CN112142199A - Device and method for improving integrated partial denitrification-anaerobic ammonia oxidation coupling denitrification performance - Google Patents
Device and method for improving integrated partial denitrification-anaerobic ammonia oxidation coupling denitrification performance Download PDFInfo
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- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 title claims abstract description 125
- 238000007254 oxidation reaction Methods 0.000 title claims abstract description 73
- 230000003647 oxidation Effects 0.000 title claims abstract description 66
- 229910021529 ammonia Inorganic materials 0.000 title claims abstract description 60
- 238000000034 method Methods 0.000 title claims abstract description 23
- 238000010168 coupling process Methods 0.000 title claims abstract description 13
- 230000008878 coupling Effects 0.000 title claims abstract description 6
- 238000005859 coupling reaction Methods 0.000 title claims abstract description 6
- 239000010802 sludge Substances 0.000 claims abstract description 43
- 241000589291 Acinetobacter Species 0.000 claims abstract description 38
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- 238000005191 phase separation Methods 0.000 claims description 23
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- XKMRRTOUMJRJIA-UHFFFAOYSA-N ammonia nh3 Chemical compound N.N XKMRRTOUMJRJIA-UHFFFAOYSA-N 0.000 claims description 4
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/28—Anaerobic digestion processes
- C02F3/2806—Anaerobic processes using solid supports for microorganisms
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/28—Anaerobic digestion processes
- C02F3/2846—Anaerobic digestion processes using upflow anaerobic sludge blanket [UASB] reactors
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/28—Anaerobic digestion processes
- C02F3/286—Anaerobic digestion processes including two or more steps
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/34—Biological treatment of water, waste water, or sewage characterised by the microorganisms used
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/10—Inorganic compounds
- C02F2101/16—Nitrogen compounds, e.g. ammonia
- C02F2101/163—Nitrates
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/30—Organic compounds
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Abstract
A device and a method for improving the integrated partial denitrification-anaerobic ammonia oxidation coupling denitrification performance belong to the field of sewage treatment. The bottom of the reactor is part of denitrification granular sludge, the anaerobic ammonia oxidation granular sludge is arranged in the middle of the reactor, and the anaerobic ammonia oxidation granular sludge inside the reactor is uniformly mixed with the embedded particles of the acinetobacter JQ 1004. The method comprises the steps of performing intensive starvation culture on acinetobacter JQ1004 to enable the acinetobacter JQ1004 to grow in a stable period and to secrete more Acyl Homoserine Lactone (AHLs) signal molecules, then placing cultured acinetobacter JQ1004 embedded particles and anaerobic ammonia oxidation particle sludge in the same reaction device, wherein the acinetobacter JQ1004 can consume an organic carbon source to reduce nitrate nitrogen under an anoxic condition, the influence of organic matters on anaerobic ammonia oxidation is reduced, and the acyl homoserine lactone signal molecules generated by the acinetobacter JQ1004 can improve the activity of anaerobic ammonia oxidation bacteria.
Description
Technical Field
The invention belongs to the field of sewage treatment, and particularly relates to a sewage treatment device mainly comprising partial denitrification sludge particles, embedded acinetobacter JQ1004 (China center for microbiological culture Collection center CGMCC 15414) and anaerobic ammonia oxidation sludge particles and an operation strategy thereof.
Background
Anammox, a process in which nitrite is used as an electron acceptor to oxidize ammonia to nitrogen, can reduce the oxygen demand by anammox biological denitrification, and a part of ammonia can be oxidized without consuming oxygen under anoxic conditions, so that it is widely considered as a cost-effective wastewater denitrification process. Anaerobic ammonia oxidation is usually combined with partial denitrification (PN) in order to obtain nitrite as substrate, which theoretically can reduce aeration by 60%, organic carbon by 100%, and sludge production by 90%. The partial denitrification/anammox (PDA) process is considered a promising method to achieve anammox in a sewage treatment plant. Note that 11% of the nitrogen, converted to nitrate by the anammox reaction, inevitably exacerbates the accumulation of nitrate in the wastewater by the presence of nitrite-oxidizing bacteria (NOB). However, the PN/anammox process cannot remove nitrate contained in the wastewater, resulting in relatively poor denitrification efficiency (51-87%). In addition, the Anammox bacterial cell has the characteristics of low yield (0.11gVSS/gNH4+ -N), long generation period (up to 32d), strong dependence on a substrate, weak environmental stress resistance and long reaction starting time caused by difficult gene amplification.
Acinetobacter JQ1004 is a gram-negative strain separated from an activated sludge sample of pilot-scale equipment of BBR (Bacillus Bacteria Bioreactor) of a high tombstone sewage treatment plant in Beijing, and can secrete AHL signal molecules. It is a facultative bacterium capable of utilizing organic carbon source to perform denitrification and reduce nitrate nitrogen under the condition of oxygen deficiency, and its survival condition is that pH is about 7.33 and temperature is about 31.8 deg.C. It has stronger stress resistance to the environment, strong multiplication capacity and wide application prospect in the field of sewage treatment.
Compared with a partial denitrification-anaerobic ammonia oxidation process, the embedding of the acinetobacter JQ1004 in the anaerobic ammonia oxidation region during the stabilization phase has the following advantages:
(1) the acinetobacter JQ1004 can reduce nitrate nitrogen under the anoxic condition, which can further improve the effluent quality of partial denitrification-anaerobic ammonia oxidation.
