CN102666398A - Foam removing device - Google Patents
Foam removing device Download PDFInfo
- Publication number
- CN102666398A CN102666398A CN2010800536150A CN201080053615A CN102666398A CN 102666398 A CN102666398 A CN 102666398A CN 2010800536150 A CN2010800536150 A CN 2010800536150A CN 201080053615 A CN201080053615 A CN 201080053615A CN 102666398 A CN102666398 A CN 102666398A
- Authority
- CN
- China
- Prior art keywords
- foam
- seawater
- discharge
- recovery groove
- drain passageway
- 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.)
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Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D19/00—Degasification of liquids
- B01D19/02—Foam dispersion or prevention
- B01D19/04—Foam dispersion or prevention by addition of chemical substances
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D19/00—Degasification of liquids
- B01D19/0005—Degasification of liquids with one or more auxiliary substances
- B01D19/001—Degasification of liquids with one or more auxiliary substances by bubbling steam through the liquid
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D21/00—Separation of suspended solid particles from liquids by sedimentation
- B01D21/24—Feed or discharge mechanisms for settling tanks
- B01D21/2433—Discharge mechanisms for floating particles
- B01D21/2438—Discharge mechanisms for floating particles provided with scrapers on the liquid surface for removing floating particles
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/08—Seawater, e.g. for desalination
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/18—Nature of the water, waste water, sewage or sludge to be treated from the purification of gaseous effluents
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2303/00—Specific treatment goals
- C02F2303/12—Prevention of foaming
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Health & Medical Sciences (AREA)
- Toxicology (AREA)
- Dispersion Chemistry (AREA)
- Removal Of Floating Material (AREA)
- Degasification And Air Bubble Elimination (AREA)
- Physical Water Treatments (AREA)
Abstract
A foam removing device (1) is installed in a discharge channel (10) into which discharge seawater flows which has been discharged after use in a power plant. A foam collecting unit (2) collects foam (B) floating at the water level (WL) of the discharge seawater flowing through the discharge channel (10). The foam (B) collected by the foam collecting unit (2) flows into a foam collection tank (3). A defoaming unit (4) defoams the foam (B) that flows into the foam collection tank (3). The foam components obtained by defoaming the aforementioned foam (B) by means of the aforementioned defoaming unit (4), and the discharge seawater which flowed into the foam collection tank (3) along with the foam, are returned by a release unit (6) to nearby the discharge channel (10).
Description
Technical field
The present invention relates in the wastewater treatment of burning coal, burning the flue gas desulfurization equipment that is suitable in the generating set of crude oil and burning heavy oil etc., relate in particular to the foam of foam being removed from the draining of using the seawater method to carry out the flue gas desulfurization equipment of desulfurization and remove device.
Background technology
In the past, be in the generating set of fuel with coal, former wet goods, the sulfurous gas (SO that the combustion exhaust of discharging from boiler (below, be called " boiler waste gas ") contains in boiler waste gas
2) oxysulfide (SOx) that waits remove after to airborne release.As the desulfurization method of implementing the flue gas desulfurization equipment that this desulfurization handles, known have lime lime-gypsum method, jet drying method and a seawer washing method.
Wherein, flue gas desulfurization equipment (below, be labeled as " sea water desulfuration device ") adopts the seawer washing method of using seawater as absorption agent.In this mode, be the internal feed seawater and the boiler waste gas of vertical thionizer (absorption tower) for example to making the such barrel shape of cylinder roughly, be absorption liquid produces the gas-to-liquid contact based on wet type thus with the seawater, oxysulfide is removed.
The seawater (discharge seawater) that uses in seawater after the desulfurization of in above-mentioned thionizer, using as absorption agent, the cooling in generating set is discharged to the off-lying sea, from the discharge seawater of sea water desulfuration device and fresh sea water mixing.Discharge that seawater flows and during draining, come decarbonate (aeration) from the effusive ventilation of ventilation nozzle on the bottom surface that is arranged on drain passageway in drain passageway through making fine ventilation bubble.
