CN211813791U - Organic waste water photocatalysis processing apparatus - Google Patents
Organic waste water photocatalysis processing apparatus Download PDFInfo
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- CN211813791U CN211813791U CN201922002999.4U CN201922002999U CN211813791U CN 211813791 U CN211813791 U CN 211813791U CN 201922002999 U CN201922002999 U CN 201922002999U CN 211813791 U CN211813791 U CN 211813791U
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Abstract
The utility model discloses an organic wastewater photocatalysis treatment device, which comprises a filtering system, wherein the filtering system is communicated with a sewage treatment tank; the input end of the photocatalytic reaction system is connected with the output end of the filtering system, and a lamp source is arranged in the photocatalytic reaction system; the aeration system is communicated with the photocatalytic reaction system; and a circulation line; and the operation power of the filtering system, the photocatalytic reaction system, the aeration system and the circulating pipeline is provided by a motor. The utility model discloses an organic waste water photocatalysis processing apparatus can reduce 75% with the organic pollutant in the beer waste water, makes its play water reach the one-level A standard among the pollutant discharge standard of town sewage treatment plant.
Description
Technical Field
The utility model relates to a sewage treatment technical field, more specifically the utility model relates to an organic waste water photocatalysis treatment device that says so.
Background
China is a large country for beer consumption, people increasingly use home-brewing beer machines along with the improvement of living standard, but the wastewater generated by brewing the beer is not properly treated, the wastewater generated by the beer production is medium-concentration and high-concentration organic wastewater generated in the beer production process, the wastewater is nontoxic but easily decayed, once the wastewater enters a water body, a large amount of dissolved oxygen is consumed, so that the dissolved oxygen in the water body is reduced, anaerobic microorganisms grow in a large amount, organic matters in the water are consumed, some toxic substances are generated, the water quality is deteriorated, a vicious circle is formed, the normal life of aquatic organisms is influenced, and serious harm is caused to the surrounding environment.
At present, beer wastewater is treated by an aerobic method or an anaerobic method, but the aerobic method has a large sludge production amount and high treatment cost; the anaerobic method has long process and slow reaction speed; the anaerobic-aerobic combined biological treatment technology has a good effect of removing pollutants, but the application of the anaerobic-aerobic combined biological treatment technology in sewage treatment is also limited by the high cost.
The photocatalytic oxidation technology is widely applied to various types in recent yearsAdvanced treatment of wastewater, TiO2The photocatalytic degradation can be carried out on organic pollutants, alkene, hydrocarbon, aldehyde, alcohol, aromatic compounds, organic dye, pesticide, surfactant, organic acid, toluene and other pollutants in organic matters can be degraded, the organic pollutants are decomposed into non-toxic and harmless carbon dioxide, water and other non-toxic and harmless inorganic matters, better engineering actual effect is achieved, and the photocatalytic degradation reactor has the advantages of high efficiency, simple process equipment, easily controlled reaction conditions and the like2The popularization and application of the photocatalytic material and the reactor in practice.
Therefore, how to provide a low-cost and high-efficiency organic wastewater photocatalytic treatment device is a problem to be solved urgently by those skilled in the art.
SUMMERY OF THE UTILITY MODEL
In view of this, the utility model provides an organic waste water photocatalysis processing apparatus has practiced thrift organic waste water's treatment cost at to a great extent, has improved reaction efficiency to still realize the recycle of catalyst.
In order to achieve the above purpose, the utility model adopts the following technical scheme:
an organic wastewater photocatalytic treatment device comprises
The filtering system is communicated with the sewage treatment tank;
the input end of the photocatalytic reaction system is connected with the output end of the filtering system, and a lamp source is arranged in the photocatalytic reaction system;
the aeration system is communicated with the photocatalytic reaction system;
and a circulation line;
and the operation power of the filtering system, the photocatalytic reaction system, the aeration system and the circulating pipeline is provided by a motor.
Preferably, in the above photocatalytic treatment apparatus for organic wastewater, the filtration system is an activated carbon filtration system, and the filtration system is any one of a fixed bed adsorber, a moving bed adsorber, or a moving bed adsorber.
