CN105624087A - Promoter for culturing nitrifying bacteria and preparation method of promoter - Google Patents

Promoter for culturing nitrifying bacteria and preparation method of promoter Download PDF

Info

Publication number
CN105624087A
CN105624087A CN201410585418.3A CN201410585418A CN105624087A CN 105624087 A CN105624087 A CN 105624087A CN 201410585418 A CN201410585418 A CN 201410585418A CN 105624087 A CN105624087 A CN 105624087A
Authority
CN
China
Prior art keywords
weight portions
slaine
accelerator
growth promoter
promoter
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.)
Granted
Application number
CN201410585418.3A
Other languages
Chinese (zh)
Other versions
CN105624087B (en
Inventor
高会杰
郭志华
孙丹凤
赵胜楠
许谦
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Sinopec Dalian Petrochemical Research Institute Co ltd
China Petroleum and Chemical Corp
Original Assignee
China Petroleum and Chemical Corp
Sinopec Dalian Research Institute of Petroleum and Petrochemicals
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by China Petroleum and Chemical Corp, Sinopec Dalian Research Institute of Petroleum and Petrochemicals filed Critical China Petroleum and Chemical Corp
Priority to CN201410585418.3A priority Critical patent/CN105624087B/en
Publication of CN105624087A publication Critical patent/CN105624087A/en
Application granted granted Critical
Publication of CN105624087B publication Critical patent/CN105624087B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Abstract

The invention discloses a promoter for culturing nitrifying bacteria. The promoter comprises the following components in parts by weight: 40-100 parts of metal salts, preferably 50-80 parts of metal salts, and 5-30 parts of polyamine substance, preferably 10-20 parts of polyamine substance, wherein the metal salts comprise calcium salt, magnesium salt and copper salt, and the molar ratio of Ca<2+> to Mg<2+> to Cu<2+> is (5-15) to (5-25) to (0.5-5), preferably (8-12) to (10-20) to (1-4). The promoter is simple in composition and easy to prepare, can be used in a culture process of nitrifying bacteria, and also can be directly fed into a sewage treatment system, so that the nitrifying bacteria can rapidly grow and breed within a short time, and the cultured nitrifying bacteria have high activity and strong impact tolerance.

