CN105621806B - A kind of biological coagulation oxidation technology of quick processing kitchen garbage, waste-water - Google Patents
A kind of biological coagulation oxidation technology of quick processing kitchen garbage, waste-water Download PDFInfo
- Publication number
- CN105621806B CN105621806B CN201610051056.9A CN201610051056A CN105621806B CN 105621806 B CN105621806 B CN 105621806B CN 201610051056 A CN201610051056 A CN 201610051056A CN 105621806 B CN105621806 B CN 105621806B
- Authority
- CN
- China
- Prior art keywords
- water
- biological
- waste
- pond
- kitchen garbage
- 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.)
- Active
Links
- 239000002351 wastewater Substances 0.000 title claims abstract description 63
- 238000005345 coagulation Methods 0.000 title claims abstract description 39
- 230000015271 coagulation Effects 0.000 title claims abstract description 39
- 239000010813 municipal solid waste Substances 0.000 title claims abstract description 33
- 230000003647 oxidation Effects 0.000 title claims abstract description 16
- 238000007254 oxidation reaction Methods 0.000 title claims abstract description 16
- 238000005516 engineering process Methods 0.000 title claims abstract description 10
- 239000007788 liquid Substances 0.000 claims abstract description 16
- 239000007787 solid Substances 0.000 claims abstract description 15
- 238000000034 method Methods 0.000 claims abstract description 14
- 238000000926 separation method Methods 0.000 claims abstract description 11
- 239000002893 slag Substances 0.000 claims abstract description 11
- 230000000694 effects Effects 0.000 claims abstract description 9
- 239000003795 chemical substances by application Substances 0.000 claims abstract description 6
- 235000016709 nutrition Nutrition 0.000 claims abstract description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 22
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims description 20
- 238000006243 chemical reaction Methods 0.000 claims description 16
- 230000020477 pH reduction Effects 0.000 claims description 15
- 238000006460 hydrolysis reaction Methods 0.000 claims description 14
- 230000007062 hydrolysis Effects 0.000 claims description 13
- 241000894006 Bacteria Species 0.000 claims description 11
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 10
- 229910052760 oxygen Inorganic materials 0.000 claims description 10
- 239000001301 oxygen Substances 0.000 claims description 10
- 238000004519 manufacturing process Methods 0.000 claims description 8
- 239000010802 sludge Substances 0.000 claims description 8
- 239000000243 solution Substances 0.000 claims description 8
- 238000005191 phase separation Methods 0.000 claims description 5
- 230000001105 regulatory effect Effects 0.000 claims description 5
- 239000002002 slurry Substances 0.000 claims description 5
- XKMRRTOUMJRJIA-UHFFFAOYSA-N ammonia nh3 Chemical compound N.N XKMRRTOUMJRJIA-UHFFFAOYSA-N 0.000 claims description 4
- 239000002068 microbial inoculum Substances 0.000 claims description 4
- 230000009471 action Effects 0.000 claims description 3
- 230000009189 diving Effects 0.000 claims description 3
- 239000003344 environmental pollutant Substances 0.000 claims description 3
- 230000000813 microbial effect Effects 0.000 claims description 3
- 239000011259 mixed solution Substances 0.000 claims description 3
- 230000035764 nutrition Effects 0.000 claims description 3
- 231100000719 pollutant Toxicity 0.000 claims description 3
- 238000001556 precipitation Methods 0.000 claims description 3
- 238000000746 purification Methods 0.000 claims description 3
- 238000011084 recovery Methods 0.000 claims description 3
- 239000006228 supernatant Substances 0.000 claims description 3
- 239000002699 waste material Substances 0.000 claims description 3
- 241000628997 Flos Species 0.000 claims description 2
- 150000001875 compounds Chemical class 0.000 claims description 2
- 238000001914 filtration Methods 0.000 claims description 2
- 238000006396 nitration reaction Methods 0.000 claims description 2
- 239000002245 particle Substances 0.000 claims description 2
- 230000001376 precipitating effect Effects 0.000 claims description 2
- 238000004062 sedimentation Methods 0.000 claims description 2
- KRKNYBCHXYNGOX-UHFFFAOYSA-N citric acid Chemical compound OC(=O)CC(O)(C(O)=O)CC(O)=O KRKNYBCHXYNGOX-UHFFFAOYSA-N 0.000 claims 3
- 244000005700 microbiome Species 0.000 abstract description 8
- 238000000855 fermentation Methods 0.000 abstract description 5
- 239000003895 organic fertilizer Substances 0.000 abstract description 4
- 230000005591 charge neutralization Effects 0.000 abstract description 3
- 230000004151 fermentation Effects 0.000 abstract description 3
- 239000001963 growth medium Substances 0.000 abstract description 2
- 239000008394 flocculating agent Substances 0.000 abstract 1
- 239000002244 precipitate Substances 0.000 abstract 1
- 238000004321 preservation Methods 0.000 description 6
- 230000008569 process Effects 0.000 description 5
- 230000008859 change Effects 0.000 description 3
- 230000018044 dehydration Effects 0.000 description 3
