed wet flue gas enters high speed stripping unit, pure air centrifugal force is small, stopped by storehouse in high-speed rotating removing, directly it is discharged by exhaust passage, partial air and droplet pass through remove in storehouse be thrown toward and remove the inner wall formation water flow in outer storehouse and flow down, part fine mist and air form the higher air stream of water capacity, into dehumidification by condensation unit, dehydration in air forms moisture film and water flow, wet flue gas still containing part fine drop is finally imported into inertial separation unit and implements separation, treated pure air is discharged via exhaust passage, complete the overall process of wet flue gas dehumidifying and air cleaning.Entire purification dehumidification process windage is lower, meets the requirement of flow at high speed, big handling capacity processing wet flue gas, and dehumidifies while purifying air to wet flue gas.
Description
Technical field
The present invention relates to technical field of air purification, more particularly to a kind of air cleaning and wet flue gas dehumidification device.
Background technique
In recent years, it is got worse the problem of air pollution, there are many existing air purifying process type, for example, filtering technique,
Scrubbing tower, moisture film fresh air technology, using cyclone dust removal as inertial separation dedusting technology of representative etc..Wherein, the inertia of cyclone dust removal
Isolation technics is to complete air cleaning operation using the high-speed motion mechanism of fluid, and other purification techniques are all or actively or passively
Air purifying operation is realized as condition to reduce flow velocity in ground.Filtering technique is by the interception of filter medium, inertia, diffusion, again
The retention of the effects such as power, electrostatic and absorption suspended particulate, allow pure air to pass through, but filtering technique passively improves wind
Resistance improves air purification efficiency and precision as cost to reduce air velocity.Scrubbing tower, moisture film technology purification techniques, are chiefly used in
Combustion tail gas, chemical industry and indoor air purification, in scrubbing tower, eminence atomizer is spraying downwards, and washing water flow is in weight
Power effect is lower to be in contact with each other chance along the air reverse flow increase that filler is flowed downward and flowed up, by water flow absorption and band
The impurity component in air is walked, but speed air flow cannot be excessively high, in case washing water is entrained by the flow of air, so, scrubbing tower is past
Air velocity is initiatively reduced toward enlarged diameter.Cyclone dust removal mechanism is that dust-contained airflow is made to rotate, by means of centrifugal force
Grit is separated to from air-flow and is trapped in wall, then so that grit is fallen into ash bucket by gravity, cyclone dust collection technology needs
Air-flow high-speed motion increases centrifugal force, expands the otherness separation and purification air of suspended particulate and air in terms of centrifugal force,
The bulky grain effect that cyclone dust collectors separate in air is good, lower to the separative efficiency of lesser solid particle.
High-temperature flue gas is also the one of the major reasons for causing haze, wet flue gas refer to largely discharge contain vapor, liquid
The industrial waste gas of state particle, for example, coal-fired flue-gas contains the water capacity of a large amount of desulphurization denitration solution after wet desulphurization denitration
Higher flue gas, wet flue gas have the characteristics that saturation water capacity is big, temperature is high and complicated component, are formed after wet desulphurization denitration
Eye-catching " white plumage cigarette " can be formed on high from the exhaust gas of smoke stack emission, this is by taking off in flue gas containing the desulfurization being largely saturated
Caused by nitre solution, these solution are spread in the sky, form long diffusion pinniform white flow of flue gas, and white plumage cigarette carries
Considerable desulphurization denitration solution, steam will appear the indiscoverable a large amount of fine solid particle objects of naked eyes and drifts with the wind after disappearing.It is existing
There is the air cleaning unit in technology while purifying air particle, cannot be considered in terms of wet flue gas takes off white processing.
Therefore, how to change in the prior art, common purifying device can not combine high temperature wet flue gas and big flow is more
Component pollutes the status of air-treatment, is those skilled in the art's urgent problem to be solved.
Summary of the invention
The object of the present invention is to provide a kind of air cleaning and wet flue gas dehumidification devices, exist to solve the above-mentioned prior art
The problem of, so that purification device is dehumidified high temperature wet flue gas, while air can be polluted to big flow multicomponent and carried out
Purification.
