CN204265505U - Balanced vortex mixed reactor - Google Patents
Balanced vortex mixed reactor Download PDFInfo
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- CN204265505U CN204265505U CN201420589321.5U CN201420589321U CN204265505U CN 204265505 U CN204265505 U CN 204265505U CN 201420589321 U CN201420589321 U CN 201420589321U CN 204265505 U CN204265505 U CN 204265505U
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Abstract
The utility model discloses a kind of balanced vortex mixed reactor, comprise and establish meshed waffle slab, at least one epitaxial lateral overgrowth of described mesh stretches the ennation forming taper, and this ennation has the inwall making current form venturi effect.This apparatus structure is simple, and taper ennation is conducive to guiding current flowing, improves flow rate of water flow; Its inwall can make the current flowing through ennation form vortex fast, make former water and flocculation medicament sufficient reacting, impel the molecule in former water and muddy impurity to form even, closely knit particle fast, its proportion is increased the weight of, after finally entering current stabilization district balance, enter settling region rapid precipitation; Vortex effect is more than 5 times of traditional micro-vortex effect, substantially increases flocculation mixing efficiency; Venturi effect adds the effect of pyramidal structure, forms a thrust of advancing to current, effectively improves flow rate of water flow, substantially increase purification efficiency.
Description
Technical field
The utility model belongs to water treatment field, especially relates to a kind of balanced vortex mixed reactor for flocculation zone.
Background technology
In existing water treatment in process, flocculation reaction is one of very important cell process, the reaction efficiency of flocculation process and thoroughness directly affect engineering construction investment and engineering operation cost, directly have influence on the treatment effect of subsequent technique simultaneously, finally have influence on effluent quality.
In existing water technology, flocculation efficiency is low, and long reaction time, effect is not ideal enough, causes a large amount of waste simultaneously, increase running cost to medicine.Occurred the flocculation tank of some micro-vortexs in the market, such as, by arranging whipping appts to improve flocculation efficiency, the operation of whipping appts, can increase energy consumption, improve production cost; Or by arranging some flaps, current are made to form certain micro-vortex effect, to improve flocculation efficiency, the improvement of this form, structure is general comparatively complicated, and just forms small vortex effect, although flocculation efficiency slightly improves, but the overall flow velocity of current does not improve, also cannot effectively change overall purification efficiency.
Utility model content
The utility model, in order to overcome the deficiencies in the prior art, provides that a kind of structure is simple, flocculation efficiency is high and contributes to improving the balanced vortex mixed reactor of flow velocity.
To achieve these goals, the utility model is by the following technical solutions: a kind of balanced vortex mixed reactor, comprise and establish meshed waffle slab, at least one epitaxial lateral overgrowth of described mesh stretches the ennation forming taper, and this ennation has the inwall making current form venturi effect.This apparatus structure is simple, and taper ennation is conducive to guiding current flowing, improves flow rate of water flow; Its inwall can make the current flowing through ennation form vortex fast, make former water and flocculation medicament sufficient reacting, impel the molecule in former water and muddy impurity to form even, closely knit particle fast, its proportion is increased the weight of, after finally entering current stabilization district balance, enter settling region rapid precipitation; Moreover because ennation has certain length, the vortex effect formed in current and ennation is fairly obvious, greatly, vortex effect is more than 5 times of traditional micro-vortex effect to vorticity, substantially increases flocculation mixing efficiency; Venturi effect adds the effect of pyramidal structure, forms a thrust of advancing to current, effectively improves flow rate of water flow, substantially increase purification efficiency.
As preferably, described ennation has spiral helicine inwall.Spiral helicine inwall, makes the current flowing through ennation form obvious whirlpool along working direction, impels the molecule in current and muddy impurity to form even, closely knit particle fast, its proportion is increased the weight of, and accelerates flow velocity.
Further, described ennation is crisscross arranged both sides before and after mesh; Be crisscross arranged, there is when ensure that minimum ennation preferably cyclonic effect.