Description

A kind of accelerator cultivating nitrobacteria and preparation method thereof
Technical field
The invention belongs to biological technical field, be specifically related to a kind of accelerator cultivating nitrobacteria and preparation method thereof.
Background technology
In biological denitrification method, it is no matter traditional nitrification-denitrification, or novel short-cut nitrification-denitrification and short distance nitration-anaerobic ammoxidation all need the Nitrification removal of ammonia and nitrogen through nitrobacteria. Nitrobacteria belongs to chemotrophy type microorganism. Biological cell is only with the energy preserved with forms such as ATP, it is impossible to directly utilize the free energy that chemical reaction discharges. In good oxygen metabolism, ATP synthesizes mainly through the oxidative phosphorylation of respiratory chain. Ammoxidation phosphorylation efficiency is very low, and the ATP that can be generated by is very limited, and these energy are mainly used in electron transition to higher energy level, and this makes nitrobacteria growth very slow, and the phase is 8 ~ 36h from generation to generation. In the cell wall of nitrobacteria, peptidoglycan content is low, protein and fat content are high, therefore environmental change is more sensitive, nitrobacteria adaptability natural in nature and toleration are poor, cannot get the mastery in growth competition with heterotroph microorganism under a lot of conditions. In sewage disposal system, when in activated sludge, nitrobacteria content is relatively low, rely on regulate the environmental condition such as dissolved oxygen and pH cannot within a short period of time fast-growth breeding, the sewage disposal system removal of ammonia and nitrogen ultimately resulting in existing operation is limited in one's ability, industrially generally can adopt and directly throw in cultured high concentration nitrobacteria in sewage disposal system to solve this problem. No matter it is in sewage disposal system, directly cultivate nitrobacteria or outside sewage disposal system, cultivate nitrobacteria, is required for adding the material promoting growth, the growth rate of nitrobacteria could be accelerated.
From biochemistry level, nitration reaction relates to the metabolic pathway of ammona monooxygenase, azanol oxygen also enzyme and nitrite oxidase co-catalysis, and converts along with complicated matter and energy. Adopt Biostimulation agent to improve the activity of these enzymes in nitrobacteria, be then solve one of slow effective way of nitrobacteria growth, nitration reaction process can be accelerated simultaneously. A lot of about the research of Biostimulation agent at present, CN200510111874.5, CN200510111876.4, CN200510111877.9 and CN200510111875.X propose the nitrobacteria growth promoter utilizing different metal salt combination respectively, and main component includes molasses, slaine (iron salt, manganese salt, calcium salt and magnesium salt) and adsorbent. After using this accelerator, ammonia nitrogen removal frank can improve more than 20%. But be mainly the materials such as zeolite powder, kieselguhr, Powdered Activated Carbon or flyash due to adsorbent, adding of these adsorbents will certainly increase sludge yield. CN201110315549.6 discloses the cultural method of a kind of short-cut nitrification and denitrification granular sludge, it is characterized in that regularly adding 5 ~ 15mg/L azanol; CN201010168453.7 discloses a kind of method of quickly starting oxygen-poor ammonia oxidizing biofilter, it is characterized in that step (2) adds azanol, challenge inoculation mud changes to oxygen-poor ammonia oxidizing biomembrane, more than invent mainly by the azanol inhibitory action to NOB, promote short distance nitration effect. CN201410141638.7 discloses the culture fluid of a kind of nitrite bacteria and preparation and cultural method, its culture fluid formula is more complicated, the element of Growth of Cells is provided except relating to ferrum, calcium, potassium, magnesium etc., further relates to cobalt, molybdenum, manganese, zinc etc. and promote the element of enzymatic synthesis.
Summary of the invention
For the deficiencies in the prior art, the invention provides a kind of accelerator cultivating nitrobacteria and preparation method thereof. This accelerator formula is simple, preparation is easily, it is possible to in the incubation of nitrobacteria, it is also possible to be directly added in sewage disposal system, making nitrobacteria to breed by fast-growth at short notice, the nitrobacteria activity cultivated is high, tolerance impact capacity is strong.
The present invention cultivates the accelerator of nitrobacteria, and including slaine and polyamines, with parts by weight, slaine is 40 ~ 100 weight portions, it is preferred to 50 ~ 80 weight portions; Polyamines is 5 ~ 30 weight portions, it is preferred to 10 ~ 20 weight portions; Described slaine is calcium salt, magnesium salt and mantoquita, Ca2+��Mg2+And Cu2+Mol ratio be (5 ~ 15): (5 ~ 25): (0.5 ~ 5), it is preferred to (8 ~ 12): (10 ~ 20): (1 ~ 4).
Calcium salt of the present invention is CaSO4Or CaCl2, it is preferable that CaSO4; Magnesium salt is MgSO4Or MgCl2, it is preferable that MgSO4; Mantoquita is CuSO4Or CuCl2, it is preferable that CuSO4��
Polyamines of the present invention is spermine, spermidine or both mixture.
Accelerator of the present invention also includes mineral acid hydroxylamines, and content is 0.5 ~ 15 weight portion, it is preferred to 2 ~ 10 weight portions. Described mineral acid hydroxylamines is one or more in oxammonium hydrochloride., oxammonium sulfate. or phosphatic hydroxylamine, it is preferred to oxammonium sulfate..
