CN221084737U - Organic silicon monomer and silicone oil production wastewater organic matter high-efficiency separation device - Google Patents
Organic silicon monomer and silicone oil production wastewater organic matter high-efficiency separation device Download PDFInfo
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- CN221084737U CN221084737U CN202322939662.2U CN202322939662U CN221084737U CN 221084737 U CN221084737 U CN 221084737U CN 202322939662 U CN202322939662 U CN 202322939662U CN 221084737 U CN221084737 U CN 221084737U
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- Prior art keywords
- filter
- wall
- barrel
- separation barrel
- organic
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- 238000000926 separation method Methods 0.000 title claims abstract description 51
- 239000002351 wastewater Substances 0.000 title claims abstract description 34
- 229920002545 silicone oil Polymers 0.000 title claims abstract description 18
- 239000000178 monomer Substances 0.000 title claims abstract description 15
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 title claims abstract description 14
- 229910052710 silicon Inorganic materials 0.000 title claims abstract description 14
- 239000010703 silicon Substances 0.000 title claims abstract description 14
- 238000004519 manufacturing process Methods 0.000 title claims description 6
- 239000005416 organic matter Substances 0.000 title claims description 5
- 239000012074 organic phase Substances 0.000 claims abstract description 18
- 239000012535 impurity Substances 0.000 claims abstract description 14
- 230000005540 biological transmission Effects 0.000 claims abstract description 9
- 230000002093 peripheral effect Effects 0.000 claims abstract description 4
- 239000008346 aqueous phase Substances 0.000 claims description 12
- 238000004581 coalescence Methods 0.000 claims description 6
- 238000001914 filtration Methods 0.000 claims description 4
- 238000009826 distribution Methods 0.000 claims description 2
- 230000008676 import Effects 0.000 claims description 2
- 239000007788 liquid Substances 0.000 abstract description 12
- 238000007790 scraping Methods 0.000 abstract description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 5
- 230000001360 synchronised effect Effects 0.000 abstract description 2
- 238000004065 wastewater treatment Methods 0.000 abstract description 2
- 239000012071 phase Substances 0.000 abstract 1
- 238000000034 method Methods 0.000 description 5
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 3
- 230000007547 defect Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 230000003287 optical effect Effects 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000000356 contaminant Substances 0.000 description 1
- KPUWHANPEXNPJT-UHFFFAOYSA-N disiloxane Chemical class [SiH3]O[SiH3] KPUWHANPEXNPJT-UHFFFAOYSA-N 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 239000002920 hazardous waste Substances 0.000 description 1
- 239000007791 liquid phase Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- -1 siloxanes Chemical class 0.000 description 1
- 239000003381 stabilizer Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 231100000331 toxic Toxicity 0.000 description 1
- 230000002588 toxic effect Effects 0.000 description 1
- 239000010891 toxic waste Substances 0.000 description 1
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- Centrifugal Separators (AREA)
Abstract
The utility model relates to the technical field of wastewater treatment, in particular to a high-efficiency separation device for organic matters in wastewater produced by organic silicon monomers and silicone oil, which comprises a separation barrel, wherein a control box is arranged at the center of the top of the separation barrel, a filter is rotatably arranged in the control box through a bevel gear transmission assembly, the filter is downwards inserted into the separation barrel, an outer mounting ring is sleeved on the outer side of a barrel body of the filter, circumferentially distributed scraping plates are arranged on the outer side of the outer mounting ring, the scraping plates are contacted with the inner wall of the separation barrel and scrape impurities on the inner wall of the separation barrel, a certain initial speed can be applied to the discharged wastewater by using a rotary accelerator, the wastewater can be ensured to be rapidly contacted with a peripheral coalescing element, water phase and an organic phase in the wastewater can be effectively separated, and the scraping plates accompanied with synchronous rotation of the accelerator can be used for wall-hanging treatment on the upper half inner wall of the separation barrel, so that the residual impurities in the inner wall can be effectively scraped, and the treatment liquid in the separation barrel can be completely discharged outwards.
Description
Technical Field
The utility model relates to the technical field of wastewater treatment, in particular to an efficient separation device for organic matters in wastewater produced by organic silicon monomers and silicone oil.
Background
The production of organosilicon, especially organosilicon monomers and silicone oils, produces large amounts of toxic and hazardous waste water, with contaminants mainly siloxanes and the remaining production materials, which if not properly treated can cause serious environmental pollution, especially siloxane and benzene-based components, and conventional treatment methods are to separate the organic phase from the aqueous phase by filtering the waste water with coalescing elements.
