CN209271417U - It is full-automatic to be separated by solid-liquid separation wash mill - Google Patents
It is full-automatic to be separated by solid-liquid separation wash mill Download PDFInfo
- Publication number
- CN209271417U CN209271417U CN201821643274.2U CN201821643274U CN209271417U CN 209271417 U CN209271417 U CN 209271417U CN 201821643274 U CN201821643274 U CN 201821643274U CN 209271417 U CN209271417 U CN 209271417U
- Authority
- CN
- China
- Prior art keywords
- solid
- full
- charging aperture
- discharging gate
- wash mill
- 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.)
- Active
Links
Abstract
The utility model discloses a kind of full-automatic separation of solid and liquid wash mills, including centrifuge, upper barrel.High-speed dispersing kettle, pump machine and triple valve, upper barrel includes cylinder, drain hole and feeding inlet, centrifuge is provided with feed nozzle, the first discharging gate and the second discharging gate for waste discharge, high-speed dispersing kettle and is provided with first charging aperture, second charging aperture and discharge port；Drain hole is connected to feed nozzle；First discharging gate is connected to first charging aperture, and the second discharging gate is connected to external water source, and discharge port and external feed pipeline are respectively communicated with the import of triple valve, and the other end of one end of the outlet pump machine of triple valve, pump machine is connected to feeding inlet.The full-automatic separation of solid and liquid wash mill of the utility model, has the advantages that washing effect is good and structure is simple.
Description
Technical field
The utility model relates to a kind of separation of solid and liquid wash mills, more particularly to a kind of full-automatic be separated by solid-liquid separation to wash dress
It sets.
Background technique
In industrial processes, it is often necessary to be separated by solid-liquid separation using some equipment to the slurries handled well, first
After the separation of solid and liquid of step, it is also necessary to there is subsequent workshop section to wash solid portion.
Currently, bigger separation and washing settling groove is widely used industrially to separate overflow and bottom after being settled
Stream, then underflow is washed.For washing twice: needing that the slurries of separation of solid and liquid are first sent into separating tank, isolate
Overflow is seen off after entering next separating tank with flood pump, and underflow pump is then passed through in underflow, mixes with the overflow of final stage subsider
Enter next sink afterwards, the overflow of sink is once washing overflow, then sees off, returns by flood pump into overflow launder
The journey that flows back uses, and underflow then enters final stage subsider after underflow pump is mixed with slurry, and what is come out from final stage subsider overflows
Stream enters overflow launder, then sends to the underflow come out with aforementioned underflow pump with flood pump and has been mixed into subsider above-mentioned (preceding
Refer to), using this kind of process, running and comparing is stablized, but the separating tank that each procedure needs is bulky, even if using high
Imitate subsider, diameter be also it is very big, it is high so as to cause investment, take up a large area.
Utility model content
The technical problem to be solved by the utility model is to provide a kind of washing effect, good and structure is simply automatically solid
Liquid separating, washing device.
The utility model is realized through the following technical scheme:
A kind of full-automatic separation of solid and liquid wash mill, including centrifuge, upper barrel, high-speed dispersing kettle, pump machine and threeway
Valve, upper barrel include cylinder, drain hole and feeding inlet, and centrifuge is provided with feed nozzle, the first discharging gate, water inlet and use
In the second discharging gate of waste discharge, high-speed dispersing kettle is provided with first charging aperture, second charging aperture and discharge port；Drain hole
It is connected to feed nozzle；First discharging gate is provided with switching valve in order to select connection outside or first charging aperture, the second discharging gate
It is connected to external water source, discharge port and external feed pipeline are respectively communicated with the import of triple valve, the outlet pump machine of triple valve
The other end of one end, pump machine is connected to feeding inlet.
Preferably, centrifuge is horizontal centrifuge.
Preferably, drain hole setting is arranged at the top of cylinder in cylinder body bottom, feeding inlet.
Preferably, the second discharging gate is connected with wastewater treatment equipment.
Preferably, the top of high-speed dispersing kettle is arranged in first charging aperture, and high-speed dispersing kettle is arranged in second charging aperture
The bottom of high-speed dispersing kettle is arranged in top, discharge port.
Preferably, the first discharging gate is connected to first charging aperture by flowmeter.
Preferably, second charging aperture is connected to external water source by flow pump.
Beneficial effect is:
Compared with prior art, the full-automatic separation of solid and liquid wash mill of the utility model passes through design centrifuge, feeding
The product being tentatively separated by solid-liquid separation in centrifuge is sent into high-speed dispersing kettle and is mixed by cylinder, high-speed dispersing kettle, pump machine and triple valve
It closes clean clear water and continues agitator treating, then the product of primary wash is sent by upper barrel by pump machine, the product of upper barrel is again
Secondary feeding centrifuge is separated by solid-liquid separation, and the water with impurity is discharged from the second discharging gate, product is fed again into high-speed dispersing kettle
Cleaning stirring, reciprocation cycle, so that washing effect is good；In addition, circulation washing be so that equipment need not prepare multiple separating tanks, and
Pump machine is separately connected the discharge port of external feed pipeline and high-speed dispersing kettle by triple valve, so that external charging is recycled with internal
Material is washed using a pump machine, pipeline is simplified, so that structure is simple.
