CN208617442U - Fenton light electrolysis oxidation treatment device - Google Patents

Fenton light electrolysis oxidation treatment device Download PDF

Info

Publication number
CN208617442U
CN208617442U CN201821008663.8U CN201821008663U CN208617442U CN 208617442 U CN208617442 U CN 208617442U CN 201821008663 U CN201821008663 U CN 201821008663U CN 208617442 U CN208617442 U CN 208617442U
Authority
CN
China
Prior art keywords
fenton
partition
reaction
reaction chamber
deflector
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
Application number
CN201821008663.8U
Other languages
Chinese (zh)
Inventor
陈涛
周现涛
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Guangdong Ying Rui Tong Environmental Technology Co Ltd
Original Assignee
Guangdong Ying Rui Tong Environmental Technology Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Guangdong Ying Rui Tong Environmental Technology Co Ltd filed Critical Guangdong Ying Rui Tong Environmental Technology Co Ltd
Priority to CN201821008663.8U priority Critical patent/CN208617442U/en
Application granted granted Critical
Publication of CN208617442U publication Critical patent/CN208617442U/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Abstract

The utility model discloses a kind of Fenton light electrolysis oxidation treatment devices, including sealing Fenton's reaction pond, sedimentation basin, air hose and blower, Fenton's reaction pond includes the sour process chamber being sequentially communicated, reaction chamber and alkali process room, sour process chamber is equipped with water inlet far from reaction chamber one end, first partition is equipped between sour process chamber and reaction chamber, first partition is fixedly connected with Fenton's reaction bottom of pond portion, second partition is equipped between reaction chamber and alkali process room, it is fixedly connected at the top of second partition and Fenton's reaction pond, runner pipe is equipped between alkali process room and sedimentation basin, blower by air hose respectively with sour process chamber, reaction chamber is connected to alkali process ceiling portion, first partition is placed in reaction chamber side equipped with the first deflector of muti-piece;Second partition is placed in reaction chamber side equipped with the second deflector of muti-piece;The first deflector of muti-piece and the arrangement alternate with each other of the second deflector of muti-piece constitute a sinuous distribution channel.The utility model provides a kind of Fenton light electrolysis oxidation treatment device that waste water can be made sufficiently to react.

Description

Fenton light electrolysis oxidation treatment device
Technical field
The utility model relates to technical field of waste water processing more particularly to a kind of Fenton light electrolysis oxidation treatment devices.
Background technique
The characteristics of electrochemical water treatment technology is a kind of novel water treatment technology, the technology is to remove waste water using electric energy In organic pollutant.Electro-chemical water processing carries out in a cell, in anode region organic pollutant by direct or indirect oxidation, Up to mineralising, while in cathodic region, organic pollutant can be reduced modification, but can not be degraded for degradation.Due to having in waste water Machine pollutant concentration is far below the concentration of water in waste water, so current efficiency of the anode region for oxidation of organic compounds is lower, generally Lower than 30%, the current efficiency of residue about 70% is for occurring the electrode reactions such as analysis oxygen, analysis chlorine;Meanwhile cathodic region is for restoring The current efficiency of organic matter is also relatively low, and generally below 30%, the current efficiency of residue about 70% is for occurring evolving hydrogen reaction.Cause This, a large amount of electric current energy consumption is wasted.
Fenton's reaction is a kind of reaction based on Fenton reagent (hydrogen peroxide and ferrous ion), is generated in the reaction with strong The hydroxyl radical free radical (- OH) of oxidisability can aoxidize the organic pollutant in waste water, degradation is until mineralising is inorganic matter.By In hydrogen peroxide and ferrous ion in molar ratio 1:1 or so, and the dosage of hydrogen peroxide is directly proportional to the organic pollutant in waste water, institute In use, will use more hydrogen peroxide and ferrous salt, and generally pH can be adjusted to after Fenton's reaction in Practical Project Neutrality, Fe3+ can be with the equal solid forms precipitating of Fe (OH) 3 at this time.
In process of production, Fenton reagent is added into Fenton's reaction pond, effluent part is next as water flow flows directly into Processing unit eventually leads to waste water and is not sufficiently reacted with Fenton reagent without mixed reaction time.
Utility model content
The Fenton light electrolysis oxidation processes that waste water can be made sufficiently to react the purpose of this utility model is to provide one kind are set It is standby.
Technical solution used by Fenton light electrolysis oxidation treatment device disclosed by the utility model is:
A kind of Fenton light electrolysis oxidation treatment device, including sealing Fenton's reaction pond, sedimentation basin, air hose and blower, it is described Fenton's reaction pond includes the sour process chamber, reaction chamber and alkali process room being sequentially communicated, and the acid process chamber is far from reaction chamber one end Equipped with water inlet, first partition, the first partition and Fenton's reaction bottom of pond portion are equipped between the acid process chamber and reaction chamber It is fixedly connected, second partition is equipped between the reaction chamber and alkali process room, the second partition and Fenton's reaction pond top are solid Fixed connection, is equipped with runner pipe between the alkali process room and sedimentation basin, the blower by air hose respectively with sour process chamber, react Room is connected to alkali process ceiling portion, and the first partition is placed in reaction chamber side equipped with the first deflector of muti-piece;Described second every Plate is placed in reaction chamber side equipped with the second deflector of muti-piece;First deflector of muti-piece and the second deflector of muti-piece are alternate with each other Arrangement constitutes a sinuous distribution channel.
Preferably, the second partition bottom end is vertical with first partition side wall is equipped with an orifice plate, and described first leads Flowing plate and the second deflector are placed in orifice plate top.
Preferably, it is equipped with the first charging port at the top of the sour process chamber, for filling acidic materials;The reaction Ceiling portion is equipped with the second charging port, and for filling Fenton reagent, alkali process ceiling portion is equipped with third charging port, for filling Alkaline matter.
Preferably, the water inlet is placed in sour chamber bottom.
It preferably, is mill weir slot structure at the top of the sedimentation basin, the precipitating bottom of pond portion is conical bottom.
The beneficial effect of Fenton light electrolysis oxidation treatment device disclosed by the utility model is: Fenton's reaction pond includes successively Sour process chamber, reaction chamber and the alkali process room of connection, sour process chamber are equipped with water inlet far from reaction chamber one end, sour process chamber and anti- It answers and is equipped with first partition between room, first partition is fixedly connected with Fenton's reaction bottom of pond portion, sets between reaction chamber and alkali process room There is second partition, is fixedly connected at the top of second partition and Fenton's reaction pond.A sinuous distribution channel is constituted in the horizontal direction, And there are fluid communications pathways between each room.Blower by air hose respectively with sour process chamber, reaction chamber and alkali process ceiling portion Connection, the internal a small amount of bubble of removing.First partition is placed in reaction chamber side equipped with the first deflector of muti-piece, and second partition is placed in instead Room side is answered to be equipped with the second deflector of muti-piece, the first deflector of muti-piece constitutes one with the arrangement alternate with each other of the second deflector of muti-piece and wriggles The distribution channel of Yan, extends the length of circulation path, to achieve the effect that waste water is sufficiently reacted with Fenton reagent.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of the utility model Fenton light electrolysis oxidation treatment device.
Specific embodiment
The utility model is further elaborated and is illustrated with Figure of description combined with specific embodiments below:
Referring to FIG. 1, a kind of Fenton light electrolysis oxidation treatment device, including sealing Fenton's reaction pond 10, sedimentation basin 20, wind Machine 40 and air hose 41.
Fenton's reaction pond 10 includes sour process chamber 11, reaction chamber 12 and the alkali process room 13 being sequentially communicated.Sour process chamber 11 Top is equipped with the first charging port 16, for filling acidic materials;The second charging port 17 is equipped at the top of reaction chamber 12, for filling sweet smell Pause reagent, third charging port 18 is equipped at the top of alkali process room 13, for filling alkaline matter.
Sour process chamber 11 is equipped with water inlet 111 far from 12 one end of reaction chamber, is equipped between sour process chamber 11 and reaction chamber 12 First partition 14, first partition 14 are fixedly connected with 10 bottom of Fenton's reaction pond, are equipped between reaction chamber 12 and alkali process room 13 It is fixedly connected at the top of second partition 15, second partition 15 and Fenton's reaction pond 10.A sinuous circulation is constituted in the horizontal direction Access, and there are fluid communications pathways between each room.
Blower 40 is connected to at the top of sour process chamber 11, reaction chamber 12 and alkali process room 13 respectively by air hose 41, in removing The a small amount of bubble in portion.First partition 14 is placed in 12 side of reaction chamber equipped with the first deflector of muti-piece 121, and second partition 15 is placed in reaction 12 side of room is equipped with the second deflector of muti-piece 122, the first deflector of muti-piece 121 and the row alternate with each other of the second deflector of muti-piece 122 Cloth constitutes a sinuous distribution channel, extends the length of circulation path, to reach the effect that waste water is sufficiently reacted with Fenton reagent Fruit.
Runner pipe 30, the conducting for waste water are equipped between alkali process room 13 and sedimentation basin 20.
15 bottom end of second partition is vertical with 14 side wall of first partition to be equipped with an orifice plate 123, and the first deflector 121 and second are led Flowing plate 122 is placed in 123 top of orifice plate.Primary filtration is carried out to waste water.
Since reaction rate of the Fenton's reaction under acidic environment is higher.Therefore, water inlet 111 is placed in sour process chamber 11 Bottom, the acidic materials and waste water that the first charging port 16 is added have the sufficient reaction time, waste water are avoided to flow directly into reaction In room 12.
In order to keep the Fenton's reaction in reaction chamber 12 more abundant, in the present embodiment, ultrasonic drilling machine is additionally provided in reaction chamber Each ultraviolet light device of structure (not marking in figure), ultrasonic synergistic ultraviolet catalytic Fenton's reaction have stronger catalytic action.
It is 21 structure of mill weir slot at the top of sedimentation basin 20, for by treated, waste water to be arranged by way of covering mill weir slot 21 Out;20 bottom of sedimentation basin is conical bottom, and the precipitating generated is made to slide into bottom, then the sewage draining exit (not marking in figure) for passing through bottom Discharge.
The utility model provides a kind of Fenton light electrolysis oxidation treatment device, and Fenton's reaction pond includes at the acid being sequentially communicated Room, reaction chamber and alkali process room are managed, sour process chamber is equipped with water inlet far from reaction chamber one end, sets between sour process chamber and reaction chamber There is first partition, first partition is fixedly connected with Fenton's reaction bottom of pond portion, second partition is equipped between reaction chamber and alkali process room, It is fixedly connected at the top of second partition and Fenton's reaction pond.Constitute a sinuous distribution channel in the horizontal direction, and each room it Between there are fluid communications pathways.Blower is connected to sour process chamber, reaction chamber and alkali process ceiling portion respectively by air hose, in removing The a small amount of bubble in portion.First partition is placed in reaction chamber side equipped with the first deflector of muti-piece, and second partition is placed in reaction chamber side and sets There is the second deflector of muti-piece, it is logical that the first deflector of muti-piece and the arrangement alternate with each other of the second deflector of muti-piece constitute a sinuous circulation Road, extends the length of circulation path, to achieve the effect that waste water is sufficiently reacted with Fenton reagent.
Finally it should be noted that above embodiments are only to illustrate the technical solution of the utility model, rather than to this reality With the limitation of novel protected range, although being explained in detail referring to preferred embodiment to the utility model, this field it is general Lead to it will be appreciated by the skilled person that can be with the technical solution of the present invention is modified or equivalently replaced, without departing from this The spirit and scope of utility model technical solution.

Claims (5)

1. a kind of Fenton light electrolysis oxidation treatment device, including sealing Fenton's reaction pond, sedimentation basin, air hose and blower, the sweet smell The reaction tank that pauses includes the sour process chamber, reaction chamber and alkali process room being sequentially communicated, and the acid process chamber is set far from reaction chamber one end There is water inlet, first partition is equipped between the acid process chamber and reaction chamber, the first partition and Fenton's reaction bottom of pond portion are solid Fixed connection, is equipped with second partition between the reaction chamber and alkali process room, the second partition and Fenton's reaction pond top are fixed Connection, between the alkali process room and sedimentation basin be equipped with runner pipe, the blower by air hose respectively with sour process chamber, reaction chamber It is connected to alkali process ceiling portion, which is characterized in that
The first partition is placed in reaction chamber side equipped with the first deflector of muti-piece;
The second partition is placed in reaction chamber side equipped with the second deflector of muti-piece;
First deflector of muti-piece and the arrangement alternate with each other of the second deflector of muti-piece constitute a sinuous distribution channel.
2. Fenton light electrolysis oxidation treatment device as described in claim 1, which is characterized in that the second partition bottom end and the One partition side wall is vertically equipped with an orifice plate, and first deflector and the second deflector are placed in orifice plate top.
3. Fenton light electrolysis oxidation treatment device as described in claim 1, which is characterized in that be equipped at the top of the acid process chamber First charging port, for filling acidic materials;The second charging port, for filling Fenton reagent, institute are equipped at the top of the reaction chamber Alkali process ceiling portion is stated equipped with third charging port, for filling alkaline matter.
4. Fenton light electrolysis oxidation treatment device as described in claim 1, which is characterized in that the water inlet is placed in sour processing Room bottom.
5. Fenton light electrolysis oxidation treatment device as described in claim 1, which is characterized in that be mill weir at the top of the sedimentation basin Slot structure, the precipitating bottom of pond portion are conical bottom.
CN201821008663.8U 2018-06-28 2018-06-28 Fenton light electrolysis oxidation treatment device Active CN208617442U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201821008663.8U CN208617442U (en) 2018-06-28 2018-06-28 Fenton light electrolysis oxidation treatment device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201821008663.8U CN208617442U (en) 2018-06-28 2018-06-28 Fenton light electrolysis oxidation treatment device

Publications (1)

Publication Number Publication Date
CN208617442U true CN208617442U (en) 2019-03-19

Family

ID=65703935

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201821008663.8U Active CN208617442U (en) 2018-06-28 2018-06-28 Fenton light electrolysis oxidation treatment device

Country Status (1)

Country Link
CN (1) CN208617442U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113786650A (en) * 2021-09-18 2021-12-14 江苏环川环境工程有限公司 Low-energy-consumption aeration high-efficiency reaction clarification tank

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113786650A (en) * 2021-09-18 2021-12-14 江苏环川环境工程有限公司 Low-energy-consumption aeration high-efficiency reaction clarification tank

Similar Documents

Publication Publication Date Title
CN101331087B (en) Electrolytic sterilizing apparatus for ship ballast water
CN102976451A (en) Wastewater treatment device and method for in-situ electric generation of H2O2 cooperating with O3 oxidation
CN108358363A (en) A kind of deep treatment method of organic sewage with high salt
CN202246327U (en) Improved electric Fenton wastewater treatment equipment
CN110240331B (en) Method and system for performing biogas desulfurization by using electrolysis and air flotation to treat biogas slurry
CN208617442U (en) Fenton light electrolysis oxidation treatment device
CN203319806U (en) Electrolysis dephosphorization device for treating domestic sewage
CN205473096U (en) Sour mother liquor effluent disposal system of purple urea
CN205387492U (en) Organic pollutant's device in optical electro -Chemistry concerted catalysis degradation waste water
CN104355467A (en) Circulating cooling water filling purification system
CN205313292U (en) Middle -size and small -size energy -conserving cooling circulating water treatment system
CN104743702B (en) One way of life sewage disposal adjusting means
CN205556329U (en) Swimming pool circulating water electrolysis type purifier
CN205313290U (en) Cooling circulating water treatment system that can reequip on line
CN108455711A (en) Circulating water sterilizing electrolytic descaling system
CN108002489B (en) Pool type electrochemical water treatment device and method
CN104692496B (en) Organic pollution wastewater treatment system and method in environmental emergent accidents
CN210505889U (en) System for performing biogas desulfurization by using electrolysis and air flotation biogas slurry treatment
CN212127829U (en) Reverse osmosis concentrate electrolytic recovery device
CN203728621U (en) Iron-carbon internal electrolysis and external electrolysis combined wastewater treatment device
KR100556291B1 (en) Electric-Chemical Processing Apparatus for Waste Water
CN110204016A (en) A kind of system and method for ammonia-containing water electrolysis unit pickling
CN104591351A (en) Ionic exchange membrane electrolytic cell device for treating chemical production wastewater
CN111747492A (en) Laboratory waste liquid electrolysis device and electrolysis method
CN204474380U (en) A kind of electrolysis with ion-exchange film slot device processing chemical production wastewater

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant