CN203491362U - Storage battery recycling separation system - Google Patents
Storage battery recycling separation system Download PDFInfo
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- CN203491362U CN203491362U CN201320543007.9U CN201320543007U CN203491362U CN 203491362 U CN203491362 U CN 203491362U CN 201320543007 U CN201320543007 U CN 201320543007U CN 203491362 U CN203491362 U CN 203491362U
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/84—Recycling of batteries or fuel cells
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Abstract
The utility model discloses a storage battery recycling separation system which comprises a breaking and screening unit, a diachylon recycling unit and a multi-level hydraulic power separation unit, wherein the breaking and screening unit is used for breaking and screening the storage battery to be recycled; the diachylon recycling unit is used for collecting the screen underflow separated by the breaking and screening unit; the multi-level hydraulic power separation unit is used for separating the oversize product separated by the breaking and screening unit; the diachylon recycling unit comprises a reservoir for supplying water to the breaking and screening unit and the diachylon recycling unit. In the system disclosed by the utility model, the water for the system is collected by the diachylon recycling unit and circularly utilized in the whole system, thereby effectively improving the utilization rate of the water resource, saving the water resource and reducing sewage discharge; the storage battery is subjected to multi-level breaking, magnetic separation, vibratory screening, sedimentation and multi-level hydraulic power separation by the devices, thereby improving the separation effect of the storage battery, realizing more complete separation and facilitating the recycling and secondary utilization; moreover, the devices are connected in order, the operation is stable, the automation degree is high, and the system is applicable to the field of modernized storage battery recycling.
Description
Technical field
The utility model relates to a kind of Battery recycling equipment, particularly a kind of Battery recycling piece-rate system.
Background technology
Along with social development, the continuous rising of battery use amount, has produced a large amount of old and useless batterys.Old and useless battery contains the electrolyte solutions such as a large amount of heavy metals and spent acid, salkali waste.If arbitrarily abandoned, corrupt battery can destroy our water source, corrodes crops and soil that we depend on for existence, and our living environment will be faced with huge threat.So the old and useless battery after using is carried out to the practicable very important of recycling, not only can prevent contaminated environment, can also wherein useful composition be recycled, economize on resources.
But, at present from domestic aggregate level, Production of Secondary Lead small scale, energy consumption is high, industrial technology is backward, adopts relatively backward PROCESS FOR TREATMENT lead-acid accumulator, artificial or adopt simple mechanical device that lead-acid accumulator is broken, take out after lead grid, the refuses such as plastic casing and dividing plate are stacked everywhere, do not made full use of and waste resource, and on plastic casing and dividing plate, also remaining lead in small, broken bits and lead plaster, cannot remove, easily cause secondary pollution.
For above-mentioned existing waste and old lead acid accumulator aspect recycling because of process equipment, technical matters, production scales etc. fall behind and exist organic efficiency low, the problem such as seriously polluted, there is researcher to propose a kind of Battery recycling method, notification number is that the patent documentation of CN102534220B discloses a kind of waste and old lead acid accumulator closed circulation recoverying and utilizing method, by fragmentation, vibrating screen sorting, magnetic separation, waterpower sorting, the methods such as eddy current sorting, first each feed separation in used and scrapped battery is come, then the plumbous mud obtaining is carried out to desulfurization, pressure filtration is processed, then by the plumbous mud of the dry desulfurization obtaining with lead grid is sent into converter successively and kier carries out melting and refining, the plumbous liquid finally refining being obtained is made lead powder, lead grid or lead pig, store for future use or work as finished product and sell.
In this application document, compound after fragmentation is cleaned to sorting on the second vibrating screen, and the plumbous mud producing in this process and acid solution are sent in holding vessel, while cleaning sorting on vibrating screen, separated lead plaster is with large quantity of moisture, need sedimentation in settling tank, in infall process, produce a large amount of waste water.
Notification number is that the patent documentation of CN202495559U discloses a kind of waste lead acid battery reclaimer, comprise casing, its inner cavity that forms, casing is provided with charging aperture and water inlet, in this casing, be provided with agitating device and conveying worm, this cavity bottom is provided with scrapper conveyor.Equipment in above-mentioned patent documentation is collected by lead plaster method of sedimentation in casing.
