CN107459127A - A kind of regulation and control municipal wastewater pipeline sulphur conversion system in situ and its operation method - Google Patents
A kind of regulation and control municipal wastewater pipeline sulphur conversion system in situ and its operation method Download PDFInfo
- Publication number
- CN107459127A CN107459127A CN201710570436.8A CN201710570436A CN107459127A CN 107459127 A CN107459127 A CN 107459127A CN 201710570436 A CN201710570436 A CN 201710570436A CN 107459127 A CN107459127 A CN 107459127A
- Authority
- CN
- China
- Prior art keywords
- municipal wastewater
- wastewater pipeline
- regulation
- lower carriage
- fixed
- 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.)
- Granted
Links
Classifications
-
- 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
- C02F3/005—Combined electrochemical biological processes
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/10—Inorganic compounds
- C02F2101/101—Sulfur compounds
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2201/00—Apparatus for treatment of water, waste water or sewage
- C02F2201/46—Apparatus for electrochemical processes
- C02F2201/461—Electrolysis apparatus
- C02F2201/46105—Details relating to the electrolytic devices
-
- 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
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Molecular Biology (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- Biodiversity & Conservation Biology (AREA)
- Microbiology (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Organic Chemistry (AREA)
- Water Treatment By Electricity Or Magnetism (AREA)
Abstract
A kind of regulation and control municipal wastewater pipeline sulphur conversion system in situ and its operation method.The system includes municipal wastewater pipeline cesspool cover, microorganism electrochemical system and crane system, the crane system upper end is fixed on cesspool cover, lower end connects microorganism electrochemical system, the crane system includes upper bracket, flexible module, lower carriage, fixture, the flexible module is fixed on cesspool cover by fixture, the upper bracket and lower carriage composition X-type, the upper end of upper bracket and lower carriage is separately fixed at flexible module both sides, the lower end of upper bracket is fixed on lower carriage, the lower end connection microorganism electrochemical system of lower carriage, the electro-chemical systems include cathode sets, anode unit, wire and telescopic tube, the cathode sets are connected with anode unit by the wire for being cased with telescopic tube, the lower end of telescopic tube and lower carriage connects, the anode unit is located at the bottom of sewage conduct.Present system is simple in construction, and sulphur changing effect is good, environmentally safe.
Description
Technical field
The invention belongs to technical field of sewage, and in particular to a kind of regulation and control municipal wastewater pipeline sulphur conversion system in situ
And its operation method.
Background technology
Municipal wastewater pipeline corrodes the economic loss brought every year to the whole world and is up to multi-million dollar, wherein hydrogen sulfide
(H2S)Corrosion has become a most important origin cause of formation of sewage conduct " short-lived " caused by release.Meanwhile sewage conduct H2S is released
Put that the poisoning of initiation is of common occurrence, the life and health to municipal drainage facility maintenance worker brings great threat.With
Urbanization in China is accelerated, municipal drainage pipe network during " 12 "(Rainwater and sewage conduct)Overall length reaches 510,000 kilometers,
Meanwhile municipal drainage pipe network gradually will include underground pipe gallery during " 13 ", therefore, municipal wastewater pipeline is studied
H2S controls meet national Important Project technical need.
Sulfate in municipal wastewater(SO4 2-)Concentration is generally in 20-200 mg/L, and some enterprises produce waste water node
SO can then be dramatically increased by being discharged into pipe network4 2-Concentration.In municipal wastewater pipeline bottom anaerobic zone, SO4 2-First in bed mud sulfate also
Opportunistic pathogen(SRB)Sulfide is converted under effect(S2-), S2-Again with the hydrogen ion in water(H+)With reference to generation H2S is escaped.It is municipal dirty
Waterpipe is difficult to set H2S centralized collection processing units, therefore, from H2S in root caused by S, i.e. sewage2-Produce and be transformed into
Hand solves H2S releases problem has stronger realistic meaning.Conventional method is by adding bactericide into pipeline(As follows chlorine
Sour sodium, molybdate etc.), highly basic, metal ion etc., inactivated by SRB, improve pH, precipitation S2-Suppress etc. mode or eliminate S2-,
Advantage is that effect is rapid, and shortcoming is that cost is higher and constitute unfavorable factor to follow-up sewage plant biochemical treatment.Bioanalysis converts
S2-Technology then relative clean, mainly utilizes nitrate nitrogen(NO3 -), oxygen(O2)Deng electron acceptor by S2-It is converted into other morphologizations
Close sulphur(S0, SO4 2-, S2O3 2-Deng), and bioanalysis is in S2-Convert and taken advantage in the controllability of target product, while cost is relative
It is relatively low, it has also become the focus and emphasis of research and technology application.
