CN109052842A - A kind of novel domestic sewage of villages and small towns treatment process - Google Patents
A kind of novel domestic sewage of villages and small towns treatment process Download PDFInfo
- Publication number
- CN109052842A CN109052842A CN201811009871.4A CN201811009871A CN109052842A CN 109052842 A CN109052842 A CN 109052842A CN 201811009871 A CN201811009871 A CN 201811009871A CN 109052842 A CN109052842 A CN 109052842A
- Authority
- CN
- China
- Prior art keywords
- sewage
- villages
- treatment process
- domestic sewage
- small towns
- 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.)
- Pending
Links
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
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
- B01D53/86—Catalytic processes
- B01D53/8678—Removing components of undefined structure
- B01D53/8687—Organic components
-
- C—CHEMISTRY; METALLURGY
- C05—FERTILISERS; MANUFACTURE THEREOF
- C05D—INORGANIC FERTILISERS NOT COVERED BY SUBCLASSES C05B, C05C; FERTILISERS PRODUCING CARBON DIOXIDE
- C05D3/00—Calcareous fertilisers
- C05D3/02—Calcareous fertilisers from limestone, calcium carbonate, calcium hydrate, slaked lime, calcium oxide, waste calcium products
-
- C—CHEMISTRY; METALLURGY
- C05—FERTILISERS; MANUFACTURE THEREOF
- C05F—ORGANIC FERTILISERS NOT COVERED BY SUBCLASSES C05B, C05C, e.g. FERTILISERS FROM WASTE OR REFUSE
- C05F7/00—Fertilisers from waste water, sewage sludge, sea slime, ooze or similar masses
-
- C—CHEMISTRY; METALLURGY
- C05—FERTILISERS; MANUFACTURE THEREOF
- C05G—MIXTURES OF FERTILISERS COVERED INDIVIDUALLY BY DIFFERENT SUBCLASSES OF CLASS C05; MIXTURES OF ONE OR MORE FERTILISERS WITH MATERIALS NOT HAVING A SPECIFIC FERTILISING ACTIVITY, e.g. PESTICIDES, SOIL-CONDITIONERS, WETTING AGENTS; FERTILISERS CHARACTERISED BY THEIR FORM
- C05G3/00—Mixtures of one or more fertilisers with additives not having a specially fertilising activity
- C05G3/80—Soil conditioners
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2255/00—Catalysts
- B01D2255/20—Metals or compounds thereof
- B01D2255/206—Rare earth metals
- B01D2255/2063—Lanthanum
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2255/00—Catalysts
- B01D2255/20—Metals or compounds thereof
- B01D2255/207—Transition metals
- B01D2255/20707—Titanium
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2255/00—Catalysts
- B01D2255/20—Metals or compounds thereof
- B01D2255/207—Transition metals
- B01D2255/20769—Molybdenum
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2255/00—Catalysts
- B01D2255/30—Silica
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2255/00—Catalysts
- B01D2255/80—Type of catalytic reaction
- B01D2255/802—Photocatalytic
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2257/00—Components to be removed
- B01D2257/70—Organic compounds not provided for in groups B01D2257/00 - B01D2257/602
- B01D2257/708—Volatile organic compounds V.O.C.'s
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2258/00—Sources of waste gases
- B01D2258/02—Other waste gases
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2259/00—Type of treatment
- B01D2259/80—Employing electric, magnetic, electromagnetic or wave energy, or particle radiation
-
- 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
- C02F1/001—Processes for the treatment of water whereby the filtration technique is of importance
-
- 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
- C02F1/66—Treatment of water, waste water, or sewage by neutralisation; pH adjustment
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2301/00—General aspects of water treatment
- C02F2301/08—Multistage treatments, e.g. repetition of the same process step under different conditions
-
- 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
-
- 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
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel
Abstract
The present invention discloses a kind of novel domestic sewage of villages and small towns treatment process, includes the following steps: that (a) sanitary sewage pre-processes;(b) pretreated purifying domestic sewage processing;(c) sludge generated in purifying domestic sewage treatment process farmyard manure production stations are transported to handle.The present invention is suitable for the sanitary sewage disposal of new village and novel small town, and can comprehensively utilize the waste generated in sewage disposal process, improves resource utilization, is conducive to build sustainable developability society.
