JP2013000658A - Treatment method of wastewater containing hydrazine and chelate formation organic compound - Google Patents

Abstract

PROBLEM TO BE SOLVED: To provide a treatment method capable of treating wastewater containing hydrazine and a chelate formation organic compound stably and efficiently.SOLUTION: A predetermined amount of the wastewater W is filled in a reaction tank 1, then air as oxygen-containing gas is sent from a diffuser tube 4 arranged on a bottom part of the reaction tank 1 by a blower 3, and a homogeneous catalyst is added from a supply means 2 of the homogeneous catalyst (a first oxidation treatment process). Then, the wastewater W is added to primary treated water W1 in the first oxidation treatment process to prepare treated raw water W2. After that, the air as the oxygen-containing gas is sent from the diffuser tube 4 arranged on the bottom part of the reaction tank 1 by the blower 3, and the homogeneous catalyst is added from the supply means 2 of the homogeneous catalyst (a second oxidation treatment process). Thereby, the hydrazine in the treated raw water W2 is oxidatively-degraded.

Description

  The present invention relates to a method for treating waste water containing hydrazine and a chelate-forming organic compound. In particular, the present invention relates to a method for treating wastewater containing hydrazine and a chelate-forming organic compound capable of stably and efficiently treating wastewater containing hydrazine and a chelate-forming organic compound with a homogeneous catalyst.

  As a method of treating wastewater containing hydrazine, oxidative decomposition of hydrazine with an oxidizing agent such as sodium hypochlorite, oxidative decomposition of hydrazine by aeration treatment with an oxygen-containing gas, hydrazine is passed through activated carbon. A removal method has been proposed. As an aeration treatment method, for example, in Patent Document 1, as a method for treating hydrazine-containing water that efficiently removes hydrazines and does not generate secondary pollution, water containing hydrazines is treated with copper in an oxidation tank. There has been proposed a method for treating hydrazine-containing water in which it is brought into contact with air in the presence of the compound and then subjected to solid-liquid separation by filtration, and the treated water is discharged out of the system while the solid content is returned to the oxidation tank again. .

  Patent Document 2 discloses a method for treating hydrazine-containing wastewater that is useful as a pretreatment step for removing hydrazine in wastewater with an ion exchange resin, and is dispersed in the presence of metallic copper or a copper salt solution in the hydrazine-containing wastewater. There has been proposed a method for decomposing and removing hydrazine.

  However, when the methods described in Patent Document 1 and Patent Document 2 are applied to wastewater containing a chelate-forming organic compound in addition to hydrazine, it has been found that oxidative decomposition of hydrazine does not proceed sufficiently.

  Wastewater containing hydrazine and chelate-forming organic compounds is discharged as semiconductor process wastewater, boiler blow water, inorganic chemical industry wastewater, etc., so even if chelate-forming organic compounds coexist, hydrazine is effectively removed by oxygen-containing gas. There is a need for a wastewater treatment method that can be oxidatively decomposed.

  Therefore, as a technique for solving such a problem, Patent Document 3 discloses that oxygen ions containing 10 to 1000 mg / L of metal ions are added to waste water containing hydrazine and a chelate-forming organic compound, and oxygen-containing gas such as air is blown. A method for oxidative degradation of hydrazine is disclosed.

JP-A-56-136695 JP 57-27913 A JP 2003-39083 A

  However, when applied to wastewater containing hydrazine and a chelate-forming organic compound by the method described in Patent Document 3, first, when metal ions are added to wastewater containing hydrazine at a high concentration, depending on conditions, metal ions may be There is a problem that the catalytic activity is reduced due to reduction and the catalytic activity is lowered. In an extreme case, the function as a catalyst may be deactivated. In addition, oxidative decomposition of hydrazine is an exothermic reaction. When a high concentration of hydrazine is treated, the liquid temperature rises until the hydrazine concentration is lowered to some extent, whereas when the hydrazine concentration is lowered, the temperature rises due to reaction heat. There is a problem that the temperature drop due to the blowing of air becomes larger and the liquid temperature is lowered, the temperature tendency is not constant, the reaction is not stable, and temperature monitoring and a cooling device are required.

