CN208700837U - A kind of recovery processing structure for sewage - Google Patents
A kind of recovery processing structure for sewage Download PDFInfo
- Publication number
- CN208700837U CN208700837U CN201820887032.1U CN201820887032U CN208700837U CN 208700837 U CN208700837 U CN 208700837U CN 201820887032 U CN201820887032 U CN 201820887032U CN 208700837 U CN208700837 U CN 208700837U
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- Prior art keywords
- water
- combination
- tank
- component
- sewage
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- 239000010865 sewage Substances 0.000 title claims abstract description 37
- 238000011084 recovery Methods 0.000 title claims abstract description 21
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 71
- 238000001914 filtration Methods 0.000 claims abstract description 11
- 230000003750 conditioning Effects 0.000 claims description 12
- 239000012528 membrane Substances 0.000 claims description 10
- 238000011068 load Methods 0.000 claims description 8
- 230000000855 fungicidal Effects 0.000 claims description 7
- 239000000417 fungicide Substances 0.000 claims description 7
- 238000002156 mixing Methods 0.000 claims description 7
- 239000002351 wastewater Substances 0.000 abstract description 20
- 238000004519 manufacturing process Methods 0.000 abstract description 12
- 230000000694 effects Effects 0.000 abstract description 6
- 239000011780 sodium chloride Substances 0.000 abstract description 6
- 238000004064 recycling Methods 0.000 abstract description 5
- 238000004134 energy conservation Methods 0.000 abstract description 4
- 239000010802 sludge Substances 0.000 description 12
- 238000000034 method Methods 0.000 description 7
- 244000005700 microbiome Species 0.000 description 5
- 239000007788 liquid Substances 0.000 description 4
- 238000000926 separation method Methods 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 2
- 238000011010 flushing procedure Methods 0.000 description 2
- 230000014759 maintenance of location Effects 0.000 description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- MYMOFIZGZYHOMD-UHFFFAOYSA-N oxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 238000004065 wastewater treatment Methods 0.000 description 2
- 241000894006 Bacteria Species 0.000 description 1
- 241000276438 Gadus morhua Species 0.000 description 1
- NMCUIPGRVMDVDB-UHFFFAOYSA-L Iron(II) chloride Chemical compound Cl[Fe]Cl NMCUIPGRVMDVDB-UHFFFAOYSA-L 0.000 description 1
- 241000108664 Nitrobacteria Species 0.000 description 1
- 241000700605 Viruses Species 0.000 description 1
- 238000005273 aeration Methods 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- QGZKDVFQNNGYKY-UHFFFAOYSA-N ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 1
- UGFAIRIUMAVXCW-UHFFFAOYSA-N carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 235000019516 cod Nutrition 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 239000000356 contaminant Substances 0.000 description 1
- 230000004059 degradation Effects 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 238000011033 desalting Methods 0.000 description 1
- 230000000249 desinfective Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000035622 drinking Effects 0.000 description 1
- 235000021271 drinking Nutrition 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 230000004634 feeding behavior Effects 0.000 description 1
- 239000003546 flue gas Substances 0.000 description 1
- 229910052731 fluorine Inorganic materials 0.000 description 1
- 239000011737 fluorine Substances 0.000 description 1
- YCKRFDGAMUMZLT-UHFFFAOYSA-N fluorine atom Chemical compound [F] YCKRFDGAMUMZLT-UHFFFAOYSA-N 0.000 description 1
- 229910001385 heavy metal Inorganic materials 0.000 description 1
- 239000010814 metallic waste Substances 0.000 description 1
- 239000010841 municipal wastewater Substances 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 238000005086 pumping Methods 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000011105 stabilization Methods 0.000 description 1
- 238000004659 sterilization and disinfection Methods 0.000 description 1
- 238000005429 turbidity Methods 0.000 description 1
- 235000020681 well water Nutrition 0.000 description 1
- 239000002349 well water Substances 0.000 description 1
Abstract
The utility model belongs to plant area's sewage treatment applied technical field, specifically disclose a kind of recovery processing structure for sewage, component is adjusted by filtering, and adjusts the anaerobic-aerobic component that component is used in combination with filtering, and the water delivery component composition being used in combination with anaerobic-aerobic component.A kind of beneficial effect of recovery processing structure for sewage of the utility model is: its is reasonable in design, can sanitary sewage to plant area, high-salt wastewater (incineration system draining), general production waste water (organic wastewater including the discharge of materialization workshop), initial rainwater carry out quick, efficient and stable purified treatment, the purpose for realizing recycling, has saved water resource, has reached energy conservation and environmental protection production requirement.
