CN101306870A - Heterotrophic nitrification aerobic granule sludge, culture method thereof and use - Google Patents
Heterotrophic nitrification aerobic granule sludge, culture method thereof and use Download PDFInfo
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- CN101306870A CN101306870A CNA2008100454850A CN200810045485A CN101306870A CN 101306870 A CN101306870 A CN 101306870A CN A2008100454850 A CNA2008100454850 A CN A2008100454850A CN 200810045485 A CN200810045485 A CN 200810045485A CN 101306870 A CN101306870 A CN 101306870A
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- 239000010802 sludge Substances 0.000 title claims abstract description 58
- 239000008187 granular material Substances 0.000 title claims description 48
- 238000012136 culture method Methods 0.000 title 1
- 239000002351 wastewater Substances 0.000 claims abstract description 42
- 238000000034 method Methods 0.000 claims abstract description 34
- XKMRRTOUMJRJIA-UHFFFAOYSA-N ammonia nh3 Chemical compound N.N XKMRRTOUMJRJIA-UHFFFAOYSA-N 0.000 claims abstract description 15
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 14
- 241000589776 Pseudomonas putida Species 0.000 claims abstract description 10
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 9
- 241000122973 Stenotrophomonas maltophilia Species 0.000 claims abstract description 9
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- 238000009395 breeding Methods 0.000 claims description 4
- 230000001488 breeding effect Effects 0.000 claims description 4
- 239000008103 glucose Substances 0.000 claims description 4
- 235000015097 nutrients Nutrition 0.000 claims description 4
- 238000012546 transfer Methods 0.000 claims description 4
- 238000005406 washing Methods 0.000 claims description 4
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- 229910002651 NO3 Inorganic materials 0.000 abstract description 3
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- MMDJDBSEMBIJBB-UHFFFAOYSA-N [O-][N+]([O-])=O.[O-][N+]([O-])=O.[O-][N+]([O-])=O.[NH6+3] Chemical compound [O-][N+]([O-])=O.[O-][N+]([O-])=O.[O-][N+]([O-])=O.[NH6+3] MMDJDBSEMBIJBB-UHFFFAOYSA-N 0.000 abstract 1
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
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- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
Abstract
The invention belongs to the environmental microorganism field, in particular relating to heterotrophic nitrification aerobic granular sludge and a cultivation method and an application thereof. An inoculated strain of the aerobic granular sludge is stenotrophomonas maltophilia and pseudomonas putida. Activated carbon is adopted to prefix a functional strain culture, ordinary activated sludge is not inoculated, and the heterotrophic nitrification aerobic granular sludge can be cultivated. The aerobic granular sludge can effectively remove ammonia nitrogen, nitrite nitrogen, nitrate nitrogen and a mixture thereof in a water body, can also simultaneously remove CODCr in organic wastewater, is applicable to the treatment of high concentrated organic nitrogen-containing wastewater and inorganic nitrogen-containing wastewater, and does not produce the accumulation of nitrite and nitrate during the denitrification. The application of the aerobic granular sludge for wastewater treatment has simple process and steady denitrification effect.
Description
Technical field
The invention belongs to the environmental microorganism field, be specifically related to a kind of cultural method and purposes of heterotrophic nitrification aerobic granule sludge.
Background technology
Nitrogenous effluent is the significant problem in the present environmental pollution improvement.Biological denitrificaion is to be acknowledged as one of most economical in the denitrogenation of waste water, effective means at present.At present the bio-denitrification technology characteristics that generally adopt are, denitrification process is that the coupling metabolism by the different microorganism one autotrophy nitrifier of two classes and the heterotrophic denitrification bacterium nitrification and denitrification by separately makes ammonia nitrogen be converted into nitrogen.