Description
Technical field
The present invention relates to sanitary sewage disposal fields, are related specifically to a kind of novel domestic sewage of villages and small towns treatment process.
Background technique
Novel urbanization makes the living standard of resident be greatly improved, and resident is made to live more poly-
Collection reduces the old residence discarded in original villages and small towns, is conducive to the centralizedly supply of the resources such as electricity, water, reduces pipeline or route
It is laid with, while being conducive to the centralized recovery processing to house refuse.But novel villages and small towns need to be exactly that life is dirty in face of a problem
How the processing of water efficiently reduces pollution of the sanitary sewage to environment.Due to the daily life of new village and novel small town
Sewage quantum of output living is less, builds biggish Sewage Disposal not only higher cost, but also the processing capacity of Sewage Disposal will
It is idle to have larger a part, and Miniature Sewage Farm processing capacity can not fully meet requirement, and exist dirty
Waste after water process is difficult to comprehensively utilize, and causes certain wasting of resources.
Summary of the invention
In view of this, being suitable for novel the purpose of the present invention is to provide a kind of novel domestic sewage of villages and small towns treatment process
The sanitary sewage disposal in rural area and novel small town, and the waste generated in sewage disposal process can be comprehensively utilized, it mentions
High resource utilization is conducive to build sustainable developability society.
In order to solve the above technical problems, The technical solution adopted by the invention is as follows: a kind of novel domestic sewage of villages and small towns processing
Technique includes the following steps:
(a) sanitary sewage pre-processes;
(b) pretreated purifying domestic sewage processing;
(c) sludge generated in purifying domestic sewage treatment process farmyard manure production stations are transported to handle:
Sludge, coal ash, white lime and the chicken manure dried are uniformly mixed obtained A according to weight ratio 4:2.5:0.7:1.8
Stalk, leaf, sheep dung, fertile soil and biogas residue are uniformly mixed obtained B material according to weight ratio 5:2:1.5:1:2.5:1.8 by material, will
A material, B material and water are put into decomposed pond according to weight ratio 2:3:0.4, closed decomposed 20-35 days, decomposed fertilizer are made, inside fertile heap
Temperature is 60-70 DEG C.
Above-mentioned novel domestic sewage of villages and small towns treatment process sets up sewage collecting station in community, in sewage in step (a)
Gathering station carries out primary filtration to community's life's sewage, filters out the solids that the grain diameter in sanitary sewage is greater than 3cm, and will
Solids is obtained by filtration and is transported to methane-generating pit progress ferment preparation of sludge gas, then by the sewage of filtered sanitary sewage pressurization pumping
Treating stations carry out purified treatment.
The solids being obtained by filtration and partial size are 30-70 microns more by above-mentioned novel domestic sewage of villages and small towns treatment process
Methane-generating pit is transported to after the mixing of hole calcium carbonate.
Above-mentioned novel domestic sewage of villages and small towns treatment process, is provided with volatile organic matter Concentration Testing in sewage collecting station
Device, the volatile organic matter concentration detection apparatus and the processing monitoring center communication connection of novel domestic sewage of villages and small towns.
Above-mentioned novel domestic sewage of villages and small towns treatment process is equipped with volatile organic matter photocatalytic degradation in sewage collecting station and fills
Set, be equipped with photochemical catalyst in volatile organic matter photocatalytic degradation device, photochemical catalyst by titanium dioxide, porous silica,
Molybdenum oxide and lanthana are formed according to weight ratio 3:10:0.6:0.4.
Above-mentioned novel domestic sewage of villages and small towns treatment process, in step (b), pretreated sanitary sewage clean water treatment packet
Include following steps:
(b-1) pretreated sanitary sewage is successively subjected to cyclic activated sludge system purified treatment;
(b-2) sanitary sewage after cyclic activated sludge system purified treatment is handled by the ecosystem pool.
