CN202379808U - Terminal garbage percolate shortcut nitrification and anaerobic ammonia oxidation combination denitrification device - Google Patents
Terminal garbage percolate shortcut nitrification and anaerobic ammonia oxidation combination denitrification device Download PDFInfo
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- CN202379808U CN202379808U CN2011205126864U CN201120512686U CN202379808U CN 202379808 U CN202379808 U CN 202379808U CN 2011205126864 U CN2011205126864 U CN 2011205126864U CN 201120512686 U CN201120512686 U CN 201120512686U CN 202379808 U CN202379808 U CN 202379808U
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Abstract
The utility model relates to a terminal garbage percolate shortcut nitrification and anaerobic ammonia oxidation combination denitrification device, and belongs to the technical field of biological denitrification of high-concentration ammonia nitrogen garbage percolate with low carbon nitrogen (C/N) ratio. The device comprises a leachate raw water tank, an A/O shortcut nitrification reactor, a sedimentation tank and an anaerobic ammonia oxidation reactor; the leachate raw water tank is communicated with a first grid chamber, namely an anoxic zone, of the shortcut nitrification reactor; the sedimentation tank is communicated with the anaerobic ammonia oxidation reactor; and the anaerobic ammonia oxidation reactor is provided with a self-circulation pipeline and a water outlet return pipe where liquid flows back to the A/O shortcut nitrification reactor. The method comprises the following steps: the A/O shortcut nitrification reactor and the anaerobic ammonia oxidation reactor are started in sequence, the A/O shortcut nitrification reactor and the anaerobic ammonia oxidation reactor system are connected in series for operation, and stoste is diluted by outlet water circulation of the anaerobic ammonia oxidation reactor. The device provided by the device is suitable for shortcut nitrification and denitrification of terminal garbage percolate in a refuse landfill and has the advantages that the process is advanced, the structure is simple, and the effects of energy conservation and consumption reduction are obvious.
Description
Technical field
The utility model relates to percolate short distance nitration and Anammox combined denitrification device in a kind of late period; Belong to low-carbon and nitrogen (C/N) than high-concentration ammonia nitrogenous wastewater bio-denitrification technology field, be applicable to the biological denitrificaion of the high ammonia-nitrogen wastewater of low C/N ratios such as percolate in late period.
Background technology
In recent years, along with the continuous increase of MSW output, landfill method became most widely used in the world processing and method of disposal gradually.The percolate that landfill produces because of have complicated component, water quality and quantity variation greatly, organism and water quality characteristicses such as ammonia nitrogen concentration height, the imbalance of microbial nutrition element ratio, make it be treated as in the international coverage one of unsolved difficult problem still.Adopt the processing percolate that single treatment technology often can not economical and efficient, need the process integration of different characteristics to use.The famine of organic carbon source is the barrier that late period, the percolate nitric efficiency can't improve, and adds the expense that organic carbon source can significantly increase sewage water denitrification.Therefore, need to propose the apparatus and method of more efficiently denitrogenation.
Bio-denitrifying sewage is through nitrated with NH
4 +-N is converted into NO
3 --N passes through denitrification again with NO
3 --N is converted into nitrogen and from water, overflows.The denitrification stage is with NO
3 --N is an electron acceptor(EA), and organism is converted into nitrogen with ammonia nitrogen and accomplishes biological denitrificaion as electron donor.But for high NH
4 +The denitrogenation of-N percolate in late period, its C/N is than only about 1, because the organic carbon source wretched insufficiency causes the traditional biological nitric efficiency to reach about 10%.
And Anammox has following advantage: because anaerobic ammonia oxidizing bacteria is an autotrophic bacteria; Carbonate/carbonic acid gas is the required inorganic carbon source of its growth; So need not molecular oxygen, the oxidation of ammonia nitrogen participates in; The reduction of nitrite nitrogen simultaneously also need not organic carbon source, and this will reduce the working cost of sewage aerobic biological denitrificaion greatly; Rate of increase of Anammox mikrobe (doubling time is 11d) and productive rate (0.11g [VSS]/g [NH
4 +]) be low-down, so sludge yield is low, yet the transformation efficiency of nitrogen but is 0.25mg [N]/(mg [SS] d), and is equal to each other with traditional aerobic nitrification; Under the condition that does not add any pharmaceutical chemicals, can reduce the working cost of sewage work, can realize the efficient removal of nitrogen again.As far as the percolate of low C/N than high ammonia nitrogen, realize that the Anammox reaction is the optimal path of its denitrogenation, also be simultaneously the denitride technology that is fit to the most with its water quality characteristics.