Some crucial emission point positions or sewage in sewage conduct stockpile place, such as resident compact district floss hole, chemical industry
The pipeline junctions such as plant effluent mouth, emphasis pumping plant, S caused by usual duct bottom2-Concentration is higher, H2S releases are stronger.NO3 -Deng
Electron acceptor is together flowed with sewage in the duct, and advantage is, " face source " property can be played to the sewage conduct of certain length
S2-Control action.At present, it is directed to and produces S2-The higher sewage conduct node of concentration, then lack " point source " of strong applicability
Property sulphur transformation technology.
Microorganism electrochemical technology/system(Bio-electrochemical System, Bes), it is Conventional electrochemical system
The redox reaction that anode and the negative electrode at least side of system are carried out under microorganism catalysis effect, it combines microorganism and electricity
The advantage of chemistry, electrode can be as " fixation " electron acceptors of microorganism, and electron acceptor need not be additionally provided by having, and reaction is held
The advantages such as the continuous strong, non-secondary pollution of property.Taken in research fields such as wastewater treatment, underground water, bed mud, soil remediation, energy recoveries
It must develop rapidly, to solve sewage conduct " point source " property S2-Control provides breach.
The content of the invention
It is difficult to produce S to municipal sewage pipe network for existing " flowing " electron acceptor that adds2-The higher sewage well point of concentration
Position carries out the problem of intensive control, it is an object of the invention to provide a kind of in situ regulation and control municipal wastewater pipeline sulphur conversion system and
Its operation method, the system architecture is simple, sulphur changing effect is good, environmentally safe.
A kind of regulation and control municipal wastewater pipeline sulphur conversion system in situ, including municipal wastewater pipeline cesspool cover, microorganism electricity
Chemical system and crane system, the crane system upper end are fixed on cesspool cover, lower end connection microorganism electrochemical
System, the crane system include upper bracket, flexible module, lower carriage, fixture, and the flexible module is consolidated by fixture
It is scheduled on cesspool cover, the upper bracket and lower carriage composition X-type, the upper end of upper bracket and lower carriage is separately fixed at flexible mould
Block both sides, the lower end of upper bracket are fixed on lower carriage, the lower end connection microorganism electrochemical system of lower carriage, the electrochemistry
System includes cathode sets, anode unit, wire and telescopic tube, and the cathode sets are connected with anode unit by wire, outside the wire
Telescopic tube, the lower end connection of the telescopic tube and lower carriage are cased with, the cathode sets are located at oilysewage surface and air interface,
The anode unit is located at the bottom of sewage conduct.
It is that the flexible module is made up of spring and thick line as improved, the upper end point of the upper bracket and lower carriage
The both sides of spring are not fixed on, and the both ends of the spring is connected with thick line, and described thick line one end is fixed on screw, and the screw is consolidated
It is scheduled on cesspool cover.
It is that the cathode sets level is placed at oilysewage surface and air interface as improved, the anode unit and pipeline
Into 0-90 °.
It is that the wire is located at being wrapped up with PE pipes outside telescopic tube, and the anode unit is by three pairs of anodes as improved
Electrode is formed in parallel, and each pair anode electrode is longitudinally asymmetric, and the cathode sets are formed in parallel by three cathode electrodes.
