CN107376505A - A kind of feldspar in powder produces waste recycle system - Google Patents
A kind of feldspar in powder produces waste recycle system Download PDFInfo
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- CN107376505A CN107376505A CN201710840271.1A CN201710840271A CN107376505A CN 107376505 A CN107376505 A CN 107376505A CN 201710840271 A CN201710840271 A CN 201710840271A CN 107376505 A CN107376505 A CN 107376505A
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- water
- concentration tower
- feldspar
- sedimentation basin
- concentration
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D36/00—Filter circuits or combinations of filters with other separating devices
- B01D36/04—Combinations of filters with settling tanks
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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
- C02F9/00—Multistage treatment of water, waste water or sewage
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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
- C02F2103/16—Nature of the water, waste water, sewage or sludge to be treated from metallurgical processes, i.e. from the production, refining or treatment of metals, e.g. galvanic wastes
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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
- C02F2201/00—Apparatus for treatment of water, waste water or sewage
- C02F2201/002—Construction details of the apparatus
Abstract
The invention discloses a kind of feldspar in powder to produce waste recycle system, belongs to waste water circulation recycling field.The present invention includes sedimentation basin, including several and be arranged side by side, sedimentation basin connection is located at the waste water ditch in water mill workshop, for reclaiming the waste water of K-feldspar slag charge in water mill workshop；Concentration tower, the concentrate of high potassium feldspar slag charge content is obtained by carrying out concentration to the waste water；Squeezer, by the concentrate squeeze and filter of concentration tower, slag charge siccative and filtered fluid are filtrated to get, the slag charge siccative is transported in recovery bin, the filtered fluid pumped back concentration tower；And clear water reserviors, it is set up in parallel below concentration tower and with sedimentation basin, clear water reserviors collect the clear water and recovery bin backflow clear water that concentration tower is filtrated to get.The present invention realizes quick cyclic utilization and the slag recycling to waste water by providing a kind of processing system for not needing chemical agent to be settled.
Description
Technical field
The present invention relates to waste water circulation recycling field, particularly a kind of feldspar in powder production waste recycle system.
Background technology
, it is necessary to ore progress and eddy flow processing etc. in the production and processing of potassium ore, can be generated in these processing steps
Substantial amounts of waste water, substantial amounts of potassium ore fine sand or fine particle etc. are contained in waste water.If directly excluded, first can pollute ring
Border, very big injury is caused to environment；Second increasingly lacks instantly in water resource, and enterprise's life can be greatly increased by wasting water source
Produce cost；Fine sand in third production excludes therewith, can increase post-processing difficulty.
In the prior art, the sewage disposal system such as metallic ore and the processing ore dressing of non-ore deposit, is by sedimentation basin, concentration tower, squeezing
Machine etc. forms.During for handling sewage, by the way that tailing sewage is discharged into sedimentation basin, and alchlor shape is put into sedimentation basin
Into mud, then it is stirred in sedimentation basin, the slag in mud is precipitated by Action of Gravity Field, it is further dense by concentration tower
Division separates out water overflow discharge.To the mud after concentration, further processing obtains siccative to squeezer.But existing processing system is deposited
Inconvenient in concentration operation, fault rate is high, treatment effeciency low the defects of waiting.
Patent 201310231885.1 discloses polishing and raw material waste residue recovery system and method by original raw material pulp water
Raceway groove and polishing pulp water raceway groove are laid out again：Respectively polishing and raw material waste residue water guide to corresponding raw material pulp water pond and
Polish pulp water pond；Waste residue water is introduced first, second concentration tower to be concentrated, first, second transferring cylinder contains riddler, and riddler will
Heavies in pulp water filter out；First, second vacuum hydroextractor carries out the steps such as vacuum dehydration.Its processing step is more, special
It is not that vacuum hydroextractor power consumption is larger, slower to sewage disposal, the unsuitable slag particle diameter of the production technology is small, and sewage quantity is big
Feldspar in powder production wastewater treatment.
