CN106807159A - The vaporous matter treating device of wet type - Google Patents
The vaporous matter treating device of wet type Download PDFInfo
- Publication number
- CN106807159A CN106807159A CN201610943422.1A CN201610943422A CN106807159A CN 106807159 A CN106807159 A CN 106807159A CN 201610943422 A CN201610943422 A CN 201610943422A CN 106807159 A CN106807159 A CN 106807159A
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- vaporous
- water
- process chamber
- storage tank
- aqua storage
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 123
- 239000000463 material Substances 0.000 claims abstract description 98
- 238000000034 method Methods 0.000 claims abstract description 66
- 239000007788 liquid Substances 0.000 claims abstract description 8
- 239000000428 dust Substances 0.000 description 15
- 230000000694 effects Effects 0.000 description 10
- 239000007789 gas Substances 0.000 description 9
- 239000002912 waste gas Substances 0.000 description 9
- 125000004122 cyclic group Chemical group 0.000 description 7
- 238000000926 separation method Methods 0.000 description 6
- 239000000779 smoke Substances 0.000 description 6
- 239000000126 substance Substances 0.000 description 6
- 239000002184 metal Substances 0.000 description 5
- 239000011248 coating agent Substances 0.000 description 4
- 238000000576 coating method Methods 0.000 description 4
- 206010000234 Abortion spontaneous Diseases 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 3
- 229910052799 carbon Inorganic materials 0.000 description 3
- 239000002781 deodorant agent Substances 0.000 description 3
- 239000000295 fuel oil Substances 0.000 description 3
- 239000003350 kerosene Substances 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 208000015994 miscarriage Diseases 0.000 description 3
- 239000000843 powder Substances 0.000 description 3
- 238000003672 processing method Methods 0.000 description 3
- 238000000746 purification Methods 0.000 description 3
- 208000000995 spontaneous abortion Diseases 0.000 description 3
- 239000007921 spray Substances 0.000 description 3
- 238000005507 spraying Methods 0.000 description 3
- 235000004443 Ricinus communis Nutrition 0.000 description 2
- 239000003463 adsorbent Substances 0.000 description 2
- 238000001914 filtration Methods 0.000 description 2
- 238000009432 framing Methods 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 230000000630 rising effect Effects 0.000 description 2
- 230000001954 sterilising effect Effects 0.000 description 2
- 238000011144 upstream manufacturing Methods 0.000 description 2
- 229920000742 Cotton Polymers 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000001877 deodorizing effect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 238000002386 leaching Methods 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 239000011490 mineral wool Substances 0.000 description 1
- 239000004745 nonwoven fabric Substances 0.000 description 1
- 239000003921 oil Substances 0.000 description 1
- -1 pulpous state Substances 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 239000011435 rock Substances 0.000 description 1
- 239000013049 sediment Substances 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 230000003068 static effect Effects 0.000 description 1
- 238000004659 sterilization and disinfection Methods 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D47/00—Separating dispersed particles from gases, air or vapours by liquid as separating agent
- B01D47/02—Separating dispersed particles from gases, air or vapours by liquid as separating agent by passing the gas or air or vapour over or through a liquid bath
-
- 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
- B01D53/14—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 absorption
-
- 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
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
- B01D53/77—Liquid phase processes
- B01D53/78—Liquid phase processes with gas-liquid contact
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Environmental & Geological Engineering (AREA)
- Health & Medical Sciences (AREA)
- Biomedical Technology (AREA)
- Separation Of Particles Using Liquids (AREA)
- Treating Waste Gases (AREA)
Abstract
The present invention provides a kind of vaporous matter treating device of wet type, and its device is easy, and also less than in the past, the pressure loss for conveying the air quantity of vaporous material is few for the water for using, and also easily safeguards.It has：Process chamber；Vaporous material suction inlet, it is formed at the process chamber and for sucking vaporous material in the process chamber；Vaporous matter discharge port, it is formed at the process chamber and makes to be drawn into the vaporous material in the process chamber to the outdoor discharge of the treatment；Aqua storage tank, it is located in the process chamber；Wavy porous racing current produces plate, its at least gas-liquid interface for being arranged at least one of water surface by vaporous matter discharge port side when being observed from the center of the aqua storage tank, and for making the water surface of the aqua storage tank produce racing current；And porous hampering plate, simultaneously for the spittle for receiving to be produced by the racing current, the vaporous material being drawn into the process chamber contacts and is cleaned with the water of the aqua storage tank for the top of its water surface for being arranged on the vaporous matter discharge port side.
