CN206751573U - The sewage disposal system of organic wastewater - Google Patents
The sewage disposal system of organic wastewater Download PDFInfo
- Publication number
- CN206751573U CN206751573U CN201720472487.2U CN201720472487U CN206751573U CN 206751573 U CN206751573 U CN 206751573U CN 201720472487 U CN201720472487 U CN 201720472487U CN 206751573 U CN206751573 U CN 206751573U
- Authority
- CN
- China
- Prior art keywords
- iron
- electrolysis
- pipe
- carbon micro
- carbon
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
Landscapes
- Water Treatment By Electricity Or Magnetism (AREA)
Abstract
The utility model discloses a kind of sewage disposal system of organic wastewater, including:First iron-carbon micro-electrolysis retort, Fenton tank, the second iron-carbon micro-electrolysis retort, neutralization flocculation sedimentation tank and pyrolysis oven.The sewage disposal system of the utility model organic wastewater, it can be effectively treated to organic wastewater.
Description
Technical field
It the utility model is related to the sewage disposal system of organic wastewater.
Background technology
Organic wastewater is exactly the waste water based on organic pollution, and organic wastewater easily causes Water Eutrophication, hazard ratio
It is larger, it is necessary to carry out special disposal.
Utility model content
The purpose of this utility model is to provide a kind of sewage disposal system of organic wastewater, and it can be carried out to organic wastewater
Effectively processing.
To achieve the above object, the technical solution of the utility model is to design a kind of sewage disposal system of organic wastewater,
Including:First iron-carbon micro-electrolysis retort, Fenton tank, the second iron-carbon micro-electrolysis retort, neutralization flocculation sedimentation tank and pyrolysis oven;
The first iron-carbon micro-electrolysis retort is vertically arranged;The bottom of first iron-carbon micro-electrolysis retort is provided with to be had for reception
The feeding mouth of machine waste water, the feeding mouth connect with waste water input pipe;The top of first iron-carbon micro-electrolysis retort is provided with iron carbon dust
Dog-house, the iron carbon dust dog-house are connected by the first iron carbon dust delivery branch pipe with iron carbon dust delivery main;The first micro- electricity of iron carbon
The first outlet pipe for exporting iron-carbon micro-electrolysis reaction water outlet is additionally provided with the top of solution retort;
The Fenton tank is vertically arranged;The bottom of Fenton tank is provided with the feeding mouth for being used for receiving iron-carbon micro-electrolysis reaction water outlet, should
Feeding mouth connects with the first outlet pipe, and the first iron-carbon micro-electrolysis retort conveys the micro- electricity of iron carbon by the first outlet pipe to Fenton tank
Solution reaction water outlet;The top of Fenton tank is provided with the second outlet pipe for being used for exporting Fenton's reaction water outlet;
The second iron-carbon micro-electrolysis retort is vertically arranged;The bottom of second iron-carbon micro-electrolysis retort, which is provided with, to be used to receive sweet smell
Pause and react the feeding mouth of water outlet, the feeding mouth connects with the second outlet pipe, and Fenton tank is micro- to the second iron carbon by the second outlet pipe
Cell reaction tank conveys Fenton's reaction water outlet;The top of second iron-carbon micro-electrolysis retort is provided with iron carbon dust dog-house, the iron carbon
Powder dog-house is connected by the second iron carbon dust delivery branch pipe with iron carbon dust delivery main;The top of second iron-carbon micro-electrolysis retort
It is additionally provided with the 3rd outlet pipe for exporting iron-carbon micro-electrolysis reaction water outlet;
The top for neutralizing flocculation sedimentation tank is provided with the feeding mouth for being used for receiving iron-carbon micro-electrolysis reaction water outlet, the pan feeding
Mouth connects with the 3rd outlet pipe, and the second iron-carbon micro-electrolysis retort conveys iron carbon by the 3rd outlet pipe to flocculation sedimentation tank is neutralized
Micro-electrolysis reaction water outlet;Neutralize and be additionally provided with the 4th outlet pipe at the top of flocculation sedimentation tank;The bottom for neutralizing flocculation sedimentation tank is provided with
For exporting the sludge carrier pipe of precipitating sludge;
The pyrolysis oven is provided with the feeding mouth for being used for receiving sludge, and the feeding mouth connects with sludge carrier pipe, neutralizes flocculation
Sedimentation basin conveys sludge by sludge carrier pipe to pyrolysis oven;Pyrolysis oven is furnished with the microwave heating equipment for being used for heating sludge.