Above-mentioned novel domestic sewage of villages and small towns treatment process carries out in step (b-1) by pretreated sanitary sewage
The pH value of pretreated sanitary sewage is adjusted before cyclic activated sludge system processing with sulfuric acid and sodium hydroxide;Pretreated life is dirty
Water carries out generation sludge in cyclic activated sludge system treatment process and is transported to farmyard manure production stations as the decomposed fertile raw material of production.
Above-mentioned novel domestic sewage of villages and small towns treatment process, sludge is transported to after farmyard manure production stations and dries granulation, and dirt is made
Mud particle, partial size are 60-150 microns.
Above-mentioned novel domestic sewage of villages and small towns treatment process, the mud granule are 120-150 microns, the mud granule table
Face is equipped with the groove that depth is 20-30 microns;When preparing A material, the partial size of white lime is 10-20 microns, and partial size is 10-12 microns
White lime, the white lime that partial size is 13-17 microns and partial size be 18-20 microns the weight ratio of white lime be 1:3:8.
Above-mentioned novel domestic sewage of villages and small towns treatment process specifically comprises the following steps: when preparation A expects
(c-1) by mud granule and white lime mixing granulation, the C that partial size is 135-170 microns is made and expects, specific method
Are as follows: while agitating to white lime surface continuous water spray mist 5-10 minutes in spray chamber, wet white lime particle is made, it will
It is to be mixed 20-30 minutes to expect up to C in 70-85% stirred tank that white lime particle and mud granule, which are moistened, in humidity;
(c-2) by mud granule and white lime mixing granulation, the D that partial size is 80-120 microns is made and expects, method particularly includes:
While agitating to chicken manure particle surface continuous water spray mist 10-15 minutes in spray chamber, wet chicken manure particle is made, it will be wet
Moistening chicken manure particle and flyash in humidity is to be mixed 15-20 minutes to expect up to D in 70-85% stirred tank;
(c-3) C material and D material are mixed 10-15 minutes in a stirring kettle and are expected up to A.
Beneficial effects of the present invention are as follows:
1. the waste generated during sanitary sewage disposal is used for the preparation of decomposed fertilizer by the present invention, money is effectively increased
The utilization rate in source.
It is used 2. being mixed using the decomposed fertilizer prepared in the present invention with farmyard manure as base fertilizer, fertility is lasting, can effectively change
It is apt to the hardened situation of hardened soil, is used continuously 2 years, soil hardening situation disappears substantially.
3. the present invention combines sanitary sewage disposal and the ecological agriculture, not only can solve after sanitary sewage preliminary purification such as
It is imported in nature water environment in the case where where to Natural Water environmental impact minimization, while the weather in novel villages and small towns can also be improved
Environment.
Specific embodiment
In order to illustrate more clearly of the present invention, below with reference to preferred embodiment, the present invention is described further.Ability
Field technique personnel should be appreciated that following specifically described content is illustrative and be not restrictive, this should not be limited with this
The protection scope of invention.
The novel domestic sewage of villages and small towns treatment process of the present invention, includes the following steps:
(a) sanitary sewage pre-processes.
When building the community in novel villages and small towns, sewage collecting station is set up in community, and at sewage collecting station to community's life
Sewage carries out primary filtration, filters out the solids that the grain diameter in sanitary sewage is greater than 3cm, and the solids that will be obtained by filtration
Methane-generating pit, which is transported to, after mixing with the porous calcium carbonate that partial size is 30-70 microns carries out ferment preparation of sludge gas, it then will be filtered
The Sewage Disposal of sanitary sewage pressurization pumping carries out purified treatment.