Patent 201010534620.5 discloses a kind of tailing sewage rapid settling-thickening tank, including outer barrel and inner cylinder, interior
Cylinder is nested with outer barrel by support frame, and the upper end of inner cylinder is to install one into sewage mouth, the centre of inner cylinder by support frame and delay
Baffle plate is rushed, charging gap is left between the edge of cushioning fender and the inwall of inner cylinder, the outer wall of inner cylinder is further fixed at least one
Ring-like reverse flow baffle, leaves spilling water gap between the outer rim of reverse flow baffle and the inwall of outer barrel, the diameter below of outer barrel gradually contracts
Small formation slag-drip opening, the upper end of outer barrel form overflow tank, and the gap of overflow tank independently separates with entering sewage mouth.The precipitation
Concentration tank can be quickly handled the larger heavier sewage containing particle, but for containing the smaller lighter sewage of particle, no
It can accomplish that rapid precipitation concentrates, because particle is smaller relatively light in sewage, when particularly sewage is extracted into precipitation concentration tank, in sewage
Grain be in suspended state, can not rapid precipitation get off, particularly as shown in the patent accompanying drawing, if persistently sewage suction,
So from precipitation concentration tank outflow be still containing the more water of tailing particles, do not reach much rapid precipitation concentration effect.
Accordingly, it is desirable to provide a kind of new technical scheme solves above-mentioned technical problem.
The content of the invention
In order to solve technical barrier of the prior art, the present invention provides a kind of feldspar in powder production waste water recycling system
System, by providing a kind of processing system for not needing chemical agent to be settled, realize the quick cyclic utilization and ore deposit to waste water
Slag recycles.Here rapid precipitation concentration can be carried out to the sewage continued to flow into by setting multiple filtration to set, especially
It is adapted to the quick cyclic utilization of the feldspar in powder production waste water of the particle containing less than 80 mesh.
According to technical scheme, there is provided a kind of feldspar in powder produces waste recycle system, and it includes,
Sedimentation basin, including several and be arranged side by side, waste water ditch of the sedimentation basin connection in the water mill workshop, for returning
Receive the waste water of K-feldspar slag charge in water mill workshop；
Concentration tower, the concentrate of high potassium feldspar slag charge content is obtained by carrying out concentration to the waste water；
Squeezer, by the concentrate squeeze and filter of concentration tower, it is filtrated to get slag charge siccative and filtered fluid, the slag charge siccative
It is transported in recovery bin, the filtered fluid pumped back concentration tower；And
Clear water reserviors, it is set up in parallel below concentration tower and with sedimentation basin, clear water reserviors collection concentration tower is filtrated to get clear
Water and recovery bin backflow clear water；
The concentration tower includes concentration tower body, leg, Ta Gai, water filtering tube, outlet pipe, overflow pipe, the first weather board and the
Two weather boards, the concentration tower body bottom are provided for the leg of support, and its bosom sets the drainage by support frame
Cylinder, water filtering tube connection outlet pipe, outlet pipe delivery port correspond to clear water reserviors；Turnover tower lid, tower lid are provided with the top of concentration tower body
On be communicated with the water inlet of sedimentation basin；The overflow pipe is located at the external side of concentration tower, and its one end connection concentrates tower body top, separately
One end corresponds to sedimentation basin；First weather board is arranged on wall in concentration tower body in a ring, and positioned at concentration tower body and water filtering tube
Between；Second weather board is in funnel-form, and below water filtering tube, its wide-mouth one end is connected with wall in concentration tower body；Institute
It is to set the blow-off valve of connection squeezer in funnelform thickening cone, thickening cone bottom to state concentration tower body bottom, and thickening cone is located at
Below second weather board；
The water filtering tube includes drainage cylinder, inner cylinder, drainage plate, filter membrane and valve, and the inner cylinder is located at drainage cylinder
It is interior, and be arranged on by support bar among drainage cylinder, the first filter chamber is formed between inner cylinder and drainage cylinder, inner cylinder is opened under being
Mouth tube structure, inner cylinder bottom are provided with filter membrane, and filter membrane forms the second filter chamber, the connection of the second filter chamber with interior tube inner chamber
Outlet pipe；The drainage cylinder bottom is in funnel-form, and its bottom is provided with the recovery valve opened down；The water filtering tube is external
It is arc structure at the top of wall, and the water inlet of face tower lid, drainage cylinder body outer wall top are provided with and set in the shape of a spiral with its center
Drainage plate；
The side wall of the drainage cylinder is made up of micropore ceramic filter material.