Description
Technical field
The present invention relates to a kind of vaporous matter treating device that can carry out exhaust-gas treatment, the dedusting of wet type etc., to cause
It is separated off from the shop including restaurant, the waste gas of manufacturing works or the discharge such as chemical plant, equipment, coating dust, black smoke etc.
The vaporous material (material flowed as gas) impacted to environment, more particularly to it is a kind of efficiently separate and recover from
The vaporous material treatment dress of wet type of the minute dusts of the carbon system ultramicro powder of the burning generation of kerosene, heavy oil etc. and application etc.
Put.
Background technology
In the past, as the emission-control equipment of the wet type using water, it is known to wash mill.Filled as conventional washing
Put, with spraying to the device of this type of waste gas, pick up waste gas and water and make it as waterfall water, deodorant liquid in vaporific
Countercurrently, so that exhaust gas contact passes through the device of this type to water and makes spraying water layer using spray nozzle and make
Waste gas alternately passes through spraying water layer and device of filter layer this type etc..Water is set to intersperse among rock alternatively, it is also possible to use
Make waste gas while cotton, non-woven fabrics, wire netting etc. and by by way of dust, water-soluble gas are stayed in water etc., but waste gas
In vaporific moisture be discharged, from environmentally consider be undesirable.In addition, for example it is also proposed shown in patent document 1 that
The wash mill of sample.
However, in conventional device as described above, because device becomes complicated, therefore exist be susceptible to failure this
Problem of sample etc..In addition, needed in using the device of this type of filter change filter, and it is as described above with
Toward use water device in, it is necessary to each device such as sprayer, conveying pump, there is also problem as maintenance expends man-hour.
In addition, it is necessary to largely use water in the device of conventional use water as described above.In addition, in that shown in patent document 1
In the case of kind of device, the pressure loss increase of air quantity, need also exist for for convey waste gas big fan as problem.
Citation
Patent document 1：Japanese Unexamined Patent Publication 8-164314 publications
The content of the invention
The invention problem to be solved
The present invention be in view of above-mentioned problem of the prior art and complete, its object is to, there is provided a kind of wet type is vaporous
Matter treating device, its device is easy, and the water for using also less than in the past, and conveys the pressure loss of the air quantity of vaporous material and subtracts
It is few, also easily safeguard.
Means for solving the problems
In order to solve above-mentioned problem, the vaporous matter treating device of wet type of the invention has：Process chamber；Vaporous material suction
Mouthful, it is formed at the process chamber, and for sucking vaporous material in the process chamber；Vaporous matter discharge port, its formation
In the process chamber, and make to be drawn into the vaporous material in the process chamber to the outdoor discharge of the treatment；Aqua storage tank, it is located at
In the process chamber；Wavy porous racing current produces plate, and it is arranged on when being observed from the center of the aqua storage tank by the vaporous thing
At least gas-liquid interface of at least one of water surface of matter outlet side, and for making the water surface of the aqua storage tank produce racing current；
And porous hampering plate, the top of its water surface for being arranged on the vaporous matter discharge port side, and for receiving by the racing current
The spittle of generation, the vaporous material being drawn into the process chamber is contacted and is cleaned by the water with the aqua storage tank.
In this manual, to include that waste gas, coating dust, black smoke etc. are impacted to environment in vaporous material vaporous
Material, also including the fine dust such as the carbon system ultramicro powder produced by the burning of kerosene, heavy oil etc. and application.
Preferably, the porous hampering plate is arranged with respect to the still water inclination of the aqua storage tank.
Preferably, the porous hampering plate is provided with multi-disc.For example, 2~3 porous hampering plates can be set.
The wavy porous racing current generation plate can also be configured to possess towards the vaporous material in the process chamber
The upstream side of interior flowing and in the water of the aqua storage tank extend inclusion removal portion.
Preferably, the wavy porous racing current produces plate and the porous hampering plate to be made up of punch metal.
Preferably, the adsorbent for adsorbing the particulate in vaporous material is put into the aqua storage tank.
By using the vaporous matter treating device of wet type of the invention, can enter to exercise the gas being drawn into the process chamber
The vaporous substance processing method of wet type that shape material is contacted and be cleaned with the water of the aqua storage tank.
Invention effect
According to the present invention, playing can provide remarkable result as a kind of vaporous matter treating device of following wet type,
In the vaporous matter treating device of the wet type, device is easy, and the water for using also less than in the past, conveys the pressure of the air quantity of vaporous material
Loss is few, also easily safeguards.
Brief description of the drawings
Fig. 1 is a sectional view for implementation method for representing the vaporous matter treating device of wet type of the invention.
Fig. 2 is that the wavy porous racing current in the vaporous matter treating device of the wet type for observing Fig. 1 from oblique upper produces plate part
Stereogram.
Fig. 3 is that the wavy porous racing current in the vaporous matter treating device of the wet type for observing Fig. 1 from obliquely downward produces plate part
Stereogram.
Fig. 4 is represent the vaporous material treatment of wet type that the vaporous matter treating device of wet type of the invention is carried out schematic
Sectional view.
Fig. 5 is the sectional view of another implementation method for representing the vaporous matter treating device of wet type of the invention.
Fig. 6 is the side partial cross-sectional of the another implementation method for representing the vaporous matter treating device of wet type of the invention.
Fig. 7 is the side view of the vaporous matter treating device of wet type of Fig. 6.
Fig. 8 is the sectional perspective perspective view of the vaporous matter treating device of wet type of Fig. 6.
Fig. 9 is the sectional perspective perspective view of the vaporous matter treating device of wet type for observing Fig. 6 from other directions.
Description of reference numerals：
10、64、76：The vaporous matter treating device of wet type of the invention；12、78：Process chamber；14、80：Vaporous material suction
Mouthful；16、82：Vaporous matter discharge port；18、84：Aqua storage tank；20：The water surface；22：Gas-liquid interface；24、86：It is wavy porous to miscarriage
Raw plate；26、88a、88b：Porous hampering plate；28、90：The vaporous material directing plate of air-tightness；30a、30b：Wall；31：Framework structure
Part；32a、32b：Side；33：Top cover portion；34、36、40：Hole；38：Inclusion removal extension；42：Opening portion；44：Incline
Plate；46：Fan；48、98：Motor；50、92：Odor removal；52：Heater；54：Decline water level；56：Rising water stage；58、
112：Discharge outlet；59：Water check valve；60、94：Odor removal exhaust outlet；62：Water droplet；66：Circulation filter；68：Circulating pump；
70：Cyclic water tank；72：Filter；74：Feed water inlet；96：Castor component；100：Magnetic valve；102：Water level induction-box；104：Only
Pump in change water；106：Cylinder mould；108：Dust acquirement filter cartridge；110：Shutter door；G：Vaporous material；G1：Vaporous material is inhaled
The vaporous material of entrance side；G2：The vaporous material of vaporous matter discharge port side；W：Water；θ1、θ2、θ3：Angle.
Specific embodiment
Hereinafter, embodiments of the present invention are illustrated referring to the drawings.Fig. 1 is represented at the vaporous material of wet type of the invention
Manage an implementation method of device.
In Fig. 1~Fig. 4, reference 10 is the vaporous matter treating device of wet type of the invention.
The vaporous matter treating device 10 of wet type has：Process chamber 12；Vaporous material suction inlet 14, it is formed at the treatment
Room 12, and for sucking vaporous material G in the process chamber 12；Vaporous matter discharge port 16, it is formed at the process chamber
12, and make to be drawn into the vaporous material G in the process chamber 12 to discharge outside the process chamber 12；Aqua storage tank 18, it is located at institute
State in process chamber 12；Wavy porous racing current produces plate 24, and it is arranged on when being observed from the center of the aqua storage tank 18 by the gas
At least gas-liquid interface of the water surface 20 in the downstream of the flowing of the vaporous material G in the side of shape matter discharge port 16, i.e. process chamber 12
22, the water surface 20 for making the aqua storage tank 18 produces racing current；And porous hampering plate 26, it is arranged on the vaporous material row
The top of the water surface 20 of 16 sides, and the spittle for receiving to be produced by the racing current are exported, is drawn into the process chamber 12
Vaporous material G is contacted and is cleaned by the water W with the aqua storage tank 18.
