CN203976534U - A kind of pure water device - Google Patents
A kind of pure water device Download PDFInfo
- Publication number
- CN203976534U CN203976534U CN201420355271.4U CN201420355271U CN203976534U CN 203976534 U CN203976534 U CN 203976534U CN 201420355271 U CN201420355271 U CN 201420355271U CN 203976534 U CN203976534 U CN 203976534U
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- tank
- water
- oxidation pond
- catalyzed oxidation
- gac
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Abstract
The utility model discloses a kind of pure water device, comprise tank, neutralization pipe, the cotton filter core of PP, flocculation tank, coagulation tank, air-floating apparatus, catalyzed oxidation pond, gac, vaporization water tank and clean water basin, in described tank, be provided with perforation pre-exposure tracheae, and side is provided with grid; Described neutralization pipe one end through grid be connected with tank, the cotton filter core of the other end and PP is connected, and neutralize manage and grid between pump is installed; One end of described flocculation tank is connected with the cotton filter core of PP, the other end is connected in coagulation tank, and is provided with floss in flocculation tank; One end of described air-floating apparatus is connected with catalyzed oxidation pond, the other end is connected with coagulation tank, and coagulation tank is connected with settling tank; One end of described vaporization water tank is connected in the gac, the other end that are connected with catalyzed oxidation pond and is connected with clean water basin, and is provided with filter membrane between vaporization water tank and gac.Not only purchase cost is low, processing cost is low, and highly-efficient treatment, is applicable to medium and small sized enterprises.
Description
Technical field
The present invention relates to water treatment field, related in particular to a kind of pure water device.
Background technology
The progress and development of modern society all be unable to do without water resources, we are all the time in the tellurian water resources of a large amount of consumption, yet tellurian water resources is limited, how to using the sewage producing later to purify and re-use the attention that more and more obtains us.
In the production process of food product pack enterprise, can produce a large amount of sewage with organism and metal ion, such sewage can not directly be disposed in river course, can not again utilize, therefore need to process it, it be reached and use or emission standard.
Traditional pure water technique and device cannot be processed organism and metal ion simultaneously, and for medium and small sized enterprises, traditional waste disposal plant is expensive, floor space is large, and does not carry out the processing cost of the great number that Yi Ci sewage disposal club brings.Therefore in medium and small sized enterprises, compound pure water processor can not be promoted effectively.
Therefore, develop a kind of buy and processing cost is low, highly-efficient treatment, the compound pure water device that is applicable to medium and small sized enterprises are difficult problems for the required solution of those skilled in the art.
Summary of the invention
The deficiency existing for prior art, object of the present invention is just to provide a kind of pure water device, and not only purchase cost is low, processing cost is low, and highly-efficient treatment, is applicable to medium and small sized enterprises.
To achieve these goals, the technical solution used in the present invention is such: a kind of pure water device, comprise tank, neutralization pipe, the cotton filter core of PP, flocculation tank, coagulation tank, air-floating apparatus, catalyzed oxidation pond, gac, vaporization water tank and clean water basin, in described tank, be provided with perforation pre-exposure tracheae, and side is provided with grid; Described neutralization pipe one end through grid be connected with tank, the cotton filter core of the other end and PP is connected, and neutralize manage and grid between pump is installed; One end of described flocculation tank is connected with the cotton filter core of PP, the other end is connected in coagulation tank, and is provided with floss in flocculation tank; One end of described air-floating apparatus is connected with catalyzed oxidation pond, the other end is connected with coagulation tank, and coagulation tank is connected with settling tank; One end of described vaporization water tank is connected in the gac, the other end that are connected with catalyzed oxidation pond and is connected with clean water basin, and is provided with filter membrane between vaporization water tank and gac.
As a kind of preferred version, described catalyzed oxidation pond is two or more, and the water-in in each catalyzed oxidation pond is connected and is provided with reversing valve, and is provided with under meter between reversing valve and air-floating apparatus.