Preferably, the side wall of the drainage cylinder from outside to inside successively by outer stainless steel fine-structure mesh, micropore ceramic filter material,
Inside and outside stainless steel fine-structure mesh composition, the drainage cylinder body bottom and top are made up of stainless steel.
Preferably, wall is arranged at intervals up and down along concentration tower body between first weather board, the first weather board and drainage
Equidistant interval is formed between cylinder, the interval specification is 3-6cm.
Preferably, the filter membrane is located at the top of the under shed of inner cylinder, and the aperture specification of the filter membrane is 0.1mm.
Preferably, the pore size filter of the micropore ceramic filter material is 0.15-0.3mm.
Preferably, the water inlet of the overflow pipe is located at the top of water filtering tube between inner cylinder, the water inlet of the overflow pipe
Front is additionally provided with water fender, the water fender upper end connection concentration tower body top, and its specification is more than the water inlet of overflow pipe
Mouth specification.
Preferably, the tower lid is articulated and connected with concentration tower body, and positioned at concentration tower body crown center, tower, which covers, to be additionally provided with
Handle.
Preferably, the first deflector and the second deflector are also set up in the thickening cone, first deflector is in tapered
Structure, its tapering are located at immediately below the second weather board the simultaneously bell mouth of the deflector of face second, and its afterbody, which is located at, is more than second
The bell mouth of deflector.
Preferably, water inlet one end of the outlet pipe is located at the middle part of inner cylinder.
Preferably, the clear water reserviors are also arranged with the sedimentation basin that battle field is washed in connection with respect to sedimentation basin side；On sedimentation basin
Side, which is horizontally set with, mounting bracket, and the water plug of connection concentration tower body tower lid water inlet is provided with mounting bracket and is stirred for sedimentation basin
The agitator mixed, the water plug include pumping motor, rotating shaft, water pump, pump mouth and water proof cylinder, the pumping motor installation
On mounting bracket, its rotating shaft is correspondingly fastened on the water pump of sedimentation basin bottom, and the water pump bottom is provided with corresponding sedimentation basin bottom
The pump mouth in portion；The water proof cylinder that sealing is formed to it, water proof cylinder one end connection mounting bracket are arranged with outside the rotating shaft, the other end connects
Water pump.
Preferably, the agitator includes stirring motor, agitating shaft, stirring vane and bracing strut, the stirring motor peace
On mounting bracket, the corresponding connection of its agitating shaft is located at the stirring vane of sedimentation basin bottom, and the bracing strut is set in inverted pyramid
Put, its larger one end is fixed with sedimentation basin side wall, and it is more a little bit smaller to be rotatably connected with agitating shaft.
Due to using above-mentioned technical proposal, the invention has the advantages that：
1. the system of the present invention includes sedimentation basin, concentration tower, squeezer and clear water reserviors etc., wherein sedimentation basin is heavy by standing
Product so that the ore particles in waste water are deposited on the bottom, then to being pumped into concentration tower；Concentration tower is further to being sent into waste water
Processing, mainly separation of solid and liquid, to the further concentration of waste water, improve its high potassium feldspar slag charge content, and be sent into squeezer；Pressure
Crusher is existing solid-liquid separation device, can obtain slag charge siccative to being sent into waste water progress separation of solid and liquid, slag charge siccative is direct
It is sent into recovery bin, and waste water caused by squeezer comes back to concentration tower concentration again；In the process, concentration tower can
To obtain meeting the clear water of re-using standard, feldspar in powder production process reclaimed water source can be used as, and obtained waste material can
To re-use.So by being lost in The present invention reduces feldspar in powder in production process, slag because of waste water, the rate of recovery reaches
More than 85%,；Waste water circulation can be recycled simultaneously.
