CN107265758A - The free of contamination comprehensive sewage treatment system of high efficiency smart - Google Patents
The free of contamination comprehensive sewage treatment system of high efficiency smart Download PDFInfo
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- CN107265758A CN107265758A CN201710477491.2A CN201710477491A CN107265758A CN 107265758 A CN107265758 A CN 107265758A CN 201710477491 A CN201710477491 A CN 201710477491A CN 107265758 A CN107265758 A CN 107265758A
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- water
- mozzle
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- 239000010865 sewage Substances 0.000 title claims abstract description 52
- 238000011109 contamination Methods 0.000 title claims abstract description 15
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 67
- 238000006243 chemical reaction Methods 0.000 claims abstract description 51
- 239000010802 sludge Substances 0.000 claims abstract description 40
- 239000011152 fibreglass Substances 0.000 claims abstract description 35
- 238000004062 sedimentation Methods 0.000 claims abstract description 21
- 230000001954 sterilising effect Effects 0.000 claims abstract description 17
- 238000004659 sterilization and disinfection Methods 0.000 claims abstract description 17
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 claims abstract description 8
- 230000001877 deodorizing effect Effects 0.000 claims abstract description 8
- 239000004568 cement Substances 0.000 claims abstract description 5
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 49
- 239000001301 oxygen Substances 0.000 claims description 49
- 229910052760 oxygen Inorganic materials 0.000 claims description 49
- 239000000463 material Substances 0.000 claims description 40
- 244000005700 microbiome Species 0.000 claims description 20
- 239000007788 liquid Substances 0.000 claims description 16
- 239000011521 glass Substances 0.000 claims description 12
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims description 10
- 229910000831 Steel Inorganic materials 0.000 claims description 8
- 239000010959 steel Substances 0.000 claims description 8
- 239000007789 gas Substances 0.000 claims description 7
- 230000001105 regulatory effect Effects 0.000 claims description 7
- 239000004677 Nylon Substances 0.000 claims description 6
- 229920001778 nylon Polymers 0.000 claims description 6
- 239000007787 solid Substances 0.000 claims description 6
- 238000007789 sealing Methods 0.000 claims description 5
- 239000000725 suspension Substances 0.000 claims description 4
- 238000004065 wastewater treatment Methods 0.000 claims description 4
- 238000010992 reflux Methods 0.000 claims description 3
- 238000000746 purification Methods 0.000 claims 1
- 238000005265 energy consumption Methods 0.000 abstract description 16
- 230000000813 microbial effect Effects 0.000 abstract description 6
- 238000009434 installation Methods 0.000 abstract description 4
- 238000012423 maintenance Methods 0.000 abstract description 4
- 239000002028 Biomass Substances 0.000 abstract description 2
- 230000009286 beneficial effect Effects 0.000 abstract description 2
- 238000000034 method Methods 0.000 description 16
- 238000005273 aeration Methods 0.000 description 15
- 238000012545 processing Methods 0.000 description 8
- 238000013461 design Methods 0.000 description 7
- 230000029087 digestion Effects 0.000 description 6
- 230000015572 biosynthetic process Effects 0.000 description 5
- 239000000203 mixture Substances 0.000 description 5
- 239000005416 organic matter Substances 0.000 description 4
- 150000003839 salts Chemical class 0.000 description 4
- 238000010586 diagram Methods 0.000 description 3
- 239000003344 environmental pollutant Substances 0.000 description 3
- 239000012530 fluid Substances 0.000 description 3
- 231100000719 pollutant Toxicity 0.000 description 3
- 238000004064 recycling Methods 0.000 description 3
- 230000035939 shock Effects 0.000 description 3
- 230000015556 catabolic process Effects 0.000 description 2
- 239000002131 composite material Substances 0.000 description 2
- 238000010276 construction Methods 0.000 description 2
- 238000006731 degradation reaction Methods 0.000 description 2
- 230000000249 desinfective effect Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 230000007306 turnover Effects 0.000 description 2
- 239000002351 wastewater Substances 0.000 description 2
- 241000894006 Bacteria Species 0.000 description 1
- 235000006508 Nelumbo nucifera Nutrition 0.000 description 1
- 240000002853 Nelumbo nucifera Species 0.000 description 1
- 235000006510 Nelumbo pentapetala Nutrition 0.000 description 1
- 230000001133 acceleration Effects 0.000 description 1
- XKMRRTOUMJRJIA-UHFFFAOYSA-N ammonia nh3 Chemical compound N.N XKMRRTOUMJRJIA-UHFFFAOYSA-N 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000004332 deodorization Methods 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000002906 microbiologic effect Effects 0.000 description 1
- 239000010841 municipal wastewater Substances 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- 239000002912 waste gas Substances 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
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M21/00—Bioreactors or fermenters specially adapted for specific uses
- C12M21/04—Bioreactors or fermenters specially adapted for specific uses for producing gas, e.g. biogas
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M23/00—Constructional details, e.g. recesses, hinges
- C12M23/34—Internal compartments or partitions
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M23/00—Constructional details, e.g. recesses, hinges
- C12M23/58—Reaction vessels connected in series or in parallel
-
- 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