To achieve the above object, the present invention provides following schemes: the present invention provides a kind of air cleaning and wet flue gas removes
Wet device, including the spray mixed cell being connected and high speed stripping unit, the spray mixed cell is connected with inlet pipeline
It is logical, spray head is provided in the spray mixed cell, the spray mixed cell can carry out spray drop to the wet flue gas of introducing
Temperature, the high speed stripping unit are connected with exhaust passage；The high speed stripping unit includes storehouse in removing outer storehouse and removing, described
The outside that outer storehouse is sleeved on storehouse in the removing is removed, there is gap between storehouse in the outer storehouse of the removing and the removing, it is described
Filter medium is set on the side wall in storehouse in removing, storehouse can rotate in the removing, the spray mixed cell and the exhaust
Channel is connected with the inner cavity in storehouse in the removing；
The outer storehouse of the removing is connected with the gap between storehouse in the removing with dehumidification by condensation unit, the dehumidification by condensation
Unit can enable the condensate moisture in flue gas, and the dehumidification by condensation unit is connected with inertial separation unit, the inertial separation list
Member can separate the drop in wet flue gas, and the outlet of the inertial separation unit is connected with the exhaust passage.
Preferably, air cleaning and wet flue gas dehumidification device further include secondary stripping unit, the outlet of the exhaust passage
It is connected with the secondary stripping unit, the secondary stripping unit is identical as the structure of the high speed stripping unit.
Preferably, air cleaning and wet flue gas dehumidification device further include secondary inertial separation unit, the exhaust passage
Outlet is connected with the secondary inertial separation unit, the structure of the secondary inertial separation unit and the inertial separation unit
It is identical.
Preferably, import air-introduced machine is set at the inlet pipeline, and setting air vacuum pumps at the exhaust passage.
Preferably, air cleaning and wet flue gas dehumidification device further include confluence pond, the high speed stripping unit, the condensation
Dehumidifying element and the inertial separation unit are connected with the confluence pond respectively.
Preferably, the filter medium is porous material.
Preferably, it is connected at the top of the high speed stripping unit and the dehumidification by condensation unit, the dehumidification by condensation list
The bottom of member is connected with the inertial separation unit, and more condenser pipes, the condenser pipe are arranged in the dehumidification by condensation unit
Between have gap.
Preferably, the spray head is atomizer, and the atomizer is connected with external water source.
The present invention achieves following technical effect compared with the existing technology: air cleaning of the invention and wet flue gas dehumidifying dress
It sets, including the spray mixed cell being connected and high speed stripping unit, sprays mixed cell and be connected with inlet pipeline, spray is mixed
It closes and is provided with spray head in unit, spray mixed cell can carry out spraying cooling to the wet flue gas of introducing, and high speed stripping unit connects
It is connected to exhaust passage；High speed stripping unit includes storehouse in removing outer storehouse and removing, and removes outer storehouse and is sleeved on the outside for removing interior storehouse,
Removing outer storehouse and removing has gap between interior storehouse, filter medium is arranged in removing on the side wall in storehouse, and removing interior storehouse can rotate,
Spray mixed cell and exhaust passage are connected with the inner cavity for removing interior storehouse；Gap in removing outer storehouse and removing between storehouse and
Dehumidification by condensation unit is connected, and dehumidification by condensation unit can enable the condensate moisture in flue gas, and dehumidification by condensation unit is connected with inertia
Separative unit, inertial separation unit can separate the drop in wet flue gas, and the outlet and exhaust of inertial separation unit are logical
Road is connected.Wet flue gas initially enters spray mixed cell, cools down after spray head sprays and is sufficiently mixed with spray water mist, mixes
Wet flue gas afterwards enters high speed stripping unit, and pure air centrifugal force is small, is stopped by storehouse in high-speed rotating removing, directly by arranging
The discharge of gas channel, partial air and droplet pass through remove in storehouse be thrown toward and remove the inner wall in outer storehouse and form water flow and flow down, partially carefully
Small droplet and air form the higher air stream of water capacity, and into dehumidification by condensation unit, the dehydration in air forms moisture film
And water flow, the wet flue gas still containing part fine drop is finally imported into inertial separation unit and implements separation, treated pure
Net air is discharged via exhaust passage, completes the overall process of wet flue gas dehumidifying and air cleaning.Entire purification dehumidification process wind
It hinders lower, meets the requirement of flow at high speed, big handling capacity processing wet flue gas, and wet flue gas is removed while purifying air
It is wet.
Detailed description of the invention
It in order to more clearly explain the embodiment of the invention or the technical proposal in the existing technology, below will be to institute in embodiment
Attached drawing to be used is needed to be briefly described, it should be apparent that, the accompanying drawings in the following description is only some implementations of the invention
Example, for those of ordinary skill in the art, without any creative labor, can also be according to these attached drawings
Obtain other attached drawings.