2. concentration tower uses multiple filtration structure in the present invention, wherein drainage cylinder lateral wall uses micropore ceramic filter material
It is made, its thickness is 3-7cm, and the side wall of micropore ceramic filter material composition can carry out first time separation of solid and liquid to waste water, obtain
To first time filtered fluid, first time filtered fluid is further deposited in the first filter chamber, and secondary mistake is carried out by the filter membrane of inner cylinder
Filter, obtains the clear water for meeting recovery, and be discharged to clear water reserviors in the second filter chamber.The small size deposited in first filter chamber is high
For potassium feldspar slag charge when concentration tower body water level is less than the first filter chamber bottom, first time filtered fluid is due to itself in the first filter chamber
Gravity directly opens recovery valve so that first time filtered fluid is directly discharged into concentration tower body in the thickening cone of bottom.Concentration tower
The slag that concentration reaches 53%-66% can be discharged.Its caused clear water can direct recycling.
Brief description of the drawings
Fig. 1 is present system workflow diagram；
Fig. 2 is functional module distribution map of the present invention；
Fig. 3 is sedimentation basin structural representation of the present invention；
Fig. 4 is concentration tower structural representation.
In accompanying drawing, 1- sedimentation basins, 2- concentration towers, 21- concentrations tower body, 22- legs, 23- towers lid, 231- water inlets, 232-
Handle, 24- overflow pipes, 241- water fenders, 25- thickening cones, 251- blow-off valves, the deflectors of 252- first, the deflectors of 253- second,
26- water filtering tubes, 261- drainages cylinder, 262- inner cylinders, 263- drainage plates, 264- filter membranes, 265- valves, 27- outlet pipes, 28-
First weather board, the weather boards of 29- second, 3- squeezers, 4- clear water reserviors, 5- water plugs, 51- pumping motors, 52- rotating shafts, 53-
Water pump, 54- pump mouths, 55- water proofs cylinder, 6- aqueducts, 7- agitators, 71- stirring motors, 72- agitating shafts, 73- stirring vanes,
74- bracing struts.
Embodiment
The invention provides a kind of feldspar in powder to produce waste recycle system, can accomplish to produce waste water to feldspar in powder
Recycle, contain a large amount of feldspars in powder in feldspar in powder production waste water, minimum feldspar in powder up to 100 mesh sizes or so,
This is caused by eddy flow processing procedure in generating process；If do not handle recovery will waste water resource and ore significantly it is former
Material.Processing procedure is more slow in existing cyclic utilization system, it is impossible to enter Line Continuity processing to sewage, and for sewage
The slag size included is also required, and the particularly existing structure of concentration tower 2 can not be carried out to the sewage of the mesh containing granular size 100
Quick processing, these all limit generation production cycling utilization of wastewater in feldspar in powder.Therefore, the present invention proposes one kind and followed again
Loop system, by setting concentration tower 2 to use multiple filtration structure so that sewage rapid precipitation can be concentrated, it discharges clear water
Utilization can be repeatedly generated without reprocessing.
The specific implementation of invention is further illustrated below in conjunction with accompanying drawing.
As shown in figure 1, being present system workflow diagram, the wherein sedimentation basin 1 of sedimentation basin 1 connection is in water mill workshop
Waste water ditch, the waste water of K-feldspar slag charge in recovery water mill workshop.Concentration tower 2 to the waste water by carrying out concentration
Obtain the concentrate of high potassium feldspar slag charge content.The concentrate squeeze and filter of concentration tower 2 is filtrated to get slag charge and done by squeezer 3
Material and filtered fluid, slag charge siccative are transported in recovery bin, filtered fluid pumped back concentration tower 2.The clear water reserviors 4 of clear water reserviors 4 collect concentration
Clear water and recovery bin the backflow clear water that tower 2 is filtrated to get.
