CN101259982A - Method and device for treating high concentration nitrogen-containing waste water by using microorganism - Google Patents
Method and device for treating high concentration nitrogen-containing waste water by using microorganism Download PDFInfo
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Abstract
The invention relates to a method of treating highly concentrated nitrogen wastewater with microorganism and a device to carry out the method. The method comprises the following steps that: wastewater passes an anaerobic pool, a facultative tank, an aerobic pool and a sedimentation pool in sequence for biochemical treatment, and is characterized in that the anaerobic pool, the facultative tank and the aerobic pool are not added with fillings, sludge in the sedimentation pool reflows to the anaerobic pool and the facultative tank through a sludge reflowing pipe. The device comprises the aerobic pool, the facultative tank, the anaerobic pool and the sedimentation pool, a nitration liquid reflowing pipe is arranged between the sedimentation pool and the facultative tank, and is characterized in that the aerobic pool, the facultative tank and the aerobic pool are not added with fillings and sludge reflowing pipes are arranged between the sedimentation pool and the anaerobic pool and the aerobic pool respectively. The method is simple in procedures and unnecessary to be added with fillings, thereby saving cost, has better effluent effect and denitrogenation effect superior to the prior A< 2>/O technology; the bacteria quantity for nitration reaction in the aerobic pool are always kept at a higher degree.
Description
Technical field
The invention belongs to and utilize microbiological treatment waste water technology field, particularly utilize the method and the device of microbiological treatment high concentration nitrogen-containing waste water.
Background technology
Trade effluent kind difference, the nitride form that wherein contains also is not quite similar, and in most of the cases is to have (ammonia nitrogen is in the majority) with the inorganic nitrogen form, in addition organonitrogen in biological treatment process also major part can be converted into the form of inorganic nitrogen.The concentration of organonitrogen or ammonia nitrogen and form depend on a number of factors in trade effluent, multiplexing etc. as the consumption of the production technology of raw material properties, employing, water and water.From trade effluent, remove the existing several different methods of ammonia nitrogen.Using in wastewater treatment at present is AAO technology, i.e. A more widely
2/ O technology.A
2/ O technology is made up of anaerobic pond, oxygen compatibility pool, Aerobic Pond, settling tank and two return-flow systems (mud return-flow system and nitrification liquid return-flow system).Sewage at first enters anaerobic pond, the anaerobically fermenting bacterium is converted into VFA (volatile fat acids) with biodegradable organism in the sewage, and polyP bacteria can decompose the poly-phosphate that stores in its body, the energy that is discharged can be survived under anaerobic environment for aerobic polyP bacteria, another part energy can supply polyP bacteria active absorption VFA class low molecule organic matter, and stores in its body with the form of PHB.Sewage enters oxygen compatibility pool subsequently, the nitrate that denitrifying bacteria utilizes the Aerobic Pond backflow mixed liquor to bring, and biodegradable organism carries out denitrification as carbon source in the sewage, reaches and reduces BOD simultaneously
5Purpose with denitrogenation.Then sewage enters the Aerobic Pond of aeration, and polyP bacteria mainly is to release energy by the PHB that stores in the decomposer to keep its growth and breeding when absorbing, utilizing biodegradable organic remaining in the sewage.Dissolved phosphorus in the simultaneously excessive picked-up surrounding environment, and store up in vivo with poly-phosphorus form makes that dissolved phosphorus concentration reaches minimum in the water outlet.And organism is after anaerobic pond, oxygen compatibility pool are utilized by polyP bacteria and denitrifying bacterium respectively, and concentration is quite low when arriving Aerobic Pond, and this helps the growth and breeding of autotrophic type nitrifier, and by nitrification ammonia nitrogen is converted into nitrate.
Anaerobic pond, oxygen compatibility pool and Aerobic Pond alternate run can reach the purpose of removing organism, denitrogenation, dephosphorization simultaneously, but this technology denitrification effect depends on return current ratio of the mixed liquid, and A
2The return current ratio of the mixed liquid of/O technology should not be too high.
In the middle of this technological process, nitrifier is long generation time, poor growth, even nitrifier quantity is enough, the startup of nitration reaction still needs the long period, and denitrifying bacteria is shorter generation time, and growth is rapid, and anti-nitration reaction starts easily; Because the single oxygen compatibility pool that is back to of mud, being actually will the nitrifier of nitrated proterties have changed under the environment of double oxygen through reaching preferably after the Aerobic Pond domestication, nitrifier is forced to adapt to double oxygen environment and adjusts, its physiologically active weakens, the denitrifying bacteria all living creatures manages activity and is activated, and when mud plug-flow during to Aerobic Pond, the nitrifier physiologically active begins again to be activated, but effectively nitration reaction quantity can only progressively improve, and denitrifying bacteria is suppressed.So, the bacterium amount that can effectively carry out nitration reaction in the Aerobic Pond can't reach higher degree all the time, has influenced the efficient of whole biological denitrificaion reaction.
Summary of the invention
What the present invention will solve is that high concentration nitrogen waste water is handled employing A
2/ O technology ammonia nitrogen removal effect is bad, and the single oxygen compatibility pool that is back to of mud causes nitrifier and denitrifying bacteria reaction conditions contradiction, and mud is short age, and efficient is low, working cost height, the technical problem of management operating inconvenience control.The purpose of this invention is to provide a kind of method of utilizing the microbiological treatment high concentration nitrogen-containing waste water, another object of the present invention provides a kind of device that is used to utilize the method for microbiological treatment high concentration nitrogen-containing waste water.
For solving the problems of the technologies described above, the technical solution used in the present invention is: the method for utilizing the microbiological treatment high concentration nitrogen-containing waste water, waste water carries out biochemical treatment through anaerobic pond, oxygen compatibility pool, Aerobic Pond and settling tank successively, it is characterized in that: all not filled in described anaerobic pond, oxygen compatibility pool, the Aerobic Pond, the mud in the described settling tank is back to anaerobic pond (A1) and Aerobic Pond (O) simultaneously by sludge return pipe.As Aerobic Pond SV
30Less than 20, or the Aerobic Pond influent ammonia nitrogen is greater than 250mg/L, and the mud that increases Aerobic Pond refluxes, and reduces mud and is back to anaerobic pond, improves the Aerobic Pond sludge concentration, reduces Aerobic Pond nitrifier load, strengthens nitrification effect, promotes ammonia nitrogen to transform.
The reflux ratio that described mud is back to anaerobic pond (A1), Aerobic Pond (O) is respectively: 0.4-0.9,0.1-0.6.
The reflux ratio that described mud is back to anaerobic pond (A1), Aerobic Pond (O) can be preferably respectively: 0.5-0.9,0.1-0.5.
Be used to utilize the device of the method for microbiological treatment high concentration nitrogen-containing waste water, comprise anaerobic pond, oxygen compatibility pool, Aerobic Pond and settling tank, be provided with the nitrification liquid reflux line between settling tank and the oxygen compatibility pool (A2), it is characterized in that: all not filled in described anaerobic pond, oxygen compatibility pool, the Aerobic Pond, be equipped with sludge return pipe between described settling tank and described anaerobic pond (A1) and the Aerobic Pond (O).
Anaerobic pond is mainly finished waste water is carried out the anaerobism pre-treatment, be used to remove portion C OD and BOD, a part of objectionable impurities in the degradation of sewage, with macromolecular organism in the waste water and the reaction of non-solubility organism generation acidification hydrolization, improved the biodegradability of sewage simultaneously, handled creating conditions to hypomere.
The backflow nitrification liquid that oxygen compatibility pool mainly utilizes electron donor that the anaerobic pond water outlet provides and Aerobic Pond to provide is finished anti-nitration reaction.
Aerobic Pond mainly is to utilize the organic cod in the degrading waste water under the environment that hangs down BOD, carries out nitration reaction simultaneously, obtains NO
3 -Or NO
2 -The nitrification liquid water outlet is back to oxygen compatibility pool by the nitrification liquid reflux line.
Settling tank is finished mud-water separation, by sludge return pipe most of mud is back to anaerobic pond and Aerobic Pond simultaneously, as required with the actual operating state mud discharging of will having more than needed.
All not filled in described anaerobic pond, oxygen compatibility pool, the Aerobic Pond.
As a further improvement on the present invention: before the anaerobic pond air flotation pool can also be set, waste water also can be removed a large amount of petroleum-type and suspended substance through the air flotation pool pre-treatment earlier before entering anaerobic pond as required.
The air flotation pool water outlet is by being pumped to anaerobic pond, and microorganism carries out biochemical reaction in waste water and the pond, and a part of objectionable impurities in the degradation of sewage has improved the biodegradability of sewage simultaneously, handles creating conditions to hypomere.
