CN204522507U - A kind of dry-discharge system for tailings - Google Patents
A kind of dry-discharge system for tailings Download PDFInfo
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- CN204522507U CN204522507U CN201520175739.6U CN201520175739U CN204522507U CN 204522507 U CN204522507 U CN 204522507U CN 201520175739 U CN201520175739 U CN 201520175739U CN 204522507 U CN204522507 U CN 204522507U
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Abstract
The utility model provides a kind of dry-discharge system for tailings, and dry heat-extraction system is: with the side direction filter screen being centered around pond feather edge at the bottom of pond, side direction filter screen and side direction filter screen connect into stillpot; First abutment wall and the second abutment wall are all centered around the outside of stillpot, and the first abutment wall is centered around the outside of the second abutment wall; Connect the lower screen of the first abutment wall and the second abutment wall, at the bottom of the first abutment wall, lower screen, the second abutment wall, pond and side direction filter screen surround into annular space, fill particulate filter in annular space; Feeder is had below lower screen.The utility model adopts simple pump valve to control, and eliminates heavy mechanical equipment, and all kinds of cost is dropped to minimum, Operation and Maintenance is very convenient, can meet the tailings glass of the various concentration of big-and-middle-sized Mineral Processing Enterprises and granularity.
Description
Technical field
The utility model relates to tailing dry row field, in particular to a kind of dry-discharge system for tailings.
Background technology
Mine tailing refers to the waste residue slag that bargh discharges after ore dressing completes, and be arrange outward with slurry form, accumulate over a long period formation Tailings Dam.The useful component content of mine tailing is minimum, under current condition of technology and economy, and should not sorting further again.The bulk deposition of mine tailing needs a large-scale Tailings Dam, great environmental pollution can be caused, but also easily cause tailing dam dam-break accident, bring potential safety hazard, so tailing dry row process is of crucial importance, it not only can save construction cost and the General Maintenance expense of traditional tailing, and gravity flow backwater can also be made to make full use of, but also greatly can save floor space, eliminate the potential safety hazard of Tailings Dam.
Tailing dry row is by thickening technique, is delivered to a kind of technology mode that it is stored up or recycled in Tailings Dam and refuse dump after Tailings Slurry being prepared into dry material.At present conventional tailing dry-type emission technology is mechanical dry-extraction method, and namely, coarseness mine tailing adopts the plant equipment such as cyclone, concentrator, dewatering screen to carry out stepwise disposal to reach dry row's effect.The plant equipment such as the fine employing of fine granularity mine tailing cyclone, concentrator, dewatering screen, filter press are carried out stepwise disposal and are reached dry row's effect.
There is following shortcoming in above-mentioned dry row's technique: equipment purchase cost is higher, and plant equipment care and maintenance in daily production environment can produce larger expense, and the power consumption of equipment and because of depreciation damage produce expense huge too, in addition, also there is many obvious deficiencies in existing technique in subparticle tailings glass.
In view of this, special proposition the utility model.
Utility model content
First object of the present utility model is to provide a kind of dry-discharge system for tailings, described dry-discharge system for tailings is only made up of filtering settling pond, not only eliminate heavy mechanical equipment, provide cost savings largely, whole system is simple to operate, easy to maintenance, water resource cyclic utilization rate is high, can be used for the Tailings Slurry processing various concentration and grade, especially, can the mine tailing of low-cost processes Ultra-fine.
Second object of the present utility model is to provide a kind of described tailing dry discharge method, and described method does not need heavy mechanical equipment, and processing cost is low, and technique is simple, and can process the mine tailing of ultra-fine grade, has filled up the blank of prior art.
In order to realize above-mentioned purpose of the present utility model, spy by the following technical solutions:
A kind of dry-discharge system for tailings, comprise filtering settling pond, described filtering settling pond comprises:
With the side direction filter screen being centered around described pond feather edge at the bottom of pond, described side direction filter screen and described side direction filter screen connect into stillpot;
First abutment wall and the second abutment wall, described first abutment wall and described second abutment wall are all centered around the outside of described stillpot, and described first abutment wall is centered around the outside of described second abutment wall;
Connect the lower screen of described first abutment wall and described second abutment wall, the horizontal plane of described lower screen lower than or the horizontal plane that flushes at the bottom of described pond; At the bottom of described first abutment wall, described lower screen, described second abutment wall, described pond and described side direction filter screen surround into annular space, be filled with particulate filter in described annular space;
Be arranged on the feeder of the below of described lower screen.
Above-mentioned dry-discharge system for tailings can complete efficient dehydration by the filtering settling pond of structure uniqueness, this filtering settling pond contains gravitational settling structure, horizontal filtering structure, the vertical multiple dehydrated structure such as filtration and filter structure, thus possess repeatedly with multi-level dehydrating function, not only eliminate relevant cost that is large-scale or complex mechanical equipment, and dewatering efficiency is also high than conventional mechanical devices, the Tailings Slurry of high concentration (20%-30%) and ultra-fine grade mine tailing can also be processed, meet the needs of big-and-middle-sized Mineral Processing Enterprises tailing dry row completely.
The operation principle of above-mentioned dry-discharge system for tailings is as follows:
Tailings Slurry is injected stillpot, along with passage of time, under gravity, most of particle deposit buildup in Tailings Slurry is at the bottom of pond, and subparticle diffusion motion together with water of fraction, to the surrounding of stillpot, enters particulate filter layer through side direction filter screen, subparticle is wherein adsorbed by particulate filter, the water oozed out flows into feeder through lower screen, now completes the dehydration of Tailings Slurry, achieves dry row.
As can be seen here, above-mentioned dry-discharge system for tailings adopts simple physical arrangement can complete all treatment process of complicated plant equipment.Certainly, this dry-discharge system for tailings also may be used for processing other suspension (sanitary sewage, trade effluent etc.).
Preferably, the horizontal plane of described lower screen is lower than the horizontal plane at the bottom of described pond, and the distance between described second abutment wall and described first abutment wall is greater than the distance between described side direction filter screen and described first abutment wall.
Said structure can ensure from side direction filter screen through pulp-water be first filter through particulate filter layer, then filtered by lower screen and enter trench, namely ensure that all filtrations of all ranks in filtering settling pond of all Tailings Slurries, fully dewatered; Avoid part from side direction filter screen through pulp-water directly by lower screen, or along Second Edge wall through lower screen.
Preferably, at the bottom of described pond, described first abutment wall, described second abutment wall form by concreting: sound construction is reliable.
Preferably, flushing pipe is provided with in described particulate filter; Arrange flushing pipe to rinse particulate filter, ensure dry be drained through journey continue carry out and particulate filter benign cycle use.
Preferably, described stillpot is provided with clean-out door: the convenient precipitation slag removed in groove.
Preferably, described particulate filter is quartz sand filter media: the advantages such as it has free from admixture, anti-pressure and abrasion-proof, mechanical strength is high, stable chemical performance, retaining power strong, high efficiency, life cycle are long.
Preferably, described feeder is trench: ingenious using underground space, saves the construction cost of filtering settling pond, and can save space.
Preferably, comprise multiple described filtering settling pond, also comprise one-level transition pond, described multiple filtering settling pond is divided into following two groups: single filter sedimentation basin group and cascade filtration sedimentation basin group;
The aperture of all filter screens of the filtering settling pond in described cascade filtration sedimentation basin group is less than the aperture of all filter screens of the filtering settling pond in described single filter sedimentation basin group;
The feeder of all filtering settling ponds in described single filter sedimentation basin group is all connected with described one-level transition pond;
The described stillpot of all filtering settling ponds in described cascade filtration sedimentation basin group is all connected with described one-level transition pond.
Single filter sedimentation basin group and cascade filtration sedimentation basin group two ranks are set, the particle in Tailings Slurry are carried out the descending filtration of particle diameter, can not only dewatering efficiency be improved, and the cleanliness factor of pulp-water of collection can be promoted, to recycle.
In actual treatment, can increase according to the concentration of Tailings Slurry and particle diameter or reduce the progression of filtering settling pond group, such as, if the concentration of Tailings Slurry is higher, three-stage filtration sedimentation basin group can also be set up, specific as follows:
Also comprise three-stage filtration sedimentation basin group and secondary transition pond, and described three-stage filtration sedimentation basin group is made up of one or more described filtering settling pond;
The aperture of all filter screens of the filtering settling pond in described three grades of sedimentation basin groups is less than the aperture of all filter screens of the filtering settling pond in described cascade filtration sedimentation basin group;
The feeder of all filtering settling ponds in described cascade filtration sedimentation basin group is all connected with described secondary transition pond;
The described stillpot of all filtering settling ponds in described three grades of sedimentation basin groups is all connected with described secondary transition pond.
Preferably, also comprise cistern, the feeder of all filtering settling ponds in described three grades of sedimentation basin groups is all connected with described cistern; Set up cistern to recycle the water obtained, turn waste into wealth, recycle.Such as rinse particulate filter by the water in following structure cistern:
Described cistern is connected by the flushing pipe of high-pressure pump with all described filtering settling ponds, and the flushing pipe of each described filtering settling pond is connected with described high-pressure pump by check valve.
Open high-pressure pump and check valve, i.e. the water of available recovery rinses the particulate filter in corresponding filtering settling pond.
Preferably, also comprise three grades of transition ponds, the stillpot of all filtering settling ponds in described cascade filtration sedimentation basin group is all connected with described three grades of transition ponds.
If filter the pulp-water obtained in three grades of sedimentation basin groups when still cannot reach the requirement of recycling, then this pulp-water can be collected three grades of transition ponds, then return in three grades of sedimentation basin groups and filter, until pulp-water meets the requirement of recycling.
A kind of tailing dry discharge method, comprises the following steps:
Steps A: Tailings Slurry is passed into pond, makes the central authorities of Tailings Slurry in pond precipitate, make simultaneously Tailings Slurry from the side in pond with horizontal direction by the first filter screen, the ore pulp once filtered;
Step B: the ore pulp once filtered described in making successively by particulate filter and the second filter screen, obtains pulp-water with direction vertically downward;
Step C: collect described pulp-water;
Wherein, described steps A and described step B carry out simultaneously.
In said method, achieve twice filter process by precipitation and horizontal filtering, then achieve other twice filtration by the absorption of particulate filter with the vertical filtration of the second filter screen, visible whole process has been carried out four times and has been filtered, abundant dehydration is carried out to Tailings Slurry, has improve dehydration rate.In addition, because steps A and step B carry out simultaneously, therefore four filtrations can be carried out simultaneously, and ensure that the continuity of dehydration, therefore, the treating capacity of the method is large.Visible, precipitation and filtration organically combine by said method, improve dehydration rate, and do not need heavy mechanical equipment, and technique is simple, saves a large amount of costs.
In addition, above-mentioned tailing dry discharge method also can be used for the Tailings Slurry processing Ultra-fine.
Preferably, also comprise at described step C: make described one-level pulp-water repeating said steps A, B, C, and after the aperture of the described steps A of carrying out and described step B all filter screens used be less than the aperture of the described steps A of formerly carrying out and described step B all filter screens used.
Through above twice repetition, the particle in Tailings Slurry is carried out the descending filtration of particle diameter, not only increased dewatering efficiency, and promoted the cleanliness factor of the pulp-water collected, to recycle.
Preferably, also comprise after described step C:
Step D: with particulate filter described in high pressure water washing, the benign cycle that this step achieves particulate filter uses.
Compared with prior art, the beneficial effects of the utility model are:
(1) dry-discharge system for tailings has that structure is simple, easy to operate concurrently, process range is wide, low cost and other advantages.
(2) dry-discharge system for tailings and method applied widely, may be used for the Tailings Slurry processing various particle diameter and various concentration.
(3) the work continuity of dry-discharge system for tailings and method and circulation degree high, operating efficiency is high, can save a large amount of energy consumptions, more caters to environmental protection production theory.
Accompanying drawing explanation
In order to be illustrated more clearly in the utility model embodiment or technical scheme of the prior art, be briefly described to the accompanying drawing used required in embodiment or description of the prior art below.