- 238000006297 dehydration reaction Methods 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 235000015097 nutrients Nutrition 0.000 description 3
- 239000003921 oil Substances 0.000 description 3
- 230000001590 oxidative effect Effects 0.000 description 3
- 229910052698 phosphorus Inorganic materials 0.000 description 3
- 241000588841 Acidiphilium sp. Species 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 229910052749 magnesium Inorganic materials 0.000 description 2
- 239000011777 magnesium Substances 0.000 description 2
- 239000005416 organic matter Substances 0.000 description 2
- 238000010248 power generation Methods 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 238000004064 recycling Methods 0.000 description 2
- 235000013311 vegetables Nutrition 0.000 description 2
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- 241000196324 Embryophyta Species 0.000 description 1
- MBMLMWLHJBBADN-UHFFFAOYSA-N Ferrous sulfide Chemical compound [Fe]=S MBMLMWLHJBBADN-UHFFFAOYSA-N 0.000 description 1
- 241000588754 Klebsiella sp. Species 0.000 description 1
- 241000756370 Klebsiella sp. F1 Species 0.000 description 1
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 1
- 241001465754 Metazoa Species 0.000 description 1
- 240000007594 Oryza sativa Species 0.000 description 1
- 235000007164 Oryza sativa Nutrition 0.000 description 1
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 1
- 229920002472 Starch Polymers 0.000 description 1
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- 239000005864 Sulphur Substances 0.000 description 1
- 241000700605 Viruses Species 0.000 description 1
- YUWBVKYVJWNVLE-UHFFFAOYSA-N [N].[P] Chemical compound [N].[P] YUWBVKYVJWNVLE-UHFFFAOYSA-N 0.000 description 1
- 238000010564 aerobic fermentation Methods 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- QGZKDVFQNNGYKY-UHFFFAOYSA-N ammonia Natural products N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 1
- 238000007630 basic procedure Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 238000011953 bioanalysis Methods 0.000 description 1
- 239000003225 biodiesel Substances 0.000 description 1
- 210000000988 bone and bone Anatomy 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- 229920002678 cellulose Polymers 0.000 description 1
- 239000001913 cellulose Substances 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 230000029087 digestion Effects 0.000 description 1
- DNJIEGIFACGWOD-UHFFFAOYSA-N ethanethiol Chemical compound CCS DNJIEGIFACGWOD-UHFFFAOYSA-N 0.000 description 1
- 239000003337 fertilizer Substances 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 239000004519 grease Substances 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Substances [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 150000002632 lipids Chemical class 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 235000013372 meat Nutrition 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 230000002906 microbiologic effect Effects 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- IJGRMHOSHXDMSA-UHFFFAOYSA-N nitrogen Substances N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 1
- 239000011574 phosphorus Substances 0.000 description 1
- 238000003672 processing method Methods 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 102000004169 proteins and genes Human genes 0.000 description 1
- 108090000623 proteins and genes Proteins 0.000 description 1
- 235000009566 rice Nutrition 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 239000008107 starch Substances 0.000 description 1
- 235000019698 starch Nutrition 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000004065 wastewater treatment Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F9/00—Multistage treatment of water, waste water or sewage
-
- 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
- C02F3/348—Biological treatment of water, waste water, or sewage characterised by the microorganisms used characterised by the way or the form in which the microorganisms are added or dosed
-
- 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
- C02F3/02—Aerobic processes
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Microbiology (AREA)
- Biodiversity & Conservation Biology (AREA)
- Separation Of Suspended Particles By Flocculating Agents (AREA)
- Treatment Of Sludge (AREA)
Abstract
The present invention provides a kind of method of quick processing kitchen garbage, waste-water, specially uses biological coagulation oxidation technology, including biological coagulation slag removing system and biological oxidation system.It is characterized in that using specific microorganism flora using kitchen garbage, waste-water is culture medium and adding a small amount of nutritional agents makes it generate a large amount of biological flocculants, it sweeps by effect polymerize with the SS in waste water and precipitates by adsorbing bridge linking effect, charge neutralization and volume, further separation of solid and liquid slagging-off is carried out using solid-liquid separating equipment, for the mud cake isolated by producing organic fertilizer after fermentation, the limpid waste water isolated realizes qualified discharge after further biological oxidation cell processing.
