CN207913690U - A kind of reunion liquid compounding system - Google Patents
A kind of reunion liquid compounding system Download PDFInfo
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- CN207913690U CN207913690U CN201721901325.2U CN201721901325U CN207913690U CN 207913690 U CN207913690 U CN 207913690U CN 201721901325 U CN201721901325 U CN 201721901325U CN 207913690 U CN207913690 U CN 207913690U
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Abstract
The utility model is related to a kind of reunion liquid compounding system, including emulsion tank, material-compound tank and blending tank, there is emulsion tank solid-state agglomerator mouth, the first water filling port and emulsion outlet is added；There is material-compound tank liquid agglomerator mouth, emulsion entrance, the second water filling port and mixture export, emulsion entrance and emulsion outlet is added；There is blending tank entry to mixed solution, third water filling port and the outlet of reunion liquid, entry to mixed solution to be connected to mixture export；It is equipped with blender in emulsion tank, material-compound tank and blending tank.Above-mentioned reunion liquid compounding system, solid-state agglomerator is mixed with water in advance and is emulsified, emulsion is extracted again is mixed to get concentration reunion liquid with liquid agglomerator, again concentration reunion liquid is diluted to obtain required reunion liquid in blending tank, the problem of water forms spherical indissoluble object and influences preparation and the using effect of reunion liquid can be met to avoid solid-state agglomerator powder in reunion liquid process for preparation existing in the prior art.
Description
Technical field
The utility model belongs to chemical agglomeration technical field, and in particular to a kind of reunion liquid compounding system.
Background technology
Coal is the main body energy in China, has reached 10.5 hundred million kilowatts by 2016 end of the year whole nation thermoelectricitys installation total amount, accounts for
The 63.6% of electric power installation total amount, and in the following quite a long time, electric power of the China based on coal fired power generation supplies
Pattern is answered not change.However the flue gas of coal-burning power plant's discharge is the important emission source of each pollutant in China's air,
The SO of super half2, NOx and inhalable particulate matter derive from coal-burning power plant, all kinds of waste water that power plant generates in addition, as desulfurization is useless
The process problem up to standard of water etc. is still more prominent.With the continuous improvement of people's environmental consciousness, the ring of coal-burning power plant in recent years
Border problem is concerned, and under the overall background of China's energy-saving and emission-reduction, a series of laws and regulations are put into effect in succession to limit and specification
The blowdown behavior of coal-burning power plant, also increasingly stringent for the pollution emission standard of coal-burning power plant, purpose is exactly to reduce to greatest extent
Coal-burning power plant's pollutant especially inhalable particulate matter, SO2, NOx, waste water etc. discharge capacity, it is final to realize the ultralow row of flue gas
It puts and wastewater zero discharge.
Inhalable particulate matter (i.e. fine particle) is because grain size is smaller, difficult charged, difficult in the pollutant of coal-burning power plant's discharge
The features such as wetting is difficult complete by the removal of the means such as traditional electrostatic precipitation, bag-type dust, and the concentration of flue gas emission mouth is still
Up to 30mg/m3, it is far above 10mg/m3Minimum discharge standard.Currently, fine particle is reunited, reinforcing dedusting technology is that more have
The processing method of effect, flue gas particles concentration that treated are better than national standard, can reach 5mg/m3Below.Reunion dedusting technology
The discharge that coal-fired fine particle is controlled by chemical agglomeration method, is not changing existing cleaner and parameter, is not increasing large size
Under the premise of equipment, can On-line construction with installation, installation site flexibly, short construction period, do not influence the normal of power plant/cement plant
Operation and production；In reunion system operation, using industry water, non-wastewater discharge, non-secondary pollution.
Currently, the preparation of reunion liquid is all that solid-state agglomerator, liquid agglomerator and water are added in blending tank to stir and evenly mix.