Dirt is diffused into view of when carrying out sewage collecting by sewage collecting station, the volatile organic matter in sewage can volatilize
It in air in water gathering station, and then diffuses in the air near sewage collecting station, will form foul gas diffusion source, because
This, is provided with volatile organic matter concentration detection apparatus, the volatile organic matter concentration detection apparatus in sewage collecting station
It is dense when the volatile organic matter in sewage collecting station in air with the processing monitoring center communication connection of novel domestic sewage of villages and small towns
When degree reaches preset value, monitoring center starting Sewage Disposal can be handled by novel domestic sewage of villages and small towns changes wind system
System carries out changing wind, is degraded by natural degradation to volatile organic matter.In the present embodiment, it is equipped with and waves in sewage collecting station
Hair property Photocatalytic Degradation of Organic device, is equipped with photochemical catalyst in volatile organic matter photocatalytic degradation device, photochemical catalyst by
Titanium dioxide, porous silica, molybdenum oxide and lanthana are formed according to weight ratio 3:10:0.6:0.4, pass through electrophoretic deposition
It is made, wherein the partial size of titanium dioxide is 1-5 microns, and the partial size of porous silica is 20-30 microns, the partial size of molybdenum oxide
It is 1-2 microns, the partial size of lanthana is 2-3 microns, and above-mentioned size grading can not only make titanium dioxide, molybdenum oxide and lanthana
Can be evenly dispersed in porous silica silicon face, also help the equal of the mixing between titanium dioxide, molybdenum oxide and lanthana
Evenness.The efficiency of photochemical catalyst catalytic degradation phenol in the present embodiment is 0.54 μm of olmin-1·cm-2, much higher than with two
Titanium oxide is 0.30 μm of olmin of catalytic efficiency of raw material photochemical catalyst as made from electrophoretic deposition-1·cm-2。
By volatile organic matter photocatalytic degradation device using the photochemical catalyst in the present invention to empty in sewage collecting station
The degradation of organic matter in gas, can for a long time in keep in sewage collecting station in air content of organics to be in one close to conventional
The level of the middle content of organics of atmosphere.
(b) pretreated purifying domestic sewage processing, includes the following steps:
(b-1) pretreated sanitary sewage is successively subjected to cyclic activated sludge system purified treatment.By pretreated life
Sewage carries out the preceding pH value that pretreated sanitary sewage is adjusted with sulfuric acid and sodium hydroxide of cyclic activated sludge system processing;After pre-processing
Sanitary sewage generate in cyclic activated sludge system treatment process sludge and be transported to farmyard manure production stations as producing decomposed fertile raw material.It is logical
It crosses cyclic activated sludge system to handle sanitary sewage, is effectively utilized the feature that its occupied area is small, processing capacity is big, so that novel
The sanitary sewage generated in villages and small towns can be handled timely and effectively.
(b-2) sanitary sewage after cyclic activated sludge system purified treatment is handled by the ecosystem pool.
Sanitary sewage after cyclic activated sludge system purified treatment meets the standard discharged in natural environment water system, still
Natural environment water system can also be had an impact, in order to further be located to the sanitary sewage after cyclic activated sludge system purified treatment
Reason, while improving the weather (such as humidity) of novel villages and small towns ambient enviroment, by the sanitary sewage after cyclic activated sludge system purified treatment
It is handled by the ecosystem pool, so as to so that the sanitary sewage after cyclic activated sludge system purified treatment passes through life in natural environment
Object purified treatment further reduced influence of the sanitary sewage after cyclic activated sludge system purified treatment to natural environment.
(c) sludge generated in purifying domestic sewage treatment process farmyard manure production stations are transported to handle:
Sludge, coal ash, white lime and the chicken manure dried are uniformly mixed obtained A according to weight ratio 4:2.5:0.7:1.8
Stalk, leaf, sheep dung, fertile soil and biogas residue are uniformly mixed obtained B material according to weight ratio 5:2:1.5:1:2.5:1.8 by material, will
A material, B material and water are put into decomposed pond according to weight ratio 2:3:0.4, closed decomposed 20-35 days, decomposed fertilizer are made, inside fertile heap
Temperature is 70 DEG C.
Wherein, first the sludge generated in purifying domestic sewage treatment process is transported to after farmyard manure production stations and dries granulation,
Mud granule is made, partial size is 120-150 microns, and the mud granule surface is equipped with the groove that depth is 20-30 microns;Preparation
When A expects, the partial size of white lime is 10-20 microns, the white lime that partial size is 10-12 microns, the white lime that partial size is 13-17 microns
The weight ratio for the white lime for being 18-20 microns with partial size is 1:3:8, the mixture being made of these three white limes, not only can be with
Evenly dispersed degree of the white lime in decomposed fertile raw material is improved, and large-sized white lime can be to avoid decomposed initial phase
Temperature rises too fast, it is possible to reduce thermal loss when winter prepares decomposed fertilizer when unclosed decomposed pond.