Description
One, technical field
The present invention relates to a kind of waste water treatment process, more particularly to a kind of quick processing kitchen garbage three phase separation waste water
Technique belongs to field of environment engineering technology.
Two, background technology
Kitchen garbage is the sanitary waste that resident is formed during personal consumption, is easily rotted, and stench is distributed, and is passed
Broadcast bacterium and virus.Kitchen garbage includes mainly rice, food remnants, vegetables, vegetable and animals oils, meat bone etc., and chemically ingredient is next
Say there is starch, cellulose, protein, lipid and inorganic salts etc..Since kitchen garbage moisture content is high (70~90%) and organic
Matter content is high, is suitble to be handled using bioanalysis.
The processing method of kitchen garbage is mainly using the method focused on after collecting at present, and majority is using anaerobic fermentation
Form is handled.Its basic procedure is：(1) material feeding that the kitchen garbage come concentrates receipts to be transported to kitchen garbage treatment plant will be collected
Hole；(2) rubbish is subjected to mechanical sorting, recycling removes the abitotic substances such as various plastic products, glass/metal tank；(3) it is crushed
Slurrying, then 70-90 DEG C of thermophilic digestion；(4) above-mentioned slurries are divided by oil using three-phase separator (a kind of Horizontal helical type centrifuge)
Fat part, wastewater fraction and kitchen slag.Oil fraction deep processing is prepared into biodiesel, kitchen slag then can deep processing at feed,
Fertilizer or directly landfill are done after aerobic fermentation or are burned.Three phase separation wastewater fraction then enters methane-generating pit fermentation producing methane, natural pond
Liquid qualified discharge or is discharged into pipe network and enters municipal sewage plant and be further processed using materialization and biochemical treatment.
However, the kitchen garbage, waste-water pH after three phase separation is in acid (pH < 4.5), suspended solids (SS) content is high
(80000-100000mg/L), COD high (majority is in 90000-120000mg/L), in addition, also containing a large amount of ammonia nitrogens, remaining grease
Deng being a kind of extremely intractable high concentrated organic wastewater.Therefore, cause the anaerobic fermentation time very long (usually at 25-30 days), natural pond
Liquid processing is difficult, and the processing of later stage aerobic-anaerobic is still up to nearly 10 days, and it is difficult up to standard to be discharged still, shows coloration depth, COD
Majority needs further the materializations measures such as coagulation air-float to be used to carry out advanced treating in 500mg/L or more.Due to processing time
Long, water is again difficult up to standard, causes structures volume big, and investment is big, and operating cost is high.Therefore, above-mentioned kitchen garbage, waste-water is solved to exist
The problems in biochemical treatment is particularly important.
Three, invention content
The present invention provides a kind of method of quick processing kitchen garbage, waste-water can be fast using biological coagulation oxidation technology
SS, COD in speed removal kitchen garbage, waste-water can significantly shorten later stage anaerobism with the high advantage of processing time is short, removal rate
Natural pond and biochemical treatment time are produced, the water quality of water outlet is greatly improved.