But solid-state agglomerator powder meets water electrode and easily forms spherical indissoluble object (being frequently referred to " flake ")：When solid-state agglomerator powder is added
When in water, viscosity is very big after solid-state agglomerator powder chance water-solubleization on agglomerates surface, and solid-state agglomerator powder is mutually bonded in
Together, it forms fluid-tight film and is wrapped in agglomerates surface, and then water is prevented to enter inside agglomerates, to form spherical indissoluble
Object.The density and mixed solution density difference of spherical indissoluble object are little, and spherical indissoluble object disperse is in the solution, it is difficult to it removes, from
And influence the preparation and application of reunion liquid.
Utility model content
The utility model embodiment is related to a kind of reunion liquid compounding system, can at least solve the segmental defect of the prior art.
The utility model embodiment is related to a kind of reunion liquid compounding system, including emulsion tank, material-compound tank and blending tank,
There is the emulsion tank solid-state agglomerator mouth, the first water filling port and emulsion outlet is added；
There is the material-compound tank liquid agglomerator mouth, emulsion entrance, the second water filling port and mixture export, institute is added
State emulsion entrance and the emulsion outlet；
The blending tank have entry to mixed solution, third water filling port and reunion liquid outlet, the entry to mixed solution with it is described
Mixture export is connected to；
It is equipped with blender in the emulsion tank, the material-compound tank and the blending tank.
As one of embodiment, be disposed with solid hopper above the emulsion tank, the solid hopper by tremie pipe with it is described
Mouth connection is added in solid-state agglomerator, and metering units are equipped in the tremie pipe.
As one of embodiment, the metering units include batch box, the tremie pipe, the batch box and the solid material
Bucket is each equipped with heating mechanism.
As one of embodiment, the heating mechanism includes heating tube of the screw arrangement in corresponding utensil inner cavity；
Or, the tremie pipe, the batch box and the solid hopper are ironware, the heating mechanism includes coiling
Heating tube on corresponding utensil outer wall.
As one of embodiment, it is disposed with above the material-compound tank and the liquid material that mouth is connected to is added with the liquid agglomerator
Tank, the liquid tank is interior to be equipped with the first liquid level detection unit.
As one of embodiment, the liquid tank is connected with fluid infusion bucket, and the fluid infusion bucket passes through liquid supplementation channel and the liquid
Batch can connects, and the kinetic pump with the first liquid level detection unit interlocked control is equipped in the liquid supplementation channel.
As one of embodiment, the second level sensing is equipped in the emulsion tank, the material-compound tank and the blending tank
Unit.
As one of embodiment, the emulsion tank, the material-compound tank and the mixing pot bottom are respectively connected with blow down branch,
It is equipped with blowdown valve on each blow down branch.
As one of embodiment, which further includes blowdown manifold, each blow down branch with the blowdown
Manifold connections are equipped with blowdown main valve on the blowdown manifold.
As one of embodiment, also there is the blending tank desulfurization wastewater mouth is added, and mouth connection is added in the desulfurization wastewater
There is desulfurization wastewater organization of supply.
The utility model embodiment at least has the advantages that：
Solid-state agglomerator is mixed with water emulsify in advance, then taken out by reunion liquid compounding system provided by the utility model
It takes emulsion to be mixed to get concentration reunion liquid with liquid agglomerator, then concentration reunion liquid is diluted to obtain institute in blending tank
The reunion liquid needed can be formed spherical to avoid solid-state agglomerator powder chance water in reunion liquid process for preparation existing in the prior art
Indissoluble object and the problem of influence preparation and the using effect of reunion liquid.Reunite by previously prepared concentration reunion liquid, then to concentration
Liquid dilutes and prepares the reunion liquid that is suitable for the application of, convenient for the reunion liquid that controls the addition of agglomerator and finally obtain
Concentration；Moreover, first preparing concentrate, the reunion liquid of prepared and diluted, the storage of concentrate do not need big volume again when needed
Storage device can save equipment cost and space, and convenient for management.
Description of the drawings
In order to illustrate the embodiment of the utility model or the technical proposal in the existing technology more clearly, below will be to embodiment
Or attached drawing needed to be used in the description of the prior art is briefly described, it should be apparent that, the accompanying drawings in the following description is only
It is some embodiments of the utility model, for those of ordinary skill in the art, in the premise not made the creative labor
Under, it can also be obtained according to these attached drawings other attached drawings.