The zone that makes the fine effusive ventilation of ventilation bubble and discharge the decarbonate of seawater of so, implementing in the drain passageway is called the ventilation zone.
When discharging the adjustment of pH value and DO value of seawater through above-mentioned decarbonate; Since the interaction of the foaming composition of the organism that contains in fine ventilation bubble, the seawater etc., and in drain passageway, can produce foam on the water surface of mobile discharge seawater.Directly discharge and difficult the elimination with discharging by the peripherad marine site of seawater from drain passageway for this foam.Therefore, have this foam and float on outer sea and the preferred problem that on view, becomes.
In addition, even in the flue gas desulfurization equipment that does not adopt the seawer washing method, also there is the problem that possibly produce the foaming problem because of seawater proterties etc.
In order to solve the above problems, proposed to discharge the technology (for example, with reference to patent documentation 1) that seawater is removed foam from mobile in drain passageway.Through so foam being removed, and can solve the problem on the view that foam causes from discharging seawater.
[TP formerly]
[patent documentation]
Real the opening of [patent documentation 1] Japan put down the 5-22092 communique
Summary of the invention
Yet such like the technology of patent documentation 1, from discharge the method that seawater removes foam, existence is difficult to problem that the foaming composition that contains in the foam of removing is handled.
For example, consider to have foaming composition is formed powdery or slurries shape from foam separation, to the treatment process that Hui Chu abandons of abandoning of generating set.Yet; Foaming composition is different owing to the difference of burnt fuel in the boiler; And with the isolating method of foaming composition, promptly based on the separation method of strainer, do not establish based on the separation method of cf-, existence can't easily separate such problem from foam with foaming composition from foam.
The present invention makes in order to solve above-mentioned problem, and its purpose is to provide a kind of foam that can foam removed and easily foaming composition handled from the seawater face of drain passageway to remove device.
To achieve these goals, the present invention provides following method.
The present invention relates to a kind of foam and remove device; Be arranged in generating set on the drain passageway that the discharge seawater that uses and be discharged from flow through; It is characterized in that said foam is removed device and had: the water surface to the said discharge seawater of mobile in said drain passageway is attend the foam recovery portion that institute's buoyant foam reclaims; The foam recovery groove that foam flowed into by this foam recovery portion recovery; Froth breaking portion with the foam elimination that flow into this foam recovery groove; And make through said foam being eliminated the foaming composition that obtains, and turned back near the discharge portion of said drain passageway with the said discharge seawater that said foam flow into said foam recovery groove by said froth breaking portion.
According to the present invention, the water surface of discharging seawater from mobile drain passageway is recovered to the foam of foam recovery groove and is eliminated by froth breaking portion, this foamy foaming composition with the discharge seawater of foam recovery groove turn back to drain passageway near.Therefore, and foaming composition is compared from discharging the isolating method of seawater as powder or slurries, can easily be handled foaming composition.
Need to prove that the organism that foaming composition contains in seawater with script etc. is a principal constituent, even therefore foaming composition returns to drain passageway, mobile discharge seawater can not conflicted with environmental criteria yet in drain passageway.
In foregoing invention, preferably, be provided with the mixing part that the said discharge seawater that flows into said foam is stirred at said foam recovery groove.
According to the present invention, through the discharge seawater that flow into the foam recovery groove is stirred, and foaming composition can not precipitate to the foam recovery groove.In other words, return drain passageway through discharge portion with discharging seawater, therefore be difficult to be deposited to the bottom surface of foam recovery groove through the foaming composition after the stirring of mixing part.
Usually, when the discharge seawater of foam recovery groove not being stirred, because of the available volume reducing of sedimentary foaming composition foam recovery groove, the operation that therefore need sedimentary foaming composition be removed.With respect to this, to remove in the device at foam of the present invention, foaming composition can not be deposited to the bottom surface of foam recovery groove, the operation that therefore need sedimentary foaming composition not removed, and, can reduce the frequency that carries out operation.