As shown in Fig. 2 flat functional distribution map of the present invention.Wherein, sedimentation basin 1 is located at the both sides of clear water reserviors 4, and sedimentation basin 1 wraps
Include several and be arranged side by side, connected between sedimentation basin 1 by top overfall, water plug 5 is provided with sedimentation basin 1 and is stirred
Device 7 to be mixed, and concentration tower 2 is pumped into by aqueduct 6, agitator 7 is used to be stirred sedimentation basin 1, is advantageous to wastewater sedimentation,
Simultaneously by the bottom precipitation rearrangement of sedimentation basin 1, water plug 5 is facilitated to pump the higher waste water of concentration containing slag to concentration
Tower 2.Concentration tower 2 is erected at the top of clear water reserviors 4.Two group precipitation ponds 1 and two groups of concentration towers 2 are set here, for corresponding to water respectively
Grind waste water caused by waste water caused by workshop and washery.
As shown in figure 3, the top of sedimentation basin 1, which is horizontally set with, mounting bracket, the connection concentration tower lid of tower body 21 is installed on mounting bracket
The water plug 5 of 23 water inlets 231 and the agitator 7 stirred for sedimentation basin 1.Water plug 5 includes water plug 51, rotating shaft
52nd, water pump 53, pump mouth 54 and water proof cylinder 55, water plug 51 are arranged on mounting bracket, and its rotating shaft 52 is corresponding to be fastened on
The water pump 53 of the bottom of sedimentation basin 1, the bottom of water pump 53 are provided with the pump mouth 54 of the corresponding bottom of sedimentation basin 1.It is arranged with outside rotating shaft 52 pair
It forms the water proof cylinder 55 of sealing, the one end of water proof cylinder 55 connection mounting bracket, other end connection water pump 53.Agitator 7 includes stirring
Motor 71, agitating shaft 72, stirring vane 73 and bracing strut 74；Stirring motor 71 is arranged on mounting bracket, its correspondence of agitating shaft 72
Connection is positioned at the stirring vane 73 of the bottom of sedimentation basin 1, and bracing strut 74 is in inverted pyramid setting, its larger one end and the side of sedimentation basin 1
Wall is fixed, and it is more a little bit smaller to be rotatably connected with agitating shaft 72.
As shown in figure 4, concentration tower 2 includes concentration tower body 21, leg 22, tower lid 23, water filtering tube 26, outlet pipe 27, overflow
Pipe 24, the first weather board 28 and the second weather board 29；Concentration tower body 21 bottom is provided for the leg 22 of support, its bosom
Water filtering tube 26 is set by support frame, water filtering tube 26 connects outlet pipe 27, and the delivery port of outlet pipe 27 corresponds to clear water reserviors 4.Concentration tower
The top of body 21 is provided with turnover tower lid 23, and the water inlet 231 of sedimentation basin 1 is communicated with tower lid 23.Overflow pipe 24 is positioned at dense
The outside of contracting tower body 21, its one end connection concentration tower body 21 top, the other end correspond to sedimentation basin 1；The water inlet of overflow pipe 24 231
Between the top of water filtering tube 26 and inner cylinder 262, the front of water inlet 231 of overflow pipe 24 is additionally provided with water fender 241, water fender
The top of 241 upper ends connection concentration tower body 21, and its specification is more than the specification of water inlet 231 of overflow pipe 24.First weather board 28 is in
Annular is arranged on the concentration inwall of tower body 21, and between concentration tower body 21 and water filtering tube 26；Second weather board 29 is in funnel-form,
And it is connected positioned at the lower section of water filtering tube 26, its wide-mouth one end with the concentration inwall of tower body 21.Along concentration tower body between first weather board 28
21 inwalls are arranged at intervals up and down, equidistant interval are formed between the first weather board 28 and water filtering tube 26, interval specification is 4cm.It is dense
The bottom of contracting tower body 21 is in funnelform thickening cone 25, and the bottom of thickening cone 25 sets the blow-off valve 251 of connection squeezer 3, concentration
Bucket 25 is positioned at the lower section of the second weather board 29.
