CN1526652A - Continuous circular flow-type optoelectric catalytic fixed bed reactor with 3D electrodes and its organic sewage treating method - Google Patents
Continuous circular flow-type optoelectric catalytic fixed bed reactor with 3D electrodes and its organic sewage treating method Download PDFInfo
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Abstract
The continuous circular flow-type optoelectric catalytic fixed bed reactor has structure including casing, microporous titanium plate cathode, porous titanium ring anode, double-layer U-shaped quartz tube, UV lamp inside the U-tube as light source, optoelectric catalytic reaction chamber formed between the cathode and the anode, fixed bed 3D particle electrode set inside the reaction chamber and formed via painting nano TiO2 onto SiO2 particle, and continuous circulating unit comprising liquid storage and pump connected between the liquid inlet and liquid outlet of the reaction chamber. The present invention also provides the method and technological conditions of treating organic sewage with the reactor. Inside the reactor, voltage higher than the oxidation potential of the pollutant is applied to raise the photocatalytic and eletrocatalytic oxidation efficiency.
Description
Technical Field
The invention relates to a continuous circulating flow type fixed bed three-dimensional electrode photoelectrocatalysis reactor for treating organic wastewater and a method for treating organic wastewater by using the same.
Technical Field
Although there are many patents on heterogeneous photocatalytic technology, the application of heterogeneous photocatalysis to the actual wastewater treatment is not very common due to the rapid recombination of photogenerated electrons and holes. Therefore, in order to actually realize the practical industrial application of heterogeneous photocatalytic treatment of organic wastewater, the inhibition of the recombination of photogenerated electrons and holes is one of the key problems that must be solved for improving the photocatalytic efficiency. For this reason, many methods for improving the photocatalytic efficiency have been proposed in recent years, such as noble metal deposition on the surface of a semiconductor, metal ion doping, or addition of aninorganic co-adsorbent and application of an anodic bias voltage, etc., of which the bias voltage method is most attractive. The photoelectrochemical technology of the external bias voltage is that an anode bias voltage is applied to a photoelectric electrode, so that a potential gradient is formed in the electrode, and photo-generated electrons and holes move in opposite directions respectively, so that the recombination rate of the holes and the photo-generated electrons can be greatly reduced under certain conditions, and the external electric field enhancement effect of the photocatalysis efficiency is greatly improved. CN1377728 discloses the invention named "three-phase three-dimensional electrode reactor", this invention combines three-dimensional electrode reactor and photocatalytic reactor to form the photoelectric reactor, is used for handling organic waste water, but because this reactor only combines three-dimensional electrode (active carbon is the packing particle) and TiO2 suspended state photocatalytic reactor of the upper half, light, electric synergy is poor, has influenced the treatment effect to organic waste water. And the treatment efficiency of the wastewater is not high due to the limited contact area and contact time of the wastewater with the electrocatalyst in the reactor.
Disclosure of Invention
The invention aims to provide a continuous circulating flow type fixed bed three-dimensional electrode photoelectrocatalysis reactor which can fully exert the efficiency of light and electricity synergistic catalytic oxidation, and also provides a method for treating organic wastewater by using the photoelectrocatalysis reactor to obtain higher treatment efficiency.
The invention relates to a continuous circulating flow type fixed bed three-dimensional electrode photoelectrocatalysis reactor, which comprises a reactor shell, a microporous titanium plate cathode, a porous titanium ring anode, a double-layer U-shaped quartz tube and a light source UV lamp arranged in the double-layer U-shaped quartz tube, wherein the microporous titanium plate cathode is positioned at the lower part of the shell, an air chamber is formed between the microporous titanium plate cathode and the bottom of the shell and provided with an air inlet, the porous titanium ring anode is positioned at the upper part of the shell, a photoelectrocatalysis reaction chamber is formed between the microporous titanium plate cathode and the porous titanium ring anode, a liquid inlet is arranged at the lower part of the reactor, a liquid outlet is arranged at the upper part of the reactor, the double-layer U-shaped quartz tube anda direct current power supply is connected between the electrode and the porous titanium ring anode, and the device is characterized in that a fixed bed three-dimensional particle electrode is arranged in the photoelectrocatalysis reaction chamber, and the fixed bed three-dimensional particle electrode is made of nano TiO2Coating on SiO2The particle is formed on the reaction chamber, and a continuous circulating device consisting of a liquid storage device and a pump is connected between a liquid inlet and a liquid outlet of the reaction chamber.
