A kind of feldspar in powder production waste recycle system
The present invention relates to waste water recycling field, especially a kind of feldspar in powder produces waste recycle system.
In the production and processing of potassium ore, need, to ore progress and eddy flow processing etc., to generate in these processing steps
A large amount of waste water contains a large amount of potassium ore fine sand or fine particle etc. in waste water.If directly excluded, first can pollute ring
Very big injury is caused in border to environment；Second increasingly lacks instantly in water resource, and waste water source can greatly increase enterprise's life
Produce cost；Fine sand in third production excludes therewith, can increase post-processing difficulty.
In the prior art, the sewage disposal systems such as metallic ore and the processing ore dressing of non-mine, are by sedimentation basin, concentration tower, squeezing
The compositions such as machine.When for treated sewage, by the way that tailing sewage to be discharged into sedimentation basin, and alchlor shape is put into sedimentation basin
It at mud, is then stirred in sedimentation basin, the slag in mud is made to be precipitated by gravity, it is further dense by concentration tower
Division separates out water overflow discharge.Squeezer is further processed to obtain siccative to the mud after concentration.But existing processing system is deposited
The defects of inconvenient, high failure rate in concentration operation, treatment effeciency is low equal.
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 the first, second concentration tower to be concentrated, which contains riddler, and riddler will
Heavies in pulp water filter out；The progress vacuum dehydration of first, second vacuum hydroextractor and etc..Its processing step is more, special
It is not that vacuum hydroextractor energy 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 by supporting rack in outer barrel, and the upper end of inner cylinder is into sewage mouth, and the centre of inner cylinder is installed one by supporting rack and delayed
Baffle is rushed, there are charging gaps, the outer wall of inner cylinder to be further fixed at least one between the edge of cushioning fender and the inner wall of inner cylinder
Ring-like reverse flow baffle, there are spilling water gaps, the following diameter of outer barrel gradually to contract between the outer rim of reverse flow baffle and the inner wall of outer barrel
The upper end of small formation slag-drip opening, outer barrel forms overflow sink, and the gap of overflow sink is independently separated with into sewage mouth.The precipitation
Concentration tank can quickly be handled the larger heavier sewage containing particle, but for containing the smaller lighter sewage of particle, no
It can accomplish that rapid precipitation concentrates, since particle is smaller relatively light in sewage, when especially sewage is extracted into precipitation concentration tank, in sewage
Grain be in suspended state, can not rapid precipitation get off, especially as shown in the patent accompanying drawing, if continue sewage suction,
What is so flowed out from precipitation concentration tank is still the effect that rapid precipitation is much not achieved containing the more water of tailing particles and concentrates.
Accordingly, it is desirable to provide a kind of new technical solution solves above-mentioned technical problem.
In order to solve technical barrier in the prior art, the present invention provides a kind of feldspar in powder production waste water recycling system
System realizes quick cyclic utilization and mine to waste water by providing a kind of processing system for not needing chemical agent and being settled
Slag recycles.Here it is arranged by the way that multiple filtration is arranged and can carries out rapid precipitation concentration to the sewage continued to flow into, especially
It is suitble to the quick cyclic utilization of the feldspar in powder production waste water containing the particle less than 80 mesh.