  The present invention has been made in view of the above problems, and a method for treating wastewater containing hydrazine and a chelate-forming organic compound capable of stably and efficiently treating wastewater containing hydrazine and a chelate-forming organic compound. The purpose is to provide.

  In order to solve the above-mentioned problems, the present invention is a method for treating wastewater containing hydrazine and a chelate-forming organic compound and having a hydrazine concentration exceeding 3000 mg / L, comprising adding a homogeneous catalyst to the wastewater, The first oxidation treatment step for reducing the hydrazine concentration in the wastewater by oxidatively decomposing hydrazine in the step, and preparing the treated raw water by adding the wastewater to the primary treatment water of the first oxidation treatment step, this treatment A method for treating wastewater containing hydrazine and a chelate-forming organic compound, comprising: adding a homogeneous catalyst to raw water and oxidizing and decomposing hydrazine with an oxygen-containing gas to obtain treated water. Provided (Invention 1)

  According to this invention (Invention 1), in the first oxidation treatment step, a homogeneous catalyst such as copper sulfate is added to the waste water containing hydrazine having a hydrazine concentration exceeding 3000 mg / L and a chelate-forming organic compound, and aerated. By doing so, hydrazine is oxidatively decomposed to a certain concentration. Next, in the second oxidation treatment step, the waste water is added to the primary treated water in which the concentration of hydrazine has been reduced to some extent to prepare a treated raw water by controlling the concentration of hydrazine, and a homogeneous catalyst is further added to the treated raw water. By adding and aeration treatment, it is possible to obtain a treated water by stably and efficiently treating hydrazine while suppressing temperature rise.

  In the said invention (invention 1), it is preferable that the hydrazine density | concentration in the said processing raw water is 3000 mg / L or less (invention 2).

  According to this invention (Invention 2), by adding a homogeneous catalyst to the treated raw water having a hydrazine concentration of 3000 mg / L or less and subjecting to aeration treatment, the temperature rise is suppressed and hydrazine is stably and efficiently decomposed. can do.

  In the said invention (invention 1 and 2), it is preferable to set the addition of the said waste_water | drain to the said primary treated water according to the progress of the oxidation reaction by the said homogeneous catalyst (invention 3).

  According to this invention (invention 3), by controlling the amount of wastewater added to the primary treated water according to the residual hydrazine concentration by oxidative decomposition of hydrazine in the first oxidation treatment step, a predetermined hydrazine concentration Since the following raw water can be treated, hydrazine can be stably oxidatively decomposed.

  According to the method for treating wastewater containing hydrazine and a chelate-forming organic compound of the present invention, in the first oxidation treatment step, wastewater containing hydrazine and a chelate-forming organic compound having a hydrazine concentration exceeding 3000 mg / L is added to copper sulfate or the like. By adding a homogeneous catalyst and subjecting to aeration, hydrazine is oxidatively decomposed to a certain level. Next, in the second oxidation treatment step, the waste water is added to the primary treated water in which the concentration of hydrazine has been reduced to some extent to prepare a treated raw water by controlling the concentration of hydrazine, and a homogeneous catalyst is further added to the treated raw water. By adding and aeration treatment, it is possible to obtain a treated water by stably and efficiently treating hydrazine while suppressing temperature rise.

The reason why such an effect is obtained is as follows. That is, when hydrazine is oxidatively decomposed with an oxygen-containing gas such as air, a homogeneous catalyst that releases copper ions and the like is often used to efficiently treat hydrazine. However, when a homogeneous catalyst is added to wastewater containing hydrazine at a high concentration, metal ions resulting from the homogeneous catalyst are reduced to become metal, and the catalytic activity is greatly reduced. As a result, the hydrazine oxidative decomposition reaction represented by the following formula (1) does not proceed, and the hydrazine treatment is considered to be poor.
N ₂ H ₄ + O ₂ → N ₂ + 2H ₂ O ΔH = −622 kJ / mol (1)
(catalyst)

  After the treatment as described above, the remaining oxidizing agent is reduced with a reducing agent, and after removing metal ions from the obtained treated water, the BOD component is removed by biological treatment, etc. By removing harmful substances from the waste water containing the chelate-forming organic compound, treated water with good water quality can be obtained.

It is a systematic diagram which shows the system which can implement the processing method of the waste_water | drain containing the hydrazine and chelate formation organic compound which concern on one Embodiment of this invention.

  Hereinafter, with reference to FIG. 1, the processing method of the waste_water | drain containing the hydrazine and chelate formation organic compound of this embodiment is demonstrated. FIG. 1 is a system diagram showing a system capable of implementing a method for treating wastewater containing hydrazine and a chelate-forming organic compound according to an embodiment of the present invention.

  In FIG. 1, 1 is a reaction tank for introducing waste water W containing hydrazine and a chelate-forming organic compound, and 2 is a homogeneous catalyst supply means. A diffuser pipe 4 connected to the blower 3 is provided at the bottom of the reaction tank 1.

  In the treatment system having the above-described configuration, the waste water W contains hydrazine at a high concentration exceeding 3000 mg / L. When the concentration of hydrazine is 3000 mg / L or less, the effect of the method of the present embodiment cannot be sufficiently exhibited. In addition, about a content rate to a chelate formation organic compound, it is common to contain 1000-20000 mg / L. Further, the pH of the waste water W is usually highly alkaline, for example, pH 13 or more.

  In this embodiment, the homogeneous catalyst is an oxidation catalyst that releases ions uniformly dispersed in the reaction system (water), and releases copper ions, iron ions, cobalt ions, nickel ions, and the like. Sulfates and hydrochlorides of these metals can be used. Specifically, an aqueous solution of copper sulfate, copper chloride, nickel sulfate, nickel chloride or the like can be used. Among these, copper sulfate (copper ions) can be particularly preferably used because it has an effect of remarkably accelerating the oxidative decomposition of hydrazine. When a chelate-forming organic compound is present in the waste water, the copper ions form a chelate complex, so even if it is alkaline at high pH, it can be present in water at a high concentration.

  Next, the method of this embodiment which processes the waste_water | drain W using the above systems and a homogeneous catalyst is demonstrated below.

(First oxidation treatment process)
First, when a predetermined amount of waste water W is filled in the reaction tank 1, the pH is adjusted to 9 to 13, particularly 10 to 12, by adding an acid such as sulfuric acid as necessary. If the pH of the waste water W is less than 9, or if the pH exceeds 13, it is not preferable because the oxidative decomposition rate of hydrazine may decrease. Subsequently, air as an oxygen-containing gas is sent from the air diffuser 4 provided at the bottom of the reaction vessel 1 by the blower 3, and the above-described homogeneous catalyst (metal ions) is added from the homogeneous catalyst supply means 2. As a specific operation, a water-soluble metal salt or an aqueous solution of a metal salt is added and mixed uniformly. As a result, hydrazine is oxidatively decomposed into primary treated water W1.

The blowing amount of the oxygen-containing gas (air) is preferably 1 to 10 m ³ / min per 1 m ^{3 of} waste water, and particularly preferably 1.5 to ⁵ m ³ / min. When blowing of oxygen-containing gas is less than the waste water 1 m ³ per 1 m ^3, while the mixing with the homogeneous catalyst and waste water W which may not be performed uniformly, blowing amount of oxygen-containing gas (air), drainage If it exceeds 10 m ³ per m ³ , the volume of the reaction tank 1 and the oxygen blowing power become excessive, and the gas-liquid contact efficiency between the oxygen-containing gas and the waste water W may be reduced.

  The addition amount of the homogeneous catalyst from the homogeneous catalyst supply means 2 may be 10 to 300 mg / L of the homogeneous catalyst with respect to the waste water W (metal ion cold conversion). By the first oxidation treatment step as described above, the concentration of hydrazine is lowered to 100 mg / L or less.

By the first oxidation treatment step as described above, the temperature of the primary treated water W1 is increased by about 20 to 60 ° C. with respect to the waste water W.

(Second oxidation process)
Next, the waste water W is added to the primary treated water W1 of the first oxidation treatment step to prepare the treated raw water W2. Specifically, according to the hydrazine concentration of the waste water W and the hydrazine concentration of the primary treated water W1, the waste water W is added so that the hydrazine concentration of the treated raw water W2 is preferably 3000 mg / L or less, particularly 2000 mg / L or less. To do. Thereafter, the same operation as the first oxidation treatment step described above may be repeated. Specifically, an acid such as sulfuric acid is added to the treated raw water W2 as necessary, and then air is sent from the air diffuser 4 provided at the bottom of the reaction tank 1 by the blower 3 to supply the homogeneous catalyst 2 To the above-mentioned homogeneous catalyst (metal ion). Thereby, the hydrazine in the treated raw water W2 is oxidatively decomposed.

  The treatment time of the second oxidation treatment step as described above, that is, the residence time of the treated raw water W2 in the reaction tank 1 can be appropriately selected according to the target hydrazine removal amount. It is preferably 2.0 hours, particularly preferably 0.4 to 1.5 hours. If the residence time in the reaction tank 1 is less than 0.1 hour, the hydrazine may be insufficiently oxidized and decomposed, but if it exceeds 2.0 hours, no further improvement in the effect can be obtained. Processing efficiency decreases.

  By the second oxidation treatment step as described above, the treated water W3 having a hydrazine concentration reduced to 100 mg / L or less can be discharged. Further, the treated water W3 has a temperature increase of 10 ° C. or less with respect to the treated raw water W2, and has an effect that it is significantly reduced compared to the first oxidation treatment step.

(Post-processing process)
The treated water W3 obtained by oxidizing and decomposing hydrazine as described above is, for example, obtained by removing the remaining hydrazine by oxidizing it with an oxidizing agent such as sodium hypochlorite and hydrogen peroxide, and then treating the treated water W3 with ions. Metal ions in the treated water W3 are removed by contacting with an exchange resin, a chelate resin, or the like. Subsequently, treated water with good water quality can be obtained by removing the chelate-forming organic compound and the other BOD components by means of biological treatment means or the like.

  As mentioned above, although the processing method of the waste_water | drain W containing the hydrazine and chelate formation organic compound of this embodiment has been demonstrated, this invention is not limited to the said embodiment, A various deformation | transformation implementation is possible.

  For example, in the present embodiment, air is used as it is as the oxygen-containing gas, but oxygen-enriched air can also be used. The method for supplying the oxygen-containing gas is not limited to aeration by the diffuser tube 4, and for example, using a packed tower, a wet wall tower, a plate tower, a spray tower, a scrubber, a bubble tower, etc. The hydrazine can be oxidatively decomposed by contacting the wastewater to which is added.

  Furthermore, in the said embodiment, although it processed by the batch type, it can also process by a continuous type. In the case of the continuous type, the reaction tank 1 may be a volume capable of ensuring a sufficient reaction time (residence time).

The following specific examples further illustrate the present invention.
[Comparative Example 1]
(First oxidation treatment process)
Waste water W was prepared by adding sulfuric acid to pH 13.7 semiconductor factory waste water containing 20000 mg / L of hydrazine and 12000 mg / L of citric acid, which is a chelate-forming organic compound, to adjust the pH to about 12. The temperature of the wastewater to which this sulfuric acid was added was 56 ° C. Next, after leaving this waste water W to reach 20 ° C., 130 L was supplied to the reaction tank 1, and air was blown from the air diffuser 4 to the waste water W 1 L at 60 L / hr by the blower 3 to perform air aeration.

