CN1318519A - Sewage electrolyzing purifier and its usage - Google Patents
Sewage electrolyzing purifier and its usage Download PDFInfo
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- CN1318519A CN1318519A CN 00114206 CN00114206A CN1318519A CN 1318519 A CN1318519 A CN 1318519A CN 00114206 CN00114206 CN 00114206 CN 00114206 A CN00114206 A CN 00114206A CN 1318519 A CN1318519 A CN 1318519A
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- water
- sewage
- case
- silica frost
- scum silica
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Abstract
Under the action of metal electrode and through electrolytic coagulation and co-precipitation, electrochemical oxidoreduction, etc., pollutant in sewage is coagulated and adhered to small bubbles emitted from plate to float upwards and the sewage is purified. The purifier of the present invention is strong in pollutant eliminating capacity, small, flexible and suitable for use to purity sewage from printing, textile printing and other industry.
Description
The present invention relates to a kind of electrolysis generation cohesion, coprecipitated, electrochemical oxidation-principles such as reduction of utilizing, make pollutent with the micro bubble come-up of separating out on the battery lead plate, thereby sewage is purified.
The interpolation medicament is generally adopted in traditional similar sewage disposal, handles through the method for stirring and precipitation process, makes the numerous and diverse treatment project investment of treatment process big, the working cost height.
The objective of the invention is: provide a kind of occupation of land few, equipment can move flexibly, reduced investment, the sewage electrolyzing purifier that purification efficiency is high.
Another object of the present invention provides the science using method of said apparatus.
First purpose of the present invention is achieved in that the interior two ends of casing (1) parallel inserted has metal electrode board (2), (3); Electrode (2), (3) are connected with the positive and negative electrode of electrolysis power (4) respectively, parallel inserted has metal sheet (15) between electrode (2), (3), the top of casing (1) has scum silica frost that overflow ducts (5) is arranged, the water-dilution channel (6) of band valve (14) is established at the middle part, and sewage water entry to be clean (7) is established in the bottom.When starting power supply (4), sewage in the case (1) is under the acting in conjunction of two positive-negative electrode plates (2) (3) and (15), coacervation appears in pollutent and the micro bubble of being separated out on the pole plate adheres to come-up, and the scum silica frost of come-up overflows through pipeline from overflow ducts (5) discharges, and makes the back level and handles; Treated water purification enters clean water chamber (11) level after clear water output (13) effluxes work by (6) and handles after separating.Battery lead plate is participated in reaction directly in sewage treatment process, be the solubility electrode.
Said apparatus of the present invention can be perfect like this: casing (1) and separator box (A) disjunctor, scum silica frost overflow ducts (5), water-dilution channel (6) are located at respectively on the plate (8) of two casees case splicings; Division plate (9) is separated into scum chamber (10) and clean water chamber (11) with case (A); Scum silica frost overflow ducts (5) is lower than place, case (1) top at plate (8); Water-dilution channel (6) is located at the position of division plate (9) below near plate (9), and (6) are in clean water chamber (11) and have clear water output (13).Be spaced apart 1-3CM between the metal sheet (15).Metal sheet (15) is made by aluminium, zinc, iron or their alloy material.Case (1) and case (A) are made by insulating material.
The experiment proved that: the distance between the metal sheet (15) has effect preferably in the 1-3CM scope; The selection of metal sheet (15) is arranged as aluminium, zinc, iron from effect; And be arranged as iron, zinc, aluminium from cost.General employing iron is the processing needs that material can satisfy general sewage, can adopt for example aluminium, the such material of zinc for the big sewage of intractability.
Second purpose of the present invention is achieved in that sewage to be clean is entered case (1) through water entry (7) starts power supply (4) work when reaching the specified water yield, when the come-up scum silica frost after overflow ducts (5) overflows, open the valve (14) of water-dilution channel (6), making purifies waste water effluxes; The flow of regulated valve (14) makes sewage flooding quantity and clear water aquifer yield and scum silica frost go out the quantity of slag and keep balance aspect amount, makes treatment sewage be able to continuous purification and handles.With sewage to be clean in water entry (7) enters case (1), when reaching the nominal water yield, start power supply (4) work, the scum silica frost of come-up overflows to scum chamber (10) through the overflow ducts (5) of plate (8) top, makes the back level from scum silica frost outlet (12) discharge and handles; Open the valve (14) of clear water output (13) this moment, purifying waste water in the case (1) flows into clean water chamber (11) from water-dilution channel (6), and level is handled after clear water output is discharged work; Control sewage flooding quantity and clear water aquifer yield and scum silica frost go out the quantity of slag and keep balance aspect amounts, make sewage be able to continuous purification and handle.