The said equipment, in infall process, needs a large amount of water resourcess, and lead plaster mixed liquor upper strata still contains a large amount of lead plasters, if effectively do not filter and process with regard to outer row, and waste water resource not only, and can cause serious water pollution.
Utility model content
The utility model provides a kind of Battery recycling piece-rate system, and single to solve existing reclaimer separation, separating effect is not good, the problem that water resource waste is serious.
A Battery recycling piece-rate system, comprising:
Crushing and screening unit, carries out fragmentation and screening to storage battery to be recycled; Lead plaster recovery unit, the screenings that the separation of crushing and screening unit is obtained is collected; Multi-stage water power separative element, the oversize that the separation of crushing and screening unit is obtained carries out separation;
Described lead plaster recovery unit comprises:
Top is provided with the subsider of the first overfall, and this subsider is for receiving the screenings that the unit separation of described crushing and screening obtains;
Be arranged on the interior scrapper conveyor for delivery of sedimentation lead plaster of subsider;
Be positioned at scrapper conveyor discharging opening below for collecting the recycling can of lead plaster;
With the sedimentation basin of inlet, described inlet is communicated with the first overfall, and the bottom of this sedimentation basin is with discharge gate, and described discharge gate is connected with the transfer pipeline that precipitation lead plaster is transported to recycling can charging aperture, and the top of described sedimentation basin is with the second overfall;
By the cistern of pipeline connection to the second overfall, described cistern to crushing and screening unit and lead plaster recovery unit supply water.
During said system work, after the screening of crushing and screening unit, obtain entering subsider with the lead plaster of large quantity of moisture, the larger lead plaster rapid subsidence of proportion is to subsider bottom, and lead plaster mixed liquor continues to fall into subsider, and the upper strata mixed liquor height in subsider arrives the first overfall, upper strata mixed liquor flows out from the first overfall, by described inlet, enter sedimentation basin, in sedimentation basin, mixed liquor carries out secondary sedimentation.By secondary sedimentation, arrange, the larger lead plaster of proportion sinks fast in subsider, and the lead plaster that proportion is less enters and in sedimentation basin, carries out secondary sedimentation, thereby effectively improves the settling efficiency of lead plaster.
In secondary infall process, the lead plaster in mixed liquor is settled down to sedimentation basin bottom, and the cleaner mixed liquor in upper strata enters described cistern by the second overfall, cistern to crushing and screening unit and lead plaster recovery unit supply water.
In said process, water is sieved to subsider in vibration, then to sedimentation basin, finally by cistern, carries out retaining, and to crushing and screening unit and lead plaster recovery unit supply water, water resources is recycled, realize sewage zero-discharge, be beneficial to conservation of nature environment.
In order to improve the separation rate of lead plaster, preferred, described crushing and screening unit comprises:
Storage battery is carried out to broken for the first time one-level disintegrating machine; The acid liquor filtering transport network of docking one-level disintegrating machine discharging opening; Be positioned at acid liquor filtering transport network below for collecting the acid solution feeder of acid solution; Below is provided with the concentration equipment of conveyer belt, and described conveyer belt is accepted the compound of the top of described acid liquor filtering transport network; Charging aperture is arranged on the secondary breaker of described conveyer belt below, the compound for second-time breakage through magnetic separation; The lead plaster separation vibrating sieve of docking secondary breaker discharging opening.
One-level disintegrating machine is by after storage battery fragmentation, and the acid solution in storage battery flows out, and by acid liquor filtering transport network, filters, and by acid solution feeder, is collected; Concentration equipment is isolated the magnetic metal in the compound of primary fragmentation, afterwards the compound by concentration equipment is carried out to second-time breakage, and the mixture particle after second-time breakage is less, enters lead plaster separation vibrating sieve and carries out Isolation and screening.
Further preferred, described lead plaster separation vibrating sieve comprises: frame, by the first damping part, be connected the first vibrating bin with frame, be arranged on the first vibrating motor on the first vibrating bin and be arranged on the material transport network of accepting secondary breaker discharging opening in the first vibrating bin, described subsider is positioned at material transport network below for collecting undersize material;
In described the first vibrating bin, be also provided with some showers that are positioned at material transport network top, the arrival end of every shower extends to the first vibrating bin outside and is supplied water by described cistern, and the tube wall of every shower is provided with some spray heads.
