CN203212400U - Rotational flow centrifugal separation device - Google Patents
Rotational flow centrifugal separation device Download PDFInfo
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- CN203212400U CN203212400U CN 201320090771 CN201320090771U CN203212400U CN 203212400 U CN203212400 U CN 203212400U CN 201320090771 CN201320090771 CN 201320090771 CN 201320090771 U CN201320090771 U CN 201320090771U CN 203212400 U CN203212400 U CN 203212400U
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- eddy flow
- centrifugal separation
- flow centrifugal
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Abstract
The utility model provides a rotational flow centrifugal separation device which comprises a medicine dissolving box, a counter, a water pump, a solution mixing reactor, a solid-liquid distributor, a solid-liquid rotational flow centrifugal separator, a middle water collection tank or a solution collection tank, and a sewage collection tank, wherein the medicine outlet end of the medicine dissolving box is sequentially connected with the counter and the liquid inlet of the water pump; the liquid outlet of the water pump is connected with the solution mixing reactor; the solution mixing reactor, the solid-liquid distributor and the solid-liquid rotational flow centrifugal separator are sequentially connected; the solid-liquid rotational flow centrifugal separator is provided with a clear water or solution outlet end and a suspended matter or solid matter outlet end; the clear water or solution outlet end is connected with the middle water collection tank or the solution collection tank; the suspended matter or solid matter outlet end is connected with the sewage collection tank. The rotational flow centrifugal separation device is high in removing efficiency, short in reaction time, wide in use range, easy to clean and long in service life.
Description
Technical field
The utility model relates to sewage, wastewater treatment and solid-liquid separation processing technology field, particularly a kind of eddy flow centrifugal separation equipment.
Background technology
Environmental pollution is a global problem, the aggravation gradually along with industrial development, the middle of last century especially, the development of chemical industry, organism kinds and the quantity of synthetic grow with each passing day, and a lot of organism has intoxicating, teratogenesis, carcinogenic, mutagenesis to human, biology.It is difficult for by biological degradation, long-term accumulation in environment, the stable and united and people's of serious threat human society physical and mental health.
Because the wide material sources that the suspended substance of sewage, waste water and other solution, emulsion or colloidal solid thing are handled, chemistry, pharmacy, agricultural chemicals, medical science, metallurgy, plating, printing and dyeing, mining, petrochemical complex, rubbish draw fields such as percolate, in addition industries such as beverage, wine brewing, food-processing.Its kind, concentration, characteristic are different, the composition complexity.Therefore, need a kind of simple to operation, treatment effect good, running cost is low, the solid, liquid of the sewage, waste water and other solution that contain high concentration suspended matter, emulsion and colloidal solid thing of non-secondary pollution separates treatment facility at present.
Current sewage, method of wastewater treatment and equipment commonly used mainly contain:
One, chemical coagulation place technology:
Its advantage: chemical coagulation can be removed suspended particle and colloidalmaterial, and is easy to operate through the flotation of equipment post precipitation, technical maturity.Its shortcoming: the electrochemical treatment method can only be handled specific waste water, take up an area of many, efficient is low, energy consumption is big, running cost is high, easily cause secondary pollution.
Two, filter:
Its advantage: simple to operate, can from liquid, separate, remove suspended substance and colloidalmaterial effectively.Its shortcoming: suspended substance easily penetrates filtering layer, and emulsion and suspended substance accumulation easily produce walk or clay coating, stop up filtrate; Backwash is frequent, and water, gas loss are big.
Three, membrane sepn;
Its advantage: the rate of recovery (water rate/rate of recovery) height, suspended substance and colloidalmaterial and dissolved substance can be separated, be removed to stable water outlet effectively from liquid; Film can be changed separately, but plural serial stage peace through transport row.Its shortcoming: film easily pollutes and causes flux to reduce; And cleaning frequency height; Investment is big, and the running cost height cleans loaded down with trivial details.
All there are the restriction that is subjected to influent concentration in above technology of the prior art and method, and the working cost height, inapplicable contain high concentration suspended matter, emulsion and contain the colloidal solid thing sewage, waste water or other solution processing with separate.