Technical solution according to the present invention provides a kind of feldspar in powder production waste recycle system comprising,
Sedimentation basin, including several and be arranged side by side, sedimentation basin connection be located at water mill workshop in waste water ditch, be used for back
Receive the waste water of K-feldspar slag charge in water mill workshop；
Concentration tower obtains the concentrate of high potassium feldspar slag charge content by carrying out concentration to the waste water；
Slag charge siccative and filtered fluid, the slag charge siccative is obtained by filtration in the concentrate squeeze and filter of concentration tower by squeezer
It is transported in recovery bin, the filtered fluid pumped back concentration tower；And
Clear water reserviors are set up in parallel below concentration tower and with sedimentation basin, and clear water reserviors collection concentration tower is obtained by filtration clear
Water and recovery bin reflux clear water；
The concentration tower includes concentration tower body, stabilizer blade, Ta Gai, water filtering tube, outlet pipe, overflow pipe, the first weather board and the
The stabilizer blade being used to support is arranged in two weather boards, the concentration tower body lower part, and the drainage is arranged by supporting rack in bosom
Cylinder, water filtering tube connect outlet pipe, and outlet pipe water outlet corresponds to clear water reserviors；It concentrates and is equipped with turnover tower lid, tower lid at the top of tower body
It is equipped with the water inlet of connection sedimentation basin；The overflow pipe is located at the external side of concentration tower, and one end connection concentrates tower body top, separately
One end corresponds to sedimentation basin；First weather board is arranged in a ring in concentration tower body inner wall, and positioned at concentration tower body and water filtering tube
Between；Second weather board is in funnel-form, and below water filtering tube, and wide-mouth one end is connect with concentration tower body inner wall；Institute
It is in funnelform thickening cone, the blow-off valve of thickening cone bottom setting connection squeezer to state concentration tower body lower part, 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 among drainage cylinder by supporting rod, the first filter chamber is formed between inner cylinder and drainage cylinder, inner cylinder is opened under being
Mouth tube structure, inner cylinder lower part 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；Drainage cylinder lower part is in funnel-form, and bottom is provided with the recovery valve opened downward；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 is equipped with to be arranged in the shape of a spiral with its center
The side wall of the drainage cylinder is made 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,
Interior stainless steel fine-structure mesh composition, the drainage cylinder body bottom and top are made of stainless steel.
Preferably, edge concentrates tower body inner wall between the upper and lower every setting, the first weather board and drainage between first weather board
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, water fender upper end connection concentration tower body top, and its specification is more than the water inlet of overflow pipe
Preferably, the tower lid and concentration tower body articulated connection, and positioned at concentration tower body top center, tower, which covers, to be additionally provided with
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 has been horizontally set with mounting bracket, and the water plug of connection concentration tower body tower lid water inlet is equipped on mounting bracket and is stirred for sedimentation basin
Blender, the water plug includes pumping motor, shaft, water pump, pump mouth and water proof cylinder, and the pumping motor is mounted on
On mounting bracket, shaft is correspondingly connected with the water pump for being fixed on sedimentation basin bottom, and the water pump bottom is equipped with corresponding sedimentation basin bottom
Pump mouth；The water proof cylinder that sealing is formed to it is arranged with outside the shaft, water proof cylinder one end connects mounting bracket, other end connection
Preferably, the blender includes stirring motor, agitating shaft, stirring blade and bracing strut, the stirring motor peace
On mounting bracket, agitating shaft is correspondingly connected with the stirring blade positioned at sedimentation basin bottom, and the bracing strut is set in inverted pyramid
It sets, larger one end is fixed with sedimentation basin side wall, and smaller one end is rotatably connected with agitating shaft.
Due to the adoption of the above technical scheme, 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, is mainly separated by solid-liquid separation, is further concentrated to waste water, improve its high potassium feldspar slag charge content, and be sent into squeezer；Pressure
Crusher is existing solid-liquid separation device, can be separated by solid-liquid separation to obtain slag charge siccative to being sent into waste water, slag charge siccative is direct
It is sent into recovery bin, and the waste water that squeezer generates comes back to concentration tower concentration again；In the process, concentration tower can
To obtain meeting the clear water of re-using standard, the sources feldspar in powder production process Zhong Shui can be used as, and obtained waste material can
To re-use.Reduce feldspar in powder in production process, slag through the invention in this way because waste water is lost in, the rate of recovery reaches
85% or more,；It simultaneously can be to waste water cycling and reutilization.
2. concentration tower uses multiple filtration structure, wherein drainage cylinder lateral wall to use micropore ceramic filter material in the present invention
It is made, thickness 3-7cm, 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, in the clear water that the second filter chamber obtains meeting recycling, and is discharged to clear water reserviors.The small size deposited in first filter chamber is high
For potassium feldspar slag charge when concentrating tower body water level less than the first filter chamber bottom, first time filtered fluid is due to itself in the first filter chamber
Gravity, which is directly opened, restores valve so that first time filtered fluid is directly discharged into concentration tower body in the thickening cone of lower part.Concentration tower
The slag that concentration reaches 53%-66% can be discharged.Its clear water generated can direct recycling.