The compound of second-time breakage is in lead plaster separation vibrating sieve, on the one hand, by the effect of the first vibrating motor, material transport network drives compound vibration, make the materials such as lead plaster and plastic housing and screen more easily separated, and in vibration processes lead plaster more easily the mesh by material transport network fall in the subsider being arranged on below described material transport network.On the other hand, above material transport network, shower is set, to compound water spray, utilizes the impulse force of water by feed separation such as lead plaster and plastic housing and screens, lead plaster easier mesh by material transport network under the washing away of water falls in subsider simultaneously.By above two kinds of methods, can effectively increase the separation rate of lead plaster, improve the rate of recovery of lead plaster in old and useless battery.
In order to improve the deposition efficiency of sedimentation basin, preferably, described sedimentation basin is drawn in until the long and narrow bottom forming downwards gradually by middle part, described discharge gate is communicated with the middle part in bottom lengths direction, in described bottom, be provided with conveying ribbon along its length, described conveying ribbon is coaxial mounted two parts, is in respectively discharge gate both sides, and two parts carry the mass transport direction of ribbon relative.Because described sedimentation basin is drawn in downwards by middle part gradually until the long and narrow bottom forming, even therefore a small amount of lead plaster precipitation also can form certain thickness in long and narrow bottom, is convenient to carry.The conveying ribbon being equipped with in long and narrow bottom, by the lead plaster of precipitation from being sent to the discharge gate being communicated with at bottom lengths direction middle part.Described sedimentation basin when in lead plaster mixed liquor, lead plaster content is less, still can precipitate and collect, and effectively improves settling efficiency.
In order to prevent that the excessive material of volume from entering sedimentation basin, preferred, the pipeline between described the first overfall and the inlet of sedimentation basin is provided with lautertuns.Mixed liquor enters lautertuns by the first overfall, in lautertuns, larger plastics and the metallic particles of shape in mixed liquor can be filtered, and avoids it to enter the normal operation that ribbon is carried in sedimentation basin impact.
In order to improve the rate of recovery of lead plaster, preferred, described sedimentation basin is provided with two, inlet access in parallel first overfall of two sedimentation basins, and the inlet of one of them sedimentation basin is provided with hydraulic valve.Described hydraulic valve at pressure hour, in closed condition, now, only have and do not have the work of the sedimentation basin of hydraulic valve, when this sedimentation basin is inner, stop up, in the time of cannot getting rid of lead plaster and/or mixed liquor, it is large that the pressure at inlet place becomes, described hydraulic valve is open, and mixed liquor is entered be provided with to carry out sedimentation in the sedimentation basin of hydraulic valve.
In order to make the feed separation in storage battery more complete, preferred, multi-stage water power separative element comprises:
The first hydraulic flotation device of docking material transport network oversize discharging opening; The sinking material of collecting the first hydraulic flotation device by feed screw carries out the hydraulic reverse flushing device that water rushes flotation; The flotation vibrating screen of the light material outlet of docking hydraulic reverse flushing device; By feed screw, collect flotation vibrating screen screenings and carry out the second hydraulic flotation device of FLOTATION SEPARATION; The 3rd hydraulic flotation device of charging aperture docking flotation Vibration Screen material loading outlet and the outlet of the second hydraulic flotation device light material.
The light plastics floating of light specific gravity in the first hydraulic flotation device, the compounds such as metal, heavy plastics and dividing plate sink; The compound sinking enters hydraulic reverse flushing device and carries out water punching screening, heavy metal sinks, the compounds such as the heavy plastics that proportion is relatively little and dividing plate are gone out hydraulic reverse flushing device by water, enter flotation vibrating screen, the heavy plastics mixture that particle is less enters the second hydraulic flotation device by vibrating screen, in the first hydraulic flotation device, the light plastics of floating do not float, and heavy plastics is sunk; Upper buoyant in the oversize of flotation vibrating screen and the second hydraulic flotation device carries out flotation at the 3rd hydraulic flotation device, lower jetsam difficult with fragmentation compared with heavy material, large and there is certain volume material such as weights such as dividing plates, upper buoyant be light plastics.By above multi-stage water power separative element, can be by light plastics, heavy plastics, metal, is difficult to fragmentation compared with Weight material separation, and separation is more complete, is convenient to reclaim and secondary utilization, improves Battery recycling effect.