Described perforation pre-exposure tracheae adopts gap aeration, stir under water, water in tank is carried out to airoxidation, can prevent that suspended substance from precipitating in sewage equalizing tank on the one hand, can remove certain sulfurous gas on the other hand, reduce the consumption of neutralization reagent, the oxidation that is conducive to objectionable impurities is separated; Described grid is removed twister and the larger floating matter of volume in water.
Described neutralization pipe Balancing degree, general organic sewage is acid, and pH value is between 1-3, and chemical oxygen demand COD is 10000mg/L left and right, enters neutralization Guan Houke Balancing degree.
The cotton filter core of described PP is effectively removed the various granule foreigns in water, has multi-layer type depth structure, and pollutant holding capability is large, is applicable to the filtration of soda acid and organic solvent, and installs and change conveniently.
In described flocculation tank groove, be provided with floss, utilize the absorption net of floss to catch the settlement separate of function acceleration harmful metal ion, heavy metal ion, can also reduce fluorinion concentration in inorganic sewage by adsorption equally; In groove, also need to add flocculation agent, reduce some electromotive forces with electrical particle in water, make its concentrated, sedimentation.
In described coagulation tank, part suspended impurity pollutent again obtains flocculating and carries out preliminary sedimentation, alleviates follow-up processing load, improves system processing efficiency.
Described air-floating apparatus can further be removed not the material of flocculation sediment in time, effectively removes suspended impurity, oil, colourity and partial organic substances in organic sewage.
Described oxidation catalysis pond direct oxidation organic pollutant, or macromole organic pollutant is oxidized to small molecules organic pollutant, improve the biodegradability of organic sewage, remove preferably organic pollutant.In the process of degraded COD, interrupt the two key chromophoric grouies in organic molecule, as azo-group, nitro, sulfuration hydroxyl, carbon imino-etc., reach the object of decolouring, effectively improve BOD/COD value simultaneously, make it to be easy to biochemical degradation.
Some reluctant liquid dissolubility pollutents of described activated carbon treatment.
Described gasification water tank is vaporized treated water, then is condensed into liquid water, purifies.
Compared with prior art, beneficial effect of the present invention:
1. construction costs is low, floor space is little;
Energy consumption low, save processing cost;
3. good purification.
Accompanying drawing explanation
Fig. 1 is structural representation of the present invention.
Embodiment
Below in conjunction with the drawings and specific embodiments, the present invention is further described.
Embodiment 1:
As shown in Figure 1, a kind of pure water device, comprise tank 1, neutralization pipe 2, the cotton filter core 3 of PP, flocculation tank 4, coagulation tank 5, air-floating apparatus 6, catalyzed oxidation pond 7, gac 8, vaporization water tank 9 and clean water basin 10, in described tank 1, be provided with perforation pre-exposure tracheae 12, and side is provided with grid 18; Described neutralization manage 2 one end through grid 18 be connected with tank 1, the cotton filter core 3 of the other end and PP is connected, and neutralize manage 2 and grid 18 between pump 13 is installed; One end of described flocculation tank 4 is connected with the cotton filter core 3 of PP, the other end is connected in coagulation tank 5, and is provided with floss 14 in flocculation tank 4; One end of described air-floating apparatus 6 is connected with catalyzed oxidation pond 7, the other end is connected with coagulation tank 5, and coagulation tank 5 is connected with settling tank 11; One end of described vaporization water tank 9 is connected in the gac 8, the other end that are connected with catalyzed oxidation pond 7 and is connected with clean water basin 10, and is provided with filter membrane 17 between vaporization water tank 9 and gac 8; Described catalyzed oxidation pond 7 is two, and the water-in in these two catalyzed oxidation ponds 7 is connected and is provided with reversing valve 16, and is provided with under meter 15 between reversing valve 16 and air-floating apparatus 6.During concrete enforcement, sewage is passed into tank 1, perforation pre-exposure tracheae 12 in tank 1 is used gap aeration, stir under water, water in tank 1 is carried out to airoxidation, twister and the larger floating matter of volume through grid 18, removed in water again, by pump 13, again water is entered to