Description
Technical field
The utility model belongs to plant area's sewage treatment applied technical field, and in particular to a kind of recovery processing for sewage
Structure carries out quick, efficient and stable purified treatment to sewage, completes recycling and reuses, applied widely.
Background technique
1) sanitary sewage: including dining room, office, shower, dormitory, lavatory draining etc.；2) incineration system drains: incineration plants
Draining COD containing part, BOD in flue gas purification system, sewage, and contain a certain amount of salinity, and pH is in acidity,
Belong to high-salt wastewater by water quality characteristics, drains into waste water processing station, plant area and be evaporated desalting processing；3) security landfill field percolate；
4) materialization System drainage: the waste liquid (heavy metal waste liquid, spent acid alkali wasteliquid, fluorine-containing waste liquid) that off-site is sent passes through materializing strategy system
The sewage being discharged after system processing, according to the difference of water quality characteristics, the waste water of materialization system discharge is divided into two kinds；5) general production
Waste water: including mill floor flushing waste water, laboratory draining, collection vessel flushing waste water etc.；6) it initial rainwater: mainly produces
Pollute operating area initial polluted rain water.
To sum up, the process object of plant area's Sewage Disposal is mainly four classes: sanitary sewage, high-salt wastewater (incineration system row
Water), general production waste water (organic wastewater including the discharge of materialization workshop), initial rainwater.
There are many current method handled sewage plant area, but all can not achieve quick, efficient and stable
The requirement directly recycled is not achieved in purified treatment, this is current urgently to be resolved.
Therefore, based on the above issues, the utility model provides a kind of recovery processing structure for sewage.
Utility model content
Purpose of utility model: the purpose of the utility model is to provide a kind of recovery processing structure for sewage, structures
Design rationally, can sanitary sewage to plant area, high-salt wastewater (incineration system draining), general produce waste water (including materialization vehicle
Between the organic wastewater that is discharged), initial rainwater carry out quick, efficient and stable purified treatment, realize the mesh of recycling
, it saved water resource, reached energy conservation and environmental protection production requirement.
Technical solution: the utility model provides a kind of recovery processing structure for sewage, by filtering adjusting component, and with
Filtering adjusts the anaerobic-aerobic component that component is used in combination, and the water delivery component group being used in combination with anaerobic-aerobic component
At；The filtering adjusts component, including conditioning tank, and the first grid, the second grid that are used in combination with conditioning tank, and setting
The first water pump being used in combination in conditioning tank and with the second grid, wherein the first water pump is pumped water is adjusted to second
Grid；The anaerobic-aerobic component, including it is used in combination anaerobic pond, aerobic tank, and be arranged in anaerobic pond, aerobic tank connection wall
Interior gap, and the second water pump, the film filter structure that are arranged in aerobic tank, wherein the second water pump is by the water in aerobic tank
It pumps to anaerobic pond；The water delivery component, including vacuum pump, and the pumping being used in combination with vacuum pump are connect with film filter structure
Sucking pump, and the permanent flow valve being used in combination with suction pump, and the water flow instrument being used in combination with permanent flow valve, and be arranged aerobic
The header tank of pond side, wherein the water in aerobic tank is after film filter structure, vacuum pump, suction pump, permanent flow valve, water flow instrument
It is discharged into header tank.