Fig. 1 is the overall structure diagram of air cleaning of the invention and wet flue gas dehumidification device；
Fig. 2 is the overall structure signal in air cleaning of the invention and wet flue gas dehumidification device other specific embodiments
Figure；
Fig. 3 is the overall structure signal in air cleaning of the invention and another specific embodiment of wet flue gas dehumidification device
Figure；
Overall structure diagram when Fig. 4 is air cleaning of the invention and wet flue gas dehumidification device raising efficiency of dust collection.
Wherein, 1 is spray mixed cell, and 2 be high speed stripping unit, and 3 be dehumidification by condensation unit, and 4 be inertial separation unit,
5 be import air-introduced machine, and 6 be exhaust passage, and 7 be storehouse in removing, and 8 pump to remove outer storehouse, 9 for air vacuum, and 10 be pond of converging, 11
It is secondary inertial separation unit for secondary stripping unit, 12.
Specific embodiment
Following will be combined with the drawings in the embodiments of the present invention, and technical solution in the embodiment of the present invention carries out clear, complete
Site preparation description, it is clear that described embodiments are only a part of the embodiments of the present invention, instead of all the embodiments.It is based on
Embodiment in the present invention, it is obtained by those of ordinary skill in the art without making creative efforts every other
Embodiment shall fall within the protection scope of the present invention.
The object of the present invention is to provide a kind of air cleaning and wet flue gas dehumidification devices, exist to solve the above-mentioned prior art
The problem of, so that purification device is dehumidified high temperature wet flue gas, while air can be polluted to big flow multicomponent and carried out
Purification.
In order to make the foregoing objectives, features and advantages of the present invention clearer and more comprehensible, with reference to the accompanying drawing and specific real
Applying mode, the present invention is described in further detail.
Please refer to Fig. 1-4, wherein Fig. 1 is air cleaning of the invention and the overall structure signal of wet flue gas dehumidification device
Figure, Fig. 2 are the overall structure diagram in air cleaning of the invention and wet flue gas dehumidification device other specific embodiments, figure
3 be the overall structure diagram in air cleaning of the invention and another specific embodiment of wet flue gas dehumidification device, and Fig. 4 is this
The air cleaning of invention and wet flue gas dehumidification device improve overall structure diagram when efficiency of dust collection.
The present invention provides a kind of air cleaning and wet flue gas dehumidification device, including the spray mixed cell 1 and height being connected
Fast stripping unit 2, spray mixed cell 1 are connected with inlet pipeline, spray and are provided with spray head in mixed cell 1, spray mixing
Unit 1 can carry out spraying cooling to the wet flue gas of introducing, and high speed stripping unit 2 is connected with exhaust passage 6；High speed stripping unit
2 include removing storehouse 7 in inside and outside storehouse 8 and removing, removes inside and outside storehouse 8 and is sleeved on the outside for removing interior storehouse 7, removes inside and outside storehouse 8 and stripping
It from having gap between interior storehouse 7, removes and filter medium is set on 7 side wall of interior storehouse, removing interior storehouse 7 can rotate, spray mixing list
Member 1 and exhaust passage 6 are connected with the inner cavity for removing interior storehouse 7；Gap in removing inside and outside storehouse 8 and removing between storehouse 7 with it is cold
Solidifying Dehumidifying element 3 is connected, and dehumidification by condensation unit 3 can enable the condensate moisture in flue gas, and dehumidification by condensation unit 3 is connected with inertia
Separative unit 4, inertial separation unit 4 can separate the drop in wet flue gas, the outlet and exhaust of inertial separation unit 4
Channel 6 is connected.
Wet flue gas is first directed to spray mixed cell 1, cools down after spray head sprays and is sufficiently mixed with spray water mist, mixes
Wet flue gas afterwards enters high speed stripping unit 2, and pure air centrifugal force is small, is stopped by storehouse 7 in high-speed rotating removing, directly by
Exhaust passage 6 is discharged, and partial air and the droplet filter medium in storehouse 7 in removing are thrown toward the inner wall shape for removing inside and outside storehouse 8
It is flowed down at water flow, part fine mist and air form the higher air stream of water capacity, into dehumidification by condensation unit 3, in air
Dehydration form moisture film and water flow, it is real that the wet flue gas still containing part fine drop is finally imported into inertial separation unit 4
Separation is applied, treated pure air is discharged via exhaust passage 6, completes the full mistake of wet flue gas dehumidifying and air cleaning
Journey.Entire purification dehumidification process windage is lower, meets the requirement of flow at high speed, big handling capacity processing wet flue gas, and empty in purification
It dehumidifies while gas to wet flue gas.Herein it should be noted that being in the prior art used by inertial separation unit 4
Inertial separation machine, when using air-flow reef it in or with the collision such as baffle, the operation that particle is separated from air-flow,
The separation of fine drop is completed, therefore, details are not described herein again for the specific structure of inertial separation unit 4.