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2203/00—Apparatus and plants for the biological treatment of water, waste water or sewage
- C02F2203/006—Apparatus and plants for the biological treatment of water, waste water or sewage details of construction, e.g. specially adapted seals, modules, connections
-
- 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
- C02F2301/02—Fluid flow conditions
-
- 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
- C02F3/10—Packings; Fillings; Grids
- C02F3/101—Arranged-type packing, e.g. stacks, arrays
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/28—Anaerobic digestion processes
- C02F3/2806—Anaerobic processes using solid supports for microorganisms
-
- 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 invention provides a kind of free of contamination comprehensive sewage treatment system of high efficiency smart, mud mouth, water pipe, aerobic reaction tank, sludge pump, sludge pipe, ozone collecting pipe, aspiration pump, deodorizing tower, sterilization sedimentation basin are taken out including sewage inlet, anaerobic reaction-pot, anaerobic reaction-pot, the beneficial effects of the present invention are：Cement pit is replaced using fiberglass retort, save civilwork engineering quantity, save cost, save equipment installation period, control system uses hommization automatic running, system can be according to the water situation of same period, fan operation energy consumption is automatically controlled, when water is few, blower fan automatically selects low-frequency operation or intermittent operation, to reduce operation energy consumption, system architecture is simple, and whole service management is simple, maintenance rate and the low feature of maintenance cost, the unique internal structure of system makes that the microbial biomass of unit volume is more, and respective handling is better.
Description
【Technical field】
At a kind of integrated waste water treatment system, more particularly to a kind of free of contamination composite wastewater of high efficiency smart
Reason system.
【Background technology】
With increasingly increase, the acceleration of process of industrialization of China's urban population, the discharge capacity of municipal wastewater also increases year by year
Plus, and the most of existing sewage treatment facility in city of China is essentially all to be made a return journey using traditional activated sludge process except in sewage
The pollutant such as COD, BOD, ammonia nitrogen, the sewage disposal process of activated sludge process is primarily present, and construction cost is high, and operation energy consumption is too
Height, secondary pollution is serious (excess sludge, foul smell etc.), and artificial cumbersome, stable water outlet is difficult to ensure.
The problem of existing now with traditional wastewater treatment technology：A large amount of civil engineerings, construction, installation cost are high, and the cycle is long,
Civil engineering is it is difficult to ensure that water-tight or air tight, odor pollution, and the secondary pollution such as excess sludge is serious, and water is few or for a long time
When anhydrous, blower fan is constantly in normal high frequency operation, and operation energy consumption and expense are high, in addition, complex operation, operation is unstable
Fixed, resistance to overload shock is poor.
【The content of the invention】
The problem of present invention aims at solving to exist now with traditional wastewater treatment technology：A large amount of civil engineerings, build,
Installation cost is high, and the cycle is long, and civil engineering is it is difficult to ensure that water-tight or air tight, odor pollution, the secondary pollution such as excess sludge
Seriously, when water is few or anhydrous for a long time, blower fan is constantly in normal high frequency operation, and operation energy consumption and expense are high, separately
Outside, complex operation, fluctuation of service, resistance to overload shock difference deficiency and provide a kind of new and effective free of contamination synthesis of intelligence
Sewage disposal system.
The present invention is achieved through the following technical solutions：A kind of free of contamination composite wastewater processing system of high efficiency smart
System, including sewage inlet, anaerobic reaction-pot, anaerobic reaction-pot take out mud mouth, it is water pipe, aerobic reaction tank, sludge pump, sludge pipe, smelly
Oxygen collecting pipe, aspiration pump, deodorizing tower, sterilization sedimentation basin, the anaerobic reaction-pot front end are connected with sewage inlet, and the anaerobism is anti-
Answer tank top provided with several collecting methanes mouthful and access hole, the collecting methane mouthful and access hole are connected with biogas airway tube,
The biogas of the biogas airway tube is used to purify storage applications, and the anaerobic reaction pot bottom takes out mud mouthful provided with anaerobic reaction-pot；
The aerobic reaction tank top is provided with several foul smell collection ports, and the foul smell collection port is connected with foul smell collection
Pipe, the foul smell collecting pipe is connected with the aspiration pump, and the aspiration pump is connected by conduit with the deodorizing tower, described aerobic
React pot bottom and be provided with discharge pipeline, the aerobic reaction tank tail end is connected with sterilization sedimentation basin；
The anaerobic reaction-pot end is connected by water pipe with the aerobic reaction tank top；
Described sludge pump one end is connected by sludge pipe with the anaerobic reaction pot sidewall, and the sludge pump other end passes through
Sludge pipe is connected with the aerobic reaction pot bottom, and the sludge pipe is provided with stop valve.