The preparation method of the accelerator of cultivation nitrobacteria of the present invention, including following content: (1) prepares metal salt solution according to consisting of and weight portion: slaine is 40 ~ 100 weight portions, being preferably 50 ~ 80 weight portions, described slaine is calcium salt, magnesium salt and mantoquita, Ca in slaine2+��Mg2+And Cu2+Mol ratio be (5 ~ 15): (5 ~ 25): (0.5 ~ 5), it is preferred to (8 ~ 12): (10 ~ 20): (1 ~ 4); (2) by 5 ~ 30 weight portions before using, it is preferred to the polyamines of 10 ~ 20 weight portions joins in metal salt solution.
Calcium salt described in step of the present invention (1) is CaSO4Or CaCl2, it is preferable that CaSO4; Magnesium salt is MgSO4Or MgCl2, it is preferable that MgSO4; Mantoquita is CuSO4Or CuCl2, it is preferable that CuSO4��
Polyamines described in step of the present invention (2) is spermine, spermidine or both mixture.
Further, can also add content before using in step of the present invention (2) is 0.5 ~ 15 weight portion, being preferably the mineral acid azanol of 2 ~ 10 weight portions, described mineral acid azanol is one or more in oxammonium hydrochloride., oxammonium sulfate. or phosphatic hydroxylamine, it is preferred to oxammonium sulfate..
Nitrobacteria growth promoter of the present invention may be used for the incubation of nitrobacteria, it is possible to for improving the ammonia nitrogen removal effect of sewage disposal system, it is also possible to for quickly starting and the fast quick-recovery of the system that is hit containing ammonia system. Concrete needs determines dosage according to sewage character, treating capacity and treatment effect. In use, first accelerator is dissolved, then according to promoter concentration 10 ~ 100mg/L adds in sewage.
Compared with prior art, the method have the advantages that
1, utilize the metal ion that slaine provides to grow required element as nitrobacteria, simultaneously as the activity of the component raising enzyme of enzyme, it is possible to fast degradation substrate, accelerate enzymatic reaction process. Polyamines and metal ion combined effect, it is possible to accelerate cell proliferation, and settleability and the stability of gather in the crops thalline can be improved, prolongation thalline service life.
2, can directly participating in the metabolic process of nitrobacteria as the substrate of azanol oxygen also enzyme, shorten enzymatic reaction process appropriate addition of mineral acid azanol, the activator simultaneously as cell can accelerated cell growth.
3, the present invention is by selecting component and the proportioning of nitrobacteria growth promoter, under the combined effect of slaine, polyamines and mineral acid azanol, it is achieved the purpose of fast culture nitrobacteria. The invention solves the problem that nitrobacteria growth is slow, may also speed up nitration reaction process simultaneously, improve the treatment effect of waste water. After using accelerator, the growth rate of nitrobacteria can increase by 10 ~ 100 times, and the ammonia nitrogen removal frank of ammonia-containing water can improve more than 30%, moreover it is possible to solves the fast recovery problem of the nitrated ammonia nitrogen removal ability of sewage disposal system being hit well.
Detailed description of the invention
Below in conjunction with specific embodiment, the present invention program is described in detail.
The formula of the nitrobacteria growth promoter of embodiment 1 ~ 8 and comparative example 1-4 is in Table 1.
The formula of table 1 accelerator and ratio
The major pollutants COD concentration contained in the waste water of certain enterprise discharge is about 1000mg/L, ammonia nitrogen concentration is about 150mg/L, this factory's anaerobic-aerobic (A/O) technique processes, but in water outlet after treatment, COD concentration is still up to more than 60mg/L less than 60mg/L ammonia nitrogen concentration. The accelerator that in utilization, table proportioning configures, configuration concentration is 0.5g/L, every day is that 30mg/L adds according to promoter concentration in sewage, after adding 15 days, ammonia nitrogen removal frank improves more than 10% stopping and adding, system continues to run with 15 days, and water sampling is analyzed water outlet ammonia nitrogen concentration and calculates ammonia nitrogen removal frank. After adding, concrete result is in Table 2, effluent quality from each embodiment of table 2, when adding accelerator, water outlet ammonia nitrogen concentration is 75mg/L, ammonia nitrogen removal frank only has 50%, and after adding accelerator, water outlet ammonia nitrogen concentration is below 30mg/L, and ammonia nitrogen removal frank is all higher than 80%, during when accelerator containing only the slaine having in formula or polyamines, water outlet ammonia nitrogen concentration still between 30 ~ 50mg/L, ammonia nitrogen removal frank is lower than 80%. As can be seen here, the growth promoter of the present invention is used can to significantly improve the clearance of ammonia nitrogen in sewage.
Table 2 adopts the treatment effect of different formulations accelerator
Example Water outlet ammonia nitrogen concentration, mg/L Ammonia nitrogen removal frank, % Sludge settling ratio SV30, %
Embodiment 1 22.5 85.0 24
Embodiment 2 26.0 82.7 28
Embodiment 3 28.1 81.3 30
Embodiment 4 23.7 84.2 29
Embodiment 5 29.9 80.1 27
Embodiment 6 24.5 83.7 33
Embodiment 7 14.3 90.5 20
Embodiment 8 17.4 88.4 23
Comparative example 1 35.0 76.7 38
Comparative example 2 38.9 74.1 36
Comparative example 3 45.3 69.8 40
Comparative example 4 41.3 72.5 37
It is not added with accelerator 75.0 50.0 48
After process terminates, Aeration tank active sludge intermixture is carried out sludge settling ratio SV30Detection, result is as shown in table 2, illustrates that growth promoter of the present invention contributes to mud and better settles.

Claims (11)

1. the accelerator cultivating nitrobacteria, it is characterised in that include slaine and polyamines, with parts by weight, slaine is 40 ~ 100 weight portions, and polyamines is 5 ~ 30 weight portions; Described slaine is calcium salt, magnesium salt and mantoquita, Ca2+��Mg2+And Cu2+Mol ratio be (5 ~ 15): (5 ~ 25): (0.5 ~ 5).
2. the growth promoter described in claim 1, it is characterised in that: slaine is 50 ~ 80 weight portions, and polyamines is 10 ~ 20 weight portions, Ca2+��Mg2+And Cu2+Mol ratio be (8 ~ 12): (10 ~ 20): (1 ~ 4).
3. the growth promoter described in claim 1 or 2, it is characterised in that: calcium salt is CaSO4Or CaCl2, magnesium salt is MgSO4Or MgCl2, mantoquita is CuSO4Or CuCl2��
4. the growth promoter described in claim 1 or 2, it is characterised in that: calcium salt is CaSO4, magnesium salt is MgSO4, mantoquita is CuSO4��
5. the growth promoter described in claim 1 or 2, it is characterised in that: polyamines is spermine, spermidine or both mixture.
6. the growth promoter described in claim 1 or 2, it is characterised in that: described accelerator also includes mineral acid azanol, and content is 0.5 ~ 15 weight portion.
7. the growth promoter described in claim 6, it is characterised in that: mineral acid azanol is one or more in oxammonium hydrochloride., oxammonium sulfate. or phosphatic hydroxylamine, and content is 2 ~ 10 weight portions.
8. the growth promoter described in claim 6, it is characterised in that: mineral acid hydroxylamines is oxammonium sulfate..
9. the preparation method of the accelerator cultivating nitrobacteria, it is characterized in that including following content: (1) prepares metal salt solution according to consisting of and weight portion: slaine is 40 ~ 100 weight portions, it is preferably 50 ~ 80 weight portions, described slaine is calcium salt, magnesium salt and mantoquita, Ca in slaine2+��Mg2+And Cu2+Mol ratio be (5 ~ 15): (5 ~ 25): (0.5 ~ 5), it is preferred to (8 ~ 12): (10 ~ 20): (1 ~ 4); (2) by 5 ~ 30 weight portions before using, it is preferred to the polyamines of 10 ~ 20 weight portions joins in metal salt solution.
10. in accordance with the method for claim 9, it is characterised in that: it is additionally added, before step (2) uses, the mineral acid azanol that content is 0.5 ~ 15 weight portion, it is preferred to 2 ~ 10 weight portions; Mineral acid azanol is one or more in oxammonium hydrochloride., oxammonium sulfate. or phosphatic hydroxylamine.
11. the application of the arbitrary described accelerator of claim 1-10, it is characterised in that: in use, first accelerator is dissolved, then according to promoter concentration 10 ~ 100mg/L adds in sewage.
CN201410585418.3A 2014-10-28 2014-10-28 Promoter for culturing nitrifying bacteria and preparation method thereof Active CN105624087B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201410585418.3A CN105624087B (en) 2014-10-28 2014-10-28 Promoter for culturing nitrifying bacteria and preparation method thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201410585418.3A CN105624087B (en) 2014-10-28 2014-10-28 Promoter for culturing nitrifying bacteria and preparation method thereof

Publications (2)

Publication Number Publication Date
CN105624087A true CN105624087A (en) 2016-06-01
CN105624087B CN105624087B (en) 2019-12-10

Family

ID=56039437

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201410585418.3A Active CN105624087B (en) 2014-10-28 2014-10-28 Promoter for culturing nitrifying bacteria and preparation method thereof

Country Status (1)

Country Link
CN (1) CN105624087B (en)

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1986443A (en) * 2005-12-22 2007-06-27 中国石化上海石油化工股份有限公司 Nitrobacteria growth promoter
CN1986446A (en) * 2005-12-22 2007-06-27 中国石化上海石油化工股份有限公司 Nitrobacteria growth promoter
CN101045578A (en) * 2006-03-29 2007-10-03 中国石化上海石油化工股份有限公司 Method for removing sewage aminonitrogen by activated sludge process
CN101045577A (en) * 2006-03-29 2007-10-03 中国石化上海石油化工股份有限公司 Method for removing sewage aminonitrogen by activated sludge process
CN101062812A (en) * 2006-04-27 2007-10-31 中国石化上海石油化工股份有限公司 Method for removing sewage ammonia nitrogen by active sludge oxidation ditch technique
CN101899401A (en) * 2009-05-25 2010-12-01 中国石油化工股份有限公司 Microbial agent for treating ammonia-containing waste water and preparation method thereof
CN101898828A (en) * 2009-05-25 2010-12-01 中国石油化工股份有限公司 Method for culturing granular sludge by shortcut denitrification