Water filtering tube 26 includes drainage cylinder 261, inner cylinder 262, drainage plate 263, filter membrane 264 and valve 265；Inner cylinder 262
It is arranged in drainage cylinder 261, and by support bar among drainage cylinder 261, between inner cylinder 262 and drainage cylinder 261
Form the first filter chamber；Inner cylinder 262 is under shed tube structure, and the bottom of inner cylinder 262 is provided with filter membrane 264, filter membrane 264 with
The inner chamber of inner cylinder 262 forms the second filter chamber, the second filter chamber connection outlet pipe 27；Filter membrane 264 is located at the under shed of inner cylinder 262
Top, the aperture specification of filter membrane 264 is 0.1mm.The bottom of drainage cylinder 261 is in funnel-form, and its bottom is provided with opens down
The recovery valve 265 opened.It is arc structure at the top of the outer wall of drainage cylinder 261, and the water inlet 231 of face tower lid 23, water filtering tube
The outer wall top of body 261 is provided with the drainage plate 263 set in the shape of a spiral with its center.The side wall of drainage cylinder 261 is by micropore ceramics
Filtering material is made；The pore size filter of micropore ceramic filter material is 0.2mm, thickness 5cm.
Further, the side wall of drainage cylinder 261 is from outside to inside successively by outer stainless steel fine-structure mesh, micropore ceramic filter material
Material, inside and outside stainless steel fine-structure mesh composition, the bottom of drainage cylinder 261 and top are made up of stainless steel.Micropore ceramic filter material can
To filter small slag particle very well, and it is not easy to result in blockage, easy clean and maintenance.Drainage cylinder 261 can directly be lifted and taken
Go out, can so change different micropore ceramic filter materials as needed.
Further, tower lid 23 is articulated and connected with concentration tower body 21, and on the concentration crown center of tower body 21, tower lid 23
It is additionally provided with handle 232.Tower lid 23 can be opened, and facilitate the regular maintenance of concentration tower 2.
Further, the first deflector 252 and the second deflector 253 are also set up in thickening cone 25, the first deflector 252 is in
Tapered structure, its tapering are located at the bell mouth of the underface of the second weather board 29 and the second deflector of face 253, and its afterbody is located at
More than the bell mouth of the second deflector 253.First deflector 252 can to enter thickening cone 25 sewage carry out water conservancy diversion, second
Deflector 253 can reduce the rolling of sewage, it is quickly calmed down, beneficial to concentrating and precipitating.
Described above is the detailed description for the present invention preferably possible embodiments, but embodiment is not limited to this hair
Bright patent claim, the equal change completed or modification change under the technical spirit suggested by all present invention, all should belong to
Cover the scope of the claims in the present invention.