The aerobic particle mud technology be developed in recent years than faster one of more novel dirty water living creature processing technique.The particle form that aerobic particle mud is exclusive makes it have the good settleability that active sludge is short of, high biological density.Therefore, the aerobic particle mud technology has become the hot spot technology of sewage disposal, and what a lot of scholars success was arranged turns out aerobic particle mud, and its Preliminary Applications in the test of wastewater treatment, and has been obtained satisfied treatment effect.But, the aerobic particle mud in existing these reports all be by common aerobic or anaerobic sludge as starting culture, under the reinforcement selective action of the domestication of specific substrates and Incubation Condition, form.In this domestication process, function stem quantity increases gradually, needs the regular hour just can finish the enrichment propagation of function yeast.And because this process is the natural enrichment process of bacterial strain in the seed sludge fully, the functional performance of the aerobic particle mud that the seed sludge that different biophase are formed is cultivated is difference to some extent also, makes the functional property of the aerobic particle mud cultivated have certain unstable.Present aerobic denitrogenation granule sludge in the different zones that aerobic particle mud provides, is finished the denitrification functions of nitration denitrification mainly by the microorganism of autotrophy nitrifier with the different physiology monoids of aerobic denitrifying bacteria two classes jointly.The denitrification functions of aerobic denitrogenation granule sludge depends on the cometabolism of this two quasi-microorganism, and the required physiological condition difference of this two quasi-microorganism, so the population regulation and control of autotrophy nitrifier and nitrification bacteria are technological difficulties in the granule sludge.
In recent years, the heterotrophic nitrification phenomenon constantly is found and reports, some nitrification bacterias are separated, and some can also carry out aerobic denitrification simultaneously.Nitrification bacteria is easy to cultivate, and propagation is very fast, and the substrate utilization scope is wide, can stable existence in the wastewater biological denitrificaion system.The heterotrophic nitrification process is compared with the autotrophy nitrifying process, can be in lower temperature and oxyty (0.5~2.8mg/L) time generation, and the water quality requirement to waste water is wideer, C/N is than taking place more than 2.0, therefore in all higher sewage disposal of organic concentration and ammonia nitrogen concentration, the heterotrophic nitrification denitrogenation with autotrophy nitrated denitrogenation compare and have certain advantage.
Therefore, directly the heterotrophic nitrification function stem culture that adopts artificial culture to obtain is an inoculum, shorten the generation time of function stem, in conjunction with the two advantage of heterotrophic nitrification denitrogenation and aerobic particle mud, cultivate the stable efficient denitrification aerobic particle mud of functional performance, not only can obtain good denitrogenation of waste water effect, and can shorten system start time, expand the condition of water quality of temperature applicable range and suitable waste water, realize the denitrogenation of waste water high-efficiency economy, the pollution problem of environment is made contributions for solving serious day by day nitrogenous compound.
Summary of the invention
At above problem, the purpose of this invention is to provide a kind of pure growth with two strain nitrification bacterias is the cultural method of the heterotrophic nitrification aerobic granule sludge of starting culture, and this heterotrophic nitrification aerobic granule sludge has the ability that removes nitrogen and COD in the water body.
Another object of the present invention provides a kind of method of cultivation of being finished the heterotrophic nitrification aerobic granule sludge of ammonia nitrogen removal by allotrophic nitrobacteria, class bacterium---finish by one by nitrification bacteria for the denitrification process of this heterotrophic nitrification aerobic granule sludge, finishes different with the denitrogenation of general aerobic particle mud by autotrophy nitrifier and aerobic denitrifying bacteria two class floras.
Another object of the present invention provides a kind of bacterial strain and pre-fixes method, and making the bacterial strain pure growth is that starting culture can be cultivated aerobic particle mud.
Another object of the present invention provides a kind of culture condition, makes this heterotrophic nitrification aerobic granule sludge can show heterotrophism denitrogenation ability.
Can reach above each purpose by the present invention.
The present invention can be achieved in the following manner:
1. two strain bacterial strains among the present invention are and have the bioactive allotrophic nitrobacteria of denitrogenation, can remove ammonia nitrogen and COD in the water body, and in denitrification process, detect the accumulation less than nitrite and nitrate.More specifically, this two strains bacterial strain is respectively germ oligotrophy unit cell (Stenotrophomonas maltophilia strain DN1.1) and pseudomonas putida (Pseudomonas putida strain DN1.2), preservation registration number is respectively CCTCC M 207074 and CCTCC M207075, the preservation place is Chinese typical culture collection center, and the preservation time is on May 25th, 2007.