For the ease of the material to separated, reclaim, process and store, preferred, also comprise that, to the horizontal pressing device that under the 3rd hydraulic flotation device, jetsam carries out press filtration, described horizontal pressing device comprises:
Frame, is fixed on the discharge chambe in frame, and discharge chambe bottom is provided with leaking hole, described discharge chambe in two opposite sides respectively with charging aperture and discharging opening; From described charging aperture to discharge chambe, be pressed into the spiral swager of material; For opening or close the closing device of discharging opening; Described closing device comprises: with the seal head of discharging opening form fit; Be arranged in frame, the cylinder of thrust is provided to seal head; Relative with frame fixing, for guiding the cephalomotor guide post of sealing; For send the testing agency of reset signal to cylinder according to the displacement of described seal head.
While carrying out press filtration, start cylinder, seal head is coordinated with discharging opening, close discharging opening, now, the mutual butt of slide bar and seal head.Then spiral swager is constantly transported to material in discharge chambe, and because the volume of discharge chambe is certain, ever-increasing material compresses in discharge chambe, dehydration in the time of material compression, and the filtrate of generation is discharged by leaking hole.Because of described cylinder-pressing power certain, material in discharge chambe reaches after predetermined degree of compression, and material meeting reverse push movable sealing head, makes seal head have less displacement, drive with the slide bar of seal head butt and produce displacement, displacement transducer is tested slide bar and is produced displacement, thereby sends reset signal to cylinder, and cylinder resets, seal head is return, open discharging opening, spiral swager continues charging, and the material having compressed is squeezed out discharging opening by follow-up material.
In order to improve the material efficiency of hydraulic reverse flushing device, preferably, described hydraulic reverse flushing device comprises: the flotation cylinder of vertically-arranged, and described flotation cylinder is bending near place, top, bending angle is 15～35 degree, and described bending part comprises the inner side identical with overbending direction and the outside contrary with overbending direction; The top of described flotation cylinder has light material outlet, and bottom has heavier feeds outlet, and the sidewall in described bending part outside has compound import;
Described hydraulic reverse flushing device also comprises the hydraulic reverse washing pipe that the feed screw that dock with heavier feeds outlet and water jet are communicated to flotation cylinder bottom, and described cistern is to this hydraulic reverse washing pipe water supply.
During described hydraulic reverse flushing device work, in described flotation cylinder, be full of water, compound drops into feed well and enters flotation cylinder by compound import, hydraulic reverse washing pipe is washed by water in flotation cylinder, water impact compound upwards, the material that proportion is larger, for example metal still sinks down into flotation cylinder bottom, and discharges by feed screw; The material floating that proportion is lighter, along with current overflow light material outlet, discharges by material outlet canal; The bending of described flotation cylinder top arranges, the light material of floating is more easily discharged from light material outlet, but angle is unsuitable excessive, when bending angle is excessive, can make compound import and flotation cylinder cross section overlapping area excessive, the recoil strength of water can reduce compound charging efficiency, and therefore, bending angle is preferably 25 degree.
Preferably, described flotation vibrating screen comprises: the screening net of the light material outlet of docking hydraulic reverse flushing device; The second vibrating bin being connected with frame by the second damping part, described screening net is arranged in vibrating bin second; Be arranged on the second vibrating motor on the second vibrating bin.
Light material enters screening net, and under the effect of vibrating motor, the moving material vibrating of screening guipure, the less proportion of the particle material screen larger than water chosen to screening side off the net, and volume is larger, and the material that proportion is little passes through the online side of screening under the impulse force of water.
The beneficial effects of the utility model:
1) Battery recycling piece-rate system of the present utility model, collects system water by lead plaster recovery unit is set, and recycles in whole system, effectively improves the utilance of water resources, and saving water resource reduces sewage discharge.