[invention effect]
Foam according to the present invention is removed device; The water surface of discharging seawater from mobile drain passageway is recovered to the foam of foam recovery groove and is eliminated by froth breaking portion; This foamy foaming composition with the discharge seawater of foam recovery groove turn back to drain passageway near, therefore play and can from the seawater face of drain passageway, the such effect of foaming composition removed and easily handled to foam.
Description of drawings
Fig. 1 is that the foam of an explanation embodiment of the present invention is removed the vertical view of the structure of device.
Fig. 2 is the schematic synoptic diagram of the foam of explanatory view 1 structure of removing device.
Fig. 3 is the synoptic diagram of structure of the foam recovery portion of explanatory view 1.
Fig. 4 is the sectional view of structure of the guide portion of explanatory view 3.
Fig. 5 is the synoptic diagram of configuration of foam recovery groove, froth breaking portion and the mixing part of explanatory view 2.
Embodiment
Referring to figs. 1 through Fig. 5, explain that the foam of an embodiment of the present invention is removed device.
Fig. 1 is that the foam of this embodiment of explanation is removed the vertical view of the structure of device.Fig. 2 is the schematic synoptic diagram of the foam of explanatory view 1 structure of removing device.
It is to separate the device of removing and handling with attending the buoyant foam B of institute from the water surface WL that for example uses seawater after the desulfurization that seawater discharges as the flue gas desulfurization equipment of absorption agent promptly to discharge seawater that the foam of this embodiment is removed device 1, and is that the water surface WL that mobile in drain passageway 10 is discharged seawater is attend the device that the buoyant foam B of institute handles.
Like Fig. 1 and shown in Figure 2, remove device 1 at foam and mainly be provided with foam recovery portion 2, foam recovery groove 3, froth breaking portion 4, mixing part 5, reach discharge portion 6.
As shown in Figure 1, drain passageway 10 is the streams that surrounded by wall 11, and is with the stream of the discharge seawater of discharging from flue gas desulfurization equipment to the off-lying sea discharging.Regional 12A, 12B, 12C promptly take a breath in the zone that drain passageway 10 is provided with the decarbonate of discharging seawater.
Need to prove,, can use known structure, do not limit especially as the structure of the regional 12A of ventilation, 12B, 12C.
Fig. 3 is the synoptic diagram of structure of the foam recovery portion of explanatory view 1.
To shown in Figure 3, foam recovery portion 2 will reclaim from drain passageway 10 by buoyant foam B on the water surface WL that discharges seawater like Fig. 1.
Mainly be provided with guide portion 21, foam maintaining part 22, dolly 23, reach directing plate 14 in foam recovery portion 2.
Fig. 4 is the sectional view of structure of the guide portion of explanatory view 3.
Like Fig. 3 and shown in Figure 4, be provided with a pair of beam-like element 21A and trolley track 21B in guide portion 21.
A pair of beam-like element 21A crosscut drain passageway 10 and extending is linked and the concrete that extends in parallel to each other forms by the upper end with the wall 11 of drain passageway 10.
Trolley track 21B is the tabular member that is formed by the stainless steel of the upper surface that is configured in beam-like element 21A metals such as (SUS).Be configured to, configuration dolly 23 on trolley track 21B is arranged on the rake face 23B skived foam of dolly bottom and on directing plate 14, slides.
On the other hand, the lower surface of the beam-like element 21A in the guide portion 21 that disposed of the downstream side (downside of Fig. 3) in discharging the flowing of seawater disposes foam maintaining part 22.
The end of foam recovery groove 3 sides (right side of Fig. 2) in the guide portion 21 is outstanding towards foam recovery groove 3 from drain passageway 10.
On the other hand, between a pair of guide portion 21 of the wall 11 of drain passageway 10, be provided with peristome 13 and directing plate 14.
Peristome 13 is that mobile foam B compares with other part to the part that foam recovery groove 3 flows in drain passageway 10, is the part of the height step-down of wall 11.Be provided with directing plate 14 at peristome 13.
Directing plate 14 makes in drain passageway 10 mobile foam B when foam recovery groove 3 flows into, with foam B with discharge seawater and separate.In addition, directing plate 14 is arranged on the inclined wall of peristome 13, constitutes from the drain passageway 10 oblique face of square neck towards foam recovery groove 3 and upwards.
Need to prove that the high mode of maximum stage when full sea (for example water level) that directing plate 14 is discharged seawater with its upper end than mobile in drain passageway 10 disposes.
Foam maintaining part 22 is with the membranaceous or tabular parts that remain on the below in the zone that dolly 23 moves back and forth with the discharge seawater of drain passageway 10 towards the foam B of downstream flow.Therefore, the lower end of foam maintaining part 22 arrives the water surface WL of mobile discharge seawater in drain passageway 10 at least.
Need to prove,, can use curtain wall, bubble to assemble the known parts of buoyancy aid, oil barrier etc. as foam maintaining part 22.
Dolly 23 moves back and forth on guide portion 21, will be reclaimed to foam recovery groove 3 by the foam that foam maintaining part 22 is kept thus.
Mainly be provided with dolly main body 23A and rake face 23B at dolly 23.
Dolly main body 23A keeps rake face 23B, moves back and forth on the trolley track 21B of guide portion 21 by being arranged on the wheel on the dolly main body 23A.The parts of the known generation motivating force of use phonomoter etc. in the moving of dolly main body 23A.
Rake face 23B moves back and forth with dolly main body 23A, will in drain passageway 10, reclaim to foam recovery groove 3 by mobile foam B thus.Rake face 23B forms membranaceous or tabular, and is installed in that dolly main body 23A goes up and the lower end arrives the mode of mobile foam B in drain passageway 10 at least and disposes with the upper end.
In addition, rake face 23B collects foam B when the direction near peristome 13 moves, and when the direction of leaving peristome 13 moves, does not collect foam B.
Particularly, rake face 23B is bent into two towards peristome 13 sides near the central authorities of above-below direction.When the direction near peristome 13 moves, rake face 23B extends as the crow flies, collects foam B by following the bringing in of rake face 23B.On the other hand, when the direction of leaving peristome 13 moves, rake face 23B towards peristome 13 direction bendings, therefore can not collect foam B by following the bringing in of rake face 23B near central authorities.
But perhaps replace the structure that rake face 23B is formed bending, also can with rake face 23B form can recoverable deformation towards peristome 13 directions structure, limit especially.
Fig. 5 is the synoptic diagram of configuration of foam recovery groove, froth breaking portion and the mixing part of explanatory view 2.
Like Fig. 2 and shown in Figure 5, mainly be provided with first area 31 of carrying out froth breaking and the second area 32 that carries out froth breaking and stirring at foam recovery groove 3.
The foam B that foam recovery groove 3 is reclaimed eliminates in froth breaking portion 4.
Like Fig. 2 and shown in Figure 5, mainly be provided with froth breaking nozzle 41 and froth breaking atomizing pump 42 in froth breaking portion 4.
Froth breaking nozzle 41 sprays seawater from the top and eliminates foam B for foam B.Supply with the discharge seawater from froth breaking atomizing pump 42 to froth breaking nozzle 41.Froth breaking nozzle 41 is configured in first area 31 and the top of second area 32 in the foam recovery groove 3.
Need to prove,, can use known structure, do not limit especially as the structure of froth breaking nozzle 41.
Froth breaking atomizing pump 42 will be supplied with to froth breaking nozzle 41 from the seawater that drain passageway 10 is obtained.In this embodiment, be applicable to that the example that is provided with 2 froth breaking atomizing pumps 42 describes.Thus, can use a froth breaking atomizing pump 42 that seawater is supplied with to froth breaking nozzle 41, and with another froth breaking atomizing pump 42 as preparing.
