CN2659867Y - Film-active carbon integrated water purifier - Google Patents
Film-active carbon integrated water purifier Download PDFInfo
- Publication number
- CN2659867Y CN2659867Y CN 03260467 CN03260467U CN2659867Y CN 2659867 Y CN2659867 Y CN 2659867Y CN 03260467 CN03260467 CN 03260467 CN 03260467 U CN03260467 U CN 03260467U CN 2659867 Y CN2659867 Y CN 2659867Y
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- CN
- China
- Prior art keywords
- membrane
- active carbon
- utility
- water
- model
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- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
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Abstract
A membrane-active carbon all-in-one purifier is provided. The utility model is provided with active carbon and a membrane module in an adsorption tank, one side of the bottom of which is arranged with a raw water inlet, the bottom of the membrane module is arranged with an aerated conduit with air gates, the conduit is connected with an air supply, the top of the membrane is connected with a water pump through a pipeline. The device is simply in structure, but the device is provided with a plurality of separating functions including active carbon adsorption, membrane separation, biological oxidation, etc. The utility model can not only eliminate deliquescent organic matter and pathogenic microorganism in raw water, denitrify (which makes up the shortage that MF and UF membranes can not denitrify), reduce the load of membrane separation, lighten the degree of membrane pollution, and maintain the high flux of the membrane stably and everlastingly, but also reduce the operating pressure, reduce treating cost, and guarantee the stable running of equipments. The utility model is high in automatization, and can realize an automatical and continuous running.
Description
Affiliated technical field
The utility model belongs to a kind of water treating equipment, especially can produce, the integrated purifying equipment of safe and Wholesome Drinking Water.
Background technology
At present, adopt film and gac coupling, be used for the high-quality water treatment, normally activated carbon treatment equipment and film device are set to separate unit, connect to form water purifying plant by pipeline, yet, the pressure that exists required water is bigger, and activated carbon filtration pressure is also bigger, simultaneously, the electric energy energy consumption is bigger, the comparatively complicated floor space of said apparatus is big, and gac is in compaction state, and impurity is relatively poor in the removal water, the gac utilization ratio is lower, handles problems such as the water yield is little.
Summary of the invention
The purpose of this utility model is to overcome the weak point that exists in the above-mentioned technology, provides a kind of simple in structure, reasonable in design, for the resident provides safety, fine device for purifying potable water.
For achieving the above object, the technical scheme that the utility model adopted is: gac and membrane module are housed in the adsorption tank, adsorption tank bottom one side is provided with original water inlet, and the membrane module below is provided with the aeration tube of taking pore out of that links to each other with source of the gas, and the film top joins with water pump by the road.
The utility model has the advantages that:
Although the composition of 1 device is simple, have multiple separation functions such as charcoal absorption, membrane sepn and bio-oxidation.
2, can remove dissolved organic matter in the former water and pathogenic microbes, denitrogenation (Mi has mended the deficiency that the MF/UF film can not denitrogenation), reduce the membrane sepn load, alleviate the film pollution level, stable, keep the high-throughput of film enduringly, can reduce working pressure again, reduce processing cost, guarantee the equipment aim of stable operation.
3, level of automation height can be realized automatically operation continuously.
Description of drawings
Fig. 1 is the utility model structural representation;
Embodiment
Below in conjunction with accompanying drawing embodiment of the present utility model is described in further detail.
As shown in Figure 1, the utility model is that gac 2 and membrane module 3 are housed in adsorption tank 1, and adsorption tank 1 bottom one side is provided with original water inlet 6, and membrane module 3 belows are provided with the aeration tube of taking pore 8 out of 4 that links to each other with source of the gas 7, and the film top joins with water pump 5 by the road.
The utility model is continuously sent into former water in the adsorption tank that gac and membrane module are housed, and to adsorption tank expose to the sun into air, make wherein former water and gac thorough mixing.In hydraulic detention time, the organic pollutant in the water is by charcoal absorption and further by the superior microorganism group degraded in surface formation.Water pump is continuously worked, and under the effect of water pump, the source, water source constantly sees through membrane module, and wherein impurity is held back by membrane module.The water outlet of water pump is the tap water of safe and high quality.Described membrane module is immersed in below the water surface of adsorption tank.