(2) The secretion of the acinetobacter JQ1004 contains Acyl Homoserine Lactones (AHLs) signal molecules, and the AHLs can promote the expression of anaerobic ammonia oxidation activity genes and are beneficial to the formation of a biological membrane.
(3) The acinetobacter JQ1004 has stronger adaptability to the environment, the JQ1004 in the inoculation stabilization period can also have longer survival time, and the system can run more stably in a sewage biochemical system.
Disclosure of Invention
Because of partial denitrification, anaerobic ammonium oxidation microorganisms are sensitive to environmental changes, such as interference on organic matters or weak resistance to toxic and harmful substances in matrixes, and especially when the partial denitrification coupled anaerobic ammonium oxidation process is applied to mainstream wastewater treatment, the activity of the microorganisms is inhibited by the organic matters in the mainstream wastewater, so that incomplete denitrification is caused.
Therefore, the invention provides a device for inoculating acinetobacter JQ1004 embedded particles in an integrated partial denitrification coupling anaerobic ammonia oxidation area to perform enhanced denitrification and an operation method. The main innovation point is that the Acinetobacter JQ1004 is subjected to enhanced starvation culture, so that the growth of the Acinetobacter JQ1004 is in a stable period and can secrete more Acyl Homoserine Lactone (AHLs) signal molecules, then the cultured Acinetobacter JQ1004 embedded particles and anaerobic ammonia oxidation particle sludge in the stable period are placed in the same reaction device and are uniformly mixed, the Acinetobacter JQ1004 can consume an organic carbon source to reduce nitrate nitrogen under the anoxic condition, the influence of the organic matter on anaerobic ammonia oxidation is reduced, and meanwhile, the Acyl Homoserine Lactone (AHLs) signal molecules generated by the Acinetobacter JQ1004 can also improve the activity of anaerobic ammonia oxidation bacteria. The bottom of the reactor is part of denitrification granular sludge, the anaerobic ammonia oxidation granular sludge is arranged in the middle of the reactor, and the anaerobic ammonia oxidation granular sludge inside the reactor is uniformly mixed with the embedded particles of the acinetobacter JQ 1004.
The utility model provides an improve device of integral type partial denitrification-anaerobic ammonium oxidation coupling process denitrogenation performance which characterized in that includes:
the reactor is a UASB reactor made of organic slope glass, the bottommost part of the reactor is a partial denitrification area, partial denitrification granular sludge is inoculated, polyethylene balls are used as fillers, and the filling ratio is 35%; an anaerobic ammonia oxidation area is arranged above part of the denitrification area, and the part of the denitrification area is separated from the anaerobic ammonia oxidation area by a partition plate which can allow a solution to pass through; inoculating anaerobic ammonium oxidation granular sludge in the anaerobic ammonium oxidation area, adopting pall rings and sponges as fillers, wherein the filling ratio is 30%, and simultaneously adding JQ1004 embedding particles into the anaerobic ammonium oxidation area, wherein the filling ratio is 15%; the top of the reactor is a three-phase separation area, the anaerobic ammonia oxidation area and the three-phase separation area are separated by a partition board through which the solution can pass, and a screen mesh with 18 meshes is paved on the partition board; the three-phase separation area is internally provided with a three-phase separation device and is provided with an overflow groove, the lower part of the three-phase separation area is connected with a water inlet at the bottom of part of the denitrification area through a reflux port and a reflux pump, and the overflow groove is provided with a water outlet for discharging water overflowing from the overflow groove;
the side surface of the upper part of the anaerobic ammonia oxidation area is connected and communicated with a constant-temperature water bath through a circulating outlet, and the constant-temperature water bath is connected and communicated with a circulating inlet on the side surface of the lower part of the denitrification area through a water area circulating pump;
the water tank is connected with a water inlet at the bottom of the partial denitrification area through a water inlet peristaltic pump.
And a pH online electrode and a DO online electrode are arranged in the anaerobic ammonia oxidation area.
The upper side and the lower side of the anaerobic ammonia oxidation area are both provided with sampling ports, and the side of the partial denitrification area is also provided with a sampling port.
The volume ratio of the partial denitrification area to the anaerobic ammonia oxidation area is 1: 2.5.
Feeding water in a continuous flow mode, pumping the artificial simulation wastewater containing nitrate from the bottom of the reactor through a peristaltic pump, and performing partial denitrification to reduce nitrate nitrogen into nitrite nitrogen; then, ammonia nitrogen and nitrite are converted into nitrogen and partial nitrate through anaerobic ammonia oxidation reaction, JQ1004 bacteria can carry out denitrification to reduce the nitrate generated by the reaction of water inflow and anaerobic ammonia oxidation, and AHLs signal molecules secreted by the JQ1004 bacteria can strengthen the anaerobic ammonia oxidation reaction; and finally, in the three-phase separation area, the generated gas is discharged through an exhaust pipe, part of effluent flows back to a water inlet of a partial denitrification area at the bottom of the reactor through a return port in the three-phase separation area, and the overflow water in the overflow groove is discharged through a water outlet.
Wherein, the preparation and culture of the acinetobacter JQ1004 embedded particles:
(1) culturing and strengthening acinetobacter JQ 1004:
1) transferring pure strain JQ1004 preserved in 40% glycerol at-80 deg.C to LB culture medium for enrichment, and activating at 30 deg.C and 120r/min for 12 h;
2) then transferring the culture medium into a denitrification culture medium (100m L culture medium in a 250m L conical flask) with the C/N ratio of 7 at the inoculation amount of 5 percent, and culturing the culture medium for 24 hours at the temperature of 30 ℃ at 180r/min for separation and purification;
3) then, the strain was subjected to starvation culture, and the isolated and purified bacteria were inoculated in a denitrification medium with a C/N ratio of 4 at an inoculum size of 20% for 6 hours, and then inoculated in a denitrification medium with a C/N ratio of 2.5 at an inoculum size of 20% for 6 hours (other culture conditions were the same as the medium composition).
4) Finally, centrifuging the expanded culture solution of the strain (for example, centrifuging 100mL in a high-speed centrifuge at 4000 r/min for 20min), discarding the supernatant, and repeatedly washing with physiological saline for 2-3 times to prepare a JQ1004 suspension of the strain for later use;
(2) preparation of Acinetobacter JQ1004 embedded particles:
1) respectively mixing 10%, 1% and 89% by volume of mixed solution of polyvinyl alcohol (PVA), sodium alginate and deionized water, and heating to completely dissolve the mixed solution to obtain PVA-sodium alginate mixed solution;
2) after the PVA-sodium alginate mixed solution is cooled to room temperature, adding the cultured strains, and uniformly mixing the strains; the concentration of the strain in the mixed solution of PVA and sodium alginate is 15-20 mg.L-1；
3) Then adding boric acid into the solution, continuously stirring the solution to enable the solution to reach a saturated state, cutting the mixed solution into 4mm multiplied by 4mm small cubes after the mixed solution gel is solid, adding the small cubes into 3-5 wt% of calcium chloride solution, and continuously stirring the small cubes during the period of time to prevent the small cubes from being bonded; then crosslinking for 24h at 4 ℃, taking out the small cubes after crosslinking, washing the small cubes with deionized water for 2-3 times, and storing the small cubes in a refrigerator refrigerating chamber at 4 ℃ for later use.
Wherein the culture of the anammox bacteria:
inoculating anaerobic ammonium oxidation granular sludge into a 100L UASB reactor, setting the temperature of the reactor at 28-32 ℃, keeping the pH at 7.1-7.3, and keeping the DO less than 0.4 mg.L-1The artificial wastewater is used for acclimatization culture, and the Hydraulic Retention Time (HRT) of the anaerobic ammonium oxidation bacteria culture is 12 h.
The simulated wastewater comprises the following components: NH (NH)4 +-N (calculated as N) 45-60 mg.L-1、NO2 –-N (calculated as N) 55-80 mg.L-1、KH2PO4 20mg·L-1、MgSO4·7H2O 90mg·L-1、NaHCO3 460mg·L-1、 CaCl2·2H2O 25mg·L-1The content of the trace element solution I is 1ml/L, and the content of the trace element solution II is 1 ml/L;
composition of the trace element solution i: EDTA 5 g.L-1And FeSO4 5g·L-1；
Composition of microelement solution II: EDTA 15 g.L-1、ZnSO4·7H2O 0.43g·L-1、MnCl2·4H2O 0.99g·L-1、CuSO4·5H2O 0.25g·L-1，NaMoO4·2H2O 0.22g·L-1、NiCl2·6H2O 0.19g·L-1And H3BO4 0.014g·L-1。
Wherein, part of denitrifying bacteria are cultured:
inoculating partial denitrification sludge from A/A/O process anoxic tank, such as A/A/O process from sewage treatment plant in Beijing TokyoThe sludge taken back is stood firstly and then supernatant is removed, then scum is filtered by a fine-mesh sieve, and then the sludge is inoculated into an SBR reactor, wherein the MLSS concentration of the inoculated sludge in the reactor is 4740 mg.L-1The MLVSS concentration is 3077 mg.L-1MLVSS/MLSS is 0.65, then the operation is started under the condition of manual water distribution, the temperature is controlled to be about 28 ℃, the pH is kept to be about 7.5, the drainage ratio is 50 percent, and DO is less than 0.5 mg.L-1After long-term operation, the sludge settling performance in the reactor is good, the appearance is in a gray floccule shape, and the accumulation rate of the nitrite is stabilized to be more than 70%.
Wherein, manual water distribution: NO3 -The content of-N (calculated as N) is 65-80 mg.L-1Anhydrous sodium acetate (calculated as COD) 200--1(COD/NO3 --N is 3), NH4 +-N (calculated as N) 20-30 mg.L-1、 KH2PO4 20mg·L-1、MgSO4·7H2O 90mg·L-1、CaCl2·2H2O 25mg·L-1The content of the trace element solution I is 1ml/L, the content of the trace element solution II is 1ml/L,
composition of the trace element solution i: EDTA 5 g.L-1And FeSO4 5g·L-1；
Composition of microelement solution II: EDTA 15 g.L-1、ZnSO4·7H2O 0.43g·L-1、MnCl2·4H2O 0.99g·L-1、CuSO4·5H2O 0.25g·L-1，NaMoO4·2H2O 0.22g·L-1、NiCl2·6H2O 0.19g·L-1And H3BO4 0.014g·L-1。
Operation of the reactor
The reactor is a UASB reactor made of organic slope glass, and water is fed in a continuous flow mode; the bottom of the reactor is a partial denitrification area, partial denitrification granular sludge cultured in the step is inoculated into the partial denitrification area, and the concentration of the inoculated sludge is 3000-4000 mg.L-1Polyethylene is used as a filler, and the filling ratio is 25-35%; followed by a JQ1004 bag containing AcinetobacterThe anaerobic ammonia oxidation area embedded with particles is inoculated with cultured anaerobic ammonia oxidation granular sludge, and the concentration of the inoculated sludge is 2000-4000 mg.L-1And (3) wrapping pall rings and sponge by using flow separation balls made of polypropylene as fillers, wherein the volume ratio of the flow separation balls to the sponge is preferably 1: 1, the filling ratio is 25-30%, and meanwhile, acinetobacter JQ1004 embedding particles are uniformly added, wherein the filling ratio is 10-15%; the top is a three-phase separation area, the areas are separated by a partition plate, and a screen mesh with 18 meshes is laid on the partition plate.
The method for improving partial denitrification-anaerobic ammonia oxidation coupling denitrification performance by adopting the device is characterized by comprising the following steps:
pumping artificial simulation wastewater containing nitrate from the bottom of the reactor through a peristaltic pump, and carrying out partial denitrification to reduce nitrate nitrogen into nitrite nitrogen; then, ammonia nitrogen and nitrite are converted into nitrogen and partial nitrate through anaerobic ammonia oxidation reaction, JQ1004 bacteria can carry out denitrification to reduce the nitrate generated by the reaction of water inflow and anaerobic ammonia oxidation, and AHLs signal molecules secreted by the JQ1004 bacteria can strengthen the anaerobic ammonia oxidation reaction; and finally, in the three-phase separation area, the generated gas is discharged through an exhaust pipe, part of effluent flows back to a water inlet of a partial denitrification area at the bottom of the reactor through a return port in the three-phase separation area, and the overflow water in the overflow groove is discharged through a water outlet.
(1) The reactor start-up period is divided into two phases: in the first stage, the time is 50-60 days, and the Hydraulic Retention Time (HRT) of the UASB reactor is 20-24 h; the duration of the second stage is 50-80 days, the biomass growth in PDA is promoted, the reactor obtains high denitrification rate (NRR), and the inflow speed is increased from 6.25-7.5 L.h-1Increased to 12.5 L.h-1Reducing the HRT from 20-24h to 12 h; the second stage of biofilm formation, stable sludge concentration in the reactor, and COD and NH of effluent4 +-N、NO3 -The N removal effect is stable, and the reactor is started successfully.
(2) Controlling the operating conditions of the reactor:
according to the water flow direction, a partial denitrification area, an anaerobic ammonia oxidation area containing Acinetobacter JQ1004 embedded particles and a three-phase separation area are sequentially arranged; the hydraulic retention time is 12 h.
The reactor temperature is controlled at 28-32 deg.C, pH is 7.3-7.8, and DO is controlled at 0.1-0.4 mg.L-1The sludge reflux ratio is 30-55%.
The partial denitrification/anaerobic ammonia oxidation treatment of the municipal sewage with low carbon-nitrogen ratio has the following advantages:
(1) synchronous denitration, decarbonization and denitrogenation can be completed by the single-stage reactor;
(2) the preposed part is subjected to denitrification to remove organic matters in raw water and provide a matrix for anaerobic ammonium oxidation bacteria;
(3) the acinetobacter JQ1004 can perform denitrification under the anoxic condition and the aerobic condition, and can reduce nitrite nitrogen and nitrate nitrogen under the anoxic condition, so that the effluent quality of partial denitrification-anaerobic ammonia oxidation can be further improved, and advanced treatment is realized.
(4) The secretion of the acinetobacter JQ1004 contains Acyl Homoserine Lactones (AHLs) signal molecules, and the AHLs can promote the expression of anaerobic ammonia oxidation activity genes and are beneficial to the formation of a biological membrane.
Drawings
FIG. 1 is a schematic structural diagram of an embodiment of the invention for improving the integrated partial denitrification-anammox coupled denitrification process;
wherein: 1-manual water distribution tank; 2-a water inlet peristaltic pump; 3-a water inlet; 4-a polyethylene filler; 5-a sampling port; 6, a partition board; 7-reactor constant temperature water bath layer; 8-pall ring and sponge regulating filler; 9-acinetobacter JQ1004 embedded particles; 10-pH on-line electrode; 11-DO online electrode; 12-a three-phase separation unit; 13-water outlet; 14-an overflow tank; 15-reflux port; 16-reflux pump; 17-water bath circulating pump; 18-constant temperature water bath;
the specific implementation method comprises the following steps:
the present invention will be further described with reference to the following examples, but the present invention is not limited to the following examples.
The acinetobacter JQ1004 is preserved in China general microbiological culture Collection center (CGMCC) in 2018, 03 and 06 months, and the preservation number is CGMCC No.15414, and meanwhile, the published patent 201811084608.1 is disclosed.
Example 1
The specific structure is shown in figure 1.
(1) Acinetobacter JQ1004 medium components
LB culture medium NaCl 10.00 g.L-1Tryptone 10.00 g.L-15.00 g.L of yeast extract-1；
Denitrifying Medium (separation and purification Medium) (CH)2COONa)2·6H2O 4.136g·L-1,KNO3 0.72g·L-1,0.565g·L-1K2HPO4 0.565g·L-1,MgSO4·7H2O 0.20g·L-12.50mL of trace elements, trace element solution Na2EDTA 50.00g·L-1,ZnSO4·7H2O 2.20g·L-1,CaCl2 5.50g·L-1, MnCl·4H2O 5.06g·L-1,FeSO4 5.00g·L-1,CuSO4·5H2O 1.57g·L-1,CoCl2·6H2O 1.60g·L-1Both media were sterilized at 121 ℃ for 15min before use, pH by Na2HPO4And NaH2PO4The buffer solution is adjusted to be between 7.0 and 7.3, and 1.5 to 2 percent of agar is required to be added into the solid culture medium.
(2) Culture of anammox bacteria
Artificially simulating domestic sewage to culture bacteria, wherein the water distribution component is NH4 +-N (calculated as N) 45-60 mg.L-1、NO2 –-N (calculated as N) 55-70 mg.L-1、KH2PO4 20mg·L-1、MgSO4·7H2O 90mg·L-1、NaHCO3 460mg·L-1、CaCl2·2H2O 25mg·L-1(ii) a Trace element solution i: 1ml/L, EDTA 5 g.L-1And FeSO4 5g·L-1；
And (3) a trace element solution II: 1ml/L, EDTA 15 g.L-1、ZnSO4·7H2O 0.43g·L-1、MnCl2·4H2O 0.99g·L-1、CuSO4·5H2O 0.25g·L-1，NaMoO4·2H2O 0.22g·L-1、NiCl2·6H2O 0.19g·L-1And H3BO4 0.014g·L-1Hydraulic Retention Time (HRT)12h, temperature 28-32 deg.C, pH 7.1-7.3, and DO less than 0.4 mg.L-1The reactor adopts lower-concentration inflow water and higher HRT at the initial starting stage; after the reactor is started successfully, the water inlet concentration can be increased, and the HRT can be reduced. After the anaerobic ammonium oxidation sludge is cultured, the denitrification rate of the UASB reactor under the stable operation is more than 90 percent, and the sludge particle size is 2-3 mm.
(3) Operation of the UASB reactor
1) Starting the reactor:
the reactor start-up period is divided into two phases. In the first stage (the time is 50-60 days), the UASB reactor is controlled at 6.25-7.5 L.h-1The inflow rate of (d) is operated, resulting in a Hydraulic Retention Time (HRT) of 20-24 h. In the second stage (duration 50-80 days), the biomass growth in the PDA is promoted and a high denitrification rate (NRR) is obtained in the reactor, with an inflow rate from 6.25 to 7.5 l.h-1Increased to 12.5 L.h-1Resulting in a reduction of the HRT from 20-24h to 12 h. The second stage of biofilm formation, stable sludge concentration in the reactor, and COD and NH of effluent4 +-N、 NO3 -The N removal effect is stable, and the reactor is started successfully.
2) Controlling the operating conditions of the reactor:
the reactor is a partial denitrification area, an acinetobacter JQ1004 embedded particle-anaerobic ammonia oxidation area and a three-phase separation area in turn according to the water flow direction as shown in the figure; the effective volume is 150L, the hydraulic retention time is 12h, and the volume ratio of the partial denitrification area to the Acinetobacter JQ1004 embedded particle-anaerobic ammonia oxidation area is 1: 2.5. The reactor temperature is controlled at 28-32 deg.C, pH is 7.3-7.8, and DO is controlled at 0.1-0.4 mg.L-1The sludge reflux ratio is 30-55%.
The components of the reactor water inflow simulation domestic sewage are as follows: NH (NH)4Cl (calculated as N) 45-60 mg.L-1200-250 mg-L anhydrous sodium acetate (calculated by COD)-1，NO3 --N (in terms of N) contentIs 65-80 mg.L-1，NaHCO3Is 460 mg.L-1，CaCl225mg·L-1，KH2PO4 20mg·L-1，MgSO4·7H2O 90mg·L-1。
The feed water flows from the lower part of the reactor, firstly passes through a partial denitrification area: the filling ratio of the polyethylene (phi 25mm multiplied by 10 mm) filler is 25-35%, and the nitrate is converted into nitrite through partial denitrification; secondly, the influent water passes through an acinetobacter JQ1004 embedded particle-anaerobic ammonia oxidation area: sponge filler (the material is hydrophilic polyurethane, 20mm multiplied by 20mm cube) and pall ring filler (25mm multiplied by 3mm) are mixed according to the proportion of 1: 1, coating the mixture by a flow separation ball (the material is polypropylene, phi 100mm), wherein the filling ratio is about 25-30%, embedding a small cube (a cube with the size of 4mm multiplied by 4 mm) by JQ1004, wherein the filling ratio is 10-15%, converting nitrite and ammonia nitrogen into nitrogen and a small amount of nitrate nitrogen, and simultaneously denitrifying the generated nitrate nitrogen into nitrite nitrogen for anaerobic ammonia oxidation reaction by using the acinetobacter JQ 1004; thirdly, the last part of liquid flows back to a part of denitrification area, and the generated gas and the effluent are separated by a three-phase separation device.
In the first stage of the actual operation process, COD and NH of inlet water and outlet water are periodically measured every 3 days4 +-N、NO3 -N content, the effect of removal of the reactor was checked. Adjusting the mass concentration ratio of initial COD to nitrate nitrogen within the range of 2.5-3.5, adjusting a reflux pump to properly increase the reflux ratio to reduce the inflow load, and enabling the effluent NO to be3 -The content is less than 1 mg.L-1(ii) a In the second stage, COD and NH of the effluent are periodically measured every 7 days4 +-N、NO3 -And (4) reducing the reflux ratio to increase the water inlet load so as to keep the nitrogen removal rate of the reactor stable.
4) The denitrification effect of the coupling process is as follows:
through the operation of 140d, the reactor can realize synchronous denitration, decarbonization and denitrogenation, and the treatment effect is stable, COD, NH4 +-N and NO3 -The N removal rate is respectively as high as 86.3%, 95.7% and 98.9%.
Claims (9)
1. The utility model provides an improve device of integral type partial denitrification-anaerobic ammonium oxidation coupling process denitrogenation performance which characterized in that includes:
the reactor is a UASB reactor made of organic slope glass, the bottommost part of the reactor is a partial denitrification area, partial denitrification granular sludge is inoculated, and polyethylene balls are used as fillers; an anaerobic ammonia oxidation area is arranged above part of the denitrification area, and the part of the denitrification area is separated from the anaerobic ammonia oxidation area by a partition plate which can allow a solution to pass through; inoculating anaerobic ammonium oxidation granular sludge in an anaerobic ammonium oxidation area, adopting pall rings and sponges as fillers, wherein the filling ratio is 30%, and simultaneously adding JQ1004 embedding particles into the anaerobic ammonium oxidation area; the top of the reactor is a three-phase separation area, the anaerobic ammonia oxidation area and the three-phase separation area are separated by a partition board through which the solution can pass, and a screen mesh with 18 meshes is paved on the partition board; the three-phase separation area is internally provided with a three-phase separation device and is provided with an overflow groove, the lower part of the three-phase separation area is connected with a water inlet at the bottom of part of the denitrification area through a reflux port and a reflux pump, and the overflow groove is provided with a water outlet for discharging water overflowing from the overflow groove;
the side surface of the upper part of the anaerobic ammonia oxidation area is connected and communicated with a constant-temperature water bath through a circulating outlet, and the constant-temperature water bath is connected and communicated with a circulating inlet on the side surface of the lower part of the denitrification area through a water area circulating pump;
the water tank is connected with a water inlet at the bottom of the partial denitrification area through a water inlet peristaltic pump.
2. The device for improving the denitrification performance of the integrated partial denitrification-anammox coupling process according to claim 1, wherein a pH on-line electrode and a DO on-line electrode are arranged in the anammox area.
3. The apparatus for improving the denitrification performance of the integrated partial denitrification-anammox coupling process in claim 1, wherein the upper side and the lower side of the anammox zone are provided with sampling ports, and the side of the partial denitrification zone is also provided with sampling ports.
4. The device for improving the denitrification performance of the integrated partial denitrification-anaerobic ammonia oxidation coupling process according to claim 1, wherein the volume ratio of the partial denitrification area to the anaerobic ammonia oxidation area is 1: 2.5.
5. The apparatus for improving the denitrification performance of the integrated partial denitrification-anammox coupled process according to claim 1, wherein the preparation and culture of the embedded particles of acinetobacter JQ 1004:
(1) culturing and strengthening acinetobacter JQ 1004:
1) transferring pure strain JQ1004 preserved in 40% glycerol at-80 deg.C to LB culture medium for enrichment, and activating at 30 deg.C and 120r/min for 12 h;
2) then transferring the strain to a denitrification culture medium with a C/N ratio of 7 by using an inoculum size of 5 percent, and culturing the strain at 30 ℃ for 24 hours at 180r/min for separation and purification;
3) then, starvation culture is carried out on the bacterial strain, the separated and purified bacteria are transferred to a denitrification culture medium with a C/N ratio of 4 for culture for 6 hours in an inoculation amount of 20%, and then the bacteria are transferred to a denitrification culture medium with a C/N ratio of 2.5 for culture for 6 hours in an inoculation amount of 20%;
4) finally, taking an expanded culture solution of the strain, centrifuging, removing a supernatant, and repeatedly washing with physiological saline for 2-3 times to prepare a JQ1004 suspension of the strain for later use;
(2) preparation of Acinetobacter JQ1004 embedded particles:
1) respectively mixing 10%, 1% and 89% by volume of mixed solution of polyvinyl alcohol (PVA), sodium alginate and deionized water, and heating to completely dissolve the mixed solution to obtain PVA-sodium alginate mixed solution;
2) after the PVA-sodium alginate mixed solution is cooled to room temperature, adding the cultured strains, and uniformly mixing the strains; the concentration of the strain in the PVA-sodium alginate mixed solution is 15-20 mg.L-1；
3) Then adding boric acid into the solution, continuously stirring the solution to enable the solution to reach a saturated state, cutting the mixed solution into 4mm multiplied by 4mm small cubes after the mixed solution gel is solid, adding the small cubes into 3-5 wt% of calcium chloride solution, and continuously stirring the small cubes during the period of time to prevent the small cubes from being bonded; then crosslinking for 24h at 4 ℃, taking out the small cubes after crosslinking, washing the small cubes with deionized water for 2-3 times, and storing the small cubes in a refrigerator refrigerating chamber at 4 ℃ for later use.
6. The apparatus of claim 1, wherein the culture of anammox bacteria:
inoculating anaerobic ammonium oxidation granular sludge into a 100L UASB reactor, setting the temperature of the reactor at 28-32 ℃, keeping the pH at 7.1-7.3, and keeping the DO less than 0.4 mg.L-1Carrying out acclimatization culture by using simulated wastewater, wherein the Hydraulic Retention Time (HRT) of the anaerobic ammonium oxidation bacteria culture is 12 h;
the simulated wastewater comprises the following components: NH (NH)4 +-N (calculated as N) 45-60 mg.L-1、NO2 –-N (calculated as N) 55-80 mg.L-1、KH2PO4 20mg·L-1、MgSO4·7H2O 90mg·L-1、NaHCO3 460mg·L-1、CaCl2·2H2O 25mg·L-1The content of the trace element solution I is 1ml/L, and the content of the trace element solution II is 1 ml/L;
composition of the trace element solution i: EDTA 5 g.L-1And FeSO4 5g·L-1；
Composition of microelement solution II: EDTA 15 g.L-1、ZnSO4·7H2O 0.43g·L-1、MnCl2·4H2O 0.99g·L-1、CuSO4·5H2O 0.25g·L-1，NaMoO4·2H2O 0.22g·L-1、NiCl2·6H2O 0.19g·L-1And H3BO4 0.014g·L-1；
Wherein, part of denitrifying bacteria are cultured:
process for taking inoculated partial denitrification sludge from A/A/OAn anoxic tank, such as an anoxic tank of A/A/O process from sewage treatment plant of Beijing high tombstone shop, is prepared by standing the taken-back sludge, removing supernatant, filtering out dross by using a fine-mesh sieve, inoculating the scum into an SBR reactor, and inoculating the sludge in the SBR reactor to obtain MLSS with the concentration of 4740 mg.L-1The MLVSS concentration is 3077 mg.L-1MLVSS/MLSS is 0.65, then the operation is started under the condition of manual water distribution, the temperature is controlled to be about 28 ℃, the pH is kept to be about 7.5, the drainage ratio is 50 percent, and DO is less than 0.5 mg.L-1After long-term operation, the sludge settling performance in the reactor is good, the appearance is in a gray floccule shape, and the accumulation rate of the nitrite is stabilized to be more than 70%;
wherein, manual water distribution: NO3 -The content of-N (calculated as N) is 65-80 mg.L-1Anhydrous sodium acetate (calculated as COD) 200--1(COD/NO3 --N is 3), NH4 +-N (calculated as N) 20-30 mg.L-1、KH2PO4 20mg·L-1、MgSO4·7H2O 90mg·L-1、CaCl2·2H2O 25mg·L-1The content of the trace element solution I is 1ml/L, the content of the trace element solution II is 1ml/L,
composition of the trace element solution i: EDTA 5 g.L-1And FeSO4 5g·L-1；
Composition of microelement solution II: EDTA 15 g.L-1、ZnSO4·7H2O 0.43g·L-1、MnCl2·4H2O 0.99g·L-1、CuSO4·5H2O 0.25g·L-1，NaMoO4·2H2O 0.22g·L-1、NiCl2·6H2O 0.19g·L-1And H3BO4 0.014g·L-1。
7. The apparatus for improving the denitrification performance of the integrated partial denitrification-anaerobic ammonia oxidation coupling process according to claim 1, wherein the reactor is an UASB reactor made of organic glass and is fed with water in a continuous flow manner; the bottom of the reactor is a partial denitrification zone to which the seeding step is appliedThe concentration of the inoculated sludge of the cultured partial denitrification granular sludge is 3000-4000 mg.L-1Polyethylene is used as a filler, and the filling ratio is 25-35%; then an anaerobic ammonia oxidation area containing Acinetobacter JQ1004 embedded particles is arranged, cultured anaerobic ammonia oxidation granular sludge is inoculated into the anaerobic ammonia oxidation area, and the concentration of the inoculated sludge is 2000-4000 mg.L-1And (3) wrapping pall rings and sponge by using flow separation balls made of polypropylene as fillers, wherein the volume ratio of the flow separation balls to the sponge is preferably 1: 1, the filling ratio is 25-30%, and meanwhile, acinetobacter JQ1004 embedding particles are uniformly added, wherein the filling ratio is 10-15%; the top is a three-phase separation area, the areas are separated by a partition plate, and a screen mesh with 18 meshes is laid on the partition plate.
8. The method for improving partial denitrification-anaerobic ammonium oxidation coupling denitrification performance by adopting the device of claims 1-7 is characterized by comprising the following steps:
pumping artificial simulation wastewater containing nitrate from the bottom of the reactor through a peristaltic pump, and carrying out partial denitrification to reduce nitrate nitrogen into nitrite nitrogen; then, ammonia nitrogen and nitrite are converted into nitrogen and partial nitrate through anaerobic ammonia oxidation reaction, JQ1004 bacteria can carry out denitrification to reduce the nitrate generated by the reaction of water inflow and anaerobic ammonia oxidation, and AHLs signal molecules secreted by the JQ1004 bacteria can strengthen the anaerobic ammonia oxidation reaction; and finally, in the three-phase separation area, the generated gas is discharged through an exhaust pipe, part of effluent flows back to a water inlet of a partial denitrification area at the bottom of the reactor through a return port in the three-phase separation area, and the overflow water in the overflow groove is discharged through a water outlet.