Need to prove that when the quantitative change of the foam B that should eliminate, the platform number of froth breaking atomizing pump 42 that can be through changing work is dealt with, and limits especially.
The inlet side (upstream side) of froth breaking atomizing pump 42 be provided be essentially standard-sized sheet or full cut-off froth breaking with flow valve 43, outlet side (downstream side) be provided with adjusting to pump flow into or from the froth breaking of the flow of the effusive discharge seawater of pump with flow valve 43.
Mixing part 5 prevents that the foaming composition of foam B is deposited to the bottom surface of foam recovery groove 3.Mixing part 5 is configured in the second area 32 of foam recovery groove 3, in this embodiment, is applicable to that the example that is provided with 6 mixing parts 5 describes.
As shown in Figure 2,5 mainly are provided with rotating part 51, stirring phonomoter 52 in the mixing part.
Discharge seawater in the second area 32 of 51 pairs of foam recovery grooves 3 of rotating part stirs, and prevents that the foaming composition of foam B from precipitating.
The stirring parts that is provided with bar-shaped axial region and extends at rotating part 51 with axial region quadrature ground.The axial region of rotating part 51 connects into stirring phonomoter 52 can transmit rotary driving force, and the axial region of rotating part 51 and stirring parts drive by stirring phonomoter 52 rotations.
Stir 51 rotations of phonomoter 52 driven in rotation portions.In this embodiment, be applicable to that rotating part 51 and the example that stirring phonomoter 52 disposes one to one describe.
Need to prove that the ratio of rotating part 51 and the number that stirs phonomoter 52 can also can be more than this for one to one both, also can be below this, limited especially.
Need to prove that when the amount of discharge seawater that returns to drain passageway 10 and foaming composition changed, the platform number of foam slurry pump 62 that can be through changing work was dealt with, and limits especially.
The inlet side (upstream side) of foam slurry pump 62 be provided be essentially standard-sized sheet or full cut-off discharging with flow valve 63, outlet side (downstream side) be provided with adjusting to pump flow into or from the discharging of the flow of the effusive discharge seawater of pump with flow valve 63.
Next, referring to figs. 1 through Fig. 5, explain that the foam that is made up of above-mentioned structure removes the effect of device 1.
The discharge seawater of for example discharging from flue gas desulfurization equipment flows into to drain passageway 10, and is as shown in Figure 1, in the regional 12A of ventilation, 12B, 12C, carries out decarbonate.Form foam B at the water surface WL that has carried out the discharge seawater behind the decarbonate, (downside of Fig. 1) flows foam B towards downstream with discharging seawater.
Like Fig. 2 and shown in Figure 3, below foam recovery portion 2, stopped under the effect of foam maintaining part 22 towards the foam B of downstream flow.
The foam B that is stopped is recovered to foam recovery groove 3 through the dolly 23 that on the direction of crosscut drain passageway 10, moves back and forth along guide portion 21.
Particularly, when dolly main body 23A along guide portion 21 when foam recovery groove 3 moves, through the rake face 23B that extends downwards from dolly main body 23A, the foam B that will stop collects towards foam recovery groove 3.
When rake face 23B arrival is arranged at the inclined wall 14 of peristome 13, be accompanied by moving of dolly main body 23A, the lower end of rake face 23B is lifted to the top along the wall of inclined wall 14.At this moment, foam B is kept by rake face 23B, discharge on the other hand seawater the gap of rake face 23B and inclined wall 14 towards below flow down.That is, foam B separates with the discharge seawater.
When the end of foam recovery groove 3 sides of rake face 23B through inclined wall 14, the foam B that is kept by rake face 23B falls to foam recovery groove 3.
The foam B that drops to foam recovery groove 3 is directed to first area 31 at first, is directed to second area 32 then.
