CN109111027A - A method of improving greenhouse Chinese turtle aquaculture effluent treatment effeciency - Google Patents
A method of improving greenhouse Chinese turtle aquaculture effluent treatment effeciency Download PDFInfo
- Publication number
- CN109111027A CN109111027A CN201810962395.1A CN201810962395A CN109111027A CN 109111027 A CN109111027 A CN 109111027A CN 201810962395 A CN201810962395 A CN 201810962395A CN 109111027 A CN109111027 A CN 109111027A
- Authority
- CN
- China
- Prior art keywords
- layer
- active carbon
- treatment effeciency
- haydite
- effluent treatment
- 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.)
- Withdrawn
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/28—Treatment of water, waste water, or sewage by sorption
- C02F1/281—Treatment of water, waste water, or sewage by sorption using inorganic sorbents
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/28—Treatment of water, waste water, or sewage by sorption
- C02F1/283—Treatment of water, waste water, or sewage by sorption using coal, charred products, or inorganic mixtures containing them
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/02—Aerobic processes
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/30—Organic compounds
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/20—Nature of the water, waste water, sewage or sludge to be treated from animal husbandry
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Organic Chemistry (AREA)
- Biodiversity & Conservation Biology (AREA)
- Microbiology (AREA)
- Inorganic Chemistry (AREA)
- Farming Of Fish And Shellfish (AREA)
- Biological Treatment Of Waste Water (AREA)
Abstract
The invention discloses a kind of methods for improving greenhouse Chinese turtle aquaculture effluent treatment effeciency, the method carries out in biological aerated filter, the filtrate of biological aerated filter is made of haydite and active carbon, the filter material layer of biological aerated filter has 2 layers, it is active carbon layer at the middle and upper levels, and lower layer is the mixed filler layer of haydite and active carbon.Technical solution of the present invention can effectively shorten wastewater treatment cycle, and improve removal efficiency of nitrogen and phosphorus in waste water, thus realize the efficient process of Chinese turtle aquaculture effluent, it is at low cost, and suitable large-scale promotion easy to operate.
Description
Technical field
The present invention relates to breeding soft-shell turtle technical field more particularly to a kind of improve greenhouse Chinese turtle aquaculture effluent treatment effeciency
Method.
Background technique
China is the country that breeding soft-shell turtle is largest in the world, and 2010, breeding soft-shell turtle amount was up to 29.08 ten thousand t, growth rate
Up to 13.1%, nearly 15,000,000,000 yuan of annual value of production, to keep soft-shelled turtle fast-growth, soft-shelled turtle is generally using high protein fish-meal as staple food.By
In efficiency of feed utilization only 70%~80%, breeding wastewater contains a large amount of high protein feeds and soft-shelled turtle excrement, and greenhouse soft-shelled turtle is caused to be supported
Grow the nitrogen (N) and phosphorus (P) that waste water contains high concentration.The unordered discharge of greenhouse Chinese turtle aquaculture effluent has become Yangtze River Delta rural area
One of important pollution sources, it is especially particularly evident in greenhouse breeding soft-shell turtle compact district, do not have also at present a set of feeding for greenhouse soft-shelled turtle
Waste water quality is grown, and contaminant removal efficiency is high, operational administrative is simple, is suitble to the processing method promoted and applied.
Biofilter has many advantages, such as that operating load is high, occupied area is small, investment is small, treatment effeciency is high, supports in aquatic products
It grows in wastewater treatment and is widely applied, and the selection of filler all has very big influence to filter tank treatment efficiency, operating cost etc., is to mention
Rise the key of biological aerated filter treatment effect.Haydite and carbon leaching material have flourishing pore structure, huge specific surface
Long-pending and stable physics and chemical property is excellent adsorbent and bio-carrier.
Summary of the invention
Based on the low technical problem of Chinese turtle aquaculture effluent treatment effeciency existing for background technique, the invention proposes one kind to mention
The method of hot room Chinese turtle aquaculture effluent treatment effeciency, can effectively shorten wastewater treatment cycle, and improves nitrogen phosphorus in waste water and go
Except rate, to realize the efficient process of Chinese turtle aquaculture effluent.
A kind of method improving greenhouse Chinese turtle aquaculture effluent treatment effeciency proposed by the present invention, the method is in aeration and biological
It is carried out in filter tank, the filtrate of the biological aerated filter is made of haydite and active carbon.
Preferably, the filter material layer of the biological aerated filter has 2 layers, it is at the middle and upper levels active carbon layer, lower layer is haydite
With the mixed filler layer of active carbon.
Preferably, the described method comprises the following steps:
(1) it loads filtrate: being first uniformly mixed haydite and active carbon, be seated in biological aerated filter and mixed as bottom
Packing layer is highly 50-100m, and layer of active carbon layer is loaded on mixed filler layer, and upper layer active carbon layer height is 40-
60mm;
(2) biofilm: starting waste water lifting pump flows into waste water to be processed in biological aerated filter and floods filter material layer, bored exposure
Biofilm culture in 1-4 days;
(3) it runs: bringing into operation after stablizing, setting water flow is 100-200L/h.
Preferably, bottom activated carbon particle size is 0.1-1mm in step (1), haydite partial size is 3-5mm, upper layer active carbon
Partial size is 1-10mm.
Preferably, in step (2), gas-water ratio 3-3.5:1.
Preferably, in step (3), gas-water ratio 4.57-5:1.
Preferably, water conservancy load is 2.5-3m in step (3)3/(m2h)。
Preferably, the mass ratio of haydite and active carbon is 3-10:1 in mixed filler layer.
Preferably, being equipped with separation net, the mesh diameter of the separation net between upper layer active carbon layer and mixed filler layer
Less than the particle size of upper layer active carbon.
Technical solution of the present invention is using haydite and active carbon combined stuffing, strong absorption property of the effective use haydite to nitrogen phosphorus
With active carbon to the absorption property of impurity and dissolved organic matter, deep add is carried out using upper layer active carbon on the basis of haydite absorption
Work further removes remaining a small amount of ammonia nitrogen and dissolved organic matter in waste water.Haydite and active carbon are uniformly mixed as mixed
Packing layer is closed, the lesser active carbon of partial size is dispersed between the biggish haydite particles of partial size, and granularity of activated carbon is smaller, therefore
Specific surface area with higher, it is larger to the adsorption capacity of the intracorporal nitrogen phosphorus compound of water, organic matter and oxygen in water,
So that nitrogen phosphorus compound, organic matter and oxygen in water are more enriched in mixed filler layer, the mixing of haydite and active carbon
Filling provides abundant and necessary nutriment for the formation of biomembrane, is conducive to the formation of biomembrane, shortens Biofilm Colonization
Period improve filter tank waste water treatment efficiency, furthermore the active carbon in mixed filler layer helps to improve the attachment of biomembrane
The phenomenon that power, the turbulent flow for avoiding high gas-water ratio from being formed causes biofilm detachment.The increase of aeration quantity promotes biomembrane more
Newly, while the effect of stronger air scour makes biofilm detachment, increases water turbidity, during biofilm, institute during biofilm formation
The oxygen concentration needed is lower, and setting gas-water ratio is 3-3.5:1, has not only been able to satisfy microorganism growth demand, but also can ensure the steady of biomembrane
Fixed attachment, after biofilm terminates and stablizes, adjustment gas-water ratio is 4.57-5:1, because of the unit concentration in biological aerated filter
Nitrogen oxygen demand is 4.57 times of the oxygen demand of unit concentration organic matter, and the gas-water ratio range of 4.57-5:1 both can guarantee biomembrane
Sufficient oxygen demand, bottom active carbon under the stronger adhesive force of biomembrane again be avoided that falling off for biomembrane, further mention
The waste treatment capacity and efficiency in high filter tank.Separation net is set between upper layer active carbon layer and mixed filler layer, keeps upper layer active
Charcoal is kept completely separate with haydite layer, when activated carbon adsorption is close to saturation, need to only be taken out upper layer by separation net, and sudden and violent under air
Shining several hours can be completed desorption, realize active carbon efficiently utilize with reusable purpose, reduce cost.Therefore, originally
Inventing filter tank has efficient waste treatment capacity, at low cost, and suitable large-scale promotion easy to operate.