In addition, near the center of process chamber 12, being provided with the vaporous material directing plate 28 of air-tightness.The vaporous material of air-tightness draws
Guide plate 28 plays a part of the stream for limiting and guiding the vaporous material G being drawn into process chamber 12, so as to obtain vaporous material inhale
The vaporous material G1 and the water W of aqua storage tank 18 of the side of entrance 14 are contacted and are turned into the vaporous material G2 of the side of vaporous matter discharge port 16.
Therefore, in the present invention, it is preferred to set the vaporous material directing plate 28 of air-tightness.In addition, the vaporous material directing plate 28 of air-tightness is adopted
With wall 30a, the 30b contacted with vaporous material G relative to the structure that the water surface of aqua storage tank 18 leans forward.θ shown in Fig. 11It is storage
Angle between the water surface and wall 30b of tank 18, in the example in fig 1, θ1It is 60 °.For example, the side of vaporous matter discharge port 16
The vaporous material directing plate 28 of air-tightness wall 30b and the water surface of aqua storage tank 18 between angle, θ1Preferably 80 °~50 °.
It should be noted that the wall 30a and aqua storage tank of the vaporous material directing plate 28 of air-tightness for the vaporous side of material suction inlet 14
Angle between 18 water surface, is also to lean forward, and is not particularly limited, but is for example preferably 80 °~50 °.
As shown in Figure 2 to 3, the vaporous material directing plate 28 of air-tightness is located at framing component 31, except being connect with vaporous material G
Also there is side 32a, 32b and top cover portion 33 outside tactile wall 30a, 30b, but due to side 32a, 32b and process chamber 12
Inwall abut, therefore, as long as playing the stream for limiting and guiding the vaporous material G being drawn into process chamber 12 as described above
Effect, it is also possible to using being not provided with the construction of side 32a, 32b.
As shown in Figure 2 to 3, wavy porous racing current produces plate 24 to form wavy, and offers many holes 34.In illustrated example
In, show that wavy porous racing current produces plate 24 to use the example of the punch metal of SUS.For example, hole 34 can be preferably used
A diameter of 3mm~5mm or so, aperture opening ratio be that 50%~60% or so, wave height is the punch metal of 10mm~20mm or so.But
Be, wavy porous racing current produce plate 24 according to air quantity to be processed, dust to dust species or size etc. and change hole 34
Diameter, or change wave height or broken number (frequency of ripple).
The porous hampering plate 26 is installed on the vaporous material directing plate 28 of air-tightness, is arranged with respect to the aqua storage tank 18
The water surface 20 still water incline.As shown in Figure 2 to 3, many holes 36 are offered on the porous hampering plate 26.In diagram
In example, show that porous hampering plate 26 has used the example of the punch metal of SUS.For example, the diameter in hole 36 can be preferably used
For 3mm~5mm or so, aperture opening ratio are that 50%~60% or so, wave height is the punch metal of 10mm~20mm or so.Shown in Fig. 1
θ2It is the angle between the water surface of aqua storage tank 18 and porous hampering plate 26, in the example in fig 1, θ2It is 30 °.For example, aqua storage tank
Angle between 18 water surface and porous hampering plate 26 is preferably 45 °~25 °.Also, it is preferred that making above-mentioned angle, θ1With angle, θ2
Relation be θ1＞ θ2。
It should be noted that in the example in the figures, show porous hampering plate 26 with the vaporous side of material suction inlet 14
Compared to and towards the side of vaporous matter discharge port 16 and aqua storage tank 18 water surface distance of separation mode (towards right in illustrated example
On) inclined example, but as long as playing a part of to receive the spittle that is produced by racing current, it is also possible to make porous hampering plate 26 with
The side of vaporous matter discharge port 16 compare and towards the mode of the vaporous side of material suction inlet 14 and the water surface distance of separation of aqua storage tank 18
(if in other words, being illustrated in the same manner as Fig. 1, towards upper left) inclines.