neutralization pipe 2 Balancing degree, then after the cotton filter core 3 of PP, effectively remove the various granule foreigns in water, pass into again flocculation tank 4, due to the interior flocculation agent that added of flocculation tank 4, reduce some electromotive forces with electrical particle in water, it is concentrated, sedimentation, and be provided with floss 14, utilize the absorption net of floss 14 to catch function acceleration harmful metal ion, heavy metal ion settlement separate, can also reduce fluorinion concentration in inorganic sewage by adsorption equally, pass into again coagulation tank 5, partial suspended foreign-matter contamination again obtains flocculation and carries out preliminary sedimentation, throw out enters settling tank 11, through air-floating apparatus 6, further remove not the material of flocculation sediment in time again, remove the suspended impurity in organic sewage, oil, colourity and partial organic substances, under meter 15 is controlled the flow of water, through reversing valve 16, pass into catalyzed oxidation pond 7 again, after has expired in one of them catalyzed oxidation pond 7, reversing valve 16 commutations, water passes into another catalyzed oxidation pond 7, the water that passes through catalyzed oxidation pond 7 direct oxidation organic pollutants or macromole organic pollutant is oxidized to small molecules organic pollutant is through gac 8, then by gac 8, process some reluctant liquid dissolubility pollutents, finally by mistakeization water tank, treated water is vaporized and is condensed into liquid water again and purifies and import clean water basin 10.
Finally it should be noted that, above embodiment is the non-limiting technical scheme in order to technical scheme of the present invention to be described only, those of ordinary skill in the art is to be understood that, those are modified or are equal to replacement technical scheme of the present invention, and do not depart from aim and the scope of the technical program, all should be encompassed in the middle of claim scope of the present invention.
Claims (2)
1. a pure water device, it is characterized in that: described pure water device comprises tank, neutralization pipe, the cotton filter core of PP, flocculation tank, coagulation tank, air-floating apparatus, catalyzed oxidation pond, gac, vaporization water tank and clean water basin, in described tank, be provided with perforation pre-exposure tracheae, and side is provided with grid; Described neutralization pipe one end through grid be connected with tank, the cotton filter core of the other end and PP is connected, and neutralize manage and grid between pump is installed; One end of described flocculation tank is connected with the cotton filter core of PP, the other end is connected in coagulation tank, and is provided with floss in flocculation tank; One end of described air-floating apparatus is connected with catalyzed oxidation pond, the other end is connected with coagulation tank, and coagulation tank is connected with settling tank; One end of described vaporization water tank is connected in the gac, the other end that are connected with catalyzed oxidation pond and is connected with clean water basin, and is provided with filter membrane between vaporization water tank and gac.
2. a kind of pure water device according to claim 1, is characterized in that: described catalyzed oxidation pond is two or more, and the water-in in each catalyzed oxidation pond is connected and is provided with reversing valve, and is provided with under meter between reversing valve and air-floating apparatus.
Priority Applications (1)
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CN201420355271.4U CN203976534U (en) | 2014-06-30 | 2014-06-30 | A kind of pure water device |
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CN201420355271.4U CN203976534U (en) | 2014-06-30 | 2014-06-30 | A kind of pure water device |
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CN203976534U true CN203976534U (en) | 2014-12-03 |
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CN201420355271.4U Expired - Fee Related CN203976534U (en) | 2014-06-30 | 2014-06-30 | A kind of pure water device |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104098204A (en) * | 2014-06-30 | 2014-10-15 | 苏州博云塑业有限公司 | Water purification device |
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2014
- 2014-06-30 CN CN201420355271.4U patent/CN203976534U/en not_active Expired - Fee Related
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104098204A (en) * | 2014-06-30 | 2014-10-15 | 苏州博云塑业有限公司 | Water purification device |
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C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20141203 Termination date: 20170630 |