CN217340205U - Equipment suitable for separating materials with large specific gravity difference between solid phase and liquid phase - Google Patents
Equipment suitable for separating materials with large specific gravity difference between solid phase and liquid phase Download PDFInfo
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- CN217340205U CN217340205U CN202221890568.1U CN202221890568U CN217340205U CN 217340205 U CN217340205 U CN 217340205U CN 202221890568 U CN202221890568 U CN 202221890568U CN 217340205 U CN217340205 U CN 217340205U
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- pipe section
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- liquid phase
- straight pipe
- specific gravity
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- 239000007791 liquid phase Substances 0.000 title claims abstract description 60
- 239000000463 material Substances 0.000 title claims abstract description 47
- 239000007790 solid phase Substances 0.000 title claims abstract description 30
- 230000005484 gravity Effects 0.000 title claims description 19
- 238000000926 separation method Methods 0.000 claims abstract description 11
- 238000011010 flushing procedure Methods 0.000 claims description 19
- 238000005406 washing Methods 0.000 claims description 10
- 239000007788 liquid Substances 0.000 claims description 5
- 239000012071 phase Substances 0.000 abstract description 8
- 238000005191 phase separation Methods 0.000 abstract description 4
- 238000010586 diagram Methods 0.000 description 3
- 239000000047 product Substances 0.000 description 3
- 238000004062 sedimentation Methods 0.000 description 3
- 239000010865 sewage Substances 0.000 description 3
- 230000007547 defect Effects 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 239000002638 heterogeneous catalyst Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 239000006228 supernatant Substances 0.000 description 1
- 238000007864 suspending Methods 0.000 description 1
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- Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
Abstract
The utility model provides an equipment that is fit for big material separation of solid-liquid phase proportion difference, including the one-level settling cask, the one-level settling cask includes barrel and lower barrel, wherein: the upper cylinder body comprises an upper straight pipe section and an upper conical pipe section which are arranged from top to bottom and are mutually communicated, and a material inlet at the top of the upper straight pipe section is communicated with a discharge port at the bottom of the reaction kettle; the lower cylinder comprises a lower straight pipe section and a lower conical pipe section which are arranged from top to bottom and are communicated with each other, the lower straight pipe section is communicated with the upper conical pipe section, a liquid phase pipeline is arranged in the lower straight pipe section, the pipe orifice of the liquid phase pipeline is arranged in the middle of the top of the lower straight pipe section, and a solid phase outlet is arranged at the bottom of the lower conical pipe section. The utility model discloses a structure that subsides naturally makes solid-liquid phase separation, guarantees the collection of separation effect and heavy phase material.
Description
Technical Field
The utility model relates to the technical field of sewage treatment equipment relevance, in particular to equipment suitable for separating solid-liquid phase specific gravity and large materials.
Background
The reaction kettle of the company for the high-grade heterogeneous catalyst project special for sewage treatment has the defects of large specific gravity difference of a solid phase and a liquid phase and the need of stirring, suspending, mixing and reacting. And the reation kettle of traditional structure, for example patent number CN201920477683.8, the name is a sewage treatment reation kettle, because reation kettle adopts conventional structural design, the material is in to splitter transportation process, can appear subsiding the problem, leads to the product separation effect not good, and product quality can't guarantee.
SUMMERY OF THE UTILITY MODEL
For solving the not enough of prior art, the utility model discloses combine prior art, set out from practical application, provide an equipment that is fit for the big material separation of solid-liquid phase proportion difference, the structure that adopts the nature to subside makes solid-liquid phase separation, guarantees the collection of separation effect and heavy phase material.