The anaerobic pond water outlet enters oxygen compatibility pool, oxygen compatibility pool is one of core facility of biochemical treatment, this with the water inlet in organism as the denitrifying carbon source and the energy, with the nitric nitrogen in the nitrated phegma as denitrifying nitrogenous source, carry out the denitrification denitrogenation reaction with facultative cenobium effect in the pond, make the NH in the waste water
3Pollution substance such as-N, COD is able to part removal and degraded.
Needs for the Aerobic Pond biochemical reaction that satisfies oxygen compatibility pool and back, for microorganism provides phosphorus and suitable water temperature, considered the steam heating facility on anaerobism, oxygen compatibility pool, in service should the operation according to practical situation can be operated by following parameter when oxygen compatibility pool normally moves.
The oxygen compatibility pool controlled variable is as follows:
Dissolved oxygen:＜0.5mg/l P:3-4mg/l
Water temperature: 30 ℃ of PH:7～8
The oxygen compatibility pool water outlet flows into Aerobic Pond and the active sludge thorough mixing that sends back to Aerobic Pond through sludge return pipe, by the organism in the microbiological deterioration waste water.In order to satisfy biochemical requirement, increase dissolved oxygen in the Aerobic Pond waste water by the micro-hole aerator that is provided with, for microorganism provides oxygen and mixed solution is stirred.Also need add soda ash (Na in addition
2CO
3) and microcosmic salt.Aerobic Pond can be operated by following parameter during normal operation:
Dissolved oxygen (DO): the above PH of 2-4mg/l P:3mg/l :～7.5
Basicity is in (CaCO3): about＞200mg/l MLSS:3g/l
Suitable water temperature: 25～30 ℃ (but must not sharply change)
For the concentration of narmful substance that guarantees biochemical treatment is controlled in the allowed band, in the inlet flume of Aerobic Pond, add dilution water, Aerobic Pond is provided with the froth breaking waterpipe, and foam should be opened froth breaking waterpipe valve and carry out froth breaking for a long time in Aerobic Pond.
Last Aerobic Pond water outlet enters settling tank, carries out mud-water separation in settling tank, and wherein nitrification liquid is back to oxygen compatibility pool by pipeline, and mud is back to anaerobic pond and Aerobic Pond simultaneously by pipeline, and reflux ratio is: to anaerobic pond 0.5-0.9, to Aerobic Pond 0.1-0.5.
The microorganism species that adds in total system can adopt commodity by name
The commercial preparation, include following 105 kinds of microorganisms from 47 genus.
Cetobacter aceti acetic acid acetobacter
The Acetobacter liquefaciens acetobacter that liquefies
Acetobacter xylinum acetobacter xylinum
The dry achromobacter of Achromobacter xerosis
Aeromonans hydrophila Aeromonas hydrophila
Aeromonas media Aeromonas media
Aeromonans sobria Aeromonas sobria
Bacillus alvei branch genus bacillus
Bacillus coagulans Bacillus coagulans
Bacillus subtilis subtilis
Bacillus leutis bacillus lentus
Bacillus firmus bacillus firmus
Bacillus mycoides shape genus bacillus
Bacillus megaterium bacillus megaterium
Bacillus alcalophilus Alkaliphilic bacillus
Bacillus cereus bacillus cereus
Bacillus licheniformis Bacillus licheniformis
Bacillus pumilus bacillus pumilus
Bacillus spaericus Bacillus sphaericus
Bacillus marinus bacillus marinus
Alcaligenes denitrificans denitrification subspecies
Alcaligenes faecalis Alcaligenes faecalis
Alcaligenes xylosoxydans Alcaligenes xylosoxidans
Brevibacterium acetylicum acetylene tyrothricin
Brevibacterium ammoniagenes separates the ammonia tyrothricin
Brevibacterium casei galactenzyme tyrothricin
The short genus bacillus of Brevibacillus brevis
Enterobacter cloacae enterobacter cloacae
Enterobacter aerogenes enteroaerogen
Enterobacter agglomerans enterobacter agglomerans
Thiobacillus?novellas
Thiobacillus?thioparus
Thiobacillus denitrificans denitrification thiobacillus
Thiobacillus thiooxidans thiobacillus thiooxidant
Thiorhodococcus minus sulphur rhodococcus
Rhodopseudomonas palustris Rhodopseudomonas palustris
Rhodopseudomonas acidphia rhodopseudomonas acidophilus
Gluconobacter albidus Qian Jingshi gluconobacter sp
Gluconobacte oxydans glucose oxidation and bacillus
Lactobacillus fermentum lactobacillus fermentum
Lactobacillus plantarum plant lactobacillus
Lactobacillus alimentarius digests Bacterium lacticum
Lactobacillus amylophillus food starch milk bacillus
Lactobacillus ruminis lactobacillus ruminis
Lactobacillus bervis short lactobacillus
Micrococcus leutus micrococcus luteus
Micrococcus halobius Micrococcus halobius
Pseudomonas alcaligenes Pseudomonas alcaligenes
Pseudomonas aureofaciens causes yellow pseudomonas
Pseudomonas chlororaphis Pseudomonas chlororaphis
The nitrated pseudomonas of Pseudomonas nitroreducens
Pseudomonas riboflavina riboflavin pseudomonas ..