The utility model content
At the above problem that exists in the prior art, the utility model proposes a kind of eddy flow centrifugal separation equipment, it removes the efficient height, the reaction times is short, use range is wide, and cleans simple, long service life.The technical scheme that the utility model adopts specifically is achieved in that
The utility model provides a kind of eddy flow centrifugal separation equipment, it comprises molten medicine-chest, gauger, water pump, the solution mixing reactor, solid-liquid cloth divides device, the solid-liquid cyclone centrifugal separator, middle water collecting basin or solution pool, collect dirty pond, the drug end of described molten medicine-chest is connected with the fluid inlet of described gauger and described water pump successively, the liquid outlet of described water pump connects described solution mixing reactor, described solution mixing reactor, described solid-liquid cloth divides device, described solid-liquid cyclone centrifugal separator connects successively, described solid-liquid cyclone centrifugal separator has clean water or taphole end and suspended substance or solid substance exit end, described cleaning or solution water exit end connect described middle water collecting basin or solution pool, and described suspended substance or solid substance exit end connect the dirty pond of described collection.
Preferably, also comprise wastewater disposal basin or the solution collecting tank that is connected with described water pump.
Preferably, plate or the frame that is used for a whole set of eddy flow centrifugation can be fixed by screw rod, hydraulic pressure or air pressure.
Adopt molten medicine-chest or need not dosing and carry out solid, liquid and separate when preferably, described eddy flow centrifugal separation equipment carries out medicine breakdown of emulsion, coagulation, flocculation at different solutions.
Preferably, the equipment such as spacer plate, frame or filter cloth in a whole set of eddy flow centrifugal separation equipment can be adjusted replacing.
Eddy flow centrifugal separation equipment of the present utility model has the efficient of removal height, the reaction times is short, use range is wide, schedule of operation is few, treatment effect is good, floor space is little, operation energy consumption is low, non-secondary pollution.For high concentration suspended matter, emulsion and contain in sewage, waste water and other solution processing craft of particulate matter, have do not stop up, easily assembling; Advantages such as cleaning is simple, long service life.
Description of drawings
Fig. 1 is the one-piece construction synoptic diagram of the eddy flow centrifugal separation equipment of the utility model specific embodiment.
Fig. 2 is the structural representation of the solid-liquid mixing tank in the eddy flow centrifugal separation equipment of the utility model specific embodiment.
Fig. 3 is the structural representation of the solid-liquid cyclone separator in the eddy flow centrifugal separation equipment of the utility model specific embodiment.
Embodiment
For above-mentioned purpose of the present utility model, feature and advantage can be become apparent more, below in conjunction with accompanying drawing embodiment of the present utility model is described in detail, it will be more clear making above-mentioned and other purpose, feature and advantage of the present utility model.Reference numeral identical in whole accompanying drawings is indicated identical part.Painstakingly do not draw accompanying drawing in proportion, focus on illustrating purport of the present utility model.
Fig. 1 is the one-piece construction synoptic diagram of the eddy flow centrifugal separation equipment of the utility model specific embodiment.Fig. 2 is the structural representation of the solid-liquid mixing tank in the eddy flow centrifugal separation equipment of the utility model specific embodiment.Fig. 3 is the structural representation of the solid-liquid cyclone separator in the eddy flow centrifugal separation equipment of the utility model specific embodiment.
Extremely shown in Figure 3 in conjunction with Fig. 1, the eddy flow centrifugal separation equipment of the utility model specific embodiment, it comprises molten medicine-chest 10, gauger 20, water pump 30, solution mixing reactor 40, solid-liquid cloth divides device 50, solid-liquid cyclone centrifugal separator 60, middle water collecting basin or solution pool 70, collect dirty pond 80, the drug end of molten medicine-chest 10 is connected with the fluid inlet of gauger 20 with water pump 30 successively, the liquid outlet of water pump 30 connects solution mixing reactor 40, solution mixing reactor 40, solid-liquid cloth divides device 50, solid-liquid cyclone centrifugal separator 60 connects successively, solid-liquid cyclone centrifugal separator 60 has clean water or taphole end 61 and suspended substance or solid substance exit end 62, water collecting basin or solution pool 70 in the middle of clean water or taphole end 61 connect, suspended substance or solid substance exit end 62 connect the dirty pond 80 of collection.
