JP2006055728A - Method and apparatus for treating fluorine-containing wastewater - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To prevent the excessive use of a chemical agent, to also reduce the generation amount of sludge and to suppress the concentration of fluorine in wastewater to a discharge standard or below, in the treatment of fluorine-containing wastewater. <P>SOLUTION: In the subject treatment apparatus for fluorine-containing wastewater using a calcium method, composed of a reaction tank 1, a neutralization tank 2, a flocculation tank 3 and a sedimentation tank 4, a pre-reaction tank 5 for reacting slaked lime with an aluminum flocculant is provided and an aluminum salt being a reaction product is charged in the reaction tank 1 to adsorb a fluoride in the wastewater or to be compounded with the fluoride to sediment the fluoride. By this constitution, treated water wherein fluorine treatment concentration is the discharge standard or below is obtained. <P>COPYRIGHT: (C)2006,JPO&NCIPI

Description

  The present invention relates to a treatment method and a treatment apparatus for fluorine-containing wastewater, and in particular, a fluorine-containing wastewater treatment method and treatment that can reduce fluorine in wastewater containing fluorine to below the discharge standard and also reduce the amount of chemicals used. Relates to the device.

  In recent years, there has been a problem of treatment of wastewater containing fluorine generated from an etching process or a cleaning process such as manufacturing liquid crystals, semiconductors, and solar cells.

  Also, recently, since the emission standard of fluorine has been strengthened from 15 mg / L to 8 mg / L, a more advanced treatment method is desired.

  Conventionally, as a method of removing fluorine from fluorine-containing wastewater, a method in which calcium salt is introduced into fluorine-containing wastewater to produce insoluble calcium fluoride and this is solid-liquid separated (hereinafter, this method is referred to as “calcium method”). For short).

  However, in this calcium method, the fluorine treatment concentration is limited to about 8 mg / L even under ideal conditions, and the reaction between fluorine and calcium salt is hindered in actual factory wastewater where various substances coexist. The fluorine treatment concentration is limited to 20 to 30 mg / L. For this reason, the calcium method alone cannot satisfy the emission standard of 8 mg / L.

  As a method of further reducing the treatment concentration of fluorine, a first step of adjusting fluoride-containing water to pH 4 or lower in the presence of an aluminum compound, and a calcium compound added to the discharged water generated in this first step to a pH of 5 or higher A method including a second step of solid-liquid separation after adjusting to (for example, see Patent Document 1) is known.

  This method is suitable for water that contains a fluoride and a boron compound at the same time. In particular, since the first step decomposes the borofluoride, in the second step, the calcium compound is added to adjust the pH to 5 or more. As a result, fluoride ions and calcium ions react with each other, resulting in poorly soluble precipitates of calcium fluoride.

In addition, dissolved aluminum ions are also precipitated as Al (OH) _3, and it is considered that fluoride removal is promoted by adsorption or embedding of fluoride on the surface or inside thereof.

And in the Example, 7000 ppm of calcium hydroxide (synonymous with slaked lime described in the present invention) and 4000 ppm of sulfuric acid band were added to the fluorine concentration of 365 ppm in the waste water, and the fluorine treatment concentration was 2 ppm.
Japanese Patent Laid-Open No. 57-144086

  As described above, in the conventional fluorine wastewater treatment method, there is a problem that when the fluorine treatment concentration is lowered, the amount of chemicals to be introduced becomes excessive and the amount of sludge generated increases.

  Therefore, establishment of a wastewater treatment method that satisfies a fluorine emission standard with a small amount of chemical input and sludge generation is required.

  Moreover, there exists a subject that disposal of the generated sludge is difficult, and recycling as a cement raw material is requested | required.

  The present invention solves such a conventional problem, does not excessively input chemicals, suppresses the amount of sludge generated, collects and recycles the generated sludge, and discharges fluorine. It aims at providing the wastewater treatment method of the fluorine which satisfies.

