CN106830556A - A kind of swine manure wastewater resource utilization method - Google Patents
A kind of swine manure wastewater resource utilization method Download PDFInfo
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- CN106830556A CN106830556A CN201710153655.6A CN201710153655A CN106830556A CN 106830556 A CN106830556 A CN 106830556A CN 201710153655 A CN201710153655 A CN 201710153655A CN 106830556 A CN106830556 A CN 106830556A
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- swine manure
- manure wastewater
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- flocculation reaction
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- 210000003608 fece Anatomy 0.000 title claims abstract description 96
- 239000010871 livestock manure Substances 0.000 title claims abstract description 86
- 241000282898 Sus scrofa Species 0.000 title claims abstract description 85
- 239000002351 wastewater Substances 0.000 title claims abstract description 85
- 238000000034 method Methods 0.000 title claims abstract description 18
- 238000005189 flocculation Methods 0.000 claims abstract description 66
- 230000016615 flocculation Effects 0.000 claims abstract description 66
- 238000006243 chemical reaction Methods 0.000 claims abstract description 62
- 239000000706 filtrate Substances 0.000 claims abstract description 61
- 239000007787 solid Substances 0.000 claims abstract description 61
- 239000007788 liquid Substances 0.000 claims abstract description 43
- 238000000926 separation method Methods 0.000 claims abstract description 28
- 230000001186 cumulative effect Effects 0.000 claims abstract description 25
- 244000144972 livestock Species 0.000 claims abstract description 22
- 244000144977 poultry Species 0.000 claims abstract description 21
- 239000010865 sewage Substances 0.000 claims abstract description 21
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 claims abstract description 16
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims abstract description 12
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 12
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 claims abstract description 10
- 238000003860 storage Methods 0.000 claims abstract description 9
- ODINCKMPIJJUCX-UHFFFAOYSA-N Calcium oxide Chemical compound [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 claims abstract description 8
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 claims abstract description 8
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 claims abstract description 8
- 229920002401 polyacrylamide Polymers 0.000 claims abstract description 6
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 claims abstract description 5
- 239000000203 mixture Substances 0.000 claims abstract description 5
- 229910017604 nitric acid Inorganic materials 0.000 claims abstract description 5
- 235000008733 Citrus aurantifolia Nutrition 0.000 claims abstract description 4
- 235000011941 Tilia x europaea Nutrition 0.000 claims abstract description 4
- 239000000292 calcium oxide Substances 0.000 claims abstract description 4
- 235000012255 calcium oxide Nutrition 0.000 claims abstract description 4
- 239000004571 lime Substances 0.000 claims abstract description 4
- 239000011780 sodium chloride Substances 0.000 claims abstract description 4
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims description 20
- 230000003647 oxidation Effects 0.000 claims description 17
- 238000007254 oxidation reaction Methods 0.000 claims description 17
- 239000011790 ferrous sulphate Substances 0.000 claims description 12
- 235000003891 ferrous sulphate Nutrition 0.000 claims description 12
- BAUYGSIQEAFULO-UHFFFAOYSA-L iron(2+) sulfate (anhydrous) Chemical compound [Fe+2].[O-]S([O-])(=O)=O BAUYGSIQEAFULO-UHFFFAOYSA-L 0.000 claims description 12
- 229910000359 iron(II) sulfate Inorganic materials 0.000 claims description 12
- 239000003795 chemical substances by application Substances 0.000 claims description 11
- RBTARNINKXHZNM-UHFFFAOYSA-K iron trichloride Chemical compound Cl[Fe](Cl)Cl RBTARNINKXHZNM-UHFFFAOYSA-K 0.000 claims description 11
- 229910052742 iron Inorganic materials 0.000 claims description 10
- 241001465754 Metazoa Species 0.000 claims description 9
- 238000010564 aerobic fermentation Methods 0.000 claims description 9
- 230000002550 fecal effect Effects 0.000 claims description 9
- 238000011081 inoculation Methods 0.000 claims description 9
- 239000003895 organic fertilizer Substances 0.000 claims description 9
- 241000252185 Cobitidae Species 0.000 claims description 8
- 241000276701 Oreochromis mossambicus Species 0.000 claims description 8
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 8
- 230000001877 deodorizing effect Effects 0.000 claims description 8
- 239000008394 flocculating agent Substances 0.000 claims description 8
- 229910052760 oxygen Inorganic materials 0.000 claims description 8
- 239000001301 oxygen Substances 0.000 claims description 8
- 150000001875 compounds Chemical class 0.000 claims description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 2
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 claims description 2
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 claims description 2
- 229910052799 carbon Inorganic materials 0.000 claims description 2
- 229910052708 sodium Inorganic materials 0.000 claims description 2
- 239000011734 sodium Substances 0.000 claims description 2
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 abstract description 4
- 230000008901 benefit Effects 0.000 abstract description 3
- 229910000029 sodium carbonate Inorganic materials 0.000 abstract description 2
- 239000002781 deodorant agent Substances 0.000 abstract 1
- 238000003912 environmental pollution Methods 0.000 abstract 1
- AHLWZBVXSWOPPL-RGYGYFBISA-N 20-deoxy-20-oxophorbol 12-myristate 13-acetate Chemical compound C([C@]1(O)C(=O)C(C)=C[C@H]1[C@@]1(O)[C@H](C)[C@H]2OC(=O)CCCCCCCCCCCCC)C(C=O)=C[C@H]1[C@H]1[C@]2(OC(C)=O)C1(C)C AHLWZBVXSWOPPL-RGYGYFBISA-N 0.000 description 6
- 241001602688 Pama Species 0.000 description 6
- 239000000956 alloy Substances 0.000 description 4
- 229910045601 alloy Inorganic materials 0.000 description 4
- 230000009286 beneficial effect Effects 0.000 description 3
- 241000251468 Actinopterygii Species 0.000 description 2
- 241000196324 Embryophyta Species 0.000 description 2
- 210000000170 cell membrane Anatomy 0.000 description 2
- 201000010099 disease Diseases 0.000 description 2
- 208000037265 diseases, disorders, signs and symptoms Diseases 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 238000000855 fermentation Methods 0.000 description 2
- 235000013305 food Nutrition 0.000 description 2
- 239000012528 membrane Substances 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- HRPVXLWXLXDGHG-UHFFFAOYSA-N Acrylamide Chemical compound NC(=O)C=C HRPVXLWXLXDGHG-UHFFFAOYSA-N 0.000 description 1
- 208000024827 Alzheimer disease Diseases 0.000 description 1
- 241000272814 Anser sp. Species 0.000 description 1
- 241000894006 Bacteria Species 0.000 description 1
- 241000283690 Bos taurus Species 0.000 description 1
- FGUUSXIOTUKUDN-IBGZPJMESA-N C1(=CC=CC=C1)N1C2=C(NC([C@H](C1)NC=1OC(=NN=1)C1=CC=CC=C1)=O)C=CC=C2 Chemical compound C1(=CC=CC=C1)N1C2=C(NC([C@H](C1)NC=1OC(=NN=1)C1=CC=CC=C1)=O)C=CC=C2 FGUUSXIOTUKUDN-IBGZPJMESA-N 0.000 description 1
- 244000025254 Cannabis sativa Species 0.000 description 1
- 208000024172 Cardiovascular disease Diseases 0.000 description 1
- 208000001132 Osteoporosis Diseases 0.000 description 1
- 241001494479 Pecora Species 0.000 description 1
- 206010039966 Senile dementia Diseases 0.000 description 1
- 239000004411 aluminium Substances 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- 210000004958 brain cell Anatomy 0.000 description 1
- 238000009395 breeding Methods 0.000 description 1
- 230000001488 breeding effect Effects 0.000 description 1
- 230000001684 chronic effect Effects 0.000 description 1
- 125000004122 cyclic group Chemical group 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 239000004459 forage Substances 0.000 description 1
- 230000012010 growth Effects 0.000 description 1
- 230000011132 hemopoiesis Effects 0.000 description 1
- 210000003734 kidney Anatomy 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 230000008635 plant growth Effects 0.000 description 1
- 231100000614 poison Toxicity 0.000 description 1
- 230000007096 poisonous effect Effects 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
- 239000002689 soil Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000011573 trace mineral Substances 0.000 description 1
- 235000013619 trace mineral Nutrition 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
-
- A—HUMAN NECESSITIES
- A01—AGRICULTURE; FORESTRY; ANIMAL HUSBANDRY; HUNTING; TRAPPING; FISHING
- A01K—ANIMAL HUSBANDRY; AVICULTURE; APICULTURE; PISCICULTURE; FISHING; REARING OR BREEDING ANIMALS, NOT OTHERWISE PROVIDED FOR; NEW BREEDS OF ANIMALS
- A01K61/00—Culture of aquatic animals
-
- C—CHEMISTRY; METALLURGY
- C05—FERTILISERS; MANUFACTURE THEREOF
- C05F—ORGANIC FERTILISERS NOT COVERED BY SUBCLASSES C05B, C05C, e.g. FERTILISERS FROM WASTE OR REFUSE
- C05F3/00—Fertilisers from human or animal excrements, e.g. manure
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
- C02F1/5236—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using inorganic agents
- C02F1/5245—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using inorganic agents using basic salts, e.g. of aluminium and iron