As shown in Figure 1, in the utility model specific embodiment, also comprise the wastewater disposal basin or the solution collecting tank that are connected with water pump 30, be used for depositing waste water or solution.In the utility model specific embodiment, the plate or the frame that are used for a whole set of eddy flow centrifugation can be fixed by screw rod, hydraulic pressure or air pressure; The eddy flow centrifugal separation equipment adopts molten medicine-chest or need not dosing and carry out solid, liquid and separate when carrying out medicine breakdown of emulsion, coagulation, flocculation at the character of different solutions;
A whole set of cyclone centrifugal separator is to divide device, solid-liquid cyclone centrifugal separator and filter cloth stack to form with polylith solution mixing reactor, solid-liquid cloth, small-sized treatment facility adopts screw rod to be connected and fixed, and the equipment that treatment capacity is big then utilizes hydraulic pressure or the fixedly connected one of air pressure.Equipment such as spacer plate, frame or filter cloth in a whole set of eddy flow centrifugal separation equipment can be adjusted replacing.
Fig. 2 is the structural representation of the solid-liquid mixing tank in the eddy flow centrifugal separation equipment of the utility model specific embodiment, the solid-liquid mixing tank is by viscose glue rule or irregular module in the groove of plate or frame among Fig. 2, both played guide functions, medicine breakdown of emulsion, flocculation, the coagulating agent of molten medicine-chest are fully mixed with solution, carry out adequate preparation for follow-up solid, liquid separates, itself and solid-liquid cyclone separator are connected.
Fig. 3 is the structural representation of the solid-liquid cyclone separator in the eddy flow centrifugal separation equipment of the utility model specific embodiment, the solid-liquid cyclone separator is that groove by plate or frame is connected with the solid-liquid mixing tank among Fig. 3, the selected filter cloth of the handled medium of root jade pendant or filter screen are separated by between plate or the frame, solution is under solid-liquid mixing tank and solid-liquid cyclone separator water conservancy diversion, produce centrifugal force through the pressure high speed rotating of pump, realize gravity separation.Solid matter enters the dirty pond of collection with the groove following current of plate or frame, and the solution of water or needs penetrates filter cloth or filter screen is gone into water collecting basin along the concentrated flow of plate or frame another side.
In the utility model specific embodiment, molten medicine-chest 10 is used for adding medicament automatically, and the drug end of molten medicine-chest 10 is connected with the valve of control and metered doses of medicament flow and the fluid inlet of gauger 20 and water pump 30; Being used for aspiration medicinal liquid is connected with solution mixing reactor 40 with sewage, waste water or solution to the water pump 30 in solid-liquid processing, the separating device; Solid-liquid sparger 50 is connected with the solid-liquid cyclone centrifugal separator 60 of multistage eddy flow cutting; The multistage eddy flow cutting of solid-liquid cyclone centrifugal separator 60, clean water or the taphole end 61 after the centrifugation are connected with middle water collecting basin or solution pool 70; Through the multistage eddy flow cutting of solid-liquid cyclone centrifugal separator 60, suspended substance after the centrifugation or solid substance exit end 62 with collect dirty pond 80 and be connected.
Eddy flow centrifugal separation equipment of the present utility model can carry out solid-liquid separation to high concentration suspended matter, emulsion and the sewage, waste water or other solution that contain the colloidal solid thing to be handled.
Through experimental test, eddy flow centrifugal separation equipment of the present utility model is when oil chemistry emulsifying liquid waste water CODcr concentration 200, when 000mg/L, grease concentration 〉=4500mg/L, the clearance of CODcr and grease is respectively 99.98% and 99.95%, emulsion splitter is common flocculation agent, need not to heat, add acid, add Gao Fen Tight and coagulate agent, the recyclable utilization of waste oil.
Liquor wine liquid separates with vinasse and need not to add coagulating agent and can obtain desirable pure mellow wine liquid.
Mud moment concentrates, and need not concentration basin, saves a large amount of soil and construction investment.
Eddy flow centrifugal separation equipment of the present utility model can handle poisonous, the harmful organic waste water that contains the difficult suspended substance that decomposes of emulsifying liquid waste water, the high density of high-concentration hardly-degradable, contain granular turbidity current water and all contain the liquid of suspended substance, problems such as such water treating equipment investment is big, energy consumption is high, limitation is strong, treatment effect is undesirable have been solved, and do not produce by product, non-secondary pollution.Go for the solid, liquid separation of industries such as liquor, sugar industry, fruit processing, drink and food processing and the purification of other industry simultaneously.
Eddy flow centrifugal separation equipment of the present utility model has the efficient of removal height, the reaction times is short, use range is wide, schedule of operation is few, treatment effect is good, floor space is little, operation energy consumption is low, non-secondary pollution.For high concentration suspended matter, emulsion and contain in sewage, waste water and other solution processing craft of particulate matter, have do not stop up, easily assembling; Advantages such as cleaning is simple, long service life.
In above description, a lot of details have been set forth so that fully understand the utility model.But above description only is preferred embodiment of the present utility model, and the utility model can be implemented much to be different from alternate manner described here, so the utility model is not subjected to the restriction of top disclosed concrete enforcement.Any skilled personnel are not breaking away under the technical solutions of the utility model scope situation simultaneously, all can utilize method and the technology contents of above-mentioned announcement that technical solutions of the utility model are made many possible changes and modification, or be revised as the equivalent embodiment of equivalent variations.Every content that does not break away from technical solutions of the utility model according to any simple modification, equivalent variations and the modification that technical spirit of the present utility model is done above embodiment, all still belongs in the scope of technical solutions of the utility model protection.
Claims (5)
1. eddy flow centrifugal separation equipment, it is characterized in that, comprise molten medicine-chest, gauger, water pump, the solution mixing reactor, solid-liquid cloth divides device, the solid-liquid cyclone centrifugal separator, middle water collecting basin or solution collecting tank, collect dirty pond, the drug end of described molten medicine-chest is connected with the fluid inlet of described gauger and described water pump successively, the liquid outlet of described water pump connects described solution mixing reactor, described solution mixing reactor, described solid-liquid cloth divides device, described solid-liquid cyclone centrifugal separator connects successively, described solid-liquid cyclone centrifugal separator has clean water or taphole end and suspended substance or solid substance exit end, described clean water or taphole end connect described middle water collecting basin or solution collecting tank, and described suspended substance or solid substance exit end connect the dirty pond of described collection.
2. eddy flow centrifugal separation equipment as claimed in claim 1 is characterized in that, also comprises the wastewater disposal basin or the solution pool that are connected with described water pump.
3. eddy flow centrifugal separation equipment as claimed in claim 1 is characterized in that, the plate or the frame that are used for a whole set of eddy flow centrifugation can be fixed by screw rod, hydraulic pressure or air pressure.
4. eddy flow centrifugal separation equipment as claimed in claim 1 is characterized in that, described eddy flow centrifugal separation equipment adopts molten medicine-chest or need not dosing and carry out solid, liquid and separate when carrying out medicine breakdown of emulsion, coagulation, flocculation at different solutions.
5. eddy flow centrifugal separation equipment as claimed in claim 1 is characterized in that, the equipment such as spacer plate, frame or filter cloth in a whole set of eddy flow centrifugal separation equipment can be adjusted replacing.
Priority Applications (1)
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CN 201320090771 CN203212400U (en) | 2013-02-28 | 2013-02-28 | Rotational flow centrifugal separation device |
Applications Claiming Priority (1)
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CN 201320090771 CN203212400U (en) | 2013-02-28 | 2013-02-28 | Rotational flow centrifugal separation device |
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CN203212400U true CN203212400U (en) | 2013-09-25 |
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CN 201320090771 Expired - Fee Related CN203212400U (en) | 2013-02-28 | 2013-02-28 | Rotational flow centrifugal separation device |
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103111103A (en) * | 2013-02-28 | 2013-05-22 | 闵方权 | Rotational flow centrifugal separation device |
CN105833569A (en) * | 2016-04-27 | 2016-08-10 | 长春工业大学 | Outer rotational flow limited flow channel membrane separator and method for demulsifying emulsion membrane through same |
-
2013
- 2013-02-28 CN CN 201320090771 patent/CN203212400U/en not_active Expired - Fee Related
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103111103A (en) * | 2013-02-28 | 2013-05-22 | 闵方权 | Rotational flow centrifugal separation device |
CN105833569A (en) * | 2016-04-27 | 2016-08-10 | 长春工业大学 | Outer rotational flow limited flow channel membrane separator and method for demulsifying emulsion membrane through same |
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CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20130925 Termination date: 20160228 |
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CF01 | Termination of patent right due to non-payment of annual fee |