Fig. 1 is the structural schematic diagram for the reunion liquid compounding system that the utility model embodiment provides；
Fig. 2 is the structural schematic diagram for the desulfurization wastewater organization of supply that the utility model embodiment provides.
Specific implementation mode
The following will be combined with the drawings in the embodiments of the present invention, carries out the technical scheme in the embodiment of the utility model
Clearly and completely describe, it is clear that the described embodiments are only a part of the embodiments of the utility model, rather than whole
Embodiment.Based on the embodiments of the present invention, those of ordinary skill in the art are without making creative work
The all other embodiment obtained, shall fall within the protection scope of the present invention.
Embodiment one
Such as Fig. 1, the utility model embodiment provides a kind of reunion liquid compounding system, including emulsion tank 1, material-compound tank 2 and mixed
Tank 3 is closed, there is the emulsion tank 1 solid-state agglomerator mouth, the first water filling port and emulsion outlet is added；The material-compound tank 2 has
Mouth, emulsion entrance, the second water filling port and mixture export, the emulsion entrance and the emulsification is added in liquid agglomerator
Liquid outlet；The blending tank 3 have entry to mixed solution, third water filling port and reunion liquid outlet, the entry to mixed solution with
The mixture export connection；It is equipped with blender in the emulsion tank 1, the material-compound tank 2 and the blending tank 3.Wherein：
It is preferably the top/top for being set to above-mentioned emulsion tank 1 that mouth, which is added, in above-mentioned solid-state agglomerator, for solid-state group to be added
Poly- agent accordingly arranges solid hopper 4 above the emulsion tank 1；Preferably, the solid hopper 4 by tremie pipe with it is described solid
Mouth connection is added in state agglomerator, and metering units are equipped in the tremie pipe；It can be quantitatively to emulsification by the metering units
Solid-state agglomerator is added in tank 1.Above-mentioned emulsion outlet is preferably set to lower part/bottom of emulsion tank 1；The emulsion exports
It is connect, can be matched the emulsion suction in emulsion tank 1 by power-equipments such as concentrating pumps by pipeline between emulsion entrance
In batch can 2.
It is preferably the top/top for being set to above-mentioned material-compound tank 2 that mouth, which is added, in above-mentioned liquid agglomerator, for liquid group to be added
Poly- agent accordingly arranges that mouth is added by pipeline and the liquid agglomerator in liquid tank 5, the liquid tank 5 above the material-compound tank 2
Connection；It is preferably equipped with the first liquid level detection unit in the liquid tank 5, liquid tank is detected by first liquid level detection unit
Liquid level in 5, to control the addition of liquid agglomerator.Conventional liquid level may be used in first liquid level detection unit
Detecting element, in the present embodiment, using ultrasonic level gage.Further, above-mentioned liquid tank 5 is connected with fluid infusion bucket, the benefit
Liquid bucket is connect by liquid supplementation channel with the liquid tank 5, is equipped with and first liquid level detection unit in the liquid supplementation channel
The kinetic pump of interlocked control；Liquid tank 5 is completed once to feed, which detects in liquid tank 5 under liquid level
Drop, liquid agglomerator is extracted with the kinetic pump of its interlocked control automatically from fluid infusion bucket, and liquid tank 5 is made to be restored to the liquid before charging
Behind position, kinetic pump is automatically stopped work.
Above-mentioned mixture export is preferably the lower part/bottom for being set to material-compound tank 2；The mixture export and entry to mixed solution
Between connected by pipeline, mixed liquor in material-compound tank 2 can be pumped into blending tank 3 by power-equipments such as concentrating pumps.
Such as Fig. 1, above-mentioned emulsion tank 1, material-compound tank 2 and blending tank 3 can share a set of water source, i.e. the first water filling port, the second note
The mouth of a river and third water filling port are connected to same feed pipe.