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
- C02F1/54—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using organic material
- C02F1/56—Macromolecular compounds
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/20—Nature of the water, waste water, sewage or sludge to be treated from animal husbandry
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2209/00—Controlling or monitoring parameters in water treatment
- C02F2209/08—Chemical Oxygen Demand [COD]; Biological Oxygen Demand [BOD]
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2303/00—Specific treatment goals
- C02F2303/02—Odour removal or prevention of malodour
-
- 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
-
- 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
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A40/00—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
- Y02A40/10—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in agriculture
- Y02A40/20—Fertilizers of biological origin, e.g. guano or fertilizers made from animal corpses
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A40/00—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
- Y02A40/80—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in fisheries management
- Y02A40/81—Aquaculture, e.g. of fish
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Environmental Sciences (AREA)
- Organic Chemistry (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Engineering & Computer Science (AREA)
- Marine Sciences & Fisheries (AREA)
- Zoology (AREA)
- Animal Husbandry (AREA)
- Biodiversity & Conservation Biology (AREA)
- Hydrology & Water Resources (AREA)
- Separation Of Suspended Particles By Flocculating Agents (AREA)
Abstract
The invention discloses a kind of swine manure wastewater resource utilization method,The swine manure wastewater that livestock and poultry farm is discharged first is carried out first time separation of solid and liquid by the method,Filtrate is delivered to storage pond after separation,Addition biological deodorant,Then the swine manure wastewater filter pump deposited in pond is transported to flocculation reaction groove,By volume percent,Cumulative volume based on sewage filtrate in flocculation reaction groove,0.02% to 0.50% sulfuric acid is added successively,Hydrochloric acid,Nitric acid,NaOH,Sodium carbonate,Hydrogen peroxide,Quick lime,One or more mixtures in white lime or sodium chloride,0.50% to 0.62% ferric flocculant,0.002% to 0.1% flocculant aid polyacrylamide,After the completion of being reacted in flocculation reaction groove,Second separation of solid and liquid is carried out to swine manure wastewater,Obtain solid of the water content less than 80wt%.The method does not result in secondary environmental pollution in processing procedure, and has the advantages that process is simple, comprehensive utilization ratio are high.
Description
Technical field
The present invention relates to cyclic utilization of waste field, a kind of swine manure wastewater resource utilization method is related specifically to.
Background technology
At present, the treatment to swine manure wastewater common are：Anaerobic fermentation, directly fertilising.Anaerobic fermentation investment is big, account for
Big with land area, the equipment used is considerably complicated, complex operation, and scale is hardly formed for general raiser；Directly
Connect using cultivation fecal sewage, crop will be produced to hinder root, disease, crop smothering etc. and negatively affected, and comprehensive utilization ratio is low.
The treatment of present cultivation excrement does not only exist low above-mentioned utilization rate, complex process, invests big shortcoming, also one
Individual very significant defect：Treatment swine manure wastewater commonly uses AlSnSi alloy at present, because aluminium is chronic poisonous substance, from food
Chain can be put aside in the tissue such as people's brain cell after entering human body, can trigger senile dementia, cardiovascular disease, osteoporosis, kidney work(
Can be disorderly, Duo Zhong Stubborn diseases are waited, secondary pollution can be caused using AlSnSi alloy, the resource for also having blocked feces of livestock and poultry is used.
Therefore how to obtain that a kind of process is simple, comprehensive utilization ratio be high, a kind of green recyclable swine manure wastewater money
Source Application way turns into today's society problem demanding prompt solution.
The content of the invention
It is an object of the invention to provide a kind of process is simple, comprehensive utilization ratio be high, green recyclable feces of livestock and poultry is dirty
Water resource Application way.