It is that each anode electrode is to surround cylinder by four carbon fiber guiding brushes, and the carbon is fine as improved
Tie up a diameter of 50-100 mm, long 150-500 mm of conduction brush.
It is that each cathode electrode is the circle being made up of four elliptical spiral made with carbon paper shapes as improved
Cylinder.
It is to be both needed to handle by biofilm before the anode unit Anodic electrode installation, then connect after parallel connection as improved
To wire.
It is that the crane system also includes plummer as improved, the plummer is fixed on cesspool cover, is led to
Fixture is crossed to be connected with flexible module.
The operation method of above-mentioned regulation and control municipal wastewater pipeline sulphur conversion system in situ, comprises the following steps:Bilge well is installed
Lid, crane system and microorganism electrochemical system, contain SO in municipal wastewater pipeline4 2-Sewage is by municipal wastewater pipeline bottom
Sulfate reducing bacteria in sludge is reduced into S2-, then pass through the sun in the anode unit of municipal wastewater pipeline bottom anaerobic zone
Pole anodizing is into S0, while the S generated0It is rapidly separated by sluicing effect with anode electrode;It is placed in oilysewage surface and air
Cathode electrode in the cathode sets of intersection receives electronics that anode unit passes over by oxygen reduction Cheng Shui, leads in running
Cross crane system and adjust the position of anode unit and cathode sets respectively with telescopic tube, complete sulphur in sewage and convert.
Beneficial effect:
The cathode sets of the present invention use the floatation type electrode automatically adjusted with SEA LEVEL VARIATION, are made up of the carbon paper of four lighter weights
Elliptical spiral shape is formed, when current by when current can be utilized to promote negative electrode to rotate the oxygen belt upstream face in air,
The dissolved oxygen concentration near negative electrode is improved, accelerates oxygen to receive the reaction rate that electron reduction is water in negative electrode;
The anode electrode material of anode unit of the present invention is the preferable carbon fiber brush of biocompatibility, and its cost is relatively low, and compares table
Area is larger, is advantageous to the apposition growth of microorganism, and biofilm effect is good, can promote the transmission of electronics, increases current density, when
Current by when, current scour electrode, elemental sulfur is rapidly separated with electrode, while also promoted the rotation of anode, increase is anti-
Contact area is answered, accelerates conversion of the sulfide to sulphur simple substance;
Because single electrode is influenceed by factors such as waterpower, water quality, flow velocity, microbial metabolism speed, extracellular electron transport rates, its
Electronics flowing is very limited, and each electrode in the cathode sets and anode unit of the present invention uses paralleling model, negative electrode
It is arranged side by side at oilysewage surface and air interface, anode, which is arranged side by side, to be layered in sewage conduct bottom, the placement angle of cathode sets
It is parallel with water (flow) direction, so substantially increase the reduction reaction rate of negative electrode;Crane system in the present invention is microorganism
The maintenance and repair of electro-chemical systems provides very big convenience.
Brief description of the drawings
Fig. 1 is the structural representation of the system of the embodiment of the present invention 1, wherein, 1- cesspool covers, 2- upper brackets, 3- sulfate
Reducing bacteria, 4- lower carriages, 5- fixtures, 7- cathode sets, 8- anode units, 9- telescopic tubes, 10- springs, 11- thick lines, 12- are held
Microscope carrier, 13- screws;
Fig. 2 is the top view of present system Anodic group;
Fig. 3 is the top view of cathode sets in present system;
Fig. 4 is present system Anodic group and the cut-away view of the sleeve pipe of cathode sets junction, wherein 6- wires;
Fig. 5 be present system Anodic group and pipeline into different angle when, sewage SO4 2-Concentration is 150 ± 5mg/L situation
Under, sulphur converted product in sewage(SO4 2-、S2-、S0、H2S、S2O3 2-)Concentration ratio;
Fig. 6 is present system in SO containing various concentrations4 2-Sulphur converted product in sewage(SO4 2-、S2-、S0、H2S、S2O3 2-)It is dense
Degree ratio;
Fig. 7 is SO containing various concentrations4 2-Sulphur converted product in sewage conduct(SO4 2-、S2-、S0、H2S、S2O3 2-)Concentration ratio.