The sectional view of the dry-discharge system for tailings that Fig. 1 provides for the utility model embodiment 1;
The sectional view of the dry-discharge system for tailings that Fig. 2 provides for the utility model embodiment 2;
The sectional view of the dry-discharge system for tailings that Fig. 3 provides for the utility model embodiment 4;
The top view of the dry-discharge system for tailings that Fig. 4 provides for the utility model embodiment 4;
The schematic diagram of the dry-discharge system for tailings that Fig. 5 provides for the utility model embodiment 5.
Detailed description of the invention
Below in conjunction with embodiment, embodiment of the present utility model is described in detail, but it will be understood to those of skill in the art that the following example only for illustration of the utility model, and should not be considered as limiting scope of the present utility model.Unreceipted actual conditions person in embodiment, the condition of conveniently conditioned disjunction manufacturer suggestion is carried out.Agents useful for same or the unreceipted production firm person of instrument, be and can buy by commercially available the conventional products obtained.
Embodiment 1
A kind of dry-discharge system for tailings, comprise filtering settling pond, as shown in Figure 1, described filtering settling pond comprises:
At the bottom of pond 1 and be centered around the side direction filter screen 2 at 1 edge at the bottom of described pond, described side direction filter screen 2 connects into stillpot 3 with described side direction filter screen 2;
First abutment wall 4 and the second abutment wall 5, described first abutment wall 4 and described second abutment wall 5 are all centered around the outside of described stillpot 3, and described first abutment wall 4 is centered around the outside of described second abutment wall 5;
Connect the lower screen 6 of described first abutment wall 4 and described second abutment wall 5, the horizontal plane of described lower screen 6 flushes the horizontal plane of at the bottom of described pond 1; At the bottom of described first abutment wall 4, described lower screen 6, described second abutment wall 5, described pond 1 and described side direction filter screen 2 surround into annular space, be filled with quartz sand filter media 7 in described annular space;
Be arranged on the feeder 8 of the below of described lower screen 6.
The direction of arrow in Fig. 1 refers to the flow direction of fluid (Tailings Slurry etc.).
Embodiment 2
A kind of dry-discharge system for tailings, comprise filtering settling pond, as shown in Figure 2, described filtering settling pond comprises:
At the bottom of pond 1 and be centered around the side direction filter screen 2 at 1 edge at the bottom of described pond, described side direction filter screen 2 connects into stillpot 3 with described side direction filter screen 2;
First abutment wall 4 and the second abutment wall 5, described first abutment wall 4 and described second abutment wall 5 are all centered around the outside of described stillpot 3, and described first abutment wall 4 is centered around the outside of described second abutment wall 5; Distance between described second abutment wall 5 and described first abutment wall 4 equals the distance between described side direction filter screen 2 and described first abutment wall 4.
Connect the lower screen 6 of described first abutment wall 4 and described second abutment wall 5, the horizontal plane of described lower screen 6 lower than at the bottom of described pond 1 horizontal plane; At the bottom of described first abutment wall 4, described lower screen 6, described second abutment wall 5, described pond 1 and described side direction filter screen 2 surround into annular space, be filled with quartz sand filter media 7 in described annular space;
Be arranged on the feeder 8 of the below of described lower screen 6.
The direction of arrow in Fig. 2 refers to the flow direction of fluid (Tailings Slurry etc.).
Embodiment 3
A kind of dry-discharge system for tailings, comprise filtering settling pond, as shown in Figure 3, described filtering settling pond comprises:
At the bottom of pond 1 and be centered around the side direction filter screen 2 at 1 edge at the bottom of described pond, described side direction filter screen 2 connects into stillpot 3 with described side direction filter screen 2;
First abutment wall 4 and the second abutment wall 5, described first abutment wall 4 and described second abutment wall 5 are all centered around the outside of described stillpot 3, and described first abutment wall 4 is centered around the outside of described second abutment wall 5; Distance between described second abutment wall 5 and described first abutment wall 4 is greater than the distance between described side direction filter screen 2 and described first abutment wall 4.
Connect the lower screen 6 of described first abutment wall 4 and described second abutment wall 5, the horizontal plane of described lower screen 6 lower than at the bottom of described pond 1 horizontal plane; At the bottom of described first abutment wall 4, described lower screen 6, described second abutment wall 5, described pond 1 and described side direction filter screen 2 surround into annular space, be filled with quartz sand filter media 7 in described annular space;
Be arranged on the feeder 8 of the below of described lower screen 6.