Specific embodiment
In the following, technical solution of the present invention is described in detail by specific embodiment.
Embodiment 1
A method of greenhouse Chinese turtle aquaculture effluent treatment effeciency is improved, the method carries out in biological aerated filter,
The filter material layer of biological aerated filter has 2 layers, is at the middle and upper levels active carbon layer, and lower layer is the mixed filler layer of haydite and active carbon,
Separation net is equipped between upper layer active carbon layer and mixed filler layer, the partial size that the mesh diameter of separation net is less than upper layer active carbon is big
It is small, it the described method comprises the following steps:
(1) it loads filtrate: being first uniformly mixed haydite and active carbon, be seated in biological aerated filter and mixed as bottom
Packing layer is highly 100m, and the mass ratio of haydite and active carbon is 10:1, mixed filler layer activated carbon particle size in mixed filler layer
For 1mm, haydite partial size is 5mm, and layer of active carbon layer is loaded on mixed filler layer, and upper layer active carbon layer height is 60mm,
Upper layer activated carbon particle size is 10mm;
(2) biofilm: starting waste water lifting pump flows into waste water to be processed in biological aerated filter and floods filter material layer, air water
Than for 3.5:1, bored exposure biofilm culture in 1 day;
(3) it runs: bringing into operation after stablizing, setting water flow is 200L/h, and gas-water ratio 5:1, water conservancy load is 3m3/
(m2h)。
The present embodiment is lower 15 degrees Celsius progress in room temperature, and the biofilm period is 21 days, using following analysis method: COD:
COD Quick testing instrument (measurement is CODcr);Total nitrogen: over cure acid oxidase-ultraviolet spectrophotometry;Total phosphorus: potassium peroxydisulfate disappears
Solution.Through detecting, COD removal rate is 85%, and the removal rate of total nitrogen is up to 96.3%, and total tp removal rate is up to 97%.
Embodiment 2
A method of greenhouse Chinese turtle aquaculture effluent treatment effeciency is improved, the method carries out in biological aerated filter,
The filter material layer of biological aerated filter has 2 layers, is at the middle and upper levels active carbon layer, and lower layer is the mixed filler layer of haydite and active carbon,
Separation net is equipped between upper layer active carbon layer and mixed filler layer, the partial size that the mesh diameter of separation net is less than upper layer active carbon is big
It is small, it the described method comprises the following steps:
(1) it loads filtrate: being first uniformly mixed haydite and active carbon, be seated in biological aerated filter and mixed as bottom
Packing layer is highly 70m, and the mass ratio of haydite and active carbon is 6:1 in mixed filler layer, and mixed filler layer activated carbon particle size is
0.4mm, haydite partial size are 3.5mm, layer of active carbon layer are loaded on mixed filler layer, upper layer active carbon layer height is
55mm, upper layer activated carbon particle size are 3mm;
(2) biofilm: starting waste water lifting pump flows into waste water to be processed in biological aerated filter and floods filter material layer, air water
Than for 3.2:1, bored exposure biofilm culture in 2 days;
(3) it runs: bringing into operation after stablizing, setting water flow is 140L/h, gas-water ratio 4.6:1, and water conservancy load is
2.7m3/(m2h)。
The present embodiment is lower 15 degrees Celsius progress in room temperature, and the biofilm period is 21 days, using following analysis method: COD:
COD Quick testing instrument (measurement is CODcr);Total nitrogen: over cure acid oxidase-ultraviolet spectrophotometry;Total phosphorus: potassium peroxydisulfate disappears
Solution.Through detecting, COD removal rate is 89%, and the removal rate of total nitrogen is up to 98.4%, and total tp removal rate is up to 97.8%.
Embodiment 3
A method of greenhouse Chinese turtle aquaculture effluent treatment effeciency is improved, the method carries out in biological aerated filter,
The filter material layer of biological aerated filter has 2 layers, is at the middle and upper levels active carbon layer, and lower layer is the mixed filler layer of haydite and active carbon,
Separation net is equipped between upper layer active carbon layer and mixed filler layer, the partial size that the mesh diameter of separation net is less than upper layer active carbon is big
It is small, it the described method comprises the following steps:
(1) it loads filtrate: being first uniformly mixed haydite and active carbon, be seated in biological aerated filter and mixed as bottom
Packing layer is highly 50m, and the mass ratio of haydite and active carbon is 3:1 in mixed filler layer, and mixed filler layer activated carbon particle size is
0.1mm, haydite partial size are 3mm, and layer of active carbon layer is loaded on mixed filler layer, and upper layer active carbon layer height is 40mm,
Upper layer activated carbon particle size is 1mm;
(2) biofilm: starting waste water lifting pump flows into waste water to be processed in biological aerated filter and floods filter material layer, air water
Than for 3:1, bored exposure biofilm culture in 4 days;
(3) it runs: bringing into operation after stablizing, setting water flow is 100L/h, gas-water ratio 4.57:1, and water conservancy load is
2.5m3/(m2h)。
The present embodiment is lower 15 degrees Celsius progress in room temperature, and the biofilm period is 21 days, using following analysis method: COD:
COD Quick testing instrument (measurement is CODcr);Total nitrogen: over cure acid oxidase-ultraviolet spectrophotometry;Total phosphorus: potassium peroxydisulfate disappears
Solution.Through detecting, COD removal rate is 87.1%, and the removal rate of total nitrogen is up to 98.5%, and total tp removal rate is up to 95%.
The foregoing is only a preferred embodiment of the present invention, but scope of protection of the present invention is not limited thereto,
Anyone skilled in the art in the technical scope disclosed by the present invention, according to the technique and scheme of the present invention and its
Inventive concept is subject to equivalent substitution or change, should be covered by the protection scope of the present invention.
Claims (9)
1. a kind of method for improving greenhouse Chinese turtle aquaculture effluent treatment effeciency, which is characterized in that the method is filtered in aeration and biological
It is carried out in pond, the filtrate of the biological aerated filter is made of haydite and active carbon.
2. a kind of method for improving greenhouse Chinese turtle aquaculture effluent treatment effeciency according to claim 1, which is characterized in that institute
The filter material layer for stating biological aerated filter has 2 layers, is at the middle and upper levels active carbon layer, and lower layer is the mixed fillers of haydite and active carbon
Layer.
3. a kind of method for improving greenhouse Chinese turtle aquaculture effluent treatment effeciency according to claim 2, which is characterized in that institute
State method the following steps are included:
(1) it loads filtrate: being first uniformly mixed haydite and active carbon, be seated in biological aerated filter as bottom mixed fillers
Layer, is highly 50-100m, and layer of active carbon layer is loaded on mixed filler layer, and upper layer active carbon layer height is 40-60mm;
(2) biofilm: starting waste water lifting pump flows into waste water to be processed in biological aerated filter and floods filter material layer, bored exposure 1-4
Its biofilm culture;
(3) it runs: bringing into operation after stablizing, setting water flow is 100-200L/h.
4. a kind of method for improving greenhouse Chinese turtle aquaculture effluent treatment effeciency according to claim 3, which is characterized in that step
Suddenly in (1), bottom activated carbon particle size is 0.1-1mm, and haydite partial size is 3-5mm, and upper layer activated carbon particle size is 1-10mm.
5. a kind of method for improving greenhouse Chinese turtle aquaculture effluent treatment effeciency according to claim 3, which is characterized in that step
Suddenly in (2), gas-water ratio 3-3.5:1.
6. a kind of method for improving greenhouse Chinese turtle aquaculture effluent treatment effeciency according to claim 3, which is characterized in that step
Suddenly in (3), gas-water ratio 4.57-5:1.
7. a kind of method for improving greenhouse Chinese turtle aquaculture effluent treatment effeciency according to claim 3, which is characterized in that step
Suddenly in (3), water conservancy load is 2.5-3m3/(m2h)。
8. a kind of method of raising greenhouse Chinese turtle aquaculture effluent treatment effeciency according to claim 2-7 any one,
It is characterized in that, the mass ratio of haydite and active carbon is 3-10:1 in mixed filler layer.
9. a kind of greenhouse Chinese turtle aquaculture effluent high-efficiency purifying method according to claim 8, which is characterized in that upper layer activity
Separation net is equipped between layer of charcoal and mixed filler layer, the mesh diameter of the separation net is less than the particle size of upper layer active carbon.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201810962395.1A CN109111027A (en) | 2018-08-22 | 2018-08-22 | A method of improving greenhouse Chinese turtle aquaculture effluent treatment effeciency |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201810962395.1A CN109111027A (en) | 2018-08-22 | 2018-08-22 | A method of improving greenhouse Chinese turtle aquaculture effluent treatment effeciency |
Publications (1)
Publication Number | Publication Date |
---|---|
CN109111027A true CN109111027A (en) | 2019-01-01 |
Family
ID=64860081
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201810962395.1A Withdrawn CN109111027A (en) | 2018-08-22 | 2018-08-22 | A method of improving greenhouse Chinese turtle aquaculture effluent treatment effeciency |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN109111027A (en) |
-
2018
- 2018-08-22 CN CN201810962395.1A patent/CN109111027A/en not_active Withdrawn
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN108467118B (en) | Method for removing nitrogen and phosphorus in aquaculture wastewater by using immobilized algae bacteria | |
CN204090789U (en) | A kind of aquiculture waste water circulating treating system | |
CN1981574A (en) | Aquiculturing system process for works with circulating water | |
CN104085979A (en) | Nano biological filler for purifying aquaculture wastewater in biological filter tank and preparation method of nano biological filler | |
WO2018201733A1 (en) | Micro-ecological floating bed for aquaculture water purification and using method thereof | |
CN107473389A (en) | Couple microorganism and light electrolysis combination floating bed device and the method for handling sanitary sewage | |
JP6621342B2 (en) | Method for producing biological activated carbon to which nitrifying bacteria are attached and advanced water purification method | |
CN106396298A (en) | Purification device for treating poultry farming wastewater through solar bio-floating bed | |
CN103951044B (en) | A kind of non-sintered rapid biofilm biologic packing material and preparation method thereof | |
CN110217890A (en) | Strengthen the device and method of water body nitrogen removal based on aerobic denitrification fungi | |
CN103563830A (en) | Technology for economical and practical circulating water breeding of cynoglossus semilaevis | |
CN207784023U (en) | A kind of totally-enclosed fluidized bed bio filtration cycle water system | |
CN104098173A (en) | Biological aerated filter provided with suspended bed | |
CN108862610B (en) | Device for cultivating microalgae by using sewage and manufacturing method thereof | |
CN109111026A (en) | A kind of Novel biological aerated filter and its application | |
CN109111024A (en) | A kind of biological aerated filter purification Chinese turtle aquaculture effluent method | |
CN207276242U (en) | Ozone and activated carbon catalysis oxidation biofilter | |
CN109111061A (en) | Livestock breeding wastewater circulation recycling system and method | |
CN110668578B (en) | Application of aerobic pre-film modified material | |
CN109133503A (en) | A kind of greenhouse Chinese turtle aquaculture effluent high-efficiency purifying method | |
CN102583713A (en) | Integrated bioaugmenting burned diatomite dynamic membrane gravity flow effluent-discharging drinking water purification process | |
CN201785245U (en) | Compound biological packing and bioreactor thereof | |
CN105314730B (en) | A kind of automatic water process biochemical reactor in sewage river course | |
CN206843188U (en) | The terminal oxidized pool purifier of Process for Treatment of Swine Wastewater technique | |
CN109111027A (en) | A method of improving greenhouse Chinese turtle aquaculture effluent treatment effeciency |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
WW01 | Invention patent application withdrawn after publication | ||
WW01 | Invention patent application withdrawn after publication |
Application publication date: 20190101 |