In other specific embodiments of the invention, white efficiency is taken off in order to further increase air cleaning and wet flue gas,
Air cleaning and wet flue gas dehumidification device further include secondary stripping unit 11, the outlet of exhaust passage 6 and secondary stripping unit 11
It is connected, secondary spin-drying can be carried out to air derived from exhaust passage 6, by untreated clean drop and particulate pollutant
Further separation, is discharged clean air, and secondary stripping unit 11 is identical as the structure of high speed stripping unit 2.
In another embodiment of the present invention, for the purposes of further increasing to further increase air cleaning
And wet flue gas takes off white efficiency, air cleaning and wet flue gas dehumidification device further include secondary inertial separation unit 12, exhaust passage 6
Outlet is connected with secondary inertial separation unit 12, carries out secondary inertial separation to air derived from exhaust passage 6, can also be used
Untreated clean drop and particulate pollutant are made further separating treatment by cyclonic separation machine, improve degree of purification, and two
Secondary inertial separation unit 12 is identical as the structure of inertial separation unit 4.
It should be noted that it is higher to form water capacity via part fine mist derived from high speed stripping unit 2 and air
Air stream, can also first import inertial separation unit 4, since water capacity is higher, the more former solid particle size of drop increases, and is easy
Attachment film forming, 4 efficiency of inertial separation unit greatly improve, and are conducive to inhibit solid particle secondary precipitation, enhancing air cleaning effect
Rate specifically please refers to Fig. 4.
Specifically, import air-introduced machine 5 is set at inlet pipeline, and setting air vacuum pumps 9 at exhaust passage 6, passes through air inducing
Power traction stream, and water conservancy diversion is carried out to air using the negative pressure that air vacuum pump 9 generates, make wet flue gas smooth flow.
More specifically, air cleaning and wet flue gas dehumidification device further include confluence pond 10, high speed stripping unit 2, condensation are removed
Wet unit 3 and inertial separation unit 4 are connected with confluence pond 10 respectively, high speed stripping unit 2, dehumidification by condensation unit 3 and inertia
The mixing water that separative unit 4 flows out is gathered in confluence pond 10, and the mixed liquor a part collected in pond 10 of converging is handled through cooling
After can be re-used as shower water, rest part discharges outward.
In this embodiment, filter medium is the porous material of large specific surface area, and porous material is the prior art,
It is not elaborated herein.
Further, high speed stripping unit 2 is connected with the top of dehumidification by condensation unit 3, the bottom of dehumidification by condensation unit 3
It is connected with inertial separation unit 4, more condenser pipes is set in dehumidification by condensation unit 3, there is gap between condenser pipe.
Spray head is atomizer, and atomizer is connected with external water source.Atomizer enhance spray water mist and gas and
The exposure level of particulate matter improves cooling efficiency.
High temperature wet flue gas experienced spray mixed cell 1, high speed stripping unit 2, dehumidification by condensation unit 3 and inertial separation list
Member 4.The wet flue gas of introducing initially enters spray mixed cell 1 under the action of air-introduced machine, and wet flue gas is cooled down, and and shower water
Mist is sufficiently mixed；Mixed wet flue gas imports high speed stripping unit 2, and pure air centrifugal force is small, by high-speed rotating filtering
Dielectric impedance, square exhaust passage 6 is discharged directly up, droplet and partial air pass through remove in storehouse 7 filter medium get rid of to
The inner sidewall for removing inside and outside storehouse 8 forms downlink water flow, and part fine mist and air form the higher air stream of water capacity, empty
9 suction function of gas vacuum pump imports dehumidification by condensation unit 3, and the moisture in air is precipitated under the cooling effect of cooling tube forms water
Film and downlink water flow；Wet flue gas still containing part fine drop is finally imported into inertial separation unit 4 and implements separation, by place
The pure air of reason by the pure air of exhaust passage 6 and high speed stripping unit 2 converge so complete wet flue gas removing take off it is white
Overall process, converges from the outflux of the lower part of several units and shower water and wet flue gas out takes off white mixing water and concentrate on converging
Pond 10.