The wavy porous racing current produces plate 24 to possess the flowing in the process chamber 12 towards the vaporous material G
Upstream side and among the water W of the aqua storage tank 18 extend inclusion removal extension 38.The inclusion removal extends
Portion 38 produces plate 24 to be integrally connected with wavy porous racing current, in the example in the figures, to prolonging among the water W of the aqua storage tank 18
Stretch, as the porous hang plate with many holes 40.For example, the wavy porous racing current can be produced the tail portion of plate 24
It is configured to the hang plate extended among the water W to the aqua storage tank 18.Inclusion removal extension 38 is arranged with respect to water storage
The water surface of groove 18 is inclined.In the example in the figures, θ3It is 30 °.The water surface of the inclusion removal extension 38 relative to aqua storage tank 18
Angle, θ3For example it is preferably 60 °~20 °.
It should be noted that as shown in figure 3, being formed with framing component 31 and opening that vaporous material suction inlet 14 is connected
Oral area 42.
In Fig. 1, reference 46 is fan, and it is driven using motor 48.In addition, reference 50 is deodorant dress
Put, internally possess for removing the heater 52 of water removal and the filter of leaching dust etc..As the example of filter, for example
Enumerate using cloth or use rock wool containing water etc..So, using fan 46, formed from vaporous material suction inlet 14
Towards the flowing of the vaporous material G of vaporous matter discharge port 16, by vaporous material G from vaporous matter discharge port 16 towards deodorant dress
50 conveyings and further purification are put, and is finally discharged into the atmosphere from odor removal exhaust outlet 60.
Hang plate 44 is provided with the aqua storage tank 18, is configured to be arranged from discharge outlet 58 when water W is contaminated
Water.It should be noted that the inclination on hang plate 44, in illustrated example, shows the example of inclined upward to the right, but also can
Enough make the reversal of dip, be set to inclined upward to the left.Reference 59 is the water check valve for being installed on discharge outlet 58.
By using the vaporous matter treating device 10 of wet type of the invention, enforcement can be entered and be drawn into the process chamber 12
The vaporous material G vaporous substance processing methods of wet type that contact and be cleaned with the water W of the aqua storage tank 18.
More particularly, can using the vaporous substance processing method of wet type of the vaporous matter treating device of wet type of the invention
Carried out according to following separation and recovery method：Water miscible material in for vaporous material, the water W using aqua storage tank 18 enters
Row is collected, and for the sediment in vaporous material, pulpous state, solid, makes its sedimentation separation in aqua storage tank 18, in vaporous material
Granular material be placed into the adsorbent adsorbing separation of aqua storage tank 18.
Based on Fig. 1~Fig. 4, the effect of the vaporous matter treating device 10 of wet type of the invention is further elaborated with.
Vaporous material G from the discharge such as manufacturing works or chemical plant, equipment is from vaporous material suction inlet 14 to process chamber
Flow into 12 and towards vaporous matter discharge port 16.
The vaporous side of material suction inlet 14 and vaporous thing are divided into by the vaporous material directing plate 28 of air-tightness inside process chamber 12
The side of matter outlet 16, therefore when vaporous material G is inhaled into inside, as shown in figure 4, the water surface 20 of aqua storage tank 18 and static shape
State is compared, in the vaporous side of material suction inlet 14, water level slightly falling head t1(for example, 5mm or so) and turn into descending water position
54.On the other hand, in the side of vaporous matter discharge port 16, water level slightly lifting height t2(for example, 10mm or so) and turn into
Rising water stage 56.
Then, the vaporous material G1 of the vaporous side of material suction inlet 14 via it is wavy it is porous racing current produce plate 24 and and aqua storage tank
18 water W contacts, and towards the side of vaporous matter discharge port 16, as vaporous material G2.Now, using wavy porous to miscarriage
Raw plate 24, when being observed from the center of the aqua storage tank 18 by the gas in the side of vaporous matter discharge port 16, process chamber 12
The water surface 20 in the downstream of the flowing of shape material G, by fan 46 draw including the air including vaporous material G and by fan 46
The water for picking up collides with the hole of wavy porous racing current generation plate 24 and attempts to deviate from and turn into fierce racing current.Now,
Produce bubble, the spittle.In addition, in the case of including field trashes such as larger dust etc. in vaporous material G, using wavy porous
Racing current produces the inclusion removal extension 38 of plate 24 to remove it.
By racing current, though produce the spittle, the water droplet 62 of the spittle and the porous hampering plate 26 of the top for being arranged on the water surface 20
Contact and be shot back, return to aqua storage tank 18.Thus, the water droplet 62 for dispersing will not be made to enter fan 46.
So, vaporous material G is contacted and is cleaned by the water W with aqua storage tank 18.The particle such as black smoke or oil smoke, coating compared with
Big material is removed by water W.Then, the vaporous material G2 of the side of vaporous matter discharge port 16 is discharged from vaporous matter discharge port 16,
And deliver to odor removal 50.In odor removal 50, in the filter after vaporous material G by heater 52 by being heated, have
Machine gas or smell are removed, while being also carried out sterilization.So, finally discharged into the atmosphere from odor removal exhaust outlet 60.
Even if in addition, the vaporous material G sucked from vaporous material suction inlet 14 is high temperature, it is also possible to by above-mentioned water W
Racing current cooled down after be passed to fan 46.Therefore, even if not being that resistance to Hot-air fan can also be used.
So, in the method for the invention, the pressure loss for conveying the air quantity of vaporous material is less, and water resistance
It is smaller, therefore larger fan (big electric power) is not needed, can compactly make.In addition, the water for using can be a small amount of, if wearing
Filtering water intaking, the filter of dust are circulated, then only just being capable of long time running by changing filter.
The vaporous matter treating device of wet type of the invention, can efficiently separate and recover by the combustion of kerosene, heavy oil etc.
Burn the carbon system ultramicro powder for producing, it is also possible to dedusting.
In the vaporous matter treating device of wet type of the invention, water-soluble gas composition can be made efficiently to be dissolved in water
In.
In addition, being combined by with the odor removal of heater has been used as described above, additionally it is possible to deodorizing sterilizing.
Fig. 5 shows another implementation method of the vaporous matter treating device of wet type of the invention.In Figure 5, reference 64
It is the vaporous matter treating device of wet type of another embodiment of the present invention.The vaporous matter treating device 64 of wet type is above-mentioned wet
Circulation filter 66 is installed in the vaporous matter treating device 10 of formula.Circulation filter 66 is configured to make using circulating pump 68
The water of aqua storage tank 18 is circulated to cyclic water tank 70, and the water after being filtered by filter 72 returns to cyclic water tank 70.In addition, from feed water inlet
74 automatically feed water towards cyclic water tank 70, and the water in cyclic water tank 70 is maintained into constant basis.
The coating included in vaporous material floats on the water and turns into film, but by installing circulation filter 66, in dress
Circulation filter 66 delivered to by circulating pump 68 during the water of aqua storage tank 18 is flow at great speed in the operating put and is filtered.Pass through
The water of filter 72 is cleaned, and then, if supplying water to correspondingly cyclic water tank 70 with the amount for reducing, the consumption of water is very
It is small.Because the particle in the water for falling into aqua storage tank 18 is than larger, as long as therefore can just be filtered using non-woven paper making filter 72
Take.By so composition, also simple and filter is also cheap for device, therefore is effective.
Fig. 6~Fig. 9 shows the another implementation method of the vaporous matter treating device of wet type of the invention.In Fig. 6~Fig. 9,
Reference 76 is the vaporous matter treating device of wet type.The vaporous matter treating device 76 of wet type has：Process chamber 78；Vaporous material
Suction inlet 80, it is formed at the process chamber 78, and for sucking vaporous material in the process chamber 78；Vaporous material discharge
Mouthfuls 82, it is formed at the process chamber 78, and make to be drawn into the vaporous material in the process chamber 78 to the process chamber 78 outside
Discharge；Aqua storage tank 84, it is located in the process chamber；Wavy porous racing current produces plate 86, and it is arranged on from the aqua storage tank 84
Center when observing by least gas-liquid interface of at least one of water surface of the side of vaporous matter discharge port 82, and be used for
The water surface of the aqua storage tank 84 is set to produce racing current；And porous hampering plate 88a, 88b, they are arranged on the vaporous material discharge
The top of the water surface of 82 sides of mouth, and the spittle for receiving to be produced by the racing current, are drawn into vaporous in the process chamber 78
Material is contacted and is cleaned by the water with the aqua storage tank 84.
In the example of Fig. 6~Fig. 9, show water be introduced into aqua storage tank 84 in state, but on porous being run quickly wavy
The raw plate 86 of miscarriage is arranged at least when being observed from the center of the aqua storage tank 84 by the side of vaporous matter discharge port 82
The structure of at least gas-liquid interface of the water surface for dividing is identical with the implementation method shown in Fig. 1.In addition, wavy porous racing current produces plate
86 produce the identical punched-plate of plate 24 to constitute by with the wavy porous racing current shown in Fig. 2.
Porous hampering plate 88a, 88b are two panels in illustrated example, are inclined relative to the still water of the aqua storage tank 84 and set
Put, and the porous hampering plate of two panels is configured with identical angle of inclination.The water surface of the aqua storage tank 84 and porous hampering plate
88a, 88b each between angle in illustrated example be 30 °.In addition, porous hampering plate 88a, 88b are porous as shown in Fig. 2
The identical punched-plate of hampering plate 26 is constituted.
In addition, being provided with the vaporous material directing plate 90 of air-tightness in process chamber 78, the separation separated in process chamber 78 is played
The effect of plate.The vaporous material directing plate 90 of air-tightness is played to be made with the vaporous identical of material directing plate 28 of air-tightness shown in Fig. 2
With.
In the example of Fig. 6~Fig. 9, top will be arranged on the identical odor removal 92 of odor removal 50 shown in Fig. 1,
It is provided with the odor removal 92 and the identical odor removal exhaust outlet 94 of odor removal exhaust outlet 60 shown in Fig. 1.
Castor component 96 is provided with the bottom of device, can easily be moved.In addition, reference 98 is for making wind
The motor for rotating is fanned, it is identical with the motor 48 shown in Fig. 1.
Reference 100 is magnetic valve, is the valve for supplying water to aqua storage tank 84.Reference 102 is as circulation
The water level induction-box of water tank.Water level induction-box 102 be manage aqua storage tank 84 water level and water supply case, play with shown in Fig. 5
The same effect of cyclic water tank 70.Reference 104 is to be used to draw the water in aqua storage tank 84 as circulating pump and obtain dust
Pump in the purification water for being purified, plays the effect same with the circulating pump 68 shown in Fig. 5.
In addition, reference 106 is the cylinder mould as the dust acquirement of filter, play and the filter shown in Fig. 5
72 same effects.Cylinder mould 106 is arranged in dust acquirement filter cartridge 108 with pump 104 in purification water, and use is obtained in dust
The top of filter cartridge 108 is provided with shutter door 110, to cause to throw away the dust accumulated in cylinder mould 106.Reference 112 is row
The mouth of a river.
In the implementation method of Fig. 6~Fig. 9, the porous hampering plate of two panels is provided with.The basic work of the purified treatment of vaporous material
With identical with the implementation method shown in Fig. 1, Fig. 5.In addition, the water of the aqua storage tank 84 in the implementation method on Fig. 6~Fig. 9 is followed
The effect of ring filtering, it is also essentially identical with implementation method shown in Fig. 5.
In the implementation method of Fig. 6~Fig. 9, under the vaporous material directing plate 90 of the drill-through air-tightness of vaporous material being attracted
Side, produces plate 86 to collide, and produce plate 86 through wavy porous racing current with wavy porous racing current in the lump with the water being now imported into
Hole, therefore produce fierce spray and bubble.In addition, the spray contacted with porous hampering plate 88a, the 88b on top and as swash
Strong rainwater is poured into downwards like that.Two panels is set to by by the porous hampering plate, is blocked less and preferably with the pressure loss
The effect of water.
In the case where the kitchen in the shops such as restaurant is arranged at, the reduction vaporous matter treating device of wet type of the invention is used
Size device, in the case where manufacturing works, chemical plant, equipment is arranged at, use increase the vaporous material of wet type
The device of the size of processing unit.In the case where the shops such as restaurant are arranged at, removal companion can be efficiently separated
Smoke evacuation produced with culinary art etc..If in addition, reduce the size of the vaporous matter treating device of wet type, at the restaurant or work
In factory, facility, it is also possible to be placed on desk, use on the table.So, the vaporous matter treating device of wet type of the invention can
By be arranged on produce smoke evacuation, the various places of waste gas and carry out purified treatment.
It should be noted that the invention is not restricted to above-mentioned implementation method.Aforesaid way for illustrate, with power of the invention
The substantially identical structure of technological thought described in sharp claim and play the same role the situation of effect and be all contained in this
In the technical scope of invention.
Claims (3)
1. the vaporous matter treating device of a kind of wet type, wherein,
The vaporous matter treating device of wet type has：
Process chamber；
Vaporous material suction inlet, it is formed at the process chamber, and for sucking vaporous material in the process chamber；
Vaporous matter discharge port, it is formed at the process chamber, and makes to be drawn into the vaporous material in the process chamber to described
The outdoor discharge for the treatment of；
Aqua storage tank, it is located in the process chamber；
Wavy porous racing current produces plate, and it is arranged on when being observed from the center of the aqua storage tank by the vaporous matter discharge port side
At least one of water surface at least gas-liquid interface, and for make the aqua storage tank the water surface produce racing current；And
Porous hampering plate, the top of its water surface for being arranged on the vaporous matter discharge port side, and for receiving by the racing current
The spittle of generation,
The vaporous material being drawn into the process chamber is contacted and is cleaned by the water with the aqua storage tank.
2. the vaporous matter treating device of wet type according to claim 1, wherein,
The still water that the porous hampering plate is arranged with respect to the aqua storage tank is inclined.
3. the vaporous matter treating device of wet type according to claim 1 and 2, wherein,
The porous hampering plate is provided with multi-disc.
Applications Claiming Priority (4)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2015231821 | 2015-11-27 | ||
| JP2015-231821 | 2015-11-27 | ||
| JP2016-111853 | 2016-06-03 | ||
| JP2016111853A JP6749146B2 (en) | 2015-11-27 | 2016-06-03 | Wet gaseous substance treatment equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN106807159A true CN106807159A (en) | 2017-06-09 |
Family
ID=59058395
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610943422.1A Pending CN106807159A (en) | 2015-11-27 | 2016-11-01 | The vaporous matter treating device of wet type |
Country Status (2)
| Country | Link |
|---|---|
| JP (1) | JP6749146B2 (en) |
| CN (1) | CN106807159A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2021129303A1 (en) * | 2019-12-26 | 2021-07-01 | 青岛海尔洗衣机有限公司 | Gas dryer system |
Families Citing this family (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP6906232B2 (en) * | 2018-01-19 | 2021-07-21 | 株式会社ネイブヒート | Wet particulate matter processing equipment |
| CN108659891B (en) * | 2018-07-19 | 2023-05-12 | 唐山炬能节能科技有限公司 | Biomass combustible gas washing and purifying device |
| KR102178733B1 (en) | 2018-09-28 | 2020-11-13 | 주식회사 포스코 | Alien substance capturing apparatus and electrical steel sheet manufacturing facility having thereof |
| JP2020075214A (en) * | 2018-11-07 | 2020-05-21 | 株式会社ネイブヒート | Wet type gaseous substance treatment device and wet type gaseous substance treatment method |
| CN113476998A (en) * | 2021-07-30 | 2021-10-08 | 中国建筑一局(集团)有限公司 | Movable negative pressure suction dust treatment device |
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| CN85205228U (en) * | 1985-12-05 | 1987-02-04 | 航天部621所环保设备厂 | Plastic eluviating dust catcher |
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| CN201120232Y (en) * | 2007-10-25 | 2008-09-24 | 陈永杰 | Air bubble wet collector |
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| WO2021129303A1 (en) * | 2019-12-26 | 2021-07-01 | 青岛海尔洗衣机有限公司 | Gas dryer system |
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Also Published As
| Publication number | Publication date |
|---|---|
| JP6749146B2 (en) | 2020-09-02 |
| JP2017104843A (en) | 2017-06-15 |
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