Further, tank body is divided into some lattice by the anaerobic reaction-pot by dividing plate, in tank body and panel, panel dative
Same level up and down between plate is vertically located, and sets some can perforate to tow connector, then using glass-reinforced plastic material by even
Fitting is cemented, after glass steel material hardening after, using nylon rope through panel and tank body and panel and panel it is vertical
Corresponding connector, and stretch above and below fixation, formation two layers of some biological bed rope frame for being parallel to each other, then by between certain
It is uniform that anaerobe bed, anaerobe bed and rope frame are installed away from two layers of biological bed rope frame upright position up and down
Connection is tensed using binding or using band, prevents from coming off, and is thusly-formed the microorganism bed of solid, is immersed in anaerobic reaction-pot
In, connected between anaerobic reaction-pot by pipeline and use Inlet and outlet water to cross water mode, panel overflow head piece using upper entering and lower leaving
It is embedded in panel and is cemented by glass-reinforced plastic material sealing using channel bend, should from the pipeline connecting bend of bottom water outlet
Pipe makes it be fixed in panel by glass-reinforced plastic material, and the first order of anaerobic reaction-pot is provided with sludge reflux tube connection ports, biogas
Collected and imported by biogas pipe by Chi Kou and purified, bunkerage, in case using.
Further, tank body is divided into some lattice by the aerobic reaction tank by dividing plate, in tank body and panel and panel
Same level up and down between panel is vertical to be located, set it is some can perforation to tow connector, then using glass-reinforced plastic material
Suspension member is cemented, after after glass steel material hardening, makes to reeve panel and tank body, it is vertical corresponding between panel and panel
Connector, and two layers some or a plurality of rope frame being parallel to each other are stretched above and below fixation, formation, then at a certain distance upper
Microorganism bed is installed in lower two layers of rope frame upright position, and microorganism bed is connected by nylon rope with rope frame, and junction is used
Binding is tensed with band, prevents from coming off, and is thusly-formed the microorganism bed of solid, is immersed in aerobic reaction tank, aerobic reaction
The water mode excessively of upper entering and lower leaving is connected and used between tank by pipeline, panel overflow head piece is embedded in panel using channel bend
Above and by glass-reinforced plastic material sealing cement, from the pipeline connecting bend of bottom water outlet, the pipe consolidates it by glass-reinforced plastic material
It is scheduled in panel, one or more gas-liquid mixed mozzle of the middle setting in each lattice aerobic reaction tank, aerobic reaction tank is each
Level is designed using dissolved oxygen mozzle, and water (flow) direction is the similar rectangular magnet centered on dissolved oxygen mozzle in aerobic reaction tank
Distribution diagram of magnetic line of force, from N extremely toward S direction, it is anti-that mozzle lower end is vertically fixed on fiberglass by glass-reinforced plastic material
Answer the bottom of tank, and in mozzle away from bottom different directions provided with several holes are provided with, aeration tube is directly protruding into mozzle, is exposed
Tracheae does not fall bottom of pond, but aeration tube is fixed on into Chi Kou by top-support, and aeration tube upper end sets loose joint, and gas regulation
Valve, the size of aeration quantity is adjusted by air valve, and aeration tube produces bubble in dissolved oxygen mozzle, and bubble, which rises, drives sewage edge to lead
Flow tube is flowed up, and the sewage at Aerobic Pond bottom is flowed up automatically into circulation port and with bubble, gas-water mixture outflow water conservancy diversion
Manage and vertical raised to aerobic retort liquid level, formed centered on mozzle vertical fluid level point, the liquid level at center is higher than periphery,
Water naturally from middle toward perimeter, and it is descending until in loop head, Aerobic Pond liquid flow direction be similar to the arctic upward
The South Pole magnetic figure of rectangular magnet perpendicular to the ground down, by constantly supplying, makes sewage be flowed through repeatedly as the magnetic line of force
Microorganism bed, forms an organic pollution imitated in natural partial circulating, sewage again and again by microorganism bed
Microbial digestion is decomposed, and sewage gradually becomes limpid, and system water outlet can reach respective design requirement.