In order to realize the purpose, using following technical scheme：
A kind of swine manure wastewater resource utilization method, comprises the following steps：
A. swine manure wastewater livestock and poultry farm discharged, feeding solid-liquid separating machine carries out first time separation of solid and liquid, leaches
Solid, for producing biological organic fertilizer, obtains the weight content of solid in swine manure wastewater filtrate for 0.3wt% extremely in addition
5wt%；
B. the swine manure wastewater filtrate for first time separation of solid and liquid in step a being obtained is delivered to storage pond, adds biological deodorizing
Agent；
C. the swine manure wastewater filter pump deposited in pond is transported to flocculation reaction groove, by volume percent, adds base
Sulfuric acid, hydrochloric acid, nitric acid, NaOH, the carbon of swine manure wastewater filtrate cumulative volume 0.02% to 0.50% in flocculation reaction groove
One or more mixtures in sour sodium, hydrogen peroxide, quick lime, white lime or sodium chloride；
D. volume percent is pressed, to the swine manure wastewater filtrate addition of flocculation reaction groove based on animal dung in flocculation reaction groove
Just the ferric flocculant of sewage filtrate cumulative volume 0.50% to 0.62%；
E. volume percent is pressed, to the swine manure wastewater filtrate addition of flocculation reaction groove based on livestock and poultry in flocculation reaction groove
The flocculant aid polyacrylamide of fecal sewage filtrate cumulative volume 0.002% to 0.1%；
F. after the completion of being reacted in flocculation reaction groove, second separation of solid and liquid is carried out to swine manure wastewater, obtains water content and be less than
The solid of 80wt%, gained liquid inoculation biological flora, enters oxidation pond, carries out aerobic fermentation to solids content less than 0.1wt%,
COD COD<50mg/L, biochemical oxygen demand (BOD) BOD<50 mg/L, deliver Tilapia mossambica, and loach to oxidation pond is raised.
Preferably, iron-based flocculating agent addition is between the 0.54% to 0.58% of processed sewage volume in the step b.
It is highly preferred that the iron-based flocculating agent preferably is selected from ferrous sulfate, one kind in polyiron sulfate or ferric trichloride or two
Plant thing mixed above.
It is particularly preferred that the iron-based flocculating agent is the compound of ferrous sulfate and ferric trichloride, its volume ratio is 1：10-
10：1.
Highly preferred iron-based flocculating agent is the compound of ferrous sulfate and ferric trichloride in the present invention, and its volume ratio is 1：
4-1：6.
The flocculant aid polyacrylamide is poly- selected from PAMA, PAMC or nonionic
One or more of acrylamide.
The water of oxidation pond discharge, can be used to pour yellow hayland in the step f, and pond sludge can be used as hayland
Base manure；The herbage of output, can the herbivorous livestock such as rear cattle, sheep, goose, by being inoculated with beneficial microbe strain, it is possible to use bacterium
Kind of growth is fast, the characteristics of to environmental condition strong adaptability, is beneficial to the control of service condition, makes sewage disposal completely up to standard.Through
The swine manure wastewater of present invention treatment is crossed, can be used to breed fish, irrigated pasture growing and rinse livestock and poultry farm, accomplish that circulation makes
With realizing zero release of pollutant.
Relative to prior art, the invention has the advantages that：
1. operating cost is low, convenient management and operation is simple, swine manure wastewater can complete resource utilize, economic benefit
It is good, can be received by numerous raisers；
2. national environmental protection is met, agricultural, high-tech three industries policy and agriculture future thrust can be promoted the use of all
Livestock and poultry breeding industry night soil-treatment, meet the target that national waste processes industrialization；
3. AlSnSi alloy is replaced with iron-based flocculating agent, it is to avoid the secondary pollution that AlSnSi alloy is caused, iron is hematopoiesis unit
Element, is also the trace element required for animal and plant growth, even if it is also useful and harmless to human body to flow into food chain；
4. one kind or several in sulfuric acid, hydrochloric acid, nitric acid, NaOH, sodium carbonate, hydrogen peroxide, quick lime, white lime or sodium chloride
Kind of mixture plays the role of preferably to abolish cell membrane to the subparticle in sewage, during it first to add flocculation reaction groove
Filtrate can be conducive to flocculation reaction；
5. ferric flocculant is used, and is aided with polyacrylamide as flocculant aid, the two is used cooperatively, settle the effect phase of flocculation
The efficiency for using cooperatively to other flocculants and flocculant aid is more preferable.
Specific embodiment
The present invention is further illustrated below by specific embodiment, following examples are the present invention preferably embodiment party
Formula, but embodiments of the present invention are not limited by following embodiments.