Pseudomonas putina pseudomonas putida ..
Pseudomonas facilis Pseudomonas facilis
Paenibacillus gluconolyticus separates the glucan genus bacillus
Paenibacillus thiaminlyticus separates sulphur glairin class bud pole bacterium
Saccharomyces?telluris
Beggiatoa?alba
Nitrobacter winogradskyi bacterium nitrobacter
Nitrosomonas europaea Nitrosomonas
Nitrosococcus?nitrosus
The narrow and small luminous bacillus of Photobacterium angustum
Photobacterium phosphoreum photobacterium phosphoreum
Photobacterium leiognathi abalone luminous bacillus
The richly endowed bacterium of Haloferax denitrificans denitrification salt
The richly endowed bacterium of Haloferax mediterranei Mediterranean Sea salt
Methanobacterium bryantii Bu Shi methagen
Methanobacterium paluster marsh methagen
Methanobacterium uliginosum mire methagen
Cellulomonas biazotes dinitrogen cellulomonas cartae
Cellulomonas fimi muck cellulomonas cartae
Kurthia zopfii Zuo Shi Al Kut Salmonella
Thiosphaera?pantotropha
Alcaligenes?sp
Chlorobium limicola mud is given birth to green bacterium
The long red bacterium of Erythrobacter longus
The red Zymomonas mobilis of Erothromonas ursincola
Azomonas macrocytogenes giant cell nitrogen Zymomonas mobilis
The yellow bacillus flavus of Xanthobacter flavus
Methylcoccus capsulatus pod membrane methyl coccus
Alteromonas denitrificans denitrification replaces Zymomonas mobilis
Alteromonas nigrifaciens produces black alternately Zymomonas mobilis
Telluria mxita mixes the refreshing bacterium in ground
Bacteroides cellulosovens Bacteroides cellulosolvens
Bacteroides stercoris Bacteroides stercoris
Many nutritive muds of Ilyobacter ploytropus bacillus
The false butyric acid vibrios of Pseudobutyrivibrio ruminis cud
Zymomonas mobilis is supported in Syntrophomonas wolfei Ao Shi syntrophism
The simple pimelobacter sp of Pimelobacter simplex
Pimelobacter tumescens swelling pimelobacter sp
The short shape bacillus of Brachybacterium faecium excrement
Jonesia denitrificans denitrification Jones Salmonella
The rotten rare bacillus of Rarobacter faecitabidus slag
Eubacterium formicigenerans Eubacterium formicigenerans
Eubacterium nitritogenes Eubacterium nitrotogenes
Eubacterium xylanophilum has a liking for the polyxylose Eubacterium
The aurantia small bacillus of Exiguobacterium aurantiacum
Bacillus is supported in Synteophobacter wolinii Wo Shi syntrophism
Water treatment technological process of the present invention is succinct, need not hang filler, has saved investment, and management operating is succinct, the water outlet better effects if, and the denitrification functions effect is better than existing A
2/ O technology, mud is back to Aerobic Pond, has continued the physiologically active with the nitrifying bacteria community of taming, and makes the bacterium amount of effectively carrying out nitration reaction in the Aerobic Pond remain higher degree.Particularly as Aerobic Pond SV
30Less than 20%, or the Aerobic Pond influent ammonia nitrogen adopts the present invention can improve the Aerobic Pond sludge concentration during greater than 250mg/L, reduces Aerobic Pond nitrifier load, strengthens nitrification effect, promotes ammonia nitrogen to transform.After method of the present invention was handled, the coking chemical waste water ammonia nitrogen can be controlled at below the 15mg/L, and COD can be controlled at below the 100mg/L, and other indexs also can reach national grade one discharge standard.Except that coking waste water, the present invention also is applicable to the factory effluent of difficult degradations such as pharmacy waste water, fermentation waste water, food enterprise waste water, can also be used for the processing of municipal wastewater, sanitary sewage.
Do not have additional carbon in the whole process of the present invention, and because the efficient of HSBEMBM microorganism species can reduce processing cost greatly.
Description of drawings
Fig. 1 is conventional A
2/ O water technology synoptic diagram
Fig. 2 the present invention handles the process flow sheet of high concentration nitrogen-containing waste water
Annotate: among the figure: A: sewage B: nitrification liquid backflow C: mud refluxes
Embodiment
As shown in Figure 2, with anaerobic pond 1, oxygen compatibility pool 2, Aerobic Pond 3 and settling tank 4 have spatially constituted four main unit, and settling tank is provided with the Digestive system reflux line to oxygen compatibility pool 2, and settling tank also is provided with sludge return pipe to anaerobic pond 1 and Aerobic Pond 3; Anaerobic pond 1 and Aerobic Pond 3 are respectively arranged with the independent switch of control return sludge ratio.
The waste water that enters system is earlier through air flotation pool, and pre-treatment removes deoils and suspended substance (and slag).Waste water enters in the anaerobic pond 1 then, and the anaerobism cenobium is carried out biochemical reaction in waste water and the pond under the situation of oxygen deprivation, and a part of objectionable impurities in the degradation of sewage has improved the biodegradability of sewage simultaneously, handles creating conditions to hypomere.In order to satisfy the needs of anaerobic pond and anoxic pond biochemical reaction, for microorganism provides nutrition phosphorus source, in anaerobic pond, be provided with microcosmic salt and add pipeline, in service should the operation according to practical situation, anaerobic pond can be operated by following parameter.
P :～4mg/l PH :～7.5 water temperatures :～30 ℃ (must not sharply change)
Anaerobic pond 1 water outlet enters oxygen compatibility pool 2, this with the water inlet in organism as the denitrifying carbon source and the energy, as denitrifying nitrogenous source, in the pond, carry out the denitrification denitrogenation reaction with the nitric nitrogen in the nitrated phegma under the facultative cenobium effect of combination, make the NH in the waste water
3Pollution substance such as-N, COD is able to part removal and degraded.
Needs for Aerobic Pond 3 biochemical reactions that satisfy oxygen compatibility pool 2 and back, for microorganism provides phosphorus and suitable water temperature, considered the steam heating facility at anaerobism, oxygen compatibility pool, in service should the operation according to practical situation can be operated by following parameter when oxygen compatibility pool normally moves.
Oxygen compatibility pool 2 controlled variable are as follows:
Dissolved oxygen:＜0.5mg/l P:3-4mg/l
Water temperature :～30 ℃ of PH:7～8
Oxygen compatibility pool 2 water outlets flow into Aerobic Pond 3 and the active sludge thorough mixing that sends back to Aerobic Pond through sludge return pipe, by the organism in the microbiological deterioration waste water.In order to satisfy biochemical requirement, increase dissolved oxygen in the Aerobic Pond waste water by the micro-hole aerator that is provided with, for microorganism provides oxygen and mixed solution is stirred.Also need add soda ash (Na in addition
2CO3) and microcosmic salt.Soda ash flows to segmentation by the Aerobic Pond mixed solution and adds.Aerobic Pond 3 water outlets are back to oxygen compatibility pool 2 by the nitrification liquid return line, and Aerobic Pond 3 can be operated by following parameter during normal operation:
Dissolved oxygen (DO): the above PH of 2-4mg/l P :～3mg/l :～7.5
Basicity is with (CaCO
3) meter: about＞200mg/l MLSS:3g/l
Suitable water temperature: 25～30 ℃ (but must not sharply change)
For the concentration of narmful substance that guarantees biochemical treatment is controlled in the allowed band, in the inlet flume of Aerobic Pond 3, add dilution water, Aerobic Pond 3 is provided with the froth breaking waterpipe, and foam should be opened froth breaking waterpipe valve and carry out froth breaking for a long time in Aerobic Pond 3.