2. the cultural method of Stenotrophomonas maltophilia strain DN 1.1 and Pseudomonas putida strain DN 1.2 among the present invention
(1) employed substratum:
Extractum carnis substratum (g/L): extractum carnis 5.0, peptone 10.0, NaCl 5.0, transfer 7.2~7.4,121 ℃ of sterilizations of pH 20 minutes.As make solid medium, then add agar 1.5%~2.0%.
(2) culture condition:
The Stenotrophomonas maltophilia strain DN1.1 that preserves on the extractum carnis medium slant and Pseudomonasputida strain DN1.2 scraped with transfering loop get a ring bacterium and be inoculated in the extractum carnis liquid nutrient medium, 30~35 ℃, 170~200rpm shaking culture can be gathered in the crops bacterium liquid in 20~24 hours.
3. employed reactor among the present invention
Reactor is cylindrical, and material is a synthetic glass, bottom surface diameter 8cm, high 1.0m, virtual height 80cm, useful volume 4L.4 thief holes, successively apart from bottom surface 60cm, 50cm, 40cm, 30cm, mud discharging mouth is apart from bottom surface 10cm.Configuration ACO-012 electromagnetic type air compressor and micro porous aeration head, LZB glass rotors gas meter.
4. the method that pre-fixes of Stenotrophomonas maltophilia strain DN 1.1 and Pseudomonas putida strain DN1.2 among the present invention
Use the bacterial strain method of pre-fixing provided by the invention can effectively pre-fix the starting culture of aerobic particle mud.
(1) simulated wastewater (g/L): KH
2PO
40.7, MgSO
47H
2O 0.5, CaCl
22H
2O 0.5, (NH
4)
2SO
40.5~1, glucose 1~4, NaOH transfers pH 7.2~7.4
(2) active carbon powder: available from Chongqing Bei Bei Fine Chemical Works, analytical pure powdered carbon.
(3) cultivation of inoculating strain: scrape from the extractum carnis medium slant and to get a ring lawn, inoculation is gone in the extractum carnis liquid nutrient medium, and 30~35 ℃, 170~200rpm shaking culture 20~24 hours can be gathered in the crops bacterium liquid.
(4) the bacterium liquid with results is loaded in the centrifuge tube, and the centrifugal 5min of 4000rpm outwells supernatant liquor, with simulated wastewater the thalline after centrifugal is washed in the reactor.
(5) preparation of active carbon powder: take by weighing 1-3g/L (reactor) active carbon powder and be loaded in the beaker, add an amount of simulated wastewater detergent active charcoal,, leave standstill 30min with glass stick or the about 30min of magnetic stirrer, outwell supernatant liquor, gac is washed in the reactor with simulated wastewater.
(6) bacterial strain pre-fixes in reactor: in the reactor that inserts thalline and gac, inject simulated wastewater to virtual height, aeration head is placed reactor bottom, and the beginning aeration, aeration rate is controlled at 100-110L/h.Aeration continues 3 days, does not change simulated wastewater in this process.
(7) after vexed the exposing to the sun 3 days, begin to change the water running reactor.Cultivate aerobic particle mud according to method described in 5.
5. the method for cultivation of heterotrophic nitrification aerobic granule sludge of the present invention
Use heterotrophic nitrification aerobic granule sludge method of cultivation provided by the present invention can successfully cultivate heterotrophic nitrification aerobic granule sludge.
(1) cultivating heterotrophic nitrification aerobic granule sludge uses simulated wastewater as substratum.
Simulated wastewater (g/L): KH
2PO
40.7, MgSO
47H
2O 0.5, CaCl
22H
2O 0.5, (NH
4)
2SO
40.5~1, glucose 1~4, NaOH transfers pH 7.2~7.4
(2) cultivating process concrete operations condition:
A. before particle forms (being about 25 days): reactor adopts the SBR mode to move, and the cycle of operation is 12h, the 5min of intaking in the phase weekly, aeration 708min, sedimentation 2min, draining 5min.Reactor NH
4 +-N is controlled at 106-212mg/Ld; COD is controlled at 1000-4000mg/Ld; Aeration rate is controlled at 100-180L/h, and initial aeration rate is 100L/h, and with the prolongation of the time of cultivation, aeration rate progressively is increased to 180L/h; Settling time is progressively reduced to 5min by 18min; Volume of displacement is controlled at 2-3.5L phase weekly; Cultivating temperature is controlled in the 10-30 ℃ of scope.
B. particle initially forms the phase (be about 6 days, occur small-particle in the reactor, particle diameter mostly is 0.5~0.8mm): reactor NH
4 +-N load is controlled at 106mg/Ld; The COD load is controlled at 2000mg/Ld; Aeration rate is controlled at 200L/h; Settling time is 2min; Phase volume of displacement 2L weekly; Cultivating temperature is controlled in the 10-30 ℃ of scope.
C. particle growth period (be about 10 days, complete granulating in the reactor, particle diameter mostly is about 1mm): reactor NH
4 +-N load is controlled at 212mg/Ld; The COD load is controlled at 4000mg/Ld; Aeration rate is controlled at 200L/h; Settling time is 2min; Phase volume of displacement 2L weekly; Cultivating temperature is controlled in the 10-30 ℃ of scope.
(3) sampling and analyzing method in the cultivating process: when the reactor aeration from the thief hole of distance bottom surface 50cm sampling 6mL, 6000rpm, centrifugal 5min gets supernatant liquor and measures.
(4) water sample detection method:
NH
4 +-N: adopt Whitfield's ointment-hypochlorite spectrophotometry
NO
2 --N: adopt N-(1-naphthyl)-quadrol light-intensity method
NO
3 --N: adopt the DMP spectrophotometry
TN: adopt alkaline Potassium Persulphate method to clear up ultraviolet spectrophotometry
COD
Cr: adopt potassium bichromate to clear up spectrophotometry
" water and waste water check and analysis method " (the 4th edition) that above method is all published with reference to the China Environmental Science Press.
NH
4 +-N, NO
2 --N, NO
3 --N, TN, COD
CrDeng mensuration adopt the multi-functional water quality analyser of German WTW (TheSpectroquant Analysis System PhotoLab S12), model PhotoLab S12, operating voltage 12V.Disappearing to boil uses WTW company to produce CR 2200 well heaters.Test agent is the matched reagent that Merck ﹠ Co., Inc. produces.
6. heterotrophic nitrification aerobic granule sludge of the present invention is used for the denitrogenation condition of nitrogenous effluent treatment
Heterotrophic nitrification aerobic granule sludge of the present invention can be used for COD
CrThe processing of the nitrogenous effluent of≤10000mg/L, ammonia-nitrogen content≤1000mg/L, pH4~10, treatment condition are temperature 10-37 ℃, pH6-9, aeration.
7. heterotrophic nitrification aerobic granule sludge of the present invention is used for the denitrogenation condition that breeding wastewater is handled
Heterotrophic nitrification aerobic granule sludge of the present invention can be used for COD
CrThe processing of the breeding wastewater of≤10000mg/L, ammonia-nitrogen content≤1000mg/L, pH4~10, treatment condition are temperature 10-37 ℃, pH6-9, aeration 94-96h.
Employed two strain function stem Stenotrophomonas maltophilia strain DN1.1 and Pseudomonas putida strain DN1.2 have done the preservation of patented procedure among the present invention, preserving number is respectively CCTCC M 207074 and CCTCC M 207075, in the present invention, Stenotrophomonas maltophilia strain DN1.1 is equal to CCTCC M207074, and Pseudomonas putida strain DN 1.2 is equal to CCTCC M 207075.
The present invention has the following advantages:
(1) but employed two strain inoculating strain heterotrophic growths among the present invention, matrix utilizes scope wide, is easy to cultivate.
(2) employed two strain inoculating strains can be removed ammonia nitrogen and COD in the organic waste water simultaneously among the present invention.
(3) employed two strain inoculating strains mainly carry out the dissimilarity denitrogenation among the present invention under the heterotrophism condition.
(4) the present invention can use the bacterial strain pure growth as the inoculum of cultivating aerobic particle mud, does not need to add other mud, can guarantee the aerobic particle mud definite functions that forms like this.
(5) the heterotrophic nitrification aerobic granule sludge settling velocity cultivated of the present invention is fast, and effectively the biological concentration height, tolerates high organic loading and high ammonia nitrogen loading simultaneously at the time that can shorten denitrogenation and remove COD.
(6) heterotrophic nitrification aerobic granule sludge cultivated of the present invention can be used for the processing of high density organic nitrogen-containing waste water, and in denitrification process, can not produce the accumulation of nitrite and nitrate, can finish quick denitrogenation in a treatment system.It is simple to use this heterotrophic nitrification aerobic granule sludge to handle waster water process, and denitrification effect is stable.
Further illustrate the present invention below in conjunction with specific embodiment, should be appreciated that these embodiment only are used to the present invention is described and are not used in restriction the scope of protection of present invention.
Description of drawings
Accompanying drawing 1 heterotrophic nitrification aerobic granule sludge photo
Accompanying drawing 2 heterotrophic nitrification aerobic granule sludge particle entire scan Electronic Speculum Photomicrographs
Accompanying drawing 3 heterotrophic nitrification aerobic granule sludge surface biological scanning phase electromicroscopic photographs
Accompanying drawing 4 heterotrophic nitrification aerobic granule sludge particle section biophase scanning electron microscope Photomicrographs
Embodiment
Embodiment 1: the cultivation of heterotrophic nitrification aerobic granule sludge of the present invention
(1) extractum carnis substratum, was sterilized 20 minutes by 121 ℃.
(2) bacterial strain Stenotrophomonas maltophilia strain DN 1.1 and Pseudomonas putida strainDN1.2 are seeded to respectively in the extractum carnis liquid nutrient medium of 500mL sterilization, 35 ℃, 170rpm cultivates 24h.With the centrifugal 5min of cultured bacterium liquid 4000rpm, with inserting reactor behind a small amount of simulated wastewater resuspension.
(3) the 15g active carbon powder is placed the 500mL beaker, add the 200mL simulated wastewater, glass stick all is transferred in the reactor after stirring 30min.Reactor is cylindrical, and material is a synthetic glass, bottom surface diameter 8cm, high 1.0m, virtual height 80cm, useful volume 4L.4 thief holes, successively apart from bottom surface 60cm, 50cm, 40cm, 30cm, mud discharging mouth is apart from bottom surface 10cm.Configuration ACO-012 electromagnetic type air compressor and micro porous aeration head, LZB glass rotors gas meter.Add simulated wastewater in the reactor to 4L.
(4) the controlling reactor aeration rate is 100-110L/h, vexed exposing to the sun 3 days.
(5) cultivate according to cultivating schedule of operation.The concrete operational condition of cultivating sees Table 1.
(6) obtain sophisticated heterotrophic nitrification aerobic granule sludge.This heterotrophic nitrification aerobic granule sludge is faint yellow grain of rice shape; Particulate water ratio: 84.96%; MLSS:5.5469g/L; Particle size range: 0.3-1.5mm; Subsidence rate: 0.25m/min; This particle principal element (removing protium) kind (content 〉=1%) and relative percentage composition: O 34.36%, C 56.70%, and N 6.75%, and P 1.21%, and Si 0.98%.
(7) observation of heterotrophic nitrification aerobic granule sludge.The use scanning electron microscope is carried out microscopic examination to the integral body and the section of heterotrophic nitrification aerobic granule sludge.Observations is seen accompanying drawing 1-4.
Table 1 heterotrophic nitrification aerobic granule sludge is cultivated operational condition
Embodiment 2: heterotrophic nitrification aerobic granule sludge of the present invention is to the removal of simulated wastewater ammonia nitrogen
Table 2 heterotrophic nitrification aerobic granule sludge is to the removal of simulated wastewater ammonia nitrogen
Simulated wastewater ammonia nitrogen concentration 212mg/L, COD concentration 4000mg/L.Reactor is cylindrical, and material is a synthetic glass, bottom surface diameter 8cm, high 1.0m, virtual height 80cm, useful volume 4L.4 thief holes, successively apart from bottom surface 60cm, 50cm, 40cm, 30cm, mud discharging mouth is apart from bottom surface 10cm.Configuration ACO-012 electromagnetic type air compressor and micro porous aeration head, LZB glass rotors gas meter.Reactor moves at low temperatures (11-15 ℃) operation in the SBR mode, and the cycle of operation is 12h, the 5min of intaking in the phase weekly, aeration 708min, sedimentation 2min, draining 5min.Aeration rate 200L/h, volume of displacement 2L.Per 2 cycle timing samplings detect.Experimental result sees Table 2.Can find out that from table 2 this heterotrophic nitrification aerobic granule sludge is 70.75%~76.42% to the reactor ammonia-N removal rate in 12h.The clearance of COD is more than 90% after measured.Proof heterotrophic nitrification aerobic granule sludge (11-15 ℃) under cold condition has good denitrogenation and removes the COD ability.