Embodiment 1
A. swine manure wastewater livestock and poultry farm discharged, feeding solid-liquid separating machine carries out first time separation of solid and liquid, leaches
Solid, for producing biological organic fertilizer, the weight content that solid in swine manure wastewater filtrate is obtained in addition is 0.32wt%；
B. the swine manure wastewater filtrate for first time separation of solid and liquid in step a being obtained is delivered to storage pond, adds biological deodorizing
Agent；
C. the swine manure wastewater filter pump deposited in pond is transported to flocculation reaction groove, by volume percent, adds base
The sulfuric acid of swine manure wastewater filtrate cumulative volume 0.03% in flocculation reaction groove；
D. volume percent is pressed, to the swine manure wastewater filtrate addition of flocculation reaction groove based on animal dung in flocculation reaction groove
Just the ferric flocculant of sewage filtrate cumulative volume 0.52%：Ferrous sulfate；
E. volume percent is pressed, to the swine manure wastewater filtrate addition of flocculation reaction groove based on livestock and poultry in flocculation reaction groove
The flocculant aid of fecal sewage filtrate cumulative volume 0.002%：PAMC；
F. after the completion of being reacted in flocculation reaction groove, second separation of solid and liquid is carried out to swine manure wastewater, obtaining water content is
The solid of 77wt%, gained liquid inoculation biological flora, enters oxidation pond, carries out aerobic fermentation to solids content less than 0.1wt%,
COD COD<50mg/L, biochemical oxygen demand (BOD) BOD<50 mg/L, deliver Tilapia mossambica, and loach to oxidation pond is raised.
Embodiment 2
A. swine manure wastewater livestock and poultry farm discharged, feeding solid-liquid separating machine carries out first time separation of solid and liquid, leaches
Solid, for producing biological organic fertilizer, the weight content that solid in swine manure wastewater filtrate is obtained in addition is 4wt%；
B. the swine manure wastewater filtrate for first time separation of solid and liquid in step a being obtained is delivered to storage pond, adds biological deodorizing
Agent；
C. the swine manure wastewater filter pump deposited in pond is transported to flocculation reaction groove, by volume percent, adds base
The hydrochloric acid of swine manure wastewater filtrate cumulative volume 0.40% in flocculation reaction groove；
D. volume percent is pressed, to the swine manure wastewater filtrate addition of flocculation reaction groove based on animal dung in flocculation reaction groove
Just the ferric flocculant of sewage filtrate cumulative volume 0.56%：Ferric flocculant is made up of ferrous sulfate and ferric trichloride, and volume ratio is 1：9；
E. volume percent is pressed, to the swine manure wastewater filtrate addition of flocculation reaction groove based on livestock and poultry in flocculation reaction groove
The flocculant aid of fecal sewage filtrate cumulative volume 0.05%:PAMA；
F. after the completion of being reacted in flocculation reaction groove, second separation of solid and liquid is carried out to swine manure wastewater, obtaining water content is
The solid of 55wt%, gained liquid inoculation biological flora, enters oxidation pond, carries out aerobic fermentation to solids content less than 0.1wt%,
COD COD<50mg/L, biochemical oxygen demand (BOD) BOD<50 mg/L, deliver Tilapia mossambica, and loach to oxidation pond is raised.
Embodiment 3
A. swine manure wastewater livestock and poultry farm discharged, feeding solid-liquid separating machine carries out first time separation of solid and liquid, leaches
Solid, for producing biological organic fertilizer, the weight content that solid in swine manure wastewater filtrate is obtained in addition is 4wt%；
B. the swine manure wastewater filtrate for first time separation of solid and liquid in step a being obtained is delivered to storage pond, adds biological deodorizing
Agent；
C. the swine manure wastewater filter pump deposited in pond is transported to flocculation reaction groove, by volume percent, adds base
The nitric acid of swine manure wastewater filtrate cumulative volume 0.16% in flocculation reaction groove；
D. volume percent is pressed, to the swine manure wastewater filtrate addition of flocculation reaction groove based on animal dung in flocculation reaction groove
Just the ferric flocculant of sewage filtrate cumulative volume 0.54%：Ferric flocculant is made up of ferrous sulfate and ferric trichloride, and volume ratio is 9：1；
E. volume percent is pressed, to the swine manure wastewater filtrate addition of flocculation reaction groove based on livestock and poultry in flocculation reaction groove
The flocculant aid of fecal sewage filtrate cumulative volume 0.08%:PAMA；
F. after the completion of being reacted in flocculation reaction groove, second separation of solid and liquid is carried out to swine manure wastewater, obtaining water content is
The solid of 55wt%, gained liquid inoculation biological flora, enters oxidation pond, carries out aerobic fermentation to solids content less than 0.1wt%,
COD COD<50mg/L, biochemical oxygen demand (BOD) BOD<50 mg/L, deliver Tilapia mossambica, and loach to oxidation pond is raised.