Fig. 1 is a kind of primary formation synoptic diagram, and sewage to be clean enters in the casing from (7).Under the pressure of water pump, upwards flow, clear water (6) outflow after metal sheet (comprising battery lead plate) is cleaned from clear water from water-dilution channel, the cotton-shaped impurity of come-up overflows from overflow ducts (5).Water balance in the case (1) can realize like this: regulate the flooding quantity of sump pump, the by-pass valve control (14) on water-dilution channel (6) adjusts the water yield; Fig. 2 is a kind of actual using appts; Utilize casing (1), casing (2) disjunctor flows out scum silica frost and clear liquid respectively from water-dilution channel (6) clear water output (13) of scum chamber (10) top overflow ducts (5), scum silica frost outlet (12), clean water chamber (11).The equilibrium principle of the water yield is the same.
Method of the present invention can be perfect like this: make the interior sewage pre-treatment of case (1) 15 to 30 minutes after starting power supply (4), open clear water output by-pass valve control (14).The operating voltage of power supply (4) is the 100-320 volt, and working current is the 3-28 ampere.
The present invention is owing to adopted under the effect of solubility pole plate participation, make the pollutants in sewage cohesion, and adhered to come-up by the micro bubble that on pole plate, produces simultaneously, by separate chamber (2) treated sewage pollution thing is broken away from from water body, thereby reach the purpose of purification.Because this device need not to add other medicament in sewage treatment process, cancelled devices such as stirring and dosing and simplified cleaning section, has saved the cost input, has reduced input cost.This equipment can move installation flexibly.The interval of the present invention's metal sheet in the selection of power supply, voltage, electric current is first-class done perfect.
Fig. 1. basic structure schematic diagram of the present invention.
Fig. 2. a kind of product structure synoptic diagram of the present invention.
Fig. 3. the synoptic diagram of the division plate of device of the present invention (9).
Fig. 4. web plate (8) synoptic diagram of casing of device of the present invention (1) and separator box (A).
Embodiment 1: adopt the DJDI-0.5 electrolysis machine to handle printing waste water
(1): casing is made by PVC sheet material welding processing, and volume is 0.22M
3
(2), (3): each one of 3mm Plate Steel is of a size of 375 * 500.
(4): automatically controlled screen output services voltage is that 180 volts, working current are 5 amperes.
(6): open the double water distributing pore on clean water chamber scope inner panel (8), the aperture is that 10mm, every row's quantity are 15.
(7): the DN25 pvc pipe.
(9): plate is from the horizontal by 15 angles between clean water chamber and scum chamber.
(10), (11): volume is 0.04M
3
(12): the DN50 pvc pipe is installed on end, position at the bottom of the deslagging chamber.
(13): the DN25 pvc pipe.
(14): DN25 PVC ball valve.
(15): the 3mm Plate Steel, be of a size of 375 * 400, totally 66 of quantity, clear distance is 12mm between plate.
Embodiment 2: adopt DJDI-10 electrolysis machine treatment of Bleaching and Dyeing Wastewater.
(1): casing is made by PVC sheet material welding processing, and volume is 2.3M
3
(2), (3): each three of 3mm Plate Steels are of a size of 325 * 850.
(4): automatically controlled screen output services voltage is that 220 volts, working current are 20 amperes.
(6): open the double water distributing pore on clean water chamber scope inner panel (8), the aperture is that 10mm, every row's quantity are 50.
(7): the DN50 pvc pipe.
(9): plate is from the horizontal by 15 angles between clean water chamber and scum chamber.
(10), (11): volume is 0.2M
3
(12): the DN100 pvc pipe is installed on end, position at the bottom of the deslagging chamber.
(13): DN80 pvc pipe, totally two.
(14): DN80 PVC ball valve, totally two.
(15): the 3mm Plate Steel, be of a size of 375 * 400, totally 66 of quantity, clear distance is 12mm between plate.
Fig. 1 to Fig. 4 is seen in connection between above-mentioned parts.
Claims (9)
1. sewage electrolyzing purifier, it is characterized in that: the interior two ends of casing (1) parallel inserted has metal electrode board (2), (3); Electrode (2), (3) are connected with the positive and negative electrode of electrolysis power (4) respectively, parallel inserted has metal sheet (15) between electrode (2), (3), scum silica frost overflow ducts (5) is arranged at the top of casing (1), the middle part is provided with the water-dilution channel (6) of band valve (14), and sewage water entry to be clean (7) is established in the bottom.
2. device according to claim 1 is characterized in that: casing (1) and separator box (A) disjunctor; Scum silica frost overflow ducts (5), water-dilution channel (6) are located at respectively on the plate (8) of two casees case splicings; Division plate (9) is separated into scum chamber (10) and clean water chamber (11) with case (A); Scum silica frost overflow ducts (5) is lower than place, case (1) top at plate (8); Water-dilution channel (6) is located at the position of division plate (9) below near plate (9), and (6) are on the plate (8); Clean water chamber (11) is provided with clear water output (13).
