CN201095604Y - Integral sewage treating device - Google Patents
Integral sewage treating device Download PDFInfo
- Publication number
- CN201095604Y CN201095604Y CNU2007201442118U CN200720144211U CN201095604Y CN 201095604 Y CN201095604 Y CN 201095604Y CN U2007201442118 U CNU2007201442118 U CN U2007201442118U CN 200720144211 U CN200720144211 U CN 200720144211U CN 201095604 Y CN201095604 Y CN 201095604Y
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- cylinder housing
- circuit cylinder
- hollow circuit
- sewage treating
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Abstract
The utility model discloses a device used for sewage treatment, in particular relates to an integral device which is formed by the combination of a traditional hydraulic vortex flow technique and a bubble flotation separation technique. The device is mainly composed of a hydrocyclone head, a hollow columnar shell body and a base, wherein, the sewage enters from the hydrocyclone head along the tangent direction and flows down rotatablely; the gas enters from an air inlet of the hollow columnar shell body and is divided into tiny bubbles by a hollow gas distribution pipe in the shell body; the tiny bubbles are cut by the sewage that flows down rotatablely and are fully mixed with the sewage, thereby improving the mixing efficiency largely. The device of the utility model is suitable for various devices for the sewage treatment and the mineral separation, more particularly used in middle-small devices.
Description
Technical field
The utility model is a kind of device that is used for sewage disposal, especially a kind of integrated apparatus that traditional waterpower cyclone technique and bubble flotation technology are combined and form.
Background technology
Traditional hydrocyclone is made up of a swirler head and a hollow circular cylinder that has the tangential direction material inlet.The swirler head is made up of the upflow tube of tangent line material inlet and hollow circular cylinder.Upflow tube has certain depth of penetration, and upflow tube has two functions: 1, as the fluidic guider, it will be become the high speed rotary fluid by the direct fluid that tangential direction enters.2, as the relief outlet of overflow.Rotary fluid is rotating along cylindrical tube wall and is flowing to the bottom and discharge from the bottom, because the action of centrifugal force of eddy flow, the heavy particle in water will be discharged from the bottom along tube wall, and particle that proportion is little and most water are then discharged from overflow port.Hydrocyclone also can be together in series and form the multiple-stage treatment system.
Traditional aeration mainly contains two kinds: the method for the method of nature and machinery.Aeration is mainly used to improve organic physicochemical property in the water, and it can be used for the organism in the water of decomposition, and simultaneously, it also can be used for removing the peculiar smell in anhydrating.After empty G﹠W mixed, volatile organic matter can be transferred in the gas phase by aeration and remove.Simultaneously, aeration can provide enough oxygen and carbonic acid gas, removes or reduces hydrogen sulfide or other gas that contains peculiar smell in the water.Elements such as the iron of aeration in also can oxidizing water, manganese, the carbon dioxide reaction in element such as the iron after the oxidation, manganese and the water generates the material of indissoluble, is removed by precipitation or filtering method again.
Developed a lot of equipment though utilize traditional hydrocyclone technology and traditional aeration process, and be widely used in the water treatment.But the effect that these equipment played is more single, and processing efficiency is not high yet, perhaps plays the effect of hydrocyclone, perhaps plays the effect of aeration.The equipment that does not also occur at present two kinds of technical tie-ups are got up and develop.
The utility model content
At the above-mentioned deficiency of prior art, technical problem to be solved in the utility model provides a kind of integrated sewage treating apparatus that hydrocyclone technology and bubble flotation technology are combined and form, to remedy the deficiencies in the prior art and defective.
In order to solve the problems of the technologies described above, the utility model is realized by the integrated apparatus that utilizes hydrocyclone technology and bubble flotation technology to develop.This integrated sewage treating apparatus, mainly constitute by swirler head, hollow circuit cylinder housing and base, the swirler head is positioned at the top of hollow circuit cylinder housing, and the swirler head is provided with the volatile matter outlet of vertical direction and the sewage inlet that links to each other with the swirler head with tangential direction; The swirler head is connected with stainless steel lathe dog or glue with the hollow circuit cylinder housing; The hollow circuit cylinder housing is provided with gas inlet, is provided with the hollow gas distribution tube in the hollow circuit cylinder housing, and the two ends of hollow circuit cylinder housing and hollow gas distribution tube are connected with silica gel makes its sealing; The hollow circuit cylinder lower part of frame is a base, and the hollow circuit cylinder housing is connected by stainless steel lathe dog or glue with base.
With respect to prior art, the utility model integrated sewage treating apparatus, its core component are to be made of a swirler head, a hollow circular cylinder and a base that has micropore air inlet layer.Waste water or slurry enter hollow circular cylinder with the high speed tangential direction and form the rotary fluid of high speed rotating, gas cuts into a large amount of micro-bubbles by micropore by the air inlet layer and by the rotary fluid of high speed rotating and mixes with rotary fluid, because the centrifugal action of high-speed rotational, particle is to the inwall high-speed motion of hollow gas distribution tube, and bubble is then to the central motion of hollow gas distribution tube.High speed relative movement between this particle and the bubble and highdensity bubbles volume have increased the collision rate between particle and the bubble greatly, thereby have improved flotation efficiency greatly.
The utility model integrated sewage treating apparatus also is a kind of aerating apparatus efficiently on the other hand.A large amount of bubbles that high pressure injects have improved the contact efficiency of gas and water, thereby have improved unit efficient greatly.
It also is conspicuous that the utility model integrated sewage treating apparatus has beneficial effect: 1, this device combines traditional water conservancy cyclone technique and bubble flotation technology, makes this device can play multiple action.2, this device uses unique hollow gas distribution tube, can make the air distribution that is pressed into become small bubble.3, this device unique cyclone device head design makes the waste water or the slurry that enter enter the rotary fluid that hollow posts forms high speed rotating with tangential direction, and cuts a large amount of micro-bubbles that are pressed into, and has improved mixing efficiency greatly.4, this device processing speed is fast, has greatly improved the processing efficiency of unit.5, this device uses wide, easy handling.
Description of drawings
Fig. 1 is a structural representation of the present utility model
Wherein: 1 is the volatile matter outlet; 2 is sewage inlet; 3 is gas inlet; 4 is the hollow gas distribution tube; 5 is base; 6 is the swirler head; 7 is tensimeter; 8 is the hollow circuit cylinder housing; 9 is stage body; 10 is that outer silk is gone up a section hollow circular cylinder; 11 are the following section hollow circular cylinder of internal thread.
Embodiment
The utility model is described in further detail below in conjunction with drawings and Examples.
As shown in Figure 1, in the integrated sewage treating apparatus of forming that hydrocyclone technology and bubble flotation technology are combined that the utility model one preferred embodiment provides, swirler head 6 is positioned at the top of hollow circuit cylinder housing 8, and the volatile matter outlet 1 of vertical direction and the sewage inlet 2 that links to each other with swirler head 6 main parts with tangential direction are arranged on the swirler head 6; Swirler head 6 is connected with hollow circuit cylinder housing 8 usefulness stainless steel lathe dog; Tensimeter 7 and gas inlet 3 are arranged on the hollow circuit cylinder housing 8, and hollow gas distribution tube 4 is contained in hollow circuit cylinder housing 8 the insides, and two of hollow circuit cylinder housing 8 and hollow gas distribution tube 4 is connected with silica gel makes its sealing; The bottom of hollow circuit cylinder housing 8 is a base 5, and hollow circuit cylinder housing 8 also is connected by stainless steel lathe dog with base 5.Base 5 upward cuts hollow circular cylinder 10 and the following section hollow circular cylinder 11 of internal thread by stage body 9, outer silk and forms.
In the present embodiment, 3cm in the hollow circuit cylinder housing 8 is stretched in the lower end of volatile matter outlet 1; The internal diameter of hollow circuit cylinder housing 8 is 75mm, and thickness is 3mm; Leave the space of 3mm between hollow circuit cylinder housing 8 and the hollow gas distribution tube 4; Stage body 9 is fixed together with following section hollow circular cylinder 11, and the height of stage body 9 is 30cm, and the diameter of upper and lower table top is 30mm.
In the present embodiment, the employed material of whole integrated sewage treating apparatus is stainless steel.
Below in conjunction with description of drawings principle of work of the present utility model.
As shown in Figure 1, waste water or slurry enter hollow circuit cylinder housing 8 and form the rotary fluid of high speed rotating from sewage inlet 2 with the high speed tangential direction, gas enters and cuts into a large amount of micro-bubbles by micropore by the air inlet layer and by the rotary fluid of high speed rotating from gas inlet 3, because the centrifugal action of high-speed rotational, particle is by the inwall high-speed motion of hollow gas distribution tube 4, and bubble is then to the central motion of hollow gas distribution tube 4.High speed relative movement between this particle and the bubble and highdensity bubbles volume have increased the collision rate between particle and the bubble greatly, thereby have improved flotation efficiency greatly.
Claims (8)
1, a kind of integrated sewage treating apparatus, it is characterized in that, this device mainly is made of swirler head, hollow circuit cylinder housing and base, the swirler head is positioned at the top of hollow circuit cylinder housing, and the swirler head is provided with the volatile matter outlet of vertical direction and the sewage inlet that links to each other with the swirler head with tangential direction; The swirler head is connected with stainless steel lathe dog or glue with the hollow circuit cylinder housing; The hollow circuit cylinder housing is provided with gas inlet, is provided with the hollow gas distribution tube in the hollow circuit cylinder housing, and the two ends of hollow circuit cylinder housing and hollow gas distribution tube are connected with silica gel makes its sealing; The hollow circuit cylinder lower part of frame is a base, and the hollow circuit cylinder housing is connected by stainless steel lathe dog or glue with base.