Embodiment
Below in conjunction with the accompanying drawings technical solution of the present invention is elaborated with embodiment.
Embodiment 1
A kind of regulation and control municipal wastewater pipeline sulphur conversion system in situ, including municipal wastewater pipeline cesspool cover, microorganism electrochemical
System and crane system, the crane system upper end are fixed on cesspool cover 1, lower end connection microorganism electrochemical system
System, the crane system include upper bracket 2, flexible module, lower carriage 4, fixture 5, and the flexible module passes through fixture 5
It is fixed on cesspool cover 1, the upper bracket 2 forms X-type with lower carriage 4, and the upper end of upper bracket 2 and lower carriage 4 is fixed respectively
In flexible module both sides, module of stretching shrinks the size for changing X-type angle, completes flexible purpose, realize microorganism electrochemical
The change of the position of system.The lower end of upper bracket 2 is fixed on lower carriage 4, the lower end connection microorganism electrochemical system of lower carriage 4
System, the electro-chemical systems include cathode sets 7, anode unit 8, wire 6 and telescopic tube 9, the cathode sets 7 and anode unit 8 by
Wire 6 connects, and is cased with telescopic tube 9 outside the wire 6, the telescopic tube 9 is connected with the lower end of lower carriage 4, the negative electrode
For group 7 at oilysewage surface and air interface, the anode unit 8 is located at the bottom of sewage conduct.
In order to prevent short circuit, the part that the wire 6 is located at outside telescopic tube 9 is wrapped up with PE pipes, then using conduction
Cream and plastic clip connecting wire and extraneous resistance, form closed-loop path.In addition, when cathode sets 7 are with SEA LEVEL VARIATION, with telescopic
The PE pipes of the cathode sets 7 of the top of pipe 9 connection also move up and down therewith, solid with the PE pipes of the bottom jointed anode group 8 of telescopic tube 9
It is scheduled on crane, the wire 6 inside telescopic tube 9 can extend or shorten with the change in location of cathode sets 7.
The flexible module is made up of spring 10 and thick line 11, and the upper end of the upper bracket 2 and lower carriage 4 is separately fixed at
The both sides of spring 10, the both ends thick line 11 of spring 10 are connected, and described one end of thick line 11 is fixed on screw 13, the screw 13
It is fixed on cesspool cover 1.In running, thick line 11 is twitched by rotary screw 13, drives spring 10 to deform upon, and then
Change the X-type angle number of degrees of upper bracket 2 and lower carriage 4 so that upper bracket 2 is pasted close or remote from cesspool cover 1 with lower carriage 4, complete
Change into the position of microorganism electrochemical system;When all supports all press close to cesspool cover 1, mobile cesspool cover can be passed through
1 takes out crane system together with microorganism electrochemical system, is easy to the maintenance and repair of microorganism electrochemical system.
Further improved to be, the crane system also includes plummer 12, and the plummer 12 is fixed on bilge well
On lid 1, and it is connected by fixture 5 and flexible module.The distance that can realize both ends of the spring by rotary screw 13 changes,
Contraction process is completed, and plummer 12 can reduce abrasion of the screw 13 to cesspool cover.
Each anode electrode of the anode unit 8 is the cylinder surrounded by four carbon fiber guiding brushes, the carbon fiber
A diameter of 50-100 mm of conduction brush, long 150-500 mm, it is from carbon fiber guiding brush because carbon fiber biological compatibility
It is good, and specific surface area is big, is advantageous to the apposition growth of microorganism, and biofilm effect is good, can promote the transmission of electronics, increases electrode
Density, when current by when, wash away electrode, elemental sulfur is rapidly separated with electrode, while also promoted the rotation of anode, increase
Reaction contact area, accelerate conversion of the sulfide to sulphur simple substance.