Detailed description of the invention
Specific embodiment of the present utility model is described in further detail below in conjunction with attached drawing, in which:
Fig. 1 is the full-automatic separation of solid and liquid wash mill structural schematic diagram of the utility model.
Specific embodiment
Be separated by solid-liquid separation wash mill as shown in Figure 1, a kind of full-automatic, including centrifuge 1, upper barrel 2, high-speed dispersing kettle 3,
Pump machine 4 and triple valve 5, upper barrel 2 include cylinder 21, drain hole 22 and feeding inlet 23, and centrifuge 1 is provided with feed nozzle
11, for discharging the first discharging gate 12 of the solid product of moisture content, water inlet 14 and for the second discharging of waste discharge
Mouth 13, water inlet 14 connect external water source (not marking in figure) and are used to provide moisture cleaning in centrifuge separation or set
Cleaning inside is provided when standby maintenance, high-speed dispersing kettle 3 is provided with first charging aperture 31, second charging aperture 32 and discharge port 33；
Drain hole 22 is connected to feed nozzle 11 and is separated by solid-liquid separation for continuing feeding to centrifuge 1；First discharging gate 12 is provided with steering
Valve 121 is aqueous when the first discharging gate 12 is connected to first charging aperture 31 in order to select connection external or first charging aperture 31
Solid product is divided to be sent into high-speed dispersing kettle 3, the second discharging gate 13 is connected to external water source (not marking in figure), in the process of stirring
In, be passed through clean clear water and play washing effect, after washing, discharge port 33 by pump machine 4 by water-containing products be transported into
In material mouth 23, product to be separated by solid-liquid separation is obtained in upper barrel 2, is sent into product to be separated by solid-liquid separation again by emptying nozzle 22
It being stirred in centrifuge 1, whole process circulation carries out, so that washing effect is good, and is not necessarily to excessive centrifuge or separating tank, knot
Structure is simple；When washing, which finishes, to be needed to discharge, outside the first discharging gate 12 is connected under the course changing control of switching valve 121, discharge
Product；Discharge port 33 and external feed pipeline 51 can be respectively communicated with the import (not marking in figure) of triple valve 5, and triple valve 5 goes out
One end of mouthful (not marking in figure) connection pump machine 4, the other end of pump machine 4 are connected to feeding inlet 23, and the feeding of outside manufacture can also be with
It is pumped by pump machine 4 into upper barrel 2, is carried out by triple valve 5 so that operation, structure can be completed without multiple pump machines 4
It is simple and at low cost.
Preferable embodiment, centrifuge 1 are horizontal centrifuge, and centrifugal effect is good and can be convenient centrifuge 1 is steady
Solid setting on rack (not marked in figure).
Preferable embodiment, in 21 bottom of cylinder, feeding inlet 23 is arranged at 21 top of cylinder the setting of drain hole 22, so that
Structure is simple, and product, which can use self weight and flow into, need not be arranged pump in centrifuge 1.
Preferable embodiment, as shown in Figure 1, the second discharging gate 13 is connected with wastewater treatment equipment 6, the waste water of discharge is first
It is discharged again after the processing of wastewater treatment equipment 6, so that production process is environmentally friendly.
The top of high-speed dispersing kettle 3 is arranged in preferable embodiment, first charging aperture 31, and the setting of second charging aperture 32 exists
The top of high-speed dispersing kettle 3, the bottom of high-speed dispersing kettle 3 is arranged in discharge port 33, so that structure is simple, product be can use certainly
Density current enters need not setting pump in centrifuge 1.
Preferable embodiment, as shown in Figure 1, the first discharging gate 12 is connected to first charging aperture 31 by flowmeter 7, it is convenient
The revolving speed of high-speed dispersing kettle 3 and the purge rate of pump machine 4 are adjusted according to uninterrupted, so that production process is more steady.And
And second charging aperture 32 can be connected to external water source by flow pump 8, control the water being sent into high-speed dispersing kettle 3, really
Protect cleaning efficiency.
Above embodiments are only to illustrate the technical solution of the utility model and are not intended to limit it, all without departing from this
Any modification of utility model spirit and scope or equivalent replacement should all cover the range in technical solutions of the utility model
It is interior.