In the present embodiment, the technique for preparing A material specifically comprises the following steps:
(c-1) by mud granule and white lime mixing granulation, the C that partial size is 135-170 microns is made and expects, specific method
Are as follows: while agitating to white lime surface continuous water spray mist 5-10 minutes in spray chamber, wet white lime particle is made, it will
It is to be mixed 20-30 minutes to expect up to C in 70-85% stirred tank that white lime particle and mud granule, which are moistened, in humidity;
(c-2) by mud granule and white lime mixing granulation, the D that partial size is 80-120 microns is made and expects, method particularly includes:
While agitating to chicken manure particle surface continuous water spray mist 10-15 minutes in spray chamber, wet chicken manure particle is made, it will be wet
Moistening chicken manure particle and flyash in humidity is to be mixed 15-20 minutes to expect up to D in 70-85% stirred tank;
(c-3) C material and D material are mixed 10-15 minutes in a stirring kettle and are expected up to A.
After preparing A material and B material, A material, B material and water are put into decomposed pond according to weight ratio 2:3:0.4, it is close
It closes decomposed 20-35 days, decomposed fertilizer is made.
Using decomposed fertilizer obtained in the present invention and farmyard manure according to rape made from weight ratio 1:3, the base manure of winter wheat,
The effective fertility of soil kept stablizing in 4 months, and cooperation imposes when 5 months whens can keep the 80% of effective fertility, 7 months
Fertility when soil fertility was with 1 month after urea 5kg is suitable and sustainable 1 half a month.
And using decomposed fertilizer and farmyard manure as the base manure of crops in hardened more serious soil, using the of the base manure
1 year, soil compaction rate had dropped decline 60% or so, and using the second year of the base manure, soil hardening situation disappears substantially.
The above embodiment of the present invention be only to clearly illustrate example of the present invention, and not be to the present invention
The restriction of embodiment can also make on the basis of the above description for those of ordinary skill in the art
Other various forms of variations or variation here can not be exhaustive all embodiments, all to belong to skill of the invention
The obvious changes or variations that art scheme is extended out are still in the scope of protection of the present invention.
Claims (10)
1. a kind of novel domestic sewage of villages and small towns treatment process, which comprises the steps of:
(a) sanitary sewage pre-processes;
(b) pretreated purifying domestic sewage processing;
(c) sludge generated in purifying domestic sewage treatment process farmyard manure production stations are transported to handle:
Sludge, coal ash, white lime and the chicken manure dried are uniformly mixed obtained A material according to weight ratio 4:2.5:0.7:1.8, it will
Stalk, leaf, sheep dung, fertile soil and biogas residue are uniformly mixed obtained B material according to weight ratio 5:2:1.5:1:2.5:1.8, by A material, B
Material and water are put into decomposed pond according to weight ratio 2:3:0.4, closed decomposed 20-35 days, decomposed fertilizer are made, fertile heap internal temperature is
60-70℃。
2. novel domestic sewage of villages and small towns treatment process according to claim 1, which is characterized in that in step (a), in society
Area sets up sewage collecting station, carries out primary filtration to community's life's sewage at sewage collecting station, filters out the particle in sanitary sewage
Partial size is greater than the solids of 3cm, and solids will be obtained by filtration and be transported to methane-generating pit progress ferment preparation of sludge gas, after then filtering
Sanitary sewage pressurization pumping Sewage Disposal progress purified treatment.
3. novel domestic sewage of villages and small towns treatment process according to claim 2, which is characterized in that the solid that will be obtained by filtration
Object is transported to methane-generating pit after mixing with the porous calcium carbonate that partial size is 30-70 microns.
4. novel domestic sewage of villages and small towns treatment process according to claim 3, which is characterized in that set in sewage collecting station
Volatile organic matter concentration detection apparatus is equipped with, at the volatile organic matter concentration detection apparatus and novel domestic sewage of villages and small towns
Manage monitoring center communication connection.