Preferably, the waste water input pipe also connects sulfuric acid chemical feed pipe, and sulfuric acid chemical feed pipe is provided with valve.
Preferably, first outlet pipe also connects hydrogen peroxide chemical feed pipe and ferrous sulfate chemical feed pipe, hydrogen peroxide chemical feed pipe
Valve is designed with ferrous sulfate chemical feed pipe.
Preferably, the 3rd outlet pipe also reacts pot bottom with the first iron-carbon micro-electrolysis by return duct and connected, and flows back
Pipe is also connected by drainage tube with the second outlet pipe;3rd outlet pipe is provided with a pair of valves, return duct and the 3rd outlet pipe
Connecting portion is in this between valve;Return duct is provided with a pair of valves, and the connecting portion of drainage tube and return duct is in this to valve
Between door;Second outlet pipe is provided with a pair of valves, and the connecting portion of drainage tube and the second outlet pipe is in this between valve.
Preferably, the pyrolysis oven is additionally provided with the discharging opening for exporting pyrolyzing sludge defective material, the discharging opening and iron carbon dust
Delivery main connects.
The advantages of the utility model and beneficial effect are:A kind of sewage disposal system of organic wastewater is provided, it can be right
Organic wastewater is effectively treated.
Fenton tank is the professional equipment for implementing Fenton's reaction, and Fenton's reaction is inorganic polymer composite flocculant, and process is:Hydrogen peroxide
(H2O2) and ferrous ion Fe2+Mixed solution many known organic compound such as carboxylic acid, alcohol, esters are oxidized to nothing
Machine state, reaction are given up with the ability for removing persistent organic pollutants in dyeing waste water, oily waste water, phenol wastewater, coking
Have in the wastewater treatments such as water, nitrobenzene-containing waste water, diphenylamines waste water and be widely applied very much.
Iron-carbon micro-electrolysis retort is to implement the professional equipment of Fe-C micro electrolysis, and Fe-C micro electrolysis is former using metal erosion
Logos, form the good process that galvanic cell is handled waste water, also known as internal electrolysis, Filtration with Iron Filings etc..Micro electrolysis tech
It is a kind of ideal technology of current processing high concentrated organic wastewater, also known as internal electrolysis.It is in the case of cold, is utilized
The micro-electrolysis material itself being filled in waste water produces 1.2V potential differences and carries out electrolysis processing to waste water, to reach the organic dirt of degraded
Contaminate the purpose of thing.
Organic wastewater can be successively after the first iron-carbon micro-electrolysis retort, Fenton tank, the second iron-carbon micro-electrolysis retort
Into flocculation sedimentation tank is neutralized, neutralize the clear water after flocculation sediment processing and exported by outlet pipe, the sludge of precipitation is sent into pyrolysis oven
Carry out pyrolysis processing.
Sludge can be regenerated as iron carbon dust by pyrolysis, and iron carbon dust can put into the first iron-carbon micro-electrolysis retort, the second iron carbon
Used in micro-electrolysis reaction tank.
By the valve on the second outlet pipe of operation, the 3rd outlet pipe, return duct, drainage tube, the first micro- electricity of iron carbon can be made
Solution retort, Fenton tank, the second iron-carbon micro-electrolysis retort have a variety of matching models:Iron carbon+Fenton, Fenton+iron carbon, iron carbon
+ Fenton+iron carbon etc..
Brief description of the drawings
Fig. 1 is schematic diagram of the present utility model.
Embodiment
With reference to the accompanying drawings and examples, specific embodiment of the present utility model is further described.Implement below
Example is only used for clearly illustrating the technical solution of the utility model, and can not limit protection model of the present utility model with this
Enclose.
The utility model specific implementation technical scheme be:
As shown in figure 1, a kind of sewage disposal system of organic wastewater, including:First iron-carbon micro-electrolysis retort 1, Fenton
Tank 2, the second iron-carbon micro-electrolysis retort 3, neutralize flocculation sedimentation tank 4 and pyrolysis oven 5;
The first iron-carbon micro-electrolysis retort 1 is vertically arranged;The bottom of first iron-carbon micro-electrolysis retort 1, which is provided with, to be used to receive
The feeding mouth of organic wastewater, the feeding mouth connect with waste water input pipe 11;The top of first iron-carbon micro-electrolysis retort 1 is provided with iron
Carbon dust dog-house, the iron carbon dust dog-house are connected by the first iron carbon dust delivery branch pipe 12 with iron carbon dust delivery main 51;First
The top of iron-carbon micro-electrolysis retort 1 is additionally provided with the first outlet pipe 13 for exporting iron-carbon micro-electrolysis reaction water outlet;
The Fenton tank 2 is vertically arranged;The bottom of Fenton tank 2 is provided with the feeding mouth for being used for receiving iron-carbon micro-electrolysis reaction water outlet,
The feeding mouth is connected with the first outlet pipe 13, and the first iron-carbon micro-electrolysis retort 1 is conveyed by the first outlet pipe 13 to Fenton tank 2
Iron-carbon micro-electrolysis reacts water outlet;The top of Fenton tank 2 is provided with the second outlet pipe 21 for being used for exporting Fenton's reaction water outlet;
The second iron-carbon micro-electrolysis retort 3 is vertically arranged;The bottom of second iron-carbon micro-electrolysis retort 3, which is provided with, to be used to receive
The feeding mouth of Fenton's reaction water outlet, the feeding mouth connect with the second outlet pipe 21, and Fenton tank 2 passes through the second outlet pipe 21 to second
Iron-carbon micro-electrolysis retort 3 conveys Fenton's reaction water outlet;The top of second iron-carbon micro-electrolysis retort 3 feeds intake provided with iron carbon dust
Mouthful, the iron carbon dust dog-house is connected by the second iron carbon dust delivery branch pipe 31 with iron carbon dust delivery main 51;The second micro- electricity of iron carbon
The top of solution retort 3 is additionally provided with the 3rd outlet pipe 32 for exporting iron-carbon micro-electrolysis reaction water outlet;
The top for neutralizing flocculation sedimentation tank 4 is provided with the feeding mouth for being used for receiving iron-carbon micro-electrolysis reaction water outlet, and this enters
Material mouth connects with the 3rd outlet pipe 32, the second iron-carbon micro-electrolysis retort 3 by the 3rd outlet pipe 32 to neutralize flocculation sedimentation tank 4
Convey iron-carbon micro-electrolysis reaction water outlet;The top for neutralizing flocculation sedimentation tank 4 is additionally provided with the 4th outlet pipe 41;Neutralize flocculation sedimentation tank
4 bottom is provided with the sludge carrier pipe 42 for being used for exporting precipitating sludge;
The pyrolysis oven 5 is provided with the feeding mouth for being used for receiving sludge, and the feeding mouth connects with sludge carrier pipe 42, neutralizes wadding
Solidifying sedimentation basin 4 conveys sludge by sludge carrier pipe 42 to pyrolysis oven 5;Pyrolysis oven 5 is furnished with the microwave heating for being used to heat sludge
Device.
The waste water input pipe 11 also connects sulfuric acid chemical feed pipe 14, and sulfuric acid chemical feed pipe 14 is provided with valve.
First outlet pipe 13 also connects hydrogen peroxide chemical feed pipe 22 and ferrous sulfate chemical feed pipe 23, hydrogen peroxide chemical feed pipe 22
Valve is designed with ferrous sulfate chemical feed pipe 23.
3rd outlet pipe 32 is also connected by return duct 61 with the bottom of the first iron-carbon micro-electrolysis retort 1, return duct
61 are also connected by drainage tube 62 with the second outlet pipe 21;3rd outlet pipe 32 is provided with a pair of valves, return duct 61 and the 3rd
The connecting portion of outlet pipe 32 is in this between valve;Return duct 61 is provided with a pair of valves, drainage tube 62 and return duct 61
Connecting portion is in this between valve;Second outlet pipe 21 is provided with a pair of valves, the company of the outlet pipe 21 of drainage tube 62 and second
Socket part is located at this between valve.
The pyrolysis oven 5 is additionally provided with the discharging opening for exporting pyrolyzing sludge defective material, and the discharging opening and the conveying of iron carbon dust are total
Pipe 51 connects.