A kind of method of quick processing kitchen garbage, waste-water is using biological coagulation oxidation technology, and feature exists
In using specific microorganism flora using kitchen garbage, waste-water is culture medium and adding a small amount of nutritional agents makes it generate a large amount of biology waddings
Solidifying agent is swept by effect polymerize with the SS in waste water and is precipitated by adsorbing bridge linking effect, charge neutralization and volume, further
Separation of solid and liquid slagging-off is carried out using solid-liquid separating equipment, for the mud cake isolated by producing organic fertilizer after fermentation, that isolates is clear
Clear waste water realizes qualified discharge after the processing of further biological oxidation.
The specific microorganism flora is acidophil Acidiphilium sp.J6 (depositary institutions：China Microbiological bacterium
Kind preservation administration committee common micro-organisms center, preservation address：Datun Road, Chaoyang District, Beijing City Chinese Academy of Sciences microorganism is ground
Study carefully institute, preserves number：CGMCC No.11036, preservation time：On July 2nd, 2015, Classification And Nomenclature：Acidophil
Acidiphilium sp.) and Klebsiella Klebsiella sp.F1 (depositary institutions：Chinese microorganism strain preservation management
Committee's common micro-organisms center, preservation address：Datun Road, Chaoyang District, Beijing City Institute of Microorganism, Academia Sinica, when preservation
Between：Preserve number on April 23rd, 2009：CGMCC No.3032, Classification And Nomenclature：Klebsiella Klebsiella sp.) group
At compound bacteria, the ratio of the two is 1: 1.
A kind for the treatment of process of quick processing kitchen garbage, waste-water, including biological coagulation slag removing system and biological oxygen
Change system.The biological coagulation slag removing system includes regulating reservoir, hydrolysis acidification pool, collection mud sump, microculture pond, life successively
Object coagulation reaction tank is separated by solid-liquid separation facility.The biological oxidation system includes collecting-tank, anaerobic methane production pond, Aerobic-anaerobic life
Change pond, secondary settling tank.
In above-mentioned biological treatment, waste water enters regulating reservoir and water is adjusted, and enters hydrolysis acidification pool afterwards, plays
Cooled down to the kitchen garbage, waste-water of high temperature and automatically adjusts the effect of pH.Kitchen garbage, waste-water is when hydrolysis acidification pool stops
Between be 2~3d, at this point, pH rises to 6 or so, COD removal rates 20% or so.Then, the underflow in hydrolysis acidification pool is given up
Water is pumped into collection mud sump.
The underflow waste water for collecting mud sump is pumped into biological coagulation reaction tank, in the biology coagulation reaction tank, underflow waste water with
Microbial inoculum is sufficiently mixed under the action of blender, and a small amount of microbial nutrition agent is added (mainly by N P and K calcium and magnesium
The nutrients such as iron sulphur and a small amount of organic carbon source composition), providing Institute of Micro-biology using aerating system needs O2, make in microbial inoculum
It is destroyed with mud granule internal junction Heshui in lower underflow waste water, physicochemical property is changed, and improves the dehydration property of underflow waste water
Energy.The residence time, the volume ratio of underflow waste water and bacterium solution was 5 in 1.0~5.0h in biological coagulation reaction tank for underflow waste water:
1~20: 1.
The dewatering of underflow waste water after biological coagulation reaction tank is improved, into solid-liquid separating equipment, such as
Diaphragm chamber-type press filter, is separated by solid-liquid separation, and all recycling becomes semi-oriented mud cake to SS.It, therefore, can because its moisture content is relatively low
It is powdered to be directly broken into, because it contains the nutrients such as abundant organic matter and nitrogen phosphorus, the raw material of production organic fertilizer are can be used as,
It is separated by solid-liquid separation the limpid waste water of gained and enters collecting-tank.At this point, limpid waste water SS contents reach close to 0, COD removal rates
85% or more.
Collecting-tank outlet is connect with anaerobic methane production pond, and methane-generating pit is designed as up-flow anaerobic sludge blanket (UASB), limpid useless
Water residence time in methane-generating pit is 2~3d, after methane recovery purification, for power generation and heat supply.Biogas slurry enters subsequent biochemistry
Unit.
Biochemical unit is made of a series of biochemistry pools, using A2/ O techniques are good by 1 anoxic pond, 1 anaerobic pond and 1
Oxygen pond forms, and setting diving mixer is mixed in the anoxic pond and anaerobic pond, and the aerobic tank uses Roots's wind
Machine is supplied oxygen.Biochemical unit processing time 2d or so.
The dissolved oxygen in anoxic tank a concentration of < 0.4mg/L, the anaerobic pond dissolved oxygen < 0.2mg/L, it is described aerobic
Pond dissolved oxygen concentration >=2.0mg/L.
The muddy water mixed solution that biochemistry pool comes out enters secondary settling tank, carries out mud-water separation, the water quality isolated can carry out up to standard
It discharges, sludge part is back to aerobic tank after precipitation, remaining sludge is carried out into biological coagulation pond at dehydration after concentration
Reason.
The beneficial effects of the invention are as follows：Biological flocculant is generated using specific microorganism flora, in the very short time of 1~5h
It is interior to sweep effect and the SS generation coagulations in kitchen garbage underflow waste water by adsorbing bridge linking effect, charge neutralization and volume, change
It is apt to its dehydration property, after machinery is separated by solid-liquid separation, almost 100% ground removes the pollutants such as SS and 85% or more COD in waste water, subsequently
Biological oxidation (including the anaerobic methane production and biochemical treatment) processing less than 7d need to only be passed through, kitchen garbage, waste-water row up to standard can be made
It puts.Processing time is only processed conventionally 1/5, therefore, can largely save processing investment and operating cost, have good economy
Property.
Four, it illustrates
After the specific implementation mode for having read the present invention with reference to attached drawing, those skilled in the art will be more clearly
Solve various aspects of the invention.Skilled person would appreciate that：These attached drawings are used only for cooperation specific embodiment party
Formula illustrates technical scheme of the present invention, and is not intended to and is construed as limiting to protection scope of the present invention.Wherein,
Fig. 1 is a kind of biological coagulation oxidizing process process flow chart of quick processing kitchen garbage, waste-water of the present invention.
Fig. 2 is a kind of technique stream of one embodiment of quick processing kitchen garbage, waste-water biology coagulation oxidizing process of the present invention
Cheng Tu.
Five, specific implementation mode
1 the present invention is described in further detail below in conjunction with the accompanying drawings.
A kind of biological coagulation oxidation technology of quick processing kitchen garbage, waste-water, including biological coagulation slag removing system and biology
Oxidative system.Biological coagulation slag removing system is poly- including regulating reservoir, hydrolysis acidification pool, collection mud sump, microculture pond, biology successively
Heavy reaction tank, the special slag remover of biological coagulation.The biological oxidation system includes collecting-tank, anaerobic methane production pond, Aerobic-anaerobic
Biochemistry pool, secondary settling tank.
Each pollutant concentration of kitchen garbage, waste-water is as follows：COD 108000mg/L, SS 97500mg/L, ammonia nitrogen 300mg/L.
In above-mentioned biological treatment, kitchen garbage, waste-water 10m after three phase separation3Water quality water is adjusted into regulating reservoir
Amount, subsequently into dischargeable capacity 30m3Hydrolysis acidification pool.Kitchen garbage, waste-water is 2.5d in the hydrolysis acidification pool residence time, is passed through
After hydrolysis acidification, pH rises to 6.05, COD and is reduced to 81200mg/L, and temperature is reduced to room temperature (28 DEG C).Then, by hydrolysis acid
The underflow waste water changed in pond is pumped into collection mud sump.
Collect 10m in mud sump3It is 15m that underflow waste water after hydrolysis acidification, which enters pool capacity,3Biological coagulation reaction tank,
In the biology coagulation reaction tank, by underflow wastewater volume and bacterium solution volume than 10: 1 addition bacterium solution 1m3, underflow waste water and microorganism
Bacterium solution is sufficiently mixed under the action of blender, be added account for underflow wastewater volume 0.5% microbial nutrition agent (mainly by
The nutrients such as N P and K Ca, Mg and Fe sulphur and a small amount of organic carbon source composition) 50kg, providing Institute of Micro-biology using aerating system needs O2,
Underflow waste particles object (i.e. sludge) internal junction Heshui is destroyed under microbial inoculum effect, and physicochemical property changes, and improves
Dewatering, underflow waste water residence time in biological coagulation reaction tank is 3.0h.
Underflow waste water after biological coagulation reaction tank enters the special Chamber Type Diaphragm Filter Press of biological coagulation and carries out solid-liquid
Separation, for solid therein by press filtration at semi-oriented mud cake, the moisture content of mud cake is 58%, after being directly crushed, can be used as production
The raw material of organic fertilizer are separated by solid-liquid separation the limpid waste water of gained and enter collecting-tank.At this point, limpid waste water SS contents are close to 0,
A concentration of 15600mg/L of COD, compared with raw water before processing, COD removal rates reach 85.6%.
Collecting-tank water outlet is connected with the water inlet of up-flow anaerobic sludge blanket (UASB), and limpid waste water is held in methane-generating pit
It is 2d to stay the time, and after methane recovery purification, for power generation and heat supply, biogas slurry enters subsequent biochemical unit.At this point, biogas slurry COD
Only 1820mg/L, ammonia nitrogen 216mg/L.
Biochemical unit is made of a series of biochemistry pools, using A2/ O techniques are 3m by 1 dischargeable capacity3Anoxic pond, 1
3m3Anaerobic pond and 1 15m3Aerobic tank composition.Aerobic tank mixed liquor is partly refluxed to anoxic pond, realizes that nitration denitrification is de-
Nitrogen, waterpower residence time is total 2d in biochemical unit, and wherein the waterpower residence time of aerobic tank is 1.5d.Anoxic pond and anaerobism
Diving mixer is arranged in pond to be mixed, aerobic tank is supplied oxygen using roots blower, ensures that dissolved oxygen concentration is not less than
2mg/L。
Aerobic tank muddy water mixed solution enters secondary settling tank and carries out precipitation water outlet, sedimentation time 4h.Supernatant is discharged through floss hole
Liquid, in supernatant ammonia-nitrogen content be 4.7mg/L, SS 28mg/L, COD 58mg/L, total phosphorus 0.2mg/L.
Precipitating sludge is back to the processing that biological coagulation reaction tank carries out next group.
Claims (1)
1. the biological coagulation oxidation technology of a kind of biological coagulation oxidation technology of quick processing kitchen garbage, waste-water, use includes life
Object coagulation slag removing system and biological oxidation system, it is characterised in that：The biology coagulation slag removing system includes regulating reservoir, water successively
Solve acidification pool, collection mud sump, microculture pond, biological coagulation reaction tank, the special slag remover of biological coagulation；The biological oxidation
System includes collecting-tank, anaerobic methane production pond, Aerobic-anaerobic biochemistry pool, secondary settling tank；Kitchen garbage, waste-water enters tune after three phase separation
Water quality and quantity is adjusted in section pond, and each pollutant concentration of kitchen garbage, waste-water is as follows：COD108000mg/L,
SS97500mg/L, ammonia nitrogen 300mg/L, subsequently into hydrolysis acidification pool, kitchen garbage, waste-water is in the hydrolysis acidification pool residence time
2.5d, after hydrolysis acidification, pH rises to 6.05, COD and is reduced to 81200mg/L, and temperature is reduced to room temperature, then, by water
Underflow waste water in solution acidification pool is pumped into collection mud sump, and collecting the underflow waste water in mud sump after hydrolysis acidification, to enter biological coagulation anti-
Ying Chi, in biological coagulation reaction tank, by underflow wastewater volume and bacterium solution volume than 10: 1 addition bacterium solutions, underflow waste water and micro- life
Object bacterium solution is sufficiently mixed under the action of blender, and the microbial nutrition agent for accounting for underflow wastewater volume 0.5% is added, and is used
Aerating system, which provides Institute of Micro-biology, needs O2, underflow waste particles object internal junction Heshui is destroyed under microbial inoculum effect, dense
Pulp waste water residence time in biological coagulation reaction tank is 3.0h, and the underflow waste water after biological coagulation reaction tank carries out solid-liquid
Separation, solid therein, at semi-oriented mud cake, are separated by solid-liquid separation the limpid waste water of gained and are entered collecting-tank by press filtration；Micro- life
Object is the compound bacteria that acidophil Acidiphiliumsp.J6 and citric acid K1ebsiellasp.F1 are formed in 1: 1 ratio；Collection
The water outlet in pond is connected with anaerobic methane production pond, and methane-generating pit is designed as up-flow anaerobic sludge blanket, and limpid waste water is in methane-generating pit
Residence time is 2d, and after methane recovery purification, biogas slurry enters subsequent biochemical unit, and biochemical unit uses A2/O techniques, described
Biochemical unit is aerobic-anaerobic biological pond, is made of 1 anoxic pond, 1 anaerobic pond and 1 aerobic tank, aerobic tank mixed liquor
It is partly refluxed to anoxic pond, realizes nitration denitrification denitrogenation, waterpower residence time is total 2d, wherein aerobic tank in biochemical unit
Waterpower residence time be 1.5d, setting diving mixer is mixed in anoxic pond and anaerobic pond, and aerobic tank uses Roots's wind
Machine is supplied oxygen, and ensures that dissolved oxygen concentration is not less than 2mg/L；Aerobic tank muddy water mixed solution enters secondary settling tank and carries out precipitation water outlet,
Sedimentation time is 4h, and supernatant is discharged through floss hole, and precipitating sludge is back to the place that biological coagulation reaction tank carries out next group
Reason.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610051056.9A CN105621806B (en) | 2016-01-22 | 2016-01-22 | A kind of biological coagulation oxidation technology of quick processing kitchen garbage, waste-water |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610051056.9A CN105621806B (en) | 2016-01-22 | 2016-01-22 | A kind of biological coagulation oxidation technology of quick processing kitchen garbage, waste-water |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN105621806A CN105621806A (en) | 2016-06-01 |
| CN105621806B true CN105621806B (en) | 2018-10-30 |
Family
ID=56037213
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610051056.9A Active CN105621806B (en) | 2016-01-22 | 2016-01-22 | A kind of biological coagulation oxidation technology of quick processing kitchen garbage, waste-water |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN105621806B (en) |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108359611B (en) * | 2018-02-12 | 2020-12-18 | 南京贝克特环保科技有限公司 | Biotransformation method for rapidly transforming waste animals and tissues of large-scale farm |
| CN112718803A (en) * | 2020-12-18 | 2021-04-30 | 天津市工业微生物研究所有限公司 | On-site rapid kitchen waste treatment process |
| CN113716795A (en) * | 2021-08-13 | 2021-11-30 | 深圳市利赛环保科技有限公司 | Kitchen waste biogas slurry dehydration process |
| CN115572014A (en) * | 2022-10-27 | 2023-01-06 | 大连爱德摩设备制造有限公司 | On-line strengthening treatment method and system for microorganisms in refractory sewage |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1631820A (en) * | 2005-01-14 | 2005-06-29 | 北京大学 | Combined treatment method and system for landfill leachate |
| CN104839427A (en) * | 2015-05-15 | 2015-08-19 | 吴伟浩 | Method for preparing animal drinking water or feed mixing water from kitchen waste water |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE69534296T2 (en) * | 1994-07-29 | 2006-04-27 | Chiron Corp. (N.D.Ges.D. Staates Delaware), Emeryville | Secreted E1 / E2 complex of hepatitis C virus obtained from C-terminally truncated polypeptides E1 and E2 |
-
2016
- 2016-01-22 CN CN201610051056.9A patent/CN105621806B/en active Active
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1631820A (en) * | 2005-01-14 | 2005-06-29 | 北京大学 | Combined treatment method and system for landfill leachate |
| CN104839427A (en) * | 2015-05-15 | 2015-08-19 | 吴伟浩 | Method for preparing animal drinking water or feed mixing water from kitchen waste water |
Also Published As
| Publication number | Publication date |
|---|---|
| CN105621806A (en) | 2016-06-01 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| Wu et al. | Pollution control technologies for the treatment of palm oil mill effluent (POME) through end-of-pipe processes | |