Embodiment 4
A. swine manure wastewater livestock and poultry farm discharged, feeding solid-liquid separating machine carries out first time separation of solid and liquid, leaches
Solid, for producing biological organic fertilizer, the weight content that solid in swine manure wastewater filtrate is obtained in addition is 2wt%；
B. the swine manure wastewater filtrate for first time separation of solid and liquid in step a being obtained is delivered to storage pond, adds biological deodorizing
Agent；
C. the swine manure wastewater filter pump deposited in pond is transported to flocculation reaction groove, by volume percent, adds base
The hydrochloric acid of swine manure wastewater filtrate cumulative volume 0.4% in flocculation reaction groove；
D. volume percent is pressed, to the swine manure wastewater filtrate addition of flocculation reaction groove based on animal dung in flocculation reaction groove
Just the ferric flocculant of sewage filtrate cumulative volume 0.58%：Ferric flocculant is made up of ferrous sulfate and ferric trichloride, and volume ratio is 1：4；
E. volume percent is pressed, to the swine manure wastewater filtrate addition of flocculation reaction groove based on livestock and poultry in flocculation reaction groove
The flocculant aid of fecal sewage filtrate cumulative volume 0.004%:PAMA；
F. after the completion of being reacted in flocculation reaction groove, second separation of solid and liquid is carried out to swine manure wastewater, obtaining water content is
The solid of 55wt%, gained liquid inoculation biological flora, enters oxidation pond, carries out aerobic fermentation to solids content less than 0.1wt%,
COD COD<50mg/L, biochemical oxygen demand (BOD) BOD<50 mg/L, deliver Tilapia mossambica, and loach to oxidation pond is raised.
Embodiment 5
A. swine manure wastewater livestock and poultry farm discharged, feeding solid-liquid separating machine carries out first time separation of solid and liquid, leaches
Solid, for producing biological organic fertilizer, the weight content that solid in swine manure wastewater filtrate is obtained in addition is 2wt%；
B. the swine manure wastewater filtrate for first time separation of solid and liquid in step a being obtained is delivered to storage pond, adds biological deodorizing
Agent；
C. the swine manure wastewater filter pump deposited in pond is transported to flocculation reaction groove, by volume percent, adds base
The hydrochloric acid of swine manure wastewater filtrate cumulative volume 0.4% in flocculation reaction groove；
D. volume percent is pressed, to the swine manure wastewater filtrate addition of flocculation reaction groove based on animal dung in flocculation reaction groove
Just the ferric flocculant of sewage filtrate cumulative volume 0.56%：Ferric flocculant is made up of ferrous sulfate and ferric trichloride, and volume ratio is 1：5；
E. volume percent is pressed, to the swine manure wastewater filtrate addition of flocculation reaction groove based on livestock and poultry in flocculation reaction groove
The flocculant aid of fecal sewage filtrate cumulative volume 0.026%:PAMA；
F. after the completion of being reacted in flocculation reaction groove, second separation of solid and liquid is carried out to swine manure wastewater, obtaining water content is
The solid of 55wt%, gained liquid inoculation biological flora, enters oxidation pond, carries out aerobic fermentation to solids content less than 0.1wt%,
COD COD<50mg/L, biochemical oxygen demand (BOD) BOD<50 mg/L, deliver Tilapia mossambica, and loach to oxidation pond is raised.
Embodiment 6
A. swine manure wastewater livestock and poultry farm discharged, feeding solid-liquid separating machine carries out first time separation of solid and liquid, leaches
Solid, for producing biological organic fertilizer, the weight content that solid in swine manure wastewater filtrate is obtained in addition is 2wt%；
B. the swine manure wastewater filtrate for first time separation of solid and liquid in step a being obtained is delivered to storage pond, adds biological deodorizing
Agent；
C. the swine manure wastewater filter pump deposited in pond is transported to flocculation reaction groove, by volume percent, adds base
The hydrochloric acid of swine manure wastewater filtrate cumulative volume 0.4% in flocculation reaction groove；
D. volume percent is pressed, to the swine manure wastewater filtrate addition of flocculation reaction groove based on animal dung in flocculation reaction groove
Just the ferric flocculant of sewage filtrate cumulative volume 0.56%：Ferric flocculant is made up of ferrous sulfate and ferric trichloride, and volume ratio is 1：6；
E. volume percent is pressed, to the swine manure wastewater filtrate addition of flocculation reaction groove based on livestock and poultry in flocculation reaction groove
The flocculant aid of fecal sewage filtrate cumulative volume 0.055%:PAMA；
F. after the completion of being reacted in flocculation reaction groove, second separation of solid and liquid is carried out to swine manure wastewater, obtaining water content is
The solid of 55wt%, gained liquid inoculation biological flora, enters oxidation pond, carries out aerobic fermentation to solids content less than 0.1wt%,
COD COD<50mg/L, biochemical oxygen demand (BOD) BOD<50 mg/L, deliver Tilapia mossambica, and loach to oxidation pond is raised.