Preferably, in the above organic wastewater photocatalytic treatment device, the filter system is a fixed bed adsorber, and the fixed bed adsorber is made of organic glass (PMMA-methyl methacrylate) filled with activated carbon spheres.
The beneficial effects of the above technical scheme are: the fixed bed adsorber is used for filtering and preliminary pretreatment before photocatalysis of wastewater, has the characteristics of simple structure, easy manufacture and low cost, and ensures that the device is integrally suitable for treatment of small and intermittent pollution sources and intermittent operation of adsorption and desorption, and the adsorbent can be recycled;
the activated carbon balls are used for filtering, adsorbing, decoloring and deodorizing the wastewater before photocatalysis, so that the chromaticity of the wastewater and the concentration of suspended substances are effectively reduced, and the subsequent treatment is facilitated;
in addition, the filter system adopts organic glass as a medium, has high corrosion resistance and light transmission, and greatly reduces the operation cost.
Preferably, in the above organic wastewater photocatalytic treatment device, the bottom of the filtration system is provided with a detachably connected water quantity regulating valve.
The beneficial effects of the above technical scheme are: the water quantity regulating valve can be used for controlling the sewage treatment capacity, and the replacement and recycling of the activated carbon balls filled inside are realized due to the detachable water quantity regulating valve.
Preferably, in the above photocatalytic treatment device for organic wastewater, the photocatalytic reaction system is composed of a plurality of photocatalytic reactors connected in series.
Preferably, in the above organic wastewater photocatalytic treatment device, the photocatalytic reactor is internally filled with TiO2the/ACF composite material.
Preferably, in the above organic wastewater photocatalytic treatment device, the TiO is2The preparation of the/ACF composite material comprises the following stepsThe method comprises the following steps:
weighing 35ml of absolute ethyl alcohol solution and 32ml of distilled water in a beaker, adding 5 drops of concentrated hydrochloric acid to adjust the pH value to be less than or equal to 3, and marking as A solution; to another beaker was added 35ml of butyl titanate, 23ml of glacial acetic acid, 70ml of absolute ethanol, noted as solution B. And (3) putting the solution B into a constant-temperature stirrer at the temperature of 30 ℃ for stirring, slowly adding the solution A into the solution B, and continuing stirring for 100min after the dropwise addition is finished to form wet sol. Respectively adding 1% E-15 type epoxy resin after wet sol is obtained, cutting activated carbon fiber, dipping and pulling for 2 times, drying in a blast box at 105 deg.C for 15min, and calcining in a muffle furnace at 450 deg.C for hr to obtain TiO added with cross-linking agent2the/ACF composite material.
Preferably, in the above organic wastewater photocatalytic treatment device, the light source is an ultraviolet lamp.
The beneficial effects of the above technical scheme are: the ultraviolet lamp tube emits ultraviolet light, so that the inside and the outside of the photocatalytic reactor are uniformly illuminated, and the catalytic efficiency is improved;
and it should be noted that when TiO is used2In the case of the ACF composite material, the composite material is effective only under the irradiation of an ultraviolet lamp, and the high-pressure mercury lamp and the xenon lamp cannot improve the catalytic efficiency.
Preferably, in the above organic wastewater photocatalytic treatment device, the material of the photocatalytic reactor is quartz glass.
The beneficial effects of the above technical scheme are: the quartz glass is used as an optical material, so that the normal operation of the organic wastewater photocatalytic treatment device under various severe conditions can be realized, and the reaction process is more stable.
Preferably, in the above photocatalytic treatment device for organic wastewater, a flow meter is disposed on the water inlet side of the filter system.
The beneficial effects of the above technical scheme are: the flowmeter can facilitate the observation of the flow in the wastewater treatment process and flexibly adjust according to the requirement.
Preferably, in the above organic wastewater photocatalytic treatment device, the motor provides power for the operation of the whole device.
According to the technical scheme, compare with prior art, the utility model discloses a be particularly useful for laboratory and the processing of small-scale organic waste water, through the selection to major structure and specific technology, calculation and the actual application handle, be greater than 75% with the organic pollutant removal rate in the beer waste water, make its play water reach COD <50mg/L, obtained ideal treatment, reached one-level A standard among the town sewage treatment plant pollutant emission standard.
Drawings
In order to more clearly illustrate the embodiments of the present invention or the technical solutions in the prior art, the drawings required to be used in the description of the embodiments or the prior art will be briefly described below, it is obvious that the drawings in the following description are only embodiments of the present invention, and for those skilled in the art, other drawings can be obtained according to the provided drawings without creative efforts.
FIG. 1 is a schematic view of the overall structure of the present invention;
FIG. 2 is a top view of the overall structure of the present invention;
FIG. 3 is a side view of the overall structure of the present invention;
FIG. 4 is a graph showing the effect of catalyst amount on the removal efficiency of methyl orange according to an embodiment of the present invention;
FIG. 5 is a graph showing the effect of catalyst concentration on methyl orange removal efficiency according to an embodiment of the present invention;
fig. 6 is a graph showing the effect of the shape of the catalyst on the removal efficiency of methyl orange according to the embodiment of the present invention.
In the figure:
1 is an active carbon filtering system, 2 is a photocatalytic reactor, 3 is a flowmeter, 4 is an ultraviolet lamp tube, 5 is a motor and 6 is a sewage treatment tank.
Detailed Description
The technical solutions in the embodiments of the present invention will be described clearly and completely below, and it should be understood that the described embodiments are only some embodiments of the present invention, but not all embodiments. Based on the embodiments in the present invention, all other embodiments obtained by a person skilled in the art without creative work belong to the protection scope of the present invention.
Examples
The embodiment of the utility model provides an organic waste water photocatalysis processing apparatus, including active carbon filtration system 1, two photocatalytic reactor 2, aeration systems, flowmeter 3, ultraviolet fluorescent tube 4, circulating system and motor 5.
Wherein, motor 5 provides power for whole device operation, and domestic small-size motor is adopted to this embodiment, and efficiency is 87%, and the design lift is 0.8m, and the design flow is Qmax50L/d, so a motor with 5W power is selected.
Activated carbon filtration system 1 chooses for use the fixed bed adsorber, and the cylinder made by organic glass is inside to be filled the activated carbon ball, and concrete coal matter form activated carbon of chooseing for use is as the adsorbent for filtration and preliminary pretreatment before the beer waste water photocatalysis, and the bottom is equipped with water regulating valve to can uninstall, made things convenient for the change and recycle of activated carbon ball.
Specifically, the activated carbon adsorption unit is calculated as follows: this design flow Qmax50L/d; design size D of activated carbon column Activated carbon60 mm; the height L of the adsorption layer is 0.4 m; bulk density of activated carbon rhob＝550kg/m3；
Thus, the activated carbon filtration system is designed to: the water flow velocity in the activated carbon column is 0.2 m/s; the amount of adsorbent used was 0.62 kg.
The photocatalytic reactor 2 is designed into a hollow column shape, and TiO is filled inside the reactor2The hollow part of the ACF composite material is used as a lamp source installation part, the ultraviolet lamp tube 3 is used for ultraviolet catalytic oxidation research, and the inside and the outside of the photocatalytic reactor 2 are uniformly illuminated through the ultraviolet lamp tube 3, so that the catalytic effect is improved.
Specifically, the photocatalytic reactor 2 is designed such that: the reactor height L was 0.6m, the reactor external diameter 60mm, the internal diameter 20 mm.
O in water2The content of (b) is one of important influencing factors influencing the photocatalytic efficiency, and in order to improve the removal efficiency of pollutants, the aeration system is installed in the embodiment.
The aeration efficiency and the air utilization rate are improved: the size of bubbles is reduced, the number of the bubbles is increased, the turbulence degree of liquid is improved, the installation depth of the aerator is increased, and the contact time of the bubbles and the liquid is prolonged.
Circulating system makes sewage obtain abundant processing, makes the pollutant obtain abundant degradation, reaches out water quality of water standard, also can be used to emergency treatment, improves the utility model discloses the device is at the stability and the fail safe nature of technology operation in-process.