The technical program, the recovery processing structure for sewage further includes setting gas-guide tube in aerobic tank, and
The blower being used in combination with gas-guide tube, wherein gas-guide tube is provided with several ventholes.
The technical program, the recovery processing structure for sewage further includes fungicide mixing tank, and and fungicide
The third water pump that mixing tank is used in combination, wherein the loading catheter of third water pump and film filter structure, vacuum pump, suction
The water-supply-pipe connection of pump, permanent flow valve, water flow instrument.
The technical program, the film filter structure is MBR plain film membrane module.
Compared with prior art, a kind of beneficial effect of recovery processing structure for sewage of the utility model is:
Its is reasonable in design, can sanitary sewage to plant area, high-salt wastewater (incineration system draining), general production waste water (including
The organic wastewater of materialization workshop discharge), initial rainwater carry out quick, efficient and stable purified treatment, realize recycling circulation benefit
Purpose has saved water resource, has reached energy conservation and environmental protection production requirement.
Detailed description of the invention
Fig. 1 is a kind of structural schematic diagram of recovery processing structure for sewage of the utility model；
Wherein, serial number mark is as follows in figure: the first grid of 1-, 2- conditioning tank, the first water pump of 3-, the second grid of 4-, 5- detest
Oxygen pond, 6- gap, the second water pump of 7-, 8- film filter structure, 9- vacuum pump, 10- suction pump, 11- permanent flow valve, 12- water flow
Instrument, 13- third water pump, 14- fungicide mixing tank, 15- header tank, 16- blower, 17- gas-guide tube, 18- aerobic tank.
Specific embodiment
In the following with reference to the drawings and specific embodiments, the utility model is furtherd elucidate.
Embodiment
A kind of recovery processing structure for sewage as shown in Figure 1 adjusts component by filtering, and adjusts component with filtering
The anaerobic-aerobic component being used in combination, and the water delivery component composition being used in combination with anaerobic-aerobic component；The filtering is adjusted
Component, including conditioning tank 2, and the first grid 1, the second grid 4 that are used in combination with conditioning tank 2 are saved, and is arranged in conditioning tank 2
The first water pump 3 that is interior and being used in combination with the second grid 4, wherein the first water pump 3 pumps 2 water of conditioning tank to the second grid
4；The anaerobic-aerobic component, including it is used in combination anaerobic pond 5, aerobic tank 18, and setting connects in anaerobic pond 5, aerobic tank 18
The gap 6 in wall is connect, and the second water pump 7, the film filter structure 8 that are arranged in aerobic tank 18, wherein the second water pump 7 will be got well
Water in oxygen pond 18 is pumped to anaerobic pond 5；The water delivery component, including vacuum pump 9, and and vacuum are connect with film filter structure 8
9 suction pumps 10 that are used in combination of pump, and the permanent flow valve 11 being used in combination with suction pump 10, and match and make with permanent flow valve 11
Water flow instrument 12, and the header tank 15 of 18 side of aerobic tank is set, wherein the water in aerobic tank 18 is through film filter structure
8, it is discharged into header tank 15 after vacuum pump 9, suction pump 10, permanent flow valve 11, water flow instrument 12.
It is further preferred that the recovery processing structure for sewage, further includes that gas-guide tube is arranged in aerobic tank 18
17, and the blower 16 being used in combination with gas-guide tube 17, wherein gas-guide tube 17 is provided with several ventholes；And it described is used for
The recovery processing structure of sewage further includes fungicide mixing tank 14, and the third water being used in combination with fungicide mixing tank 14
Pump 13, wherein the loading catheter and film filter structure 8, vacuum pump 9, suction pump 10, permanent flow valve 11, water flow of third water pump 13
Measure the water-supply-pipe connection of instrument 12；And the film filter structure 8 is MBR plain film membrane module.
The recovery processing structure for sewage of this structure, it is reasonable in design, it can sanitary sewage to plant area, with high salt useless
Water (incineration system draining), general production waste water (organic wastewater including the discharge of materialization workshop), initial rainwater carry out quickly,
Efficiently and stable purified treatment, it realizes the purpose of recycling, has saved water resource, reached energy conservation and environmental protection production and want
It asks.
The MBR plain film membrane module of this structure is placed in aerobic tank 8, the water after the aeration of aerobic tank 8 and biological treatment, by
Vacuum pump 9 is extracted out after leading to MBR flat sheet membrane component filters, using film separating structure by the activated sludge and macromolecular in aerobic tank 8
Organic substance retains, and saves secondary settling tank, while hydraulic detention time (HRT) and sludge retention time (SRT) can be controlled respectively
System, and substance difficult to degrade constantly reacts in the reactor, degrades.
Since the presence of MBR plain film membrane module substantially increases the ability of system separation of solid and liquid, so that it is discharged system, water
Matter and volumetric loading are all greatly improved, and the water water standard after film process is high (being more than country-level A standard), pass through
Disinfection eventually forms water quality and the high high quality reuse water of biological safety, can be directly as new raw water source.Make since film filters
With microorganism is completely trapped in MBR membrane bioreactor, and the thorough of hydraulic detention time and Age of Activated Sludge is realized
Separation, eliminates sludge bulking problem in traditional activated sludge process.MBR plain film membrane module have it is high to contaminant removal efficiency,
Nitrification ability is strong, can be nitrified simultaneously, denitrification, denitrification effect are good, stable effluent quality, excess sludge production are low, equipment
Compact, occupied area few (the only 1/3-1/2 of traditional handicraft), increment dilatation convenience, high degree of automation, easy to operate etc. are excellent
Point.
Compared with traditional sewage treatment biologic treating technique, MBR plain film membrane module has following clear superiority: equipment is tight
It gathers, land occupation is few, and since sludge concentration is improved 2~5 times in bioreactor, volumetric loading is greatly improved, and uses film
Component is instead of secondary settling tank and filter plant, therefore, compared with conventional biological treatment technique, the occupied area of membrane bioreactor
It can be greatly reduced；Effluent quality high-quality stable, due to the effect that efficiently separates of film, separating effect is much better than traditional sedimentation basin, place
Reason water outlet is extremely limpid, and suspended matter and turbidity are close to zero, and bacterium and virus are substantially removed, and effluent quality is issued better than the Ministry of Construction
The miscellaneous domestic water quality standard (CJ25.1-89) of hair can carry out reuse, while film directly as non-municipal usage of drinking
Separation is trapped microorganism in bioreactor completely, so that higher microorganism concn is able to maintain that in system,
Reaction unit is not only increased to the whole removal efficiency of pollutant, ensure that good effluent quality, simultaneous reactions device into
The various change of Water l oad (water quality and water) has good adaptability, and it is good out can to stablize acquisition for anti impulsion load
Water water quality；Excess sludge production is few, can run under high volumetric loading, low sludge loading, excess sludge production is low (theoretically may be used
To realize zero sludge discharge), reduce Treatment of Sludge expense；Ammonia nitrogen and hardly degraded organic substance are removed, since microorganism is complete
Shut off in bioreactor, thus be conducive to the retention growth for being proliferated slow microorganism such as nitrobacteria, system nitrification effect
Rate is improved.Meanwhile the hydraulic detention time of some organic matters difficult to degrade in systems can be increased, be conducive to difficult to degrade have
The raising of machine object degradation efficiency；Convenient operation and management, it is easy to accomplish automatically control, realize hydraulic detention time (HRT) and dirty
Mud residence time (SRT's) is kept completely separate, and operation controls more flexible stabilization, is the new of equipmentization easy to accomplish in sewage treatment
Technology is, it can be achieved that microcomputer automatic control, to keep operational administrative more convenient；It is easy to be transformed from traditional handicraft, can be used as
The advanced treatment unit of traditional waste water treatment process, in secondary municipal wastewater treatment plant water outlet advanced treating (to realize city
A large amount of reuses of sewage) etc. fields have broad application prospects.