  The treatment method of fluorine-containing wastewater of the present invention comprises a preliminary reaction step of reacting slaked lime with an aluminum flocculant in the fluorine-containing wastewater treatment step, and the product generated in the preliminary reaction step as a calcium source in fluorine-containing wastewater. Is provided with a reaction step of charging.

  By using this means, it is possible to obtain a method for treating fluorine-containing wastewater such that the fluorine concentration of the treated water is equal to or lower than the discharge standard.

  Another means is a treatment step of fluorine-containing wastewater, which includes a reaction step of adding an aluminum salt as a calcium source to the fluorine-containing wastewater.

  Thereby, the treatment method of the fluorine-containing waste water from which the fluorine density | concentration of treated water becomes below a discharge | emission standard, without providing a preliminary reaction process is obtained.

  Another means is a treatment process of fluorine-containing wastewater, which comprises a reaction step of simultaneously adding slaked lime and aluminum flocculant to the fluorine-containing wastewater.

  By this means, it is possible to obtain a fluorine-containing wastewater treatment method in which the fluorine concentration of the treated water is equal to or lower than the discharge standard simply by changing the chemical charging timing with the conventional treatment method.

  Another means is to determine the amount of slaked lime and aluminum flocculant input based on the fluorine concentration of the fluorine-containing waste water.

  By this means, a method for treating fluorine-containing waste water without excessive charging of the medicine can be obtained.

  Another means is that the input amount of slaked lime is 1 to 3 times the fluorine concentration of the fluorine-containing wastewater, and the input amount of the aluminum flocculant is 0.002 to 0.1 times the fluorine concentration in terms of aluminum. To do.

  By this means, a method for treating fluorine-containing waste water without excessive charging of the medicine can be obtained.

  Another means includes a preliminary reaction tank for reacting slaked lime with an aluminum flocculant, and a reaction tank for charging the fluorine-containing wastewater with a product in the preliminary reaction tank as a calcium source.

  By this means, a treatment apparatus for fluorine-containing waste water in which the fluorine concentration of the treated water is below the discharge standard is obtained.

  Another means is to provide a fluorine concentration detection means for detecting the fluorine concentration of the fluorine-containing waste water, and determine the input amount of slaked lime and aluminum flocculant according to the detected fluorine concentration.

  By this means, it is possible to obtain a fluorine-containing wastewater treatment apparatus in which no excessive amount of chemicals is introduced.

  Another means is that the amount of slaked lime is 1 to 3 times equivalent to the fluorine concentration of the fluorine-containing wastewater, and the amount of aluminum flocculant is 0.002 to 0.1 times equivalent to the fluorine concentration in terms of aluminum. To do.

  By this means, a treatment apparatus for fluorine-containing waste water without excessive injection of chemicals can be obtained.

  According to the present invention, it is possible to provide a fluorine wastewater treatment method that does not excessively add chemicals, generates less sludge, and satisfies the fluorine emission standards.

  The best mode for carrying out the present invention will be described below with reference to the drawings.

(Embodiment 1)
FIG. 1 is a process diagram of a method for treating fluorine-containing wastewater according to Embodiment 1 of the present invention.

  As shown in FIG. 1, the fluorine-containing wastewater is separated into treated water and sludge through a reaction step 11, a neutralization step 12, a coagulation step 13, and a solid-liquid separation step 14 for reacting fluorine and calcium.

  The sludge is taken through a dehydration drying process 15 to a cement factory as a collection destination and recycled as a cement raw material.

In the reaction step 11, an aluminum salt such as calcium aluminate produced by reacting slaked lime (chemical formula is Ca (OH) ₂ ) and a sulfate band (chemical formula is Al ₂ (SO ₄ ) ₃ ) in the preliminary reaction step 16, Input as a calcium source.

  Further, in the neutralization step 12, sulfuric acid is added as a neutralizing agent, and in the aggregation step 13, a polymer is input as an organic flocculant.

  As other chemicals, calcium chloride can be used instead of slaked lime, PAC (polyaluminum chloride) can be used instead of sulfuric acid band, and hydrochloric acid can be used instead of sulfuric acid. Hated.

  In the treatment method of the present invention, since no chloride is used as a chemical, the generated sludge can be easily recycled as a cement raw material.

  Next, an example of the fluorine-containing wastewater treatment apparatus of the present invention is shown in FIG.

  As shown in FIG. 2, the fluorine-containing wastewater is separated into treated water and sludge in the sedimentation tank 4 through the reaction tank 1, the neutralization tank 2, and the aggregation tank 3. The reaction tank 1 is charged with an aluminum salt such as calcium aluminate, which is a reaction product, from a preliminary reaction tank 5 for reacting slaked lime with a sulfate band.

  The input amount of slaked lime is 1 to 3 times equivalent, preferably 1.5 times equivalent to the fluorine concentration detected by the fluorine concentration detecting means 6 of the fluorine-containing waste water, and the input amount of the aluminum flocculant is the fluorine concentration in terms of aluminum. By setting the equivalent to 0.002 to 0.1-fold equivalent, preferably 0.01-fold equivalent, the optimal amount of the drug can be charged and excessive charging can be prevented.

  The pH in the reaction tank is 10.5 to 12, preferably 11.5, and the amount of sulfuric acid charged in the neutralization tank 2 is controlled by the pH detected by the pH detection means 7 in the neutralization tank 2 and neutralized. The pH in the tank 2 is adjusted to 7-8.

If the pH is 7 or less, slaked lime Ca (OH) ₂ is added to raise the pH. Next, in the coagulation tank 3, 2-3 ppm of polymer is added as an organic coagulant to promote coagulation, and is sent to the next settling tank 4 for solid-liquid separation into sludge and treated water.

  The characteristic feature of the present processing method is that it is found that the reaction is most promoted by focusing on the order of the chemicals in the reaction step. That is, it has been found that an aluminum salt such as calcium aluminate produced by reacting two kinds of chemicals, slaked lime and a sulfate band, has a great effect of removing fluorine.

  The process that led to the present invention is a test conducted by changing the fluorine content of waste water, the order of adding the chemicals, and the pH adjustment, and will be described in detail below with reference to FIG. However, the actual tested apparatus does not have the preliminary reaction tank 5, and slaked lime and a sulfuric acid band were put into the reaction tank 1 simultaneously.

First, for wastewater containing about 400 ppm of fluorine, slaked lime is 1.5 times equivalent (about 2340 ppm) of wastewater-containing fluorine in reaction tank 1, and sulfuric acid band is converted to aluminum and 0.1 times equivalent of wastewater-containing fluorine ( About 200 ppm) was added at the same time and stirred for about 30 minutes. At that time, the reaction between slaked lime and sulfate band is
4Ca (OH) ₂ + SiO ₂ , Al ₂ O ₃
→ CaO · SiO ₂ · nH ₂ O, 3Ca · Al ₂ O ₃ · nH ₂ O
The inventors estimated that aluminum salts such as calcium aluminate 3Ca.Al ₂ O ₃ .nH ₂ O were produced.

At this time, the pH in the reaction vessel 1 was 11.5.
When the pH is around 11.5, this calcium aluminate is combined with fluorine to produce calcium fluoroaluminate (chemical formulas estimated as CaAlF ₅ , Ca ₂ AlF ₇ , Ca ₃ AlF ₉ ,...). It has a coprecipitation effect that the chemical compound is adsorbed or combined and precipitates, and it is considered that fluorine in the waste water can be removed more.

  Thereafter, in the neutralization tank 2, sulfuric acid was added for neutralization and left for about 30 minutes. The pH at this time was 7-8. Thereafter, 1 to 3 mg / L of an organic flocculant polymer is added to the coagulation tank 3, and the wastewater is introduced into the precipitation tank 4, which is a solid-liquid separation process. . The fluorine concentration of the treated water at that time was 4 to 8 mg / L.

