CN218280767U - Solid-liquid static separation device - Google Patents
Solid-liquid static separation device Download PDFInfo
- Publication number
- CN218280767U CN218280767U CN202222175848.0U CN202222175848U CN218280767U CN 218280767 U CN218280767 U CN 218280767U CN 202222175848 U CN202222175848 U CN 202222175848U CN 218280767 U CN218280767 U CN 218280767U
- Authority
- CN
- China
- Prior art keywords
- solid
- liquid
- filter vat
- barrel
- liquid static
- 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
Images
Abstract
The utility model discloses a solid-liquid static separation device belongs to splitter technical field, this solid-liquid static separation device, including separation barrel and bung, the bung is installed the top of separation barrel, the filter vat is still installed to the inside of separation barrel, the position department that the below of separation barrel corresponds the filter vat installs the filter residue valve, the filtrating valve is still installed to the lateral surface of separation barrel, the inlet pipe is installed to the top of bung, the inlet pipe is located directly over the filter vat. Through setting up the filter vat, the filtration pore of filter vat can be through liquid but can not pass through the solid for the solid is whole to be piled up in the inside of filter vat, and liquid overflows into the inside of separation bucket, takes out liquid through filtrating valve 11 earlier, later recycles the filter residue valve and takes out the filter residue, not only conveniently takes out filtrating and filter residue more, the speed of the separation that also accelerates simultaneously.
Description
Technical Field
The utility model belongs to the technical field of splitter, concretely relates to static separator of solid-liquid.
Background
In a large-scale processing factory like food processing, because a production workshop can produce a large amount of liquid and solid mixtures when processing products, in most cases, the produced solid and liquid mixtures can be recycled, and particularly in a large-scale automatic processing factory, the recycling can not only save resources, but also reduce the production cost and bring higher profit.
Most of solid-liquid mixtures generated in large-scale factories adopt a static mode, so that solids are precipitated at the bottom, and then liquid on the surface layer is taken out, however, the mode takes a lot of time, for some mixtures which are easy to oxidize, the quality of secondary use is influenced, and the working efficiency of the static separation mode is too low because the amount of the mixtures is large, so that the static separation mode is not suitable for the existing fast-paced automatic processing factories.
SUMMERY OF THE UTILITY MODEL
An object of the utility model is to provide a solid-liquid static separation device to propose a current solid-liquid static separation device in solving above-mentioned background art in the use, because static mode need spend a large amount of times, thereby to some easy oxidized mixtures, can influence the quality of secondary use, secondly work efficiency is low excessively, is not suitable for the problem of the automated processing mill that now beats fast.
In order to achieve the above object, the utility model provides a following technical scheme: the utility model provides a static separator of solid-liquid, includes separation bucket and bung, the bung is installed the top of separation bucket, the filter vat is still installed to the inside of separation bucket, the below of separation bucket corresponds the position department of filter vat and installs the filter residue valve, the filtrating valve is still installed to the lateral surface of separation bucket, the inlet pipe is installed to the top of bung, the inlet pipe is located directly over the filter vat.
Preferably, the inner diameter of the feeding pipe is smaller than that of the filter vat.
Preferably, the lower end of the feed pipe extends to the inside of the filter vat.
Preferably, a vacuum valve is installed above the barrel cover, a vacuum pipe is installed on the surface of the vacuum valve, and one end of the vacuum pipe extends into the separation barrel.
Preferably, the dispersion board is installed through the installation pole in the inside of filter vat, the weeping hole has been seted up on the surface of dispersion board.
Preferably, the mounting rod is a round rod shaped like an "L".
Preferably, the number of the mounting rods and the dispersion plates is two, and the liquid leakage holes in the two dispersion plates are staggered.
Preferably, the size of the liquid leakage hole is smaller than the size of the filtering hole of the filtering barrel.
Preferably, the dispersion plate has an umbrella shape with an arc-shaped upper surface.
Preferably, the distance from the center to the edge of the dispersion plate is smaller than the inner diameter of the filter vat.
Compared with the prior art, the beneficial effects of the utility model are that:
1. through setting up the filter vat, the filtration pore of filter vat can be through liquid but can not pass through the solid for the solid is whole to be piled up in the inside of filter vat, and liquid is gone into the inside of separation bucket, takes out liquid through filtrating valve 11 earlier, and later recycle filter residue valve takes out the filter residue, not only conveniently takes out filtrating and filter residue more, the speed of the separation that also accelerates simultaneously.
2. Through utilizing vacuum valve and vacuum tube to absorb the inside air of separation barrel totally, not only can slow down the oxidation time of mixture, can accelerate the mixture simultaneously and flow into the inside time of separation barrel, improve the efficiency of work, it is exactly that the inside atmospheric pressure of separation barrel is little, and outside atmospheric pressure gives mixture atmospheric pressure, has got into speed as early as possible.
Drawings
Fig. 1 is a schematic view of the overall structure of the present invention;
fig. 2 is a schematic bottom view of the present invention;
FIG. 3 is a schematic side view of the present invention;
fig. 4 is a schematic sectional view of the position a of fig. 3 according to the present invention.
In the figure: 1. a separation barrel; 2. a barrel cover; 3. a filter vat; 4. a residue filtering valve; 5. a feed pipe; 6. a vacuum valve; 7. a vacuum tube; 8. mounting a rod; 9. a dispersion plate; 10. a weep hole; 11. and (4) a filtrate valve.
Detailed Description
The technical solutions in the embodiments of the present invention will be described clearly and completely with reference to the accompanying drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only some embodiments of the present invention, not all embodiments. Based on the embodiments in the present invention, all other embodiments obtained by a person skilled in the art without creative work belong to the protection scope of the present invention.
Referring to fig. 1-4, the present invention provides a technical solution: the utility model provides a static separator of solid-liquid, includes separation barrel 1 and bung 2, bung 2 is installed the top of separation barrel 1, filter vat 3 is still installed to the inside of separation barrel 1, the position department that the below of separation barrel 1 corresponds filter vat 3 installs filter residue valve 4, filtrate valve 11 is still installed to the lateral surface of separation barrel 1, inlet pipe 5 is installed to the top of bung 2, inlet pipe 5 is located directly over filter vat 3.
In this embodiment, through setting up filter vat 3, filter vat 3's filtration pore can be through liquid but can not pass through the solid for the solid is whole to be piled up in filter vat 3's inside, and liquid overflows into separation bucket 1's inside, takes out liquid through filtrating valve 11 earlier, and later recycle filter residue valve 4 takes out the filter residue.
Specifically, the inner diameter of the feeding pipe 5 is smaller than the inner diameter of the filter vat 3.
In this embodiment, a part of the mixture passing through the inside of the feed pipe 5 is prevented from being directly poured between the filtering barrel 3 and the separating barrel 1, which is inconvenient to clean.
Specifically, the lower end of the feeding pipe 5 extends to the inside of the filtering barrel 3.
In this embodiment, a part of the mixture passing through the inside of the feed pipe 5 is prevented from being directly poured between the filtering barrel 3 and the separating barrel 1, which is inconvenient to clean.
Specifically, a vacuum valve 6 is installed above the barrel cover 2, a vacuum tube 7 is installed on the surface of the vacuum valve 6, and one end of the vacuum tube 7 extends into the separation barrel 1.
In this embodiment, utilize vacuum valve 6 and vacuum tube 7 to absorb the air of separation barrel 1 inside totally, not only can slow down the oxidation time of mixture, can accelerate simultaneously that the mixture flows into the time of separation barrel 1 inside, improve the efficiency of work.
Specifically, the dispersion plate 9 is installed through the installation pole 8 in the inside of filter vat 3, weeping hole 10 has been seted up on the surface of dispersion plate 9.
In this embodiment, the dispersion plate 9 can disperse the solid-liquid mixture, and a part of the liquid substance can pass through the filtering holes of the filtering barrel 3 and enter between the separation barrel 1 and the filtering barrel 3.
Specifically, the mounting rod 8 is a round rod shaped like an "L".
In this embodiment, the dispersion plate 9 is easily mounted.
Specifically, the number of the mounting rods 8 and the dispersion plates 9 is two, and the two liquid leakage holes 10 in the dispersion plates 9 are staggered.
In this embodiment, when the mixture falls from the position of the weep hole 10 on the previous dispersion plate 9, the mixture will not directly fall into the inside of the filter vat 3, and at the same time, the mixture will splash between the separation vat 1 and the filter vat 3 when falling on the dispersion plate 9.
Specifically, the size of the weep hole 10 is smaller than the size of the filtration pore of the filtration barrel 3.
In this embodiment, the solid-liquid mixture can easily fall from the inside of the weep hole 10.
Specifically, the dispersion plate 9 is shaped like an umbrella with an arc-shaped upper surface.
In this embodiment, a part of the mixed liquid falling on the surface of the dispersion plate 9 may splash between the separation barrels 1 of the filter barrel 3 from the position of the dispersion plate 9, and the mixed liquid may not be filtered and separated after falling to the bottom.
Specifically, the distance from the center to the edge of the dispersion plate 9 is smaller than the inner diameter of the filter vat 3.
In this embodiment, there is enough space so that the mixed liquid along the surface of the dispersion plate 9 can enter the inside of the filter vat 3.
The utility model discloses a theory of operation and use flow: the mixture is introduced into the feeding pipe 5, the vacuum valve 6 is started to completely pump out the air inside the separation barrel 1, the flowing speed of the mixture is increased, the mixture completely falls into the inside of the filter barrel 3, the solid part completely falls into the inside of the filter barrel 3 under the action of the filter holes, the filtrate basically falls into the space between the filter barrel 3 and the separation barrel 1, then the mixture is stood for a period of time, the filtrate valve 11 is opened first to take out the liquid, the filter residue valve 4 is opened again, and the solid is taken out.