5. novel domestic sewage of villages and small towns treatment process according to claim 4, which is characterized in that sewage collecting is equipped in station
Volatile organic matter photocatalytic degradation device, volatile organic matter photocatalytic degradation device is interior to be equipped with photochemical catalyst, photochemical catalyst
It is made of titanium dioxide, porous silica, molybdenum oxide and lanthana according to weight ratio 3:10:0.6:0.4.
6. -5 any novel domestic sewage of villages and small towns treatment process according to claim 1, which is characterized in that in step (b)
In, pretreated sanitary sewage clean water treatment includes the following steps:
(b-1) pretreated sanitary sewage is successively subjected to cyclic activated sludge system purified treatment;
(b-2) sanitary sewage after cyclic activated sludge system purified treatment is handled by the ecosystem pool.
7. novel domestic sewage of villages and small towns treatment process according to claim 6, which is characterized in that in step (b-1),
Pretreated sanitary sewage is subjected to cyclic activated sludge system and handles preceding sulfuric acid and the pretreated sanitary sewage of sodium hydroxide adjusting
PH value;Will pretreated sanitary sewage carry out cyclic activated sludge system treatment process in generate sludge be transported to farmyard manure production stations as
Produce decomposed fertile raw material.
8. novel domestic sewage of villages and small towns treatment process according to claim 7, which is characterized in that sludge is transported to farmyard manure
Granulation is dried after production stations, mud granule is made, and partial size is 60-150 microns.
9. novel domestic sewage of villages and small towns treatment process according to claim 8, which is characterized in that the mud granule is
120-150 microns, the mud granule surface is equipped with the groove that depth is 20-30 microns;When preparing A material, the partial size of white lime
It is 10-20 microns, the white lime that partial size is 10-12 microns, the white lime that partial size is 13-17 microns and partial size are 18-20 microns
White lime weight ratio be 1:3:8.
10. novel domestic sewage of villages and small towns treatment process according to claim 9, which is characterized in that when preparation A material, specifically
Include the following steps:
(c-1) by mud granule and white lime mixing granulation, the C that partial size is 135-170 microns is made and expects, method particularly includes:
While agitating to white lime surface continuous water spray mist 5-10 minutes in spray chamber, wet white lime particle is made, will moisten
White lime particle and mud granule are that 20-30 minute C material to obtain the final product are mixed in 70-85% stirred tank in humidity;
(c-2) by mud granule and white lime mixing granulation, the D that partial size is 80-120 microns is made and expects, method particularly includes: it is spraying
While agitating to chicken manure particle surface continuous water spray mist 10-15 minutes in fog chamber, wet chicken manure particle is made, by wet chicken
Excrement particle and flyash are that 15-20 minute D material to obtain the final product are mixed in 70-85% stirred tank in humidity;
(c-3) C material and D material are mixed 10-15 minutes in a stirring kettle and are expected up to A.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201811009871.4A CN109052842A (en) | 2018-08-31 | 2018-08-31 | A kind of novel domestic sewage of villages and small towns treatment process |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201811009871.4A CN109052842A (en) | 2018-08-31 | 2018-08-31 | A kind of novel domestic sewage of villages and small towns treatment process |
Publications (1)
Publication Number | Publication Date |
---|---|
CN109052842A true CN109052842A (en) | 2018-12-21 |
Family
ID=64758836
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201811009871.4A Pending CN109052842A (en) | 2018-08-31 | 2018-08-31 | A kind of novel domestic sewage of villages and small towns treatment process |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN109052842A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN113354192A (en) * | 2021-05-31 | 2021-09-07 | 江苏康源环保科技有限公司 | Urban domestic sewage combined biological nitrogen and phosphorus removal device and method |
Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1209426A (en) * | 1998-08-20 | 1999-03-03 | 机械工业部机械科学研究院环境保护技术与装备研究所 | Aerobic composting technology of organic waste materials |