Further, described in the ennation be positioned on front side of mesh have and be beneficial to current and flow into and the front enlarging forming vortex, described in the ennation be positioned on rear side of mesh have and be beneficial to current and discharge and the rear enlarging forming vortex.Current are just preparing to enter this device, by the setting of front enlarging, contribute to assembling, drawing current in, current are rapidly flowed toward in the ennation of front side, and discharges mesh after forming whirlpool; And be positioned at rear enlarging on rear side of mesh towards the expansion of current circulating direction and arrange, form a similar effect of opening a sluice gate to current, current are discharged from rear enlarging at a high speed along with vortex, increase flow velocity further, improve flocculation efficiency and overall flocculating effect.
In sum, the utility model has the following advantages: 1) one-piece construction is simple, stable; 2) current can be made to form obvious vortex effect, impel the molecule in current and muddy impurity to form even, closely knit particle fast; 3) taper structure design and vortex effect contribute to improving flow rate of water flow, improve overall purification efficiency.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
Fig. 2 is another kind of structural representation of the present utility model.
Fig. 3 is another structural representation of the present utility model.
Embodiment
In order to make those skilled in the art person better understand the utility model scheme, below in conjunction with the accompanying drawing in the utility model embodiment, clear, complete description is carried out to the technical scheme in the utility model embodiment.
As Figure 1-3, a kind of balanced vortex mixed reactor, comprises waffle slab 3, during use, is disposed on respectively in filtering basin by multi-disc waffle slab 3; Waffle slab is distributed with the mesh 2 that the former current of multiple confession are logical, after the mesh that the molecule in former water and muddy impurity are arranged by these multilayers, flocculation forms even, closely knit particle gradually; In order to improve flocculation efficiency, at least one for mesh 2 epitaxial lateral overgrowth is stretched the ennation 21 forming taper, as shown in Figure 2, can only on front side of mesh or rear side formed ennation 21, also can be respectively form an ennation in the both sides, front and back of each mesh, specifically as shown in Figure 3; Ennation 21 has the inwall 211 making current form venturi effect, and as inwall 211 is arranged to spiral grooves, and the rotation direction being located at the spiral grooves of both sides before and after mesh is consistent, namely makes the vortex sense of rotation of formation in the ennation of front and back consistent; This inwall can make former water current form obvious venturi effect, flocculates into closely knit particle fast to molecule with muddy impurity; Because ennation is pyramidal structure, contribute to being formed more significantly venturi effect, virtually also greatly accelerate former water flow velocity, improve overall decontamination effect improving.
And in the present embodiment, described ennation 21 is crisscross arranged both sides before and after mesh, as shown in Figure 1, arrow represents former water circulating direction, namely wherein the front side of certain mesh is provided with ennation, the mesh be adjacent then is provided with ennation at rear side, and the ennation 21 be positioned on front side of mesh has and is beneficial to current and flows into and the front enlarging 212 forming vortex, the ennation 21 be positioned on rear side of mesh has and is beneficial to current and discharges and the rear enlarging 213 forming vortex, before and after enlarging be arranged so that the oral area of ennation is horn-like, front enlarging is conducive to gathering former water, more be conducive to forming vortex effect fast, rear enlarging is the expansion of former water discharge direction, is conducive to former water and discharges fast, increases flow velocity.
Obviously, described embodiment is only a part of embodiment of the present utility model, instead of whole embodiments.Based on the embodiment in the utility model, those of ordinary skill in the art are not making the every other embodiment obtained under creative work prerequisite, all should belong to the scope of the utility model protection.
Claims (4)
1. a balanced vortex mixed reactor, comprise the waffle slab (3) being provided with mesh (2), it is characterized in that: described mesh (2) at least one epitaxial lateral overgrowth stretches to be formed the ennation (21) of taper, this ennation (21) has the inwall (211) making current form venturi effect.
2. balanced vortex mixed reactor according to claim 1, is characterized in that: described ennation (21) has spiral helicine inwall (211).
3. balanced vortex mixed reactor according to claim 1, is characterized in that: described ennation is crisscross arranged both sides before and after mesh.
