CN102627379B - Method for storing and exciting anaerobic ammonium oxidation sludge - Google Patents

Method for storing and exciting anaerobic ammonium oxidation sludge Download PDF

Info

Publication number
CN102627379B
CN102627379B CN 201210083723 CN201210083723A CN102627379B CN 102627379 B CN102627379 B CN 102627379B CN 201210083723 CN201210083723 CN 201210083723 CN 201210083723 A CN201210083723 A CN 201210083723A CN 102627379 B CN102627379 B CN 102627379B
Authority
CN
China
Prior art keywords
preservation
concentration
inorganic salt
solution
mud
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
CN 201210083723
Other languages
Chinese (zh)
Other versions
CN102627379A (en
Inventor
金仁村
马春
阳广凤
俞津津
邢保山
张倩倩
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.)
Hangzhou Normal University
Original Assignee
Hangzhou Normal University
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 Hangzhou Normal University filed Critical Hangzhou Normal University
Priority to CN 201210083723 priority Critical patent/CN102627379B/en
Publication of CN102627379A publication Critical patent/CN102627379A/en
Application granted granted Critical
Publication of CN102627379B publication Critical patent/CN102627379B/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Micro-Organisms Or Cultivation Processes Thereof (AREA)

Abstract

The invention relates to a method for storing and exciting anaerobic ammonium oxidation sludge. The method for storing the anaerobic ammonium oxidation sludge comprises the steps as follows: firstly, washing the anaerobic ammonium oxidation sludge needed to be stored by an inorganic salt solution, and placing in a storage container; secondly, adding the inorganic salt solution for adjusting the volatile suspended solid concentration of the anaerobic ammonium oxidation sludge to be 10-36 g/L and the pH value to be 7.5-8.0; thirdly, filling argon gas; and lastly, sealing the storage container, and storing in a refrigerator of 0-4 DEG C. The method for exciting the anaerobic ammonium oxidation sludge comprises the steps as follows: taking out the anaerobic ammonium oxidation sludge, washing by the inorganic salt solution, adding a nutrient solution, filling up distillation water into an excitation container, adjusting the pH value to be 7.0-7.5, filling the argon gas, vibrating for cultivation, sampling and measuring the concentrations of NH4+-N and NO2--N in the cultivation process, and adding a matrix concentration solution as needed. The method has the advantages of simple equipment requirements, higher activity retention rate, shorter excitation time and better excitation effect.