Claims (7)
1. a kind of full-automatic separation of solid and liquid wash mill, it is characterised in that: including centrifuge (1), upper barrel (2), high speed dispersion
Kettle (3), pump machine (4) and triple valve (5), the upper barrel (2) include cylinder (21), drain hole (22) and feeding inlet
(23), the centrifuge (1) be provided with feed nozzle (11), the first discharging gate (12), connect external water source water inlet (14) with
And the second discharging gate (13) for waste discharge, the high-speed dispersing kettle (3) are provided with first charging aperture (31), the second charging
Mouth (32) and discharge port (33)；The drain hole (22) is connected to the feed nozzle (11)；First discharging gate (12) setting
There is switching valve (121) to select connection external or the first charging aperture (31), the second discharging gate (13) connection is outer
Portion water source, the discharge port (33) are respectively communicated with the import of the triple valve (5), the triple valve with external feed pipeline (51)
(5) other end of one end of pump machine described in outlet (4), the pump machine (4) is connected to the feeding inlet (23).
2. full-automatic separation of solid and liquid wash mill according to claim 1, it is characterised in that: the centrifuge (1) is sleeping
Formula centrifuge.
3. full-automatic separation of solid and liquid wash mill according to claim 1 or 2, it is characterised in that: the drain hole (22)
Setting is in the cylinder (21) bottom, and feeding inlet (23) setting is at the top of the cylinder (21).
4. full-automatic separation of solid and liquid wash mill according to claim 1 or 2, it is characterised in that: second discharging gate
(13) wastewater treatment equipment (6) are connected with.
5. full-automatic separation of solid and liquid wash mill according to claim 1 or 2, it is characterised in that: the first charging aperture
(31) setting is arranged at the top of the high-speed dispersing kettle (3), the second charging aperture (32) in the high-speed dispersing kettle (3)
Top, bottom of discharge port (33) setting in the high-speed dispersing kettle (3).
6. full-automatic separation of solid and liquid wash mill according to claim 1 or 2, it is characterised in that: first discharging gate
(12) first charging aperture (31) is connected to by flowmeter (7).
7. full-automatic separation of solid and liquid wash mill according to claim 1 or 2, it is characterised in that: the second charging aperture
(32) external water source is connected to by flow pump (8).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821643274.2U CN209271417U (en) | 2018-10-10 | 2018-10-10 | It is full-automatic to be separated by solid-liquid separation wash mill |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821643274.2U CN209271417U (en) | 2018-10-10 | 2018-10-10 | It is full-automatic to be separated by solid-liquid separation wash mill |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN209271417U true CN209271417U (en) | 2019-08-20 |
Family
ID=67604445
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201821643274.2U Active CN209271417U (en) | 2018-10-10 | 2018-10-10 | It is full-automatic to be separated by solid-liquid separation wash mill |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN209271417U (en) |
-
2018
- 2018-10-10 CN CN201821643274.2U patent/CN209271417U/en active Active
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN204523203U (en) | A kind of ore cleaning device | |
| CN204380572U (en) | A kind of liquid backflow agitating device | |
| CN204159333U (en) | A kind of water pump type still external circulating device | |
| CN108392858A (en) | A kind of thickener | |
| CN209271417U (en) | It is full-automatic to be separated by solid-liquid separation wash mill | |
| CN107572747B (en) | Red mud treatment process and treatment system in alumina production | |
| CN201342369Y (en) | Continuous overflow classifier | |
| CN205236188U (en) | New and effective carbon removal device of carborundum miropowder | |
| CN201292327Y (en) | Apparatus for separating corn plasmogen starch and protein | |
| CN209426229U (en) | A kind of fruit peel scum juice liquid recyclable device | |
| CN206494882U (en) | A kind of device of the separating starch from plumule | |
| CN202951667U (en) | Wood chip washing production line | |
| CN210045654U (en) | A crystallization rinsing spray set for preparing high-purity β -aminopropionic acid | |
| CN205435109U (en) | Adhesive waste liquid filters recovery unit | |
| CN208727303U (en) | A kind of mixing plant for sewage treatment | |
| CN207435184U (en) | A kind of waste water and dregs processing system of concrete mixing plant | |
| CN111420452A (en) | Cuprous cyanide washing and separating equipment and cuprous cyanide washing and separating method | |
| CN207243884U (en) | Biological enzyme purification and separation device | |
| CN206229365U (en) | Rosin resin washes oxidation reaction apparatus | |
| CN110552228A (en) | Paper pulp impurity separator for paper plastic of inner package of environment-friendly navigator and preparation process thereof | |
| CN205391910U (en) | Belt vacuum filter pan feeding whirl device | |
| CN205761154U (en) | Humate response system device | |
| CN206101476U (en) | Soybean soaking system | |
| CN205398130U (en) | Carbide slag preparation industry naoh reaction unit | |
| CN204841063U (en) | Hierarchical concentrated machine of tailing pulp material |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CP01 | Change in the name or title of a patent holder |
Address after: 410600 Xinkang Road, Ningxiang Economic and Technological Development Zone, Changsha City, Hunan Province Patentee after: Hunan Yacheng New Energy Co.,Ltd. Address before: 410600 Xinkang Road, Ningxiang Economic and Technological Development Zone, Changsha City, Hunan Province Patentee before: HUNAN YACHENG NEW MATERIAL CO.,LTD. |
|
| CP01 | Change in the name or title of a patent holder |