Further, the gas-liquid mixed mozzle is dissolved oxygen mozzle, and the bottom of the dissolved oxygen mozzle passes through glass
Steel material is perpendicularly fixed at the bottom of tank body, and the bottom of dissolved oxygen mozzle and the bottom different directions of tank body are provided with several holes,
Mozzle top is flushed with top rope frame, and mozzle middle and upper part is fixed on fiberglass tank body using glass-reinforced plastic material, makes to lead
The perpendicular reaction pot bottom of flow tube, oxygen exposure tube is inserted directly into dissolved oxygen mozzle from Chi Kou, and aeration tube upper end is provided with loose joint or interior
Outer tooth connection, and provided with gas control valve.
Further, different directions are provided with several holes at the bottom 30cm of the bottom of dissolved oxygen mozzle and tank body.
Further, the sterilization sedimentation basin includes sterilization sedimentation basin body, middle water pump, middle pond overfall, described to disappear
Malicious sedimentation basin body interior is provided with middle water pump, and the sterilization sedimentation basin body upper right side is provided with middle pond overfall.
Further, anaerobic reaction-pot and aerobic reaction the tank material is fiberglass.
Sewage raw water removes bulk debris, entered back into multistage anaerobic retort first by the grid in sewage inlet
Carry out between Non-energy-consumption resource reclaim processing, each anaerobic jar of sewage turnover by the way of upper entering and lower leaving, anaerobic jar outlet water at tail end
Into anoxic regulating reservoir, designed, stopped 0.5~2 hour in anoxic regulating reservoir, macromolecular using preaeration in anoxic regulating reservoir
Organic to be further degraded into small organic molecule, the material such as inorganic salts and water, the biodegradability of sewage is further improved, preferably
Oxygen processing provides the condition of water quality of high-quality, and sewage passes through aerobic and can reach design requirement after disinfecting.High concentration is organic negative
Lotus obtains in depth degradation, sewage more than 80% organic matter in anaerobic device in the anaerobic digestion device of unique Non-energy-consumption
New energy biogas is inside changed into, the composition such as inorganic salts and water, biogas purifies storage applications by relevant device, due to more than 80%
Organic matter is decomposed in anaerobic stages, greatly reduces the organic loading and operation energy consumption of aerobic reaction tank process, and sewage enters
One step is handled very easily with regard to that can reach water outlet requirement by aerobic reaction tank, and the sludge that aerobic reaction tank process is produced passes through sludge
It is pumped into anaerobic reaction-pot and carries out recycling, minimizing processing, whole process low energy consumption, non-secondary pollution again.
The beneficial effects of the present invention are：
(1) cement pit is replaced using fiberglass retort, saves civilwork engineering quantity, save cost, save system building and
Installation period, control system uses hommization automatic running, system can according to the water situation of same period (by electrically from
Time in dynamic control judges draining peak period, low ebb phase or festivals or holidays with the method for the detections such as pit level of catchmenting), automatic control
Fan operation energy consumption processed, when water is few, blower fan automatically selects low-frequency operation or intermittent operation, to reduce operation energy
Consumption, system architecture is simple, and whole service management is simple, maintenance rate and the low feature of maintenance cost, the unique internal structure of system
Make that the microbial biomass of unit volume is more, respective handling is better；
(2) sewage raw water removes bulk debris, enters back into multistage anaerobic retort first by the grid in sewage inlet
Between interior progress Non-energy-consumption resource reclaim processing, each anaerobic jar of sewage turnover by the way of upper entering and lower leaving, anaerobic jar end goes out
Water enters in anoxic regulating reservoir, anoxic regulating reservoir using preaeration design, is stopped 0.5~2 hour in anoxic regulating reservoir, big point
Son is organic to be further degraded into small organic molecule, and the material such as inorganic salts and water, the biodegradability of sewage is further improved, and is
Aerobic Process for Treatment provides the condition of water quality of high-quality, and sewage passes through aerobic and can reach design requirement after disinfecting.High concentration is organic
The organic matter that load obtains in depth degradation, sewage more than 80% in the anaerobic digestion device of unique Non-energy-consumption is filled in anaerobism
New energy biogas is changed into putting, the composition such as inorganic salts and water, biogas purifies storage applications by relevant device, due to 80% with
Upper organic matter is decomposed in anaerobic stages, greatly reduces the organic loading and operation energy consumption of aerobic process, and sewage is further
By Aerobic Process for Treatment very easily with regard to that can reach water outlet requirement, the sludge that aerobic process is produced sends into anaerobic reaction-pot by sludge pump
Recycling, minimizing processing, whole process low energy consumption, non-secondary pollution are carried out again；