The above is only the preferred embodiment of the utility model, it is noted that for the common skill of the art
It for art personnel, without departing from the principle of this utility model, can also make several improvements, these improvement also should be regarded as
The protection scope of the utility model.
Claims (4)
1. a kind of recovery processing structure for sewage, it is characterised in that: adjust component by filtering, and adjust component phase with filtering
The anaerobic-aerobic component being used cooperatively, and the water delivery component composition being used in combination with anaerobic-aerobic component；The filtering is adjusted
Component, including conditioning tank (2), and the first grid (1), the second grid (4) that are used in combination with conditioning tank (2), and setting exist
The first water pump (3) being used in combination in conditioning tank (2) and with the second grid (4), wherein the first water pump (3) is by conditioning tank (2)
Water is pumped to the second grid (4)；The anaerobic-aerobic component, including it is used in combination anaerobic pond (5), aerobic tank (18), and set
Set the gap (6) in anaerobic pond (5), aerobic tank (18) connection wall, and the second water pump being arranged in aerobic tank (18)
(7), film filter structure (8), wherein the second water pump (7) pumps the water in aerobic tank (18) to anaerobic pond (5)；The water delivery
Component, including connect vacuum pump (9) with film filter structure (8), and the suction pump (10) being used in combination with vacuum pump (9), and
The permanent flow valve (11) being used in combination with suction pump (10), and the water flow instrument (12) being used in combination with permanent flow valve (11), and
Header tank (15) in aerobic tank (18) side is set, wherein the water in aerobic tank (18) is through film filter structure (8), vacuum pump
(9), it is discharged into after suction pump (10), permanent flow valve (11), water flow instrument (12) in header tank (15).
2. a kind of recovery processing structure for sewage according to claim 1, it is characterised in that: described for sewage
It is recycled structure, further includes being arranged in aerobic tank (18) interior gas-guide tube (17), and the wind being used in combination with gas-guide tube (17)
Machine (16), wherein gas-guide tube (17) is provided with several ventholes.
3. a kind of recovery processing structure for sewage according to claim 1 or 2, it is characterised in that: described for dirt
The recovery processing structure of water further includes fungicide mixing tank (14), and the third being used in combination with fungicide mixing tank (14)
Water pump (13), wherein the loading catheter of third water pump (13) and film filter structure (8), vacuum pump (9), suction pump (10), perseverance
Flow the water-supply-pipe connection of valve (11), water flow instrument (12).
4. a kind of recovery processing structure for sewage according to claim 1, it is characterised in that: the film filter structure
It (8) is MBR plain film membrane module.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820887032.1U CN208700837U (en) | 2018-06-08 | 2018-06-08 | A kind of recovery processing structure for sewage |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820887032.1U CN208700837U (en) | 2018-06-08 | 2018-06-08 | A kind of recovery processing structure for sewage |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN208700837U true CN208700837U (en) | 2019-04-05 |
Family
ID=65935873
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201820887032.1U Expired - Fee Related CN208700837U (en) | 2018-06-08 | 2018-06-08 | A kind of recovery processing structure for sewage |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN208700837U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112875987A (en) * | 2021-01-14 | 2021-06-01 | 重庆乐乐环保科技有限公司 | Kitchen garbage treatment device |
-
2018
- 2018-06-08 CN CN201820887032.1U patent/CN208700837U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112875987A (en) * | 2021-01-14 | 2021-06-01 | 重庆乐乐环保科技有限公司 | Kitchen garbage treatment device |
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| 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: 20190405 Termination date: 20200608 |
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| CF01 | Termination of patent right due to non-payment of annual fee |