The utility model content
The purpose of the utility model is in order to solve the problems of the technologies described above, and proposes percolate short distance nitration and Anammox combined denitrification device in a kind of late period, promptly at first realizes percolated liquid in city refuse landfill middle and high concentration NH
4 +The short distance nitration reaction of-N then realizes the Anammox reaction again, finally realizes the apparatus and method of the percolate autotrophic denitrification of economical and efficient.
The purpose of the utility model realizes through following technical scheme:
A kind of late period percolate short distance nitration and Anammox combined denitrification device, it is characterized in that: said device is provided with percolate raw water box, A/O short distance nitration reactor drum, settling tank, anaerobic ammonia oxidation reactor; Be provided with heating water tank and temperature control heating unit in the middle of the percolate raw water box; Anaerobic ammonia oxidation reactor top supernatant mixes with percolate in the percolate raw water box through first return line and the 4th peristaltic pump; Second water inlet pipe and first peristaltic pump through A/O short distance nitration reactor drum is connected with the first lattice chamber as the oxygen-starved area of A/O short distance nitration reactor drum again, and whisking appliance is installed in this head lattice chamber; A/O short distance nitration reactor drum is divided into 4-8 lattice chamber with the dividing plate of the water hole that is crisscross arranged up and down; Each bottom, lattice chamber is provided with aeration head, and each top, lattice chamber is provided with air control valve, and aeration pump is communicated with aeration head through aeration tube and gas meter; A/O short distance nitration reactor drum is communicated with settling tank through first rising pipe; The settling tank bottom is that first lattice chamber is communicated with through the 3rd peristaltic pump and second return line with A/O short distance nitration reactor drum oxygen-starved area; Settling tank is provided with pipe core, below pipe core, is provided with the taper reflector; Settling tank is provided with several first sampling valves from top to bottom, and settling tank is connected with anaerobic ammonia oxidation reactor through second rising pipe and the 5th peristaltic pump;
Anaerobic ammonia oxidation reactor is provided with temperature control heating zone device and cylindrical sludge bed, and temperature control heating zone device is arranged at up and down between the cylindrical sludge bed, and cylindrical sludge bed top is provided with triphase separator and top seal plate; The top of this triphase separator is communicated with vapor pipe, alkali lye bottle and gas meter; Cylindrical sludge bed top supernatant flow into cylindrical sludge bed bottom through the 3rd return line and the 6th peristaltic pump and circulates; Settling tank is communicated with the bottom of anaerobic ammonia oxidation reactor through second rising pipe and the 5th peristaltic pump, and the percolate raw water box is communicated with the anaerobic ammonia oxidation reactor bottom through first water inlet pipe and second peristaltic pump; Water is overflowed through the discharging of the 3rd rising pipe in cylindrical sludge bed top, and the anaerobic ammonia oxidation reactor outside is provided with several second sampling valves from top to bottom.