9. The method of claim 8,
the reactor start-up period is divided into two phases: in the first stage, the time is 50-60 days, and the Hydraulic Retention Time (HRT) of the UASB reactor is 20-24 h; the duration of the second stage is 50-80 days, the biomass growth in PDA is promoted, the reactor obtains high denitrification rate (NRR), and the inflow speed is increased from 6.25-7.5 L.h-1Increased to 12.5 L.h-1Reducing the HRT from 20-24h to 12 h; second stage biofilm formation, reactionThe sludge concentration in the device is stable, and the effluent COD and NH4 +-N、NO3 -The N removal effect is stable, and the reactor is started successfully. Controlling the operating conditions of the reactor:
according to the water flow direction, a partial denitrification area, an anaerobic ammonia oxidation area containing Acinetobacter JQ1004 embedded particles and a three-phase separation area are sequentially arranged; the hydraulic retention time is 12 h;
the reactor temperature is controlled at 28-32 deg.C, pH is 7.3-7.8, and DO is controlled at 0.1-0.4 mg.L-1The sludge reflux ratio is 30-55%.
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112694170A (en) * | 2021-01-07 | 2021-04-23 | 北京工业大学 | Method and device for improving anaerobic ammonia oxidation denitrification effect and operation stability at low temperature |
| CN113184982A (en) * | 2021-04-19 | 2021-07-30 | 西安建筑科技大学 | Strengthening method and device for improving sedimentation performance of activated sludge |
| CN113461162A (en) * | 2021-07-16 | 2021-10-01 | 北京工业大学 | Method and device for improving urban domestic sewage treatment performance of ANAMMOX process |
| CN113735248A (en) * | 2021-08-16 | 2021-12-03 | 天津大学 | Integrated sectional reactor for coupling anaerobic ammonia oxidation and three-dimensional electrode membrane biological process |
| CN117326694A (en) * | 2023-09-22 | 2024-01-02 | 浙江沃乐科技有限公司 | Method for strengthening resistance of sodium dodecyl sulfate in anaerobic ammonia oxidation sludge |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CA2338248A1 (en) * | 1998-07-24 | 2000-02-03 | Paques Bio Systems B.V. | Process for the treatment of waste water containing ammonia |
| CN106430572A (en) * | 2016-11-28 | 2017-02-22 | 北京工业大学 | Method and device for joint denitrifying by denitrification and anaerobic ammonia oxidation embedding particles |
| CN109913382A (en) * | 2018-09-18 | 2019-06-21 | 北京工业大学 | A kind of acinetobacter calcoaceticus and its application |
| CN213895337U (en) * | 2020-10-09 | 2021-08-06 | 北京工业大学 | Device for improving denitrification-anaerobic ammonia oxidation coupling denitrification performance |
-
2020
- 2020-10-09 CN CN202011081238.3A patent/CN112142199B/en active Active
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CA2338248A1 (en) * | 1998-07-24 | 2000-02-03 | Paques Bio Systems B.V. | Process for the treatment of waste water containing ammonia |
| CN106430572A (en) * | 2016-11-28 | 2017-02-22 | 北京工业大学 | Method and device for joint denitrifying by denitrification and anaerobic ammonia oxidation embedding particles |
| CN109913382A (en) * | 2018-09-18 | 2019-06-21 | 北京工业大学 | A kind of acinetobacter calcoaceticus and its application |
| CN213895337U (en) * | 2020-10-09 | 2021-08-06 | 北京工业大学 | Device for improving denitrification-anaerobic ammonia oxidation coupling denitrification performance |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112694170A (en) * | 2021-01-07 | 2021-04-23 | 北京工业大学 | Method and device for improving anaerobic ammonia oxidation denitrification effect and operation stability at low temperature |
| CN112694170B (en) * | 2021-01-07 | 2023-11-17 | 北京工业大学 | Method and device for improving anaerobic ammonia oxidation denitrification effect and operation stability at low temperature |
| CN113184982A (en) * | 2021-04-19 | 2021-07-30 | 西安建筑科技大学 | Strengthening method and device for improving sedimentation performance of activated sludge |
| CN113461162A (en) * | 2021-07-16 | 2021-10-01 | 北京工业大学 | Method and device for improving urban domestic sewage treatment performance of ANAMMOX process |
| CN113461162B (en) * | 2021-07-16 | 2024-04-12 | 北京工业大学 | Method and device for improving urban domestic sewage treatment performance of ANAMMOX process |
| CN113735248A (en) * | 2021-08-16 | 2021-12-03 | 天津大学 | Integrated sectional reactor for coupling anaerobic ammonia oxidation and three-dimensional electrode membrane biological process |
| CN117326694A (en) * | 2023-09-22 | 2024-01-02 | 浙江沃乐科技有限公司 | Method for strengthening resistance of sodium dodecyl sulfate in anaerobic ammonia oxidation sludge |
| CN117326694B (en) * | 2023-09-22 | 2024-05-28 | 浙江沃乐科技有限公司 | Method for strengthening resistance of sodium dodecyl sulfate in anaerobic ammonia oxidation sludge |
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