In order to achieve the above purpose, the technical scheme of the utility model is as follows:
the utility model provides an equipment that is fit for big material separation of solid-liquid phase specific gravity difference, includes one-level settling cask, one-level settling cask includes barrel and lower barrel, wherein:
the upper barrel comprises an upper straight pipe section and an upper conical pipe section which are arranged from top to bottom and are communicated with each other, and a material inlet at the top of the upper straight pipe section is communicated with a discharge outlet at the bottom of the reaction kettle;
the lower cylinder body comprises a lower straight pipe section and a lower conical pipe section which are arranged from top to bottom and are communicated with each other, the lower straight pipe section is communicated with the upper conical pipe section, a liquid phase pipeline is arranged in the lower straight pipe section, the orifice of the liquid phase pipeline is arranged in the middle of the top of the lower straight pipe section, and a solid phase outlet is arranged at the bottom of the lower conical pipe section.
Further, the opening of the liquid phase pipeline opening is upward at the top of the lower straight pipe section.
Furthermore, an umbrella cap is arranged at the pipe orifice of the liquid phase pipeline for shielding.
Further, a circulating flushing pipeline is arranged at the lower part of the upper straight pipe section.
Further, the circulating flushing pipeline comprises an annular flushing coil and a plurality of flushing nozzles arranged on the circumference of the flushing coil.
Furthermore, a plurality of the washing nozzles are uniformly arranged along the circumferential direction of the washing coil pipe, and the washing nozzles are obliquely arranged on the inner wall of the upper straight pipe section.
Further, this equipment still includes the second grade settling cask, the inside settling pipeline that sets up of second grade settling cask communicates with liquid phase pipeline, and second grade settling cask bottom sets up the solid phase bin outlet.
Further, the bottom of the settling pipeline is provided with a mixed liquid outlet.
Further, a liquid phase outlet is arranged on one side of the secondary settling tank.
Further, the bottom of the secondary sedimentation tank is conical.
The utility model has the advantages that:
1. the utility model discloses a one-level settling cask of biconical structure who sets up makes reaction material get into by reation kettle and sinks naturally behind the settling cask by gravity, and the liquid phase passes through liquid phase pipeline and discharges, and the solid phase sinks to in the barrel down, can guarantee solid-liquid phase separation effect to guarantee the quality of product.
2. The utility model discloses a liquid phase pipeline structural design who sets up prevents to a great extent that heavy phase material from getting into the liquid phase pipeline, further guarantees solid-liquid phase separation effect.
3. The utility model discloses a two conical barrel structures have avoided the siltation of material in the barrel, and the design of flushing line can guarantee that heavy phase material is whole to flow in down the barrel.
4. The utility model discloses a second grade settling cask that sets up can carry out the solid phase of a small amount of inflow liquid phases and collect once more, realizes the thorough separation in solid-liquid phase.
Drawings
FIG. 1 is a schematic view of the overall structure of the present invention;
FIG. 2 is a schematic diagram of the structure of the primary settling tank of the present invention;
figure 3 is the utility model discloses the relevant structure schematic diagram of second grade settling cask.
Reference numerals shown in the drawings:
1. a primary settling tank; 2. a secondary settling tank; 3. an upper cylinder body; 4. a lower cylinder body; 5. an upper straight tube section; 6. an upper conical pipe section; 7. a lower straight tube section; 8. a lower conical section; 9. a liquid phase line; 10. an umbrella cap; 11. flushing the coil pipe; 12. flushing the nozzle; 13. a settling line; 14. and (5) discharging the mixed liquid.
Detailed Description
The invention is further described with reference to the accompanying drawings and the specific embodiments. It should be understood that these examples are for illustrative purposes only and are not intended to limit the scope of the present invention. Further, it should be understood that various changes or modifications of the present invention can be made by those skilled in the art after reading the teaching of the present invention, and these equivalents also fall within the scope of the present invention.
As shown in fig. 1 and 3, the relevant structural schematic diagram of the device suitable for separating materials with large specific gravity difference between solid and liquid phases is provided for this embodiment.