2) Battery recycling piece-rate system of the present utility model, carries out multiple stage crushing by equipment to storage battery, magnetic separation, and vibration screening, sedimentation and multi-stage water power sorting, the separating effect of raising storage battery, separation is more complete, is beneficial to and reclaims and secondary utilization.
3) Battery recycling piece-rate system of the present utility model, each equipment connection is orderly, stable, and automaticity is high, is applicable to modernization Battery recycling field.
Accompanying drawing explanation
Fig. 1 is structured flowchart of the present utility model.
Fig. 2 is crushing and screening cellular construction schematic diagram of the present utility model.
Fig. 3 is lead plaster recovery unit structural representation of the present utility model.
Fig. 4 is the structural representation of sedimentation basin of the present utility model.
Fig. 5 is the structural representation of another angle of sedimentation basin of the present utility model.
Fig. 6 is the structural representation of lead plaster separation vibrating sieve of the present utility model.
Fig. 7 is lead plaster separation vibrating sieve internal structure schematic diagram of the present utility model.
Fig. 8 is the structural representation of multi-stage water power separative element of the present utility model.
Fig. 9 is the structural representation that hydraulic reverse flushing device of the present utility model is connected with flotation vibrating screen.
Figure 10 is the structural representation of horizontal pressing device of the present utility model.
Embodiment
As shown in Figure 1, the Battery recycling piece-rate system of the present embodiment comprises: crushing and screening unit, carries out fragmentation and screening to storage battery to be recycled; Lead plaster recovery unit, the screenings that the separation of crushing and screening unit is obtained is collected; Multi-stage water power separative element, the oversize that the separation of crushing and screening unit is obtained carries out separation.
As shown in Figure 2, crushing and screening unit comprises: storage battery is carried out to broken for the first time one-level disintegrating machine 11; The acid liquor filtering transport network 12 of docking one-level disintegrating machine discharging opening; Be positioned at acid liquor filtering transport network 12 belows for collecting the acid solution feeder 13 of acid solution; Below is provided with the concentration equipment 14 of conveyer belt, and conveyer belt is accepted the compound of the top of described acid liquor filtering transport network 12; Charging aperture is arranged on the secondary breaker 15 of conveyer belt below, the compound for second-time breakage through magnetic separation; The lead plaster separation vibrating sieve 1 of docking secondary breaker 15 discharging openings.
As shown in Figure 3, lead plaster recovery unit comprises: top is provided with the subsider 2 of the first overfall 25, the screenings that subsider 2 obtains for receiving the separation of crushing and screening unit; Be arranged on the interior scrapper conveyor 21 for delivery of sedimentation lead plaster of subsider 2; Be positioned at scrapper conveyor 21 discharging opening belows for collecting the recycling can 22 of lead plaster; Sedimentation basin 3 with inlet 31, inlet 31 is communicated with the first overfall 25, the bottom of sedimentation basin 3 is with discharge gate 32, and discharge gate 32 is connected with the transfer pipeline that precipitation lead plaster is transported to recycling can 22 charging apertures, and the top of sedimentation basin 3 is with the second overfall 33; By the cistern 4 of pipeline connection to the second overfall 33, cistern 4 to crushing and screening unit and lead plaster recovery unit supply water.Pipeline between the first overfall 25 and the inlet 31 of sedimentation basin 3 is provided with lautertuns 36.
As shown in Figure 4 and Figure 5, sedimentation basin 3 is drawn in until the long and narrow bottom 34 forming downwards gradually by middle part, the middle part that discharge gate 32 is communicated with in bottom lengths direction, in bottom 34, be provided with conveying ribbon 35 along its length, carrying ribbon 35 is coaxial mounted two parts, be in respectively discharge gate 32 both sides, two parts carry the mass transport direction of ribbon 35 relative.
In cistern 4, be provided with liquid level sensor 41, this liquid level sensor is connected with alarm by circuit.Cistern 4 bottoms are provided with tapping valve 43, and liquid level sensor 41 transmission of signals are controlled the switching of tapping valve 43.In cistern, be also provided with the submerged pump 42 for delivery of water.