The water quality of the effluent of the embodiment of the utility model meets the first class A standard (COD is less than 50mg/L) in the pollutant discharge standard of the urban sewage treatment plant.
The utility model provides a pair of organic waste water photocatalysis treatment device's cost can refer to table 1.
TABLE 1 economic and technical analysis
The total investment of equipment budget of the embodiment is 1280 yuan, and the equipment design budget is 1500 yuan for meeting various emergency situations. The electric charge required for treating 1L of water is 0.02 yuan, the required activated carbon fiber is 0.5 yuan, and the composite material is 0.5 yuan.
The method for treating the organic wastewater by the organic wastewater photocatalytic treatment device comprises the following steps:
(1) pretreatment of wastewater: the filtered wastewater flows into an activated carbon filtering system 1 made of organic glass and filled with activated carbon balls for filtering and adsorbing the beer wastewater before photocatalysis and removing color and odor of the beer wastewater, so that the chromaticity of the beer wastewater and the concentration of suspended substances are reduced, and the conditions are optimized for the next photocatalytic reaction.
Because of O in water2The content of (b) is one of important influence factors influencing the photocatalytic efficiency, and in order to improve the removal efficiency of pollutants, filtered water flows into an aeration system to carry out aeration treatment on the wastewater.
(2) Photocatalytic oxidation treatment: the waste water after aeration treatment flows into a photocatalytic reactor 2, and when titanium dioxide collides with water, the surface of the titanium dioxide absorbs attached OH-H of (A) to (B)2O molecule, photo-excited (H)+) Capable of oxidizing these molecules, the high-energy hydroxyl groups formed being adsorbed onto the catalyst surface and thus on the TiO2The surface layer will have a significant amount of ∙ OH radicals present.
As can be seen from more experiments, the oxygen potential of many organic compounds is higher than that of TiO2So that they may also be TiO substituted2The released holes oxidize. Photon energy shines on the TiO2At the surface, electrons are released, and the electrons can react with O in the system to generate free radicals of peroxide ions. Wherein the peroxide ion radicals formed can also be converted into HO2∙、H2O2. OH, HO2∙ and H2O2Can be mutually converted.
As can be seen from the above discussion, TiO2The catalytic mechanism by which the photocatalytic reaction occurs can be statistically counted as the following:
TiO2+hv→TiO2+e-+h+
H2O+h+→∙OH+h+
OH-+h+→∙OH
o adsorbed on the surface of free electrons2The following reactions occur:
O2+e-→∙O2 -
·O2 -+H2O→HO2∙+OH-
because of HO2∙ the free radical is extremely unstable and will further produce the following reaction:
2HO2∙→O2+H2O2
HO2∙+H2O+e-→H2O2+OH-，
H2O2+e-→∙OH+OH-
after the above series of reactions, a variety of radicals with strong oxidizing or reducing power are generated. Because of the high activity of these particles and the near non-selectivity to reactants, the C-C, C-N, C-H, C-O, N-H and O-H bonds of organic materials can be destroyed, thereby oxidizing many of the bonds with TiO2The contacted organic matter can be converted into non-toxic harmless inorganic matter.
(3) And (3) post-treatment: after a period of repeated filtration and photocatalytic reaction, the treated water overflows from the water storage tank, passes through the contact tank and the bus metering tank and is finally discharged.
The following is a description of the effect that the organic wastewater photocatalysis treatment device of the utility model can achieve through simulation experiments.
(1) Effect of catalyst dosage on removal efficiency
In a self-made reaction instrument, a photocatalytic simulation experiment on methyl orange is carried out.
Separately adding self-made TiO into the reactor2ACF catalytic material (3g, 6g, 10 g). A simulation experiment was performed on methyl orange 4L at 30mg/L, and a water sample was taken out from the reactor every 10 minutes to measure the absorbance and calculate the concentration. The change in the amount of catalyst with time as shown in FIG. 2 was obtained.