The existing separation device has the defects that organic liquid phase impurities are easy to remain on the inner wall of a separation tank, so that the device is not discharged cleanly and the next use is affected, and the problem is solved, so that the high-efficiency separation device for organic matters in the wastewater of the production of the organic silicon monomers and the silicone oil is provided.
Disclosure of utility model
The utility model aims to solve the defects in the prior art, and provides a high-efficiency separation device for organic matters in wastewater produced by organic silicon monomers and silicone oil.
In order to achieve the above purpose, the present utility model adopts the following technical scheme:
The utility model provides an organic silicon monomer and high-efficient separator of silicone oil waste water organic matter, includes the separation bucket, the inner wall lower half of separation bucket is provided with a plurality of coalescence element that circumference distributes, and the inside middle part of this separation bucket is provided with multilayer stationary flow board, the top center of separation bucket is provided with the control box, the filter is installed through bevel gear drive assembly rotation to the inside of control box, the filter is tubular structure, and this filter inserts downwards in the separation bucket, the top of control box is provided with open formula pouring inlet, and the top import of filter is built-in to the lower extreme of this pouring inlet, the outside of the barrel of filter has cup jointed outer collar, outer collar's outer peripheral face is provided with a plurality of fixed bolsters, the outer end of fixed bolster is provided with the scraper blade, the scraper blade contacts in the inner wall of separation bucket and scrapes its inner wall impurity.
In a preferred technical scheme, the bevel gear transmission assembly comprises a drive bevel gear arranged on the side wall of the control box and a driven bevel gear arranged at the bottom of the control box, and a transmission motor for driving the drive bevel gear to rotate is arranged outside the control box.
In a preferred technical scheme, a through hole for inserting a filter is formed in the center of the driven bevel gear, and the filter is installed in the center of the filter through a bearing component and keeps coaxial rotation with the filter.
In a preferred technical scheme, an aqueous phase outlet and an organic phase outlet are arranged on the outer wall of the separation barrel, and the organic phase outlet is positioned above the aqueous phase outlet.
In a preferred technical scheme, the upper half part of the cylinder body of the filter is designed as a light wall, the lower half part of the cylinder body of the filter is designed as a filter wall, and the surface of the filter wall is provided with a filter hole.
In a preferred technical scheme, the filter is vertically arranged, and the lower end of the filter is rotationally fixed at the center of the bottom wall of the separation barrel.
The beneficial effects of the utility model are as follows:
1. The waste water flowing out when the filter rotates has a certain initial speed, and the waste water can accelerate to flow to the external coalescing element and rapidly coalesce due to the fact that the filter is in the rotating process, and waste water separation is accelerated.
2. In the rotating process of the filter, each scraper blade can periodically act on the inner wall of the separation barrel, and silicone oil impurities adhered on the inner wall of the separation barrel can be scraped by the scraper blade, and the scraped impurities are fused with upper liquid, so that the silicone oil impurities are conveniently discharged outwards.
To sum up, through the separator that this scheme provided, the inner wall of having solved the waste water knockout drum remains organic impurity easily, the device material discharge is not clean, influence the problem of use, this separator's propose, this rotary accelerator can apply certain initial velocity for the waste water that flows out, ensure that waste water can contact the coalescence element of periphery fast, effectively separate aqueous phase and organic phase in the waste water, and the scraper blade that accompanies accelerator synchronous rotation can carry out wall built-up processing again to knockout drum upper portion inner wall, effectively strike off the inner wall impurity and remain, ensure that the treatment fluid in the knockout drum all can outwards discharge completely, equipment is simple high-efficient, it is comparatively convenient to use.
Drawings
FIG. 1 is a schematic diagram of a front view of a separating device according to the present utility model;
FIG. 2 is a schematic diagram showing the assembly relationship of the filter according to the present utility model;
fig. 3 is a schematic top view of the distribution and assembly of the scraper according to the present utility model.
In the figure: 1. a separation barrel; 2. a control box; 3. a drive bevel gear; 4. a driven bevel gear; 5. a bearing member; 6. a filter; 61. a light wall; 62. a filter wall; 7. an outer mounting ring; 8. a fixed bracket; 9. a scraper; 10. a coalescing element; 11. a steady flow plate; 12. an aqueous phase outlet; 13. an organic phase outlet; 14. an pouring port; 15. and (5) a transmission motor.