It is that the anode electrode of anode unit 8 can be tamed and dociled by electroactive microorganism accumulating potential in a pre-installation as improved
Change the anode sulfur oxidizing organism film with catalytic activity, i.e. biofilm is handled, and the biofilm comprises the following steps that:Using three electrode bodies
Anaerobic grain sludge after break process and simulation sulfur compound sewage are first pressed 1 by system, Ag/AgCl as reference electrode:1
Ratio, which is added to, to be had been subjected in autoclaved electrochemical reactor working electrode room, and sludge passes through denitrification desulfurization before being derived from
The device of domestication, 70% nitrogen and the min of 30% carbon dioxide gas mixture 20 are then exposed to remove the dissolved oxygen in nutrient solution and anti-
Answer the air at the top of device.8 plant heights effect sulfur oxidizing bacterium strain shaking table culture in LB nutrient solutions of screening early stage is stayed overnight(In 30 DEG C,
180 rpm).Take 8 plant heights being incubated overnight to imitate the mL of sulfur oxidizing bacterium strain liquid 2, be inoculated in electrochemical reaction working electrode room, electrification
The pH value learned in reaction chamber is controlled in 8.0-8.5, and working electrode potential is controlled by electrochemical workstation, makes it
Maintain -0.27 V.First 5 days, anaerobic sludge and simulation sulfur compound sewage were changed daily, it is dirty with pure simulation sulfur compound afterwards
Water is cultivated, and during this, persistently working electrode room is aerated, temperature is maintained at 30 DEG C.
Each cathode electrode is the cylinder being made up of four elliptical spiral made with carbon paper shapes in the cathode sets 7
Body, during installation cathode sets 7 be located at oilysewage surface with air interface, it is and parallel with water (flow) direction, substantially increase the reduction of negative electrode
Reaction rate.
Embodiment 2
A kind of operation method of above-mentioned regulation and control municipal wastewater pipeline sulphur conversion system in situ, comprises the following steps:Bilge well is installed
Lid, crane system and microorganism electrochemical system, contain SO in municipal wastewater pipeline4 2-Sewage is by duct bottom sludge
Sulfate reducing bacteria 3 is reduced into S2-, then by the anodic oxidation in the anode unit 8 of duct bottom anaerobic zone into S0, together
Shi Shengcheng S0It is rapidly separated by sluicing effect with anode;It is placed in the cathode sets 7 at oilysewage surface and air interface
Negative electrode receives the electronics that passes over of anode by oxygen reduction Cheng Shui.It is electrochemical for microorganism by crane system in running
System carries out maintenance and repair.The present invention sewage in system is sampled with monitor the change in concentration of sulphur converted product and
Sampling determination H is carried out to the overhead gas of cesspool cover 12S concentration.
Embodiment 3
SO in usual sewage4 2-Fluctuation of concentration scope is 20-200 mg/L, in order to why investigate anode unit and pipeline angulation
Optimal to sewage conduct sulphur changing effect during value, the present invention is in sewage SO4 2-Concentration has done one group in the case of being 150 ± 5mg/L
Compare case(That is anode unit and pipeline is into 0 °, 30 °, 45 °, 60 °, 90 °), in addition to anode unit and pipe angle difference, remaining
Implementation steps and implementation content are same as described above.
As can be seen from Figure 5, in SO4 2-When concentration is 150 ± 5mg/L, anode unit is with pipeline into 0 °, 30 °, 45 °, 60 °, 90 °
When, S in sulphur converted product0The ratio accounted in sulfur speciation respectively reaches 67%, 70%, 83%, 68%, 60%, S2-Ratio be 19%,
8%th, 4%, 9%, 14%, it can be seen that, anode unit is more conducive to sewage conduct sulphur relative to other angles with pipeline setting at 45 ° and turned
Change, it accelerates conversion of the sulfide to sulphur simple substance, improve electrode and mass transfer in liquid phase speed and current scour make elemental sulfur,
The speed of noxious material and electrode separation.