Specific examples are applied in the present invention, and principle and implementation of the present invention are described, above embodiments
Illustrate to be merely used to help understand method and its core concept of the invention；At the same time, for those skilled in the art, according to
According to thought of the invention, there will be changes in the specific implementation manner and application range.In conclusion the content of the present specification
It should not be construed as limiting the invention.
Claims (8)
1. a kind of air cleaning and wet flue gas dehumidification device, it is characterised in that: including the spray mixed cell being connected and high speed
Stripping unit, the spray mixed cell are connected with inlet pipeline, are provided with spray head, the spray in the spray mixed cell
Spraying cooling can be carried out to the wet flue gas of introducing by drenching mixed cell, and the high speed stripping unit is connected with exhaust passage；It is described
High speed stripping unit includes storehouse in removing outer storehouse and removing, and the outer storehouse of the removing is sleeved on the outside in storehouse in the removing, described
Removing has gap between storehouse in outer storehouse and the removing, filter medium, the removing is arranged on the side wall in storehouse in the removing
Interior storehouse can rotate, and the spray mixed cell and the exhaust passage are connected with the inner cavity in storehouse in the removing；
The outer storehouse of the removing is connected with the gap between storehouse in the removing with dehumidification by condensation unit, the dehumidification by condensation unit
The condensate moisture in flue gas can be enabled, the dehumidification by condensation unit is connected with inertial separation unit, the inertial separation unit energy
Enough to separate to the drop in wet flue gas, the outlet of the inertial separation unit is connected with the exhaust passage.
2. air cleaning according to claim 1 and wet flue gas dehumidification device, it is characterised in that: further include that secondary removing is single
Member, the outlet of the exhaust passage are connected with the secondary stripping unit, and the secondary stripping unit and the high speed are removed
The structure of unit is identical.
3. air cleaning according to claim 1 and wet flue gas dehumidification device, it is characterised in that: further include secondary inertia point
From unit, the outlet of the exhaust passage is connected with the secondary inertial separation unit, the secondary inertial separation unit with
The structure of the inertial separation unit is identical.
4. air cleaning according to claim 1 and wet flue gas dehumidification device, it is characterised in that: set at the inlet pipeline
Import air-introduced machine is set, setting air vacuum pumps at the exhaust passage.
5. air cleaning according to claim 1 and wet flue gas dehumidification device, it is characterised in that: further include confluence pond, institute
High speed stripping unit, the dehumidification by condensation unit and the inertial separation unit is stated to be connected with the confluence pond respectively.
6. air cleaning according to claim 1 and wet flue gas dehumidification device, it is characterised in that: the filter medium is more
Hole material.
7. air cleaning according to claim 1 and wet flue gas dehumidification device, it is characterised in that: the high speed stripping unit
It is connected at the top of the dehumidification by condensation unit, the bottom of the dehumidification by condensation unit is connected with the inertial separation unit
It is logical, more condenser pipes are set in the dehumidification by condensation unit, there is gap between the condenser pipe.
8. air cleaning according to claim 1 and wet flue gas dehumidification device, it is characterised in that: the spray head is atomization spray
Head, the atomizer are connected with external water source.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811093414.8A CN109045918B (en) | 2018-09-19 | 2018-09-19 | Air purification and wet flue gas dehumidification device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811093414.8A CN109045918B (en) | 2018-09-19 | 2018-09-19 | Air purification and wet flue gas dehumidification device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN109045918A true CN109045918A (en) | 2018-12-21 |
| CN109045918B CN109045918B (en) | 2021-06-01 |
Family
ID=64763074
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201811093414.8A Active CN109045918B (en) | 2018-09-19 | 2018-09-19 | Air purification and wet flue gas dehumidification device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN109045918B (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111569578A (en) * | 2020-05-27 | 2020-08-25 | 刘毅 | Fog stripping fan and dynamic demisting system |