As can be seen from FIG. 2, when the addition amount of the composite material is 3g, the removal efficiency of methyl orange after 120min of reaction is 44.65%; when the addition amount of the composite material is 6g, the removal efficiency of methyl orange after 120min of reaction can reach 75.2%; when the addition amount of the composite material is 10g, the removal rate of methyl orange after reaction for 100min reaches 75.2%, and the removal rate of methyl orange after reaction for 120min can reach 80.6%. The following conclusions can be drawn: when the addition amount of the simulation reactor is more than 6g, the reaction time is more than 120min, and even if the removal rate of methyl orange under the simple photocatalysis is more than 75 percent.
(2) Effect of catalyst concentration on removal efficiency
In a self-made reactor with 3g TiO2The volume of the ACF catalytic material is 4L, and the methyl orange with the concentration of 30mg/L and 50mg/L respectively is 120min, so that the change curve of the influence of the reaction time on the removal efficiency is obtained as shown in figure 3.
As can be seen from FIG. 3, when the concentration of methyl orange is low, the removal rate of the pollutants is high in the first 60min, and the reaction is slowed down after 60 min. When the concentration of methyl orange is high, the removal rate of the pollutants is low at the beginning, and the concentration of the pollutants in the system is reduced and the removal rate is increased along with the change of the reaction time.
(3) Effect of catalyst shape on removal efficiency
Methyl orange with a volume of 4L and a concentration of 30mg/L was treated with 6g of catalytic material in the form of strips and blocks, respectively, for 120min, and the results are shown in FIG. 4.
As can be seen from FIG. 4, the block catalytic material is better filled and distributed uniformly, the removal rate before 120min is relatively high, and the strip catalytic material can achieve a similar removal rate at 120min, but the degradation of the strip catalytic material to pollutants is not stable enough. Therefore, the utility model adopts massive catalytic materials.
The embodiments in the present description are described in a progressive manner, each embodiment focuses on differences from other embodiments, and the same and similar parts among the embodiments are referred to each other. The device disclosed by the embodiment corresponds to the method disclosed by the embodiment, so that the description is simple, and the relevant points can be referred to the method part for description.
The previous description of the disclosed embodiments is provided to enable any person skilled in the art to make or use the present invention. Various modifications to these embodiments will be readily apparent to those skilled in the art, and the generic principles defined herein may be applied to other embodiments without departing from the spirit or scope of the invention. Thus, the present invention is not intended to be limited to the embodiments shown herein but is to be accorded the widest scope consistent with the principles and novel features disclosed herein.
Claims (8)
1. A photocatalytic treatment device for organic wastewater is characterized by comprising
The filtering system is communicated with the sewage treatment tank;
the input end of the photocatalytic reaction system is connected with the output end of the filtering system, and a lamp source is arranged in the photocatalytic reaction system;
the aeration system is communicated with the photocatalytic reaction system;
and a circulation line;
and the operation power of the filtering system, the photocatalytic reaction system, the aeration system and the circulating pipeline is provided by a motor.
2. The photocatalytic treatment device for organic wastewater as set forth in claim 1, wherein the filtration system is any one of a fixed bed adsorber, a moving bed adsorber, or a fluid bed adsorber.
3. The organic wastewater photocatalytic treatment device according to claim 2, characterized in that the filtering system is a fixed bed adsorber, and the fixed bed adsorber is made of organic glass filled with activated carbon balls.
4. The organic wastewater photocatalytic treatment device according to claim 2 or 3, characterized in that the bottom of the filtering system is provided with a detachably connected water quantity regulating valve.
5. The photocatalytic treatment device for organic wastewater as set forth in claim 1, wherein the photocatalytic reaction system is composed of a plurality of photocatalytic reactors connected in series.
6. An organic waste according to claim 5The water photocatalysis treatment device is characterized in that the inside of the photocatalysis reactor is filled with TiO2the/ACF composite material.
7. The organic wastewater photocatalytic treatment device according to claim 1, characterized in that the lamp source is an ultraviolet lamp.
8. The organic wastewater photocatalytic treatment device according to claim 1, characterized in that a flow meter is provided on the side of the water inlet of the filtration system.
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