CN203487012U - Energy-efficient drove feces wastewater membrane treatment device - Google Patents
Energy-efficient drove feces wastewater membrane treatment device Download PDFInfo
- Publication number
- CN203487012U CN203487012U CN201320586737.7U CN201320586737U CN203487012U CN 203487012 U CN203487012 U CN 203487012U CN 201320586737 U CN201320586737 U CN 201320586737U CN 203487012 U CN203487012 U CN 203487012U
- Authority
- CN
- China
- Prior art keywords
- sludge
- chamber
- efficient
- microbial film
- drove
- 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
- 239000012528 membrane Substances 0.000 title claims abstract description 24
- 239000002351 wastewater Substances 0.000 title claims abstract description 19
- 210000003608 fece Anatomy 0.000 title abstract 3
- 239000010802 sludge Substances 0.000 claims abstract description 39
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 14
- 238000010992 reflux Methods 0.000 claims abstract description 8
- 238000005273 aeration Methods 0.000 claims abstract description 6
- 230000000813 microbial effect Effects 0.000 claims description 29
- 239000002893 slag Substances 0.000 claims description 14
- 239000010865 sewage Substances 0.000 claims description 5
- 239000000945 filler Substances 0.000 claims description 3
- 230000008676 import Effects 0.000 claims description 3
- 239000000725 suspension Substances 0.000 claims description 3
- 238000004140 cleaning Methods 0.000 abstract description 6
- 244000144972 livestock Species 0.000 abstract description 4
- 238000000034 method Methods 0.000 abstract description 3
- XKMRRTOUMJRJIA-UHFFFAOYSA-N ammonia nh3 Chemical compound N.N XKMRRTOUMJRJIA-UHFFFAOYSA-N 0.000 abstract description 2
- 230000015556 catabolic process Effects 0.000 abstract description 2
- 238000006731 degradation reaction Methods 0.000 abstract description 2
- 238000007599 discharging Methods 0.000 abstract description 2
- 239000003651 drinking water Substances 0.000 abstract description 2
- 235000020188 drinking water Nutrition 0.000 abstract description 2
- 230000000694 effects Effects 0.000 abstract description 2
- 238000007790 scraping Methods 0.000 abstract 1
- 239000013049 sediment Substances 0.000 abstract 1
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- 238000004065 wastewater treatment Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 1
- 244000144980 herd Species 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
Images
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
- Activated Sludge Processes (AREA)
Abstract
The utility model discloses an energy-efficient drove feces wastewater membrane treatment device, which sequentially comprises an aeration chamber, a first biological membrane chamber, a second biological membrane chamber and an efficient treatment chamber. According to the device, firstly, drove feces wastewater is subjected to the activated sludge process treatment and the biological membrane treatment in sequence, thus a large amount of COD, ammonia nitrogen and SS can be removed, then the wastewater is subjected to electrolytic floatation. The wastewater which is subjected to electrolytic floatation can be drained directly from a water draining hole to be used for cleaning a corral, or pass through the membrane treatment device to be drained from a water outlet to be used as livestock drinking water. Electrolytic floatation can further enhance the degradation effect and the cleaning of the membrane treatment device. Scum generated by electrolytic floatation is conveyed to a scum hopper through a scum scraping device and is discharged from a scum discharging hole. A sludge hopper is arranged at the bottom of the first biological membrane chamber, sludge in the aeration chamber enters the first biological membrane chamber along with the wastewater and sediments into the sludge hopper, the sludge in the sludge hopper enters a sludge outlet pipe, part of the sludge is discharged from a sludge outlet, and another part of the sludge enters the aeration chamber through a sludge reflux inlet.
Description
Technical field
The utility model relates to and belongs to sewage treatment area, is specifically related to a pedigree herd excrement sewage and waste water treatment device.
Background technology
Livestock-raising meeting produces a large amount of waste water, its mainly from the movement of livestock, the Cleaning Wastewater of corral etc.At present, these waste water first pass through septic tank conventionally, and then through biological treatment, discharge after reaching emission standard, and such processing mode is more extensive, is unfavorable for Sustainable development.
Utility model content
For the problems of the prior art, the purpose of this utility model is to provide a kind of energy-efficient drove excrement dirty wastewater membrane treatment unit.
In order to achieve the above object, the technical solution of the utility model is: the dirty wastewater membrane treatment unit of a kind of energy-efficient drove excrement, comprise successively solarization air cell, the first microbial film chamber, the second microbial film chamber, efficient treatment chamber, solarization air cell bottom is communicated with the first microbial film chamber, the first top, microbial film chamber is communicated with the second top, microbial film chamber, the second bottom, microbial film chamber is communicated with efficient treatment chamber bottom, described solarization air cell top is provided with sewage import, described the first bottom, microbial film chamber is provided with sludge bucket, described sludge bucket bottom is provided with sludge outlet pipe, on described sludge outlet pipe, be provided with sludge outlet and sludge reflux mouth, described sludge reflux mouth is arranged on solarization air cell top, the entrance of described efficient treatment chamber is provided with honeycomb screen and electrofloatation device, described efficient treatment chamber top is provided with slag scraper, described slag scraper below is provided with slag bucket, on described slag bucket, be provided with slag-drip opening, in described efficient treatment chamber, be provided with membrane treatment appts, on described membrane treatment appts, be provided with water outlet, on described efficient treatment chamber, be provided with water port, described efficient chamber bottom is provided with Butterworth Hatch.
Further, the indoor suspension type filler that is provided with of described the first microbial film chamber and the second microbial film.
Further, described solarization air cell bottom is provided with microporous aeration disc.
Compared with prior art, this device can be realized the dirty wastewater treatment of the drove excrement after septic tank is processed, and from water outlet water out, can supply livestock consumption, and the water of discharging from water port can be used for the cleaning of corral.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
Embodiment
Below in conjunction with drawings and Examples, the utility model is further described.
As shown in Figure 1, the dirty wastewater membrane treatment unit of a kind of energy-efficient drove excrement, comprise successively solarization air cell 1, the first microbial film chamber 2, the second microbial film chamber 3, efficient treatment chamber 4, solarization air cell 1 bottom is communicated with the first microbial film chamber 2, the first 2 tops, microbial film chamber is communicated with 3 tops, the second microbial film chamber, the second 3 bottoms, microbial film chamber is communicated with efficient treatment chamber 4 bottoms, described solarization air cell 1 top is provided with sewage import 18, 2 bottoms, described the first microbial film chamber are provided with sludge bucket 14, described sludge bucket 14 bottoms are provided with sludge outlet pipe 15, on described sludge outlet pipe 15, be provided with sludge outlet 17 and sludge reflux mouth 16, described sludge reflux mouth 16 is arranged on solarization air cell 1 top, the entrance of described efficient treatment chamber 4 is provided with honeycomb screen 13 and electrofloatation device 12, described efficient treatment chamber 4 tops are provided with slag scraper 5, described slag scraper 5 belows are provided with slag bucket 7, on described slag bucket 7, be provided with slag-drip opening 8, in described efficient treatment chamber 4, be provided with membrane treatment appts 6, on described membrane treatment appts 6, be provided with water outlet 10, on described efficient treatment chamber 4, be provided with water port 9, described efficient chamber bottom is provided with Butterworth Hatch 11.Further, in described the first microbial film chamber 2 and the second microbial film chamber 3, be provided with suspension type filler 20.Further, described solarization air cell 1 bottom is provided with microporous aeration disc 19.
This device is first processed through activated sludge process and biomembrance process successively to the dirty waste water of drove excrement, remove a large amount of COD, ammonia nitrogen and SS wherein, then it is carried out to electrofloatation, waste water after electrofloatation can directly be discharged and be used for cleaning corral from water port, also can from water outlet, discharge for livestock drinking-water through membrane treatment appts.Electrofloatation can further promote degradation effect and strengthen the cleaning to membrane treatment appts, and the scum silica frost of its generation, delivers to slag bucket through slag scraper, and discharge from slag-drip opening.The first bottom, microbial film chamber is provided with sludge bucket, mud in solarization air cell is along with waste water enters the first microbial film chamber and is settled down in sludge bucket, and the mud in sludge bucket enters the sludge outlet discharge of a sludge outlet pipe part and a part enters solarization air cell through sludge reflux mouth.
Claims (3)
1. the dirty wastewater membrane treatment unit of energy-efficient drove excrement, comprise successively solarization air cell, the first microbial film chamber, the second microbial film chamber, efficient treatment chamber, it is characterized in that, solarization air cell bottom is communicated with the first microbial film chamber, the first top, microbial film chamber is communicated with the second top, microbial film chamber, the second bottom, microbial film chamber is communicated with efficient treatment chamber bottom, described solarization air cell top is provided with sewage import, described the first bottom, microbial film chamber is provided with sludge bucket, described sludge bucket bottom is provided with sludge outlet pipe, on described sludge outlet pipe, be provided with sludge outlet and sludge reflux mouth, described sludge reflux mouth is arranged on solarization air cell top, the entrance of described efficient treatment chamber is provided with honeycomb screen and electrofloatation device, described efficient treatment chamber top is provided with slag scraper, described slag scraper below is provided with slag bucket, on described slag bucket, be provided with slag-drip opening, in described efficient treatment chamber, be provided with membrane treatment appts, on described membrane treatment appts, be provided with water outlet, on described efficient treatment chamber, be provided with water port, described efficient chamber bottom is provided with Butterworth Hatch.
2. the dirty wastewater membrane treatment unit of a kind of energy-efficient drove excrement according to claim 1, is characterized in that the indoor suspension type filler that is provided with of described the first microbial film chamber and the second microbial film.
3. the dirty wastewater membrane treatment unit of a kind of energy-efficient drove excrement according to claim 1, is characterized in that, described solarization air cell bottom is provided with microporous aeration disc.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320586737.7U CN203487012U (en) | 2013-09-23 | 2013-09-23 | Energy-efficient drove feces wastewater membrane treatment device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320586737.7U CN203487012U (en) | 2013-09-23 | 2013-09-23 | Energy-efficient drove feces wastewater membrane treatment device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203487012U true CN203487012U (en) | 2014-03-19 |
Family
ID=50257857
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201320586737.7U Expired - Fee Related CN203487012U (en) | 2013-09-23 | 2013-09-23 | Energy-efficient drove feces wastewater membrane treatment device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203487012U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106430832A (en) * | 2016-11-05 | 2017-02-22 | 曹良军 | Dismantlement formula livestock and poultry breeding excrement sewage treatment plant |
-
2013
- 2013-09-23 CN CN201320586737.7U patent/CN203487012U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106430832A (en) * | 2016-11-05 | 2017-02-22 | 曹良军 | Dismantlement formula livestock and poultry breeding excrement sewage treatment plant |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN202529925U (en) | Air-flotation filtering integrated processing device | |
| KR101189747B1 (en) | Water supply and discharge purifying system for water tank type inland aquaculture | |
| CN103583457B (en) | A kind of pond water quality biological purification device based on aeration | |
| CN201296713Y (en) | Inner circulating biological aerated filter and retention pond combined treatment system | |
| CN203613071U (en) | Sewage treatment device | |
| CN102936086A (en) | Integral type digestion tank | |
| CN103262823B (en) | The cultivating system of industrialization stratified pumping clear water circulation and method | |
| CN204151196U (en) | A kind of livestock breeding wastewater treatment unit | |
| CN203487012U (en) | Energy-efficient drove feces wastewater membrane treatment device | |
| CN107434330B (en) | Artificial rapid infiltration sewage treatment method | |
| CN201268647Y (en) | Small-sized domestic sewage processing system | |
| CN201942559U (en) | Sludge storage pool with aeration system | |
| CN205420089U (en) | Reclaimed water reuse system | |
| CN205603432U (en) | Domestic sewage's integration treatment device | |
| CN210176673U (en) | Pig farm sewage innocent treatment system | |
| CN203775949U (en) | Integrated high-density-breeding mobile fish pond | |
| CN203461872U (en) | Biochemical treatment filler device with filtration and self-cleaning effects | |
| CN108083429B (en) | An unpowered oxidation ditch sewage treatment system | |
| CN201793465U (en) | Sludge concentration tank | |
| CN207294530U (en) | Full-automatic sewage processing unit monitoring system | |
| CN207102013U (en) | A kind of Novel sewage treatment trough | |
| CN205398376U (en) | Stabilize efficient rural domestic sewage treatment device | |
| CN205933395U (en) | Biological fungus aeration sewage treatment system of environmental protection integration | |
| CN206915965U (en) | High-efficiency tank | |
| CN203768182U (en) | Life wastewater treatment device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20140319 Termination date: 20160923 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |