JP4287775B2 - Industrial wastewater treatment method and apparatus - Google Patents

Description

  The present invention relates to a method and apparatus for treating industrial wastewater, and in particular, is suitable for treating harmful cyanogen-containing wastewater discharged from plating plants and the like, particularly wastewater containing metal cyanide complexes such as iron and nickel. The present invention relates to an industrial wastewater treatment method and apparatus.

As the processing method of the cyan-containing waste water discharged from plating factories, raw ozone (drainage) or by irradiating the note input to Rutotomoni ultraviolet, AOP method degrades cyan by or injecting hydrogen peroxide (promoting (Oxidation method) is known (for example, refer to Patent Document 1).

  However, in the conventional AOP treatment, cyan is decomposed into harmless nitrogen and carbon dioxide in one contact tank (treatment tank), so not only a large amount of ozone is required, but also UV irradiation. Even needed a lot of power. In addition, the conventional ozone injection means using an air diffuser or ejector cannot sufficiently mix raw water and ozone, the efficiency of ozone injection into raw water is low, and the amount of ozone dissolved in water is also low. It was not enough. In addition, because the ozone utilization efficiency in the contact tank is low, a large amount of exhaust ozone is discharged from the upper part of the contact tank, so the ozone treatment device for recovering and detoxifying exhaust ozone has a large capacity. Needed.

  Therefore, the present invention can reduce the amount of ozone used and reduce the power consumption by improving the treatment efficiency of the metal cyanide complex, increase the injection efficiency of ozone, and further improve the effective use of waste ozone. It is an object to provide a method and apparatus.

In order to achieve the above object, an industrial wastewater treatment method of the present invention is an industrial wastewater treatment method for decomposing a metal cyanide complex contained in industrial wastewater, wherein the industrial wastewater introduced into the first contact tank is Injecting ozone into the water containing free cyanide generated in the first decomposition step, in which ozone is injected and ultraviolet rays are irradiated to generate free cyan mainly from the metal cyanide complex, and in the first step introduced into the second contact tank to look contains a second decomposition step for decomposing the free cyanide into nitrogen and carbon dioxide, said injection of ozone in the first decomposition step, and the second decomposition step, the decomposition of the free cyanide in the second step A part of the treated water is boosted and ejected as a driving fluid from the driving fluid introduction part of the mixed-jet pump into the pump main pipe, and negatively discharged by the ejection of the driving fluid from the gas inflow part of the mixed-jet pump. Into the pump main pipe, new ozone from the ozone supply source is sucked from the gas inflow portion and exhausted ozone discharged from the first and second contact tanks is sucked from the suction portion, and the driving fluid, Ozone mixed water mixed with new ozone from the gas inflow part and exhausted ozone from the suction part is discharged from the pump main pipe to the discharge part and injected into the tanks from the bottom of the both contact tanks. It is characterized in that. Furthermore, the method of the present invention is characterized in that hydrogen peroxide is sucked from the suction part instead of sucking the exhaust ozone , or at least one of the first decomposition step and the second decomposition step , Hydrogen peroxide is injected into at least one of the first contact tank and the second contact tank from a hydrogen peroxide injection path .

Further, the industrial wastewater treatment apparatus of the present invention is an industrial wastewater treatment apparatus for decomposing a metal cyanide complex contained in industrial wastewater, and ozone injection means for injecting ozone into a tank into which the industrial wastewater flows. And a first contact tank having ultraviolet irradiation means for irradiating ultraviolet light, and a second contact tank having ozone injection means for injecting ozone into the tank into which the first treated water flowing out of the first contact tank flows. The ozone injecting means pressurizes a part of the treated water extracted from the second contact tank and ejects it into the pump main pipe as a driving fluid, and ejection of the driving fluid from the driving fluid introducing unit A gas inflow part for sucking new ozone from an ozone supply source, a suction part for sucking exhaust ozone discharged from the first and second contact tanks, and the drive The ozone mixed water mixed with the body, fresh ozone from the gas inflow part and exhausted ozone from the suction part is discharged from the pump main pipe and injected into the tanks from the bottom of the two contact tanks. And an air-jet jet pump having a discharge portion .