Solid-state agglomerator is mixed with water emulsify in advance, then extracted by reunion liquid compounding system provided in this embodiment
Emulsion is mixed to get concentration reunion liquid with liquid agglomerator, then is diluted to obtain institute to concentration reunion liquid in blending tank 3
The reunion liquid needed can be formed spherical to avoid solid-state agglomerator powder chance water in reunion liquid process for preparation existing in the prior art
Indissoluble object and the problem of influence preparation and the using effect of reunion liquid.Reunite by previously prepared concentration reunion liquid, then to concentration
Liquid dilutes and prepares the reunion liquid that is suitable for the application of, convenient for the reunion liquid that controls the addition of agglomerator and finally obtain
Concentration；Moreover, first preparing concentrate, the reunion liquid of prepared and diluted, the storage of concentrate do not need big volume again when needed
Storage device can save equipment cost and space, and convenient for management.
Conventional measuring equipment, such as weighing sensor may be used in the metering units of 4 fitted underneath of above-mentioned solid hopper；This
In embodiment, which preferably uses batch box, is controlled in setting on the tremie pipe between batch box and solid hopper 4
Valve, the control valve in the case where batch box and solid-state agglomerator are added on the tremie pipe between mouth and are arranged；Its workflow is as follows：Open control
Valve processed, which feed-is filled it up with, to be shut control valve-after quantitative barrel and opens lower control valve, and solid-state agglomerator falls into emulsion tank 1-and closes lower control
Valve.It is further preferred that avoid causing solid-state to be reunited in the water recovery in emulsion tank 1 to quantitative barrel, blanking tube wall
Agent powder bonding material precision and blocking tremie pipe, the tremie pipe, meter under the influence of on quantitative barrel and tremie pipe in turn
Measuring tank and the solid hopper 4 are each equipped with heating mechanism, are worked by heating mechanism, can be to avoid water recovery in blanking
On the inner wall of pipe, batch box and solid hopper 4.As feasible embodiment, which includes screw arrangement in corresponding utensil
Heating tube/heater strip in inner cavity；Alternatively, the tremie pipe, the batch box and the solid hopper 4 are ironware, institute
It includes coiling in heating tube/heater strip on corresponding utensil outer wall to state heating mechanism.
It is further preferred that being equipped with the second level sensing in the emulsion tank 1, the material-compound tank 2 and the blending tank 3
Unit, second liquid level detection unit are preferably to be set to the pressure sensor of corresponding tank base, pass through the second level sensing
Liquid level in the corresponding tank body of unit detection, realizes automatic blending.
In addition, such as Fig. 1, emulsion tank 1, material-compound tank 2,3 bottom of blending tank are respectively connected with blow down branch, are arranged on blow down branch
There is blowdown valve, each blowdown valve, which is both preferably, uses manual blowdown valve.Further, further include blowdown manifold, each blow down branch is equal
It is connect with blowdown manifold, blowdown main valve is set on blowdown manifold.Reunion liquid compounding system is run for 24 hours with Power Plant, but electricity
Brand-name computer group at regular intervals can maintenance down, reunion liquid compounding system also can maintenance down therewith；Emulsion, concentration after shutdown
Reunion liquid and dilution reunion liquid are stored in for a long time in tank body, pipeline, and corrosion may be caused to equipment, is blocked, therefore, it is necessary to
By the part waste liquid discharge.After the stoppage in transit of reunion liquid compounding system, the row on blowdown main valve and each blow down branch is opened successively
Dirty valve, waste liquid is discharged.
As the preferred embodiment of reunion liquid compounding system provided in this embodiment, the blending tank 3 also has desulfurization
Mouth is added in waste water, and the desulfurization wastewater is added mouth and is connected with desulfurization wastewater organization of supply.It is useless due to being incorporated desulfurization in reunion liquid
Water, the inorganic salts brought into can dramatically increase the carrying capacity of flue gas particles in flue 6, and the highly charged particulate matter of large scale holds very much
It easily traps fixed by deduster and removes so that the concentration of emission of flue gas fine particle is less than 10mg/m3, realize fine particle
Minimum discharge, and the moisture in agglomerator drop also evaporates rapidly under the high temperature action of 6 flue gas of flue, utilizes desulfurization wastewater
Inorganic salts, heavy metal ion etc. in the reunion liquid of preparation become crystal salt, and crystal salt enters deduster with large particle and goes
Except the processing realized in turn to desulfurization wastewater.I.e. desulfurization wastewater is become useful reunion liquid preparation raw material by the present embodiment, because
And processing coal-burning power plant's fine particle and desulfurization wastewater can be cooperateed with, it avoids power plant and is transformed in batches, repeats to bear caused by constructing
Face is rung.Above-mentioned desulfurization wastewater organization of supply is illustrated below：
To ensure the using effect of reunion liquid, it is suitable for the preparation raw material for first handling desulfurization wastewater and being re-used as reunion liquid afterwards.
Preferably, such as Fig. 2, the desulfurization wastewater organization of supply includes sequentially connected desulfurization wastewater pretreatment unit and membrane filtration processing
Unit, water outlet pipe and the desulfurization wastewater of the membrane filtration processing unit are added mouth and are connected to.Preferably, such as Fig. 2, the film
Filtration treatment unit includes ultrafiltration membrane 14, and water outlet control valve 16 is equipped in its water outlet pipe.It is right using ultrafiltration membrane 14
Desulfurization wastewater is filtered processing, can so that the impurity such as most particulate matter are effectively removed in desulfurization wastewater, reduces
The probability that follow-up reunion spray gun 7 blocks, meanwhile, most salinity is retained in desulfurization wastewater, ensures that subsequent reunion removes
Dirt effect.Above-mentioned ultrafiltration membrane 14 is preferably that membrane filter system is lost in cross-flow, and the anti-pollution that can improve ultrafiltration membrane 14 blocks up ability；This
In embodiment, membrane aperture further preferably selects the membrane aperture of 40 microns in 35~50 micron ranges.Certainly, it receives
The membrane filter systems such as filter membrane are also suitable in this present embodiment.
In the present embodiment, it is equipped with the structure of water outlet control valve 16 based on above-mentioned water outlet pipe, may be implemented pair
The backwash of the ultrafiltration membrane 14 specifically periodically or non-periodically carries out backwash to the ultrafiltration membrane 14, and back-washing method includes：It closes
The water outlet control valve 16 on the water outlet pipe is closed, pressurize backwash is carried out to the ultrafiltration membrane 14.Usually, surpass
It is provided with water supply pump 15 on the desulfurization wastewater pipeline of the influent side connection of filter membrane 14；The fresh water closed on water outlet pipe goes out
After mouth control valve 16, dilute side stops production water, and dilute side pipeline pressure rises, and the reversible dirt that 14 fenestra surface of ultrafiltration membrane is formed is stifled
Loosened under the action of fresh water lateral pressure, and be detached under the agitaion that above-mentioned water supply pump 15 generates ultrafiltration membrane 14 surface (into
One step can be also provided with control valve 13 on concentrated water outlet, at this point, the control valve 13 on concentrated water outlet is in the state opened),
Finally ultrafiltration membrane 14 is left with concentrated water.
Preferably, above-mentioned backwash operation regularly is carried out to the ultrafiltration membrane 14, a preferred embodiment is：
Ultrafiltration membrane 14 is often run 5~6 minutes, and the water outlet control valve 16 on water outlet pipe is closed 20~30 seconds, into
Row pressurize backwash, to ensure the high throughput of ultrafiltration membrane 14, the operation of subsequent ultrafiltration membrane 14 and backwash operation are alternately.It is above-mentioned
Water supply pump 15 preferably use big flow circulating pump 15.
Based on above-mentioned 14 backwashing function of ultrafiltration membrane, the anti-pollution that can effectively improve ultrafiltration membrane 14 blocks up ability, to improve
The service life of the ultrafiltration membrane 14 extends its cleaning frequency.
Further, such as Fig. 2, above-mentioned pretreatment unit includes clear water reserviors 12 and at least first stage precipitation tank that is sequentially connected in series,
Along desulfurization wastewater circulating direction, sedimentation basin 11, the clear water reserviors 12 described in final stage pass through desulfurization with the membrane filtration processing unit
Waste water runner pipe is sequentially connected in series.Desulfurization wastewater is pre-processed by pretreatment unit, membrane filtration processing unit can be reduced
Live load, improve membrane filtration processing unit working efficiency and service life.Final stage sedimentation basin 11 and membrane filtration processing are single
Clear water reserviors 12 are set between member, the work rhythm between pretreatment unit and membrane filtration processing unit can be coordinated, ensure pre- place
Manage the treatment effect of unit.
Preferably, such as Fig. 2, the sedimentation basin has three-level, wherein first order sedimentation basin 9 is for precipitating in desulfurization wastewater
Large particle；To milk of lime is added in second level sedimentation basin 10, sulfur-bearing recaptures agent and bodied ferric sulfate flocculation aid (preferably sequentially adds
Enter), to promote suspended particulate substance, heavy metal and at least part of sulfate radical in desulfurization wastewater to precipitate；To third level sedimentation basin
Sodium carbonate softening agent is added in 11, to promote the hardness species precipitate in desulfurization wastewater, which includes calcium, magnesium etc..
Further, as Fig. 2, above-mentioned pretreatment unit are also configured with sludge concentration tank 20, sedimentation basin bottoms at different levels are all provided with
There are mud discharging mouth, each mud discharging mouth to be connect respectively with sludge concentration tank 20 by sludge pipe, it is equal at each mud discharging mouth
Equipped with mud discharging valve.For ease of the collection and discharge of sludge, the bottom of above-mentioned each sedimentation basin is preferably V-shaped or presents under width
Narrow taper, above-mentioned mud discharging mouth are set to the bottom end of corresponding sedimentation basin.In addition, above-mentioned pretreatment unit may also include it is de-
Sulphur wastewater collection pond 8, desulfurization wastewater raw water enter regulating water quality and water in the desulfurization wastewater collecting pit 8.
Desulfurization wastewater raw water enters 8 regulating water quality of desulfurization wastewater collecting pit and water, and water outlet enters first order sedimentation basin 9,
Large particle in desulfurization wastewater sinks to 9 bottom of first order sedimentation basin, and the muddy water containing particulate matter is periodically arranged through mud discharging valve
It puts to sludge concentration tank 20, supernatant enters second level sedimentation basin 10；By being added sequentially lime into second level sedimentation basin 10
Breast, sulfur-bearing recapture the medicaments such as agent, bodied ferric sulfate flocculation aid, promote suspended particulate substance, heavy metal and part in desulfurization wastewater
Sulfate radical becomes sludge, is deposited on the bottom of second level sedimentation basin 10, and muddy water is periodically emitted into sludge condensation through mud discharging valve
Pond 20, supernatant enter third level sedimentation basin 11；By adding sodium carbonate softening agent into third level sedimentation basin 11, in waste water
The hardness substance such as calcium, magnesium becomes sludge, is deposited on the bottom of third level sedimentation basin 11, and muddy water is periodically emitted into through mud discharging valve
Sludge concentration tank 20, supernatant enter clear water reserviors 12.It can be set in above-mentioned desulfurization wastewater collecting pit and sedimentation basin at different levels
Agitating paddle is set, to improve the sedimentation effect of desulfurization wastewater.It can be set on pipeline between clear water reserviors 12 and membrane filtration processing unit
Set above-mentioned big flow circulating pump 15.
As one of preferred embodiment, the concentrated water outlet is precipitated with described in the clear water reserviors 12 or in which level-one
Pond connects, i.e., the concentrated water obtained through ultrafiltration membrane 14 is back in clear water reserviors 12 or in which first stage precipitation tank and continues with, to realize
The zero-emission of desulfurization wastewater.Preferably, such as Fig. 2, which connect with clear water reserviors 12.
It is further preferred that such as Fig. 2, the water outlet pipe is connected with fresh water collecting pond 17, the fresh water collecting pond 17
It is connected to the desulfurization wastewater entrance by fresh water runner pipe, is equipped with successively on the fresh water runner pipe along fresh water circulating direction
Diaphragm pump 18 and filter 19.The quantitative conveying of desulfurization wastewater may be implemented using diaphragm pump, while preventing desulfurization wastewater to general
The corrosion of logical material pump.Waste water in fresh water collecting pond 17, which quantitatively enters under the power of diaphragm pump 18 through filter 19, to be mixed
In tank 23；Above-mentioned filter 19 is further filtered fresh water, ensures the cleannes of reunion liquid, further decreases follow-up reunion
The probability that spray gun 7 blocks.