Embodiment 4
A kind of dry-discharge system for tailings, comprise filtering settling pond, as shown in Figure 3-4, described filtering settling pond comprises:
At the bottom of pond 1 and be centered around the side direction filter screen 2 at 1 edge at the bottom of described pond, described side direction filter screen 2 connects into stillpot 3 with described side direction filter screen 2; Described stillpot 3 is provided with clean-out door 10.
First abutment wall 4 and the second abutment wall 5, described first abutment wall 4 and described second abutment wall 5 are all centered around the outside of described stillpot 3, and described first abutment wall 4 is centered around the outside of described second abutment wall 5; Distance between described second abutment wall 5 and described first abutment wall 4 is greater than the distance between described side direction filter screen 2 and described first abutment wall 4.
Connect the lower screen 6 of described first abutment wall 4 and described second abutment wall 5, the horizontal plane of described lower screen 6 lower than at the bottom of described pond 1 horizontal plane; At the bottom of described first abutment wall 4, described lower screen 6, described second abutment wall 5, described pond 1 and described side direction filter screen 2 surround into annular space, be filled with quartz sand filter media 7 in described annular space; Flushing pipe 9 is provided with in described particulate filter 7.
Be arranged on the feeder of the below of described lower screen 6, this feeder is trench.
In addition, above-mentioned dry heat-extraction system can also arrange a Tailings Slurry injection pump 12.
Embodiment 5
A kind of dry-discharge system for tailings, as in Figure 3-5, comprise seven filtering settling ponds, these seven filtering settling ponds all adopt the structure of embodiment 4, and be divided into three groups, be respectively: single filter sedimentation basin group 13, cascade filtration sedimentation basin group 15, three-stage filtration sedimentation basin group 17, quantity is respectively: 3,2,2.In above group, the aperture of all filter screens of the filtering settling pond in described cascade filtration sedimentation basin group 15 is less than the aperture of all filter screens of the filtering settling pond in described single filter sedimentation basin group 13; The aperture of all filter screens of the filtering settling pond in described three grades of sedimentation basin groups is less than the aperture of all filter screens of the filtering settling pond in described cascade filtration sedimentation basin group 15.
Annexation between these ponds is as follows:
Arrange one-level transition pond 14, the feeder 8 of all filtering settling ponds in described single filter sedimentation basin group 13 is all connected with described one-level transition pond 14; The described stillpot 3 of all filtering settling ponds in described cascade filtration sedimentation basin group 15 is all connected with described one-level transition pond 14.
Arrange secondary transition pond 16, the feeder 8 of all filtering settling ponds in described cascade filtration sedimentation basin group 15 is all connected with described secondary transition pond 16; The described stillpot 3 of all filtering settling ponds in described three grades of sedimentation basin groups is all connected with described secondary transition pond 16.
Arrange cistern 21, the feeder 8 of all filtering settling ponds in described three grades of sedimentation basin groups is all connected with described cistern 21; Described cistern 21 is connected by the flushing pipe 9 of high-pressure pump 20 with all described filtering settling ponds, and the flushing pipe 9 of each described filtering settling pond is connected with described high-pressure pump 20 by check valve 11.
Arrange three grades of transition ponds 18, the stillpot 3 of all filtering settling ponds in described cascade filtration sedimentation basin group 15 is all connected with described three grades of transition ponds 18.
The Tailings Slurry injection pump 12 in all ponds is connected in long-pending pond 19 temporarily with Tailings Slurry.
Embodiment 6
A kind of tailing dry discharge method, comprises the following steps:
The first step: Tailings Slurry is passed into pond, makes the central authorities of Tailings Slurry in pond precipitate, make simultaneously Tailings Slurry from the side in pond with horizontal direction by the first filter screen, the ore pulp once filtered.
Second step: the ore pulp once filtered described in making successively by particulate filter and the second filter screen, obtains pulp-water with direction vertically downward; This step must be carried out with the first step simultaneously.
3rd step: collect final pulp-water.
The method realizes by any one dry-discharge system for tailings of above-described embodiment 1-4.