Furthermore, the industrial wastewater treatment apparatus of the present invention is characterized in that a hydrogen peroxide suction unit for sucking hydrogen peroxide is provided instead of the exhaust ozone suction unit . Furthermore, a hydrogen peroxide injection path for injecting hydrogen peroxide into the tank is provided in at least one of the first contact tank and the second contact tank.

  According to the present invention, cyan is decomposed in two steps: a process of generating free cyan from a metal cyan complex and a process of decomposing free cyan into nitrogen and carbon dioxide. Therefore, it is possible to perform an effective treatment with a small amount of ozone as compared with the conventional case. Moreover, since it is not necessary to irradiate ultraviolet rays in the process of decomposing free cyanide, the power required for the lamp for irradiating ultraviolet rays can be reduced. Further, by injecting hydrogen peroxide in both steps, the processing efficiency in both steps can be further improved.

  Furthermore, by using an air-fueled jet pump as means for injecting ozone into the contact tank, the efficiency of injecting ozone into water can be increased. Furthermore, the ozone utilization efficiency can be greatly improved by recovering and recycling the exhausted ozone at the suction part of the air-fueled jet pump. Moreover, the production | generation of a hydroxyl radical can be accelerated | stimulated by attracting hydrogen peroxide with an air-jet pump and mixing with ozone.

FIG. 1 is a system diagram of an industrial wastewater treatment apparatus showing a reference example of the present invention. The industrial wastewater treatment apparatus includes a first contact tank 11 into which cyan-containing wastewater that is raw water flows, and a second contact tank 12 into which primary treated water treated in the first contact tank 11 flows, The first contact tank 11 is provided with ultraviolet irradiation means 13. In addition, an ozone injection path 14 is provided at the bottom of each contact tank 11, 12, and an exhaust path 16 for exhausting exhaust ozone after collecting exhaust ozone and detoxifying the ozone treatment apparatus 15 at the top of the tank. Each is provided. Furthermore, a hydrogen peroxide injection path 17 for injecting hydrogen peroxide is provided above the contact tanks 11 and 12.

  The raw water is introduced into the first contact tank 11 from the raw water inflow path 18 provided in the upper part of the first contact tank 11 and mixed with the hydrogen peroxide injected from the hydrogen peroxide injection path 17 in the ozone injection. While descending while making alternating current contact with ozone injected from the path 14 via an air diffuser, an ejector, or the like, ultraviolet rays are irradiated from the ultraviolet irradiation unit 13. In the first decomposition step in the first contact tank 11, the metal cyanide complex is decomposed and free cyanide is generated by the photodecomposing action of ultraviolet rays and the oxidizing action of hydroxy radicals generated by the interaction of ozone, ultraviolet rays and hydrogen peroxide. Along with the dissociation and generation, a part of the generated free cyanide is oxidized and decomposed into nitrogen and carbon dioxide.

  The primary treated water that has finished the first decomposition step in the first contact tank 11 passes through the relay path 19 that connects the lower part of the first contact tank 11 and the upper part of the second contact tank 12 to the second contact tank 12. It flows in, mixes with hydrogen peroxide injected from the hydrogen peroxide injection path 17, and descends while making alternating current contact with ozone injected from the ozone injection path. In the second decomposition step in the second contact tank 12, free cyanide remaining in the water is decomposed into nitrogen and carbon dioxide by the oxidizing action of hydroxy radicals generated from ozone and hydrogen peroxide. The treated water that has undergone the free cyanide decomposition treatment flows out from the treated water outflow path 20 provided in the lower part of the second contact tank 12.

  The free cyanide generation process of the first decomposition step is basically a photodecomposition reaction of a metal cyanide complex by ultraviolet irradiation, but not only the decomposition to free cyanide is promoted by injecting ozone into this, Hydroxyl radicals, which are powerful oxidants, are generated by the interaction between ozone and ultraviolet rays, so that the free radicals are effectively decomposed into nitrogen and carbon dioxide by the hydroxy radicals. Furthermore, by adding an appropriate amount of hydrogen peroxide to this step, the generation of hydroxy radicals is promoted, the oxidative decomposition of the metal cyan complex and the decomposition of the generated free cyanogen are promoted, and the processing efficiency is further improved.

  On the other hand, the second decomposition step decomposes free cyanide remaining in the water by injecting ozone and oxidizing it. At this time, an appropriate amount of hydrogen peroxide is also injected to remove hydroxy radicals. By generating it, free cyanide can be effectively and reliably decomposed.

