CN103272414A - Alcohol waste pulse quick precipitator - Google Patents
Alcohol waste pulse quick precipitator Download PDFInfo
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- CN103272414A CN103272414A CN2013102498515A CN201310249851A CN103272414A CN 103272414 A CN103272414 A CN 103272414A CN 2013102498515 A CN2013102498515 A CN 2013102498515A CN 201310249851 A CN201310249851 A CN 201310249851A CN 103272414 A CN103272414 A CN 103272414A
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Abstract
The invention discloses an alcohol waste pulse quick precipitator; a water supply chamber, a pulse region, a water distribution downcomer, a buffering plate and a sludge collecting region are sequentially arranged at the center part of a cylinder body from the top down, a water inlet pipe is connected to the side edge of the water supply chamber, a pulse deep is arranged inside the water supply chamber, a center siphon pipe extending to the pulse region is arranged below the pulse deep, the top of the pulse deep is in pipe connection with an extraction pipe and a siphonic damage pipe which are communicated with each other, and an exhaust pipe communicated with the pulse region is arranged inside the water supply room; the bottom of the pulse region is connected with the water distribution downcomer, a settling zone is arranged on the outer side of the water distribution downcomer, the buffering plate is arranged at the bottom of the water distribution downcomer, the sludge collecting region is arranged below the buffering plate, and a blow-off pipe is arranged at the bottom of the sludge collecting region; and a water outlet slot, a water outlet header tank and a water outlet which are communicated with one another are arranged at the top of the cylinder body. The alcohol waste pulse quick precipitator provided by the invention has the advantages that the settling effect is excellent, the problem of solid-liquid separation of high-concentration alcohol sediment is solved, and the phenomenon of coking is avoided.
Description
Technical field
The present invention relates to alcohol effluent sediment and liquid Separation of Solid and Liquid treating apparatus, specifically is a kind of alcohol effluent pulse accelerated clarifier.
Background technology
General tilted plate separator commonly used or the natural pond type settling apparatus of adopting of Alcohol Production enterprise carries out the Separation of Solid and Liquid processing to alcohol effluent sediment and liquid at present, the milky colloidal precipitation thing that contains in the alcohol effluent causes serious coking in concentration process, wasted the cost of a large amount of heat energy losses and cleaning concentration tank, but also causing the serious consequence of secondary environmental pollution, present whole Alcohol Production enterprise feels headache and insurmountable thorny problem to this phenomenon.
Summary of the invention
Technical problem to be solved by this invention provides the good alcohol effluent pulse accelerated clarifier of a kind of sedimentation effect, can be the sediment Separation of Solid and Liquid in the alcohol effluent by this equipment, the sediment of separating can mix coal boiler of feeding burning together, produce heat energy, liquid can qualified discharge after carrying out biochemical treatment.
The present invention solves the problems of the technologies described above with following technical scheme:
Alcohol effluent pulse accelerated clarifier of the present invention, comprise stack shell, the centre of stack shell from top to bottom is provided with successively to hydroecium, pulse area, the water distribution down-comer, cushioning fender, Ji Wuniqu, separate for the bottom of hydroecium through space bar and pulse area, connect water inlet pipe for the side of hydroecium, the indoor longitudinal section that is provided with of feeding water is inverted U-shaped pulse Tan, the below of pulse Tan is provided with the central siphon pipe that stretches into pulse area, the top of pulse Tan is connected with exhaust tube and the siphon destructing tube that communicates by pipeline, the length of exhaust tube is greater than the length of siphon destructing tube and stretch into pulse area, and the indoor blast pipe that communicates with pulse area that is provided with feeds water; The bottom of pulse area connects the water distribution down-comer, and the LHA of water distribution down-comer is the settling zone, and the bottom of water distribution down-comer is provided with cushioning fender, and the below of cushioning fender is Ji Wuniqu, and the bottom of Ji Wuniqu is provided with blow-off pipe; The top of stack shell is provided with effluent trough, water outlet header tank and the delivery port that communicates.
At the bottom of described Ji Wuniqu was the back taper tube, collection mud was equipped with several uniform dregs-separating devices of arranging in the district.
Described dregs-separating device is that the prismatic body by up and down two symmetry arrangement combinations constitutes, and the tip of two prismatic bodies arranges respectively up and down.
Described stack shell bottom is provided with inspection opening.
Be connected on the described discharge pipeline and help washing pipe.