Embodiment 4
On the basis of embodiment 3, anode unit and pipeline angle are selected as under conditions of 45 °, with different sewage SO4 2-Concentration(50
±1.6 mg/L、100±3.4 mg/L、150±5 mg/L、200±4.5 mg/L)To investigate sewage SO4 2-Lower of fluctuation of concentration
The operation stability and operational effect of system.Meanwhile a control group is set to compare S2-、H2S cuts down effect.
As seen from Figure 6, the sulphur converted product that present system obtains under different sewage concentration(SO4 2-、S2-、S0、H2S、
S2O3 2-)Ratio, S2-Clearance is up to more than 90%, S0Conversion ratio is more than 85%, H2S yields are less than 4%;
As seen from Figure 7, S is produced in the sewage conduct of non-implant electrode2-Concentration has no significant change, H2S yields are higher than 20% thus
It can be seen that regulation and control municipal wastewater pipeline sulphur conversion system positive effect in situ, and under different sewage fluctuation of concentration, sulphur changing effect
It is stable.
In addition, the invention is not restricted to above-mentioned embodiment, as long as in without departing from the scope of the present invention, can take various
Mode implements the present invention.
Claims (9)
- A kind of in situ 1. regulation and control municipal wastewater pipeline sulphur conversion system, it is characterised in that including municipal wastewater pipeline cesspool cover, Microorganism electrochemical system and crane system, the crane system upper end are fixed on cesspool cover, and lower end connects micro- life Thing electro-chemical systems, the crane system include upper bracket, flexible module, lower carriage, fixture, and the flexible module passes through Fixture is fixed on cesspool cover, the upper bracket and lower carriage composition X-type, and the upper end of upper bracket and lower carriage is fixed respectively In flexible module both sides, the lower end of upper bracket is fixed on lower carriage, the lower end connection microorganism electrochemical system of lower carriage, institute Stating electro-chemical systems includes cathode sets, anode unit, wire and telescopic tube, and the cathode sets are connected with anode unit by wire, institute State and telescopic tube is cased with outside wire, the lower end connection of the telescopic tube and lower carriage, the cathode sets are located at oilysewage surface and sky Gas intersection, the anode unit are located at the bottom of sewage conduct.
- 2. a kind of regulation and control municipal wastewater pipeline sulphur conversion system in situ according to claim 1, it is characterised in that described to stretch Contracting module is made up of spring and thick line, and the upper end of the upper bracket and lower carriage is separately fixed at the both sides of spring, the spring Both ends are connected with thick line, and described thick line one end is fixed on screw, and the screw is fixed on cesspool cover.
- A kind of 3. regulation and control municipal wastewater pipeline sulphur conversion system in situ according to claim 1, it is characterised in that described the moon Pole group level is placed at oilysewage surface and air interface, and the anode unit is with pipeline into 0-90 °.
- 4. a kind of regulation and control municipal wastewater pipeline sulphur conversion system in situ according to claim 1, it is characterised in that described to lead Line is located at being wrapped up with PE pipes outside telescopic tube, and the anode unit is formed in parallel by three pairs of anode electrodes, and each pair anode electrode is indulged To symmetrical, the cathode sets are formed in parallel by three cathode electrodes.
- 5. 4 one kind regulation and control municipal wastewater pipeline sulphur conversion system in situ according to claim, it is characterised in that described every Individual anode electrode is to surround cylinder by four carbon fiber guiding brushes, and a diameter of 50-100 mm of the carbon fiber guiding brush are long 150-500 mm。
- 6. a kind of regulation and control municipal wastewater pipeline sulphur conversion system in situ according to claim 4, it is characterised in that described every Individual cathode electrode is the cylinder being made up of four elliptical spiral made with carbon paper shapes.
- A kind of 7. regulation and control municipal wastewater pipeline sulphur conversion system in situ according to claim 4, it is characterised in that the sun It is both needed to handle by biofilm before the group Anodic electrode installation of pole, then is connected to after parallel connection on wire.
