CN109464851A - A kind of separator of flue gas and sewage in sewer gas - Google Patents
A kind of separator of flue gas and sewage in sewer gas Download PDFInfo
- Publication number
- CN109464851A CN109464851A CN201811628519.9A CN201811628519A CN109464851A CN 109464851 A CN109464851 A CN 109464851A CN 201811628519 A CN201811628519 A CN 201811628519A CN 109464851 A CN109464851 A CN 109464851A
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- Prior art keywords
- sewage
- gas
- flue gas
- sewer
- flue
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D45/00—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces
- B01D45/04—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by utilising inertia
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D45/00—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces
- B01D45/04—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by utilising inertia
- B01D45/08—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by utilising inertia by impingement against baffle separators
Abstract
The present invention provides a kind of separators of sewage in flue gas and sewer gas, comprising: bindiny mechanism, separating mechanism and drainage mechanism；Wherein, the bindiny mechanism is arranged between the separating mechanism and flue, for conveying the flue gas in flue with sewer gas into the separating mechanism；The separating mechanism is connected with the mechanism, and the flue gas for conveying the bindiny mechanism passes through inside it with sewer gas to be collided, to realize the separation of sewage in flue gas and sewer gas；The drainage mechanism is connected with the separating mechanism, and the mechanism is discharged in the sewage for that will isolate through the separating mechanism, in order to collect the sewage.The present invention has effectively achieved the quick separating of sewage in flue gas and sewer gas, has saved the energy consumption in flue gas and sewer gas in sewage separation process, has effectively saved the cost of sewage separation.
Description
Technical field
The present invention relates to flue gas sewage separation technology fields, in particular to sewage in a kind of flue gas and sewer gas
Separator.
Background technique
Gas is separated with sewer gas, is the critical issue of the out of stock equipment of desulfurization and dedusting, and traditional equipment flue gas water content is exceeded,
In order to discharge qualification, it is necessary to using large scale equipment (cooling, heating) processing, cause energy waste, and investment is higher, enterprise is difficult to
It bears.
Summary of the invention
In consideration of it, the invention proposes a kind of separators of sewage in flue gas and sewer gas, it is intended to solve existing cigarette
Gas processing system cannot achieve the quick separating of cigarette water, and the problem that energy consumption is higher, cost is larger during the separation of cigarette water.
The invention proposes a kind of separators of sewage in flue gas and sewer gas, comprising: bindiny mechanism, separating mechanism
And drainage mechanism；Wherein,
The bindiny mechanism is arranged between the separating mechanism and flue, for by the flue gas and sewer gas in flue
It conveys into the separating mechanism；
The separating mechanism is connected with the mechanism, and the flue gas and sewer gas for conveying the bindiny mechanism are at it
Inside is by being collided, to realize the separation of sewage in flue gas and sewer gas；
The drainage mechanism is connected with the separating mechanism, and institute is discharged in the sewage for that will isolate through the separating mechanism
Mechanism is stated, in order to collect the sewage；
During use, flue gas and sewer gas in flue pass through described in the bindiny mechanism entrance described device
It in separating mechanism, and collides in separating mechanism, and realizes dirt in flue gas and sewer gas under different effect of inertia
The separation of water, the sewage isolated are discharged from the separating mechanism by the drainage mechanism, and flue gas then passes through the separation
Device continues to discharge.
Further, in above-mentioned flue gas and sewer gas in the separator of sewage, the separator include: outer cylinder,
Inner cylinder and collision cell；Wherein,
The outside of the separating mechanism is arranged in the outer cylinder, using the outer wall as the collision cell；
The inside of the outer cylinder, both ends and the outer cylinder airtight connection is arranged in the inner cylinder, and by being provided with it
Several through-holes on side wall are connected；
The collision cell is arranged between the inner cylinder and the outer cylinder, to carry out as the flue gas and sewer gas
The place of collision；
The outer tube inner wall is provided with several segments arcuate structure, to increase flue gas and sewer gas and the collision chamber
Contact area；Wherein, the length of each section of arc and the determination method of angle are as follows:
Wherein,
In formula: L1For ab sections of arc length, r is flue diameter, θ1The angle in direction is flowed to sewage for ab sections, ρ is in pipeline
The actual density of flue gas and sewer gas can be measured by supersonic detector, and ρ 0 is the standard density of water, θ0For the connection
The setting angle of mechanism；In the present embodiment, ultrasonic sensor is set in collision chamber, alternatively, in other positions of pipeline
Ultrasonic sensor is installed, to detect the actual density of flue gas and sewer gas；
Wherein,
In formula, L2For bc sections of arc length, D is the height of collision chamber, θ2The angle in direction is flowed to sewage for bc sections, ρ is
The actual density of flue gas and sewer gas, ρ in pipeline0For the standard density of water.