The method for treating organic wastewater by using the continuous circulation flow type fixed bed three-dimensional electrode photoelectrocatalysis reactor comprises the steps of loading organic wastewater to be treated into a liquid storage device, stirring the organic wastewater by using a stirrer arranged in the liquid storage device, turning on a UV lamp (ultraviolet lamp) in the photoelectrocatalysis reactor, starting an air compressor to introduce compressed air from an air inlet, adjusting the air flow, switching on a direct current power supply to apply voltage to a microporous titanium plate cathode and a porous titanium ring anode, starting a pump in a continuous circulation device, pumping the wastewater to be treated in the liquid storage device into a reaction chamber, performing photoelectrocatalysis reaction from bottom to top in the reaction chamber, and then circularly flowing back to the liquid storage device to perform a continuous circulation process. The method of the invention has the following technical conditions for carrying out reaction treatment on the organic wastewater: reactor with a reactor shellThe voltage between the microporous titanium plate cathode (9) and the porous titanium ring anode (14) is 10-30V, the air flow rate is 0.025-0.075 MPa, and Cl-containing solution can be added into the reaction solution in the reaction-An electrolyte, and the concentration of the electrolyte is maintained at 200 to 1000 mmol/L.
The invention has the following outstanding characteristics and beneficial effects:
(1) the photoelectric reactor combines a three-dimensional electrode with a fixed bed photocatalytic reactor to establish a continuous circulating flow type three-dimensional electrode-fixed bed photoelectric catalytic reactor, and sufficiently volatilizes the efficiency of the light and electricity cooperative catalytic oxidation by applying higher voltage exceeding the oxidation potential of pollutants; due to the use of TiO2The coated quartz sand is used as filling particles, and the particle electrode in the three-dimensional electrode and the photocatalyst in the photocatalysis are integrated, so that the manufacturing cost of the reactor is greatly saved, and the reaction efficiency is greatly improved.
(2) The reactor adopts a continuous circulating flow mode for wastewater, and greatly increases the contact area and the contact time of the wastewater and the photoelectric catalyst, thereby reducing the mass transfer effect of the wastewater in the fixed bed reactor and greatly improving the wastewater removal efficiency of the photoelectric catalytic reactor.
(3) In the organic wastewater treatment method of the present invention, inorganic Cl-Ions are, on the one hand, supporting electrolytes for electrochemical reactions, but may have some toxicity to photocatalysts. Therefore, it is a considerable problem to understand the influence of inorganic ions on the photoelectrocatalytic reaction. The efficiency of photoelectrocatalysis degradation is effectively improved by applying higher voltage and adding a large amount of dielectric NaCl. So that the voltage in the photoelectrocatalysis reactor can not only capture photoproduction electrons through the anode, inhibit the recombination of the photoproduction electrons and high-energy holes and improve the efficiency of the photoelectrocatalysis reaction. Meanwhile, the degradation efficiency of organic pollutants can be improved through electrochemical oxidation. More importantly, the invention can effectively improve the efficiency of photoelectrocatalysis degradation by adding a large amount of dielectric NaCl, namely when the concentration of NaCl is higher, Cl in the solution-After two equilibria of competitive adsorption and hole recombination are achieved, excessive Cl is contained in the solution-The ions can be used as supporting electrolyteThe substance enhances the electron transfer of the solution, thereby enhancing the capture effect of the external electric field on the photo-generated electrons. Meanwhile, the following main reactions also exist in the solution to greatly improve the efficiency of the photoelectrocatalysis reaction:
drawings
FIG. 1 is a schematic structural view of one embodiment of a continuous circulation flow type fixed bed three-dimensional electrode photoelectrocatalysis reactor of the present invention;
FIG. 2 is a comparison of the removal of reactive brilliant orange K-R using the method of the present invention (photo-catalysis) and other methods (photo-catalysis, electro-oxidation, adsorption);
FIG. 3 is a comparison of quinoline removal using the method of the present invention (photo-catalysis) and other methods (photo-catalysis, electro-oxidation, adsorption);
FIG. 4 is a graph showing the comparison of TOC removal rate in degrading reactive brilliant orange K-R using the method of the present invention (photo-electro-catalysis) and other methods (photo-catalysis, electro-oxidation);
FIG. 5 is a graph showing the effect of chloride ion concentration on the photoelectrocatalytic degradation of reactive brilliant orange K-R;
FIG. 6 is a graph showing the effect of chloride ion concentration on quinoline degradation.