  As described above, the decomposition process of the metal cyanide complex is performed in two stages, the metal cyanide complex is mainly decomposed in the first decomposition process, and the remaining free cyanide is decomposed in the second decomposition process stage. Thus, the processing efficiency of each decomposition process can be improved as compared with the case where the decomposition process is performed in one stage. That is, in the first decomposition step, ozone is used as an auxiliary component for the photodecomposition reaction, so that a sufficient effect can be obtained with a relatively small amount of ozone. In the second decomposition step, the metal cyanide complex is decomposed. Since it is not necessary to perform the treatment, the ultraviolet irradiation means is not required, and therefore the equipment cost and the operation cost can be reduced. At the same time, the entire processing apparatus can be reduced in size.

FIG. 2 is a system diagram of an industrial wastewater treatment apparatus showing an embodiment of the present invention. In the following description, the same components as those in the industrial wastewater treatment apparatus shown in the reference example are denoted by the same reference numerals, and detailed description thereof is omitted.

  This embodiment shows an example in which an air-mix jet pump 31 is used as means for injecting ozone into the first contact tank 11 and the second contact tank 12. Conventionally, various types of mixed gas jet pumps 31 have been used. Basically, a high-pressure driving fluid is introduced from the driving fluid introduction section 32 and is injected into the pump main pipe 33 as a jet. By jetting, gas is sucked from the gas inflow portion 34 provided in the pump main pipe 33 to form a jet in a gas-liquid mixed state (mixed state), and further, the pump main pipe is generated by this mixed-phase jet. A gas, a liquid, a granular material, and the like are sucked from a suction portion 35 provided on the side of 33, and are discharged from a discharge portion 36 in a state where they are agitated and mixed.

  Such an air-fueled jet pump 31 is capable of attracting and delivering a plurality of fluids by ejecting a driving fluid made of liquid pressurized by the pump 37 as a jet, and is powerful within the pump main pipe 33. Since the stirring and mixing action is obtained, the liquid (driving fluid) and the attracted gas or liquid can be mixed efficiently, and the pressure in the pump main pipe 33 can be kept high, so the solubility of the gas in the liquid It has the advantage that it can be raised. Therefore, compared with the case where ozone is injected using a conventional diffuser or ejector, the ozone injection efficiency can be greatly improved. As a result, the utilization efficiency of ozone in each of the contact tanks 11 and 12 is improved and the efficiency of the oxidative decomposition treatment is greatly improved, so that the consumption of ozone can be greatly reduced.

  A part of the treated water branched from the treated water outflow path 20 to the branch circulation path 38 is boosted to a predetermined pressure by the pump 37 to be a driving fluid of the mixed jet pump 31, and a driving fluid introduction part of the mixed jet pump 31. 32 is ejected into the pump main pipe 33. Due to the ejection of the driving fluid, the inside of the pump main pipe 33 becomes negative pressure, and ozone from the ozone generation source passes through the gas inflow portion 34 and is sucked into the pump main pipe 22. Further, exhaust ozone discharged from the upper portions of the contact tanks 11 and 12 from the exhaust passage 16 through the exhaust ozone recovery passage 39 is sucked and mixed from the suction portion 35.

  Therefore, a part of the treated water is discharged into the discharge unit 36 as ozone mixed water in which new ozone from the gas inflow unit 34 and exhausted ozone from the suction unit 35 are mixed, and the bottom of each contact tank 11, 12. Is injected into each of the contact tanks 11 and 12 through the ozone mixed water injection path 40 provided in FIG. At this time, since exhaust ozone is sucked and mixed, the amount of gas occupied per unit volume in the mixed-air jet pump 31 is increased as compared with the case where only new ozone is injected. The pressure in the vicinity of the outlet is increased, and the solubility of ozone dissolved in the treated water (driving fluid) can be increased. Further, by recirculating and reusing exhaust ozone, the efficiency of ozone utilization can be greatly improved, the amount of new ozone supplied through the gas inlet 34 can be reduced, and the load on the ozone treatment device 15 can be reduced. Can also be reduced.

  The ozone mixed water flowing into the contact tanks 11 and 12 is mixed with raw water or primary treated water, and further mixed with hydrogen peroxide injected from the hydrogen peroxide injection path 17. Thereby, hydroxy radicals are generated from ozone and hydrogen peroxide in the ozone mixed water, and the metal cyanide complex and the free cyanide can be efficiently decomposed.