In first area 31 and second area 32, spray the discharge seawater to foam B, and foam B is eliminated from froth breaking nozzle 41.
Supply with from drain passageway 10 by froth breaking atomizing pump 42 from the discharge seawater that froth breaking nozzle 41 sprays.In this embodiment, be applicable to that the example of 1 running in 2 froth breaking atomizing pumps 42 describes.In this case, open with flow valve 43, close with flow valve 43 at the upstream side of the froth breaking atomizing pump 42 that stops and the froth breaking of downstream side configuration at the upstream side of the froth breaking atomizing pump 42 that turns round and the froth breaking of downstream side configuration.
Therefore, discharging seawater supplies with to froth breaking nozzle 41 with the froth breaking atomizing pump 42 of flow valve 43 and running via the froth breaking of opening.
Need to prove that in Fig. 2, the froth breaking of opening represented by hollow with flow valve 43, the froth breaking of closing is represented by blacking with flow valve 43.
The foaming composition of organism that in foam B, contains in the seawater to be comprised etc., when foam B was eliminated, the discharge seawater of foaming composition in foam recovery groove 3 sneaked into.
In second area 32, discharge seawater and stir, so foaming composition also is stirred with discharging seawater by mixing part 5.
That is, stir phonomoter 52 through supply capability and produce rotary driving force, 51 rotations of driven in rotation portion.When rotating part 51 is rotated by driving, also in the discharge seawater, rotate in the stirring parts of the lower end of axial region configuration.Thus, produce current in the discharge seawater of second area 32 and for example produce round-robin current along the vertical direction, proportion is distributed in the discharge seawater than discharging the heavy foaming composition of seawater equably.
The discharge seawater of second area 32 and the foaming composition that comprises thereof turn back near the zone, bottom surface of drain passageway 10 via the drain flow path 61 and the foam slurry pump 62 of discharge portion 6.
In this embodiment, be applicable to that the example of 1 running in 2 foam slurry pumps 62 describes.In this case, open with flow valve 63, close with flow valve 63 at the upstream side of the foam slurry pump 62 that stops and the discharging of downstream side configuration at the upstream side of the foam slurry pump 62 that turns round and the discharging of downstream side configuration.
Therefore, discharging seawater supplies with to froth breaking nozzle 41 with the foam slurry pump 62 of flow valve 63 and running via the discharging of opening.
Need to prove that in Fig. 2, the discharging of opening represented by hollow with flow valve 63, the discharging of closing is represented by blacking with flow valve 63.
Need to prove that foam slurry pump 62 and discharging are controlled based on the measured value of the horizon sensor 64 that the water level of the discharge seawater that is configured in foam recovery groove 3 is measured with flow valve 63.
In addition, froth breaking atomizing pump 42, foam slurry pump 62, froth breaking also can be controlled qualification especially based on the measured value of the horizon sensor 64 that the water level of the discharge seawater that is configured in foam recovery groove 3 is measured with flow valve 43 and discharging with flow valve 63.
According to above-mentioned structure; The foam B that the water surface WL that discharges seawater from mobile drain passageway 10 is recovered to foam recovery groove 3 is eliminated by froth breaking portion 4, said foamy foaming composition with the discharge seawater of foam recovery groove 3 turn back to drain passageway 10 near.Therefore, and foaming composition is compared from discharging the isolating method of seawater as powder, slurries, can easily be handled foaming composition.
Need to prove that foaming composition is a principal constituent with the organism that comprises in the seawater etc. originally, even therefore foaming composition returns drain passageway 10, mobile is discharged seawater and also can not conflicted with environmental criteria in drain passageway 10.
Because the discharge seawater that uses 5 pairs of mixing parts to flow into foam recovery groove 3 stirs, so foaming composition can not be deposited to foam recovery groove 3.In other words, the foaming composition that stirs through mixing part 5 returns to drain passageway 10 with discharging seawater through discharge portion 6, therefore is difficult to be deposited to the bottom surface of foam recovery groove 3.
