CN100402444C - Operation mode and apparatus of short distance nitration-anaerobic ammoxidation batched biomembrane denitrogenation - Google Patents
Operation mode and apparatus of short distance nitration-anaerobic ammoxidation batched biomembrane denitrogenation Download PDFInfo
- Publication number
- CN100402444C CN100402444C CNB2006100321474A CN200610032147A CN100402444C CN 100402444 C CN100402444 C CN 100402444C CN B2006100321474 A CNB2006100321474 A CN B2006100321474A CN 200610032147 A CN200610032147 A CN 200610032147A CN 100402444 C CN100402444 C CN 100402444C
- Authority
- CN
- China
- Prior art keywords
- aeration
- reaction vessel
- sewage
- nitrite
- short distance
- 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
Images
Landscapes
- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
Abstract
One kind of short range nitrifying-anaerobic aminoxidizing sequencing batch type denitrifying biomembrane mode and plant is disclosed. The limited aerating mode with real-time control of the sewage temperature inside the reactor and high frequency alternation between aeration and anaeration can inhibit the growth of nitrite oxidizing bacteria and denitrifying bacteria so that the aminoxidizing bacteria and the anaerobic aminoxidizing bacteria become the dominant bacteria in the nitrifying and denitrifying stages. In the nitrifying stage, nitrification is stopped in the nitrite step; and in the denitrifying stage, ammonia nitrogen acts as the direct electron donor to reduce nitrite. The plant is provided with fixed spherical composite stuffing with spherical shell of polypropylene and filled inside biological composite material. Sectional discrete water feeding mode is adopted to feed the sewage to be treated in four stages into the reactor.
Description
Technical field
The invention belongs to environment protection, technical field of sewage, be specifically related to a kind of short distance nitration-anaerobic ammoxidation sequencing batch biofilm denitrification operation mode and device.
Background technology
Traditional biological denitrificaion is mainly finished jointly by nitrated-denitrification two-stage process.In the nitrated stage, the process that ammonia nitrogen is converted into nitrate nitrogen is divided into two successive reactions, at first is by ammonia oxidizing bacteria ammonia nitrogen to be converted into nitrite, by nitrite-oxidizing bacteria nitrite is converted into nitrate then.This technology has two aspect deficiencies, at first is that energy consumption is big, and the ammonia nitrogen nitrifying process needs external energy to supply with oxygen, and the Prepositive denitrification system need be provided with the bigger mixed solution internal reflux of reflux ratio, and this has also increased energy consumption.Secondly, anti-nitration reaction needs carbon source as electron donor, if carbon source deficiency (C/N is low excessively) in the sewage then need add organic carbons such as methyl alcohol, this has not only increased working cost, has also increased the difficulty of operational management.Therefore, experts and scholars both domestic and external are always at the denitrification process of attempting seeking a kind of low-consumption high-efficiency.
The synergetical principle of short distance nitration-anaerobic ammoxidation provides a novel high-efficiency biological denitrification approach for the denitrogenation of high ammonia nitrogen percolate.This approach is compared with traditional aerobic-anaerobism (A/O) biological denitrificaion approach can save 62.5% energy consumption at least, save 50% alkali number, need not additional carbon, and sludge yield is minimum in operational process, only be 15% of traditional biological denitrification process, saved running cost greatly.But also there is following problem in the synergy technology of existing short distance nitration-anaerobic ammoxidation: 1. the product nitrite of ammonia oxidation itself is teratogenesis, carcinogenic, mutagenic matter, simultaneously it also can with substance reaction such as aromatic amine, generate other nitrosification by products, such material is more harmful to receiving water body and human health; 2. the growth temperature of ammonia oxidizing bacteria and anaerobic ammonium oxidizing bacteria is all higher, in the winter time with the cryogenic north, in order to keep suitable reaction temperature, reaction process is incubated needs consumes the more energy; 3. the nitrite concentration accumulation to a certain degree can all produce toxic action to ammonia oxidizing bacteria and anaerobic ammonium oxidizing bacteria, thereby reduces nitric efficiency; 4. a full scale plant that only has at present Rotterdam, NED Dokhaven municipal wastewater to handle based on the synergy of short distance nitration-anaerobic ammoxidation is in the world coming into operation, this device is made up of preposition short distance nitration (SHARON) reaction unit and an Anammox (ANAMMOX) reaction unit, because short distance nitration carries out in different containers respectively with Anammox, make the initial cost of whole technology and floor space increase.
The bio-denitrifying sewage technology is an important research direction in current water pollution control field, the important subject that research and development are efficient, the biological denitrification process of low consumption and device have become current field of water treatment.
Summary of the invention
Technical problem to be solved by this invention is the defective that overcomes above-mentioned prior art, a kind of short distance nitration-anaerobic ammoxidation sequencing batch biofilm denitrification operation mode and device are provided, short distance nitration and Anammox are realized in same reaction vessel, shorten the reaction times, and the volume of reduction reaction vessel, nitration reaction is stopped at the nitrite stage; Adopt sectional type water inlet pattern to disperse influent load, improved the capacity of resisting impact load and the processing power of device; Can effectively control nitrite cumulative maximum concentration, reduce nitrite biomembranous toxic action is sent out, the nitric efficiency height, and treatment effect is stable.
For solving the problems of the technologies described above, the present invention adopts following technical proposals.
Short distance nitration-anaerobic ammoxidation sequencing batch biofilm denitrification operation mode of the present invention, it is characterized in that 1. aeration and the high frequency alternate run of anoxic dual mode, make and removed in time in the anoxic stage, make the cumulative maximum concentration of nitrous acid controlled at the nitrous acid of aeration phase generation; 2. carry out restricted aeration, during aeration in the reaction vessel dissolved oxygen concentration be 1.1～1.5mg/L, create the active limited low oxyty environment of nitrite-oxidizing bacteria, and the activity of ammonia oxidizing bacteria can not be suppressed under this environment.
Its concrete operation is:
I) the water inlet phase: 20%～40% of treatment sewage total amount in the cycle of operation is heated to 26 ℃～33 ℃ in the preheating tank that can heat to sewage after, join in the reaction vessel that is equiped with fixed ball-type combined stuffing in it; Flooding time is 0.1～0.4 hour;
II) reaction period: the described reaction period is divided into four aerations and anoxic circulation, and first to the 3rd aeration and anoxic circulation all comprise aeration, water inlet and anoxic three phases successively,
Aeration phase: micro-air is provided in reaction vessel, on the microbial film that fixed ball-type combined stuffing surface forms and the microorganism in the sewage is degraded by organism and the catalysis ammonia nitrogen is oxidized to nitrite, the time of each aeration phase is 1.5～2 hours;
Fill phase: stop aeration, 20%～40% of treatment sewage total amount in the cycle of operation is heated to 26 ℃～33 ℃ in the preheating tank after, join in the reaction vessel; Flooding time is 0.05～0.2 hour;
The anoxic stage: the microorganism on the microbial film and in the sewage utilizes nitrite and the ammonia nitrogen in the water to carry out Anammox reaction generation nitrogen, and the time in each anoxic stage is 1～1.5 hour;
The 4th aeration and anoxic circulation comprise the 4th aeration phase and the 4th anoxic stage and precipitation phase,
The 4th aeration phase: micro-air is provided in reaction vessel, and the microorganism on the microbial film and in the sewage is degraded by organism and the catalysis ammonia nitrogen is oxidized to nitrite, and aeration time is 1.5～2 hours;
The 4th anoxic stage and precipitation phase: stop aeration, microorganism on the microbial film and in the sewage utilizes nitrite and the ammonia nitrogen in the water to carry out Anammox reaction generation nitrogen, further remove remaining ammonia nitrogen and nitrite nitrogen, simultaneously the sewage of handling is precipitated, last 1～2 hour;
III) drainage period: the sewage after will handling is discharged reaction vessel.
Short distance nitration-anaerobic ammoxidation sequencing batch biofilm nitrogen rejection facility of the present invention, it is characterized in that it comprises the preheating tank that can heat to sewage, reaction vessel, aerator and aeration head, the preheating tank links to each other with the set water-in in reaction vessel upper end by pipeline, be equiped with fixed ball-type combined stuffing and well heater in the reaction vessel, the lower end of reaction vessel is provided with water outlet, the middle part is provided with thief hole, the top is provided with the automatic air pressure compensation flap, aeration head is installed in reaction container bottom, be positioned at ball-type combined stuffing below, aerator places reaction vessel one side, links to each other with aeration head in being loaded on reaction vessel by pipeline.
As a further improvement on the present invention, be provided with electromagnetic dosing pump between described preheating tank and the reaction vessel, be provided with gas meter between aerator and the aeration head, be provided with temperature sensor in the reaction vessel, the water outlet place has magnetic valve, and reaction vessel is provided with on one side and can realizes the automatic control section of control automatically to this device.
Be equiped with the filler fixed support in the described reaction vessel, the ball-type combined stuffing is loaded in the filler fixed support.Described aeration head is the micro-pore aeration dish of the aeration that made progress by fixed ball-type combined stuffing bottom vertical.
Described ball-type combined stuffing is made up of hollow fishnet shape spherical housing and the inside stuffing matter that is loaded in the shell, and the admission space of inside stuffing matter accounts for 30～50% of hollow fishnet shape spherical housing hollow space volume.The material of described hollow fishnet shape spherical housing is polyethylene, polyvinyl chloride, polystyrene, polypropylene or urethane, and its diameter is 50～150m.Described inside stuffing matter is made up of with 1: 1 volume proportion biological material and artificial macromolecular material.
Described biological material is the hollow ring of natural air drying, ring diameter 5～8mm, long 10～20mm; Artificial macromolecular material is the flexible filament thing of polyethylene, polyvinyl chloride, polystyrene, polypropylene or urethane plastic, and the filament diameter is 0.5～1mm.
Beneficial effect of the present invention is:
1, short distance nitration-anaerobic ammoxidation sequencing batch biofilm denitrification operation mode of the present invention, set up the cogeneration system of ammonia oxidizing bacteria and anaerobic ammonium oxidizing bacteria, accumulate ammonia oxidizing bacteria and anaerobic ammonium oxidizing bacteria fast, can suppress the growth of nitrite-oxidizing bacteria and denitrifying bacterium fast and effectively, make ammonia oxidizing bacteria and anaerobic ammonium oxidizing bacteria become the dominant bacteria in nitrification and denitrification stage respectively.In the nitrated stage, nitrification stops at the nitrite stage, and the denitrification stage is then by NH
4 +As direct electron donor reduction nitrosonium salts nitric acid, control nitrite cumulative maximum concentration has reduced nitrite to biomembranous toxic action.
2, by carrying out restricted aeration, control during aeration in the reaction vessel dissolved oxygen concentration be 1.1～1.5mg/L, under low dissolved axygen concentration, suppress nitrite-oxidizing bacteria fast and effectively, nitration reaction is stopped at the nitrite stage, and the activity of ammonia oxidizing bacteria can not be suppressed under this environment.
3, high frequency aeration and anoxic alternative intermittent operation mode make and are removed in time in the anoxic stage at the nitrous acid of aeration phase generation, thereby make the cumulative maximum concentration of nitrous acid controlled, avoided nitrite that ammonia oxidizing bacteria and anaerobic ammonium oxidizing bacteria are produced toxic action.
4, device of the present invention has only a reaction vessel, short distance nitration and Anammox are realized in same reaction vessel, have shortened the reaction times, have correspondingly reduced the volume of reaction vessel and quantity and the initial cost of handling structures, apparatus structure is simply compact, and operational management is convenient.Adopt fixed spherical combined stuffing, filler has stronger bioaffinity and wetting ability, and specific surface area is big, is easy to the microorganism growth biofilm; The filler internal core is easy to change, acid and alkali-resistance, anti-aging, long service life, and operational management is convenient.
5, electromagnetic dosing pump connects preheating tank and reaction vessel respectively, can add water at the control downhill reaction container real-time quantitative of automatic control section.Adopt the discrete water inlet pattern of sectional type, give full play to the operation advantage of sequence batch (reaction unit, load pressure is distributed to each step of reaction, improved the capacity of resisting impact load and the processing power of device, help the steady running of device.
In sum, the present invention has that operational management is convenient, floor space is little, sludge yield is little, energy consumption is low, the capital construction working cost is low, nitric efficiency is high, and characteristics such as treatment effect is stable.The denitrogenation processing that can be widely used in high-ammonia-nitrogen sewages such as livestock and poultry farm sewage, slaughterhouse sewage, small town sewage, percolate, bio-pharmaceuticals sewage.
Description of drawings
Fig. 1 is the structural representation of apparatus of the present invention;
Fig. 2 is an operation synoptic diagram of the present invention.
Each label is represented among the figure:
1, preheating tank 2, electromagnetic dosing pump
3, reaction vessel 4, ball-type combined stuffing
5, temperature sensor 6, well heater
7, aeration head 8, gas meter
9, aerator 10, automatic control section
11, automatic air pressure compensation flap 12, thief hole
13, water outlet 14, filler fixed support
Embodiment
Case study on implementation: certain small-sized rubbish landfill yard percolate denitrogenation processing.
It is 50m that certain small-sized rubbish landfill yard garbage percolation liquid treating system is daily handled the water yield
3/ day, selected device reaction container 3 useful volumes are 150m
3, preheating tank 1 volume is 50m
3
The apparatus structure of present embodiment as shown in Figure 1, it comprises the preheating tank 1 that can heat to sewage, reaction vessel 3, aerator 9 and aeration head 7, preheating tank 1 links to each other with the set water-in in reaction vessel 3 upper ends by pipeline, preheating tank 1 can preheat water inlet to 26 ℃～33 ℃, be provided with electromagnetic dosing pump 2 between preheating tank 1 and the reaction vessel 3, can implement real-time quantitative to reaction vessel 3 by set automatic control section 10 and add water, be provided with fixed ball-type combined stuffing 4 and well heater 6 in the reaction vessel 3, hang a filler fixed support 14 on the inwall of reaction vessel 3, ball-type combined stuffing 4 is loaded in the filler fixed support 14, in use, easily change, acid and alkali-resistance, anti-aging, long service life, easy for installation, help accumulation and the biomembranous formation of microorganism.6 of well heaters are loaded on reaction vessel 3 medial surfaces by mount pad, also be provided with temperature sensor 5 in the reaction vessel 3, temperature sensor 5 places the sewage in the reaction vessel 3 and links to each other with automatic control section 10, with real-time monitor water temperature, automatically real-time 6 pairs of sewage of control heater heat after the water temperature information of control section 10 reception temperature sensors 5 feedbacks, and water temperature is controlled at 28 ℃～33 ℃.The lower end of reaction vessel 3 is provided with water outlet 13, water outlet 13 places have magnetic valve, water outlet at regular time and quantity under the control of automatic control section 10, reaction vessel 3 middle parts are provided with thief hole 12, the top is provided with automatic air pressure compensation flap 11, aeration head 7 is installed in reaction vessel 3 bottoms, is positioned at ball-type combined stuffing 4 belows, is one by the make progress micro-pore aeration dish of aeration of ball-type combined stuffing 4 bottom vertical in this example.Aerator 9 places reaction vessel 3 one sides, link to each other with aeration head 7 in being loaded on reaction vessel 3 by pipeline, be provided with gas meter 8 between aerator 9 and the aeration head 7, practicable restricted aeration, during aeration in the reaction vessel 3 dissolved oxygen concentration be 1.1～1.5mg/L, create the low oxyty environment of nitrite-oxidizing bacteria growth restriction, and the activity of ammonia oxidizing bacteria can not be suppressed under this environment.Can be located at reaction vessel 3 on one side to the automatic control section 10 that the realization of this device is controlled automatically.
Ball-type combined stuffing 4 is formed 40% of the admission space duty fishnet shape spherical housing hollow space volume of inside stuffing matter by empty fishnet shape spherical housing and the inside stuffing matter that is loaded in the shell.The material of hollow fishnet shape spherical housing is a polypropylene, and diameter is 80mm; Inside stuffing matter is made up of with 1: 1 volume proportion biological material and artificial macromolecular material, and biological material is mainly the hollow ring of natural air drying, ring diameter 5～8mm, long 10～20mm; Artificial macromolecular material is the flexible filament thing of vinyon, and the filament diameter is 0.5～1mm.
The concrete operation scheme of present embodiment utilization said apparatus is:
1. the high frequency alternate run of aeration and anoxic dual mode makes and is removed in time in the anoxic stage at the nitrous acid of aeration phase generation, makes the cumulative maximum concentration of nitrous acid controlled; 2. carry out restricted aeration, during aeration in the container dissolved oxygen concentration be 1.1～1.5mg/L, create the low oxyty environment of nitrite-oxidizing bacteria growth restriction, and the activity of ammonia oxidizing bacteria can not be suppressed under this environment.Its concrete operation is as shown in Figure 2:
Fill phase 1: pending sewage is preheated in preheating tank 1 to 31 ℃, open electromagnetic dosing pump 2 and add water by water-in to reaction vessel 3, flooding quantity is 20m
3, flooding time is 0.1～0.2 hour, water temperature is controlled at 31 ℃.
Aeration phase 1: aerator 9 beginning aerations, continue aeration 1.5 hours, control the oxygen in water concentration at 1.1～1.5mg/L by gas meter 8, in reaction vessel 3, provide micro-air, disperseing to become the microbial film diffusion of small bubbles on sewage and ball-type combined stuffing 4 under the shearing action of micro-pore aeration dish, microorganism on the microbial film and in the sewage is degraded and catalysis to organism, the aerobic ammonia oxidation bacterium utilizes oxygen and ammonia nitrogen to carry out metabolism, and ammonia nitrogen is oxidized to nitrite.Because the dissolved oxygen concentration deficiency, the nitrite-oxidizing bacteria activity is suppressed, and nitrite can not be oxidized to nitrate and accumulate in device.
Fill phase 2: close aerator 9, stop aeration, open electromagnetic dosing pump 2 treatment sewage in the preheating tank 1 is added in the reaction vessel 3, flooding quantity is 10m
3, flooding time is 0.05～0.1 hour, water temperature is controlled at 31 ℃.
The anoxic stage 1: the anoxic time length is 1 hour, aerator 9 is in closing condition, microorganism on the microbial film and in the sewage utilizes nitrite and the ammonia nitrogen in the water to carry out the Anammox reaction, under the effect of anaerobic ammonium oxidizing bacteria, the oxidized reduction of nitrite and ammonia nitrogen is converted into nitrogen.
Aeration phase 2: operation control and reaction mechanism thereof are with aeration phase 1.
Fill phase 3: operation control is with fill phase 2.
The anoxic stage 2: operation control and reaction mechanism thereof are with the anoxic stage 1.
Aeration phase 3: operation control and reaction mechanism thereof are with aeration phase 1.
Fill phase 4: operation control is with fill phase 2.
The anoxic stage 3: operation control and reaction mechanism thereof are with the anoxic stage 1.
The 4th aeration phase 4: operation control and reaction mechanism thereof are with aeration phase 1.
The 4th anoxic stage 4 and precipitation phase: stop aeration, microorganism on the microbial film and in the sewage utilizes nitrite and the ammonia nitrogen in the water to carry out Anammox reaction generation nitrogen, further remove remaining ammonia nitrogen and nitrite nitrogen, this stage is unique anoxic stage that fill phase once was not set before the stage begins in the whole service cycle, and the effect in this stage is in order to remove remaining ammonia nitrogen and nitrite nitrogen in the reaction vessel completely.The 4th anoxic stage 4 was also brought into play the final sedimentary effect of sewage to handling simultaneously in the whole service cycle simultaneously, was considered as the precipitation phase in the cycle of operation, and the reaction times is shortened.Last 1 hour.
Drainage period, the magnetic valve of water outlet 13 is opened, treated wastewater disposition in the reaction vessel 3, water discharge time 0.5～1 hour.
Present embodiment influent ammonia nitrogen and total nitrogen are respectively at 215.9～498.5mg.L
-1With 289.4～613.7mg.L
-1Between the fluctuation, the water outlet ammonia nitrogen concentration all is lower than 28mg.L
-1, ammonia nitrogen is on average removed efficient and is reached 93.9%, and the water outlet total nitrogen concentration all is lower than 67mg.L
-1, total nitrogen is on average removed efficient and is reached 89%.
Claims (9)
1. short distance nitration-anaerobic ammoxidation sequencing batch biofilm denitrification operation mode, it is characterized in that 1. aeration and the high frequency alternate run of anoxic dual mode, make and removed in time in the anoxic stage, make the cumulative maximum concentration of nitrous acid controlled at the nitrous acid of aeration phase generation; 2. carry out restricted aeration, during aeration in the reaction vessel dissolved oxygen concentration be 1.1～1.5mg/L, create the active limited low oxyty environment of nitrite-oxidizing bacteria, and the activity of ammonia oxidizing bacteria can not be suppressed under this environment; Its concrete operation is:
I) the water inlet phase: 20%～40% of treatment sewage total amount in the cycle of operation is heated to 26 ℃～33 ℃ in the preheating tank that can heat to sewage after, join in the reaction vessel that is equiped with fixed ball-type combined stuffing in it; Flooding time is 0.1～0.4 hour;
II) reaction period: the described reaction period is divided into four aerations and anoxic circulation, and first to the 3rd aeration and anoxic circulation all comprise aeration, water inlet and anoxic three phases successively,
Aeration phase: micro-air is provided in reaction vessel, on the microbial film that fixed ball-type combined stuffing surface forms and the microorganism in the sewage is degraded by organism and the catalysis ammonia nitrogen is oxidized to nitrite, the time of each aeration phase is 1.5～2 hours;
Fill phase: stop aeration, 20%～40% of treatment sewage total amount in the cycle of operation is heated to 26 ℃～33 ℃ in the preheating tank after, join in the reaction vessel; Flooding time is 0.05～0.2 hour;
The anoxic stage: the microorganism on the microbial film and in the sewage utilizes nitrite and the ammonia nitrogen in the water to carry out Anammox reaction generation nitrogen, and the time in each anoxic stage is 1～1.5 hour;
The 4th aeration and anoxic circulation comprise the 4th aeration phase and the 4th anoxic stage and precipitation phase,
The 4th aeration phase: micro-air is provided in reaction vessel, and the microorganism on the microbial film and in the sewage is degraded by organism and the catalysis ammonia nitrogen is oxidized to nitrite, and aeration time is 1.5～2 hours;
The 4th anoxic stage and precipitation phase: stop aeration, microorganism on the microbial film and in the sewage utilizes nitrite and the ammonia nitrogen in the water to carry out Anammox reaction generation nitrogen, further remove remaining ammonia nitrogen and nitrite nitrogen, simultaneously the sewage of handling is precipitated, last 1～2 hour;
III) drainage period: the sewage after will handling is discharged reaction vessel.
2. short distance nitration-anaerobic ammoxidation sequencing batch biofilm nitrogen rejection facility, it is characterized in that it comprises the preheating tank (1) that can heat to sewage, reaction vessel (3), aerator (9) and aeration head (7), preheating tank (1) links to each other with the set water-in in reaction vessel (3) upper end by pipeline, be equiped with fixed ball-type combined stuffing (4) and well heater (6) in the reaction vessel (3), the lower end of reaction vessel (3) is provided with water outlet (13), the middle part is provided with thief hole (12), the top is provided with automatic air pressure compensation flap (11), aeration head (7) is installed in reaction vessel (3) bottom, be positioned at ball-type combined stuffing (4) below, aerator (9) places reaction vessel (3) one sides, and the aeration head (7) interior with being loaded on reaction vessel (3) by pipeline links to each other.
3. short distance nitration-anaerobic ammoxidation sequencing batch biofilm nitrogen rejection facility according to claim 2, it is characterized in that being provided with electromagnetic dosing pump (2) between described preheating tank (1) and the reaction vessel (3), be provided with gas meter (8) between aerator (9) and the aeration head (7), be provided with temperature sensor (5) in the reaction vessel (3), water outlet (13) locates to have magnetic valve, and reaction vessel (3) is provided with on one side and can realizes the automatic control section (10) of control automatically to this device.
4. according to claim 2 or 3 described short distance nitration-anaerobic ammoxidation sequencing batch biofilm nitrogen rejection facilitys, it is characterized in that being equiped with filler fixed support (14) in the described reaction vessel (3), ball-type combined stuffing (4) is loaded in the filler fixed support (14).
5. short distance nitration-anaerobic ammoxidation sequencing batch biofilm nitrogen rejection facility according to claim 4 is characterized in that the micro-pore aeration dish of described aeration head (7) for the aeration that made progress by fixed ball-type combined stuffing (4) bottom vertical.
6. short distance nitration-anaerobic ammoxidation sequencing batch biofilm nitrogen rejection facility according to claim 4, it is characterized in that described ball-type combined stuffing (4) is made up of hollow fishnet shape spherical housing and the inside stuffing matter that is loaded in the shell, the admission space of inside stuffing matter accounts for 30～50% of hollow fishnet shape spherical housing hollow space volume.
7. short distance nitration-anaerobic ammoxidation sequencing batch biofilm nitrogen rejection facility according to claim 6, the material that it is characterized in that described hollow fishnet shape spherical housing is polyethylene, polyvinyl chloride, polystyrene, polypropylene or urethane, and its diameter is 50～150mm.
8. short distance nitration-anaerobic ammoxidation sequencing batch biofilm nitrogen rejection facility according to claim 7 is characterized in that described inside stuffing matter is made up of with 1: 1 volume proportion biological material and artificial macromolecular material.
9. short distance nitration-anaerobic ammoxidation sequencing batch biofilm nitrogen rejection facility according to claim 8 is characterized in that described biological material is the hollow ring of natural air drying, ring diameter 5～8mm, long 10～20mm; Artificial macromolecular material is the flexible filament thing of polyethylene, polyvinyl chloride, polystyrene, polypropylene or urethane plastic, and the filament diameter is 0.5～1mm.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2006100321474A CN100402444C (en) | 2006-08-29 | 2006-08-29 | Operation mode and apparatus of short distance nitration-anaerobic ammoxidation batched biomembrane denitrogenation |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2006100321474A CN100402444C (en) | 2006-08-29 | 2006-08-29 | Operation mode and apparatus of short distance nitration-anaerobic ammoxidation batched biomembrane denitrogenation |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1927739A CN1927739A (en) | 2007-03-14 |
| CN100402444C true CN100402444C (en) | 2008-07-16 |
Family
ID=37857898
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNB2006100321474A Expired - Fee Related CN100402444C (en) | 2006-08-29 | 2006-08-29 | Operation mode and apparatus of short distance nitration-anaerobic ammoxidation batched biomembrane denitrogenation |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN100402444C (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109607777A (en) * | 2019-01-31 | 2019-04-12 | 苏伊士水务工程有限责任公司 | Sewage advanced treatment system and method by using anaerobic ammonia oxidation technology |
Families Citing this family (40)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101514064B (en) * | 2009-04-03 | 2011-06-15 | 湖南大学 | Biological denitrification device of sequencing batch internal circulation biological denitrification process |
| CN101628772B (en) * | 2009-07-24 | 2011-06-22 | 北京工业大学 | Short distance denitrifying dephosphatation double-sludge technique taking granular sludge as medium and device thereof |
| CN101993148B (en) * | 2010-12-16 | 2012-06-06 | 哈尔滨工业大学 | Sequencing-batch membrane bioreactor |
| CN102173533B (en) * | 2011-02-28 | 2012-08-08 | 桂林理工大学 | Efficient anaerobic ammonium oxidation sewage treatment method |
| CN102627373A (en) * | 2011-06-29 | 2012-08-08 | 兰州理工大学 | Micro-polluted water resource pollution treatment method |
| CN102718314B (en) * | 2012-05-24 | 2013-07-24 | 北京工业大学 | Method for quick starting of anaerobic ammonium oxidation technology at room temperature in low matrix |
| JP6230032B2 (en) * | 2012-09-13 | 2017-11-15 | ディー．シー． ウォーター アンド スーアー オーソリティー | Method and apparatus for denitrification in wastewater treatment |
| CN103382049B (en) * | 2012-11-22 | 2014-12-17 | 浙江工商大学 | Sequencing batch activated sludge reactor for sewage treatment and treatment process |
| CN102964035B (en) * | 2012-12-06 | 2013-10-23 | 北京城市排水集团有限责任公司 | Device for autotrophic nitrogen removal of composite biological membrane and operation method |
| CN103172175B (en) * | 2013-03-22 | 2014-09-17 | 北京交通大学 | Method and device for synchronous partial nitrification and biofilm anaerobic ammonia oxidation |
| WO2015019083A1 (en) * | 2013-08-06 | 2015-02-12 | Bactest Limited | Respirometer |
| CN103420481B (en) * | 2013-08-19 | 2015-03-25 | 北京工业大学 | Anaerobic ammonia oxidized coupled heterotrophic denitrifying denitrification method |
| CN103601341B (en) * | 2013-11-22 | 2015-05-20 | 北京工业大学 | SBR (Sequencing Batch Reactor) and SBBR (Sequencing Biofilm Batch Reactor) municipal sewage high-efficiency biological treatment method and device based on anaerobic ammonia oxidation |
| CN103663725B (en) * | 2013-12-05 | 2015-07-29 | 北京交通大学 | Based on Continuous Flow biological denitrification method and the device of granule sludge |
| CN103708616A (en) * | 2014-01-02 | 2014-04-09 | 济南大学 | Method for culturing nitrosation granular sludge by matching with anaerobic ammonia oxidation |
| CN104817223B (en) * | 2015-04-09 | 2016-08-17 | 浙江大学 | Chemical-biological combined removal nitrate nitrogen and the reactor of ammonia nitrogen |
| CN104787889B (en) * | 2015-04-29 | 2017-06-06 | 北京工业大学 | The method for recovering municipal sewage short distance Anammox using the micro- exposure of hypoxemia and anoxia stirring |
| CN105198084B (en) * | 2015-10-25 | 2017-11-14 | 北京工业大学 | A kind of apparatus and method that advanced nitrogen is realized by preamble part denitrification coupling ammoxidation DEAMOX techniques |
| CN106966510A (en) * | 2016-01-14 | 2017-07-21 | 中南大学 | A kind of efficient denitrification bio-carrier and its application in sewage disposal |
| CN105884026B (en) * | 2016-04-27 | 2019-04-02 | 北京清源中科环保科技有限公司 | A kind of method of the microbe carrier and the formula pollution administration water body that drifts along of core shell structure |
| CN105859042A (en) * | 2016-05-18 | 2016-08-17 | 哈尔滨工业大学深圳研究生院 | Sewage treatment method and system |
| CN106673205B (en) * | 2016-12-12 | 2019-06-11 | 同济大学 | The quick start method of integral type autotrophic denitrification system |
| CN106966498B (en) * | 2017-03-31 | 2020-04-17 | 太原理工大学 | Shortcut nitrification and denitrification coupled anaerobic ammonia oxidation denitrification process and control method |
| CN107032506B (en) * | 2017-05-24 | 2020-02-11 | 北京工业大学 | Device and method for treating domestic sewage through sectional effluent shortcut nitrification-Anammox/denitrification |
| CN107381788B (en) * | 2017-09-11 | 2020-05-05 | 河南工业大学 | Two-stage membrane aeration biomembrane reactor for advanced wastewater treatment |
| CN108658226B (en) * | 2018-05-14 | 2020-12-04 | 北京协同创新研究院 | Composite carrier capable of promoting short-cut nitrification starting and stable operation and preparation method thereof |
| CN109607769B (en) * | 2019-01-15 | 2022-12-27 | 青岛大学 | Optimized starting method for municipal sewage SPNA process |
| CN109626574B (en) * | 2019-01-15 | 2021-12-28 | 青岛大学 | Device and method for treating municipal sewage by two-stage SPNA denitrification process |
| CN109626573B (en) * | 2019-01-15 | 2022-12-27 | 青岛大学 | Method for enhancing denitrification performance of municipal sewage SPNA system by biological addition |
| CN109699560B (en) * | 2019-02-02 | 2023-07-21 | 青岛理工大学 | Internal circulation biological membrane prawn culture system and application method thereof |
| CN109650543B (en) * | 2019-02-18 | 2022-01-07 | 青岛大学 | SPNA integrated denitrification method for treating low-matrix wastewater under continuous flow condition |
| CN109987703A (en) * | 2019-04-16 | 2019-07-09 | 清华大学深圳研究生院 | Integrated short distance nitration-anaerobic ammoxidation sewage treatment acclimation method and device |
| CN110272890A (en) * | 2019-05-27 | 2019-09-24 | 天津科技大学 | Complex microorganism carrier and preparation method and the application for having autotrophic denitrification function |
| CN110697890A (en) * | 2019-09-01 | 2020-01-17 | 桂林理工大学 | Operation transformation method based on Anammox-MBR process of urban sewage treatment plant |
| CN110627321A (en) * | 2019-09-27 | 2019-12-31 | 深圳市钰华朗科技有限公司 | Aged refuse landfill leachate full-quantization treatment process and system |
| CN111470629A (en) * | 2020-04-17 | 2020-07-31 | 西安建筑科技大学 | Facultative active sludge sewage treatment method |
| CN111606419B (en) * | 2020-06-01 | 2022-05-06 | 北京工业大学 | Sewage treatment system and method with self-sufficient energy |
| CN111995083B (en) * | 2020-08-25 | 2022-05-06 | 浙江京禾水务科技有限公司 | Intelligent real-time aeration control method for anaerobic ammonia oxidation reaction process |
| CN113461156A (en) * | 2021-05-08 | 2021-10-01 | 光大水务科技发展（南京）有限公司 | Sewage treatment method for promoting shortcut nitrification-denitrification coupling anaerobic ammonia oxidation |
| CN116177802A (en) * | 2023-02-22 | 2023-05-30 | 中交第二公路勘察设计研究院有限公司 | Modularized biodegradation device and method for bionic dolphin |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1293154A (en) * | 2000-11-23 | 2001-05-02 | 中国冶金建设集团鞍山焦化耐火材料设计研究总院 | Process for removing ammoniacal nitrogen from sewage of coking |
| CN1569690A (en) * | 2004-03-26 | 2005-01-26 | 彭永臻 | SBR alternant aerobic/anaerobic technology for biological denitrification and real time control device and method thereof |
-
2006
- 2006-08-29 CN CNB2006100321474A patent/CN100402444C/en not_active Expired - Fee Related
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1293154A (en) * | 2000-11-23 | 2001-05-02 | 中国冶金建设集团鞍山焦化耐火材料设计研究总院 | Process for removing ammoniacal nitrogen from sewage of coking |
| CN1569690A (en) * | 2004-03-26 | 2005-01-26 | 彭永臻 | SBR alternant aerobic/anaerobic technology for biological denitrification and real time control device and method thereof |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109607777A (en) * | 2019-01-31 | 2019-04-12 | 苏伊士水务工程有限责任公司 | Sewage advanced treatment system and method by using anaerobic ammonia oxidation technology |
Also Published As
| Publication number | Publication date |
|---|---|
| CN1927739A (en) | 2007-03-14 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN100402444C (en) | Operation mode and apparatus of short distance nitration-anaerobic ammoxidation batched biomembrane denitrogenation | |
| CN101514064B (en) | Biological denitrification device of sequencing batch internal circulation biological denitrification process | |
| CN101759323B (en) | Treatment combined process for pig farm waste water with high nitrogen content | |
| CN101786770B (en) | Oligodynamic moving bed sanitary sewage disposal system | |
| CN101381163B (en) | Biochemical degradation system coupling hydrolytic acidification-anaerobic and aerobic | |
| CN102153239B (en) | Process and system for carrying out high-efficiency denitrification and dephosphorization treatment on urban sewage | |
| CN101565258B (en) | Compound technology of biomembrane and granular sludge for treating sulfur-bearing organic wastewater | |
| CN103922538B (en) | Livestock and poultry breeding wastewater treatment method | |
| CN103435155B (en) | Low-energy and intelligent three-dimensional ecological self-refluxing circulation nitrification method and apparatus | |
| CN206502723U (en) | A kind of reinforced phosphor-removing and sludge decrement type sewage-treatment plant | |
| CN101786730A (en) | Method and equipment for cross backflow two-stage double-expansion granular sludge treatment of coking wastewater | |
| CN101774729B (en) | Integral biological reactor based on short-range simultaneous denitrification and application thereof | |
| CN102060423A (en) | Method for acquiring denitrified carbon source by fermenting surplus sludge | |
| CN104944701A (en) | Method for enhancing sewage nitrogen and phosphorus removal and saving energy and reducing consumption based on pulse aeration | |
| CN103435156B (en) | Intelligent three-dimensional ecological external circulation nitrification method and apparatus | |
| CN105948410A (en) | IFBR-EGSB-SBR (Improved Fluidized Bed Reactor-Expanded Granular Sludge Bed-Sequencing Batch Reactor) combined process for treating chemical wastewater | |
| CN105084536A (en) | Biologically enhanced treatment method for medium-and-low concentration ammonia-nitrogen wastewater | |
| CN103435157B (en) | Low-energy and intelligent three-dimensional ecological internal circulation nitrification method and apparatus | |
| CN110217887A (en) | A kind of the substep water inlet sequencing batch reactor and method of processing waste water of livestock poultry anaerobic digestion solution | |
| CN204385034U (en) | A kind of composite rotating bio-disc waste disposal plant | |
| CN110183032A (en) | A kind of livestock breeding wastewater recycling treatment system | |
| CN110002683A (en) | Handle the continuous flow A of moderate strength municipal sewage containing ammonia nitrogen2O couples UASB denitrification dephosphorization apparatus and method | |
| CN202625975U (en) | Device for strengthening synchronous nitrification and denitrification (SND) biological nitrogen and phosphorus removal through step-feeding process | |
| CN105152330A (en) | Treatment method for landfill leachate | |
| CN103086561A (en) | Carbon and nitrogen removal system based on moving bed biomembrane reactor |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20080716 Termination date: 20140829 |
|
| EXPY | Termination of patent right or utility model |