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1986443A (en) * 2005-12-22 2007-06-27 中国石化上海石油化工股份有限公司 Nitrobacteria growth promoter
CN1986446A (en) * 2005-12-22 2007-06-27 中国石化上海石油化工股份有限公司 Nitrobacteria growth promoter
CN101045578A (en) * 2006-03-29 2007-10-03 中国石化上海石油化工股份有限公司 Method for removing sewage aminonitrogen by activated sludge process
CN101045577A (en) * 2006-03-29 2007-10-03 中国石化上海石油化工股份有限公司 Method for removing sewage aminonitrogen by activated sludge process
CN101062812A (en) * 2006-04-27 2007-10-31 中国石化上海石油化工股份有限公司 Method for removing sewage ammonia nitrogen by active sludge oxidation ditch technique
CN101899401A (en) * 2009-05-25 2010-12-01 中国石油化工股份有限公司 Microbial agent for treating ammonia-containing waste water and preparation method thereof
CN101898828A (en) * 2009-05-25 2010-12-01 中国石油化工股份有限公司 Method for culturing granular sludge by shortcut denitrification

Non-Patent Citations (3)

* Cited by examiner, † Cited by third party
Title
GUANGJING XU ET AL.: ""Partial nitrification adjusted by hydroxylamine in aerobic granules under high DO and ambient temperature and subsequent Anammox for low C/N wastewater treatment"", 《CHEMICAL ENGINEERING JOURNAL》 *
SCOTT A.ENSIN ET AL.: ""In Vitro Activation of Ammonia Monooxygenase from Nitrosomonas europaea by Copper"", 《J.BACTERIOL.》 *
刘倩: ""微量铜离子对SBR中微生物种群结构影响的分析"", 《中国优秀硕士学位论文全文数据库 工程科技I辑》 *

Also Published As

Publication number Publication date
CN105624087B (en) 2019-12-10

Similar Documents

Publication Publication Date Title
Wen et al. A novel process combining simultaneous partial nitrification, anammox and denitrification (SNAD) with denitrifying phosphorus removal (DPR) to treat sewage
CN105624094A (en) Nitrifying bacterium culture promoter as well as preparation method and application thereof
Zhu et al. Minimizing nitrous oxide in biological nutrient removal from municipal wastewater by controlling copper ion concentrations
CN105624093A (en) Nitrite bacterium culture promoter and preparation method thereof
CN102041291A (en) Method for screening denitrifying bacterium
CN106676022A (en) Method for preparing microbe bacteria liquid for treating black-odor riverway
CN106754450A (en) A kind of denitrifying microorganism culture promoter and its preparation method and application
CN105585133A (en) Bio-denitrification method for high-salt-content wastewater discharged from catalyst production process
CN105624086A (en) Nitrifying bacteria growth promoter and preparation method thereof
Ni et al. Performance and inhibition recovery of anammox reactors seeded with different types of sludge
CN105543158B (en) Nitrobacteria growth promoter and preparation method and application thereof
CN105624053A (en) Enrichment culture method for nitrifying bacteria
Zhou et al. Enhancing nitrogen removal from anaerobically-digested swine wastewater through integration of Myriophyllum aquaticum and free nitrous acid-based technology in a constructed wetland
CN106745727B (en) Denitrification method for ammonia-containing wastewater discharged in acrylic fiber production process
CN105621625A (en) Nitrite bacteria growth promoter and preparation method thereof
CN105624088A (en) Ammonia oxidizing bacteria growth promoter as well as preparation method and applications thereof
CN105621624B (en) A kind of denitrogenation method of acrylic fiber production process process discharge ammonia-containing water
CN106554076B (en) Biological treatment method of ammonia-containing wastewater
CN105621610B (en) A kind of saline sewage simultaneous nitrification-denitrification denitrogenation method
CN105624089A (en) Promoter for culturing ammonia oxidizing bacteria and preparation method of promoter
CN105624090A (en) Promoter for culturing nitrifying bacteria and preparation method of promoter
CN105624087A (en) Promoter for culturing nitrifying bacteria and preparation method of promoter
CN109880785B (en) Composition capable of promoting denitrification of nitrifying bacteria and application thereof
CN105624095A (en) Enrichment culture method for nitrifying bacteria by waste water generated in catalyst production process
CN105624054A (en) Enrichment culture method for salt-tolerant nitrifying bacteria colonies

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant
TR01 Transfer of patent right

Effective date of registration: 20230828

Address after: 100728 No. 22 North Main Street, Chaoyang District, Beijing, Chaoyangmen

Patentee after: CHINA PETROLEUM & CHEMICAL Corp.

Patentee after: Sinopec (Dalian) Petrochemical Research Institute Co.,Ltd.

Address before: 100728 No. 22 North Main Street, Chaoyang District, Beijing, Chaoyangmen

Patentee before: CHINA PETROLEUM & CHEMICAL Corp.

Patentee before: DALIAN RESEARCH INSTITUTE OF PETROLEUM AND PETROCHEMICALS, SINOPEC Corp.

TR01 Transfer of patent right