The separation apparatus of this example mainly comprises a primary settling tank 1 and a secondary settling tank 2 as shown in fig. 1. The structure of the primary settling tank 1 is shown in figure 2 and is used for connecting with a reaction kettle. Specifically, the primary settling tank 1 adopts a biconical structure design and comprises an upper barrel 3 and a lower barrel 4. The top of the upper barrel body 3 is provided with a material inlet A, a gas outlet B and a manhole M, and the material inlet A is communicated with a discharge hole at the bottom of the reaction kettle so that the primary settling tank 1 is communicated with the reaction kettle.
The upper barrel 3 mainly comprises an upper straight pipe section 5 and an upper conical pipe section 6, the upper straight pipe section 5 is arranged above the upper conical pipe section 6 and communicated with the upper conical pipe section 6, the lower barrel 4 mainly comprises a lower straight pipe section 7 and a lower conical pipe section 8, the upper part of the lower straight pipe section 7 is communicated with the upper conical pipe section 6, the lower part of the lower straight pipe section is communicated with the lower conical pipe section 8, a liquid phase pipeline 9 is arranged in the lower straight pipe section 7 and used for enabling a liquid phase to flow out, a pipe orifice of the liquid phase pipeline 9 is arranged in the middle of the top of the lower straight pipe section 7, the opening of the liquid phase pipeline is upward, and a solid phase outlet E is arranged at the bottom of the lower conical pipe section 8.
In the above structure of the present embodiment, the volume of the lower cylinder 4 should be designed to be slightly larger than the volume of the heavy phase material after natural sedimentation. After the materials are mixed in the reaction kettle, the valve of the reaction kettle is opened, so that the reaction materials enter the primary settling tank 1 and naturally sink in the primary settling tank 1 by means of gravity, and the gas in the primary settling tank 1 is discharged through the gas outlet B, so that the materials in the reaction kettle smoothly flow into the primary settling tank 1. The material relies on gravity natural settling in one-level settling cask 1, and solid phase material all subsides downwards to barrel 4 in down, and accessible solid phase export E discharges, and the supernatant passes through liquid phase pipeline 9 and discharges the natural settling separation that realizes solid-liquid phase material, has guaranteed the collection of weight material.
Owing to set up liquid phase pipeline 9, if there is not special design, heavy phase material can influence the collection of heavy phase material in getting into liquid phase pipeline 9 through the liquid phase pipeline 9 mouth of pipe, so, this embodiment has set up umbrella hat 10 in liquid phase pipeline 9's mouth of pipe department, and umbrella hat 10 is fixed at liquid phase pipeline 9 top, can effectively avoid heavy phase material to enter into in the liquid phase pipeline 9.
In order to avoid the material to silt up in last barrel 3 and can't all flow into barrel 4 down, in this embodiment, the lower part at upper portion straight tube section 5 has been equipped with the circulation flushing line, and is specific, the circulation flushing line includes annular flushing coil 11 and sets up in a plurality of washing nozzle 12 of flushing coil 11 circumference, flushing coil 11 and circulation liquid entry C intercommunication, a plurality of washing nozzle 12 evenly arranges along flushing coil 11 circumference, and washing nozzle 12 sets up to the slope of upper portion straight tube section 5 inner wall. After the sedimentation is half a hour, the circulating pump is started, the upper barrel body 3 is washed through the circulating washing pipeline, the solid-phase materials can be guaranteed to completely flow into the lower barrel body 4, and the solid-phase materials are fully recovered.
When the equipment is used, a small amount of solid-phase materials still enter the liquid-phase pipeline 9, and in order to realize the thorough recovery of the solid-phase materials, the equipment is also provided with a secondary settling tank 2. As shown in fig. 3, second grade settling cask 2 top has entry F, gas outlet G, and entry F passes through the pipeline and communicates with liquid phase pipeline 9, and second grade settling cask 2 bottom sets up to the smooth emission that can realize the solid phase material for the toper structure, and inside sets up settling cask 13 and liquid phase pipeline 9 intercommunication, and the bottom sets up solid phase bin outlet I, and one side sets up liquid phase outlet H, sets up mixed liquid outlet 14 in settling cask 13 bottom, can further retrieve the solid phase material that flows into liquid phase pipeline 9 through second grade settling cask 2.