As shown in Figure 6 and Figure 7, lead plaster separation vibrating sieve 1 comprises: frame, by the first damping part 16, be connected the first vibrating bin 17 with frame, be arranged on the first vibrating motor 18 on the first vibrating bin 17 and be arranged on the material transport network 19 of accepting secondary breaker discharging opening in the first vibrating bin 17, subsider 2 is positioned at material transport network 19 belows for collecting undersize material;
In the first vibrating bin 17, be also provided with some showers 110 that are positioned at material transport network 19 tops, the arrival end of every shower 110 extends to the first vibrating bin 17 outsides and is supplied water by cistern 4, and the tube wall of every shower 110 is provided with some spray heads 111.
As shown in Figure 8, multi-stage water power separative element comprises: the first hydraulic flotation device 5 of thing discharging opening on docking material transport network sieve 19; The sinking material of collecting the first hydraulic flotation device 5 by feed screw carries out the hydraulic reverse flushing device 6 that water rushes flotation; The flotation vibrating screen 7 of the light material outlet of docking hydraulic reverse flushing device 6; By feed screw, collect flotation vibrating screen 7 screenings and carry out the second hydraulic flotation device 51 of FLOTATION SEPARATION; The 3rd hydraulic flotation device 52 of the 7 oversize outlets of charging aperture docking flotation vibrating screen and the second hydraulic flotation device 51 light material outlets.
As shown in Figure 9, hydraulic reverse flushing device 6 comprises: the flotation cylinder 61 of vertically-arranged, and flotation cylinder 61 is bending near place, top, and bending angle is 15～35 degree, and bending part 62 comprises the inner side identical with overbending direction 63 and the outside 64 contrary with overbending direction; The top of flotation cylinder 61 has light material outlet 65, and bottom has heavier feeds outlet 66, and the sidewall in the outside 64 of bending part has compound import 67; Hydraulic reverse flushing device 6 also comprises the hydraulic reverse washing pipe 68 that is communicated to flotation cylinder 61 bottoms with heavier feeds outlet 66 feed screws that dock and water jet, and cistern 4 supplies water to this hydraulic reverse washing pipe 68.
The screening net of the light material outlet 65 of docking hydraulic reverse flushing device 6; The second vibrating bin 74 being connected with frame by the second damping part 73, screening net 71 is arranged in the second vibrating bin 74; Be arranged on the second vibrating motor 75 on the second vibrating bin 74.
As shown in figure 10, the present embodiment also comprises the horizontal pressing device 8 that under the 3rd hydraulic flotation device, jetsam carries out press filtration, comprising: frame, is fixed on the discharge chambe 81 in frame, discharge chambe 81 bottoms are provided with leaking hole, discharge chambe 81 in two opposite sides respectively with charging aperture 82 and discharging opening 83; From charging aperture 82 to discharge chambe 81, be pressed into the spiral swager 84 of material; For opening or close the closing device 85 of discharging opening;
Testing agency 89 comprises: the relative fixing fairlead 891 of frame; Slip is located in fairlead 891, and with the slide bar 892 that is in seal head 86 butts of sealing state; For gathering the displacement transducer (not shown in FIG.) of slide bar 892 displacement signals, displacement transducer transmits reset signal to cylinder 87.
In the present embodiment, discharging opening 83 is circular, and seal head 86 comprises that the conical surface of the conical section that cylindrical section and the contraction of cylindrical section end form coordinates with discharging opening 83; Slide bar 892 connects with the conical surface of seal head 86, and slide bar 892 is arcwall face with conical surface abutment end.
The foregoing is only better implementation example of the present utility model, be not limited to the utility model, all within the utility model spirit and principle, any modification of doing, be equal to replacement, improvement etc., within all should being included in protection range of the present utility model.
Claims (10)
1. a Battery recycling piece-rate system, is characterized in that, comprising:
Crushing and screening unit, carries out fragmentation and screening to storage battery to be recycled;
Lead plaster recovery unit, the screenings that the separation of crushing and screening unit is obtained is collected;
Multi-stage water power separative element, the oversize that the separation of crushing and screening unit is obtained carries out separation;
Described lead plaster recovery unit comprises:
Top is provided with the subsider of the first overfall, and this subsider is for receiving the screenings that the unit separation of described crushing and screening obtains;
Be arranged on the interior scrapper conveyor for delivery of sedimentation lead plaster of subsider;
Be positioned at scrapper conveyor discharging opening below for collecting the recycling can of lead plaster;
With the sedimentation basin of inlet, described inlet is communicated with the first overfall, and the bottom of this sedimentation basin is with discharge gate, and described discharge gate is connected with the transfer pipeline that precipitation lead plaster is transported to recycling can charging aperture, and the top of described sedimentation basin is with the second overfall;
By the cistern of pipeline connection to the second overfall, described cistern to crushing and screening unit and lead plaster recovery unit supply water.