  Then, while continuing air aeration, a copper sulfate solution was added to the reaction tank 1 so that the copper ion concentration was 200 mg / L with respect to the waste water W, the change in hydrazine concentration over time was measured, and the hydrazine concentration was 100 mg / L. The time to decrease to L was determined. As a result, the hydrazine concentration reached 100 mg / L after about 10 hours. Further, the amount of hydrazine treated per unit time was calculated to be 1990 mg / hr, and the maximum value of the increase in the liquid temperature was 30 ° C.

Examples 1 to 3
(Second oxidation process)
The treated liquid treated in Comparative Example 1 is used as the primary treated water W1, and while continuing aeration with air under the same conditions as in Comparative Example 1, the waste water W is 5% by volume (Example 1), 10% with respect to the primary treated water W1. Volume% (Example 2) and 15 volume% (Example 3) were respectively added to obtain treated raw water W2. Table 1 shows the results of measuring the hydrazine concentration (initial N ₂ H ₄ ) of these treated raw water W2.

Next, after leaving this treated raw water W2 to 20 ° C., a copper sulfate solution is added to the reaction tank 1 so that the copper ion concentration is 200 mg / L with respect to the waste water W while continuing air aeration, and hydrazine is added. Table 1 shows the results of measuring the change with time of the concentration and determining the treatment time until the hydrazine concentration is reduced to 100 mg / L. Also, the processing amount of hydrazine per unit time to calculate the (ΔN 2 _{H 4)} are shown in Table 1 The results of the maximum value of the liquid temperature rise were measured, respectively.

As is apparent from Table 1, in Examples 1 to 3 in which the hydrazine concentration was controlled to 3000 mg / L or less, the processing time until the hydrazine concentration was reduced to 100 mg / L was significantly shortened compared to Comparative Example 1. It was. This is considered to be because the reduction of copper ions was suppressed and the oxidative decomposition reaction of hydrazine was promoted. Also, the temperature rise was significantly less. This eliminates the need for a cooling device, makes it possible to apply resin lining and the like, and has the effect of facilitating material selection. These effects are good in Examples 1 and 2 where the initial N ₂ H ₄ concentration of the treated raw water W2 is around 2000 mg / L, and particularly remarkable in Example 1 where the initial N ₂ H ₄ concentration is 2000 mg / L or less. there were.

DESCRIPTION OF SYMBOLS 1 ... Reaction tank 2 ... Uniform catalyst supply means 3 ... Blower (oxygen-containing gas supply means)
4 ... Diffuser (oxygen-containing gas supply means)
W ... Wastewater W1 ... Primary treated water W2 ... Raw treated water W3 ... treated water

Claims (3)

A method for treating wastewater containing hydrazine and a chelate-forming organic compound and having a hydrazine concentration exceeding 3000 mg / L,
A first oxidation treatment step of adding a homogeneous catalyst to the waste water and oxidatively decomposing hydrazine with an oxygen-containing gas to reduce the concentration of hydrazine in the waste water;
The waste water is added to the primary treated water of the first oxidation treatment step to prepare treated raw water, a homogeneous catalyst is added to the treated raw water, and hydrazine is oxidized and decomposed with an oxygen-containing gas to obtain treated water. A wastewater treatment method comprising hydrazine and a chelate-forming organic compound, characterized by comprising a second oxidation treatment step.   The method for treating wastewater containing hydrazine and a chelate-forming organic compound according to claim 1, wherein the concentration of hydrazine in the treated raw water is 3000 mg / L or less.   The hydrazine and chelate-forming organic substance according to claim 1 or 2, wherein the addition of the waste water to the primary treated water of the first oxidation treatment step is set according to the progress of the oxidation reaction by the homogeneous catalyst. A method for treating wastewater containing compounds.

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