Utilize said apparatus to carry out percolate even flow short distance nitration and the method for Anammox combined denitrification in late period, it is characterized in that, may further comprise the steps:
Step 1: start A/O short distance nitration reactor drum: the nitrifying sludge with actual cities sewage work is that seed sludge injects A/O short distance nitration reactor drum, and sludge concentration is 5000kg MLSS/m
3About; With the actual cities consumer waste infiltration liquid is stoste, is injected into the percolate raw water box after the dilution of employing tap water, and through adding NaHCO
3The pH value of the percolate after the dilution in the raw water box is maintained about 8.0; Pump into the oxygen-starved area of A/O short distance nitration reactor drum through second water inlet pipe and first peristaltic pump; The aerating system that subsequent start-up aeration pump, air control valve and aeration head are formed carries out nitrated to the percolate that flows into A/O short distance nitration reactor drum; And regulate air control valve and make nitration reaction process dissolved oxygen be maintained 2mg/L, keep into water NH through regulating first peristaltic pump simultaneously
4 +-N the ALR=0.4kgNH that loads
4 +-N/m
3D changes in above-mentioned scope through keeping pH value and ALR, makes average free ammonia FA concentration in the A/O short distance nitration reactor drum about 20mg/L, moves A/O short distance nitration reactor drum under these conditions, as water outlet nitrous acid nitrogen NO
2 --N cumulative percentage was greater than 95% o'clock, and the A/O short distance nitration is achieved and keeps, and had possessed the influent quality requirement of anaerobic ammonia oxidation reactor;
Step 2: start anaerobic ammonia oxidation reactor: the mud with certain anaerobic ammoxidation activity in the pilot scale anaerobic ammonia oxidation reactor of certain sewage work is added to anaerobic ammonia oxidation reactor, and sludge concentration is 5kg MLSS/m
3Make the anaerobic ammonia oxidation reactor temperature be controlled at 35 ℃ through temperature control heating zone device, A/O short distance nitration reactor drum water outlet nitrite nitrogen concentration is diluted to 100mg/L with tap water, and according to NH
4 +-N/NO
2 --N ratio is to be mixed into percolate stoste at 1: 1.32, and the above-mentioned mixed solution after will diluting simultaneously is pumped into anaerobic ammonia oxidation reactor according to the flow of 30L/d; NH in the anaerobic ammonia oxidation reactor water outlet
4 +-N and NO
2 --N concentration is during all less than 15mg/L, and the Anammox reaction is achieved and keeps;
Step 3: after A/O short distance nitration reactor drum and anaerobic ammonia oxidation reactor are accomplished startup respectively; With its series operation: promptly the percolate in the percolate raw water box pumps into the oxygen-starved area of A/O short distance nitration reactor drum through second water inlet pipe and first peristaltic pump; Simultaneously the mud in the settling tank is back to the oxygen-starved area through the 3rd peristaltic pump according to 100% ratio; Then the mixed solution in the oxygen-starved area enters into the aerobic aeration district completion short distance nitration at aeration head place; Mixed solution flow into through first rising pipe and carries out mud-water separation in the settling tank in the A/O short distance nitration reactor drum (7); The supernatant of settling tank pumps into the anaerobic ammonia oxidation reactor bottom through second rising pipe and the 5th peristaltic pump, and the percolate raw water box pumps into anaerobic ammonia oxidation reactor through first water inlet pipe and second peristaltic pump and accomplishes the Anammox reaction with the nitrification liquid that flows into from settling tank; Work as NO
2 --N/NH
4 +-N＞1.32 o'clock suitably increase the flow that gets into anaerobic ammonia oxidation reactor from the percolate raw water box, work as NO on the contrary
2 --N/NH
4 +-N＜1.32 o'clock suitable the flow that gets into anaerobic ammonia oxidation reactor from the percolate raw water box that reduces; When the total nitrogen of anaerobic ammonia oxidation reactor load reaches 1kg TN/m
3More than the d, and water outlet NH
4 +-N and NO
2 --N clearance was greater than 90% o'clock, and device has been realized the whole process autotrophic denitrification process of percolate.
Beneficial effect
The utility model a kind of late period the percolate short distance nitration and Anammox combined denitrification device compared with prior art, have advantage:
The whole process autotrophic denitrification process of percolate:
1) under the condition that does not add additional carbon, realize the high-efficiency biological denitrification of percolate, solved ammonia nitrogen in high density, low ratio of carbon to ammonium late period percolate a processing difficult problem, greatly reduce operation and construction cost.
2) realization of short distance nitration makes the transform mode of ammonia nitrogen be different from traditional nitrated mode, has reduced energy consumption, has improved efficient, has reduced sludge yield.
3) Anammox total nitrogen volumetric loading can reach 0.8kg TN/m
3More than the d, need not consume basicity, further reduce working cost.
4) after this technology maturation operation, need not add outer adding medicine, and need not add water source dilution stoste, simplify management process, can directly handle the percolate in late period of high-concentration ammonia-nitrogen.
Description of drawings
Fig. 1 is the percolate short distance nitration and Anammox combined denitrification apparatus structure synoptic diagram in late period of the utility model.