2. Battery recycling piece-rate system as claimed in claim 1, is characterized in that, described crushing and screening unit comprises:
Storage battery is carried out to broken for the first time one-level disintegrating machine;
The acid liquor filtering transport network of docking one-level disintegrating machine discharging opening;
Be positioned at acid liquor filtering transport network below for collecting the acid solution feeder of acid solution;
Below is provided with the concentration equipment of conveyer belt, and described conveyer belt is accepted the compound of the top of described acid liquor filtering transport network;
Charging aperture is arranged on the secondary breaker of described conveyer belt below, the compound for second-time breakage through magnetic separation;
The lead plaster separation vibrating sieve of docking secondary breaker discharging opening.
3. Battery recycling piece-rate system as claimed in claim 2, it is characterized in that, described lead plaster separation vibrating sieve comprises: frame, by the first damping part, be connected the first vibrating bin with frame, be arranged on the first vibrating motor on the first vibrating bin and be arranged on the material transport network of accepting secondary breaker discharging opening in the first vibrating bin, described subsider is positioned at material transport network below for collecting undersize material;
In described the first vibrating bin, be also provided with some showers that are positioned at material transport network top, the arrival end of every shower extends to the first vibrating bin outside and is supplied water by described cistern, and the tube wall of every shower is provided with some spray heads.
4. Battery recycling piece-rate system as claimed in claim 1, it is characterized in that, described sedimentation basin is drawn in until the long and narrow bottom forming downwards gradually by middle part, described discharge gate is communicated with the middle part in bottom lengths direction, in described bottom, be provided with conveying ribbon along its length, described conveying ribbon is coaxial mounted two parts, is in respectively discharge gate both sides, and two parts carry the mass transport direction of ribbon relative.
5. Battery recycling piece-rate system as claimed in claim 4, is characterized in that, the pipeline between described the first overfall and the inlet of sedimentation basin is provided with lautertuns.
6. Battery recycling piece-rate system as claimed in claim 1, is characterized in that, described sedimentation basin is provided with two, inlet access in parallel first overfall of two sedimentation basins, and the inlet of one of them sedimentation basin is provided with hydraulic valve.
7. Battery recycling piece-rate system as claimed in claim 1, is characterized in that, multi-stage water power separative element comprises:
The first hydraulic flotation device of docking material transport network oversize discharging opening;
The sinking material of collecting the first hydraulic flotation device by feed screw carries out the hydraulic reverse flushing device that water rushes flotation;
The flotation vibrating screen of the light material outlet of docking hydraulic reverse flushing device;
By feed screw, collect flotation vibrating screen screenings and carry out the second hydraulic flotation device of FLOTATION SEPARATION;
The 3rd hydraulic flotation device of charging aperture docking flotation Vibration Screen material loading outlet and the outlet of the second hydraulic flotation device light material.
8. Battery recycling piece-rate system as claimed in claim 7, is characterized in that, also comprise the horizontal pressing device that under the 3rd hydraulic flotation device, jetsam carries out press filtration,
Described horizontal pressing device comprises:
Frame, is fixed on the discharge chambe in frame, and discharge chambe bottom is provided with leaking hole, described discharge chambe in two opposite sides respectively with charging aperture and discharging opening;
From described charging aperture to discharge chambe, be pressed into the spiral swager of material;
For opening or close the closing device of discharging opening;
Described closing device comprises: with the seal head of discharging opening form fit; Be arranged in frame, the cylinder of thrust is provided to seal head; Relative with frame fixing, for guiding the cephalomotor guide post of sealing; For send the testing agency of reset signal to cylinder according to the displacement of described seal head.