Although embodiments of the present invention have been shown and described, it will be appreciated by those skilled in the art that changes, modifications, substitutions and alterations can be made in these embodiments without departing from the principles and spirit of the invention, the scope of which is defined in the appended claims and their equivalents.
Claims (10)
1. A solid-liquid static separation device is characterized in that: including separation bucket (1) and bung (2), bung (2) are installed the top of separation bucket (1), filter vat (3) are still installed to the inside of separation bucket (1), the position department that the below of separation bucket (1) corresponds filter vat (3) installs filter residue valve (4), filtrate valve (11) are still installed to the lateral surface of separation bucket (1), inlet pipe (5) are installed to the top of bung (2), inlet pipe (5) are located directly over filter vat (3).
2. A solid-liquid static separation apparatus according to claim 1, characterized in that: the inner diameter of the feeding pipe (5) is smaller than that of the filter barrel (3).
3. A solid-liquid static separation apparatus according to claim 1, characterized in that: the lower end of the feeding pipe (5) extends to the interior of the filter vat (3).
4. A solid-liquid static separation apparatus according to claim 1, characterized in that: a vacuum valve (6) is installed above the barrel cover (2), a vacuum tube (7) is installed on the surface of the vacuum valve (6), and one end of the vacuum tube (7) extends into the separating barrel (1).
5. A solid-liquid static separation apparatus according to claim 1, characterized in that: the dispersion board (9) is installed through installation pole (8) in the inside of filter vat (3), weeping hole (10) have been seted up on the surface of dispersion board (9).
6. A solid-liquid static separation apparatus according to claim 5, characterized in that: the mounting rod (8) is a round rod with an L-shaped shape.
7. A solid-liquid static separation apparatus according to claim 5, characterized in that: the quantity of installation pole (8) and dispersion board (9) is provided with two, two weeping hole (10) on dispersion board (9) stagger each other.
8. A solid-liquid static separation apparatus according to claim 5, characterized in that: the size of the liquid leakage hole (10) is smaller than that of the filtering hole of the filtering barrel (3).
9. A solid-liquid static separation apparatus according to claim 5, characterized in that: the dispersion plate (9) is in the shape of an umbrella with an arc-shaped upper surface.
10. A solid-liquid static separation apparatus according to claim 5, characterized in that: the distance from the center of the dispersion plate (9) to the edge is smaller than the inner diameter of the filter barrel (3).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202222175848.0U CN218280767U (en) | 2022-08-17 | 2022-08-17 | Solid-liquid static separation device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202222175848.0U CN218280767U (en) | 2022-08-17 | 2022-08-17 | Solid-liquid static separation device |
Publications (1)
Publication Number | Publication Date |
---|---|
CN218280767U true CN218280767U (en) | 2023-01-13 |
Family
ID=84795167
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN202222175848.0U Active CN218280767U (en) | 2022-08-17 | 2022-08-17 | Solid-liquid static separation device |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN218280767U (en) |
-
2022
- 2022-08-17 CN CN202222175848.0U patent/CN218280767U/en active Active
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN107376505A (en) | A kind of feldspar in powder produces waste recycle system | |
CN110217904A (en) | A kind of wastewater purification treatment equipment | |
CN110694795B (en) | Waste engine oil recycling treatment method | |
CN211896525U (en) | Automatic slag removal type anaerobic reactor | |
CN218280767U (en) | Solid-liquid static separation device | |
WO2018103534A1 (en) | Horizontal-flow continuous sand filtration apparatus and water treatment process thereof | |
CN211864158U (en) | Sewage recycling system for concrete production | |
CN205391910U (en) | Belt vacuum filter pan feeding whirl device | |
CN208135974U (en) | A kind of sewage-treatment plant | |
CN209714502U (en) | A kind of wastewater filtering device for waste plastics recycling | |
CN207872392U (en) | A kind of secondary stock filtering and impurity removing device | |
CN204865170U (en) | Copper -containing waste water copper powder recovery unit | |
CN208372633U (en) | A kind of waste oil recycling and processing device | |
CN215559095U (en) | Novel deoiling device | |
CN210505791U (en) | Sewage treatment plant of preliminary treatment formula | |
CN219783946U (en) | Production electrolyte waste liquid recovery device | |
CN217188234U (en) | Dense water treatment facilities of industry sewage reverse osmosis membrane | |
CN217340463U (en) | Filtrate collecting mechanism of chamber filter press | |
CN205287865U (en) | Vertical vacuum pump waste oil recovery processing device | |
CN216092504U (en) | Pulp filtering device of papermaking wastewater treatment equipment | |
CN217103306U (en) | High concentration aminophenol waste water deoiling system | |
CN217068029U (en) | Separation device for extracting vanadium from red mud | |
CN218280793U (en) | Industrial wastewater filtering device | |
CN219942088U (en) | Solid waste dry-wet separation equipment for preventing and treating water pollution | |
CN220812983U (en) | Filter disc quick-change type dyeing liquid recycling box |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
GR01 | Patent grant | ||
GR01 | Patent grant |