The above is only the preferred embodiment of the utility model only, is not intended to limit the utility model, all at this
Within the spirit and principle of utility model, any modification, equivalent replacement, improvement and so on should be included in the utility model
Protection domain within.
Claims (10)
1. a kind of reunion liquid compounding system, it is characterised in that：Including emulsion tank, material-compound tank and blending tank,
There is the emulsion tank solid-state agglomerator mouth, the first water filling port and emulsion outlet is added；
There is the material-compound tank liquid agglomerator mouth, emulsion entrance, the second water filling port and mixture export, the breast is added
Change liquid entrance and the emulsion outlet；
There is the blending tank entry to mixed solution, third water filling port and the outlet of reunion liquid, the entry to mixed solution to be mixed with described
Liquid outlet；
It is equipped with blender in the emulsion tank, the material-compound tank and the blending tank.
2. reunion liquid compounding system as described in claim 1, it is characterised in that：It is disposed with solid hopper above the emulsion tank,
The solid hopper is added mouth with the solid-state agglomerator by tremie pipe and connect, and metering units are equipped in the tremie pipe.
3. reunion liquid compounding system as claimed in claim 2, it is characterised in that：The metering units include batch box, described
Tremie pipe, the batch box and the solid hopper are each equipped with heating mechanism.
4. reunion liquid compounding system as claimed in claim 3, it is characterised in that：The heating mechanism includes screw arrangement in right
Answer the heating tube in utensil inner cavity；
Or, the tremie pipe, the batch box and the solid hopper are ironware, the heating mechanism includes coiling in right
Answer the heating tube on utensil outer wall.
5. reunion liquid compounding system as described in claim 1, it is characterised in that：It is disposed with and the liquid above the material-compound tank
The liquid tank of mouth connection is added in state agglomerator, and the first liquid level detection unit is equipped in the liquid tank.
6. reunion liquid compounding system as claimed in claim 5, it is characterised in that：The liquid tank is connected with fluid infusion bucket, described
Fluid infusion bucket is connect by liquid supplementation channel with the liquid tank, is equipped with and first liquid level detection unit in the liquid supplementation channel
The kinetic pump of interlocked control.
7. reunion liquid compounding system as described in claim 1, it is characterised in that：The emulsion tank, the material-compound tank and described
The second liquid level detection unit is equipped in blending tank.
8. reunion liquid compounding system as described in claim 1, it is characterised in that：The emulsion tank, the material-compound tank and described
Mixing pot bottom is respectively connected with blow down branch, and blowdown valve is equipped on each blow down branch.
9. reunion liquid compounding system as claimed in claim 8, it is characterised in that：Further include blowdown manifold, each blow down branch is equal
It is connect with the blowdown manifold, blowdown main valve is equipped on the blowdown manifold.
10. reunion liquid compounding system as described in claim 1, it is characterised in that：The blending tank also adds with desulfurization wastewater
Entrance, the desulfurization wastewater are added mouth and are connected with desulfurization wastewater organization of supply.
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| CN201721901325.2U CN207913690U (en) | 2017-12-29 | 2017-12-29 | A kind of reunion liquid compounding system |
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| CN201721901325.2U CN207913690U (en) | 2017-12-29 | 2017-12-29 | A kind of reunion liquid compounding system |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109395524A (en) * | 2018-12-19 | 2019-03-01 | 武汉天空蓝环保科技有限公司 | The ultra-clean processing system of flue gas based on particulate matter chemical agglomeration and bag-type dust |
-
2017
- 2017-12-29 CN CN201721901325.2U patent/CN207913690U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109395524A (en) * | 2018-12-19 | 2019-03-01 | 武汉天空蓝环保科技有限公司 | The ultra-clean processing system of flue gas based on particulate matter chemical agglomeration and bag-type dust |
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