Description

A kind of preservation of Anammox mud and Activiation method
Technical field
The present invention relates to a kind of preservation and Activiation method of Anammox mud, belong to field of Environment Protection.
Background technology
Anammox is a kind of new and effective biological denitrification process, not only can save in the oxygenation energy consumption of nitration reaction in traditional denitrification process and anti-nitration reaction and need the external source organic electronic donor added, also improve nitration reaction and produce acid, denitrification produces alkali and all needs the situation neutralized.Reduce the demand of chemical reagent, prevented the secondary pollution that may occur.Since coming out, just be subject to showing great attention to.
Anaerobic ammonia oxidizing bacteria belongs to Planctomycetes, is chemosynthetic autotroph biology, poor growth.Therefore caused this technique long shortcoming start time, and anaerobic ammonia oxidizing bacteria to envrionment conditions for example, temperature, salinity, pH etc. are extremely responsive, and the easy unstability of technique is recovered slowly.
Therefore can carry out effective preservation to the anaerobic ammonia oxidizing bacteria of high-quality, and can be in the situation that needs, by certain technique means, the activity that activates anaerobic ammonia oxidizing bacteria is significant.Its inoculation source as new startup reactor can be able to be realized to the quick startup of Anammox, or, in the situation that the reactor unstability is added organism as external source, guarantee the process operation efficient stable.
Summary of the invention
The object of the present invention is to provide a kind of method of preservation and activation of Anammox mud.
The inventive method comprises method for preserving and the Activiation method of Anammox mud, wherein
The method for preserving of Anammox mud is specifically: at first will need inorganic salt solution for the Anammox mud of preservation to rinse 2~5 times, be placed in the preservation container, the volatile suspended sediment concentration that adds inorganic salt solution to adjust Anammox mud is 10~36g/L, with the NaOH solution of 1~2mol/L or the HCl solution of 1~2mol/L, the pH value of preservation liquid in container is adjusted to 7.5~8.0, then be filled with argon gas, the preservation container sealing is placed on to 0~4 ℃ of refrigerator preservation.
The Activiation method of Anammox mud is specifically: take out as required part Anammox mud in the preservation container, be placed in activation vessel, with inorganic salt solution, rinse 2~5 times, add the nutritive medium that is equivalent to activation vessel effective volume 15~20 ﹪, add distilled water that activation vessel is filled it up with, with the NaOH solution of 1~2mol/L or the HCl solution of 1~2mol/L, the pH value of liquid in activation vessel is adjusted to 7.0~7.5, then be filled with argon gas, activation vessel is placed in to the shaking culture case, cultivates under 30~35 ℃, 120~180rpm rotating speed; In culturing process every 10~12h sampling and measuring NH 4 +-N and NO 2 --N concentration, as wherein a kind of concentration is less than or equal to 5mg/L, add corresponding NH 4 +-N matrix concentrated solution or NO 2 --N matrix concentrated solution, the concentration of matrix concentrated solution is 1000~1500mg/L, 1.5~2 ﹪ that add-on is the activation vessel effective volume; After cultivating 48~120h, taking-up mud can come into operation.
The component of the inorganic salt solution in method for preserving and Activiation method and the concentration of each component are: the KH of 10~15mg/L 2pO 4, 5.6~8.4mg/L CaCl 22H 2the MgSO of O, 300~450mg/L 47H 2the KHCO of O, 1000~1500mg/L 3;
The component of the nutritive medium described in Activiation method and the concentration of each component are: the NH of 100~150mg/L 4 +the NO of-N, 100~150mg/L 2 -the KH of-N, 50~75mg/L 2pO 4, 28~42mg/L CaCl 22H 2the MgSO of O, 1500~2250mg/L 47H 2the KHCO of O, 5000~7500mg/L 3, the EDTA of 125.5~187.5mg/L, the FeSO of 57.1~85.7mg/L 47H 2the H of O, 0.0875~0.13mg/L 3bO 4, 6.19~9.28mg/L MnCl 24H 2the CuSO of O, 1.56~2.34mg/L 45H 2the ZnSO of O, 2.69~4.03mg/L 47H 2the NiCl of O, 1.31~1.97mg/L 26H 2the NaMoO of O, 1.38~2.06mg/L 42H 2the CoCl of O, 1.5~2.25mg/L 26H 2o.
The inventive method equipment requirements is simple, does not need strict process control, can realize the long-term preservation of Anammox mud, and activity preservation rate is higher; Activationary time is shorter simultaneously, and activation effect is good; Applied widely; Cost is lower.The method has solved the inoculation source problem of anaerobic ammonia oxidation process application, has a extensive future.
Embodiment
Embodiment 1.
The method for preserving of Anammox mud: at first will need the Anammox mud of preservation to rinse 2 times with inorganic salt solution, be placed in the preservation container, the volatile suspended sediment concentration that adds inorganic salt solution to adjust Anammox mud is 10g/L, with NaOH or the HCl solution of 1mol/L, the pH value of preservation liquid in container is adjusted to 7.5, then be filled with argon gas, the preservation container sealing is placed on to 0 ℃ of refrigerator preservation.
In preservation, after 1st month, its activity is 17.8mgN (gVSSh) -1, activity preservation rate is 82.8%, can think effectively preservation Anammox mud of the method.
The Activiation method of Anammox mud: take out as required part Anammox mud in the preservation container, be placed in activation vessel, with inorganic salt solution, rinse 2 times, add the nutritive medium that is equivalent to activation vessel effective volume 15 ﹪, add distilled water that activation vessel is filled it up with, with NaOH or the HCl solution of 1mol/L, the pH value of liquid in activation vessel is adjusted to 7.0, then is filled with argon gas; Activation vessel is placed in to the shaking culture case, cultivates under 30 ℃, 180rpm rotating speed; In culturing process every 12h sampling and measuring NH 4 +-N and NO 2 --N concentration, as wherein a kind of concentration is less than or equal to 5mg/L, add the NH that corresponding concentration is 1000mg/L 4 +-N matrix concentrated solution or NO 2 --N matrix concentrated solution, 2 ﹪ that add-on is the activation vessel effective volume; After cultivating 48h, taking-up mud can come into operation.
The component of above-mentioned inorganic salt solution and the concentration of each component are: the KH of 10mg/L 2pO 4, 8.4mg/L CaCl 22H 2the MgSO of O, 300mg/L 47H 2the KHCO of O, 1500mg/L 3;
The component of above-mentioned nutritive medium and the concentration of each component are: the NH of 150mg/L 4 +the NO of-N, 150mg/L 2 -the KH of-N, 50mg/L 2pO 4, 28mg/L CaCl 22H 2the MgSO of O, 2250mg/L 47H 2the KHCO of O, 7500mg/L 3, the EDTA of 125.5mg/L, the FeSO of 57.1mg/L 47H 2the H of O, 0.0875mg/L 3bO 4, 6.19mg/L MnCl 24H 2the CuSO of O, 2.34mg/L 45H 2the ZnSO of O, 4.03mg/L 47H 2the NiCl of O, 1.97mg/L 26H 2the NaMoO of O, 2.06mg/L 42H 2the CoCl of O, 2.25mg/L 26H 2o.
Experiment shows to process through the activation of 3 days, even the hungry preservation mud of 1 month, its activity can reach 19.5mgN (gVSSh) -1, return to 90.7% of the front activity of preservation.
Embodiment 2.
The method for preserving of Anammox mud: at first will need the Anammox mud of preservation to rinse 3 times with inorganic salt solution, be placed in the preservation container, the volatile suspended sediment concentration that adds inorganic salt solution to adjust Anammox mud is 20g/L, with NaOH or the HCl solution of 1.5mol/L, the pH value of preservation liquid in container is adjusted to 7.8, then be filled with argon gas, the preservation container sealing is placed on to 1 ℃ of refrigerator preservation.
In preservation, after 1st month, its activity is 18.1mgN (gVSSh) -1, activity preservation rate is 84.2%, can think effectively preservation Anammox mud of the method.
The Activiation method of Anammox mud: take out as required part Anammox mud in the preservation container, be placed in activation vessel, with inorganic salt solution, rinse 3 times, add the nutritive medium that is equivalent to activation vessel effective volume 20 ﹪, add distilled water that activation vessel is filled it up with, with NaOH or the HCl solution of 1.5mol/L, the pH value of liquid in activation vessel is adjusted to 7.2, then is filled with argon gas; Activation vessel is placed in to the shaking culture case, cultivates under 32 ℃, 150rpm rotating speed; In culturing process every 10h sampling and measuring NH 4 +-N and NO 2 --N concentration, as wherein a kind of concentration is less than or equal to 5mg/L, add the NH that corresponding concentration is 1200mg/L 4 +-N matrix concentrated solution or NO 2 --N matrix concentrated solution, 1.6 ﹪ that add-on is the activation vessel effective volume; After cultivating 60h, taking-up mud can come into operation.
The component of above-mentioned inorganic salt solution and the concentration of each component are: the KH of 12mg/L 2pO 4, 8.0mg/L CaCl 22H 2the MgSO of O, 450mg/L 47H 2the KHCO of O, 1200mg/L 3;
The component of above-mentioned nutritive medium and the concentration of each component are: the NH of 100mg/L 4 +the NO of-N, 100mg/L 2 -the KH of-N, 60mg/L 2pO 4, 35mg/L CaCl 22H 2the MgSO of O, 1500mg/L 47H 2the KHCO of O, 6000mg/L 3, the EDTA of 151mg/L, the FeSO of 60.5mg/L 47H 2the H of O, 0.1mg/L 3bO 4, 7.23mg/L MnCl 24H 2the CuSO of O, 1.56mg/L 45H 2the ZnSO of O, 2.69mg/L 47H 2the NiCl of O, 1.31mg/L 26H 2the NaMoO of O, 1.38mg/L 42H 2the CoCl of O, 1.5mg/L 26H 2o.
Experiment shows to process through the activation of 3 days, even the hungry preservation mud of 1 month, its activity can reach 19.3mgN (gVSSh) -1, return to 89.8% of the front activity of preservation.
Embodiment 3
The method for preserving of Anammox mud: at first will need the Anammox mud of preservation to rinse 4 times with inorganic salt solution, be placed in the preservation container, the volatile suspended sediment concentration that adds inorganic salt solution to adjust Anammox mud is 30g/L, with NaOH or the HCl solution of 2mol/L, the pH value of preservation liquid in container is adjusted to 8.0, then be filled with argon gas, the preservation container sealing is placed on to 4 ℃ of refrigerator preservations.
In preservation, after 1st month, its activity is 17.9mgN (gVSSh) -1, activity preservation rate is 83.3%, can think effectively preservation Anammox mud of the method.
The Activiation method of Anammox mud: take out as required part Anammox mud in the preservation container, be placed in activation vessel, with inorganic salt solution, rinse 4 times, add the nutritive medium that is equivalent to activation vessel effective volume 15 ﹪, add distilled water that activation vessel is filled it up with, with NaOH or the HCl solution of 2mol/L, the pH value of liquid in activation vessel is adjusted to 7.5, then is filled with argon gas; Activation vessel is placed in to the shaking culture case, cultivates under 35 ℃, 120rpm rotating speed; In culturing process every 11h sampling and measuring NH 4 +-N and NO 2 --N concentration, as wherein a kind of concentration is less than or equal to 5mg/L, add the NH that corresponding concentration is 1500mg/L 4 +-N matrix concentrated solution or NO 2 --N matrix concentrated solution, 1.5 ﹪ that add-on is the activation vessel effective volume; After cultivating 120h, taking-up mud can come into operation.
The component of above-mentioned inorganic salt solution and the concentration of each component are: the KH of 15mg/L 2pO 4, 5.6mg/L CaCl 22H 2the MgSO of O, 400mg/L 47H 2the KHCO of O, 1000mg/L 3;
The component of above-mentioned nutritive medium and the concentration of each component are: the NH of 120mg/L 4 +the NO of-N, 120mg/L 2 -the KH of-N, 75mg/L 2pO 4, 42mg/L CaCl 22H 2the MgSO of O, 2000mg/L 47H 2the KHCO of O, 5000mg/L 3, the EDTA of 187.5mg/L, the FeSO of 85.7mg/L 47H 2the H of O, 0.13mg/L 3bO 4, 9.28mg/L MnCl 24H 2the CuSO of O, 2.04mg/L 45H 2the ZnSO of O, 3.25mg/L 47H 2the NiCl of O, 1.58mg/L 26H 2the NaMoO of O, 1.65mg/L 42H 2the CoCl of O, 2.0mg/L 26H 2o.
Experiment shows to process through the activation of 3 days, even the hungry preservation mud of 1 month, its activity can reach 19.1mgN (gVSSh) -1, return to 88.9% of the front activity of preservation.
Embodiment 4
The method for preserving of Anammox mud: at first will need the Anammox mud of preservation to rinse 5 times with inorganic salt solution, be placed in the preservation container, the volatile suspended sediment concentration that adds inorganic salt solution to adjust Anammox mud is 36g/L, with NaOH solution or the HCl solution of 1.2mol/L, the pH value of preservation liquid in container is adjusted to 7.6, then be filled with argon gas, the preservation container sealing is placed on to 2 ℃ of refrigerator preservations.
In preservation, after 1st month, its activity is 18.4mgN (gVSSh) -1, activity preservation rate is 85.6%, can think effectively preservation Anammox mud of the method.
The Activiation method of Anammox mud: take out as required part Anammox mud in the preservation container, be placed in activation vessel, with inorganic salt solution, rinse 5 times, add the nutritive medium that is equivalent to activation vessel effective volume 18 ﹪, add distilled water that activation vessel is filled it up with, with NaOH or the HCl solution of 1.2mol/L, the pH value of liquid in activation vessel is adjusted to 7.3, then is filled with argon gas; Activation vessel is placed in to the shaking culture case, cultivates under 30 ℃, 150rpm rotating speed; In culturing process every 12h sampling and measuring NH 4 +-N and NO 2 --N concentration, as wherein a kind of concentration is less than or equal to 5mg/L, add the NH that corresponding concentration is 1500mg/L 4 +-N matrix concentrated solution or NO 2 --N matrix concentrated solution, 2 ﹪ that add-on is the activation vessel effective volume; After cultivating 96h, taking-up mud can come into operation.
The component of above-mentioned inorganic salt solution and the concentration of each component are: the KH of 13mg/L 2pO 4, 6.4mg/L CaCl 22H 2the MgSO of O, 350mg/L 47H 2the KHCO of O, 1300mg/L 3;
The component of above-mentioned nutritive medium and the concentration of each component are: the NH of 130mg/L 4 +the NO of-N, 130mg/L 2 -the KH of-N, 55mg/L 2pO 4, 30mg/L CaCl 22H 2the MgSO of O, 1800mg/L 47H 2the KHCO of O, 7000mg/L 3, the EDTA of 165.5mg/L, the FeSO of 80.2mg/L 47H 2the H of O, 0.125mg/L 3bO 4, 8.31mg/L MnCl 24H 2the CuSO of O, 1.84mg/L 45H 2the ZnSO of O, 3.53mg/L 47H 2the NiCl of O, 1.45mg/L 26H 2the NaMoO of O, 1.86mg/L 42H 2the CoCl of O, 1.85mg/L 26H 2o.
Experiment shows to process through the activation of 3 days, even the hungry preservation mud of 1 month, its activity can reach 19.3mgN (gVSSh) -1, return to 89.8% of the front activity of preservation.
Embodiment 5
The method for preserving of Anammox mud: at first will need the Anammox mud of preservation to rinse 3 times with inorganic salt solution, be placed in the preservation container, the volatile suspended sediment concentration that adds inorganic salt solution to adjust Anammox mud is 30g/L, with NaOH solution or the HCl solution of 1mol/L, the pH value of preservation liquid in container is adjusted to 7.0, then be filled with argon gas, the preservation container sealing is placed on to 3 ℃ of refrigerator preservations.
In preservation, after 1st month, its activity is 18.6mgN (gVSSh) -1, activity preservation rate is 86.5%.Therefore can think effectively preservation Anammox mud of the method.
The Activiation method of Anammox mud: take out as required part Anammox mud in the preservation container, be placed in activation vessel, with inorganic salt solution, rinse 3 times, add the nutritive medium that is equivalent to activation vessel effective volume 20 ﹪, add distilled water that activation vessel is filled it up with, with NaOH solution or the HCl solution of 1mol/L, the pH value of liquid in activation vessel is adjusted to 7.5, then is filled with argon gas; Activation vessel is placed in to the shaking culture case, cultivates under 35 ℃, 120rpm rotating speed; In culturing process every 10h sampling and measuring NH 4 +-N and NO 2 --N concentration, as wherein a kind of concentration is less than or equal to 5mg/L, add the NH that corresponding concentration is 1500mg/L 4 +-N matrix concentrated solution or NO 2 --N matrix concentrated solution, 1.8 ﹪ that add-on is the activation vessel effective volume; After cultivating 72h, taking-up mud can come into operation.
The component of above-mentioned inorganic salt solution and the concentration of each component are: the KH of 11mg/L 2pO 4, 8.4mg/L CaCl 22H 2the MgSO of O, 400mg/L 47H 2the KHCO of O, 1200mg/L 3;
The component of above-mentioned nutritive medium and the concentration of each component are: the NH of 150mg/L 4 +the NO of-N, 150mg/L 2 -the KH of-N, 50mg/L 2pO 4, 42mg/L CaCl 22H 2the MgSO of O, 2000mg/L 47H 2the KHCO of O, 5500mg/L 3, the EDTA of 143.5mg/L, the FeSO of 57.1mg/L 47H 2the H of O, 0.13mg/L 3bO 4, 6.19mg/L MnCl 24H 2the CuSO of O, 1.56mg/L 45H 2the ZnSO of O, 3.45mg/L 47H 2the NiCl of O, 1.78mg/L 26H 2the NaMoO of O, 1.66mg/L 42H 2the CoCl of O, 1.65mg/L 26H 2o.
Experiment shows to process through the activation of 3 days, even the hungry preservation mud of 1 month, its activity can reach 19.5mgN (gVSSh) -1, return to 90.7% of the front activity of preservation.

Claims (1)

1. the preservation of an Anammox mud and Activiation method comprise and it is characterized in that method for preserving and the Activiation method of Anammox mud:
The method for preserving of described Anammox mud is specifically: at first will need inorganic salt solution for the Anammox mud of preservation to rinse 2~5 times, be placed in the preservation container, the volatile suspended sediment concentration that adds inorganic salt solution to adjust Anammox mud is 10~36g/L, with the NaOH solution of 1~2mol/L or the HCl solution of 1~2mol/L, the pH value of preservation liquid in container is adjusted to 7.5~8.0, then be filled with argon gas, the preservation container sealing is placed on to 0~4 ℃ of refrigerator preservation;
The Activiation method of described Anammox mud is specifically: take out as required part Anammox mud in the preservation container, be placed in activation vessel, with inorganic salt solution, rinse 2~5 times, add the nutritive medium that is equivalent to activation vessel effective volume 15~20 ﹪, add distilled water that activation vessel is filled it up with, with the NaOH solution of 1~2mol/L or the HCl solution of 1~2mol/L, the pH value of liquid in activation vessel is adjusted to 7.0~7.5, then be filled with argon gas, activation vessel is placed in to the shaking culture case, cultivates under 30~35 ℃, 120~180rpm rotating speed; In culturing process every 10~12h sampling and measuring NH 4 +-N and NO 2 --N concentration, as wherein a kind of concentration is less than or equal to 5mg/L, add corresponding NH 4 +-N matrix concentrated solution or NO 2 --N matrix concentrated solution, the concentration of matrix concentrated solution is 1000~1500mg/L, 1.5~2 ﹪ that add-on is the activation vessel effective volume; After cultivating 48~120h, taking-up mud can come into operation;
The component of the inorganic salt solution described in method for preserving and Activiation method and the concentration of each component are: the KH of 10~15mg/L 2pO 4, 5.6~8.4mg/L CaCl 22H 2the MgSO of O, 300~450mg/L 47H 2the KHCO of O, 1000~1500mg/L 3;
The component of the nutritive medium described in Activiation method and the concentration of each component are: the NH of 100~150mg/L 4 +the NO of-N, 100~150mg/L 2 -the KH of-N, 50~75mg/L 2pO 4, 28~42mg/L CaCl 22H 2the MgSO of O, 1500~2250mg/L 47H 2the KHCO of O, 5000~7500mg/L 3, the EDTA of 125.5~187.5mg/L, the FeSO of 57.1~85.7mg/L 47H 2the H of O, 0.0875~0.13mg/L 3bO 4, 6.19~9.28mg/L MnCl 24H 2the CuSO of O, 1.56~2.34mg/L 45H 2the ZnSO of O, 2.69~4.03mg/L 47H 2the NiCl of O, 1.31~1.97mg/L 26H 2the NaMoO of O, 1.38~2.06mg/L 42H 2the CoCl of O, 1.5~2.25mg/L 26H 2o.
CN 201210083723 2012-03-27 2012-03-27 Method for storing and exciting anaerobic ammonium oxidation sludge Expired - Fee Related CN102627379B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 201210083723 CN102627379B (en) 2012-03-27 2012-03-27 Method for storing and exciting anaerobic ammonium oxidation sludge

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 201210083723 CN102627379B (en) 2012-03-27 2012-03-27 Method for storing and exciting anaerobic ammonium oxidation sludge

Publications (2)

Publication Number Publication Date
CN102627379A CN102627379A (en) 2012-08-08
CN102627379B true CN102627379B (en) 2013-12-25

Family

ID=46585810

Family Applications (1)

Application Number Title Priority Date Filing Date
CN 201210083723 Expired - Fee Related CN102627379B (en) 2012-03-27 2012-03-27 Method for storing and exciting anaerobic ammonium oxidation sludge

Country Status (1)

Country Link
CN (1) CN102627379B (en)

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103755109B (en) * 2013-12-29 2015-04-22 杭州师范大学 Storage and reactivation methods of anaerobic ammonia oxidation granule sludge
CN110129203B (en) * 2019-04-23 2021-05-11 杭州师范大学 Preservation and recovery method of anaerobic ammonium oxidation strain
CN110255710A (en) * 2019-06-14 2019-09-20 杭州师范大学 A kind of tandem type anaerobic ammonia oxidation process for high-ammonia wastewater room temperature denitrogenation
CN111170451A (en) * 2020-01-20 2020-05-19 杭州师范大学 Method for rapidly improving activity of anaerobic ammonium oxidation sludge in short period
CN116694502A (en) * 2023-03-13 2023-09-05 浙江大学 Resuscitating method for anaerobic ammonia oxidation granular sludge after long-term low-temperature preservation