Among the figure: 1-percolate raw water box; 2-temperature control heating unit; 3-first peristaltic pump; The 4-gas meter; The 5-whisking appliance; The 6-air control valve; 7-A/O short distance nitration reactor drum; The 8-dividing plate; The 9-settling tank; The 10-pipe core; 11-top seal plate; The 12-gas meter; 13-alkali lye bottle; The 14-triphase separator; The 15-anaerobic ammonia oxidation reactor; 16-cylindrical sludge bed; 17-second sampling valve; 18-temperature control heating zone device; 19-second peristaltic pump; The 20-aeration pump; 21-the 4th peristaltic pump; The 22-aeration head; 23-the 3rd peristaltic pump; 24-taper reflector; 25-first sampling valve; 26-the 5th peristaltic pump; 27-the 6th peristaltic pump; The 28-heating water tank; 29-first water inlet pipe; 30-first return line; 31-second water inlet pipe; The 32-aeration tube; 33-second return line; 34-first rising pipe; 35-second rising pipe; 36-the 3rd return line; 37-the 3rd rising pipe; The 38-vapor pipe.
Embodiment
Below in conjunction with accompanying drawing and embodiment the application's patent is further described: as shown in Figure 1; A kind of late period percolate short distance nitration and Anammox combined denitrification apparatus and method, said device is provided with percolate raw water box 1, A/O short distance nitration reactor drum 7, settling tank 9, anaerobic ammonia oxidation reactor 15; Be provided with heating water tank 28 and temperature control heating unit 2 in the middle of the percolate raw water box 1; Anaerobic ammonia oxidation reactor 15 top supernatants mix with percolate in the percolate raw water box 1 through first return line 30 and the 4th peristaltic pump 21; Second water inlet pipe 31 and first peristaltic pump 3 through A/O short distance nitration reactor drum 7 is connected with the first lattice chamber as the oxygen-starved area of A/O short distance nitration reactor drum 7 again, and whisking appliance 5 is installed in this head lattice chamber; Be crisscross arranged the up and down dividing plate 8 of water hole of A/O short distance nitration reactor drum 7 usefulness is divided into 4-8 lattice chamber; Each bottom, lattice chamber is provided with aeration head 22, and each top, lattice chamber is provided with air control valve 6, and aeration pump 20 is communicated with aeration head 22 through aeration tube 32 and gas meter 4; A/O short distance nitration reactor drum 7 is communicated with settling tank 9 through first rising pipe 34; Settling tank 9 bottoms are that first lattice chamber is communicated with through the 3rd peristaltic pump 23 and second return line 33 with A/O short distance nitration reactor drum 7 oxygen-starved areas; Settling tank 9 is provided with pipe core 10, below pipe core 10, is provided with taper reflector 24; Settling tank 9 is provided with several first sampling valves 25 from top to bottom, and settling tank 9 is connected with anaerobic ammonia oxidation reactor 15 through second rising pipe 35 and the 5th peristaltic pump 26;
Anaerobic ammonia oxidation reactor 15 is provided with temperature control heating zone device 18 and cylindrical sludge bed 16, and temperature control heating zone device 18 is arranged at up and down between the cylindrical sludge bed 16, and cylindrical sludge bed 16 tops are provided with triphase separator 14 and top seal plate 11; The top of this triphase separator 14 is communicated with vapor pipe 38, alkali lye bottle 13 and gas meter 12; Cylindrical sludge bed 16 top supernatants flow into cylindrical sludge bed 16 bottoms through the 3rd return line 36 and the 6th peristaltic pump 27 and circulate; Settling tank 9 is communicated with the bottom of anaerobic ammonia oxidation reactor 15 through second rising pipe 35 and the 5th peristaltic pump 26, and percolate raw water box 1 is communicated with anaerobic ammonia oxidation reactor 15 bottoms through first water inlet pipe 29 and second peristaltic pump 19; Water is overflowed through 37 dischargings of the 3rd rising pipe in cylindrical sludge bed 16 tops, and anaerobic ammonia oxidation reactor 15 outsides are provided with several second sampling valves 17 from top to bottom.