Flocculation tank is equipped with two-layer stirring slurry, eight meters of maximum stirring linear speed degree per second, toward wadding in above-described embodiment 1-5 steps b
Cell membrane is sequentially added in solidifying groove and abolish agent, iron-based flocculating agent, flocculant aid polyacrylamide so that in swine manure wastewater
Subparticle is condensed into siderotil flower, is easy to subsequent processing.
The swine manure wastewater flocculated in above-described embodiment 1-5 steps f carries out the through membrane pump input plate and frame filter press
Secondary separation of solid and liquid, membrane pump operating pressure be six atmospheric pressure, the solid of plate and frame filter press institute output, water content is in 80wt%
Hereinafter, as production biological organic fertilizer, the filtrate of plate and frame filter press institute output after inoculation beneficial microbe strain, then is passed through
Aerobic fermentation reacts, and can be used to breed fish, planting forage grass, rinses plant.
Claims (5)
1. a kind of swine manure wastewater resource utilization method, it is characterised in that comprise the following steps：
A. swine manure wastewater livestock and poultry farm discharged, feeding solid-liquid separating machine carries out first time separation of solid and liquid, leaches
Solid, for producing biological organic fertilizer, obtains the weight content of solid in swine manure wastewater filtrate for 0.3wt% extremely in addition
5wt%；
B. the swine manure wastewater filtrate for first time separation of solid and liquid in step a being obtained is delivered to storage pond, adds biological deodorizing
Agent；
C. the swine manure wastewater filter pump deposited in pond is transported to flocculation reaction groove, by volume percent, adds base
Sulfuric acid, hydrochloric acid, nitric acid, NaOH, the carbon of swine manure wastewater filtrate cumulative volume 0.02% to 0.50% in flocculation reaction groove
One or more mixtures in sour sodium, hydrogen peroxide, quick lime, white lime or sodium chloride；
D. volume percent is pressed, to the swine manure wastewater filtrate addition of flocculation reaction groove based on animal dung in flocculation reaction groove
Just the ferric flocculant of sewage filtrate cumulative volume 0.50% to 0.62%；
E. volume percent is pressed, to the swine manure wastewater filtrate addition of flocculation reaction groove based on livestock and poultry in flocculation reaction groove
The flocculant aid polyacrylamide of fecal sewage filtrate cumulative volume 0.002% to 0.1%；
F. after the completion of being reacted in flocculation reaction groove, second separation of solid and liquid is carried out to swine manure wastewater, obtains water content and be less than
The solid of 80wt%, gained liquid inoculation biological flora, enters oxidation pond, carries out aerobic fermentation to solids content less than 0.1wt%,
COD COD<50mg/L, biochemical oxygen demand (BOD) BOD<50 mg/L, deliver Tilapia mossambica, and loach to oxidation pond is raised.
2. a kind of swine manure wastewater resources circulation method according to claim 1, it is characterised in that in the step b
Iron-based flocculating agent addition is the 0.54%-0.58% of swine manure wastewater filtrate in flocculation reaction groove.
3. a kind of swine manure wastewater resources circulation method according to claim 2, it is characterised in that the iron system flocculation
Agent is selected from one or more mixtures in ferrous sulfate, polyiron sulfate or ferric trichloride.
4. a kind of swine manure wastewater resources circulation method according to claim 3, it is characterised in that the iron system flocculation
Agent is the compound of ferrous sulfate and ferric trichloride, and its volume ratio is 1：10-10：1.
5. a kind of swine manure wastewater resources circulation method according to claim 4, it is characterised in that the ferrous sulfate
It is 1 with the volume ratio of ferric trichloride：4-1：6.
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Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107399796A (en) * | 2017-09-20 | 2017-11-28 | 青岛亚通达铁路设备有限公司 | A kind of processing method of liquid dung |
| CN107954546A (en) * | 2017-11-24 | 2018-04-24 | 天峨县平昌生态农业有限公司 | A kind of processing method for cultivating family's poultry waster water |
| CN109205931A (en) * | 2018-09-17 | 2019-01-15 | 温州科技职业学院 | A kind for the treatment of of swine wastewater and circulation reuse method |
| CN109851094A (en) * | 2019-01-29 | 2019-06-07 | 江西英特科胜动保科技有限公司 | A kind of animal wastes water dirt method for separating and processing |
| CN110642485A (en) * | 2019-10-30 | 2020-01-03 | 冯强 | Method for treating animal excrement |
| CN111004060A (en) * | 2019-12-31 | 2020-04-14 | 陕西天仁雪农业科技有限公司 | Method for producing organic fertilizer from excrement in septic tank |
| CN113480346A (en) * | 2021-08-18 | 2021-10-08 | 安徽坤健生物科技有限公司 | Biological treatment process for preparing organic biofertilizer from chicken manure |
| CN114230090A (en) * | 2021-12-03 | 2022-03-25 | 兴源环境科技股份有限公司 | Method for treating livestock and poultry manure |
| CN114763290A (en) * | 2021-01-12 | 2022-07-19 | 天津国丰民裕农业科技有限公司 | Dirty processing system of excrement |
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| CN116583492A (en) * | 2020-07-15 | 2023-08-11 | 轨迹方案Ipco有限责任公司 | Improved methods and compositions for treating manure |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101654318A (en) * | 2009-09-08 | 2010-02-24 | 北京昊业怡生科技有限公司 | Excrement centralized processing method |
| CN102745866A (en) * | 2012-07-19 | 2012-10-24 | 北京世纪国瑞环境工程技术有限公司 | Non-hazardous recycling treatment method for excrement |
| CN105152416A (en) * | 2015-10-14 | 2015-12-16 | 周智 | Method for treating liquid dung in pig farms |
-
2017
- 2017-03-15 CN CN201710153655.6A patent/CN106830556A/en active Pending
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101654318A (en) * | 2009-09-08 | 2010-02-24 | 北京昊业怡生科技有限公司 | Excrement centralized processing method |
| CN102745866A (en) * | 2012-07-19 | 2012-10-24 | 北京世纪国瑞环境工程技术有限公司 | Non-hazardous recycling treatment method for excrement |
| CN105152416A (en) * | 2015-10-14 | 2015-12-16 | 周智 | Method for treating liquid dung in pig farms |
Cited By (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107399796A (en) * | 2017-09-20 | 2017-11-28 | 青岛亚通达铁路设备有限公司 | A kind of processing method of liquid dung |
| CN107954546A (en) * | 2017-11-24 | 2018-04-24 | 天峨县平昌生态农业有限公司 | A kind of processing method for cultivating family's poultry waster water |
| CN109205931A (en) * | 2018-09-17 | 2019-01-15 | 温州科技职业学院 | A kind for the treatment of of swine wastewater and circulation reuse method |
| CN109851094A (en) * | 2019-01-29 | 2019-06-07 | 江西英特科胜动保科技有限公司 | A kind of animal wastes water dirt method for separating and processing |
| CN110642485A (en) * | 2019-10-30 | 2020-01-03 | 冯强 | Method for treating animal excrement |
| CN111004060A (en) * | 2019-12-31 | 2020-04-14 | 陕西天仁雪农业科技有限公司 | Method for producing organic fertilizer from excrement in septic tank |
| CN116583492A (en) * | 2020-07-15 | 2023-08-11 | 轨迹方案Ipco有限责任公司 | Improved methods and compositions for treating manure |
| CN114763290A (en) * | 2021-01-12 | 2022-07-19 | 天津国丰民裕农业科技有限公司 | Dirty processing system of excrement |
| CN113480346A (en) * | 2021-08-18 | 2021-10-08 | 安徽坤健生物科技有限公司 | Biological treatment process for preparing organic biofertilizer from chicken manure |
| CN114230090A (en) * | 2021-12-03 | 2022-03-25 | 兴源环境科技股份有限公司 | Method for treating livestock and poultry manure |
| CN114230090B (en) * | 2021-12-03 | 2023-11-14 | 兴源环境科技股份有限公司 | Livestock manure treatment method |
| CN115520948A (en) * | 2022-10-21 | 2022-12-27 | 湘潭县湘为农牧有限公司 | Method for treating pig raising excrement sewage |
| CN115520948B (en) * | 2022-10-21 | 2024-04-16 | 湘潭县湘为农牧有限公司 | Pig raising fecal sewage treatment method |
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