| CN114558384A (en) * | 2022-03-28 | 2022-05-31 | 北京亿华通科技股份有限公司 | Gas-liquid separation device with visual gas flow |
Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4110088A (en) * | 1976-06-18 | 1978-08-29 | Cold David M | Apparatus and method for removal of pollutants from flue gas |
| CN2552584Y (en) * | 2001-12-18 | 2003-05-28 | 周明连 | Tubular purifier |
| JP2004337694A (en) * | 2003-05-14 | 2004-12-02 | Takayoshi Imai | Dehumidification apparatus |
| CN102481504A (en) * | 2009-06-11 | 2012-05-30 | Ntnu技术转移股份有限公司 | A separator for a gas/liquid flow |
| CN102580408A (en) * | 2012-03-20 | 2012-07-18 | 杨东进 | Active centrifugal gas-liquid separation device |
| CN204447666U (en) * | 2015-02-05 | 2015-07-08 | 陈相荣 | A kind of smoke condensation device with dust-removal and desulfurizing denitration function |
| CN105107352A (en) * | 2015-07-21 | 2015-12-02 | 无锡翱翔环保机械有限公司 | Wet two-stage cyclone desulfurization tower |
-
2018
- 2018-09-19 CN CN201811093414.8A patent/CN109045918B/en active Active
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4110088A (en) * | 1976-06-18 | 1978-08-29 | Cold David M | Apparatus and method for removal of pollutants from flue gas |
| CN2552584Y (en) * | 2001-12-18 | 2003-05-28 | 周明连 | Tubular purifier |
| JP2004337694A (en) * | 2003-05-14 | 2004-12-02 | Takayoshi Imai | Dehumidification apparatus |
| CN102481504A (en) * | 2009-06-11 | 2012-05-30 | Ntnu技术转移股份有限公司 | A separator for a gas/liquid flow |
| CN102580408A (en) * | 2012-03-20 | 2012-07-18 | 杨东进 | Active centrifugal gas-liquid separation device |
| CN204447666U (en) * | 2015-02-05 | 2015-07-08 | 陈相荣 | A kind of smoke condensation device with dust-removal and desulfurizing denitration function |
| CN105107352A (en) * | 2015-07-21 | 2015-12-02 | 无锡翱翔环保机械有限公司 | Wet two-stage cyclone desulfurization tower |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111569578A (en) * | 2020-05-27 | 2020-08-25 | 刘毅 | Fog stripping fan and dynamic demisting system |
| CN114558384A (en) * | 2022-03-28 | 2022-05-31 | 北京亿华通科技股份有限公司 | Gas-liquid separation device with visual gas flow |
| CN114558384B (en) * | 2022-03-28 | 2024-03-22 | 北京亿华通科技股份有限公司 | Visual gas-liquid separation of air current |
Also Published As
| Publication number | Publication date |
|---|---|
| CN109045918B (en) | 2021-06-01 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN103736354B (en) | The round-the-clock wet dust separater of scavenging vehicle and combination dust removal process method | |
| US20140182453A1 (en) | Centrifugal wet type cleaner | |
| CN202427310U (en) | Water curtain type dust and waste gas treatment device | |
| CN105797524A (en) | Heteropolar electric charge fogdrop coalescence dust-removing device and method thereof | |
| CN104906896A (en) | Cloud type dust removal system | |
| CN103157561B (en) | Wet type multicyclone and the dust pelletizing system with above-mentioned deduster | |
| CN107789970A (en) | A kind of box type air purifyer | |
| CN203935739U (en) | A kind of device for air cleaning | |
| CN206577585U (en) | A kind of lead smelting exhaust processing system | |
| CN208990512U (en) | A kind of flue gas of wet desulphurization disappears white system | |
| CN107096344A (en) | A kind of industrial waste gas and floating outstanding particle purifying processing system | |
| CN204051344U (en) | A kind of dusting desulfurizing integrated machine | |
| CN109045918A (en) | A kind of air cleaning and wet flue gas dehumidification device | |
| CN104190190A (en) | Dedusting and desulfurization integrated machine | |
| CN107485951B (en) | A kind of bag filter | |
| CN104524916B (en) | A kind of gas purification dust collection method | |
| CN108554085A (en) | A kind of air purification method and its purifier removed PM2.5 and realize indoor and outdoor air purification convection current | |
| CN102512901B (en) | Composite dust-removing and collaborative desulfurization and denitration device capable of wetting flue gas | |
| CN207786317U (en) | A kind of Jenner's moral box type air purifyer | |
| CN205084534U (en) | Small -size tertiary defroster | |
| CN203724963U (en) | All-weather wet type dust removing device for sweeper | |
| CN207203660U (en) | A kind of vertical demister | |
| CN108159850A (en) | A kind of cold stripper of water mist fluid and dehumidifying demister and its dehumidifying defogging method | |
| CN206572625U (en) | Electrostatic spray is combined wet filter system | |
| CN205379776U (en) | Wet process sprays whirl integration air purification device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| GR01 | Patent grant | ||
| GR01 | Patent grant |