Percolate raw water box (1) internal diameter is 40cm, highly is 60cm, and cubic capacity is 50L.A/O short distance nitration reactor drum (7) is respectively 10L with the useful volume of anaerobic ammonia oxidation reactor (15); 10L; The useful volume of settling tank (9) is 20L; A/O short distance nitration reactor drum (7) is of a size of L * B * H=50cm * 10cm * 30cm, is equally divided into 8 lattice chambers, and lattice chamber the 1st is the anoxia stirring district.Anaerobic ammonia oxidation reactor (15) is made up of upper and lower two portions; The internal diameter on top, external diameter and highly be respectively 12,13,50cm; The internal diameter of lower section, external diameter and highly be respectively 8,9,140cm, upper and lower two portions are by truncated cone-shaped synthetic glass pipe coupling, useful volume is 11.5L.
Get Beijing and fill out the percolate that rubbish buries, its ammonia nitrogen concentration is up to 2300mg/L, COD/NH
4 +-N=1.5 is typical case's percolate in late period.
(1) start A/O short distance nitration reactor drum 7: the nitrifying sludge with actual cities sewage work is that seed sludge injects A/O short distance nitration reactor drum 7, and sludge concentration is 5000kg MLSS/m
3About; With the actual cities consumer waste infiltration liquid is stoste, is injected into percolate raw water box 1 after the dilution of employing tap water, and through adding NaHCO
3The pH value of the percolate after the dilution in the raw water box 1 is maintained about 8.0; Be pumped into the oxygen-starved area of A/O short distance nitration reactor drum 7 through second water inlet pipe 31 and first peristaltic pump 3; The aerating system that subsequent start-up aeration pump 20, air control valve 6 and aeration head 22 are formed carries out nitrated to the percolate that flows into A/O short distance nitration reactor drum 7; And regulate air control valve 6 and make nitration reaction process dissolved oxygen be maintained 2mg/L, keep into water NH through regulating first peristaltic pump 3 simultaneously
4 +-N the ALR=0.4kgNH that loads
4 +-N/m
3D changes in above-mentioned scope through keeping pH value and ALR, makes average free ammonia FA concentration in the A/O short distance nitration reactor drum 7 about 20mg/L, moves A/O short distance nitration reactor drum 7 under these conditions, as water outlet nitrous acid nitrogen NO
2 --N cumulative percentage was greater than 95% o'clock, and the A/O short distance nitration is achieved and keeps, and had possessed the influent quality requirement of anaerobic ammonia oxidation reactor;
(2) start anaerobic ammonia oxidation reactor 15: the mud with certain anaerobic ammoxidation activity in the pilot scale anaerobic ammonia oxidation reactor of certain sewage work is added to anaerobic ammonia oxidation reactor to anaerobic ammonia oxidation reactor 15, and sludge concentration is 5kgMLSS/m
3Make anaerobic ammonia oxidation reactor 15 temperature be controlled at 35 ℃ through temperature control heating zone device 18, A/O short distance nitration reactor drum 7 water outlet nitrite nitrogen concentration are diluted to 100mg/L with tap water, and according to NH
4 +-N/NO
2 --N ratio is to be mixed into percolate stoste at 1: 1.32, and the above-mentioned mixed solution after will diluting simultaneously is pumped into anaerobic ammonia oxidation reactor 15 according to the flow of 30L/d; NH in anaerobic ammonia oxidation reactor water outlet 15
4 +-N and NO
2 --N concentration is during all less than 15mg/L, and the Anammox reaction is achieved and keeps;
(3) after A/O short distance nitration reactor drum 7 is accomplished startup respectively with anaerobic ammonia oxidation reactor 15; With its series operation: promptly the percolate in the percolate raw water box 1 is pumped into the oxygen-starved area of A/O short distance nitration reactor drum 7 through second water inlet pipe 31 and first peristaltic pump 3; Simultaneously the mud in the settling tank 9 is back to the oxygen-starved area through the 3rd peristaltic pump 23 according to 100% ratio; Then the mixed solution in the oxygen-starved area enters into the aerobic aeration district completion short distance nitration at aeration head 22 places; Mixed solution flow into through first rising pipe 34 and carries out mud-water separation in the settling tank 9 in the A/O short distance nitration reactor drum 7; The supernatant of settling tank 9 is pumped into anaerobic ammonia oxidation reactor 15 bottoms through second rising pipe 35 and the 5th peristaltic pump 26, and percolate raw water box 1 pumps into anaerobic ammonia oxidation reactor 15 through first water inlet pipe 29 and second peristaltic pump 19 and accomplishes the Anammox reaction with the nitrification liquid that flows into from settling tank 9; Work as NO
2 --N/NH
4 +-N＞1.32 o'clock suitably increase the flow that gets into anaerobic ammonia oxidation reactor 15 from percolate raw water box 1, work as NO on the contrary
2 --N/NH
4 +-N＜1.32 o'clock suitable the flow that gets into anaerobic ammonia oxidation reactor 15 from percolate raw water box 1 that reduces; When the total nitrogen of anaerobic ammonia oxidation reactor 15 load reaches 1kg TN/m
3More than the d, and water outlet NH
4 +-N and NO
2 --N clearance was greater than 90% o'clock, and device has been realized the whole process autotrophic denitrification process of percolate.
(4) A/O short distance nitration reactor drum is at room temperature 20-30 ℃, and the operating temperature of anaerobic ammonium oxidation tank is 35 ℃, and the average ammonia nitrogen concentration of percolate is 2100mg/L, COD/NH
4 +Under the condition of-N=1.5, the test-results of steady running shows: A/O reactor drum short distance nitration pond NO
2 --N cumulative percentage is more than 95%, and the total nitrogen TN＜50mg/L of system's water outlet, TN clearance be greater than 80%, water outlet NH
4 +-N and NO
2 --N is all less than 15mg/L, and the total nitrogen of anaerobic ammonia oxidation reactor load is 0.8Kg TN/m
3About.
More than be first specific embodiment of the utility model, the enforcement of the utility model is not limited thereto.
Claims (1)
- One kind late period percolate short distance nitration and Anammox combined denitrification device, it is characterized in that: said device is provided with percolate raw water box (1), A/O short distance nitration reactor drum (7), settling tank (9), anaerobic ammonia oxidation reactor (15); Be provided with heating water tank (28) and temperature control heating unit (2) in the middle of the percolate raw water box (1); Anaerobic ammonia oxidation reactor (15) top supernatant mixes with percolate in the percolate raw water box (1) through first return line (30) and the 4th peristaltic pump (21); Second water inlet pipe (31) and first peristaltic pump (3) through A/O short distance nitration reactor drum (7) is connected with the first lattice chamber as the oxygen-starved area of A/O short distance nitration reactor drum (7) again, and whisking appliance (5) is installed in this head lattice chamber; A/O short distance nitration reactor drum (7) is divided into 4-8 lattice chamber with the dividing plate (8) of the water hole that is crisscross arranged up and down; Each bottom, lattice chamber is provided with aeration head (22), and each top, lattice chamber is provided with air control valve (6), and aeration pump (20) is communicated with aeration head (22) through aeration tube (32) and gas meter (4); A/O short distance nitration reactor drum (7) is communicated with settling tank (9) through first rising pipe (34); Settling tank (9) bottom is that first lattice chamber is communicated with through the 3rd peristaltic pump (23) and second return line (33) with A/O short distance nitration reactor drum (7) oxygen-starved area; Settling tank (9) is provided with pipe core (10), is provided with taper reflector (24) in pipe core (10) below; Settling tank (9) is provided with several first sampling valves (25) from top to bottom, and settling tank (9) is connected with anaerobic ammonia oxidation reactor (15) through second rising pipe (35) and the 5th peristaltic pump (26);Anaerobic ammonia oxidation reactor (15) is provided with temperature control heating zone device (18) and cylindrical sludge bed (16); Temperature control heating zone device (18) is arranged at up and down between the cylindrical sludge bed (16), and cylindrical sludge bed (16) top is provided with triphase separator (14) and top seal plate (11); The top of this triphase separator (14) is communicated with vapor pipe (38), alkali lye bottle (13) and gas meter (12); Cylindrical sludge bed (16) top supernatant flow into cylindrical sludge bed (16) bottom through the 3rd return line (36) and the 6th peristaltic pump (27) and circulates; Settling tank (9) is communicated with the bottom of anaerobic ammonia oxidation reactor (15) through second rising pipe (35) and the 5th peristaltic pump (26), and percolate raw water box (1) is communicated with anaerobic ammonia oxidation reactor (15) bottom through first water inlet pipe (29) and second peristaltic pump (19); Water is overflowed through the 3rd rising pipe (37) discharging in cylindrical sludge bed (16) top, and anaerobic ammonia oxidation reactor (15) outside is provided with several second sampling valves (17) from top to bottom.
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| CN2011205126864U CN202379808U (en) | 2011-12-09 | 2011-12-09 | Terminal garbage percolate shortcut nitrification and anaerobic ammonia oxidation combination denitrification device |
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|---|---|---|---|
| CN2011205126864U CN202379808U (en) | 2011-12-09 | 2011-12-09 | Terminal garbage percolate shortcut nitrification and anaerobic ammonia oxidation combination denitrification device |
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Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102515429A (en) * | 2011-12-09 | 2012-06-27 | 北京工业大学 | Device and method for combined denitrification of anoxic-oxic (A/O) shortcut nitrification and anaerobic ammonia oxidation of late-stage landfill leachate |
| CN102864068A (en) * | 2012-09-07 | 2013-01-09 | 上海同济环境工程科技有限公司 | Device for fast screening and culturing anaerobic ammonia oxidation microbial communities |
| CN103663692A (en) * | 2013-09-03 | 2014-03-26 | 杭州师范大学 | Integrated shortcut nitrification/anaerobic ammoxidation reactor |
| CN105130118A (en) * | 2015-08-28 | 2015-12-09 | 北京工业大学 | Partial-nitrification-and-anaerobic-ammonia-oxidation-combined denitrification method and device for synchronously treating urban sewage and mature landfill leachate |
| CN110104903A (en) * | 2019-06-10 | 2019-08-09 | 南方创业（天津）科技发展有限公司 | A kind of integration short distance nitration Anammox equipment and its treatment process |
| CN110156280A (en) * | 2019-06-28 | 2019-08-23 | 苏州无为环境科技有限公司 | A kind of wastewater treatment method of organic nitrogen containing high concentration |
| CN112250177A (en) * | 2020-09-23 | 2021-01-22 | 北京工业大学 | Device and method for realizing efficient denitrification of landfill leachate by utilizing shortcut nitrification-anaerobic ammonia oxidation |
-
2011
- 2011-12-09 CN CN2011205126864U patent/CN202379808U/en not_active Withdrawn - After Issue
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102515429A (en) * | 2011-12-09 | 2012-06-27 | 北京工业大学 | Device and method for combined denitrification of anoxic-oxic (A/O) shortcut nitrification and anaerobic ammonia oxidation of late-stage landfill leachate |
| CN102864068A (en) * | 2012-09-07 | 2013-01-09 | 上海同济环境工程科技有限公司 | Device for fast screening and culturing anaerobic ammonia oxidation microbial communities |
| CN103663692A (en) * | 2013-09-03 | 2014-03-26 | 杭州师范大学 | Integrated shortcut nitrification/anaerobic ammoxidation reactor |
| CN105130118A (en) * | 2015-08-28 | 2015-12-09 | 北京工业大学 | Partial-nitrification-and-anaerobic-ammonia-oxidation-combined denitrification method and device for synchronously treating urban sewage and mature landfill leachate |
| CN110104903A (en) * | 2019-06-10 | 2019-08-09 | 南方创业（天津）科技发展有限公司 | A kind of integration short distance nitration Anammox equipment and its treatment process |
| CN110156280A (en) * | 2019-06-28 | 2019-08-23 | 苏州无为环境科技有限公司 | A kind of wastewater treatment method of organic nitrogen containing high concentration |
| CN112250177A (en) * | 2020-09-23 | 2021-01-22 | 北京工业大学 | Device and method for realizing efficient denitrification of landfill leachate by utilizing shortcut nitrification-anaerobic ammonia oxidation |
| CN112250177B (en) * | 2020-09-23 | 2023-02-07 | 北京工业大学 | Device and method for realizing efficient denitrification of landfill leachate by utilizing shortcut nitrification-anaerobic ammonia oxidation |
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