(3) aerobic reaction tank is at different levels is designed using dissolved oxygen mozzle, and water (flow) direction is led with dissolved oxygen in aerobic reaction tank
Centered on flow tube, the distribution diagram of magnetic line of force of similar rectangular magnet, from N extremely toward S direction, mozzle is fixed on fiberglass retort
Bottom, aeration tube is directly protruding into mozzle, and aeration tube produces bubble in dissolved oxygen mozzle, and bubble, which rises, drives sewage edge
Mozzle is flowed up, and the sewage at Aerobic Pond bottom is flowed up automatically into circulation port and with bubble, and gas-water mixture outflow is led
Flow tube is simultaneously vertical raised to aerobic retort liquid level, is formed centered on mozzle vertical fluid level point, the liquid level at center is higher than week
Side, water is naturally from middle toward perimeter, and descending until loop head；Liquid flow direction is similar to arctic court in Aerobic Pond
The upper South Pole magnetic figure of rectangular magnet perpendicular to the ground down, by constantly supplying, makes sewage be flowed repeatedly as the magnetic line of force
Through microorganism bed, an organic pollution imitated in natural partial circulating, sewage is formed again and again by microorganism bed
Microbial digestion decompose, sewage gradually becomes limpid, and system water outlet can reach respective design requirement；This mode structure letter
Single, pollutant is decomposed by the microorganism species on microorganism bed, digestion, and converts it into energy, new microbial bacteria etc.,
Therefore sludge yield is few, and system resistance to overload shock is strong, stable water outlet, high treating effect；
(4) aerobic reaction tanks at different levels are equipped with discharge pipeline, and set separate control valves, aerobic process on every one-level discharge pipeline
The sludge of generation, the anaerobic reaction-pot for sending into Non-energy-consumption by sludge pump carries out minimizing, and innoxious, recycling is produced
Biogas collected by equipment, purify, store, application, aerobic process produce waste gas pass through pipeline all collect carry out deodorization
Discharged after processing, urban reclaimed water standard direct reuse is can reach after outputted aerobic water is sterile-processed, whole processing procedure is realized
Various material full resource utilizations, the system stresses, pollutant resourcesization utilize, hommization automatic operating mode, build and
The design such as operating cost is low, management service is simple.
【Brief description of the drawings】
Fig. 1 is the free of contamination comprehensive sewage treatment system structural representation of high efficiency smart of the present invention；
Fig. 2 is anaerobic reaction-pot cross-sectional view of the present invention；
Fig. 3 is aerobic reaction tank cross-sectional view of the present invention；
Reference：1st, sewage inlet；2nd, anaerobic reaction-pot；21st, collecting methane mouthful and access hole；22nd, biogas airway tube；
23rd, dividing plate；24th, overfall；25th, anaerobe bed；26th, biological bed rope frame；27th, cord attachment；28th, overflow pipe；3、
Anaerobic reaction-pot takes out mud mouthful；4th, water pipe；5th, aerobic reaction tank；51st, foul smell collection port；52nd, gas control valve；53rd, dissolved oxygen water conservancy diversion
Pipe；54th, aeration tube；55th, loop head；56th, aerobic microbiological bed；6th, sludge pump；7th, sludge pipe；71st, stop valve；8th, ozone is received
Collector；9th, aspiration pump；10th, deodorizing tower；11st, sedimentation basin is sterilized；110th, sedimentation basin body is sterilized；111st, middle water pump；112nd, reclaimed water
Pond overflow lip.
【Embodiment】
Below in conjunction with the accompanying drawings and embodiment is described further to the present invention：
As shown in Figure 1, Figure 2, Figure 3 shows, the free of contamination comprehensive sewage treatment system of a kind of high efficiency smart, including sewage inlet 1,
Anaerobic reaction-pot 2, anaerobic reaction-pot take out mud mouthfuls 3, water pipe 4, aerobic reaction tank 5, sludge pump 6, sludge pipe 7, ozone collecting pipe 8,
Aspiration pump 9, deodorizing tower 10, sterilization sedimentation basin 11, the front end of anaerobic reaction-pot 2 is connected with sewage inlet 1, the anaerobic reaction
The top of tank 2 is connected with biogas air guide provided with several collecting methanes mouthful and access hole 21, the collecting methane mouthful and access hole 21
Pipe 22, the biogas of the biogas airway tube 22 is used to purify storage utilization, and the bottom of anaerobic reaction-pot 2 is provided with anaerobic reaction-pot
Take out mud mouthful 3；
The top of aerobic reaction tank 5 is provided with several foul smell collection ports 51, and the foul smell collection port 51 is connected with ozone
Collecting pipe 8, the ozone collecting pipe 8 is connected with the aspiration pump 9, and the aspiration pump 9 is connected by conduit with the deodorizing tower 10
Connect, the bottom of aerobic reaction tank 5 is provided with discharge pipeline, the tail end of aerobic reaction tank 5 is connected with sterilization sedimentation basin 11；
The end of anaerobic reaction-pot 2 is connected by water pipe 4 with the top of aerobic reaction tank 5；
Described one end of sludge pump 6 is connected by sludge pipe 7 with the side wall of anaerobic reaction-pot 2, the other end of sludge pump 6
Connected by sludge pipe 7 with the bottom of aerobic reaction tank 5, the sludge pipe 7 is provided with stop valve 71.
Preferably, tank body is divided into some lattice by the anaerobic reaction-pot 2 by dividing plate 23, in tank body and panel, panel with
Same level up and down between panel is vertically located, and some energy perforation is set to tow connector 27, then using glass-reinforced plastic material
Connector is cemented, after after glass steel material hardening, using nylon rope through panel and tank body and panel and panel
Vertical corresponding connector, and two layers of some biological bed rope frame 26 for being parallel to each other is stretched above and below fixation, formation, then press
One determining deviation is uniform to install anaerobe bed 25, anaerobe bed in two layers of upright position of biological bed rope frame 26 up and down
25, with the connection of rope frame 26 or using bundling or being tensed using band, are prevented from coming off, are thusly-formed the microorganism bed 25 of solid,
It is immersed in anaerobic reaction-pot 2, is connected between anaerobic reaction-pot 2 by pipeline and use Inlet and outlet water to cross water using upper entering and lower leaving
Mode, panel overflow head piece 24 is embedded in panel using channel bend and cemented by glass-reinforced plastic material sealing, is gone out from bottom
The pipeline connecting bend of water, overflow pipe 28 makes it be fixed in panel by glass-reinforced plastic material, and the first order of anaerobic reaction-pot 2 is set
There are sludge reflux tube connection ports, biogas is collected by Chi Kou and imported by biogas pipe and purified, storage and application.
Preferably, tank body is divided into some lattice by the aerobic reaction tank 5 by dividing plate 23, in tank body and panel, panel with
Same level up and down between panel is vertically located, and some energy perforation is set to tow connector 27, then using glass-reinforced plastic material
Suspension member is cemented, after after glass steel material hardening, makes to reeve panel and tank body, it is vertical corresponding between panel and panel
Connector, and two layers of some rope frame 26 for being parallel to each other is stretched above and below fixation, formation, then at a certain distance up and down two
Microorganism bed 25 is installed in the upright position of layer rope frame 26, and microorganism bed 25 is connected by nylon rope with rope frame 26, junction
Tensed using binding or with band, prevent from coming off, be thusly-formed the microorganism bed of solid, be immersed in aerobic reaction tank 5, it is aerobic
The water mode excessively of upper entering and lower leaving is connected and used between retort 5 by pipeline, panel overflow head piece 24 is pre- using channel bend
It is embedded in panel and is cemented by glass-reinforced plastic material sealing, from the pipeline connecting bend of bottom water outlet, the pipe passes through glass steel
Material makes it be fixed in panel, one or more gas-liquid mixed dissolved oxygen mozzle of the middle setting in each lattice aerobic reaction tank 5
53, the bottom of dissolved oxygen mozzle 53 is perpendicularly fixed at the bottom of glass tank body by glass-reinforced plastic material, and pipe is different away from tank base
Direction is provided with several holes, and the top of dissolved oxygen mozzle 53 is flushed with top rope frame 26, and the middle and upper part of dissolved oxygen mozzle 53 uses glass
Glass Steel material is fixed on fiberglass tank body, makes the perpendicular reaction pot bottom of dissolved oxygen mozzle 53, and oxygen increasing tube is directly inserted from Chi Kou
Enter in gas-liquid mixed dissolved oxygen mozzle 53, oxygen increasing tube upper end is connected provided with loose joint or inside and outside tooth, and has gas control valve 52, aerobic
Retort 5 is at different levels to be designed using dissolved oxygen mozzle 53, and water (flow) direction is in being with dissolved oxygen mozzle 53 in aerobic reaction tank 5
The heart, the distribution diagram of magnetic line of force of similar rectangular magnet, from N extremely toward S direction, the lower end of dissolved oxygen mozzle 53 will by glass-reinforced plastic material
It is vertically fixed on the bottom of fiberglass retort, and opens several holes away from bottom different directions in dissolved oxygen mozzle 53, aeration
Pipe 54 is directly protruding into dissolved oxygen mozzle 53, and aeration tube 54 does not fall bottom of pond, but is fixed on aeration tube 54 by top-support
Chi Kou, the upper end of aeration tube 54 sets loose joint, and gas control valve 52, and the size of 52 aeration quantity, aeration tube 54 are adjusted by air valve