2, integrated sewage treating apparatus according to claim 1 is characterized in that: the hollow circuit cylinder housing is provided with tensimeter
3, integrated sewage treating apparatus according to claim 1 is characterized in that: 1～5cm in the hollow circuit cylinder housing is stretched in the lower end of volatile matter outlet.
4, integrated sewage treating apparatus according to claim 1 and 2 is characterized in that: the internal diameter of hollow circuit cylinder housing is 50～100mm, and thickness is 1～5mm.
5, integrated sewage treating apparatus according to claim 4 is characterized in that: the space of leaving 1mm～5mm between hollow circuit cylinder housing and the hollow gas distribution tube.
6, integrated sewage treating apparatus according to claim 1 is characterized in that: base upward cuts a hollow circular cylinder and the following section hollow circular cylinder of internal thread by stage body, outer silk and constitutes.
7, integrated sewage treating apparatus according to claim 6 is characterized in that: stage body is fixed together with a following section hollow circular cylinder, and the height of stage body is 10～50cm, and the diameter of upper and lower table top is 10～50mm.
8, integrated sewage treating apparatus according to claim 1 is characterized in that: this installs employed material is in plastics, stainless steel and the aluminium alloy one or more.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2007201442118U CN201095604Y (en) | 2007-09-28 | 2007-09-28 | Integral sewage treating device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2007201442118U CN201095604Y (en) | 2007-09-28 | 2007-09-28 | Integral sewage treating device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201095604Y true CN201095604Y (en) | 2008-08-06 |
Family
ID=39922660
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNU2007201442118U Expired - Lifetime CN201095604Y (en) | 2007-09-28 | 2007-09-28 | Integral sewage treating device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201095604Y (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107445327A (en) * | 2016-05-30 | 2017-12-08 | 上海京明环境科技有限公司 | A kind of integrated apparatus and method of waterpower collaboration flotation processing sewage |
| CN112934023A (en) * | 2016-03-16 | 2021-06-11 | 纳米及先进材料研发院有限公司 | System and method for generating oxidizing bubbles in a fluid |
-
2007
- 2007-09-28 CN CNU2007201442118U patent/CN201095604Y/en not_active Expired - Lifetime
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112934023A (en) * | 2016-03-16 | 2021-06-11 | 纳米及先进材料研发院有限公司 | System and method for generating oxidizing bubbles in a fluid |
| CN107445327A (en) * | 2016-05-30 | 2017-12-08 | 上海京明环境科技有限公司 | A kind of integrated apparatus and method of waterpower collaboration flotation processing sewage |
| CN107445327B (en) * | 2016-05-30 | 2020-11-17 | 上海京明环境科技有限公司 | Integrated device and method for treating sewage through hydraulic collaborative flotation |
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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: SHANGHAI FEIKAI PHOTOELECTRICITY MATERIALS CO., LT Free format text: FORMER OWNER: SHANGHAI FEINUOYA ENVIRONMENTAL TECHNOLOGY CO., LTD. Effective date: 20091016 |
|
| C41 | Transfer of patent application or patent right or utility model | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20091016 Address after: No. 169, GUI Qiao Road, Shanghai, Pudong New Area: 201206 Patentee after: Feikai Photoelectric Material Co., Ltd., Shanghai Address before: No. 169, GUI Qiao Road, Shanghai, Pudong New Area: 201206 Patentee before: Shanghai Feinuoya Environment Protection Technology Co., Ltd. |
|
| ASS | Succession or assignment of patent right |
Owner name: SHANGHAI PHICHEM CORPORATION Free format text: FORMER OWNER: FEIKAI PHOTOELECTRIC MATERIAL CO LTD, SHANGHAI Effective date: 20110509 |
|
| C41 | Transfer of patent application or patent right or utility model | ||
| COR | Change of bibliographic data |
Free format text: CORRECT: ADDRESS; FROM: 201206 NO. 169, GUIQIAO ROAD, PUDONG NEW DISTRICT, SHANGHAI TO: 201206 NO. 169, GUIQIAO ROAD, JINQIAO EXPORT PROCESSING ZONE, PUDONG NEW DISTRICT, SHANGHAI |
|
| TR01 | Transfer of patent right |
Effective date of registration: 20110509 Address after: 201206, 169 Jinqiao Road, Jinqiao Export Processing Zone, Shanghai, Pudong New Area Patentee after: Shanghai PhiChem Photoelectric Material Co., Ltd. Address before: 201206, No. 169, GUI Qiao Road, Shanghai, Pudong New Area Patentee before: Feikai Photoelectric Material Co., Ltd., Shanghai |
|
| CX01 | Expiry of patent term | ||
| CX01 | Expiry of patent term |
Granted publication date: 20080806 |