  On the other hand, in the background art, as described above, 7000 ppm of calcium hydroxide and 4000 ppm of sulfuric acid band are added to 365 ppm of fluorine ions in the waste water, and the treatment concentration is lower than that of the treatment method and treatment apparatus of the present invention. However, calcium hydroxide is used approximately 3 times and sulfate band is used 20 times. In the treatment method and treatment apparatus of the present invention, the amount of chemical used is greatly reduced, and the generation of sludge is also reduced to the amount of chemical used. Proportionally decreases.

  Furthermore, in the background art, the pH of the treated water is 10 or more and a neutralization step / neutralization tank is required for the post-treatment, whereas in the present invention, the pH of the treated water is 7 to 8, and the post-treatment In addition, the neutralization process and neutralization tank are unnecessary.

  Conventionally, it was necessary to stir for 30 minutes in this reaction tank to ensure the reaction time, but in this test, the discharge standard of 8 mg / L could be satisfied even in 15 minutes and 10 minutes, and the reaction time was The reaction tank 1 can be made smaller for the same amount of treated water.

  In addition, from the effect of calcium aluminate, the reaction with fluorine should be accelerated when aluminum salt such as calcium aluminate is introduced directly into the reaction tank 1 rather than simultaneous addition of slaked lime and sulfuric acid band. In the case where an aluminum salt such as calcium is not commercially available, it is considered more effective that the preliminary reaction tank 5 previously reacts slaked lime with a sulfate band to produce an aluminum salt such as calcium aluminate.

  In this test, the fluorine content in the wastewater was also reduced to 140 ppm fluorine, and it was confirmed that the treatment standard could be satisfied with the amount of chemical used in proportion to the fluorine concentration.

  The method and apparatus for treating fluorine-containing wastewater according to the present invention can reduce the amount of fluorine in wastewater containing fluorine to below the discharge standard, and also reduce the amount of chemical used and sludge.

Process flowchart showing an example of the processing method of the present invention The schematic diagram which shows an example of the processing apparatus of this invention

Explanation of symbols

DESCRIPTION OF SYMBOLS 1 Reaction tank 2 Neutralization tank 3 Aggregation tank 4 Settling tank 5 Preliminary reaction tank 6 Fluorine concentration detection means 7 pH detection means

Claims (8)

A fluorine-containing wastewater treatment process comprising a preliminary reaction step of reacting slaked lime with an aluminum flocculant in a treatment process of fluorine-containing wastewater, and a reaction step of charging the fluorine-containing wastewater with a product in the preliminary reaction step as a calcium source Processing method. A method for treating fluorine-containing wastewater, comprising a reaction step of adding aluminum salt as a calcium source to fluorine-containing wastewater in a treatment process of fluorine-containing wastewater. A method for treating fluorine-containing wastewater, comprising a reaction step of simultaneously adding slaked lime and aluminum flocculant to fluorine-containing wastewater in a treatment process of fluorine-containing wastewater. The processing method of the fluorine-containing wastewater of Claim 1 or 3 which determines the input amount of slaked lime and an aluminum flocculant based on the fluorine concentration of fluorine-containing wastewater. 5. The amount of slaked lime input is 1 to 3 times equivalent to the fluorine concentration of fluorine-containing wastewater, and the amount of aluminum flocculant input is 0.002 to 0.1 times equivalent to the fluorine concentration in terms of aluminum. The treatment method of fluorine-containing waste water as described. An apparatus for treating fluorine-containing wastewater, comprising: a preliminary reaction tank for reacting slaked lime with an aluminum flocculant, and a reaction tank for charging the fluorine-containing wastewater with a product in the preliminary reaction tank as a calcium source. The fluorine-containing wastewater treatment apparatus according to claim 6, wherein a fluorine-concentration detection means for detecting the fluorine concentration of the fluorine-containing wastewater is provided, and the input amounts of slaked lime and aluminum flocculant are determined according to the detected fluorine concentration. The amount of slaked lime is 1 to 3 equivalents of the fluorine concentration of fluorine-containing wastewater, and the amount of aluminum flocculant is 0.002 to 0.1 equivalents of the fluorine concentration in terms of aluminum. The fluorine-containing waste water treatment apparatus as described.

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