This device is in suspension and the high density gac of flow state in reactor has very big specific surface area, efficiently the organic pollutant in the planar water; Simultaneously, because the water in the adsorption tank does not discharge, therefore microbial biomass wherein constantly increases, and then forms the powder biological activated carbon.The dominant microflora that is adsorbed on the gac has very strong oxidative decomposition capacity, degradation of organic substances effectively to the organic pollutant in the water.
Air pump in adsorption tank, expose to the sun into air not only play and mix and stir and prevent the effect that film pollutes, and can increase the content of oxygen in water, for powder biological activated carbon degradable organic pollutant provides better condition.
Under the suction function of water pump, the membrane module in the adsorption tank can allow in water and the water some to human body beneficial's trace element by and macrobead pollution substance, pathogenic micro-organism etc. are held back, therefore obtain safety, fine tap water.
Claims (1)
1. a film---gac integral water purifying device, comprise source of the gas, gac, adsorption tank, it is characterized in that: gac (2) and membrane module (3) are housed in the adsorption tank (1), adsorption tank (1) bottom one side is provided with original water inlet (6), membrane module (3) below is provided with the aeration tube of taking pore (8) out of (4) that links to each other with source of the gas (7), and the film top joins with water pump (5) by the road.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 03260467 CN2659867Y (en) | 2003-09-01 | 2003-09-01 | Film-active carbon integrated water purifier |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 03260467 CN2659867Y (en) | 2003-09-01 | 2003-09-01 | Film-active carbon integrated water purifier |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2659867Y true CN2659867Y (en) | 2004-12-01 |
Family
ID=34329143
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 03260467 Expired - Lifetime CN2659867Y (en) | 2003-09-01 | 2003-09-01 | Film-active carbon integrated water purifier |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2659867Y (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102515419A (en) * | 2011-11-29 | 2012-06-27 | 同济大学 | Short-flow micro-polluted raw water treatment combined system integrated with adsorption, biological oxidation and membrane separation technologies |
| CN101613131B (en) * | 2008-06-27 | 2013-04-03 | 大晃机械工业株式会社 | Water purifying device |
| CN105858938A (en) * | 2016-06-13 | 2016-08-17 | 江苏索普（集团）有限公司 | Pretreating method for high-salinity wastewater generated in preparation of hydrazine hydrate through ketazine method |
| CN108101266A (en) * | 2018-01-31 | 2018-06-01 | 济南大学 | A kind of integrated apparatus and its application method of granular activated carbon coupling ceramic membrane advanced treatment of industrial wastewater |
-
2003
- 2003-09-01 CN CN 03260467 patent/CN2659867Y/en not_active Expired - Lifetime
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101613131B (en) * | 2008-06-27 | 2013-04-03 | 大晃机械工业株式会社 | Water purifying device |
| CN102515419A (en) * | 2011-11-29 | 2012-06-27 | 同济大学 | Short-flow micro-polluted raw water treatment combined system integrated with adsorption, biological oxidation and membrane separation technologies |
| CN105858938A (en) * | 2016-06-13 | 2016-08-17 | 江苏索普（集团）有限公司 | Pretreating method for high-salinity wastewater generated in preparation of hydrazine hydrate through ketazine method |
| CN108101266A (en) * | 2018-01-31 | 2018-06-01 | 济南大学 | A kind of integrated apparatus and its application method of granular activated carbon coupling ceramic membrane advanced treatment of industrial wastewater |
| CN108101266B (en) * | 2018-01-31 | 2021-02-19 | 济南大学 | Integrated device for advanced treatment of industrial wastewater by coupling granular activated carbon with ceramic membrane and use method of integrated device |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CX01 | Expiry of patent term |
Expiration termination date: 20130901 Granted publication date: 20041201 |