3. device according to claim 1 and 2 is characterized in that: be spaced apart 1 to 3CM between the metal sheet (15).
4. device according to claim 1 and 2 is characterized in that: metal sheet (15) is made by aluminium, zinc, iron or their alloy material.
5. device according to claim 1 and 2 is characterized in that: case (1) and case (A) are made by insulating material.
6. the using method of the described device of claim 1, it is characterized in that: sewage to be clean is entered case (1) through water entry (7) start power supply (4) when reaching the specified water yield and start working, when the come-up scum silica frost after overflow ducts (5) overflows, open the valve (14) of water-dilution channel (6), the sewage after the purification is effluxed; Regulated valve (14) flow makes sewage flooding quantity and clear water output and scum silica frost go out the quantity of slag and keep balance aspect amount, handles thereby make sewage be able to continuous purification.
7. the using method of the described device of claim 2, it is characterized in that: with sewage to be clean in water entry (7) enters case (1), when reaching the nominal water yield, start power supply (4) work, the scum silica frost of come-up overflows to scum chamber (10) through the overflow ducts (5) of the utmost point (8) top, discharges through scum silica frost outlet (12) and makes environmental protection treatment; Open the valve (14) of clear water output (13) this moment, what case (1) was interior flows into clean water chamber (11) through purifying waste water from water-dilution channel (6), level processing after clear water output is discharged work; Control sewage flooding quantity and clear water aquifer yield and scum silica frost go out the quantity of slag and keep balance aspect amounts, make sewage be able to continuous purification and handle.
8. according to claim 6 or 7 described methods, it is characterized in that: make the interior sewage pre-treatment of case (1) 15 to 30 minutes after starting power supply (4), open clear water output by-pass valve control (14).
9. device according to claim 1 and 2 is characterized in that: the operating voltage of power supply (4) is the 100-320 volt, and working current is the 3-28 ampere.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 00114206 CN1318519A (en) | 2000-04-17 | 2000-04-17 | Sewage electrolyzing purifier and its usage |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 00114206 CN1318519A (en) | 2000-04-17 | 2000-04-17 | Sewage electrolyzing purifier and its usage |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN1318519A true CN1318519A (en) | 2001-10-24 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 00114206 Pending CN1318519A (en) | 2000-04-17 | 2000-04-17 | Sewage electrolyzing purifier and its usage |
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Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1328181C (en) * | 2005-06-28 | 2007-07-25 | 陕西师范大学 | Treater of sewage by electrochemistr catalyzing oxidizing |
| CN101481158B (en) * | 2009-02-12 | 2010-12-29 | 杨汝明 | Low voltage electrochemical flocculation waste water treating device |
| CN101293686B (en) * | 2007-04-23 | 2011-01-12 | 河南大学 | Electrization device for treatment of water |
| CN101638257B (en) * | 2009-07-17 | 2011-07-20 | 东北大学 | Method and device for treating dye wastewater employing periodic reverse electrocoagulation |
| CN102241429A (en) * | 2010-05-13 | 2011-11-16 | 吴全海 | Small-sized flexible and movable landscape water treatment device (submerged purifier) |
| CN104445529A (en) * | 2014-11-18 | 2015-03-25 | 北京师范大学 | Up-flow electro-catalytic reactor |
| CN108430932A (en) * | 2015-10-08 | 2018-08-21 | 莫列斯有限公司 | A kind of manufacturing device of electrolysis water |
-
2000
- 2000-04-17 CN CN 00114206 patent/CN1318519A/en active Pending
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1328181C (en) * | 2005-06-28 | 2007-07-25 | 陕西师范大学 | Treater of sewage by electrochemistr catalyzing oxidizing |
| CN101293686B (en) * | 2007-04-23 | 2011-01-12 | 河南大学 | Electrization device for treatment of water |
| CN101481158B (en) * | 2009-02-12 | 2010-12-29 | 杨汝明 | Low voltage electrochemical flocculation waste water treating device |
| CN101638257B (en) * | 2009-07-17 | 2011-07-20 | 东北大学 | Method and device for treating dye wastewater employing periodic reverse electrocoagulation |
| CN102241429A (en) * | 2010-05-13 | 2011-11-16 | 吴全海 | Small-sized flexible and movable landscape water treatment device (submerged purifier) |
| CN104445529A (en) * | 2014-11-18 | 2015-03-25 | 北京师范大学 | Up-flow electro-catalytic reactor |
| CN108430932A (en) * | 2015-10-08 | 2018-08-21 | 莫列斯有限公司 | A kind of manufacturing device of electrolysis water |
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