9. Battery recycling piece-rate system as claimed in claim 7, it is characterized in that, described hydraulic reverse flushing device comprises: the flotation cylinder of vertically-arranged, described flotation cylinder is bending near place, top, bending angle is 15～35 degree, and described bending part comprises the inner side identical with overbending direction and the outside contrary with overbending direction;
The top of described flotation cylinder has light material outlet, and bottom has heavier feeds outlet, and the sidewall in described bending part outside has compound import;
Described hydraulic reverse flushing device also comprises the hydraulic reverse washing pipe that the feed screw that dock with heavier feeds outlet and water jet are communicated to flotation cylinder bottom, and described cistern is to this hydraulic reverse washing pipe water supply.
10. Battery recycling piece-rate system as claimed in claim 9, is characterized in that, described flotation vibrating screen comprises:
Frame;
The screening net of the light material outlet of docking hydraulic reverse flushing device;
The second vibrating bin being connected with frame by the second damping part, described screening net is arranged in vibrating bin second;
Be arranged on the second vibrating motor on the second vibrating bin.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320543007.9U CN203491362U (en) | 2013-09-02 | 2013-09-02 | Storage battery recycling separation system |
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| Application Number | Priority Date | Filing Date | Title |
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| CN201320543007.9U CN203491362U (en) | 2013-09-02 | 2013-09-02 | Storage battery recycling separation system |
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| CN203491362U true CN203491362U (en) | 2014-03-19 |
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| CN201320543007.9U Expired - Fee Related CN203491362U (en) | 2013-09-02 | 2013-09-02 | Storage battery recycling separation system |
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Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104014414A (en) * | 2014-05-23 | 2014-09-03 | 株洲金鼎高端装备有限公司 | Secondary sorting method for waste lead-acid battery broken materials |
| CN105070972A (en) * | 2015-08-31 | 2015-11-18 | 淄博火炬能源有限责任公司 | Recycling method and device for waste diachylon of lead-acid storage battery |
| CN106269194A (en) * | 2016-08-22 | 2017-01-04 | 哈尔滨巴特瑞资源再生科技有限公司 | A kind of charged breaker of power old and useless battery and breaking method |
| CN109065994A (en) * | 2018-07-26 | 2018-12-21 | 武汉科技大学 | A kind of battery remanufactures disassembly, cleaning separation system |
| CN112221653A (en) * | 2020-06-15 | 2021-01-15 | 宁夏瑞银有色金属科技有限公司 | Crushing and separating method and system for lead-acid storage battery |
| CN112563600A (en) * | 2020-11-05 | 2021-03-26 | 浙江天能动力能源有限公司 | Method for recycling waste lead plaster of waste polar plate |
-
2013
- 2013-09-02 CN CN201320543007.9U patent/CN203491362U/en not_active Expired - Fee Related
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104014414A (en) * | 2014-05-23 | 2014-09-03 | 株洲金鼎高端装备有限公司 | Secondary sorting method for waste lead-acid battery broken materials |
| CN105070972A (en) * | 2015-08-31 | 2015-11-18 | 淄博火炬能源有限责任公司 | Recycling method and device for waste diachylon of lead-acid storage battery |
| CN105070972B (en) * | 2015-08-31 | 2017-08-04 | 淄博火炬能源有限责任公司 | The recoverying and utilizing method and its device of lead-acid accumulator scrap lead cream |
| CN106269194A (en) * | 2016-08-22 | 2017-01-04 | 哈尔滨巴特瑞资源再生科技有限公司 | A kind of charged breaker of power old and useless battery and breaking method |
| CN109065994A (en) * | 2018-07-26 | 2018-12-21 | 武汉科技大学 | A kind of battery remanufactures disassembly, cleaning separation system |
| CN109065994B (en) * | 2018-07-26 | 2021-02-19 | 武汉科技大学 | Cleaning and sorting system for remanufacturing, disassembling and cleaning storage battery |
| CN112221653A (en) * | 2020-06-15 | 2021-01-15 | 宁夏瑞银有色金属科技有限公司 | Crushing and separating method and system for lead-acid storage battery |
| CN112563600A (en) * | 2020-11-05 | 2021-03-26 | 浙江天能动力能源有限公司 | Method for recycling waste lead plaster of waste polar plate |
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