Embodiment 7
A kind of tailing dry discharge method, comprises the following steps:
The first step: Tailings Slurry is passed into first order pond, makes the central authorities of Tailings Slurry in pond precipitate, make simultaneously Tailings Slurry from the side in pond with horizontal direction by the first filter screen, obtain filter ore pulp.
Second step: the ore pulp that the first step is filtered successively by particulate filter and the second filter screen, collects the one-level pulp-water obtained with direction vertically downward; This step must be carried out with the first step simultaneously.
3rd step: one-level pulp-water is passed into pond, the second level, makes the central authorities of pulp-water in pond precipitate, make simultaneously one-level pulp-water from the side in pond with horizontal direction by the 3rd filter screen, obtain filter ore pulp.
4th step: the ore pulp that the 3rd step is filtered successively by particulate filter and the 4th filter screen, collects the secondary pulp-water obtained with direction vertically downward; This step must be carried out with the 3rd step simultaneously.
The aperture of above 3rd filter screen and the 4th filter screen is all less than the aperture of the first filter screen and the second filter screen.
If the water clarification degree of secondary pulp-water reaches the requirement of recycling, then complete dryly being drained through journey; If the water clarification degree of secondary pulp-water can't reach the requirement of recycling, then continue the filter process repeating the first step and second step, until clarity reaches requirement, and often repeat once, the aperture of filter screen just reduces a rank, and the degree of reduction is selected according to the particle diameter of particle in ore pulp.In above method, after the particulate filter in each pond completes adsorption filtration, need high pressure water washing be used, so that particulate filter recycles.
Above method realizes by any dry heat-extraction system of embodiment 3-5.
For further illustrating technique effect of the present utility model, the following provide concrete test example.
Test example 1
This test adopts the equipment of embodiment 1 and the method for embodiment 6.
Handled mine tailing character: mine tailing is Liu Gangtun autumn iron ore magnetic iron ore mine tailing, and pulp density is 25%, and granularity is that 200 object particles account for 85%, and clay content is 0.5%.
Result: mine tailing water content is 19%, reaches dry row's standard.
Test example 2
The result of this test to the utility model and prior art contrasts.Mine tailing character handled by two groups is identical.
The utility model group
Adopt the equipment of embodiment 5 and the method for embodiment 7.
Handled mine tailing character: mine tailing is Liu Gangtun autumn iron ore magnetic iron ore mine tailing, and pulp density is 25%, and granularity-200 order particle accounts for 85%, and clay content is 0.5%, and the total treating capacity of mine tailing is 100 tons.
Result:
The total treating capacity of ore pulp is about 400 tons, enters treatment pond with the speed of 50 tons/hour, and eight hourly workers do complete, and before scarfing cinder, mine tailing water content is 18%, reaches dry row's standard.This test drops into construction fund 300,000 yuan altogether, process ore pulp 400 tons, the electricity charge 180 yuan, labour cost 150 yuan (administrative staff one).
Prior art group
What Liu Gang collectd that autumn iron ore adopts is " cyclone+dense device+dewatering screen " technique, under treating capacity and this experiment same case, and construction investment need 700,000 yuan, the electricity charge 1000 yuan, labour cost 450 yuan (at least needing 3 workmans), mine tailing water content is 17%, reaches dry row's standard.
To sum up, the cost of the dry ore discharge slurry of the utility model significantly reduces.
Test example 3
The data of ultra-fine mine tailing
This test have employed the equipment of embodiment 5 and the method for embodiment 7., mine tailing is aluminium manufacturer of Guangxi pingguo bauxite tail mud, and granularity is-200 order about 40%, 300 order ~ 450 orders about 60%, and pulp density 20%, clay content is 1.6%.Clean water quality in work, can fully recycle, the mine tailing of 90% is piled up in scarfing cinder previous stage pond, water content is 20.8%, piles up 8% mine tailing in secondary pond, and water content is 22.2%, 2% mine tailing is piled up in three grades of ponds, water content is 24.9%, and mine tailing average moisture content is 23.6, can reach dry row's standard.