Description of the drawings
Fig. 1 is present system work flow diagram；
Fig. 2 is function module distribution map of the present invention；
Fig. 3 is sedimentation basin structural schematic diagram of the present invention；
Fig. 4 is concentration tower structural schematic diagram.
In attached drawing, 1- sedimentation basins, 2- concentration towers, 21- concentrations tower body, 22- stabilizer blades, 23- towers lid, 231- water inlets, 232-
Handle, 24- overflow pipes, 241- water fenders, 25- thickening cones, 251- blow-off valves, the first deflectors of 252-, the second deflectors of 253-,
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 second weather boards of 29-, 3- squeezers, 4- clear water reserviors, 5- water plugs, 51- pumping motors, 52- shafts,
53- water pumps, 54- pump mouths, 55- water proofs cylinder, 6- aqueducts, 7- blenders, 71- stirring motors, 72- agitating shafts, 73- stirrings
Blade, 74- bracing struts.
Specific implementation mode
The present invention provides a kind of feldspars in powder to produce waste recycle system, can accomplish to produce waste water to feldspar in powder
Recycle, feldspar in powder, which produces, contains a large amount of feldspars in powder in waste water, minimum feldspar in powder up to 100 mesh sizes or so,
This is generated in eddy flow processing procedure in generating process；If do not handle recycling will waste water resource and ore significantly it is former
Material.Processing procedure is more slow in existing cyclic utilization system, cannot be handled into Line Continuity sewage, and for sewage
The slag size included also requires, and especially existing 2 structure of concentration tower cannot carry out the sewage of 100 mesh containing granular size
Quickly processing, these, which are all limited, generates production cycling utilization of wastewater in feldspar in powder.Therefore, the present invention proposes one kind and follows again
Loop system uses multiple filtration structure so that can be concentrated to sewage rapid precipitation, clear water is discharged by the way that concentration tower 2 is arranged
Utilization can be repeatedly generated without reprocessing.
The specific implementation of invention is further illustrated below in conjunction with attached drawing.
As shown in Figure 1, being present system work flow diagram, wherein 1 sedimentation basin 1 of sedimentation basin connection is located in water mill workshop
Waste water ditch, the waste water of K-feldspar slag charge in recycling water mill workshop.Concentration tower 2 to the waste water by carrying out concentration
Obtain the concentrate of high potassium feldspar slag charge content.It is dry that slag charge is obtained by filtration in the concentrate squeeze and filter of concentration tower 2 by squeezer 3
Material and filtered fluid, slag charge siccative are transported in recovery bin, filtered fluid pumped back concentration tower 2.4 clear water reserviors 4 of clear water reserviors collect concentration
Clear water and recovery bin the reflux clear water that tower 2 is obtained by filtration.
As shown in Fig. 2, flat functional distribution map of the present invention.Wherein, sedimentation basin 1 is located at 4 both sides of clear water reserviors, and sedimentation basin 1 wraps
It includes several and is arranged side by side, be connected to by top overflow port between sedimentation basin 1, water plug 5 is provided in sedimentation basin 1 and is stirred
Device 7 to be mixed, and concentration tower 2 is pumped by aqueduct 6, blender 7 is used to be stirred sedimentation basin 1, is conducive to wastewater sedimentation,
Simultaneously by 1 bottom precipitation rearrangement of sedimentation basin, facilitate water plug 5 that can pump the higher waste water of concentration containing slag to concentration
Tower 2.Concentration tower 2 is erected at 4 top of clear water reserviors.Two group precipitation ponds 1 and two groups of concentration towers 2 are set here, for corresponding to water respectively
Grind the waste water that workshop generates and the waste water that washery generates.
As Figure 2-3, the top of sedimentation basin 1 has been horizontally set with mounting bracket, be equipped on mounting bracket connection concentration tower body tower lid into
The water plug 5 at the mouth of a river and the blender 7 stirred for sedimentation basin 1.Water plug 5 includes water plug 51, shaft 52, water pump
53, pump mouth 54 and water proof cylinder 55, water plug 51 are mounted on mounting bracket, and shaft 52, which is correspondingly connected with, is fixed on sedimentation basin 1
The water pump 53 of bottom, 53 bottom of water pump are equipped with the pump mouth 54 of 1 bottom of corresponding sedimentation basin.Be arranged with outside shaft 52 it is formed it is close
The water proof cylinder 55 of envelope, 55 one end of water proof cylinder connect mounting bracket, and the other end connects water pump 53.Blender 7 include stirring motor 71,
Agitating shaft 72, stirring blade 73 and bracing strut 74；Stirring motor 71 is mounted on mounting bracket, and agitating shaft 72, which is correspondingly connected with, to be located at
The stirring blade 73 of 1 bottom of sedimentation basin, bracing strut 74 are arranged in inverted pyramid, and larger one end is fixed with 1 side wall of sedimentation basin,
Smaller one end is rotatably connected with agitating shaft 72.