  In the mixed-air jet pump 31, it is also possible to suck hydrogen peroxide from the suction portion 35, and by mixing the hydrogen peroxide from here, hydrogen peroxide and ozone are mixed effectively. Thus, the production of hydroxy radicals can be further promoted.

It is a systematic diagram of an industrial wastewater treatment apparatus showing a reference example of the present invention. It is a systematic diagram of the industrial waste water treatment equipment which shows one example of the present invention.

Explanation of symbols

  DESCRIPTION OF SYMBOLS 11 ... 1st contact tank, 12 ... 2nd contact tank, 13 ... Ultraviolet irradiation means, 14 ... Ozone injection path, 15 ... Ozone processing apparatus, 16 ... Exhaust path, 17 ... Hydrogen peroxide injection path, 18 ... Raw water inflow path , 19 ... relay path, 20 ... treated water outflow path, 31 ... mixed gas jet pump, 32 ... drive fluid introduction part, 33 ... pump main pipe, 34 ... gas inflow part, 35 ... suction part, 36 ... discharge part, 37 ... Pump, 38 ... Branch circulation path, 39 ... Exhaust ozone recovery path, 40 ... Ozone mixed water injection path

Claims (6)

In an industrial wastewater treatment method for decomposing a metal cyanide complex contained in industrial wastewater, ozone is injected into the industrial wastewater introduced into the first contact tank, and ultraviolet rays are irradiated to release mainly from the metal cyanide complex. A first decomposition step for generating cyan, and a second decomposition for injecting ozone into the free cyanide-containing water generated in the first step introduced into the second contact tank to decompose the free cyan into nitrogen and carbon dioxide. and a step viewed including the injection of ozone in the first decomposition step, and the second decomposition step, admission jet a portion of the treated water in the second step was completed decomposition of free cyanide as a boost to drive fluid A new supply from an ozone supply source is injected into the pump main from the pump's driving fluid introduction section and into the pump main, which is negative pressure due to the ejection of the driving fluid from the gas inflow section of the mixed jet pump. Fresh ozone from the gas inflow section and exhausted ozone discharged from the first and second contact tanks from the suction section, and the drive fluid, new ozone from the gas inflow section and exhaust from the suction section. A method for treating industrial wastewater, characterized in that ozone mixed water mixed with ozone is discharged from the inside of the pump main pipe to a discharge section and injected into each tank from the bottom of the both contact tanks . The industrial wastewater treatment method according to claim 1 , wherein hydrogen peroxide is sucked from the suction section instead of the exhaust ozone suction . In at least one of said first and second steps, claims, characterized in that to inject the hydrogen peroxide to at least one of hydrogen peroxide injected the first contact vessel from the path and a second contact tank The method for treating industrial wastewater according to 1 . In an industrial wastewater treatment apparatus for decomposing a metal cyanide complex contained in industrial wastewater, the wastewater treatment apparatus has first ozone injection means for injecting ozone into the tank into which the industrial wastewater flows and ultraviolet irradiation means for irradiating ultraviolet rays. A contact tank; and a second contact tank having ozone injection means for injecting ozone into the tank into which the first treated water flowing out of the first contact tank flows, wherein the ozone injection means is the second contact tank. A part of the treated water extracted from the pump and pumping it into the pump main pipe as a driving fluid, and the pump main pipe having a negative pressure due to the ejection of the driving fluid from the driving fluid inlet A gas inflow part for sucking in new ozone from the ozone supply source, a suction part for sucking out exhaust ozone discharged from the first and second contact tanks, the drive fluid, and a new ozone from the gas inflow part. Emissions and ozone mixing water and exhaust ozone are mixed from the suction unit by discharging from the pump the tube, admission jet pump and a discharge portion for injecting each of the from the bottom of both contact vessel in each tank Industrial wastewater treatment equipment characterized by The industrial wastewater treatment apparatus according to claim 4, further comprising a hydrogen peroxide suction unit that sucks hydrogen peroxide instead of the exhaust ozone suction unit . The industrial wastewater treatment according to claim 4, wherein a hydrogen peroxide injection path for injecting hydrogen peroxide into the tank is provided in at least one of the first contact tank and the second contact tank. apparatus.

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