Described above is only preferred embodiment of the present utility model, it is noted that for the common skill of the art
For art personnel, on the premise of the utility model technical principle is not departed from, some improvements and modifications can also be made, these change
Enter and retouch and also should be regarded as the scope of protection of the utility model.
Claims (5)
1. the sewage disposal system of organic wastewater, it is characterised in that including:First iron-carbon micro-electrolysis retort, Fenton tank, second
Iron-carbon micro-electrolysis retort, neutralize flocculation sedimentation tank and pyrolysis oven;
The first iron-carbon micro-electrolysis retort is vertically arranged;The bottom of first iron-carbon micro-electrolysis retort, which is provided with, to be used to receive organic waste
The feeding mouth of water, the feeding mouth connect with waste water input pipe;The top of first iron-carbon micro-electrolysis retort feeds intake provided with iron carbon dust
Mouthful, the iron carbon dust dog-house is connected by the first iron carbon dust delivery branch pipe with iron carbon dust delivery main;First iron-carbon micro-electrolysis is anti-
Answer the first outlet pipe being additionally provided with the top of tank for exporting iron-carbon micro-electrolysis reaction water outlet;
The Fenton tank is vertically arranged;The bottom of Fenton tank is provided with the feeding mouth for being used for receiving iron-carbon micro-electrolysis reaction water outlet, the pan feeding
Mouth connects with the first outlet pipe, and the first iron-carbon micro-electrolysis retort is anti-to Fenton tank conveying iron-carbon micro-electrolysis by the first outlet pipe
Answer water outlet;The top of Fenton tank is provided with the second outlet pipe for being used for exporting Fenton's reaction water outlet;
The second iron-carbon micro-electrolysis retort is vertically arranged;The bottom of second iron-carbon micro-electrolysis retort is provided with anti-for receiving Fenton
The feeding mouth of water outlet is answered, the feeding mouth connects with the second outlet pipe, and Fenton tank is by the second outlet pipe to the second iron-carbon micro-electrolysis
Retort conveys Fenton's reaction water outlet;The top of second iron-carbon micro-electrolysis retort is provided with iron carbon dust dog-house, and the iron carbon dust is thrown
Material mouth is connected by the second iron carbon dust delivery branch pipe with iron carbon dust delivery main;The top of second iron-carbon micro-electrolysis retort is also set
There is the 3rd outlet pipe for exporting iron-carbon micro-electrolysis reaction water outlet;
It is described neutralize flocculation sedimentation tank top be provided be used for receive iron-carbon micro-electrolysis reaction water outlet feeding mouth, the feeding mouth with
3rd outlet pipe connects, and the second iron-carbon micro-electrolysis retort conveys the micro- electricity of iron carbon by the 3rd outlet pipe to flocculation sedimentation tank is neutralized
Solution reaction water outlet;Neutralize and be additionally provided with the 4th outlet pipe at the top of flocculation sedimentation tank;The bottom of neutralization flocculation sedimentation tank, which is provided with, to be used for
Export the sludge carrier pipe of precipitating sludge;
The pyrolysis oven is provided with the feeding mouth for being used for receiving sludge, and the feeding mouth connects with sludge carrier pipe, neutralizes flocculation sediment
Pond conveys sludge by sludge carrier pipe to pyrolysis oven;Pyrolysis oven is furnished with the microwave heating equipment for being used for heating sludge.
2. the sewage disposal system of organic wastewater according to claim 1, it is characterised in that the waste water input pipe also connects
Logical sulfuric acid chemical feed pipe, sulfuric acid chemical feed pipe are provided with valve.
3. the sewage disposal system of organic wastewater according to claim 2, it is characterised in that first outlet pipe also connects
Lead to hydrogen peroxide chemical feed pipe and ferrous sulfate chemical feed pipe, valve is designed with hydrogen peroxide chemical feed pipe and ferrous sulfate chemical feed pipe.
4. the sewage disposal system of organic wastewater according to claim 3, it is characterised in that the 3rd outlet pipe is also logical
Cross return duct to connect with the first iron-carbon micro-electrolysis reaction pot bottom, return duct is also connected by drainage tube with the second outlet pipe;The
Three outlet pipes are provided with a pair of valves, and the connecting portion of return duct and the 3rd outlet pipe is in this between valve;Set on return duct
There are a pair of valves, the connecting portion of drainage tube and return duct is in this between valve;Second outlet pipe is provided with a pair of valves, draws
The connecting portion of flow tube and the second outlet pipe is in this between valve.
5. the sewage disposal system of organic wastewater according to claim 4, it is characterised in that the pyrolysis oven is additionally provided with use
In the discharging opening of output pyrolyzing sludge defective material, the discharging opening connects with iron carbon dust delivery main.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201720472487.2U CN206751573U (en) | 2017-05-02 | 2017-05-02 | The sewage disposal system of organic wastewater |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201720472487.2U CN206751573U (en) | 2017-05-02 | 2017-05-02 | The sewage disposal system of organic wastewater |
Publications (1)
Publication Number | Publication Date |
---|---|
CN206751573U true CN206751573U (en) | 2017-12-15 |
Family
ID=60616403
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201720472487.2U Active CN206751573U (en) | 2017-05-02 | 2017-05-02 | The sewage disposal system of organic wastewater |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN206751573U (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108929708A (en) * | 2018-06-26 | 2018-12-04 | 浙江奇彩环境科技股份有限公司 | Sodium chloride abraum salt recycling processing method during a kind of DYE PRODUCTION |
CN109721195A (en) * | 2019-03-07 | 2019-05-07 | 山东龙安泰环保科技有限公司 | A kind of method of interior circulation catalysis oxidation waste water |
-
2017
- 2017-05-02 CN CN201720472487.2U patent/CN206751573U/en active Active
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108929708A (en) * | 2018-06-26 | 2018-12-04 | 浙江奇彩环境科技股份有限公司 | Sodium chloride abraum salt recycling processing method during a kind of DYE PRODUCTION |
CN109721195A (en) * | 2019-03-07 | 2019-05-07 | 山东龙安泰环保科技有限公司 | A kind of method of interior circulation catalysis oxidation waste water |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN201495143U (en) | Metal ion contained acidic waste water treatment system | |
CN101698550A (en) | Advanced treating method of landfill leachate | |
CN205676306U (en) | A kind of environment protection sewage processing means | |
CN206751573U (en) | The sewage disposal system of organic wastewater | |
CN101746918A (en) | Process for treating acid wastewater in mine and reclaiming valuable metals in wastewater | |
CN103848513A (en) | Fluorine-containing wastewater treatment method based on Fenton oxidation reaction, and apparatus thereof | |
CN201770522U (en) | Electric flocculation equipment for treating mixed electroplating wastewater | |
CN106082530A (en) | A kind of integrated treatment photovoltaic energy enterprise productive life method of wastewater treatment | |
CN211712893U (en) | Difficult degradation industrial waste water treatment system | |
CN210193483U (en) | Device and system for efficiently removing total nitrogen through iron-carbon catalytic reduction | |
CN209161700U (en) | A kind of combined electrical flocculation sewage-treatment plant for strengthening electro-oxidation process | |
CN103073093A (en) | Multistage inclined-plate type electric filter bed and application thereof in purification of heavy metal wastewater | |
CN203346204U (en) | Circulating cooling two-stage clarification and softening system for waste water | |
CN202558721U (en) | Concentrated solution processing device for landfill leachate | |
CN202246302U (en) | Fluorine-containing wastewater treatment device | |
CN101838084B (en) | Biochemical regulation and treatment process for sewage of urban domestic garbage transfer station | |
CN213171877U (en) | Device for treating arsenic-containing waste acid | |
CN210367244U (en) | Portable landfill leachate environmental protection processing apparatus | |
CN211999335U (en) | Integrated treatment device for waste water in acid pickling and phosphorization production | |
CN204661465U (en) | The pre-processing device of high density cutting fluid sewage | |
CN210711146U (en) | Sugar industry effluent treatment plant | |
CN204058141U (en) | A kind of PCB comprehensive wastewater treatment facility | |
CN206705895U (en) | A kind of waste water of heat-engine plant processing and reclaiming system | |
CN209778440U (en) | Automatic integrated treatment system for aquaculture wastewater | |
CN208857069U (en) | A kind of chemical nickle-plating wastewater contaminant degradation system |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
GR01 | Patent grant | ||
GR01 | Patent grant |