The Aerobic Pond water outlet enters settling tank 4 and carries out mud-water separation, nitrification liquid is back to oxygen compatibility pool 2 by the nitrification liquid reflux line, mud is back to anaerobic pond 1 by sludge return pipe with 60% mud, 40% mud is back to the water outlet COD about 150mg/L of Aerobic Pond 3. after the present invention handles, and ammonia nitrogen is not higher than 10mg/L.Data by table 1 contrast as can be known, the water outlet COD about 200mg/L of same waste water after conventional A/O art breading, and the about 25mg/L of ammonia nitrogen, visible wastewater treatment efficiency of the present invention is significantly better than conventional A/O water technology.
Table 1
Claims (5)
1, utilizes the method for microbiological treatment high concentration nitrogen-containing waste water, waste water carries out biochemical treatment through anaerobic pond, oxygen compatibility pool, Aerobic Pond and settling tank successively, it is characterized in that: all not filled in described anaerobic pond, oxygen compatibility pool, the Aerobic Pond, the mud in the described settling tank is back to anaerobic pond (A1) and Aerobic Pond (O) simultaneously by sludge return pipe.
2, want 1 described method according to right, it is characterized in that: the reflux ratio that described mud is back to anaerobic pond (A1), Aerobic Pond (O) is respectively: 0.4-0.9,0.1-0.6.
3, want 2 described methods according to right, it is characterized in that: elder generation was through an air flotation pool before waste water entered anaerobic pond, and a large amount of petroleum-type and suspended substance are removed in pre-treatment.
4, the device that is used for the described method of claim 1, comprise anaerobic pond, oxygen compatibility pool, Aerobic Pond and settling tank, be provided with the nitrification liquid reflux line between between settling tank and the oxygen compatibility pool (A2), it is characterized in that: all not filled in described anaerobic pond, oxygen compatibility pool, the Aerobic Pond, be equipped with sludge return pipe between described settling tank and described anaerobic pond (A1) and the Aerobic Pond (O).
5, device according to claim 4 is characterized in that: also comprise an air flotation pool before the anaerobic pond.
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| CNA2007101648670A CN101259982A (en) | 2007-12-28 | 2007-12-28 | Method and device for treating high concentration nitrogen-containing waste water by using microorganism |
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| CNA2007101648670A CN101259982A (en) | 2007-12-28 | 2007-12-28 | Method and device for treating high concentration nitrogen-containing waste water by using microorganism |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102791641A (en) * | 2010-03-10 | 2012-11-21 | 齐克拉-斯图尔茨污水处理技术有限公司 | Method for the biological purification of ammonium-containing wastewater |
| CN109504642A (en) * | 2019-01-21 | 2019-03-22 | 中国科学院成都生物研究所 | One plant of denitrifying bacterium and its application |
| CN110102177A (en) * | 2019-04-09 | 2019-08-09 | 卢松 | A kind of technique purifying slurry-spraying pelletizing flue gas |
| CN111087127A (en) * | 2019-12-23 | 2020-05-01 | 南京中赢生态农业科技发展有限公司 | Combined type nitrogen and phosphorus removal water treatment device and system thereof |
-
2007
- 2007-12-28 CN CNA2007101648670A patent/CN101259982A/en active Pending
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102791641A (en) * | 2010-03-10 | 2012-11-21 | 齐克拉-斯图尔茨污水处理技术有限公司 | Method for the biological purification of ammonium-containing wastewater |
| CN102791641B (en) * | 2010-03-10 | 2014-10-29 | 达蒙有限公司 | Method for the biological purification of ammonium-containing wastewater |
| CN109504642A (en) * | 2019-01-21 | 2019-03-22 | 中国科学院成都生物研究所 | One plant of denitrifying bacterium and its application |
| CN109504642B (en) * | 2019-01-21 | 2022-01-04 | 中国科学院成都生物研究所 | Denitrifying bacterium and application thereof |
| CN110102177A (en) * | 2019-04-09 | 2019-08-09 | 卢松 | A kind of technique purifying slurry-spraying pelletizing flue gas |
| CN110102177B (en) * | 2019-04-09 | 2021-11-26 | 内蒙古阜丰生物科技有限公司 | Process for purifying flue gas generated in guniting granulation |
| CN111087127A (en) * | 2019-12-23 | 2020-05-01 | 南京中赢生态农业科技发展有限公司 | Combined type nitrogen and phosphorus removal water treatment device and system thereof |
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Open date: 20080910 |