| Ahmed et al. | Production of biogas and performance evaluation of existing treatment processes in palm oil mill effluent (POME) | |
| CN106219871B (en) | Livestock and poultry breeding wastewater treatment method | |
| CN102227382B (en) | Method and apparatus for integratedly treating domestic wastewater and organic garbage | |
| CN102531295B (en) | Method for jointly treating different garbage | |
| CN109513722A (en) | A kind of restaurant garbage treating system and processing method | |
| Hassan et al. | Treatment of palm oil wastewaters | |
| CN109455874A (en) | A kind of changing food waste into resources recovery and processing system | |
| CN103524001B (en) | Treatment method for high fat food processing wastewater | |
| CN101337838A (en) | Combined anaerobic fermentation process for organic solid wastes | |
| CN101921809A (en) | Kitchen waste disposal method | |
| CN103613245B (en) | Treatment process for waste water in neuropeptide product production | |
| CN105621806B (en) | A kind of biological coagulation oxidation technology of quick processing kitchen garbage, waste-water | |
| CN102010104A (en) | Method for treating riboflavin fermentation waste water | |
| CN202519137U (en) | Combined treatment device of waste incineration field percolate | |
| CN111807660A (en) | Resourceful treatment system and method for kitchen waste, straw and municipal sludge | |
| CN105502802B (en) | A kind of method of quick treatment scale piggery waste waste water | |
| CN114850170A (en) | Kitchen garbage resource and energy recovery pollution-reducing carbon-reducing cooperative device | |
| CN112808738A (en) | Method for preparing carbon source by utilizing kitchen waste | |
| CN102500608A (en) | Anaerobic treatment process for high-concentration kitchen waste | |
| CN105293842A (en) | Process for treating fecal sewage in culture pond | |
| Stephenson et al. | Evaluation of startup and operation of four anaerobic processes treating a synthetic meat waste | |
| CN105110557A (en) | Method for treating kitchen wastewater through flocculation flotation-oil production microorganisms | |
| CN203112650U (en) | Kitchen waste wastewater treatment system | |
| CN105502852B (en) | A kind of method of quick processing garbage burning factory landfill leachate |
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: 20191030 Address after: Weigang Xuanwu District of Nanjing Jiangsu province 210095 No. 1 Patentee after: NANJING AGRICULTURAL University Address before: No. 9 Zhongshan Science Park by the road in Liuhe District of Nanjing City, Jiangsu province 211505 Patentee before: NANJING BEIKETE ENVIRONMENTAL PROTECTION TECHNOLOGY CO.,LTD. |
|
| TR01 | Transfer of patent right | ||
| EE01 | Entry into force of recordation of patent licensing contract | ||
| EE01 | Entry into force of recordation of patent licensing contract |
Application publication date: 20160601 Assignee: EUROPE ASIA HUADU (YIXING) ENVIRONMENTAL PROTECTION Co.,Ltd. Assignor: NANJING AGRICULTURAL University Contract record no.: X2020980001183 Denomination of invention: Biological coagulation oxidation process for rapidly treating kitchen waste wastewater Granted publication date: 20181030 License type: Exclusive License Record date: 20200331 |
|
| EC01 | Cancellation of recordation of patent licensing contract | ||
| EC01 | Cancellation of recordation of patent licensing contract |
Assignee: EUROPE ASIA HUADU (YIXING) ENVIRONMENTAL PROTECTION CO.,LTD. Assignor: NANJING AGRICULTURAL University Contract record no.: X2020980001183 Date of cancellation: 20230414 |
|
| EE01 | Entry into force of recordation of patent licensing contract | ||
| EE01 | Entry into force of recordation of patent licensing contract |
Application publication date: 20160601 Assignee: NANJING BEIKETE ENVIRONMENTAL PROTECTION TECHNOLOGY CO.,LTD. Assignor: NANJING AGRICULTURAL University Contract record no.: X2023980046863 Denomination of invention: A Rapid Biological Agglomeration and Oxidation Process for Treating Kitchen Waste Wastewater Granted publication date: 20181030 License type: Common License Record date: 20231115 |