- A kind of 8. regulation and control municipal wastewater pipeline sulphur conversion system in situ according to claim 1, it is characterised in that the liter Drop frame system also includes plummer, and the plummer is fixed on cesspool cover, is connected by fixture and flexible module.
- 9. based on a kind of operation method of regulation and control municipal wastewater pipeline sulphur conversion system in situ described in claim 1, its feature It is, comprises the following steps:Cesspool cover, crane system and microorganism electrochemical system be installed, in municipal wastewater pipeline Containing SO4 2-Sewage is reduced into S by the sulfate reducing bacteria in municipal wastewater pipeline base sludge2-, then by positioned at municipal wastewater Anode electrode in the anode unit of duct bottom anaerobic zone is oxidized to S0, while the S generated0Pass through sluicing effect and anode Electrode is rapidly separated;Cathode electrode in the cathode sets being placed at oilysewage surface and air interface receives the electricity that anode unit passes over Oxygen reduction Cheng Shui is adjusted the position of anode unit and cathode sets by son respectively by crane system and telescopic tube in running Put, complete sulphur in sewage and convert.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201710570436.8A CN107459127B (en) | 2017-07-13 | 2017-07-13 | In-situ regulation and control municipal sewage pipeline sulfur conversion system and operation method thereof |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201710570436.8A CN107459127B (en) | 2017-07-13 | 2017-07-13 | In-situ regulation and control municipal sewage pipeline sulfur conversion system and operation method thereof |
Publications (2)
Publication Number | Publication Date |
---|---|
CN107459127A true CN107459127A (en) | 2017-12-12 |
CN107459127B CN107459127B (en) | 2020-12-08 |
Family
ID=60546321
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201710570436.8A Active CN107459127B (en) | 2017-07-13 | 2017-07-13 | In-situ regulation and control municipal sewage pipeline sulfur conversion system and operation method thereof |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN107459127B (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110697982A (en) * | 2019-10-23 | 2020-01-17 | 盐城工学院 | Zero-valent iron system for in-situ removal of hydrogen sulfide in municipal sewage pipeline well and operation method thereof |
CN110759489A (en) * | 2019-11-15 | 2020-02-07 | 盐城工学院 | Electricity-zero-valent iron system for accelerating removal of sulfide in sewage pipeline |
CN110803741A (en) * | 2019-10-17 | 2020-02-18 | 上海市政工程设计研究总院(集团)有限公司 | Guide rail type electrolysis system suitable for drainage pipeline in-situ purification |
CN113443790A (en) * | 2021-07-22 | 2021-09-28 | 裴自川 | Multiple filter equipment is used in municipal sewage treatment |
CN113880235A (en) * | 2021-11-16 | 2022-01-04 | 吉林建筑大学 | Solar energy combined type electrolysis sewage treatment flotation device |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102249397A (en) * | 2011-05-16 | 2011-11-23 | 合肥工业大学 | Bio-electrochemical enhanced waste water treatment device |
US20120070696A1 (en) * | 2010-09-21 | 2012-03-22 | Advanced Environmental Technologies, Llc | Methods and Systems for Enhanced Oxidative and Reductive Remediation |
CN204662641U (en) * | 2015-03-25 | 2015-09-23 | 湖北雨乐环保科技有限公司 | A kind of rainwater-collecting cuts dirty settler |
-
2017
- 2017-07-13 CN CN201710570436.8A patent/CN107459127B/en active Active
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20120070696A1 (en) * | 2010-09-21 | 2012-03-22 | Advanced Environmental Technologies, Llc | Methods and Systems for Enhanced Oxidative and Reductive Remediation |
CN102249397A (en) * | 2011-05-16 | 2011-11-23 | 合肥工业大学 | Bio-electrochemical enhanced waste water treatment device |
CN204662641U (en) * | 2015-03-25 | 2015-09-23 | 湖北雨乐环保科技有限公司 | A kind of rainwater-collecting cuts dirty settler |
Non-Patent Citations (1)
Title |
