CN204325071U - A kind of effluent cycle utilizes purification system - Google Patents
A kind of effluent cycle utilizes purification system Download PDFInfo
- Publication number
- CN204325071U CN204325071U CN201420718415.8U CN201420718415U CN204325071U CN 204325071 U CN204325071 U CN 204325071U CN 201420718415 U CN201420718415 U CN 201420718415U CN 204325071 U CN204325071 U CN 204325071U
- Authority
- CN
- China
- Prior art keywords
- case
- activated charcoal
- charcoal filter
- aeration
- buffer
- Prior art date
- 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 - Fee Related
Links
- 238000000746 purification Methods 0.000 title claims abstract description 16
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 61
- 238000005273 aeration Methods 0.000 claims abstract description 29
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 26
- 229920002678 cellulose Polymers 0.000 claims abstract description 21
- 239000001913 cellulose Substances 0.000 claims abstract description 21
- 239000012528 membrane Substances 0.000 claims abstract description 21
- 238000001556 precipitation Methods 0.000 claims abstract description 18
- 238000011001 backwashing Methods 0.000 claims abstract description 17
- 239000010865 sewage Substances 0.000 claims abstract description 13
- 238000011010 flushing procedure Methods 0.000 claims abstract description 11
- 239000000463 material Substances 0.000 claims abstract description 7
- 239000006004 Quartz sand Substances 0.000 claims description 7
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 7
- 229910052799 carbon Inorganic materials 0.000 claims description 3
- 239000000706 filtrate Substances 0.000 claims description 3
- 239000000835 fiber Substances 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 238000004140 cleaning Methods 0.000 description 1
- 230000008878 coupling Effects 0.000 description 1
- 238000010168 coupling process Methods 0.000 description 1
- 238000005859 coupling reaction Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
Landscapes
- Water Treatment By Sorption (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The utility model discloses a kind of effluent cycle and utilize purification system, it comprise connect in turn store dirty case, aeration case, buffer-precipitation case, activated charcoal filter, cellulose membrane strainer and clear water tanks, described aeration case is divided into anaerobic zone and aerobic zone, in anaerobic zone and aerobic zone, biofilter material is set, aeration tube is provided with bottom aeration case, the sewage storing dirty case enters aeration case by anaerobic zone from the top down, then from bottom to top by entering buffer-precipitation case behind aerobic zone, buffer-precipitation case is connected by force (forcing) pump with between activated charcoal filter, the water side of activated charcoal filter and cellulose membrane strainer arranges counter-flushing pipeline, counter-flushing pipeline arranges backwashing pump and is connected with clear water tanks, the feed-water end of activated charcoal filter and cellulose membrane strainer arranges backwashing sewer valve.The utility model has simple and compact for structure, that treatment capacity is large, processing speed is fast feature, and cost is lower, is convenient to promote.
Description
Technical field
The utility model belongs to sewage purification field, is specifically related to a kind of effluent cycle and utilizes purification system.
Background technology
In the place that some water sources are rare, the recycling of sewage is particularly important, is directly connected to vital conjuncture.Such as desert Travel Adventure, sea navigation, space travel etc.Local at these, because water resources is precious, must recycle after the sewage purification after use.
Have now some high-efficient purification equipment, specially for field exploitations such as spaces, these equipment manufacturing cost are expensive, cannot popularize.Therefore, the sewage purification and reuse equipment that a kind of cost of development and Design is low, easy to use is needed.
Utility model content
The utility model object is to provide a kind of effluent cycle and utilizes purification system, solves the problem that existing effluent cycle utilizes purification system to involve great expense.
The technical solution of the utility model is: a kind of effluent cycle utilizes purification system, it comprise connect in turn store dirty case, aeration case, buffer-precipitation case, activated charcoal filter, cellulose membrane strainer and clear water tanks, described aeration case is divided into anaerobic zone and aerobic zone, in anaerobic zone and aerobic zone, biofilter material is set, aeration tube is provided with bottom aeration case, the sewage storing dirty case enters aeration case by anaerobic zone from the top down, then from bottom to top by entering buffer-precipitation case behind aerobic zone, buffer-precipitation case is connected by force (forcing) pump with between activated charcoal filter, the water side of activated charcoal filter and cellulose membrane strainer arranges counter-flushing pipeline, counter-flushing pipeline arranges backwashing pump and is connected with clear water tanks, the feed-water end of activated charcoal filter and cellulose membrane strainer arranges backwashing sewer valve.
Further, the filtrate of described activated charcoal filter is made up of quartz sand layer and active carbon layer, and quartz sand layer is arranged on feed-water end.
The operation logic of native system is: sewage enters aeration case from storing dirty case, process in anaerobic zone and aerobic zone, sewage after process enters in buffer-precipitation case, then to be pumped by sewage by force (forcing) pump and reaches reference to standard by activated charcoal filter and cellulose membrane filter cleaning successively.
The utility model compared with prior art tool has the following advantages:
The utility model, by bio-aeration pool and activated charcoal filter and the coupling of cellulose membrane strainer, reaches the object of sewage purification and reuse, have simple and compact for structure, that treatment capacity is large, processing speed is fast feature, and cost is lower, is convenient to promote.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model;
In figure, Reference numeral is: 1-aeration case, 11-anaerobic zone, 12-aerobic zone, 13-aeration tube, 2-buffer-precipitation case, 3-force (forcing) pump, 4-activated charcoal filter, 5-cellulose membrane strainer, 6-clear water tanks, 7-backwashing pump, the backwashing sewer valve of 8-activated charcoal filter, the backwashing sewer valve of 9-cellulose membrane strainer, 10-stores dirty case.
Embodiment
Embodiment 1
A kind of effluent cycle utilizes purification system, it comprise connect in turn store dirty case 10, aeration case 1, buffer-precipitation case 2, activated charcoal filter 4, cellulose membrane strainer 5 and clear water tanks 6.Described aeration case 1 is divided into anaerobic zone 11 and aerobic zone 12, arranges biofilter material in anaerobic zone 11 and aerobic zone 12, and biofilter material adopts the fiber of bigger serface.Aeration tube 13 is provided with bottom aeration case 1.The sewage storing dirty case 10 enters aeration case 1 by anaerobic zone 11 from the top down, then from bottom to top by entering buffer-precipitation case 2 behind aerobic zone 12.Be connected by force (forcing) pump 3 between buffer-precipitation case 2 with activated charcoal filter 4, the water side of activated charcoal filter 4 and cellulose membrane strainer 5 arranges counter-flushing pipeline, counter-flushing pipeline arranged backwashing pump 7 and be connected with clear water tanks 6, the feed-water end of activated charcoal filter 4 and cellulose membrane strainer 5 arranges backwashing sewer valve, is respectively the backwashing sewer valve 8 of activated charcoal filter and the backwashing sewer valve 9 of cellulose membrane strainer.
Embodiment 2
A kind of effluent cycle utilizes purification system, it comprise connect in turn store dirty case 10, aeration case 1, buffer-precipitation case 2, activated charcoal filter 4, cellulose membrane strainer 5 and clear water tanks 6.Described aeration case 1 is divided into anaerobic zone 11 and aerobic zone 12, arranges biofilter material in anaerobic zone 11 and aerobic zone 12, and biofilter material adopts the fiber of bigger serface.Aeration tube 13 is provided with bottom aeration case 1.The sewage storing dirty case 10 enters aeration case 1 by anaerobic zone 11 from the top down, then from bottom to top by entering buffer-precipitation case 2 behind aerobic zone 12.Be connected by force (forcing) pump 3 between buffer-precipitation case 2 with activated charcoal filter 4, the water side of activated charcoal filter 4 and cellulose membrane strainer 5 arranges counter-flushing pipeline, counter-flushing pipeline arranged backwashing pump 7 and be connected with clear water tanks 6, the feed-water end of activated charcoal filter 4 and cellulose membrane strainer 5 arranges backwashing sewer valve, is respectively the backwashing sewer valve 8 of activated charcoal filter and the backwashing sewer valve 9 of cellulose membrane strainer.
The filtrate of described activated charcoal filter 4 is made up of quartz sand layer and active carbon layer, quartz sand layer is arranged on feed-water end, arrange quartz sand layer both can play a supporting role, coarse filtration effect can be played again, prevent some the larger impurity in buffer-precipitation case 2 from entering, and when being convenient to back flushing, impurity is discharged.
The above embodiment only have expressed the embodiment of the application, and it describes comparatively concrete and detailed, but therefore can not be interpreted as the restriction to the application's protection domain.It should be pointed out that for the person of ordinary skill of the art, under the prerequisite not departing from technical scheme design, can also make some distortion and improvement, these all belong to the protection domain of the application.
Claims (2)
1. an effluent cycle utilizes purification system, it is characterized in that, comprise connect in turn store dirty case, aeration case, buffer-precipitation case, activated charcoal filter, cellulose membrane strainer and clear water tanks, described aeration case is divided into anaerobic zone and aerobic zone, in anaerobic zone and aerobic zone, biofilter material is set, aeration tube is provided with bottom aeration case, the sewage storing dirty case enters aeration case by anaerobic zone from the top down, then from bottom to top by entering buffer-precipitation case behind aerobic zone, buffer-precipitation case is connected by force (forcing) pump with between activated charcoal filter, the water side of activated charcoal filter and cellulose membrane strainer arranges counter-flushing pipeline, counter-flushing pipeline arranges backwashing pump and is connected with clear water tanks, the feed-water end of activated charcoal filter and cellulose membrane strainer arranges backwashing sewer valve.
2. a kind of effluent cycle according to claim 1 utilizes purification system, it is characterized in that, the filtrate of described activated charcoal filter is made up of quartz sand layer and active carbon layer, and quartz sand layer is arranged on feed-water end.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201420718415.8U CN204325071U (en) | 2014-11-26 | 2014-11-26 | A kind of effluent cycle utilizes purification system |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201420718415.8U CN204325071U (en) | 2014-11-26 | 2014-11-26 | A kind of effluent cycle utilizes purification system |
Publications (1)
Publication Number | Publication Date |
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CN204325071U true CN204325071U (en) | 2015-05-13 |
Family
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Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CN201420718415.8U Expired - Fee Related CN204325071U (en) | 2014-11-26 | 2014-11-26 | A kind of effluent cycle utilizes purification system |
Country Status (1)
Country | Link |
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CN (1) | CN204325071U (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105928097A (en) * | 2016-06-07 | 2016-09-07 | 河南中烟工业有限责任公司 | Micromist humidification discharge water recycling device of central air conditioner |
-
2014
- 2014-11-26 CN CN201420718415.8U patent/CN204325071U/en not_active Expired - Fee Related
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105928097A (en) * | 2016-06-07 | 2016-09-07 | 河南中烟工业有限责任公司 | Micromist humidification discharge water recycling device of central air conditioner |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20150513 |