Embodiment 3: heterotrophic nitrification aerobic granule sludge of the present invention is to the treatment effect of chicken house waste water
Chicken house waste water is taken from the poulty house, Chengdu, ammonia nitrogen concentration 755mg/L, COD concentration 8500mg/L.Get the about 200mL of heterotrophic nitrification aerobic granule sludge, with 500mL stroke-physiological saline solution washing 3 times.Leave standstill 5min after the last washing, outwell supernatant liquor, get this washing back heterotrophic nitrification aerobic granule sludge of 150mL, add the 2L graduated cylinder, add chicken house waste water to 1L.Aeration head is placed in the graduated cylinder bottom, and aeration rate is controlled at 80-90L/h, and temperature of reaction is 11-15 ℃, and timing sampling is measured.Experimental result sees Table 3.As can be seen from Table 3, under this heterotrophic nitrification aerobic granule sludge cold condition chicken house waste water is also had the denitrogenation ability,, ammonia-N removal rate is reached 65.56%, the clearance of COD is reached 90.47% experiment the 31st hour.After this because of carbon source deficiency in the waste water, so add glucose 2g and 2.5g respectively at 36h and 46h respectively.Experiment moves to 94h, and ammonia-N removal rate is reached 89.93%, and ammonia-nitrogen content is 76mg/L in the waste water, and COD content is 54mg/L, has reached livestock breeding wastewater emission standard (GB18596-2001).
Table 3 heterotrophic nitrification aerobic granule sludge is handled chicken house waste water result
Claims (6)
1. heterotrophic nitrification aerobic granule sludge, it is characterized in that containing in this granule sludge function stem germ oligotrophy unit cell (Stenotrophomonas maltophilia strain DN1.1) and pseudomonas putida (Pseudomonas putidastrain DN1.2), preservation registration number is respectively CCTCC M 207074 and CCTCC M 207075.
2. method of cultivating the function stem of heterotrophic nitrification aerobic granule sludge described in the claim 1, it is characterized in that: adopt beef-protein medium, at pH 7.2~7.4,30~35 ℃, shaking culture is 20~24 hours under 170~200rpm condition, can obtain heterotrophic nitrification function stem nutrient solution.
3. a simulated wastewater of cultivating heterotrophic nitrification aerobic granule sludge described in the claim 1 is characterized in that: simulated wastewater (g/L): KH
2PO
40.7, MgSO
47H
2O 0.5, CaCl
22H
2O 0.5, (NH
4)
2SO
40.5~1, glucose 1~4, NaOH transfers pH 7.2~7.4.
4. the method that pre-fixes of cultivating the function stem of heterotrophic nitrification aerobic granule sludge described in the claim 1 is characterized in that: with cultivating the centrifugal collection thalline of bacterium liquid of results in the claim 2, wash in the reactor with simulated wastewater described in the claim 3.Taking by weighing 1-3g/L (reactor) active carbon powder adds in the reactor with the washing of simulated wastewater described in the claim 3 back.Inject simulated wastewater described in the claim 3 then to the reactor virtual height, aeration 3 days.
5. method of cultivating heterotrophic nitrification aerobic granule sludge described in the claim 1, it is characterized in that: according to claim 4ly finish the reactor that function stem pre-fixes, adopt the SBR mode to move, with simulated wastewater described in the claim 3 is matrix, progressively improve ammonia nitrogen loading and organic loading, the control settling time is cultivated aerobic particle mud less than 5min.
6. the application of the heterotrophic nitrification aerobic granule sludge described in the claim 1 in water body biological denitrificaion and breeding wastewater processing.
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