As shown in figure 4, concentration tower 2 includes concentration tower body 21, stabilizer blade 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；The stabilizer blade 22 being used to support, bosom is arranged in 21 lower part of concentration tower body
Water filtering tube 26 is set by supporting rack, water filtering tube 26 connects outlet pipe 27, and 27 water outlet of outlet pipe corresponds to clear water reserviors 4.Concentration tower
21 top of body is equipped with turnover tower lid 23, and tower lid 23 is equipped with the water inlet 231 of connection sedimentation basin 1.Overflow pipe 24 is located at dense
21 outside of contracting tower body, 21 top of one end connection concentration tower body, the other end correspond to sedimentation basin 1；The water inlet of overflow pipe 24 231
Between 26 top of water filtering tube and inner cylinder 262,231 front of water inlet of overflow pipe 24 is additionally provided with water fender 241, water fender
241 upper ends connection concentration tower body, 21 top, and its specification is more than 231 specification of water inlet of overflow pipe 24.First weather board 28 is in
Annular setting is located in concentration 21 inner wall of tower body between concentration tower body 21 and water filtering tube 26；Second weather board 29 is in funnel-form,
And positioned at 26 lower section of water filtering tube, wide-mouth one end is connect with concentration 21 inner wall of tower body.Along concentration tower body between first weather board 28
21 inner walls form equidistant interval between setting, the first weather board 28 and water filtering tube 26 between the upper and lower, and interval specification is 4cm.It is dense
21 lower part of contracting tower body is in funnelform thickening cone 25, the blow-off valve 251 of 25 bottom of thickening cone setting connection squeezer 3, concentration
Bucket 25 is located at 29 lower section of the second weather board.
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 among drainage cylinder 261 in drainage cylinder 261, and by supporting rod, between inner cylinder 262 and drainage cylinder 261
Form the first filter chamber；Inner cylinder 262 is under shed tube structure, and 262 lower part of inner cylinder is provided with filter membrane 264, filter membrane 264
The second filter chamber is formed with 262 inner cavity of inner cylinder, the second filter chamber is connected to outlet pipe 27；Filter membrane 264 is located under inner cylinder 262
The aperture specification of the top of opening, filter membrane 264 is 0.1mm.261 lower part of drainage cylinder is in funnel-form, and bottom is provided with court
The recovery valve 265 of lower unlatching.It is arc structure at the top of 261 outer wall of drainage cylinder, and the water inlet 231 of face tower lid 23, filter
261 outer wall top of water drum body is equipped with the drainage plate 263 being arranged in the shape of a spiral with its center.The side wall of drainage cylinder 261 is by micropore
Ceramic filter 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, interior stainless steel fine-structure mesh composition, 261 bottom of drainage cylinder and top are made of stainless steel.Micropore ceramic filter material can be with
Small slag particle is filtered very well, and is not easy to result in blockage, maintenance easy to clean.Drainage cylinder 261 can directly lift taking-up,
Different micropore ceramic filter materials can be replaced as needed in this way.
Further, tower lid 23 is articulated and connected with concentration tower body 21, and on 21 top center of concentration tower body, tower lid 23
It is additionally provided with handle 232.Tower lid 23 can be opened, and 2 daily maintenance of concentration tower is facilitated.
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, tapering is located at immediately below the second weather board 29 and the bell mouth of the second deflector of face 253, and a tail portion 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 made quickly to calm down, and be conducive to concentrating and precipitating.
Above description is the detailed description for the present invention preferably possible embodiments, but embodiment is not limited to this hair
Bright patent claim, it is all the present invention suggested by technical spirit under completed same changes or modifications change, should all belong to
In the covered the scope of the claims of the present invention.