Wherein,
In formula, L3For cd sections of arc length, θ3The angle in direction is flowed to sewage for cd sections.
Further, for above-mentioned flue gas with the separator of sewage in sewer gas, the average diameter of the outer cylinder is institute
1.3 times of specification for stating inner diameter of steel flue.
Further, for above-mentioned flue gas with the separator of sewage in sewer gas, the height of the inner cylinder is its diameter
1.5 times.
Further, in above-mentioned flue gas and sewer gas in the separator of sewage, the height of the outer cylinder with it is described interior
The height of cylinder is equal.
Further, for above-mentioned flue gas with the separator of sewage in sewer gas, the bindiny mechanism is a tubulose structure
Part, the 1/5 of a diameter of inner diameter of steel flue.
Further, for above-mentioned flue gas with the separator of sewage in sewer gas, the drainage mechanism is a tubulose structure
Part is arranged in the outer tube side wall bottom.
Further, in above-mentioned flue gas and sewer gas in the separator of sewage, the area of several through-holes and it is
The 1/3 of the inner cylinder lateral area.
Further, in above-mentioned flue gas and sewer gas in the separator of sewage, the spacing between the adjacent through-hole
It is the 1/3 of the through-hole diameter.
Further, in above-mentioned flue gas and sewer gas in the separator of sewage, further includes: collecting-tank, it is described to catchment
Pond is used for the sewage of the discharge of drainage mechanism described in access, and the water outlet of the drainage mechanism is closed by sewage.
Compared with prior art, the beneficial effects of the present invention are sewage in flue gas provided by the invention and sewer gas
Separator, during use, flue gas in flue enters described separate by the bindiny mechanism with sewer gas
It in mechanism, collides in separating mechanism, and realizes point of sewage in flue gas and sewer gas under different effect of inertia
Be discharged from the separating mechanism from, the sewage isolated by the drainage mechanism, flue gas then pass through the separating mechanism after
Continuous discharge, has effectively achieved the quick separating of sewage in flue gas and sewer gas, has saved sewage in flue gas and sewer gas
The cost of sewage separation has effectively been saved in energy consumption in separation process.
Especially, in flue gas and sewer gas of the invention sewage separator, in separating mechanism is arranged to
Cylinder, outer cylinder and collision cell three parts, wherein inner cylinder is directly connect with bindiny mechanism, and upper end outlet connects flue, cylinder pressure
It is flue gas pressures；The pressure of collision cell is lower than inner cylinder pressure between outer cylinder and inner cylinder, and system forms negative pressure field, the high flue gas of pressure
It is rapidly diffused into the low collision cell of pressure with sewer gas；Meanwhile smoke density is less than sewage air tightness, in this way in blower height
Speed traction is lower to hit inner cylinder, and the big substance of density, inertia is big, and the small substance inertia of density is small, and the big goods and materials of inertia are brought together,
Sewage pearl is formed, the small substance of inertia is continued forward, to be discharged to flue by blower traction, effectively further ensures flue gas and dirt
The quick separating of sewage in water gas has greatly saved the energy consumption in flue gas and sewer gas in sewage separation process, in turn
Save the cost of sewage separation.
Detailed description of the invention
By reading the following detailed description of the preferred embodiment, various other advantages and benefits are common for this field
Technical staff will become clear.The drawings are only for the purpose of illustrating a preferred embodiment, and is not considered as to the present invention
Limitation.And throughout the drawings, the same reference numbers will be used to refer to the same parts.In the accompanying drawings:
Fig. 1 is the structural schematic diagram of sewage separating device in the flue gas and sewer gas of the embodiment of the present invention；
Fig. 2 is the structural schematic diagram of the inner cylinder in the separating mechanism of the embodiment of the present invention；
Fig. 3 is the curved configuration schematic diagram of the inner wall of the outer cylinder of the embodiment of the present invention.
Specific embodiment
Exemplary embodiments of the present disclosure are described in more detail below with reference to accompanying drawings.Although showing the disclosure in attached drawing
Exemplary embodiment, it being understood, however, that may be realized in various forms the disclosure without should be by embodiments set forth here
It is limited.On the contrary, these embodiments are provided to facilitate a more thoroughly understanding of the present invention, and can be by the scope of the present disclosure
It is fully disclosed to those skilled in the art.It should be noted that in the absence of conflict, embodiment in the present invention and
Feature in embodiment can be combined with each other.The present invention will be described in detail below with reference to the accompanying drawings and embodiments.
It is the separator of sewage in the flue gas and sewer gas of the embodiment of the present invention refering to fig. 1 shown in -2 comprising:
Separating mechanism 1, bindiny mechanism 2 and drainage mechanism 3；Wherein, the separating mechanism 1 is connected with the bindiny mechanism 2, and being used for will
The flue gas that the bindiny mechanism 2 conveys passes through inside it with sewer gas to be collided, to realize in flue gas and sewer gas
The separation of sewage；The bindiny mechanism 2 is arranged between the separating mechanism 1 and flue, for by flue gas in flue and dirty
Water gas is conveyed into the separating mechanism 1；The drainage mechanism 3 is connected with the separating mechanism 2, and being used for will be through the separation
The separating mechanism 1 is discharged in the sewage that mechanism 2 isolates, in order to collect the sewage.During use, in flue
Flue gas and sewer gas are entered in the separating mechanism 1 by the bindiny mechanism 2, are collided in separating mechanism 1, and
The separation of sewage in flue gas and sewer gas is realized under different effect of inertia, the sewage isolated passes through the drainage mechanism 3
It is discharged from the separating mechanism 1, flue gas then passes through the separating mechanism 1 and continues to discharge, and has effectively achieved flue gas and sewage
The quick separating of sewage in gas has saved the energy consumption in flue gas and sewer gas in sewage separation process, effectively saves
The cost of sewage separation.
Specifically, the separating mechanism 1 includes: outer cylinder 11, inner cylinder 12 and collision cell 13；Wherein, the outer cylinder 1 is
The outside of the separating mechanism 1 is arranged in one housing member, using the outer wall as the collision cell 13；The outer cylinder 11
Cross sectional shape can for rectangle, circle and triangle etc. arbitrary shapes, be set as long as it can be enclosed together with the inner cylinder
The collision cell 13, and as its outer wall.The inner cylinder 12 is a housing member, is arranged in the outer cylinder 11
Portion, and being directly connected with the bindiny mechanism 2, using as flue gas cylinder road, both ends respectively with 11 airtight connection of outer cylinder, with
The collision cell 13 is formed between the outer cylinder 11 at it, and a number of through-hole 121, institute are offered on its side wall
Through-hole 121 is stated for being connected to 12 internal chamber of inner cylinder and the collision cell 13, makes the high pressure flue gas inside the inner cylinder 12
It can promptly be diffused into the low collision cell 13 of pressure, to ensure that flue gas and the collision of sewage in sewer gas separate.It is described
The cross sectional shape of inner cylinder 12 can for rectangle, circle and triangle etc. arbitrary shapes, as long as it can be with the outer cylinder 11
It encloses together and is set as the collision cell 13, and as its inner wall.The collision cell 13 setting the inner cylinder 12 with it is described outer
Between cylinder 11, to the place collided as the flue gas and sewer gas, in order to flue gas in the inner cylinder and dirty
Water gas can promptly enter in the collision cell 13 under the driving of pressure difference is collided, and then realizes flue gas and sewage gas
The quick separating of body sewage.In the present embodiment, the outer cylinder 11 is that a cross sectional shape is circular cylindrical shell, the inner cylinder 12
Also be circular cylindrical shell for a cross sectional shape, the concentric inside that the outer cylinder 11 is set, both ends respectively with it is described
The both ends airtight connection of outer cylinder 11, and several through-holes 121 by being provided on its side wall are connected.The collision cell 13 is to set
It sets in the annular compartment between the inner cylinder 12 and the outer cylinder 11, to what is collided as the flue gas and sewer gas
Place.Meanwhile the average diameter of the outer cylinder 11 is 1.3 times of specification of 12 diameters in described, height and the inner cylinder 12
