CN205516666U - Tailing separator - Google Patents
Tailing separator Download PDFInfo
- Publication number
- CN205516666U CN205516666U CN201620113831.4U CN201620113831U CN205516666U CN 205516666 U CN205516666 U CN 205516666U CN 201620113831 U CN201620113831 U CN 201620113831U CN 205516666 U CN205516666 U CN 205516666U
- Authority
- CN
- China
- Prior art keywords
- valve
- liquid
- tailing
- mine tailing
- precipitation bucket
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
- 239000007788 liquid Substances 0.000 claims abstract description 37
- 239000000463 material Substances 0.000 claims abstract description 4
- 230000000740 bleeding effect Effects 0.000 claims description 7
- 230000005484 gravity Effects 0.000 claims description 4
- 238000000926 separation method Methods 0.000 abstract description 10
- 238000001556 precipitation Methods 0.000 abstract description 8
- 238000012423 maintenance Methods 0.000 abstract description 2
- 238000000034 method Methods 0.000 abstract description 2
- 239000007787 solid Substances 0.000 abstract 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000002244 precipitate Substances 0.000 description 2
- 238000012271 agricultural production Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 239000000706 filtrate Substances 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 238000005381 potential energy Methods 0.000 description 1
- 239000011435 rock Substances 0.000 description 1
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- Jet Pumps And Other Pumps (AREA)
Abstract
The utility model discloses tailing separator belongs to tailing separation technical field, mainly solves need filter material and back flush that prior art realized the solid -liquid separation existence, and the consumptive material is many, and the maintenance cost is big, the poor problem of work efficiency. Including precipitation bucket and vertical setting of types pipe, precipitation bucket is located the support, and its characteristics are: precipitation bucket upper portion is provided with feed inlet and gas vent, and the tailing input tube is penetrated to the precipitation bucket middle part by the feed inlet, and is provided with the feed valve on the tailing input tube, and gas vent department is provided with discharge valve, being close the lateral wall at top, precipitation bucket be provided with liquid tailing outlet port on, vertical setting of types pipe one end and the switch -on of liquid tailing outlet port, the other end is connected with the liquid valve, precipitation bucket's lower part is provided with futilely the valve. The size of correction liquor valve, dry valve and feed valve make the negative pressure in the precipitation bucket be fit for the row of doing emission standard can, disengaging process is continuous, convenient to use, solid -liquid separation is efficient.
Description
Technical field
This utility model belongs to mine tailing separation technology field, is specifically related to mine tailing separator.
Background technology
Tailings Dam is the dangerous matter sources of an artificial mud-rock flow with high potential energy.The most tens of up to more than ten years
Year period in, various naturally (rainwater, earthquake, rat holes etc.) and artificial (mismanagement etc.) no
Profit factor at every moment or periodically threatens its safety.The fact shows again and again, and Tailings Dam once has an accident,
Huge disaster and loss will be caused to industrial and agricultural production and downstream people's lives and properties.By the liquid in mine tailing
Separate, it is achieved dry last person ore deposit, the degree of danger of Tailings Dam can be substantially reduced.
At present, the solid-liquor separation of prior art mine tailing uses the mode essence filtered be to retain precipitate and allow liquid
The mode that body is slipped away, filters and needs filtrate and backwash, and consumptive material is many, and maintenance cost is big, and work efficiency is poor.
Summary of the invention
This utility model mainly solves the problem that prior art realizes the existence of solid-liquid separation, it is provided that need not
Filter device can directly carry out the efficient mine tailing separator of solid-liquor separation.
This utility model adopts the technical scheme that for solving above-mentioned technical problem:
Mine tailing separator, including settling box and vertical setting of types pipe, described settling box is positioned on support, is characterized in:
Described settling box top is provided with charging aperture and air vent, and mine tailing input pipe is penetrated to settling box by charging aperture
Being provided with inlet valve in portion, and mine tailing input pipe, exhaust ports is provided with air bleeding valve;At settling box close to top
Liquid tailing outlet port it is provided with on the sidewall in portion;Described vertical setting of types pipe one end is connected with liquid tailing outlet port,
The other end is connected with liquid valve;The bottom of described settling box is provided with dry valve.
The length of described vertical setting of types pipe be enough to overcome atmospheric pressure so that it is interior liquid produces gravity flow.
The pump extracting liquid mine tailing out it is provided with on described vertical setting of types pipe.
This utility model compared with prior art, has the advantages that
Owing to this utility model have employed settling box and vertical setting of types pipe, make mine tailing mine tailing input pipe in settling box
Forming the gravity flow of liquid mine tailing to liquid tailing outlet port at Kou, dry row's mouth air pressure upwards promotes precipitation
Moisture in thing solid-state mine tailing moves upward, in the breathability that precipitate solid-state mine tailing has makes solid-state mine tailing
Atmospheric pressure is two-way trends towards balance, naturally drains downwards.Adjust liquid valve, dry valve
And the size of inlet valve makes the negative pressure in settling box be suitable for the discharge standard of dry row, separation process continuously,
Easy to use, solid-liquid separation efficiency is high.
Accompanying drawing explanation
Fig. 1 is this utility model structural representation.
In figure: 1 inlet valve;2 settling boxs;3 mine tailing input pipes;4 solid-state mine tailings;5 supports;
6 dry valves;7 liquid mine tailings;8 air bleeding valves;9 liquid tailing outlet ports;10 vertical setting of types pipes;11
Liquid valve.
Detailed description of the invention
As it is shown in figure 1, mine tailing separator, including settling box 2 and vertical setting of types pipe 10, described settling box 2 is positioned at
On support 5, it is characterized in: described settling box 2 top is provided with charging aperture and air vent, mine tailing input pipe 3
Being penetrated in the middle part of settling box 2 by charging aperture, and be provided with inlet valve 1 on mine tailing input pipe 3, exhaust ports sets
It is equipped with air bleeding valve 8;On the sidewall at top, it is provided with liquid tailing outlet port 9 at settling box 2;Described perpendicular
Comb 10 one end is connected with liquid tailing outlet port 9, and the other end is connected with liquid valve 11;Described settling box 2
Bottom be provided with dry valve 6.
The length of described vertical setting of types pipe 10 be enough to overcome atmospheric pressure so that it is interior liquid produces gravity flow.
The pump extracting liquid mine tailing 7 out it is provided with on described vertical setting of types pipe 10.
Using method: when this utility model enables first, dry valve 6 closes, and air bleeding valve 8 is opened, and liquid is arranged
Valve 11 cuts out, and inlet valve 1 is opened, when settling box 2 is filled, when i.e. air bleeding valve 8 has liquid mine tailing to flow out,
Now, closing air bleeding valve 8, open liquid valve 11 and dry valve 6, inlet valve 1 remains on, heavy
In the bucket of shallow lake under negative pressure state, this utility model enters normal operating conditions, and that discharges at dry valve 6 consolidates
When state mine tailing 4 liquid content is bigger, the dry valve of scalable 6, inlet valve 1 and the size of liquid valve 11, make institute
Row's solid-state mine tailing 4 is up to standard, it is achieved the solid-liquid separation of mine tailing;In the case of vertical setting of types pipe 10 is provided with pump,
Pump can be started carry out discharging liquid mine tailing 7.
Claims (3)
1. mine tailing separator, including settling box (2) and vertical setting of types pipe (10), described settling box (2) is positioned at
On support (5), it is characterized in that: described settling box (2) top is provided with charging aperture and air vent, mine tailing
Input pipe (3) by charging aperture penetrate to settling box (2) middle part, and be provided with on mine tailing input pipe (3) into
Material valve (1), exhaust ports is provided with air bleeding valve (8);Arrange on the sidewall at top at settling box (2)
There is liquid tailing outlet port (9);Described vertical setting of types pipe (10) one end is connected with liquid tailing outlet port (9),
The other end is connected with liquid valve (11);The bottom of described settling box (2) is provided with dry valve (6).
Mine tailing separator the most according to claim 1, is characterized in that: the length of described vertical setting of types pipe (10)
Degree be enough to overcome atmospheric pressure so that it is interior liquid produces gravity flow.
Mine tailing separator the most according to claim 1, is characterized in that: set on described vertical setting of types pipe (10)
It is equipped with the pump extracting liquid mine tailing (7) out.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201620113831.4U CN205516666U (en) | 2016-02-04 | 2016-02-04 | Tailing separator |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201620113831.4U CN205516666U (en) | 2016-02-04 | 2016-02-04 | Tailing separator |
Publications (1)
Publication Number | Publication Date |
---|---|
CN205516666U true CN205516666U (en) | 2016-08-31 |
Family
ID=56776171
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201620113831.4U Expired - Fee Related CN205516666U (en) | 2016-02-04 | 2016-02-04 | Tailing separator |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN205516666U (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN112717482A (en) * | 2020-11-27 | 2021-04-30 | 中国恩菲工程技术有限公司 | A subside device and processing system for zinc electrodeposition anode mud is handled |
-
2016
- 2016-02-04 CN CN201620113831.4U patent/CN205516666U/en not_active Expired - Fee Related
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN112717482A (en) * | 2020-11-27 | 2021-04-30 | 中国恩菲工程技术有限公司 | A subside device and processing system for zinc electrodeposition anode mud is handled |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160831 |