US20030015469A1 (en) * | 2001-04-17 | 2003-01-23 | Hedenland Michael David | Modified intermittent cycle, extended aeration system (miceas) |
CN101885563A (en) * | 2010-04-29 | 2010-11-17 | 重庆大学 | SBR+ artificial wetland combined treatment system for domestic sewage recycling |
CN105152456A (en) * | 2015-07-11 | 2015-12-16 | 四川海和风科技有限公司 | Domestic sewage treatment apparatus for colleges |
CN106957130A (en) * | 2017-03-31 | 2017-07-18 | 温州大学 | A kind of processing method of sanitary sewage and organic solid castoff |
CN107055932A (en) * | 2016-12-13 | 2017-08-18 | 九江精密测试技术研究所 | A kind of marine domestic sewage processing system |
-
2018
- 2018-08-31 CN CN201811009871.4A patent/CN109052842A/en active Pending
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1209426A (en) * | 1998-08-20 | 1999-03-03 | 机械工业部机械科学研究院环境保护技术与装备研究所 | Aerobic composting technology of organic waste materials |
US20030015469A1 (en) * | 2001-04-17 | 2003-01-23 | Hedenland Michael David | Modified intermittent cycle, extended aeration system (miceas) |
CN101885563A (en) * | 2010-04-29 | 2010-11-17 | 重庆大学 | SBR+ artificial wetland combined treatment system for domestic sewage recycling |
CN105152456A (en) * | 2015-07-11 | 2015-12-16 | 四川海和风科技有限公司 | Domestic sewage treatment apparatus for colleges |
CN107055932A (en) * | 2016-12-13 | 2017-08-18 | 九江精密测试技术研究所 | A kind of marine domestic sewage processing system |
CN106957130A (en) * | 2017-03-31 | 2017-07-18 | 温州大学 | A kind of processing method of sanitary sewage and organic solid castoff |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN113354192A (en) * | 2021-05-31 | 2021-09-07 | 江苏康源环保科技有限公司 | Urban domestic sewage combined biological nitrogen and phosphorus removal device and method |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN102976565B (en) | Miniature living sewage wastewater continuous processing device | |
CN110079448B (en) | Method and device for preparing biogas through straw and excrement three-stage co-fermentation | |
CN111333203A (en) | Ecological slow-release carbon source and preparation method and application thereof | |
CN110467276A (en) | A kind of preparation and application of sulphur autotrophy and heterotrophic denitrification denitrification organisms filler | |
CN108947098A (en) | The processing method of pig breeding wastewater | |
CN110981579A (en) | Method for preparing organic fertilizer by combining anaerobic fermentation of red mud | |
CN102964043A (en) | Technical method for preparing methane by using feces | |
CN113149120A (en) | Nitrogen neutralization process of sludge anaerobic digestion and incineration coupled system | |
CN109052842A (en) | A kind of novel domestic sewage of villages and small towns treatment process | |
CN112225419A (en) | Method for resource utilization of livestock and poultry manure | |
CN203187497U (en) | Zero-energy-consumption artificial wetland sewage treatment system | |
CN107555762A (en) | A kind of flyash replaces the method and device of Lime And Sewage Sludge dehydration | |
CN103043860B (en) | Leachate utilizing equipment and method in biomass landfilling process | |
CN105969835B (en) | Method for preparing methane by straw and excrement combined fermentation | |
CN108727098A (en) | The method for preparing fertilizer using pig breeding wastewater | |
CN101723496A (en) | Solid-liquid separation method of biogas residue liquid | |
CN204939182U (en) | A kind of Process for Treatment of Swine Wastewater system based on microbiological fuel cell | |
CN109775919B (en) | Biochemical environment-friendly process for effectively treating xanthan gum industrial wastewater | |
CN102815824B (en) | Method for extracting phosphorus from urban excrement | |
CN205773592U (en) | Unpowered aerobic reactor | |
CN105858893B (en) | A kind of Water warfare pipe | |
CN213570024U (en) | Culture wastewater glycolysis treatment system | |
CN111362544A (en) | Method for producing liquid organic fertilizer and clean reuse water of farm from biogas slurry | |
CN205442960U (en) | Garbage leachate treatment system | |
CN210736472U (en) | High-efficient anaerobism is produced hydrogen and discharge processing apparatus up to standard after pig farm waste water preliminary treatment |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
RJ01 | Rejection of invention patent application after publication |
Application publication date: 20181221 |
|
RJ01 | Rejection of invention patent application after publication |