Bubble is produced in dissolved oxygen mozzle 53, bubble, which rises, drives sewage to be flowed up along mozzle, and the sewage at Aerobic Pond bottom is automatic
Flowed up into circulation port and with bubble, gas-water mixture outflow dissolved oxygen mozzle 53 is simultaneously vertical to the aerobic liquid level of retort 5
Projection, is formed centered on the vertical fluid level point of dissolved oxygen mozzle 53, and the liquid level at center is higher than periphery, and water is naturally from middle toward periphery
Flowing, and it is descending until in loop head 55, Aerobic Pond direction of liquid flow be similar to perpendicular to the ground that the South Pole is directed downwardly upward for the arctic
The magnetic figure of rectangular magnet, by constantly supplying, makes sewage flow through microorganism bed 25 repeatedly as the magnetic line of force, forms one
The individual organic pollution imitated in natural partial circulating, sewage is decomposed by the microbial digestion on microorganism bed again and again,
Sewage gradually becomes limpid, and system water outlet can reach respective design requirement.
Preferably, the gas-liquid mixed mozzle is dissolved oxygen mozzle 53, and the bottom of the dissolved oxygen mozzle 53 passes through glass
Glass Steel material is perpendicularly fixed at the bottom of glass tank body, and the bottom of dissolved oxygen mozzle and the bottom different directions of tank body are provided with some
Individual hole, mozzle top is flushed with top rope frame, and mozzle middle and upper part is fixed on fiberglass tank body using glass-reinforced plastic material,
Make the perpendicular reaction pot bottom of mozzle, oxygen exposure tube 54 is inserted directly into dissolved oxygen mozzle 53 from Chi Kou, and the upper end of oxygen exposure tube 54 is set
There are loose joint or the connection of inside and outside tooth, and provided with gas control valve 52.
Preferably, different directions are provided with several holes at the bottom 30cm of the bottom of dissolved oxygen mozzle and tank body.
Preferably, the sterilization sedimentation basin 11 includes sterilization sedimentation basin body 110, middle water pump 111, middle pond overflow lip 112,
The inside of sterilization sedimentation basin body 110 is provided with middle water pump 111, and the upper right side of sterilization sedimentation basin body 110 is provided with middle pond
Overflow lip 112.
Preferably, anaerobic reaction-pot 2 and aerobic reaction tank 5 material is fiberglass.
The announcement and teaching of book according to the above description, those skilled in the art in the invention can also be to above-mentioned embodiment party
Formula carries out appropriate change and modification.Therefore, the invention is not limited in embodiment disclosed and described above, to this
Some modifications and changes of invention should also be as falling into the scope of the claims of the present invention.Although in addition, this specification
In used some specific terms, but these terms are merely for convenience of description, do not constitute any limitation to the present invention.
Claims (7)
1. a kind of free of contamination comprehensive sewage treatment system of high efficiency smart, it is characterised in that：Including sewage inlet, anaerobic reaction
Tank, anaerobic reaction-pot are taken out mud mouth, water pipe, aerobic reaction tank, sludge pump, sludge pipe, ozone collecting pipe, aspiration pump, deodorizing tower, disappeared
Malicious sedimentation basin, the anaerobic reaction-pot front end is connected with sewage inlet, and the anaerobic reaction tank top is received provided with several biogas
Ji Kou and access hole, the collecting methane mouthful and access hole are connected with biogas airway tube, and the biogas of the biogas airway tube is used for
Purification storage is used, and the anaerobic reaction pot bottom takes out mud mouthful provided with anaerobic reaction-pot；
The aerobic reaction tank top is provided with several foul smell collection ports, and the foul smell collection port is connected with ozone collecting pipe, institute
State ozone collecting pipe to be connected with the aspiration pump, the aspiration pump is connected by conduit with the deodorizing tower, the aerobic reaction
Pot bottom is provided with discharge pipeline, and the aerobic reaction tank tail end is connected with sterilization sedimentation basin；
The anaerobic reaction-pot end is connected by water pipe with the aerobic reaction tank top；
Described sludge pump one end is connected by sludge pipe with the anaerobic reaction pot sidewall, and the sludge pump other end passes through sludge
Pipe is connected with the aerobic reaction pot bottom, and the sludge pipe is provided with stop valve.
2. the free of contamination comprehensive sewage treatment system of high efficiency smart according to claim 1, it is characterised in that：The anaerobism
Tank body is divided into some lattice by retort by dividing plate, and the same level up and down between tank body and panel and panel and panel is vertical
Place, is set some energy perforation to tow connector, then cements suspension member using glass-reinforced plastic material, treat that glass steel material is hardened
Afterwards, using nylon rope through panel and tank body and panel and panel vertical corresponding connector, and stretch fixation, shape
Into two layers of some biological bed rope frame for being parallel to each other up and down, then hung down at a certain distance in two layers of biological bed rope frame up and down
Straight position, uniformly installs anaerobe bed, and anaerobe bed is drawn with the connection of rope frame or using binding or using band
Tightly, prevent from coming off, be thusly-formed the microorganism bed of solid, be immersed in anaerobic reaction-pot, pass through pipeline between anaerobic reaction-pot
Connection, crosses water mode, panel overflow head piece is embedded in panel and by fiberglass using channel bend using upper entering and lower leaving
Material sealing is cemented, and from the pipeline connecting bend of bottom water outlet, overflow pipe makes it be fixed in panel, detested by glass-reinforced plastic material
The first order of oxygen retort is provided with sludge reflux tube connection ports, and biogas is collected by Chi Kou and imported by biogas pipe and purified and store
Equipment is deposited, in case using.
3. the free of contamination comprehensive sewage treatment system of high efficiency smart according to claim 1, it is characterised in that：It is described aerobic
Tank body is divided into some lattice by retort by dividing plate, and the same level up and down between tank body and panel and panel and panel is vertical
Place, is set some connectors that can be perforated to tow, then cements suspension member using glass-reinforced plastic material, treat that glass steel material is hard
After change, make to reeve vertical corresponding connector between panel and tank body and panel and panel, and stretch fixation, formed
Two layers some or a plurality of rope frame being parallel to each other up and down, then at a certain distance in two layers of rope frame upright position peace up and down
Microorganism bed is filled, microorganism bed is connected by nylon rope with rope frame, and junction is using binding or is tensed with band, anti-anti-avulsion
Fall, be thusly-formed the microorganism bed of solid, be immersed in aerobic reaction tank, connect and use by pipeline between aerobic reaction tank
The water mode excessively of upper entering and lower leaving, panel overflow head piece is embedded in panel using channel bend and seals viscous by glass-reinforced plastic material
Jail, from the pipeline connecting bend of bottom water outlet, overflow pipe makes it be fixed in panel by glass-reinforced plastic material, aerobic in each lattice
Middle setting one or more gas-liquid mixed mozzle in retort.
4. the free of contamination comprehensive sewage treatment system of high efficiency smart according to claim 3, it is characterised in that：The gas-liquid
Mixing mozzle is dissolved oxygen mozzle, and the bottom of the dissolved oxygen mozzle is perpendicularly fixed at the bottom of tank body by glass-reinforced plastic material
Portion, the bottom of dissolved oxygen mozzle and the bottom different directions of tank body are provided with several holes, dissolved oxygen mozzle top and top rope
Frame is flushed, and dissolved oxygen mozzle middle and upper part is fixed on tank body using glass-reinforced plastic material, makes the perpendicular retort bottom of dissolved oxygen mozzle
Portion, oxygen exposure tube is inserted directly into dissolved oxygen mozzle from Chi Kou, and oxygen exposure tube upper end is connected provided with loose joint or inside and outside tooth, and provided with gas
Regulating valve.
5. the free of contamination comprehensive sewage treatment system of high efficiency smart according to claim 4, it is characterised in that：Dissolved oxygen water conservancy diversion
Different directions are provided with several holes at the bottom of pipe and the bottom 30cm of tank body.
6. the free of contamination comprehensive sewage treatment system of high efficiency smart according to claim 1, it is characterised in that：The sterilization
Sedimentation basin includes sterilization sedimentation basin body, middle water pump, middle pond overflow lip, and the sterilization sedimentation basin body interior is provided with middle water pump,
The sterilization sedimentation basin body upper right side is provided with middle pond overflow lip.
7. the free of contamination integrated waste water treatment system of high efficiency smart according to claim 1, it is characterised in that：The anaerobism
Retort and aerobic reaction tank material are fiberglass.
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| JP3302227B2 (en) * | 1995-09-06 | 2002-07-15 | シャープ株式会社 | Wastewater treatment device and wastewater treatment method |
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