4. balanced vortex mixed reactor according to claim 1, it is characterized in that: described in the ennation (21) be positioned on front side of mesh have and be beneficial to current and flow into and the front enlarging (212) forming vortex, described in the ennation (21) be positioned on rear side of mesh have and be beneficial to current and discharge and the rear enlarging (213) forming vortex.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420589321.5U CN204265505U (en) | 2014-10-13 | 2014-10-13 | Balanced vortex mixed reactor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420589321.5U CN204265505U (en) | 2014-10-13 | 2014-10-13 | Balanced vortex mixed reactor |
Publications (1)
| Publication Number | Publication Date |
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| CN204265505U true CN204265505U (en) | 2015-04-15 |
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| CN201420589321.5U Active CN204265505U (en) | 2014-10-13 | 2014-10-13 | Balanced vortex mixed reactor |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109020026A (en) * | 2018-08-18 | 2018-12-18 | 陈立波 | A kind of processing pond of oil-containing sanitary sewage |
| CN113149169A (en) * | 2021-04-30 | 2021-07-23 | 浙江联池水务设备股份有限公司 | Modular reaction flocculator for water treatment and manufacturing method |
| CN114906911A (en) * | 2022-05-07 | 2022-08-16 | 中铁第一勘察设计院集团有限公司 | Flow self-adaptation reaction formula vortex flocculation system |
| CN117069348A (en) * | 2023-10-17 | 2023-11-17 | 南通东来冶金装备有限公司 | High-efficient turbid water purifier |
-
2014
- 2014-10-13 CN CN201420589321.5U patent/CN204265505U/en active Active
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109020026A (en) * | 2018-08-18 | 2018-12-18 | 陈立波 | A kind of processing pond of oil-containing sanitary sewage |
| CN113149169A (en) * | 2021-04-30 | 2021-07-23 | 浙江联池水务设备股份有限公司 | Modular reaction flocculator for water treatment and manufacturing method |
| CN113149169B (en) * | 2021-04-30 | 2024-02-23 | 浙江联池水务设备股份有限公司 | Modular reaction flocculator for water treatment and manufacturing method |
| CN114906911A (en) * | 2022-05-07 | 2022-08-16 | 中铁第一勘察设计院集团有限公司 | Flow self-adaptation reaction formula vortex flocculation system |
| CN114906911B (en) * | 2022-05-07 | 2024-02-27 | 中铁第一勘察设计院集团有限公司 | Flow self-adaptive counterattack type vortex flocculation system |
| CN117069348A (en) * | 2023-10-17 | 2023-11-17 | 南通东来冶金装备有限公司 | High-efficient turbid water purifier |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| ASS | Succession or assignment of patent right |
Owner name: ZHEJIANG LIANCHI WATER EQUIPMENT CO., LTD. Free format text: FORMER OWNER: CHI WANQING Effective date: 20150710 |
|
| C41 | Transfer of patent application or patent right or utility model | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20150710 Address after: Yuhang District, Hangzhou City, Zhejiang Province, 310000 West No. 1500 Building 2 room 413 Patentee after: Zhejiang Lianchi Water Equipment Co., Ltd. Address before: Taizhou City, Zhejiang province 317605 Ring Road No. 20-3 Truman town of Yuhuan County Patentee before: Chi Wanqing |
|
| C56 | Change in the name or address of the patentee | ||
| CP01 | Change in the name or title of a patent holder |
Address after: Yuhang District, Hangzhou City, Zhejiang Province, 310000 West No. 1500 Building 2 room 413 Patentee after: Zhejiang pool water equipment Limited by Share Ltd Address before: Yuhang District, Hangzhou City, Zhejiang Province, 310000 West No. 1500 Building 2 room 413 Patentee before: Zhejiang Lianchi Water Equipment Co., Ltd. |
|
| CP02 | Change in the address of a patent holder |
Address after: Room 407, building 18, No. 998, Wenyi West Road, Yuhang District, Hangzhou City, Zhejiang Province 310000 Patentee after: ZHEJIANG LIANCHI WATER EQUIPMENT STOCK Co.,Ltd. Address before: Room 413, building 2, 1500 Wenyi West Road, Yuhang District, Hangzhou City, Zhejiang Province 310000 Patentee before: ZHEJIANG LIANCHI WATER EQUIPMENT STOCK Co.,Ltd. |
|
| CP02 | Change in the address of a patent holder |