Detailed Description
The following description of the embodiments of the present utility model will be made clearly and completely with reference to the accompanying drawings, in which it is apparent that the embodiments described are only some embodiments of the present utility model, but not all embodiments.
In this embodiment, referring to fig. 1-3, the device for efficiently separating organic matters from waste water produced by organic silicon monomers and silicone oil comprises a separation barrel 1, wherein a plurality of coalescence elements 10 distributed circumferentially are arranged at the lower half part of the inner wall of the separation barrel 1, a plurality of steady flow plates 11 are arranged at the middle part of the inner part of the separation barrel 1, under the prior art, waste water enters the coalescence elements 10, a large amount of organic matters are coalesced on inner fibers of the coalescence elements 10, and grow into large liquid drops along with water flow, the organic liquid drops are lighter than water, gradually float upwards and pass through the steady flow plates 11 above, and are gradually separated into an organic phase and an aqueous phase upper layer and a lower layer under the action of gravity. It should be added that, with reference to fig. 1, the outer wall of the separation barrel 1 is provided with an aqueous phase outlet 12 and an organic phase outlet 13, the organic phase outlet 13 is located above the aqueous phase outlet 12, when the upper layer and the lower layer are layered, the upper layer liquid is discharged from the organic phase outlet 13, and the lower layer liquid is discharged from the aqueous phase outlet 12.
The center of the top of the separation barrel 1 is provided with a control box 2, a filter 6 is rotatably arranged in the control box 2 through a bevel gear transmission assembly, the filter 6 is of a barrel structure, and the filter 6 is downwards inserted into the separation barrel 1. The center of the driven bevel gear 4 is provided with a through hole for inserting the filter 6, and the filter 6 is mounted at the center of the filter 6 through a bearing member 5 and is kept coaxially rotated with the filter 6.
The top of the control box 2 is provided with an open pouring opening 14, the lower end of which pouring opening 14 is built into the top inlet of the filter 6, and the pouring opening 14 is used for pouring the waste water, which can enter the filter 6 along the pouring opening 14 and finally into the separation tank 1.
It should be noted that the bevel gear transmission assembly includes a drive bevel gear 3 disposed on a side wall of the control box 2 and a driven bevel gear 4 disposed at a bottom of the control box 2, and a transmission motor 15 for driving the drive bevel gear 3 to rotate is disposed outside the control box 2. By means of the drive motor 15, the drive bevel gear 3 and the driven bevel gear 4 can be controlled to rotate and finally the filter 6 can be controlled to rotate, wherein the purpose of the rotation of the filter 6 is to ensure that when wastewater flows out from the lower end of the filter 6 into the separation barrel 1, the discharged wastewater has a certain initial velocity, and because the filter 6 is in the process of rotating, the wastewater can accelerate to flow to the external coalescing element 10 and coalesce quickly, and wastewater separation is accelerated.
In addition, as shown in fig. 1, the upper half part of the barrel body of the filter 6 is designed as a light wall 61, the lower half part of the barrel body of the filter 6 is designed as a filter wall 62, the surface of the filter wall 62 is provided with a filter hole, the filter 6 is vertically arranged, and the lower end of the filter 6 is rotationally fixed at the center of the bottom wall of the separation barrel 1. The upper half of the filter 6 is designed as a light wall 61, which aims to avoid that waste water directly overflows from the upper half of the filter 6 when pouring, because the upper half space of the separating drum 1 is used for containing separated organic phase, and if the upper half of the filter 6 is also provided with a filter hole, water liquid and organic liquid are mixed, and the effect of waste water separation can be influenced. So that only the lower half of the filter 6 is provided with the filter holes.
It should be further noted that, the stabilizer 11 is just located at the middle position, the organic phase separated from the upper layer contacts the optical wall 61, and the aqueous phase separated from the lower layer is communicated with the filter 6, so that the organic phase liquid does not have larger fluctuation due to the contact of the organic phase liquid with the optical wall 61 during the rotation of the filter 6, and the organic phase of the upper layer is not secondarily mixed with the wastewater.