Height it is equal, be 1.5 times of 12 diameter of inner cylinder.In addition, several through-holes 121 opened up on 12 side wall of inner cylinder
Area and be the 1/3 of 12 lateral area of inner cylinder, the spacing between the adjacent through-hole 121 are the 1/ of 121 diameter of through-hole
3.During use, the flue gas in flue and sewer gas are entered in the separating mechanism 1 by the bindiny mechanism 2
In inner cylinder 12, since the pressure of collision cell is lower than 12 pressure of inner cylinder, system forms negative pressure field, and pushes in the driving of pressure difference
The high flue gas of power runs through the through-hole 121 being provided on 12 side wall of inner cylinder with sewer gas and is diffused into the low collision cell 13 of pressure
It inside collides, and realizes the quick separating of sewage in flue gas and sewer gas, the dirt isolated under different effect of inertia
Water is discharged from the separating mechanism 1 by the drainage mechanism 3, and flue gas then passes through the separating mechanism 1 and continues to discharge, effectively
Ground realizes the quick separating of sewage in flue gas and sewer gas, has saved in flue gas and sewer gas in sewage separation process
The cost of sewage separation has effectively been saved in energy consumption.
Specifically, the bindiny mechanism 2 is a tubular element, one end is connected with flue, and the other end passes through described point
The side wall of outer cylinder 11 of structure 1 of disembarking directly is connected with the inner cylinder 12, using as by flue flue gas and sewage gas convey into
Channel in the separating mechanism 1, and ensure that the pressure in 1 inner cylinder 12 of separating mechanism is consistent with the pressure in the flue.Institute
State tubular element cross sectional shape can for rectangle, circle and triangle etc. in arbitrary shapes, with the separating mechanism 1
The link position of cylinder can be selected according to the specific requirements of service condition, as long as can ensure the flue gas and sewage in flue
Gas can be conveyed rapidly in the pressure and the flue made in 1 inner cylinder 12 of separating mechanism into the channel in the separating mechanism 1
Pressure it is consistent.Angle, which is arranged, as it to select as the case may be between 0-180 degree.In the present embodiment,
The bindiny mechanism 2 is the 1/5 circular tube shaped component that a diameter is 12 diameter of inner cylinder, and one end is connected with flue, the other end
Side wall of 11 side wall of outer cylinder directly with 1/3 height and position of inner cylinder across the separating mechanism 1 is vertically connected, using as will
Flue gas and sewage gas in flue are conveyed into the channel in the separating mechanism 1, and ensure the pressure in 1 inner cylinder 12 of separating mechanism
It is consistent with the pressure in the flue.
Specifically, the drainage mechanism 3 is a tubular element, the outer wall of one end and 1 outer cylinder 11 of separating mechanism
It is connected, during use collision cell 13 of the sewage for that will be isolated through the separating mechanism 1 from the separating mechanism 1
Interior timely, to prevent the sewage isolated from flowing everywhere in the separating mechanism 1, the flue gas being separated is taken away, Jin Eryan
Ghost image rings the separating effect of separating mechanism 1.The cross sectional shape of the tubular element can for rectangle, circle and triangle etc.
Arbitrary shape, setting position can be designed according to the specific requirements of service condition, as long as can ensure in collision cell 13
The sewage isolated can timely be discharged.As for its be arranged angle can as the case may be for 0-180 degree it
Between select.In the present embodiment, the drainage mechanism 3 is a circular tube shaped component, outside the one end vertical connection separating mechanism 1
The bottom of cylinder side wall, during use for the sewage that will be isolated through the separating mechanism 1 from the separating mechanism 1
It is discharged in time in collision cell, effectively prevents the sewage isolated and flowed everywhere in the separating mechanism, is separated
Flue gas is taken away, and then seriously affects the separating effect of separating mechanism.
Specifically, further including header tank in above-described embodiment, the header tank is a housing member, is arranged described
Going out for the drainage mechanism is closed for collecting the sewage of the drainage mechanism discharge, and by sewage in the lower section of drainage mechanism
Water end (W.E.), to prevent drainage mechanism air in drainage procedure from flowing backward into the collision cell by drainage mechanism, Jin Erying
Ring the pressure difference in the separating mechanism.The cross sectional shape of the header tank can be the arbitrary shapes such as rectangle, triangle, circle,
As long as can be used as access container.It can be any materials such as metal, plastics and wood as its making material.
In the present embodiment, the water tank is a rectangular metal case component, the lower section of the drainage mechanism is arranged in, for collecting
The sewage of drainage mechanism discharge, and the water outlet of the drainage mechanism is closed by sewage, to prevent the drainage mechanism
Air is flowed backward by drainage mechanism into the collision cell in drainage procedure, and then influences the pressure difference in the separating mechanism.
As shown in fig.3, in above-described embodiment, in order to further ensure that flue gas and sewer gas in the collision advantage
It can not adequately be collided, and then flue gas is enable farthest to be separated with the sewage in sewer gas, it can be
The inner wall of the outer cylinder 11 is set as curved shape arcuate structure, to increase the contact of flue gas with sewer gas and the collision chamber
Area；Wherein, the length of each section of arc and the determination method of angle are as follows:
Wherein,
In formula: L1For ab sections of arc length, r is flue diameter, θ1The angle in direction is flowed to sewage for ab sections, ρ is in pipeline
The actual density of flue gas and sewer gas can be measured, ρ by supersonic detector0For the standard density of water, θ0For the connection
The setting angle of mechanism；In the present embodiment, ultrasonic sensor is set in collision chamber, alternatively, in other positions of pipeline
Ultrasonic sensor is installed, to detect the actual density of flue gas and sewer gas.
Wherein,
In formula, L2For bc sections of arc length, D is the height of collision chamber, θ2The angle in direction is flowed to sewage for bc sections, ρ is
The actual density of flue gas and sewer gas, ρ in pipeline0For the standard density of water.
Wherein,In formula, L3For cd sections of arc length, θ3For cd
Section flows to the angle in direction with sewage；In the present embodiment, cd sections of selection rectilinear forms, can be conducive to be attached to outer tube side wall
Upper sewage, which is rapidly fallen, realizes that sewage collects, and then is discharged by drainage mechanism.
Obviously it can be concluded that, the separator of sewage in flue gas provided by the invention and sewer gas, what is used
In the process, the flue gas in flue and sewer gas are entered in the separating mechanism by the bindiny mechanism, in separating mechanism
It collides, and realizes the separation of sewage in flue gas and sewer gas under different effect of inertia, the sewage isolated passes through
The drainage mechanism is discharged from the separating mechanism, and flue gas then passes through the separator and continues to discharge, and has effectively achieved
The quick separating of sewage in flue gas and sewer gas, has saved the energy consumption in flue gas and sewer gas in sewage separation process, has had
The cost of sewage separation is saved to effect.Especially, by the way that separating mechanism is arranged to inner cylinder, outer cylinder and collision cell three
Point, wherein inner cylinder is directly connect with bindiny mechanism, and upper end outlet connects flue, and cylinder pressure is flue gas pressures；Outer cylinder and inner cylinder
Between the pressure of collision cell be lower than inner cylinder pressure, system forms negative pressure field, and the high flue gas of pressure rapidly diffuses into sewer gas
In the low collision cell of pressure；Meanwhile smoke density is less than sewage air tightness, hits inner cylinder under blower high speed traction in this way, it is close
Big substance is spent, inertia is big, and the small substance inertia of density is small, and the big goods and materials of inertia are brought together, and forms sewage pearl, the small object of inertia
Matter by blower traction continue forward, be discharged to flue, effectively further ensure flue gas in sewer gas sewage it is quick
The energy consumption in flue gas and sewer gas in sewage separation process has greatly been saved in separation, so save sewage separation at
This.
Obviously, various changes and modifications can be made to the invention without departing from essence of the invention by those skilled in the art
Mind and range.In this way, if these modifications and changes of the present invention belongs to the range of the claims in the present invention and its equivalent technologies
Within, then the present invention is also intended to include these modifications and variations.
Claims (10)
1. the separator of sewage in a kind of flue gas and sewer gas characterized by comprising bindiny mechanism, separating mechanism with
And drainage mechanism；Wherein,
The bindiny mechanism is arranged between the separating mechanism and flue, for conveying the flue gas in flue with sewer gas
Into in the separating mechanism；
The separating mechanism is connected with the mechanism, and the flue gas for conveying the bindiny mechanism and sewer gas are inside it
By being collided, to realize the separation of sewage in flue gas and sewer gas；
The drainage mechanism is connected with the separating mechanism, and the machine is discharged in the sewage for that will isolate through the separating mechanism
Structure, in order to collect the sewage；
During use, the flue gas in flue enters described separate by the bindiny mechanism with sewer gas to described device
It in mechanism, and collides in separating mechanism, and realizes sewage in flue gas and sewer gas under different effect of inertia
Separation, the sewage isolated are discharged from the separating mechanism by the drainage mechanism, and flue gas then passes through the separator
Continue to discharge.
2. the separator of sewage in flue gas according to claim 1 and sewer gas, which is characterized in that the separation dress
Set includes: outer cylinder, inner cylinder and collision cell；Wherein,
The outside of the separating mechanism is arranged in the outer cylinder, using the outer wall as the collision cell；
The inside of the outer cylinder, both ends and the outer cylinder airtight connection is arranged in the inner cylinder, and by being provided with its side wall
On several through-holes be connected；
The collision cell is arranged between the inner cylinder and the outer cylinder, to be collided as the flue gas with sewer gas
Place；
The outer tube inner wall is provided with several segments arcuate structure, to increase the contact of flue gas with sewer gas and the collision chamber
Area；Wherein, the length of each section of arc and the determination method of angle are as follows:
Wherein,
In formula: L1For ab sections of arc length, r is flue diameter, θ1The angle in direction is flowed to sewage for ab sections, ρ is flue gas in pipeline
With the actual density of sewer gas, can be measured by supersonic detector, ρ0For the standard density of water, θ0For the bindiny mechanism
Setting angle；In the present embodiment, ultrasonic sensor is set in collision chamber, alternatively, the other positions in pipeline are set
Ultrasonic sensor is set, to detect the actual density of flue gas and sewer gas；
Wherein,
In formula, L2For bc sections of arc length, D is the height of collision chamber, θ2The angle in direction is flowed to sewage for bc sections, ρ is pipeline
The actual density of middle flue gas and sewer gas, ρ0For the standard density of water；
Wherein,
In formula, L3For cd sections of arc length, θ3The angle in direction is flowed to sewage for cd sections.
3. the separator of sewage in flue gas according to claim 2 and sewer gas, which is characterized in that the outer cylinder
Average diameter is 1.3 times of specification of the inner diameter of steel flue.
4. the separator of sewage in flue gas according to claim 2 and sewer gas, which is characterized in that the inner cylinder
Height is 1.5 times of its diameter.
5. the separator of sewage in flue gas according to claim 2 and sewer gas, which is characterized in that the outer cylinder
Height is equal with the height of the inner cylinder.
6. the separator of sewage in flue gas according to claim 2 and sewer gas, which is characterized in that the connection machine
Structure be a tubular element, the 1/5 of a diameter of inner diameter of steel flue.
7. the separator of sewage in flue gas according to claim 2 and sewer gas, which is characterized in that the draught engine
Structure is a tubular element, is arranged in the outer tube side wall bottom.
8. the separator of sewage in flue gas according to claim 2 and sewer gas, which is characterized in that described several logical
The area in hole and be the 1/3 of the inner cylinder lateral area.
9. the separator of sewage in flue gas according to claim 8 and sewer gas, which is characterized in that adjacent described logical
Spacing between hole is the 1/3 of the through-hole diameter.
10. the separator of sewage in flue gas according to any one of claims 1 to 9 and sewer gas, which is characterized in that
Further include: header tank, sewage of the header tank for the discharge of drainage mechanism described in access, and the draining is closed by sewage
The water outlet of mechanism.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811628519.9A CN109464851A (en) | 2018-12-28 | 2018-12-28 | A kind of separator of flue gas and sewage in sewer gas |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811628519.9A CN109464851A (en) | 2018-12-28 | 2018-12-28 | A kind of separator of flue gas and sewage in sewer gas |
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| Publication Number | Publication Date |
|---|---|
| CN109464851A true CN109464851A (en) | 2019-03-15 |
Family
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| CN201811628519.9A Pending CN109464851A (en) | 2018-12-28 | 2018-12-28 | A kind of separator of flue gas and sewage in sewer gas |
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