Although illustrate and describe the utility model with specific embodiment, however it will be appreciated that can to make when not deviating from spirit and scope of the present utility model many other change and amendment.Therefore, this means to comprise all such changes and modifications belonged within the scope of the utility model in the following claims.
Claims (10)
1. a dry-discharge system for tailings, is characterized in that, comprises filtering settling pond, and described filtering settling pond comprises:
With the side direction filter screen being centered around described pond feather edge at the bottom of pond, described side direction filter screen and described side direction filter screen connect into stillpot;
First abutment wall and the second abutment wall, described first abutment wall and described second abutment wall are all centered around the outside of described stillpot, and described first abutment wall is centered around the outside of described second abutment wall;
Connect the lower screen of described first abutment wall and described second abutment wall, the horizontal plane of described lower screen lower than or the horizontal plane that flushes at the bottom of described pond; At the bottom of described first abutment wall, described lower screen, described second abutment wall, described pond and described side direction filter screen surround into annular space, be filled with particulate filter in described annular space;
Be arranged on the feeder of the below of described lower screen.
2. dry-discharge system for tailings according to claim 1, it is characterized in that, the horizontal plane of described lower screen is lower than the horizontal plane at the bottom of described pond, and the distance between described second abutment wall and described first abutment wall is greater than the distance between described side direction filter screen and described first abutment wall.
3. dry-discharge system for tailings according to claim 1, is characterized in that, is provided with flushing pipe in described particulate filter.
4. dry-discharge system for tailings according to claim 1, is characterized in that, described stillpot is provided with clean-out door.
5. dry-discharge system for tailings according to claim 1, is characterized in that, described particulate filter is quartz sand filter media.
6. dry-discharge system for tailings according to claim 1, is characterized in that, described feeder is trench.
7. dry-discharge system for tailings according to claim 1, is characterized in that, comprises multiple described filtering settling pond, also comprises one-level transition pond, and described multiple filtering settling pond is divided into following two groups: single filter sedimentation basin group and cascade filtration sedimentation basin group;
The aperture of all filter screens of the filtering settling pond in described cascade filtration sedimentation basin group is less than the aperture of all filter screens of the filtering settling pond in described single filter sedimentation basin group;
The feeder of all filtering settling ponds in described single filter sedimentation basin group is all connected with described one-level transition pond;
The described stillpot of all filtering settling ponds in described cascade filtration sedimentation basin group is all connected with described one-level transition pond.
8. dry-discharge system for tailings according to claim 7, is characterized in that, also comprises three-stage filtration sedimentation basin group and secondary transition pond, and described three-stage filtration sedimentation basin group is made up of one or more described filtering settling pond;
The aperture of all filter screens of the filtering settling pond in described three grades of sedimentation basin groups is less than the aperture of all filter screens of the filtering settling pond in described cascade filtration sedimentation basin group;
The feeder of all filtering settling ponds in described cascade filtration sedimentation basin group is all connected with described secondary transition pond;
The described stillpot of all filtering settling ponds in described three grades of sedimentation basin groups is all connected with described secondary transition pond.
9. dry-discharge system for tailings according to claim 8, is characterized in that, also comprises cistern, and the feeder of all filtering settling ponds in described three grades of sedimentation basin groups is all connected with described cistern; Preferably, described cistern is connected by the flushing pipe of high-pressure pump with all described filtering settling ponds, and the flushing pipe of each described filtering settling pond is connected with described high-pressure pump by check valve.
10. dry-discharge system for tailings according to claim 8, is characterized in that, also comprises three grades of transition ponds, and the stillpot of all filtering settling ponds in described cascade filtration sedimentation basin group is all connected with described three grades of transition ponds.
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104722137A (en) * | 2015-03-26 | 2015-06-24 | 屠海东 | Dry discharge system and dry discharge method for tailings |
| CN105689104A (en) * | 2016-02-03 | 2016-06-22 | 山东佳星环保科技有限公司 | Water-saving coal separation method |
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2015
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104722137A (en) * | 2015-03-26 | 2015-06-24 | 屠海东 | Dry discharge system and dry discharge method for tailings |
| CN105689104A (en) * | 2016-02-03 | 2016-06-22 | 山东佳星环保科技有限公司 | Water-saving coal separation method |
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