The outside of the cylinder body of the filter 6 is sleeved with an outer mounting ring 7, the outer peripheral surface of the outer mounting ring 7 is provided with a plurality of fixing brackets 8, the outer ends of the fixing brackets 8 are provided with scraping plates 9, and the scraping plates 9 are contacted with the inner wall of the separation barrel 1 and scrape impurities on the inner wall. In the process of rotating the filter 6, each scraping plate 9 also periodically acts on the inner wall of the separation barrel 1, and silicone oil impurities adhered on the inner wall of the separation barrel 1 can be scraped off by using the scraping plates 9, and the scraped impurities are fused with upper liquid, so that the impurities are conveniently discharged outwards.
Finally, it should be specifically mentioned that in this embodiment, the rotation speed of the filter 6 should not be too high, and should be designed to be one minute or more per rotation normally, so that the scraping speed of the scraper 9 is not too high, and the organic phase liquid formed on the upper layer is not greatly stirred, which can ensure that the inner wall of the separation barrel 1 is scraped and the separation effect is good.
The foregoing is only a preferred embodiment of the present utility model, but the scope of the present utility model is not limited thereto, and any person skilled in the art, who is within the scope of the present utility model, should make equivalent substitutions or modifications according to the technical scheme of the present utility model and the inventive concept thereof, and should be covered by the scope of the present utility model.
Claims (6)
1. The utility model provides an organic silicon monomer and high-efficient separator of silicone oil waste water organic matter, includes separation barrel (1), the inner wall lower half of separation barrel (1) is provided with a plurality of coalescence element (10) of circumference distribution, and the inside middle part of this separation barrel (1) is provided with multilayer stationary flow board (11), a serial communication port, the top center of separation barrel (1) is provided with control box (2), filter (6) are installed through bevel gear drive assembly rotation to the inside of control box (2), filter (6) are barrel structure, and this filter (6) insert downwards in separation barrel (1), the top of control box (2) is provided with open type pouring inlet (14), and the top import of this pouring inlet (14) is built-in filter (6), outer collar (7) have been cup jointed in the barrel outside of filter (6), the outer peripheral face of outer collar (7) is provided with a plurality of fixed bolster (8), the outer end of fixed bolster (8) is provided with scraper blade (9), scraper blade (9) contact in the inner wall of separation barrel (1) and its impurity.
2. The efficient organic silicon monomer and silicone oil production wastewater organic matter separation device according to claim 1, wherein the bevel gear transmission assembly comprises a drive bevel gear (3) arranged on the side wall of the control box (2) and a driven bevel gear (4) arranged at the bottom of the control box (2), and a transmission motor (15) for driving the drive bevel gear (3) to rotate is arranged outside the control box (2).
3. The device for efficiently separating organic matters from the wastewater produced by the organic silicon monomers and the silicone oil according to claim 2, wherein a through hole for inserting a filter (6) is formed in the center of the driven bevel gear (4), and the filter (6) is installed in the center of the filter (6) through a bearing component (5) and keeps coaxial rotation with the filter.
4. The device for efficiently separating organic matters from the wastewater produced by the organic silicon monomers and the silicone oil according to claim 1, wherein an aqueous phase outlet (12) and an organic phase outlet (13) are arranged on the outer wall of the separation barrel (1), and the organic phase outlet (13) is positioned above the aqueous phase outlet (12).
5. The device for efficiently separating organic matters from the wastewater produced by the organic silicon monomers and the silicone oil according to claim 1, wherein the upper half part of the barrel body of the filter (6) is designed to be a light wall (61), the lower half part of the barrel body of the filter (6) is designed to be a filtering wall (62), and the surface of the filtering wall (62) is provided with a filtering hole.
6. The device for efficiently separating organic matters from the wastewater produced by the organic silicon monomers and the silicone oil according to claim 5, wherein the filter (6) is vertically arranged, and the lower end of the filter (6) is rotationally fixed at the center of the bottom wall of the separating barrel (1).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202322939662.2U CN221084737U (en) | 2023-11-01 | 2023-11-01 | Organic silicon monomer and silicone oil production wastewater organic matter high-efficiency separation device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202322939662.2U CN221084737U (en) | 2023-11-01 | 2023-11-01 | Organic silicon monomer and silicone oil production wastewater organic matter high-efficiency separation device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN221084737U true CN221084737U (en) | 2024-06-07 |
Family
ID=91303192
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202322939662.2U Active CN221084737U (en) | 2023-11-01 | 2023-11-01 | Organic silicon monomer and silicone oil production wastewater organic matter high-efficiency separation device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN221084737U (en) |
-
2023
- 2023-11-01 CN CN202322939662.2U patent/CN221084737U/en active Active
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| GR01 | Patent grant |