Usually, when the discharge seawater of foam recovery groove 3 not being stirred, because of the available volume reducing of sedimentary foaming composition foam recovery groove 3, the operation that therefore need sedimentary foaming composition be removed.With respect to this, remove in the device 1 at the foam of this embodiment, because foaming composition can not be deposited to the bottom surface of foam recovery groove 3, the operation that therefore need sedimentary foaming composition not removed, and can reduce the frequency that carries out operation.
[label declaration]
1 foam is removed device
2 foam recovery portions
3 foam recovery grooves
4 froth breaking portions
5 mixing parts
6 discharge portion
Claims (2)
1. a foam is removed device, is arranged in generating set on the drain passageway that the discharge seawater that uses and be discharged from flow through, and wherein, said foam is removed device and had:
The water surface to the said discharge seawater of mobile in said drain passageway is attend the foam recovery portion that institute's buoyant foam reclaims;
The foam recovery groove that foam flowed into by this foam recovery portion recovery;
Froth breaking portion with the foam elimination that flow into this foam recovery groove; And
Make through said foam being eliminated the foaming composition that obtains, and turned back near the discharge portion of said drain passageway from said foam recovery groove with the said discharge seawater that said foam flow into said foam recovery groove by said froth breaking portion.
2. foam according to claim 1 is removed device, wherein,
Be provided with the mixing part that the said discharge seawater that flows into said foam is stirred at said foam recovery groove.
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2009-272762 | 2009-11-30 | ||
| JP2009272762A JP5595019B2 (en) | 2009-11-30 | 2009-11-30 | Foam treatment device |
| PCT/JP2010/064955 WO2011065082A1 (en) | 2009-11-30 | 2010-09-01 | Foam removing device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN102666398A true CN102666398A (en) | 2012-09-12 |
| CN102666398B CN102666398B (en) | 2015-04-29 |
Family
ID=44066185
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201080053615.0A Active CN102666398B (en) | 2009-11-30 | 2010-09-01 | Foam removing device |
Country Status (5)
| Country | Link |
|---|---|
| JP (1) | JP5595019B2 (en) |
| CN (1) | CN102666398B (en) |
| SA (1) | SA110310718B1 (en) |
| TW (1) | TWI424963B (en) |
| WO (1) | WO2011065082A1 (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104383721A (en) * | 2014-11-18 | 2015-03-04 | 庞海峰 | Method and equipment for filtering liquid bubbles |
| CN106745987A (en) * | 2016-12-21 | 2017-05-31 | 武汉凯迪电力环保有限公司 | A kind of high-efficiency low energy consumption sea water desulfuration oxidative system |
| CN106955508A (en) * | 2017-05-26 | 2017-07-18 | 华润电力（海丰）有限公司 | A kind of spray defoaming device |
| CN114411445A (en) * | 2022-01-25 | 2022-04-29 | 临沂大瑞木业有限公司 | Production equipment and method of composite impregnated paper |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US9771279B2 (en) * | 2015-03-31 | 2017-09-26 | General Electric Technology Gmbh | Foam intercept system |
| CN108002589A (en) * | 2017-12-06 | 2018-05-08 | 天津核海源科技发展有限公司 | A kind of contamination collection device in nuclear power station draining |