---|
谢静怡 著: "《环境生物电化学原理与应用》", 31 July 2014, 哈尔滨工业大学出版社 * |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110803741A (en) * | 2019-10-17 | 2020-02-18 | 上海市政工程设计研究总院(集团)有限公司 | Guide rail type electrolysis system suitable for drainage pipeline in-situ purification |
CN110697982A (en) * | 2019-10-23 | 2020-01-17 | 盐城工学院 | Zero-valent iron system for in-situ removal of hydrogen sulfide in municipal sewage pipeline well and operation method thereof |
CN110759489A (en) * | 2019-11-15 | 2020-02-07 | 盐城工学院 | Electricity-zero-valent iron system for accelerating removal of sulfide in sewage pipeline |
CN113443790A (en) * | 2021-07-22 | 2021-09-28 | 裴自川 | Multiple filter equipment is used in municipal sewage treatment |
CN113880235A (en) * | 2021-11-16 | 2022-01-04 | 吉林建筑大学 | Solar energy combined type electrolysis sewage treatment flotation device |
CN113880235B (en) * | 2021-11-16 | 2023-03-07 | 吉林建筑大学 | Solar energy combined type electrolysis sewage treatment flotation device |
Also Published As
Publication number | Publication date |
---|---|
CN107459127B (en) | 2020-12-08 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN107459127A (en) | A kind of regulation and control municipal wastewater pipeline sulphur conversion system in situ and its operation method | |
CN104377378B (en) | A kind of microorganism electrochemical device and method for repairing groundwater azotate pollution | |
CN105481206B (en) | A kind of control method of black smelly river lake original position ecological reestablishment integrated system | |
CN104787977A (en) | Continuous flow integrated electrode bio-membrane reactor and nitrate removal technology | |
CN104310581A (en) | Rotary electrode biomembrane reactor and method for treating oxidizing pollutants | |
CN102249424A (en) | Proton exchange membrane-free microbiological fuel cell sewage treatment system and application method thereof | |
CN103319002A (en) | Method for biological treatment of sulfate wastewater employing synchronous electric catalysis of anode and cathode | |
CN106116019A (en) | A kind of membraneless microbiological fuel cell void tower formula catalytic oxidation membrane bioreactor coupled system | |
CN106630147A (en) | Device and method for removing nitrate of water body based on biological membrane reactor | |
CN206502728U (en) | A kind of in-situ treatment device of black and odorous water bed mud | |
CN104860397A (en) | Electrochemical-biological fluidized bed reactor and wastewater treatment method | |
CN102249409B (en) | Device and method for strengthening treatment of anaerobic sewage by using solar energy | |
CN207619194U (en) | A kind of automation oxidation ditch device for during tertiary sewage treatment | |
CN208071436U (en) | A kind of regulation and control municipal wastewater pipeline sulphur conversion system in situ | |
CN103966078A (en) | Device and method for producing hydrogen and methane by embedded biological electrolysis | |
CN204185296U (en) | A kind of rotating electrode biofilm reactor | |
CN110342637A (en) | Device and method for improving low-temperature biological denitrification efficiency | |
CN102424474A (en) | New method for acclimating active sludge resisting high chloride ion wastewater | |
NL2029927B1 (en) | A process to treat a carbon dioxide comprising gas | |
CN207002526U (en) | A kind of multi-functional organic waste biochemical degradation device for experimental teaching | |
CN105445432B (en) | A kind of water sludge interface materialization regulator control system for landscape water body in-situ immobilization | |
CN201224703Y (en) | Unpowered efficient dispersing domestic sewage treatment complete equipment | |
CN211226566U (en) | Electricity-zero-valent iron system for accelerating removal of sulfide in sewage pipeline | |
CN204643965U (en) | Overflow type electrochemica biological membrane reactor | |
CN208454594U (en) | A kind of water treatment system |
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 | ||
GR01 | Patent grant | ||
GR01 | Patent grant |