CN208700827U - A kind of biological-chemical processing unit for organic wastewater with difficult degradation thereby - Google Patents
A kind of biological-chemical processing unit for organic wastewater with difficult degradation thereby Download PDFInfo
- Publication number
- CN208700827U CN208700827U CN201820077185.XU CN201820077185U CN208700827U CN 208700827 U CN208700827 U CN 208700827U CN 201820077185 U CN201820077185 U CN 201820077185U CN 208700827 U CN208700827 U CN 208700827U
- Authority
- CN
- China
- Prior art keywords
- layer
- biological
- sand filter
- reaction layer
- chemical
- 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
- 239000002351 wastewater Substances 0.000 title abstract description 19
- 238000012993 chemical processing Methods 0.000 title description 13
- 230000015556 catabolic process Effects 0.000 title description 11
- 238000006731 degradation reaction Methods 0.000 title description 11
- 239000004576 sand Substances 0.000 claims abstract description 36
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 28
- 239000000126 substance Substances 0.000 claims abstract description 22
- 238000006243 chemical reaction Methods 0.000 claims abstract description 19
- 239000010815 organic waste Substances 0.000 claims abstract 2
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 claims description 27
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 20
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 18
- 239000001301 oxygen Substances 0.000 claims description 18
- 229910052760 oxygen Inorganic materials 0.000 claims description 18
- 239000006185 dispersion Substances 0.000 claims description 16
- 239000003610 charcoal Substances 0.000 claims description 11
- 239000002245 particle Substances 0.000 claims description 10
- 244000005700 microbiome Species 0.000 claims description 8
- 239000004746 geotextile Substances 0.000 claims description 6
- 239000004575 stone Substances 0.000 claims description 6
- 210000003437 trachea Anatomy 0.000 claims 4
- 239000002985 plastic film Substances 0.000 claims 1
- 239000010865 sewage Substances 0.000 abstract description 6
- 230000031018 biological processes and functions Effects 0.000 abstract 1
- 238000000034 method Methods 0.000 description 33
- 238000012545 processing Methods 0.000 description 17
- 229910052799 carbon Inorganic materials 0.000 description 14
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 8
- 230000014759 maintenance of location Effects 0.000 description 8
- 239000000356 contaminant Substances 0.000 description 6
- 239000012141 concentrate Substances 0.000 description 5
- 238000000354 decomposition reaction Methods 0.000 description 5
- 238000005516 engineering process Methods 0.000 description 5
- 239000003344 environmental pollutant Substances 0.000 description 5
- 231100000719 pollutant Toxicity 0.000 description 5
- 238000010992 reflux Methods 0.000 description 5
- 239000000149 chemical water pollutant Substances 0.000 description 4
- 239000012535 impurity Substances 0.000 description 4
- 239000000463 material Substances 0.000 description 4
- 229910052757 nitrogen Inorganic materials 0.000 description 4
- 239000005416 organic matter Substances 0.000 description 4
- 230000003647 oxidation Effects 0.000 description 4
- 238000007254 oxidation reaction Methods 0.000 description 4
- 239000007787 solid Substances 0.000 description 4
- 239000007789 gas Substances 0.000 description 3
- 150000003384 small molecules Chemical class 0.000 description 3
- 239000013589 supplement Substances 0.000 description 3
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 2
- 238000007664 blowing Methods 0.000 description 2
- 238000001914 filtration Methods 0.000 description 2
- 230000008595 infiltration Effects 0.000 description 2
- 238000001764 infiltration Methods 0.000 description 2
- 239000012528 membrane Substances 0.000 description 2
- 230000000813 microbial effect Effects 0.000 description 2
- 239000012028 Fenton's reagent Substances 0.000 description 1
- 239000002250 absorbent Substances 0.000 description 1
- 230000002745 absorbent Effects 0.000 description 1
- 230000000844 anti-bacterial effect Effects 0.000 description 1
- 238000002306 biochemical method Methods 0.000 description 1
- 238000010170 biological method Methods 0.000 description 1
- 238000001311 chemical methods and process Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000002848 electrochemical method Methods 0.000 description 1
- 238000005868 electrolysis reaction Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 230000003311 flocculating effect Effects 0.000 description 1
- 150000002505 iron Chemical class 0.000 description 1
- 238000002955 isolation Methods 0.000 description 1
- 230000007483 microbial process Effects 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000005457 optimization Methods 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 230000001954 sterilising effect Effects 0.000 description 1
- 238000004659 sterilization and disinfection Methods 0.000 description 1
- 238000003911 water pollution Methods 0.000 description 1
Landscapes
- Biological Treatment Of Waste Water (AREA)
- Treatment Of Water By Oxidation Or Reduction (AREA)
Abstract
本实用新型提供一种用于难降解有机废水的生物‑化学处理装置，包括砂滤池、位于砂滤池后端的地埋坑体；地埋坑体自上而下设置四层，分别为分散层、生物反应层、化学反应层和蓄水层。新的装置中化学处理不存在二次污染同时能够促进生物过程。采用模块化装置，为难降解有机废水的处理提供新的途径，进一步提升污水处理出水指标，实现污水零排放的目标。
The utility model provides a biological-chemical treatment device for refractory organic waste water, comprising a sand filter tank and an underground pit body located at the rear end of the sand filter tank; the underground pit body is provided with four layers from top to bottom, which are respectively dispersed layer, biological reaction layer, chemical reaction layer and aquifer. The chemical treatment in the new device has no secondary pollution and can promote biological processes. The modular device is adopted to provide a new way for the treatment of refractory organic wastewater, further improve the effluent index of sewage treatment, and achieve the goal of zero discharge of sewage.
Description
Technical field
The utility model relates to concentrates in the device of organic wastewater with difficult degradation thereby in Environment control engineering and various water harnessings
Controlling device, specially promote Recalcitrant chemicals to be decomposed into small molecule contaminants using chemical energy, then pass through the micro- life of environment
Object acts on degradation of contaminant, finally realizes zero release of pollutant.
Background technique
Water pollution control technology is continued to develop since the industrial revolution, has been formed already using biochemical method as core, together
When combine new material development, also gradually develop membrane separation technique, the previous mature technology of the optimizations such as electrochemical techniques.Water is dirty at present
Dye administer in there are still the problem of be conventional biochemical treatment process and now more universal membrane bioreactor (MBR) work
Skill technology can not completely remove pollutant or right in experience high-concentration sewage such as landfill leachate, the objects such as particular industry waste water
The concentrate method generated in processing is few.
Organic wastewater and inorganic wastewater can be classified as according to pollutant component in high-concentration sewage, for most of inorganic
The processing of waste water, due to the natural quality of bioprocess, generally mostly with physico-chemical process flocculating setting or rich absorbent.But it is right
In the processing of high concentrated organic wastewater, then can be broken by electrochemical method, chemical oxidation method etc. organic matter long-chain or
Direct chemical digesting organic matter forms other small-molecule substances.More research institute's approval method has Fenton reagent, Fenton iron
Salt method, electrolysis method, ozone oxidation etc. serial of methods, high concentration, which is all extremely effectively treated, in these methods in theoretical degree has
Machine waste water, or even also there is very good effect to the processing of some high concentration inorganic wastewaters.
New method is merely using these methods in greatest problem present on practical application, and cost is difficult to control.Therefore
The utility model is directed to the improvement of high concentrated organic wastewater, proposes mature chemical method is square in conjunction with traditional biological method
Formula forms the device that more market receives.
Utility model content
For the processing for solving organic wastewater with difficult degradation thereby, the utility model proposes a kind of lifes for organic wastewater with difficult degradation thereby
Object-chemical processing device promotes Recalcitrant chemicals to be decomposed into small molecule contaminants, then passes through environmental microorganism using chemical energy
Degradation of contaminant is acted on, finally realizes zero release of pollutant.
The utility model is by taking the concentrate of landfill leachate or tail water processing as an example.The processing technology routine of the utility model
Be divided into two steps: first step is chemical treatment step, breaks the chemical bond of high concentration organic contaminant by chemical method
Protection, second step is biological treatment step, handles degradation of contaminant concentration by traditional biological, simultaneously because difficult decomposition is organic
Object is fully processed, and can be realized complete processing.
The process route chart of concentrate or tail water processing for landfill leachate is shown in Fig. 1, and waste water to be processed is main in Fig. 1
By retention section I and retention section II.Retaining section I is biological processing section, and retention section II is chemical treatment section.
Biological treatment section will be continually fed into air or purity oxygen, provide the oxygen molecule needed for biology aerobic decomposes；Chemistry
Processing section is continually fed into ozone, and ozone has extremely strong oxidation, can break organic-matter chemical key protection.
The purpose that chemical treatment section is placed in biological treatment section rear end is because ozone is equally made microorganism by sterilization
With, therefore it is placed in rear end and can be avoided micropopulation and coerced, while biological treatment section is placed in front end, carbon source in water,
Nitrogen source can ensure microorganism decomposition process.
It is arranged by reflux, it can be ensured that ozone natural decomposition is oxygen, forms oxygen saturation mixed flow and supplements biological section
Oxygen, carbon source, nitrogen source demand.Reflux ratio is controlled, is to realize the regulatable key factor of technique.
The utility model passes through " buried biological-chemical processing unit " (i.e. a kind of life for organic wastewater with difficult degradation thereby
Object-chemical processing device) show technique application method: Fig. 2 is " buried biological-chemical processing unit " longitudinal procedure figure.
A kind of biological-chemical processing unit for organic wastewater with difficult degradation thereby, including sand filter, positioned at sand filter rear end
Buried pit body；Four layers, respectively dispersion layer, biological respinse layer, chemically reactive layer and aquifer are arranged in buried pit body from top to bottom.
Biological respinse layer is charcoal or active carbon layer, the first gas-guide tube of interior laying in biological respinse layer, the first gas-guide tube
It is connected to air pump or oxygen generator, blowing air or oxygen in the first gas-guide tube.
Chemically reactive layer is charcoal or active carbon layer, and the second gas-guide tube is laid in chemically reactive layer, and the second gas-guide tube connects
Lead to ozone generator, leads to ozone in the second gas-guide tube.
Sand filter is multistage sand filter, fills sandy gravel stratum in sand filter, gravel particles 1-2mm, the height of sand filter by
Grade reduces.
Dispersion layer is stone layer (rubble gravel bed), and chad particle is 20-200mm cobble in dispersion layer.Aquifer is multilayer
Waterproof plastic plate.It is isolated between biological respinse layer and chemically reactive layer, between chemically reactive layer and aquifer with geotextiles.
The charcoal or active carbon layer of biological respinse layer are equipped with immobilized microorganism.Ozone intermittence is released in the chemically reactive layer
It puts.Outlet pipe connects chemically reactive layer bottom and sand filter.
Water first passes around multistage sand filter removal solid impurity, reduces solid impurity to ozone unnecessary consumption.By sand
After the filtering in filter tank, water is entered in buried pit body by pipeline, and four layers, respectively dispersion layer are arranged in pit body from top to bottom, raw
Object conversion zone, chemically reactive layer and aquifer.Dispersion layer is laid with common stones, it is therefore an objective to (1) make water distribution more equal
It is even, (2) between water and gas time of contact it is longer.Biological respinse layer and chemically reactive layer are laid with charcoal or active carbon,
Charcoal or active carbon have extremely strong adsorptivity, realize the retention of sewage, interior laying gas-guide tube in biological respinse layer, by common
Air pump or oxygen generator generate air or oxygen；It is laid with gas-guide tube in chemically reactive layer, ozone is generated by ozone generator.It stores
Water layer is water tether layer after processing, is the waterproof plastic plate of multilayer.Level is directly with the isolation of common geotextiles.
Gravel particles are 1-2mm gravel in the sand filter, can suitably increase sand grains rugosity according to infiltration rate, or reduce
Gravel series.Chad particle is 20-200mm cobble in the dispersion layer.It can be mixed into immobilization in advance in the biological respinse layer
Microbial material, to maintain biological reactions rates to stablize.Ozone is released to intermittent release in the chemically reactive layer.
Compared with the existing technology, the utility model has the advantage that
1, technique is grafted strong, and technique core is biological respinse, chemically reacts to break the chemical key protection of pollutant, because
This can be applied under a variety of situations, can be individually formed process flow, or as collateral branch's process supplement other process routes it
In.
2, implementation pattern is varied, and device described in the utility model is the buried process of simple type, material
It is easy to get, Project Realization is simple, does not have secondary pollution risk.
3, technique investment is cheap compared to more simple chemical treatment, and utility model device core is microbial process,
Reaction condition satisfies the requirements down, does not need additional energy investment.
Detailed description of the invention
Fig. 1 is the utility model process route chart；
Fig. 2 is with " buried biological-chemical processing unit " composition schematic diagram；
1. sand filter in figure, 2. water distributors, 3. dispersion layers, 4. biological respinse layers, 5. geotextiles, 6. aquifers, 7. air guides
Pipe, 8. air pumps, 9. ozone generators, 10. outlet pipes, 11 chemically reactive layer；
Fig. 3 is with " buried biological-chemical processing unit " air water trend graph；
Real segment is processing water trend, and phantom line segments are gas trend.
Specific embodiment
Utility model will be further explained below with reference to the attached drawings and specific embodiments.
The process route chart of concentrate or tail water processing for landfill leachate is shown in Fig. 1, and waste water to be processed is main in Fig. 1
By retention section I and retention section II.Retaining section I is biological processing section, and retention section II is chemical treatment section.
Biological treatment section will be continually fed into air or purity oxygen, provide the oxygen molecule needed for biology aerobic decomposes；Chemistry
Processing section is continually fed into ozone, and ozone has extremely strong oxidation, can break organic-matter chemical key protection.
Chemical treatment section be placed in biological treatment section purpose be because, ozone for microorganism equally by bactericidal effect,
Therefore it is placed in rear end and can be avoided micropopulation and coerced, while biological section is placed in front end, the carbon source, nitrogen source in water can
Ensure microorganism decomposition process.
It is arranged by reflux, it can be ensured that ozone natural decomposition is oxygen, forms oxygen saturation mixed flow and supplements biological section
Oxygen, carbon source, nitrogen source demand.Reflux ratio is controlled, is to realize the regulatable key factor of technique.
The utility model shows the application method of technique by " buried biological-chemical processing unit ": Fig. 2 is " buried
Formula biological-chemical processing unit " longitudinal procedure figure.Fig. 3 is with " buried biological-chemical processing unit " air water trend graph.
A kind of biological-chemical processing unit for organic wastewater with difficult degradation thereby, including sand filter 1, be located at sand filter rear end
Buried pit body；Four layers, respectively dispersion layer 3, biological respinse layer 4,11 and of chemically reactive layer are arranged in buried pit body from top to bottom
Aquifer 6.
Biological respinse layer is charcoal or active carbon layer, the first gas-guide tube of interior laying in biological respinse layer, the first gas-guide tube
It is connected to air pump 8 or oxygen generator, blowing air or oxygen in the first gas-guide tube.
Chemically reactive layer is charcoal or active carbon layer, and the second gas-guide tube is laid in chemically reactive layer, and the second gas-guide tube connects
Lead to ozone generator 9, leads to ozone in the second gas-guide tube.
Sand filter is multistage sand filter (being three-level sand filter in Fig. 2), fills sandy gravel stratum, gravel particles 1- in sand filter
The height of 2mm, sand filter reduce step by step.Dispersion layer is stone layer (rubble gravel bed), and chad particle is 20-200mm in dispersion layer
Cobble.Aquifer is the waterproof plastic plate of multilayer.Between biological respinse layer and chemically reactive layer, chemically reactive layer and aquifer
Between with geotextiles 5 be isolated.The charcoal or active carbon layer of biological respinse layer are equipped with immobilized microorganism.The chemical reaction
Ozone intermittence release in layer.Outlet pipe 10 connects chemically reactive layer bottom and sand filter (to form reflux, treated water
It is again introduced into sand filter).
Water first passes around multistage sand filter removal solid impurity, reduces solid impurity to ozone unnecessary consumption.By sand
After the filtering in filter tank, water is entered in buried pit body by pipeline (water distributor 2), and buried pit body is arranged four layers from top to bottom, point
It Wei not dispersion layer, biological respinse layer, chemically reactive layer and aquifer.Dispersion layer is laid with common stones, it is therefore an objective to (1) be made
Water distribution is more uniform, (2) between water and gas time of contact it is longer.Biological respinse layer and chemically reactive layer are with charcoal or active carbon
It is laid with, charcoal or active carbon have extremely strong adsorptivity, realize the retention of sewage, interior laying air guide in biological respinse layer
Pipe 7 generates air or oxygen by common air pump or oxygen generator；Gas-guide tube 7 is laid in chemically reactive layer, by ozone generator
Generate ozone.Aquifer is water tether layer after processing, is the waterproof plastic plate of multilayer.Between level with common geotextiles every
From.
Gravel particles are 1-2mm gravel in the sand filter, can suitably increase sand grains rugosity according to infiltration rate, or reduce
Gravel series.Chad particle is 20-200mm cobble in the dispersion layer.It can be mixed into immobilization in advance in the biological respinse layer
Microbial material, to maintain biological reactions rates to stablize.Ozone is released to intermittent release in the chemically reactive layer.
The above is only the preferred embodiment of the utility model, it should be pointed out that: for the common skill of the art
For art personnel, without departing from the principle of this utility model, several improvements and modifications can also be made, these improve and
Retouching also should be regarded as the protection scope of the utility model.
Claims (1)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820077185.XU CN208700827U (en) | 2018-01-17 | 2018-01-17 | A kind of biological-chemical processing unit for organic wastewater with difficult degradation thereby |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820077185.XU CN208700827U (en) | 2018-01-17 | 2018-01-17 | A kind of biological-chemical processing unit for organic wastewater with difficult degradation thereby |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN208700827U true CN208700827U (en) | 2019-04-05 |
Family
ID=65912241
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201820077185.XU Expired - Fee Related CN208700827U (en) | 2018-01-17 | 2018-01-17 | A kind of biological-chemical processing unit for organic wastewater with difficult degradation thereby |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN208700827U (en) |
-
2018
- 2018-01-17 CN CN201820077185.XU patent/CN208700827U/en not_active Expired - Fee Related
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN102775025B (en) | Municipal life wastewater treatment system with high efficiency and low energy consumption | |
| WO2008052413A1 (en) | A deeply sewage treating method and apparatus without sludge discharging | |
| CN206476860U (en) | A kind of oily waste water treatment reclamation set | |
| CN102583908B (en) | Garbage leachate treatment process | |
| WO2010133177A1 (en) | Landfill leachate wastewater treatment system and process thereof | |
| CN106673373A (en) | Sustainable and efficient sewage treatment system | |
| CN106830565A (en) | A kind of waste water advanced removal of carbon and nitrogen processing unit and its technique | |
| CN106145571A (en) | A kind of chemical wastewater treatment station Tailwater Depth processing system and processing method | |
| CN106430581A (en) | Aeration type downward-flow constructed wetland wastewater treatment system | |
| CN201301254Y (en) | Buried type oligodynamic sewage treatment device | |
| CN103319047A (en) | Landfill leachate treatment system | |
| Qian et al. | Water treatment of polluted rivers in cities based on biological filter technology | |
| CN206562380U (en) | A kind of unpowered sewage complex biological processing integrated apparatus | |
| CN109879538A (en) | A kind of high total nitrogen, high salinity antibiotics pharmacy waste water processing method | |
| CN206680346U (en) | A kind of waste water advanced removal of carbon and nitrogen processing unit | |
| CN206318832U (en) | Sewage treatment unit | |
| CN202945124U (en) | Urban sewage treatment system with high efficiency and low energy consumption | |
| CN105541040B (en) | A kind of method and its device that short-cut nitrification and denitrification is realized in artificial swamp | |
| CN107473514A (en) | A kind of domestic landfill leachate treatment system and technique | |
| CN201406361Y (en) | A landfill leachate wastewater treatment device | |
| CN208700827U (en) | A kind of biological-chemical processing unit for organic wastewater with difficult degradation thereby | |
| CN218811022U (en) | Integrated treatment device for deep denitrification of garbage penetration filtrate | |
| CN207877521U (en) | A kind of garbage leachate treatment device | |
| CN214611790U (en) | Double-group B-BAF filter tank device | |
| CN109824204A (en) | Method and system for fast and efficient start-up and intensive treatment of landfill leachate |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| 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: 20190405 |