CN213950857U - Wastewater treatment device for ozone coupling three-dimensional electrocatalytic oxidation - Google Patents
Wastewater treatment device for ozone coupling three-dimensional electrocatalytic oxidation Download PDFInfo
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- CN213950857U CN213950857U CN202022655925.3U CN202022655925U CN213950857U CN 213950857 U CN213950857 U CN 213950857U CN 202022655925 U CN202022655925 U CN 202022655925U CN 213950857 U CN213950857 U CN 213950857U
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Abstract
The utility model discloses a waste water treatment device and method of three-dimensional electrocatalytic oxidation of ozone coupling, including the reaction tower, three-dimensional electro-catalytic device is equipped with in the reaction tower, and the reaction tower inner chamber at three-dimensional electro-catalytic device place has constituted the electrolytic bath, is equipped with ozone catalytic device in the reaction tower of three-dimensional electro-catalytic device below, and ozone catalytic device includes ozone generator and the ozone catalyst layer and the aeration equipment of dress in the reaction tower, and the ozone catalyst layer is established in aeration equipment's top, and aeration equipment passes through the admission line and is connected with ozone generator. The utility model discloses with ozone catalytic oxidation and three-dimensional electro-catalysis coupling in an oxidation tower for the waste water oxidation of extremely difficult degradation is more abundant, with make full use of the oxygen behind the ozone oxidation, has greatly improved electro-catalysis efficiency, makes waste water oxidation more thorough, easy operation, and easily control takes up an area of fewly, has reduced manufacturing cost and running cost again.
Description
Technical Field
The utility model relates to an industrial water treatment technology, in particular to a wastewater treatment device of ozone coupling three-dimensional electrocatalytic oxidation.
Background
The advanced oxidation water treatment technology has excellent mineralization effect on organic pollutants in the industrial wastewater difficult to degrade, such as ozone oxidation technology, electrochemical technology, photocatalytic technology and the like, and mainly utilizes hydroxyl radicals (.OH E) generated in the system0=2.8 eV vs SHE), ozone (O)3 E0Strong oxidizing agents such as =2.07 eV vs SHE) oxidize or mineralize organic pollutants into harmless substances. The advanced oxidation water treatment technology can be used independently or in a coupling way, and can also be used as a pretreatment technology of biochemical treatment engineering.
The ozone oxidation technology for degrading organic pollutants mainly realizes (1) direct oxidation degradation of organic pollutants by electrophilic attack of ozone molecules in acidic solution through two ways; (2) ozone molecules in the more basic solution undergo self-decomposition, generating hydroxyl radicals (. OH), thereby mineralizing the organic pollutants. But the ozone oxidation has certain selectivity, a plurality of intermediate products and high energy consumption in the oxidation process, and the oxygen with higher content in the ozone gas is completely wasted.
Under the action of current, the surface of the electrode undergoes redox reaction, and in the process, strong-oxidizing free radicals are generated to mineralize organic matters, so that other chemical reagents are not needed, the device is simple and easy to operate, and the device is widely applied to organic waste water which is difficult to degrade. However, electrochemical techniques also have some drawbacks: (1) the treatment efficiency of the wastewater is limited to a certain extent by current and mass transfer; (2) the device for treating the wastewater has smaller relative scale, the electrode material often contains noble metal, the service life is limited, the price is high, and the wastewater treatment cost is increased.
SUMMERY OF THE UTILITY MODEL
The utility model aims to solve the technical problem that to prior art not enough, provide a reasonable in design, with make full use of oxygen and remaining ozone after the ozone oxidation, greatly improved electrocatalysis efficiency, make the waste water treatment plant of the three-dimensional electrocatalysis oxidation of ozone coupling of waste water oxidation more thorough.
In order to achieve the above purpose, the utility model adopts the following technical scheme:
a wastewater treatment device of ozone coupling three-dimensional electrocatalytic oxidation is characterized by comprising a reaction tower, wherein the lower part of the reaction tower is provided with a water inlet, the upper part of the reaction tower is provided with an exhaust port and an overflow port, a three-dimensional electrocatalytic device is arranged in the reaction tower, an inner cavity of the reaction tower where the three-dimensional electrocatalytic device is positioned forms an electrolytic cell, an ozone catalytic device is arranged in the reaction tower below the three-dimensional electrocatalytic device,
the ozone catalytic device comprises an ozone generator, an ozone catalyst layer and an aeration device, wherein the ozone catalyst layer and the aeration device are arranged in the reaction tower, the ozone catalyst layer is arranged above the aeration device, and the aeration device is connected with the ozone generator through an air inlet pipeline.
The utility model aims to solve the technical problem can also be realized through following technical scheme, three-dimensional electro-catalysis device is including establishing electrode and the electrochemical catalyst layer in the reaction tower, and the electrode cartridge is in the electrochemical catalyst in situ, the electrode is equipped with two, and one is the positive pole, and one is the negative pole, and each utmost point is equipped with a plate electrode at least, and homopolar polylith plate electrode closely arranges, and the total width of plate electrode is 0.6 one 0.8 times of tower internal diameter, and plate electrode length exceeds catalyst layer height and goes out 10 one 15CM, and the plate electrode is 0.3 one 0.4 times distance of tower internal diameter apart from the tower center.
The utility model discloses the technical problem that solve can also be realized through following technical scheme, be equipped with the column plate that is used for laying ozone catalyst or electrochemical catalyst in the reaction tower, the column plate top is equipped with the clamp plate, has constituted the space that is used for filling ozone catalyst or electrochemical catalyst between column plate, clamp plate and the reaction tower lateral wall, is fixed with the overlap joint piece that supports column plate or clamp plate on the reaction tower lateral wall.
The technical problem to be solved by the utility model can also be realized by the following technical proposal, the upper part of the reaction tower is provided with a return port, the return port is connected with a return pipeline, the water outlet end of the return pipeline is connected with a water distributor arranged below the ozone catalyst layer through a sewage pump, the return pipeline is provided with a return valve, the water inlet end of the sewage pump is also connected with a water inlet pipeline, the water inlet pipeline is provided with a sewage regulating valve,
the water outlet of the overflow port is treated water, if the water outlet is unqualified in detection, the water inlet pipeline can be closed, the return valve is fully opened, and sewage forms self circulation through the sewage pump until the water outlet is qualified.
The utility model discloses the technical problem that will solve can also be realized through following technical scheme install fluidflowmeter on the backflow pipeline.
The utility model discloses the technical problem that will solve can also be realized through following technical scheme install gas flowmeter on the admission line.
Compared with the prior art, the utility model discloses possess following advantage:
1) the multi-electrode catalytic oxidation and the ozone catalytic oxidation are combined, and oxygen and residual ozone generated by the ozone catalytic oxidation are further subjected to electrocatalytic oxidation while the ozone catalytic oxidation is carried out, so that organic matters difficult to degrade are more thoroughly and completely mineralized;
2) because the device does not generally produce precipitates in the oxidation process and the gas produced by the device has the air flotation function, even a small amount of precipitates can be discharged along with the wastewater;
3) oxygen generated by catalytic oxidation of ozone is utilized in electrocatalytic oxidation, and the oxygen and the electrocatalytic oxidation are cooperated, so that the efficiency is improved, and substances and energy are fully utilized;
4) the graphite electrode is adopted as the electrode, so that the cost is low and the service life is long;
5) the reaction device is integrated, the operation is simple, the occupied area is small, the device is movable, the investment is low, and the operating cost is low;
6) the wastewater treatment has wide application range, is particularly suitable for high-concentration refractory wastewater, can be matched with advanced treatment, and oxygen generated by tail gas can be used for aerobic biochemical treatment or oxygen-enriched ozone preparation.
Drawings
FIG. 1 is a schematic diagram of a wastewater treatment apparatus according to the present invention;
FIG. 2 is a cross-sectional view of a reaction column in which a three-dimensional electrocatalytic device is located.
In the figure: 1-a reaction tower, 2-an electrochemical catalyst, 3-an electrode, 4-an ozone catalyst, 5-a water distributor, 6-an aeration device, 7-an overflow port, 8-an exhaust port, 9-a return port, 10-a power supply, 11-a gas flowmeter, 12-an ozone generator, 13-a liquid flowmeter, 14-a return valve, 15-a sewage pump, 16-a sewage regulating valve and 17-a water inlet pipeline.
Detailed Description
The technical solutions in the embodiments of the present invention will be described clearly and completely with reference to the accompanying drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only some embodiments of the present invention, not all embodiments.
In the description of the present invention, it is to be understood that the terms "upper", "lower", "front", "rear", "left", "right", "top", "bottom", "inner", "outer", and the like indicate orientations or positional relationships based on the orientations or positional relationships shown in the drawings, and are only for convenience of description and simplicity of description, and do not indicate or imply that the device or element being referred to must have a particular orientation, be constructed and operated in a particular orientation, and therefore, should not be construed as limiting the present invention.
Referring to fig. 1, the wastewater treatment device of ozone coupling three-dimensional electrocatalytic oxidation comprises a reaction tower 1, a water inlet is arranged at the lower part of the reaction tower, an exhaust port 8 and an overflow port 7 are arranged at the upper part of the reaction tower 1, a three-dimensional electrocatalytic device is arranged in the reaction tower 1, an electrolytic cell is formed in the inner cavity of the reaction tower 1 where the three-dimensional electrocatalytic device is positioned, an ozone catalytic device is arranged in the reaction tower 1 below the three-dimensional electrocatalytic device,
the ozone catalytic device comprises an ozone generator 12, an ozone catalyst layer 4 and an aeration device 5, wherein the ozone catalyst layer 4 and the aeration device 5 are arranged in the reaction tower 1, the ozone catalyst layer 4 is arranged above the aeration device 5, the aeration device 5 is connected with the ozone generator 12 through an air inlet pipeline, the aeration device is provided with an aeration disc arranged along the circumferential direction of the reaction tower, the aeration disc is provided with a plurality of nano-scale aeration micropores, and the air inlet pipeline is provided with a gas flowmeter 11.
The three-dimensional electro-catalysis device comprises an electrode 3 and an electrochemical catalyst layer 2 which are arranged in a reaction tower 1, the electrode 3 is inserted in the electrochemical catalyst layer 2, the electrode 3 is electrically connected with a power supply 10 arranged outside the reaction tower, the power supply adopts a direct current power supply, the electrode is a graphite electrode, two electrodes are arranged, one electrode is a positive electrode, the other electrode is a negative electrode, the positive electrode and the negative electrode are opposite, each electrode is at least provided with an electrode plate, a plurality of electrode plates with the same electrode are closely arranged, the total width of the electrode plates is 0.6-0.8 time of the inner diameter of the tower, the length of the electrode plates is 10-15 CM higher than that of the catalyst layer, the distance between the electrode plates and the center of the tower is 0.3-0.4 time of the inner diameter of the tower, the cost is low, the service life is long, and the electrochemical catalyst is a columnar material prepared by compounding activated carbon and a plurality of metal oxides.
A tower plate for placing the ozone catalyst or the electrochemical catalyst is arranged in the reaction tower 1, a pressure plate is arranged above the tower plate, a space for filling the ozone catalyst or the electrochemical catalyst is formed among the tower plate, the pressure plate and the side wall of the reaction tower, and a lapping block for supporting the tower plate or the pressure plate is fixed on the side wall of the reaction tower 1.
1 upper portion of reaction tower is equipped with backward flow mouth 9, and backward flow mouth 9 department is connected with the backflow pipeline, and backflow pipeline goes out the water end and passes through sewage pump 15 and be connected with the water-locator 5 of establishing below the ozone catalyst layer, installs backflow valve 14 on the backflow pipeline, sewage pump 15's the end of intaking still is connected with inlet channel 17, installs sewage governing valve 16 on the inlet channel install fluidflowmeter 13 on the backflow pipeline, and the water-locator is the titanium alloy coil pipe, and it has a plurality of apopores to open on the coil pipe.
The device is made of a glass fiber reinforced plastic shell with a PTFE lining, wherein the PTFE gaskets are all PTFE gaskets, and the micro-pore aeration and water distributor are all titanium alloy; the gas flow rate and the liquid flow rate can be adjusted according to the water quality condition of the wastewater and the water outlet requirement, the application range is wide, and the operation elasticity is high; the direct current intensity is controlled at 5-25mA/cm2The voltage control band is within 48V, so that the operation is safe and easy to control; the device can be used for industrial wastewater with the salt content within 1.5 percent.
A wastewater treatment method of ozone coupling three-dimensional electrocatalytic oxidation adopts the wastewater treatment device, and comprises the following steps,
(1) injecting wastewater into the reaction tower through a sewage pump, adjusting the flow through a liquid flowmeter, and uniformly entering the reaction tower through a water distributor;
(2) when the wastewater is immersed in the ozone catalyst layer, starting the ozone generator, sending the ozone with the concentration of 80-150mg/L into the reaction tower, and starting aeration through the aeration device;
(3) when the wastewater overflows from the overflow outlet, the direct current power supply is switched on, and the current intensity between the electrode plates is controlled to be 5-25mA/cm2The power supply voltage is 12-48v, and the waste water is subjected to electrooxidation treatment;
(4) the sewage regulating valve is used for regulating the water inlet flow, the return valve is used for regulating the water return flow, the detection index of the outlet water meets the water outlet requirement, the gas flowmeter is regulated to balance the gas, and the tail gas containing oxygen is introduced into the oxidation pond of the biochemical system.
The upper part of the reaction tower is mainly provided with a three-dimensional electro-catalytic device, and the lower part of the reaction tower is mainly provided with an ozone catalytic device. The utility model is simple in operation, easily control, with ozone catalytic oxidation and three-dimensional electro-catalysis coupling in an oxidation tower for the waste water oxidation of extremely difficult degradation is more abundant, with make full use of the oxygen behind the ozone oxidation, greatly improved electro-catalysis efficiency, make waste water oxidation more thorough, but wide application in industrial waste water nursing field, integrated device takes up an area of fewly, manufacturing cost and running cost have been reduced again, the current intensity control between the electrode plate is at 5-25mA/cm2The operation voltage control band is within 48V, so that the operation is safe and easy to control. The device can be used for industrial wastewater with the salt content within 1.5 percent.
The above, only be the concrete implementation of the preferred embodiment of the present invention, but the protection scope of the present invention is not limited thereto, and any person skilled in the art is in the technical scope of the present invention, according to the technical solution of the present invention and the utility model, the concept of which is equivalent to replace or change, should be covered within the protection scope of the present invention.
Claims (8)
1. The utility model provides a waste water treatment device of three-dimensional electrocatalytic oxidation of ozone coupling which characterized in that: comprises a reaction tower, a water inlet is arranged at the lower part of the reaction tower, an exhaust port and an overflow port are arranged at the upper part of the reaction tower, a three-dimensional electro-catalysis device is arranged in the reaction tower, an ozone catalysis device is arranged in the reaction tower below the three-dimensional electro-catalysis device,
the ozone catalytic device comprises an ozone generator, an ozone catalyst layer and an aeration device, wherein the ozone catalyst layer and the aeration device are arranged in the reaction tower, the ozone catalyst layer is arranged above the aeration device, and the aeration device is connected with the ozone generator through an air inlet pipeline.
2. The ozone-coupled three-dimensional electrocatalytic oxidation wastewater treatment device as recited in claim 1, wherein the three-dimensional electrocatalytic oxidation wastewater treatment device comprises electrodes and an electrochemical catalyst layer, the electrodes are arranged in the reaction tower, the electrodes are inserted into the electrochemical catalyst layer, and the electrodes are electrically connected with a power supply arranged outside the reaction tower.
3. The ozone-coupled three-dimensional electrocatalytic oxidation wastewater treatment device as set forth in claim 2, wherein said electrodes are provided in two, one being a positive electrode and one being a negative electrode, each of which is provided with at least one electrode plate.
4. The ozone-coupled three-dimensional electrocatalytic oxidation wastewater treatment device as set forth in claim 3, wherein the total width of the electrode plate is 0.6-0.8 times the inner diameter of the tower, the length of the electrode plate is 10-15 CM higher than that of the catalyst layer, and the distance from the electrode plate to the center of the tower is 0.3-0.4 times the inner diameter of the tower.
5. The wastewater treatment device for ozone-coupled three-dimensional electrocatalytic oxidation as claimed in claim 1 or 2, wherein a tower plate for placing an ozone catalyst or an electrochemical catalyst is arranged in the reaction tower, a pressure plate is arranged above the tower plate, a space for filling the ozone catalyst or the electrochemical catalyst is formed among the tower plate, the pressure plate and the side wall of the reaction tower, and a lapping block for supporting the tower plate or the pressure plate is fixed on the side wall of the reaction tower.
6. The ozone-coupled three-dimensional electrocatalytic oxidation wastewater treatment device as claimed in claim 1, wherein a reflux port is arranged at the upper part of the reaction tower, a reflux pipeline is connected to the reflux port, the water outlet end of the reflux pipeline is connected with a water distributor arranged below the ozone catalyst layer through a sewage pump, and a reflux valve is arranged on the reflux pipeline.
7. The ozone-coupled three-dimensional electrocatalytic oxidation wastewater treatment device as claimed in claim 6, wherein a water inlet pipeline is further connected to the water inlet end of the sewage pump, and a sewage regulating valve is mounted on the water inlet pipeline.
8. The wastewater treatment device for ozone-coupled three-dimensional electrocatalytic oxidation as set forth in claim 6 or 7, wherein a liquid flow meter is installed on said return pipe, and a gas flow meter is installed on said gas inlet pipe.
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| Application Number | Priority Date | Filing Date | Title |
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| CN202022655925.3U CN213950857U (en) | 2020-11-17 | 2020-11-17 | Wastewater treatment device for ozone coupling three-dimensional electrocatalytic oxidation |
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| Application Number | Priority Date | Filing Date | Title |
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| CN202022655925.3U CN213950857U (en) | 2020-11-17 | 2020-11-17 | Wastewater treatment device for ozone coupling three-dimensional electrocatalytic oxidation |
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| CN202022655925.3U Active CN213950857U (en) | 2020-11-17 | 2020-11-17 | Wastewater treatment device for ozone coupling three-dimensional electrocatalytic oxidation |
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