Described effluent trough comprises interior annular effluent trough, exterior annular effluent trough and the strip effluent trough that connects interior annular effluent trough and exterior annular effluent trough.
The present invention is by adopting bell-type pulse sedimentation-separation technology, with alcohol effluent Separation of Solid and Liquid again.From molasses tangerine pond, pumping in the pulse precipitation apparatus, waste liquid enters from the equipment top, dive from top to down, utilize the effect of underriding power, most of sediment is deposited to collection mud device, again through countercurrent depressurization rise help heavy, utilize the pulse spacing, sedimentation and do not form fluctuation, separate through the benign cycle of equipment, make to go out the water deposit clearance after the processing and reach more than 98%.
Alcohol effluent pulse accelerated clarifier of the present invention has the following advantages:
1. effectively remove the sediment in the alcohol effluent, guarantee concentration tank is not formed coking phenomenon.
2. equipment is installed regularly blowdown magnetic valve, and operation can not interrupted; Simple to operate, operating cost is low, need not the personal management.
3. present device is higher more than 80% than the effect of settling of the general tilted plate separator of using always and natural pond type settling apparatus, thoroughly solved the difficult problem of alcohol in high concentration sediment Separation of Solid and Liquid, for Alcohol Production enterprise had both created economic benefit, contribute for reducing the environmental pollution discharging again.
Description of drawings
Fig. 1 is structural representation of the present invention.
Fig. 2 is the schematic top plan view of Fig. 1.
Among the figure: water inlet pipe 1, give hydroecium 2, blast pipe 3, pulse cover 4, siphon destructing tube 5, exhaust tube 6, pulse area 7, water outlet header tank 8, delivery port 9, space bar 10, interior annular effluent trough 11, central siphon pipe 12, stack shell 13, water distribution down-comer 14, settling zone 15, dregs-separating device 16, help washing pipe 17, blow-off pipe 18, support angle steel 19, collection mud district 20, buffering plate washer 21, support channel-section steel 22, feet 23, inspection opening 24, bar shaped effluent trough 25, exterior annular effluent trough 26.
The specific embodiment
As shown in drawings; Alcohol effluent pulse accelerated clarifier of the present invention mainly is made of pulse area 7 and settling zone 15 and collection mud district 20, for the centre of cylindrical stack shell 13 from top to bottom is provided with successively to hydroecium 2, pulse area 7, water distribution down-comer 14, cushioning fender 21, collection mud district 20, separate for the bottom of hydroecium 2 through space bar 10 and pulse area 7, connect water inlet pipe 1 for the side of hydroecium 2, be inverted U-shaped pulse Tan 4 to being provided with the longitudinal section in the hydroecium 2, the below of pulse Tan 4 is provided with the central siphon pipe 12 that stretches into pulse area 7, the top of pulse Tan 4 is connected with exhaust tube 6 and the siphon destructing tube 5 that communicates by pipeline, the length of exhaust tube 6 maintains an equal level mutually greater than the length of siphon destructing tube 5 and the bottom of stretching into pulse area 7 and central siphon pipe 12, gives in the hydroecium 2 and is provided with the blast pipe 3 that communicates with pulse area 7; The bottom of pulse area 7 connects water distribution down-comer 14, and the LHA of water distribution down-comer 14 is settling zone 15, and the bottom of water distribution down-comer 14 is provided with cushioning fender 21, and cushioning fender 21 and water distribution down-comer 14 are by supporting channel-section steel 22 support fixation; The below of cushioning fender 21 is the collection mud district 20 at the bottom of the back taper tube.For the ease of deslagging, alleviate the shock wave of spoil disposal, 20 are equipped with several uniform dregs-separating devices 16 of arranging in collection mud district, dregs-separating device 16 is made of the prismatic body of two symmetry arrangement combinations up and down, the tip of two prismatic bodies arranges respectively up and down, and dregs-separating device 16 is by supporting angle steel 19 support fixation.The bottom in collection mud district 20 is provided with blow-off pipe 18; The strip effluent trough 25 that the top of stack shell 13 is provided with interior annular effluent trough 11, exterior annular effluent trough 26 and connects interior annular effluent trough 11 and exterior annular effluent trough 6, exterior annular effluent trough 26 is connected with water outlet header tank 8, and water outlet header tank 8 is provided with delivery port 9; The bottom of stack shell is provided with the feet 23 that supports entire equipment and the inspection opening 24 that is used for watching inner case, is connected on the discharge pipeline 18 and helps washing pipe 17.
During use, alcohol effluent rotates into to hydroecium 2 through water inlet pipe 1, water level progressively rises, inner air tube enters pulse area 7 by exhaust tube 6, again by blast pipe 3 to the stack shell outside drain, the top that rises to pulse cover 4 when water level produces negative pressure, when water level surpasses central siphon pipe 12 certain altitudes (sealing), waste liquid just flows out and the formation siphon from central siphon pipe 12, and waste liquid is sucked water distribution down-comer 14, flows to settling zone 15 through cushioning fender 20; When water level drops to when being lower than siphon destructing tube 5, from siphon destructing tube 5 inhaled airs the vacuum tube of central siphon pipe 12 is destroyed, central siphon pipe 12 just again the siphon waste liquid form and dam, liquid level is rising gradually again; Go round and begin again.Per pulse period is about 45 seconds/time.Guarantee that the pulse water yield reaches equipment design treating capacity; Fill benefit discontinuously, settling zone 15 is not formed fluctuation, precipitating sludge is evenly sunk.The mud that sinks is concentrated to mud district 20 and is discharged to collect in the mud sump through discharge pipeline 18 and further handles.As run into when stopping up, help towards blowdown from helping washing pipe 17 with the waste liquid that has pressure.
The present invention makes the waste liquid water flow section sudden enlargement through buffer board 21 by buffer board 21 is set, and the sediment that sinks to collection mud district 20 is not formed and destroys.All the time water content is not too high to guarantee sediment.
And waste liquid enters into settling zone 15 through cushioning fender 21, and it is moved up and down regularly, is conducive to sediment collision cohesion, and uniform settlement is avoided the partial penetration phenomenon, and plays a part to filter the same; Waste liquid slowly rises to interior annular effluent trough 11, strip effluent trough 25 and exterior annular effluent trough 26 after through settling zone 15, flows to water outlet header tank 8 again and delivers to through delivery port 9 and concentrate the workshop and carry out concentration.So just realize rapid subsidence processing effect.
The present invention has installed a periodical blowdown magnetic valve normally in service in the blow-off pipe 18, set blowing period and blowing time, guarantees not influence the operation of equipment continuity and without the personal management.
Internals of the present invention all adopts welding manner fastening; Be conducive to the stability moved and easy to maintenance like this.
Claims (6)
1. alcohol effluent pulse accelerated clarifier, comprise stack shell, it is characterized in that, the centre of stack shell from top to bottom is provided with successively to hydroecium, pulse area, the water distribution down-comer, cushioning fender, Ji Wuniqu, separate for the bottom of hydroecium through space bar and pulse area, connect water inlet pipe for the side of hydroecium, the indoor longitudinal section that is provided with of feeding water is inverted U-shaped pulse Tan, the below of pulse Tan is provided with the central siphon pipe that stretches into pulse area, the top of pulse Tan is connected with exhaust tube and the siphon destructing tube that communicates by pipeline, the length of exhaust tube is greater than the length of siphon destructing tube and stretch into pulse area, and the indoor blast pipe that communicates with pulse area that is provided with feeds water; The bottom of pulse area connects the water distribution down-comer, and the LHA of water distribution down-comer is the settling zone, and the bottom of water distribution down-comer is provided with cushioning fender, and the below of cushioning fender is Ji Wuniqu, and the bottom of Ji Wuniqu is provided with blow-off pipe; The top of stack shell is provided with effluent trough, water outlet header tank and the delivery port that communicates.
2. according to the described alcohol effluent pulse of claim 1 accelerated clarifier, it is characterized in that at the bottom of described Ji Wuniqu was the back taper tube, collection mud was equipped with several uniform dregs-separating devices of arranging in the district.
3. according to the described alcohol effluent pulse of claim 2 accelerated clarifier, it is characterized in that described dregs-separating device is that the prismatic body by up and down two symmetry arrangement combinations constitutes, the tip of two prismatic bodies arranges respectively up and down.
4. according to the described alcohol effluent pulse of claim 1 accelerated clarifier, it is characterized in that described stack shell bottom is provided with inspection opening.
5. according to the described alcohol effluent pulse of claim 1 accelerated clarifier, it is characterized in that, be connected on the described discharge pipeline and help washing pipe.
6. according to the described alcohol effluent pulse of claim 1 accelerated clarifier, it is characterized in that described effluent trough comprises interior annular effluent trough, exterior annular effluent trough and the strip effluent trough that connects interior annular effluent trough and exterior annular effluent trough.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201310249851.5A CN103272414B (en) | 2013-06-21 | 2013-06-21 | Alcohol waste pulse quick precipitator |
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| Application Number | Priority Date | Filing Date | Title |
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| CN201310249851.5A CN103272414B (en) | 2013-06-21 | 2013-06-21 | Alcohol waste pulse quick precipitator |
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| CN103272414A true CN103272414A (en) | 2013-09-04 |
| CN103272414B CN103272414B (en) | 2015-04-01 |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104857745A (en) * | 2015-03-12 | 2015-08-26 | 广西农垦糖业集团星星制糖有限公司 | Continuous precipitator |
| CN106075968A (en) * | 2016-08-11 | 2016-11-09 | 铁道第三勘察设计院集团有限公司 | A kind of spiral-flow type spiral settler of automatic control system spoil disposal |
| CN106110720A (en) * | 2016-08-11 | 2016-11-16 | 铁道第三勘察设计院集团有限公司 | A kind of waterpower controls siphon-type full-automatic cyclone sediment device |
| CN106267918A (en) * | 2016-09-06 | 2017-01-04 | 云南文山铝业有限公司 | Purifier |
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| CN2102308U (en) * | 1991-04-30 | 1992-04-22 | 广西贵港甘蔗化工厂 | White water separator of paper production |
| CN1061633A (en) * | 1991-04-30 | 1992-06-03 | 广西贵港甘蔗化工厂 | Mthod of white water from paper making separating technology and equipment |
| JP2002058913A (en) * | 2000-08-22 | 2002-02-26 | Nishihara Environ Sanit Res Corp | Solid-liquid separator having stirring flow forming means |
| JP2003019403A (en) * | 2001-07-10 | 2003-01-21 | Yoshikimi Watanabe | Jet stirring type solid-liquid separation apparatus |
| CN201082875Y (en) * | 2007-08-24 | 2008-07-09 | 宜兴市清涵环保工程有限公司 | Energy-saving impulse anaerobic reactor |
| CN203329422U (en) * | 2013-06-21 | 2013-12-11 | 南宁汇贤环保工程有限公司 | Pulse rapid settler for alcohol waste liquor |
-
2013
- 2013-06-21 CN CN201310249851.5A patent/CN103272414B/en active Active
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2102308U (en) * | 1991-04-30 | 1992-04-22 | 广西贵港甘蔗化工厂 | White water separator of paper production |
| CN1061633A (en) * | 1991-04-30 | 1992-06-03 | 广西贵港甘蔗化工厂 | Mthod of white water from paper making separating technology and equipment |
| JP2002058913A (en) * | 2000-08-22 | 2002-02-26 | Nishihara Environ Sanit Res Corp | Solid-liquid separator having stirring flow forming means |
| JP2003019403A (en) * | 2001-07-10 | 2003-01-21 | Yoshikimi Watanabe | Jet stirring type solid-liquid separation apparatus |
| CN201082875Y (en) * | 2007-08-24 | 2008-07-09 | 宜兴市清涵环保工程有限公司 | Energy-saving impulse anaerobic reactor |
| CN203329422U (en) * | 2013-06-21 | 2013-12-11 | 南宁汇贤环保工程有限公司 | Pulse rapid settler for alcohol waste liquor |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104857745A (en) * | 2015-03-12 | 2015-08-26 | 广西农垦糖业集团星星制糖有限公司 | Continuous precipitator |
| CN106075968A (en) * | 2016-08-11 | 2016-11-09 | 铁道第三勘察设计院集团有限公司 | A kind of spiral-flow type spiral settler of automatic control system spoil disposal |
| CN106110720A (en) * | 2016-08-11 | 2016-11-16 | 铁道第三勘察设计院集团有限公司 | A kind of waterpower controls siphon-type full-automatic cyclone sediment device |
| CN106110720B (en) * | 2016-08-11 | 2018-01-02 | 中国铁路设计集团有限公司 | A kind of waterpower controls siphon-type full-automatic cyclone sediment device |
| CN106267918A (en) * | 2016-09-06 | 2017-01-04 | 云南文山铝业有限公司 | Purifier |
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| CN103272414B (en) | 2015-04-01 |
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