Claims (10)
1. The utility model provides an equipment that is fit for big material separation of solid-liquid phase specific gravity difference, its characterized in that includes one-level settling cask, one-level settling cask includes barrel and lower barrel, wherein:
the upper barrel comprises an upper straight pipe section and an upper conical pipe section which are arranged from top to bottom and are communicated with each other, and a material inlet at the top of the upper straight pipe section is communicated with a discharge outlet at the bottom of the reaction kettle;
the lower cylinder body comprises a lower straight pipe section and a lower conical pipe section which are arranged from top to bottom and are communicated with each other, the lower straight pipe section is communicated with the upper conical pipe section, a liquid phase pipeline is arranged in the lower straight pipe section, the orifice of the liquid phase pipeline is arranged in the middle of the top of the lower straight pipe section, and a solid phase outlet is arranged at the bottom of the lower conical pipe section.
2. The apparatus for separating materials with large difference in specific gravity between solid and liquid phases as claimed in claim 1, wherein the liquid phase pipeline has its orifice opened upward at the top of the lower straight pipe section.
3. The apparatus for separating materials with large difference in specific gravity between solid and liquid phases as claimed in claim 2, wherein the pipe orifice of the liquid phase pipeline is covered by an umbrella cap.
4. The apparatus for separating materials with large difference in specific gravity between solid and liquid phases as claimed in claim 1, wherein a circular flushing line is provided at the lower part of the upper straight pipe section.
5. The apparatus for separating materials with large difference in specific gravity between solid and liquid phases according to claim 4, wherein the circulating flushing line comprises an annular flushing coil and a plurality of flushing nozzles arranged on the circumference of the flushing coil.
6. The apparatus for separating materials with large difference in specific gravity between solid and liquid phases as claimed in claim 5, wherein a plurality of said washing nozzles are uniformly arranged along the circumference of the washing coil pipe, and the washing nozzles are inclined toward the inner wall of the upper straight pipe section.
7. The apparatus for separating materials with large difference in specific gravity between solid and liquid phases as claimed in any one of claims 1 to 6, further comprising a secondary settling tank, wherein a settling pipeline is arranged in the secondary settling tank and communicated with the liquid phase pipeline, and a solid phase discharge port is arranged at the bottom of the secondary settling tank.
8. The apparatus for separating materials with large specific gravity difference between solid and liquid phases according to claim 7, wherein a mixed liquid outlet is arranged at the bottom of the settling pipeline.
9. The apparatus for separating materials with large difference in specific gravity between solid and liquid phases as claimed in claim 7, wherein a liquid phase outlet is provided at one side of the secondary settling tank.
10. The apparatus for separation of materials with large difference in specific gravity between solid and liquid phases according to claim 7, wherein the bottom of the secondary settling tank is tapered.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202221890568.1U CN217340205U (en) | 2022-07-22 | 2022-07-22 | Equipment suitable for separating materials with large specific gravity difference between solid phase and liquid phase |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202221890568.1U CN217340205U (en) | 2022-07-22 | 2022-07-22 | Equipment suitable for separating materials with large specific gravity difference between solid phase and liquid phase |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN217340205U true CN217340205U (en) | 2022-09-02 |
Family
ID=83039182
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202221890568.1U Active CN217340205U (en) | 2022-07-22 | 2022-07-22 | Equipment suitable for separating materials with large specific gravity difference between solid phase and liquid phase |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN217340205U (en) |
-
2022
- 2022-07-22 CN CN202221890568.1U patent/CN217340205U/en active Active
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| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of utility model: A device suitable for separating materials with large specific gravity differences between solid and liquid phases Granted publication date: 20220902 Pledgee: Shandong Shanghe Rural Commercial Bank Co.,Ltd. Pledgor: Shuizhige (Shandong) Environmental Protection Technology Co.,Ltd. Registration number: Y2024980014980 |