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101831392A (en) * 2009-03-10 2010-09-15 中国科学院成都生物研究所 Autotrophic and allotrophic symbiosis ammonia oxidation bacterial agent as well as culture method and application thereof
CN102061281A (en) * 2010-11-30 2011-05-18 哈尔滨工业大学 Method for enriching and culturing anaerobic ammonia oxidizing bacteria by using membrane bioreactor
CN102190371A (en) * 2010-03-18 2011-09-21 华东师范大学 Breeding method for anaerobic ammonium oxidation granular sludge
CN102336505A (en) * 2011-07-18 2012-02-01 杭州师范大学 Preservation method for anaerobic ammonium oxidation granular sludge

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101831392A (en) * 2009-03-10 2010-09-15 中国科学院成都生物研究所 Autotrophic and allotrophic symbiosis ammonia oxidation bacterial agent as well as culture method and application thereof
CN102190371A (en) * 2010-03-18 2011-09-21 华东师范大学 Breeding method for anaerobic ammonium oxidation granular sludge
CN102061281A (en) * 2010-11-30 2011-05-18 哈尔滨工业大学 Method for enriching and culturing anaerobic ammonia oxidizing bacteria by using membrane bioreactor
CN102336505A (en) * 2011-07-18 2012-02-01 杭州师范大学 Preservation method for anaerobic ammonium oxidation granular sludge

Also Published As

Publication number Publication date
CN102627379A (en) 2012-08-08

Similar Documents

Publication Publication Date Title
CN102627379B (en) Method for storing and exciting anaerobic ammonium oxidation sludge
Liu et al. Enhancement of anammox activity by addition of compatible solutes at high salinity conditions
Chen et al. Enhancement of anammox performance by Cu (II), Ni (II) and Fe (III) supplementation
CN102336505B (en) Preservation method for anaerobic ammonium oxidation granular sludge
CN104891651A (en) Method for operating anaerobic ammoxidation reactor capable of rapidly restarting heavy metal pollution
CN103975788A (en) Microbial fuel cell bonsai and method for in-situ hexavalent chromium-polluted soil remediation
CN102966341A (en) Method for increasing stratum layer oil recovery factor by utilizing wastewater
Ruirui et al. Application of zeolite adsorption and biological anaerobic digestion technology on hydrothermal liquefaction wastewater
CN103421854A (en) Biological preparation method of (S)-3-(dimethylamino)-1-(thiophene-2-radical)-1-propyl alcohol
CN104445846B (en) A kind of method of anaerobic ammonium oxidation sludge activity of quick active heavy metal contamination
CN106115932A (en) Sponge iron is collaborative with microorganism goes removing sulfate and the method for Cr (VI) waste water
CN107574189A (en) A kind of fermentation method for producing of 1,3 propane diols based on clostridium butyricum
CN103265142A (en) Method for treating acidic mine waste water
CN105731650A (en) Completely biological control nitrophenol enhanced electrochemical degradation method
Cristiani et al. Electron recycle concept in a microbial electrolysis cell for biogas upgrading
CN106268675A (en) A kind of preparation of triethylene tetramine modified magnetic palm bark adsorbent
CN103951054A (en) Method for treating perchlorate in inorganic water body by using continuous flow anaerobic bioreactor
CN104276650B (en) A kind of method of degradation of methylene blue
CN105645554A (en) Processing method of circulating water
CN204151139U (en) A kind of sequence batch (A/O linked system wastewater treatment equipment realizing waste water short distance nitration
CN104326548A (en) Method for degrading safranine T
CN105251467A (en) Preparation method of material with high methyl blue adsorption performance
Detchanamurthy et al. Studies on the influence of different metabolic uncouplers on the biodegradation of toluene in a differential biofilter reactor
CN102177880B (en) Constant-speed plant transfusion device
CN103787560B (en) A kind of liquid memory method of the aerobic particle mud based on acetone dehydration

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20131225