Claims (11)
1. a kind of feldspar in powder produces waste recycle system, it is characterised in that：Including,
Sedimentation basin, including several and be arranged side by side, waste water ditch of the sedimentation basin connection in the water mill workshop, for recycle-water
Grind the waste water of K-feldspar slag charge in workshop；
Concentration tower, the concentrate of high potassium feldspar slag charge content is obtained by carrying out concentration to the waste water；
Squeezer, by the concentrate squeeze and filter of concentration tower, it is filtrated to get slag charge siccative and filtered fluid, the slag charge siccative conveying
Into recovery bin, the filtered fluid pumped back concentration tower；And
Clear water reserviors, be set up in parallel below the concentration tower and with sedimentation basin, clear water reserviors collect the clear water that concentration tower is filtrated to get and
Recovery bin backflow clear water；
The concentration tower, which includes concentration tower body, leg, Ta Gai, water filtering tube, outlet pipe, overflow pipe, the first weather board and second, leads
Water plate, the concentration tower body bottom are provided for the leg of support, and its bosom sets the water filtering tube by support frame, filters
Water drum connects outlet pipe, and outlet pipe delivery port corresponds to clear water reserviors；Turnover tower lid is provided with the top of concentration tower body, tower, which covers, to be provided with
Connect the water inlet of sedimentation basin；The overflow pipe is located at the external side of concentration tower, its one end connection concentration tower body top, the other end pair
Answer sedimentation basin；First weather board is arranged on wall in concentration tower body in a ring, and between concentration tower body and water filtering tube；Institute
It is in funnel-form to state the second weather board, and below water filtering tube, its wide-mouth one end is connected with wall in concentration tower body；The concentration tower
Body bottom is to set the blow-off valve of connection squeezer in funnelform thickening cone, thickening cone bottom, and thickening cone is located at the second water guide
Below plate；
The water filtering tube includes drainage cylinder, inner cylinder, drainage plate, filter membrane and valve, and the inner cylinder is located in water filtering tube body, and
It is arranged on by support bar among drainage cylinder, the first filter chamber is formed between inner cylinder and drainage cylinder, inner cylinder is under shed cylinder
Body structure, inner cylinder bottom are provided with filter membrane, and filter membrane forms the second filter chamber, the connection water outlet of the second filter chamber with interior tube inner chamber
Pipe；The drainage cylinder bottom is in funnel-form, and its bottom is provided with the recovery valve opened down；The drainage cylinder body outer wall top
Portion is arc structure, and the water inlet of face tower lid, and drainage cylinder body outer wall top is provided with is drawn with what its center was set in the shape of a spiral
Flowing plate；
The side wall of the drainage cylinder is made up of micropore ceramic filter material.
A kind of 2. feldspar in powder production waste recycle system according to claim 1, it is characterised in that：The water filtering tube
The side wall of body is made up of outer stainless steel fine-structure mesh, micropore ceramic filter material, inside and outside stainless steel fine-structure mesh successively from outside to inside, the filter
Water cylinder body bottom and top are made up of stainless steel.
A kind of 3. feldspar in powder production waste recycle system according to claim 1, it is characterised in that：Described first leads
Wall is arranged at intervals up and down along concentration tower body between water plate, and equidistant interval is formed between the first weather board and water filtering tube, described
Interval specification is 3-6cm.
A kind of 4. feldspar in powder production waste recycle system according to claim 1, it is characterised in that：The filter membrane
Positioned at the top of the under shed of inner cylinder, the aperture specification of the filter membrane is 0.1mm.
A kind of 5. feldspar in powder production waste recycle system according to claim 1, it is characterised in that：The micropore pottery
The pore size filter of porcelain filtering material is 0.15-0.3mm.
A kind of 6. feldspar in powder production waste recycle system according to claim 1, it is characterised in that：The overflow pipe
Water inlet be located at the top of water filtering tube between inner cylinder, be additionally provided with water fender immediately ahead of the water inlet of the overflow pipe, it is described
At the top of water fender upper end connection concentration tower body, and its specification is more than the water inlet specification of overflow pipe.
A kind of 7. feldspar in powder production waste recycle system according to claim 1, it is characterised in that：The tower lid with
Concentration tower body is articulated and connected, and positioned at concentration tower body crown center, tower, which covers, is additionally provided with handle.
A kind of 8. feldspar in powder production waste recycle system according to claim 1, it is characterised in that：The thickening cone
The first deflector and the second deflector are inside also set up, first deflector is in tapered structure, and its tapering is located at the second weather board
Underface and the bell mouth of the deflector of face second, its afterbody are located at the bell mouth more than the second deflector.
A kind of 9. feldspar in powder production waste recycle system according to claim 1, it is characterised in that：The outlet pipe
Water inlet one end be located at the middle part of inner cylinder.
A kind of 10. feldspar in powder production waste recycle system according to claim 1, it is characterised in that：The clear water
Pond is also arranged with the sedimentation basin that battle field is washed in connection with respect to sedimentation basin side；Being horizontally set with above sedimentation basin is having mounting bracket, mounting bracket
On be provided with connection concentration tower body tower lid water inlet water plug and for sedimentation basin stirring agitator, the water plug
Including pumping motor, rotating shaft, water pump, pump mouth and water proof cylinder, the pumping motor is arranged on mounting bracket, and its rotating shaft correspondingly connects
The water pump for being fixed on sedimentation basin bottom is connect, the water pump bottom is provided with the pump mouth of corresponding sedimentation basin bottom；The rotating shaft overcoat
Provided with the water proof cylinder that sealing is formed to it, water proof cylinder one end connection mounting bracket, other end connection water pump.
A kind of 11. feldspar in powder production waste recycle system according to claim 9, it is characterised in that：The stirring
Device includes stirring motor, agitating shaft, stirring vane and bracing strut, and the stirring motor is arranged on mounting bracket, its agitating shaft pair
The stirring vane positioned at sedimentation basin bottom should be connected, the bracing strut is set in inverted pyramid, its larger one end and sedimentation basin side
Wall is fixed, and it is more a little bit smaller to be rotatably connected with agitating shaft.
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| CN201710840271.1A CN107376505B (en) | 2017-09-15 | 2017-09-15 | A kind of feldspar in powder production waste recycle system |
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Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
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| CN109019927A (en) * | 2018-08-30 | 2018-12-18 | 贺州市骏鑫矿产品有限责任公司 | A kind of sewage-treatment plant of ore production |
| CN109052689A (en) * | 2018-08-30 | 2018-12-21 | 贺州市骏鑫矿产品有限责任公司 | Ore sewage treatment system |
| CN109052691A (en) * | 2018-08-31 | 2018-12-21 | 贺州市骏鑫矿产品有限责任公司 | A kind of feldspar in powder production sewage treatment system |
| CN109126278A (en) * | 2018-09-30 | 2019-01-04 | 贺州市骏鑫矿产品有限责任公司 | A kind of feldspar in powder production waste utilization system |
| CN109133457A (en) * | 2018-09-30 | 2019-01-04 | 贺州市骏鑫矿产品有限责任公司 | A kind of feldspar in powder production sewage treatment method |
| CN109133430A (en) * | 2018-09-30 | 2019-01-04 | 贺州市骏鑫矿产品有限责任公司 | A kind of circulation utilization method of feldspar in powder production waste water |
| CN111573807A (en) * | 2020-05-28 | 2020-08-25 | 贺州市骏鑫矿产品有限责任公司 | Potassium feldspar powder waste liquid recovery processing system |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN108947003A (en) * | 2018-07-05 | 2018-12-07 | 珠海市盛西源机电设备有限公司 | The solid face water mill cooling water self-skimming circulatory system |
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| CN109052689A (en) * | 2018-08-30 | 2018-12-21 | 贺州市骏鑫矿产品有限责任公司 | Ore sewage treatment system |
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| CN109052691B (en) * | 2018-08-31 | 2021-11-09 | 贺州市骏鑫矿产品有限责任公司 | Potassium feldspar powder production sewage treatment system |
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| CN109133457A (en) * | 2018-09-30 | 2019-01-04 | 贺州市骏鑫矿产品有限责任公司 | A kind of feldspar in powder production sewage treatment method |
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| CN111573807A (en) * | 2020-05-28 | 2020-08-25 | 贺州市骏鑫矿产品有限责任公司 | Potassium feldspar powder waste liquid recovery processing system |
| CN111573807B (en) * | 2020-05-28 | 2022-01-28 | 贺州市骏鑫矿产品有限责任公司 | Potassium feldspar powder waste liquid recovery processing system |
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Denomination of invention: A recycling system for wastewater from potassium feldspar powder production Effective date of registration: 20211108 Granted publication date: 20180731 Pledgee: Bank of Guilin Co., Ltd. Hezhou branch Pledgor: Hezhou Junxin mineral products Co., Ltd Registration number: Y2021450000045 |
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