| US20200354241A1 (en) * | 2019-05-10 | 2020-11-12 | Sugino Machine Limited | Liquid treatment apparatus and liquid treatment method |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH01151803U (en) * | 1988-03-25 | 1989-10-19 | ||
| JPH0294574A (en) * | 1988-09-30 | 1990-04-05 | Teijin Ltd | Flexible solar cell sheet |
| JP2008200620A (en) * | 2007-02-21 | 2008-09-04 | Mitsubishi Heavy Ind Ltd | Bubble recovery apparatus and bubble recovery system |
| WO2009014053A1 (en) * | 2007-07-24 | 2009-01-29 | Mitsubishi Heavy Industries, Ltd. | Foam recovery apparatus and foam recovery system |
| CN101428904A (en) * | 2008-12-05 | 2009-05-13 | 安徽工业大学 | Gas winding cycle stream stirring system for open type oxygen lack pool |
| CN201321408Y (en) * | 2008-12-31 | 2009-10-07 | 大连力达环境工程有限公司 | Non-clogging water jetting foam breaker |
Family Cites Families (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CH662551A5 (en) * | 1984-05-03 | 1987-10-15 | Werner Nill | CATCHING DEVICE FOR FOAM. |
| JPH0994574A (en) * | 1995-09-29 | 1997-04-08 | Hitachi Kiden Kogyo Ltd | Method for crushing scum and apparatus therefor |
| JP2005040734A (en) * | 2003-07-24 | 2005-02-17 | Hotani:Kk | Method for separating oil-mixed alkaline liquid |
| JP4908278B2 (en) * | 2007-03-19 | 2012-04-04 | 株式会社東芝 | Defoaming method for foaming waste liquid |
-
2009
- 2009-11-30 JP JP2009272762A patent/JP5595019B2/en active Active
-
2010
- 2010-09-01 WO PCT/JP2010/064955 patent/WO2011065082A1/en active Application Filing
- 2010-09-01 CN CN201080053615.0A patent/CN102666398B/en active Active
- 2010-09-15 TW TW099131307A patent/TWI424963B/en active
- 2010-09-25 SA SA110310718A patent/SA110310718B1/en unknown
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH01151803U (en) * | 1988-03-25 | 1989-10-19 | ||
| JPH0294574A (en) * | 1988-09-30 | 1990-04-05 | Teijin Ltd | Flexible solar cell sheet |
| JP2008200620A (en) * | 2007-02-21 | 2008-09-04 | Mitsubishi Heavy Ind Ltd | Bubble recovery apparatus and bubble recovery system |
| WO2009014053A1 (en) * | 2007-07-24 | 2009-01-29 | Mitsubishi Heavy Industries, Ltd. | Foam recovery apparatus and foam recovery system |
| CN101428904A (en) * | 2008-12-05 | 2009-05-13 | 安徽工业大学 | Gas winding cycle stream stirring system for open type oxygen lack pool |
| CN201321408Y (en) * | 2008-12-31 | 2009-10-07 | 大连力达环境工程有限公司 | Non-clogging water jetting foam breaker |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104383721A (en) * | 2014-11-18 | 2015-03-04 | 庞海峰 | Method and equipment for filtering liquid bubbles |
| CN106745987A (en) * | 2016-12-21 | 2017-05-31 | 武汉凯迪电力环保有限公司 | A kind of high-efficiency low energy consumption sea water desulfuration oxidative system |
| CN106745987B (en) * | 2016-12-21 | 2023-03-14 | 武汉凯迪电力环保有限公司 | High-efficient low energy consumption sea water desulfurization oxidation system |
| CN106955508A (en) * | 2017-05-26 | 2017-07-18 | 华润电力（海丰）有限公司 | A kind of spray defoaming device |
| CN114411445A (en) * | 2022-01-25 | 2022-04-29 | 临沂大瑞木业有限公司 | Production equipment and method of composite impregnated paper |
| CN114411445B (en) * | 2022-01-25 | 2023-01-03 | 临沂大瑞木业有限公司 | Production equipment and method of composite impregnated paper |
Also Published As
| Publication number | Publication date |
|---|---|
| TWI424963B (en) | 2014-02-01 |
| WO2011065082A1 (en) | 2011-06-03 |
| JP5595019B2 (en) | 2014-09-24 |
| SA110310718B1 (en) | 2015-02-05 |
| TW201127754A (en) | 2011-08-16 |
| CN102666398B (en) | 2015-04-29 |
| JP2011115675A (en) | 2011-06-16 |
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