Detailed Description
As shown in figure 1, the continuous circulation flow type fixed bed three-dimensional electrode photoelectrocatalysis reactor consists of a flow type photoelectrocatalysis reactor 1 and a liquid storage device 5, the reactor consists of a hard glass outer sleeve 12 and a base 7 made of a PVC plate to form a reactor shell, the lower part of the reactor is provided with a microporous titanium plate cathode 9, and the reactor is provided with a titanium plate cathodeThe cathode of the microporous titanium plate is provided with micropores with the aperture smaller than 40 mu m and is used as a gas distribution plate, a gas chamber 8 is formed between the cathode and the bottom of the shell, the gas chamber is provided with a gas inlet 6, the upper part of the reactor is provided with a porous titanium ring anode 13, a reaction chamber is formed between the porous titanium ring anode 13 and the microporous titanium plate cathode 9, a double-layer U-shaped quartz tube 14 with a 500W ultraviolet lamp 2 arranged therein is vertically arranged in the reaction chamber, the double-layer U-shaped quartz tube is introduced with cooling water through a water inlet and a water outlet (17 and 18) to keep the temperature of the solution in the reactor, and the reaction chamber between the porous titanium ring anode and the microporous titanium plate cathode is filled with nano TiO2The quartz sand 10 is used as a photocatalyst in a fixed bed photocatalytic reactor, a direct current power supply 3 is connected between a porous titanium ring anode and a microporous titanium plate cathode, and when voltage is applied to electrodes in the reaction process, photocatalyst particles of the fixed bed form a three-dimensional electrode, namely, a particle electrode in a three-dimensional electrode electrochemical reactor, namely, the photoelectrochemical reactor is a coupling body of the fixed bed photocatalytic reactor and the three-dimensional electrode electrochemical reactor. A liquid inlet 15 is arranged at the lower part of the reaction chamber, a liquid outlet 16 is arranged at the upper part of the reactor (above the porous titanium ring anode 13), a continuous circulating device consisting of a liquid storage device 5 and a pump 4 is connected between the liquid inlet 15 and the liquid outlet 16, and a stirrer 11 is arranged in the liquid storage device 5.
Example one
The continuous circulating flow type fixed bed three-dimensional electrode photoelectrocatalysis reactor of the invention is used for treating the wastewater with the pH value of 5.6 of 0.5mmol/LThe active dye waste liquid is at 30.0V voltage and 0.05MPa air flow rate, and the electrolyte Cl-Under the condition that the concentration is 0.5mol/L, the removal rate of the reactive dye is 96 percent when the photoelectrocatalysis reaction is carried out for 60min, which is higher than 70 percent and 77 percent when only the photoelectrocatalysis and the electrochemical oxidation are carried out; the TOC change and the degradation rate of the reactive dye in the degradation process have similar change trends! Namely, the TOC removal rate of the reactive dye solution is 61% when the photoelectrocatalysis reaction is carried out for 150min, which is higher than 49% and 17% of the TOC removal rate only in photocatalysis and electrochemical oxidation;
example two
The invention relates to a continuous circulating flow type fixed bed three-dimensional electrode photoelectrocatalysis reactorTreating 0.25mmol/L quinoline solution with pH of 6.8 at 30.0V voltage and air flow rate of 0.075MPa and Cl electrolyte-Under the condition that the concentration is 0.5mol/L, the removal rate of quinoline is 73 percent when the photoelectrocatalysis reaction is 60min, which is higher than 52 percent and 26 percent when only in photocatalysis and electrochemical oxidation; the quinoline removal rate increased to over 93% when the photoelectrocatalytic reaction was 120min, but was also higher than 71% and 38% when only photocatalytic and electrochemical oxidation were used; the TOC changes in the degradation process of quinoline and the degradation rate thereof have similar trend! Namely, the TOC removal rate of the quinoline solution is 41% when the photoelectrocatalysis reaction is carried out for 60min, which is higher than38% and 7% of the TOC removal rate only in photocatalysis and electrochemical oxidation; while the TOC removal rate of the quinoline solution at 100min of the photoelectrocatalytic reaction was 53%, which was higher than 43% and 9% of the TOC removal rate only at the photocatalysed and electrochemical oxidation.
EXAMPLE III
The continuous circulating flow type fixed bed three-dimensional electrode photoelectrocatalysis reactor is used for treating 0.5mmol/L active dye waste liquid with pH value of 5.6 at the air flow rate of 0.05MPa and the electrolyte Cl-Under the condition that the concentration is 0.5mol/L and the voltage is 10V, the removal rate of the reactive dye is 84 percent when the photoelectrocatalysis reaction is carried out for 60min, and the removal rate of the reactive dye is 96 percent when the voltage is increased to 30V and the photoelectrocatalysis reaction is carried out for 60 min. The degradation rate of the reactive dye is also 0.0300min at 10V voltage-1Increase to 0.0539min of 30V-1. During the degradation process of quinoline, the degradation rate and the degradation rate of quinoline have similar change trend with that of the reactive dye! When the continuous circulating flow type fixed bed three-dimensional electrode photoelectrocatalysis reactor of the invention is used for treating 0.25mmol/L quinoline solution with pH value of 6.8, the air flow rate is 0.05MPa, and the electrolyte Cl-Under the condition that the concentration is 0.5mol/L and the voltage is 10V, the removal rate of quinoline is 75% when the photoelectrocatalysis reaction is 120min, and the removal rate of quinoline is 96% when the voltage is increased to 30V and the photoelectrocatalysis reaction is 120 min. The degradation rate of quinoline also ranged from 0.0116min at 10V-1Increasing to 0.0267min at 30V-1。
Example four
Inorganic anions, e.g. Cl-、SO4 2-、PO4 3-The components are common components in industrial and agricultural wastewater, and the existence of the components generally has adverse effect on the photocatalytic technology. However, the photoelectrocatalysis reactor is used for common photocatalysis quenching ion Cl-Not only has good anti-toxin effect, but also can be added with quenching ions Cl-The efficiency of the photoelectrocatalysis reaction is effectively improved. And the increase of the concentration of chloride ions in the solution has a promoting effect on the photoelectric catalytic oxidation efficiency. When the continuous circulating flow type fixed bed three-dimensional electrode photoelectrocatalysis reactor is used for treating 0.5mmol/L active brilliant orange K-R solution with pH value of 5.6, the voltage is 30.0V and the voltage is 0.05When Cl is generated under the condition of MPa air flow rate-When the concentration is 0.2mol/L, the removal rate of reactive brilliant orange K-R is increased to more than 92% from 84% after reaction for 60min, and the corresponding kinetic rate constant is formed by Cl-0.0208min at 0-1The increase was 0.0404min-1(ii) a When Cl is present-When the concentration is increased to 1mmol/L, the removal rate of reactive brilliant orange K-R is increased to more than 98 percent from the original 84 percent after reaction for 60min, and the degradation rate constant is also changed from Cl-0.0208 increase at 0 to 0.0805min-1。
EXAMPLE five
When the continuous circulating flow type fixed bed three-dimensional electrode photoelectrocatalysis reactor is used for treating 0.25mmol/L quinoline solution with pH value of 6.8, Cl is generated under the conditions of 30.0V voltage and 0.05MPa air flow rate-When the concentration is 0.2mol/L, the quinoline removal rate is increased to more than 72 percent from the original 63 percent after the reaction for 120min, and the rate constant is determined by Cl-0.088min when equal to 0-1The increase is 0.0112min-1(ii) a When Cl is present-When the concentration is increased to 1mol/L, the removal rate of quinoline is increased to 98 percent from the original 63 percent after 120min of reaction, and the degradation rate constant is also changed from Cl-The increase of 0.0088 when the time is 0 is 0.0327min-1。
Claims (3)
1. A continuous circulation flow type fixed bed three-dimensional electrode photoelectrocatalysis reactor comprises a reactor shell, a microporous titanium plate cathode (9), a porous titanium ring anode (13), a double-layer U-shaped quartz tube (14) anda light source UV lamp (2) arranged in the double-layer U-shaped quartz tube, a microporous titanium plate cathode (9) is arranged at the lower part of the shell, an air chamber (8) is formed between the microporous titanium plate cathode and the bottom of the shell, the air chamber is provided with an air inlet (6), a porous titanium ring anode (13) is arranged at the upper part of the shell, a photoelectrocatalysis reaction chamber is formed between the microporous titanium plate cathode (9) and the porous titanium ring anode (13), a liquid inlet (15) is arranged at the lower part of the reactor, a liquid outlet (16) is arranged at the upper part of the reactor, the double-layer U-shaped quartz tube (14) and the light source UV lamp (2) are arranged in the reaction chamber, and a direct current power supply (3) is connected between the microporous titanium plate cathode (9) and the porous titanium ring anode (13), the light source UV lamp is characterized in that a fixed bed three-dimensional particle2Coating on SiO2The particles are arranged, and a continuous circulating device consisting of a liquid storage device (5) and a pump (4) is connected between a liquid inlet (15) and a liquid outlet (16) of the reaction chamber.
2. The method for treating organic wastewater by using the continuous circulation flow type fixed bed three-dimensional electrode photoelectrocatalysis reactor of claim 1 is as follows: loading organic wastewater to be treated into a liquid storage device, stirring by using a stirrer, then opening a UV lamp of a photoelectrocatalysis reactor, starting an air compressor to introduce compressed air from an air inlet, adjusting the air flow, switching on a direct current power supply to apply voltage to a microporous titanium plate cathode and a porous titanium ring anode, then starting a pump in a continuous circulating device, pumping the wastewater to be treated in the liquid storage device into a reaction chamber, performing photoelectrocatalysis reaction from bottom to top through the reaction chamber, then circularly flowing back to the liquid storage device, performing a continuous circulating process, and performing reaction treatment on the organic wastewater, wherein the technical conditions are as follows: voltage of 10-30V is applied between a microporous titanium plate cathode and a porous titanium ring anode of the reactor, air flow rate is 0.025-0.075 Mpa, and Cl-containing solution is added into reaction liquid in the reaction-Electrolyte, and the concentration of the electrolyte is kept between 200mM and 1000 mM.
3. The method for treating organic wastewater according to claim 2, wherein said Cl is contained-The electrolyte is NaCl.
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| CN1303257C (en) * | 2004-12-28 | 2007-03-07 | 中山大学 | Particle electrode catalyst filling for three-dimensional electrode and preparation method thereof |
| CN101224401B (en) * | 2007-10-19 | 2010-07-07 | 东华大学 | Fixed bed inhomogeneous three dimensional electrode photo electrocatalysis reactor |
| CN101785971A (en) * | 2010-04-09 | 2010-07-28 | 华中科技大学 | Photoelectrocatalysis device used for degrading gaseous-phase organic pollutant |
| CN101844849A (en) * | 2010-05-27 | 2010-09-29 | 南京工业大学 | Method for electrolysis-catalytic oxidation joint treatment on salt-containing organic wastewater |
| CN103359805A (en) * | 2013-05-14 | 2013-10-23 | 江南大学 | Electrically assisted photo-catalytic reactor for treating hardly-degradable organic wastewater |
| CN104925911A (en) * | 2015-04-29 | 2015-09-23 | 四川和鼎环保工程有限责任公司 | Dynamic electrocatalytic oxidation experiment system for sewage |
| CN106348403A (en) * | 2016-11-21 | 2017-01-25 | 北京益清源环保科技有限公司 | Modified quartz particle electrode with function of removing furan through electrocatalysis and preparation method thereof |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN1303257C (en) * | 2004-12-28 | 2007-03-07 | 中山大学 | Particle electrode catalyst filling for three-dimensional electrode and preparation method thereof |
| CN101224401B (en) * | 2007-10-19 | 2010-07-07 | 东华大学 | Fixed bed inhomogeneous three dimensional electrode photo electrocatalysis reactor |
| CN101785971A (en) * | 2010-04-09 | 2010-07-28 | 华中科技大学 | Photoelectrocatalysis device used for degrading gaseous-phase organic pollutant |
| CN101844849A (en) * | 2010-05-27 | 2010-09-29 | 南京工业大学 | Method for electrolysis-catalytic oxidation joint treatment on salt-containing organic wastewater |
| CN101844849B (en) * | 2010-05-27 | 2011-08-31 | 南京工业大学 | Method for electrolysis-catalytic oxidation joint treatment on salt-containing organic wastewater |
| CN103359805B (en) * | 2013-05-14 | 2015-05-13 | 江南大学 | Electrically assisted photo-catalytic reactor for treating hardly-degradable organic wastewater |
| CN103359805A (en) * | 2013-05-14 | 2013-10-23 | 江南大学 | Electrically assisted photo-catalytic reactor for treating hardly-degradable organic wastewater |
| CN104925911A (en) * | 2015-04-29 | 2015-09-23 | 四川和鼎环保工程有限责任公司 | Dynamic electrocatalytic oxidation experiment system for sewage |
| CN106422992A (en) * | 2016-08-22 | 2017-02-22 | 江苏金点环保科技有限公司 | Novel photoelectric joint catalysis device |
| CN106348403A (en) * | 2016-11-21 | 2017-01-25 | 北京益清源环保科技有限公司 | Modified quartz particle electrode with function of removing furan through electrocatalysis and preparation method thereof |
| CN108249545A (en) * | 2018-03-09 | 2018-07-06 | 南京大学 | A kind of photoelectricity-Fenton azo dye wastewaters treatment reactor and application method |
| CN108249545B (en) * | 2018-03-09 | 2023-12-26 | 南京大学 | photoelectric-Fenton azo dye wastewater treatment reactor and use method thereof |
| CN109928456A (en) * | 2019-04-29 | 2019-06-25 | 上海观流智能科技有限公司 | Photo catalysis reactor and photocatalysis method |
| CN109928456B (en) * | 2019-04-29 | 2023-07-28 | 上海柏中观澈智能科技有限公司 | Photocatalytic reactor and photocatalytic method |
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