JP2009233605A - Treatment method of boron fluoride-containing water - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To provide a treatment method of boron fluoride-containing water capable of efficiently decomposing and removing boron fluoride while suppressing the charge amount of a chemical agent, and a manufacturing method of a decomposition agent of boron fluoride using it. <P>SOLUTION: The treatment method of boron fluoride-containing water includes: a first process for decomposing boron fluoride being a compound of fluorine and boron by adding an aluminum compound to the boron fluoride-containing water; a second process for performing solid-liquid separation by adding a calcium compound to the boron fluoride-containing water in order to treat fluorine produced by decomposition; and a third process for obtaining an aluminum-containing precipitate by solid-liquid separation by adding an aluminum salt to the liquid obtained by solid-liquid separation. The aluminum-containing precipitate obtained in the third process is used for the decomposition of the boron fluoride-containing water in the first process. <P>COPYRIGHT: (C)2010,JPO&INPIT

Description

  The present invention relates to a method for treating borofluoride-containing water, and more particularly, to a treatment method in which an aluminum compound is added and adjusted to be acidic and decomposed into fluorine and boron, and a method for producing a borofluoride decomposing agent used in the method. .

  Fluorine (F) is currently provided with wastewater standards, and is used, for example, in the manufacture of glass products, pharmaceuticals, cosmetics, resin products, plating products, etc., and is contained in the manufacturing wastewater. It is also included in flue gas desulfurization effluent from coal-fired power plants, waste incineration scouring effluent, and nickel plating factory effluent. Fluorine is known to cause acute toxicities such as vomiting, gastritis, and kidney damage, and chronic toxicities such as osteomalacia and motor dysfunction when taken in large quantities by humans. Therefore, in Japan, the wastewater standard value has recently been strengthened from 15 ppm to 8 ppm, and the treatment of fluorine wastewater is regarded as important.

  As a method for treating such fluorine wastewater, a method of reacting with calcium and fixing to calcium fluoride is generally used, and a method of treating by adding an aluminum salt as an advanced treatment is widespread. However, if boron is contained in the fluorine waste water, a substance present as a compound form of borofluoride is generated, and it is difficult to remove by the simple calcium method or aluminum method described above.

  Therefore, as a method of decomposing and removing borofluoride in the waste water, for example, heating the liquid, adding trivalent aluminum ions, pyrolyzing the borofluoride, making calcium into an alkali, and incorporating fluorine into the silicon salt A method for precipitation and removal has been proposed (see Patent Document 1).

  Also, a dust removal tower that removes dust and gaseous compounds contained in exhaust gas using an aqueous absorbing liquid, and an oxide such as sodium, potassium, ammonium, and calcium, and a compound such as carbonate on the downstream side of the dust removal tower Fluorine compounds contained in desulfurization effluent by adding a water-soluble iron compound to the desulfurization effluent extracted from the absorption liquid circulation tank of the dust removal tower A method for treating desulfurized wastewater including a step of decomposing and a device for carrying out the method has been proposed (see Patent Document 2).

  Further, an aluminum compound is added to waste water containing borofluoride so that the aluminum element is 0.1 to 5 mol with respect to 1 mol of fluorine element contained in the borofluoride, and the pH is kept at 6 or less, and aeration The processing method including the process to perform is proposed (refer patent document 3). This aluminum compound can be added by dehydrating sludge containing aluminum hydroxide, and the fluorine component can be fixed in a short time by aeration. Further, it is disclosed that the boron component can be fixed by adding a magnesium component, and other components such as lead can be fixed by adding an iron and / or aluminum component.

  However, the conventional method of decomposing borofluoride using an aluminum compound or an iron compound has a problem in that the cost increases because a large amount of chemicals or auxiliary materials must be input.

  Therefore, it is desired to provide a method for efficiently decomposing and removing borofluoride with a reduced amount of chemicals, and promptly providing a borofluoride decomposing agent that can efficiently decompose and remove borofluoride. This is the current situation.

Japanese Patent Laid-Open No. Sho 62-22796 JP-A-9-131593 JP 2000-189980 A

  An object of the present invention is to solve various problems in the prior art and achieve the following objects. That is, the present invention provides a method for treating borofluoride-containing water, which enables efficient decomposition and removal of borofluoride with a reduced amount of drug, and a method for producing a borofluoride decomposing agent used in the method. For the purpose.

  As a result of intensive studies by the present inventors in order to solve the above problems, new materials such as aluminum chloride have been added so far to decompose borofluoride. By using sludge separated and separated, aluminum (Al), which has been landfilled as dehydrated starch, can be used effectively, and borofluoride can be decomposed at low cost and energy saving without adding new materials. I found out.

The present invention is based on the above findings by the present inventors, and means for solving the above problems are as follows. That is,
<1> a first step of decomposing borofluoride by adding an aluminum compound to borofluoride-containing water that is a compound of fluorine and boron;
A second step of adding a calcium compound to treat fluorine generated by decomposition, and solid-liquid separation;
Adding an aluminum salt to the liquid obtained by the solid-liquid separation, and obtaining a porridge containing aluminum by solid-liquid separation, and
The method for treating borofluoride-containing water is characterized in that the porcelain containing aluminum obtained in the third step is used for decomposition of the borofluoride-containing water in the first step.
<2> In the method for treating borofluoride-containing water by adding an aluminum compound to borofluoride-containing water, which is a compound of fluorine and boron, and decomposing the borofluoride-containing water, the aluminum compound is used as the aluminum compound. This is a method for treating borofluoride-containing water.
<3> The borofluoride-containing water according to any one of <1> to <2>, wherein the porcelain containing aluminum in the third step is precipitated by a thickener and collected from an underflow port of the thickener. It is a processing method.
<4> The aluminum compound is aluminum hydroxide that can be dissolved as an aluminum ion in an acidic region or an alkaline region,
The borofluoride-containing water according to any one of <1> to <3>, wherein the calcium compound is at least one of slaked lime or calcium carbonate, and the aluminum salt is at least one of aluminum chloride and aluminum sulfate. It is a processing method.
<5> An aluminum compound is added to borofluoride-containing water to adjust the pH to 2 to 4, then a calcium compound is added to adjust the pH to 9 to 10, an aluminum salt is added to the supernatant to adjust the pH to 6 to 7, and the residue is generated. A method for producing a borofluoride decomposing agent obtained by solid-liquid separation.

  In the method for treating borofluoride-containing water of the present invention, the amount of novel chemicals used during treatment of borofluoride-containing water was suppressed. Moreover, the porcelain which can decompose borofluoride efficiently was able to be manufactured. Boron fluoride is decomposed by adding an aluminum compound at high temperature and low pH, but the addition ratio of Al / F (mol) = 1.1 or less is sufficient, and the starch generated by the above-mentioned advanced treatment is sufficient. It was found that the decomposition performance of aluminum was exhibited even when the product was used as an additive, and the decomposition rate was higher than that of a reagent of aluminum hydroxide having a similar composition.

  According to the present invention, various problems in the prior art can be solved, and a borofluoride-containing water treatment method capable of efficiently decomposing and removing borofluoride with a reduced amount of chemicals, and a borofluoride used in the method. A method for producing a chemical decomposition agent can be provided.

  The method for treating borofluoride-containing water of the present invention includes a first step, a second step, and a third step, and further includes other steps as necessary.

<First step>
The first step is a step of adding an aluminum compound to borofluoride-containing water that is a compound of fluorine and boron to decompose the borofluoride.

The borofluoride is a compound of boron (B) and fluorine (F), but combines with other salts such as sodium to form various borofluorides. In aqueous solution, it exists as borofluoride ion (BF ₄ ⁻ ). In the present invention, borofluoride ion contained in industrially generated waste water can be applied.

The said aluminum compound should just melt | dissolve in borofluoride containing water and an aluminum ion produces | generates. Aluminum is an amphoteric metal that dissolves in both acid and alkali, but preferably an aluminum compound that dissolves in an acidic region, which is a decomposition condition of borofluoride, is economical.
In the method for treating borofluoride-containing water, the residue containing aluminum obtained in the third step is used for the decomposition of the borofluoride-containing water in the first step.

In the first step, the addition amount of the aluminum compound may be appropriately set depending on the concentration of the borofluoride in the target treated water, and the molar ratio of aluminum to fluorine is preferably 0.3 or more in terms of Al / F. 0 or more is more preferable. In addition, it is preferable that the upper limit of molar ratio (Al / F) is 1.1 or less. When the molar ratio (Al / F) is less than 0.3, the borofluoride is not sufficiently decomposed and the treatment needs to be repeated.
Further, the pH is set to an acidic region of 2 to 4, and the aluminum compound is dissolved in aluminum ions, and at the same time, the borofluoride ions are converted into 3BF ₄ ⁻ + 2Al ³⁺ + 6H ₂ O → 2AlF ₆ ^{3 −} + 3H ₃ BO ₃ + 3H ⁺ Thus, it is decomposed into fluorine and boron substances.

<Second step>
The second step is a step in which a calcium compound is added and solid-liquid separation is performed in order to treat fluorine generated by decomposition.

Examples of the calcium compound include slaked lime and calcium carbonate.
In the second step, the solution before the reaction is acidic, but a calcium compound, preferably slaked lime is added, and the pH is preferably neutralized to about pH 9 to 10, and the type of calcium compound is adjusted to this range. Adjust the addition amount. Under these conditions, fluorine decomposed in the first step is fixed and removed as calcium salts such as calcium fluoride, and at the same time, harmful substances such as lead, cadmium and chromium contained in the wastewater are fixed and removed. Can do. The residue produced in this step is subjected to solid-liquid separation and the supernatant liquid side is used in the next third step.

<Third step>
The third step is a step in which an aluminum salt is added to the liquid obtained by solid-liquid separation, and an article containing aluminum is obtained by solid-liquid separation.
An aluminum salt is added to the trace fluorine-containing material contained in the liquid obtained by the solid-liquid separation to generate an aluminum-containing product, and the aluminum-containing product can be obtained by solid-liquid separation.

In the second step, fluorine is fixed as calcium fluoride, but the third step is a step for further treating fluorine ions of about 20 ppm due to the solubility of calcium fluoride.
In the third step, an aluminum salt is added to the liquid obtained from the second step.
Examples of the aluminum salt include aluminum chloride and aluminum sulfate.
The addition amount of the aluminum salt is adjusted so that the molar ratio of aluminum to fluorine is Al / F = 5 or more.
In addition, since the pH of waste water falls by adding aluminum salt, it adjusts to pH 6-7 using an alkali chemicals. Specifically, it is preferable to adjust to pH 6.7. Examples of the alkaline agent include caustic soda and slaked lime.
Since the aluminum-derived aluminum compound used as a chemical is generated as a residue by the advanced treatment of fluorine, the residue is recovered by solid-liquid separation. The collected residue is used as an aluminum compound in the first step. Thereby, borofluoride can be decomposed | disassembled efficiently.

  The porcelain containing aluminum obtained in the third step has an excellent ability to decompose borofluoride, and the molar ratio of aluminum to total fluorine in the wastewater to be treated is 0.3 or more in Al / F and decomposes borofluoride. Is possible. That is, the porridge can be used as an alternative to the aluminum agent to be newly added in the first step, and the amount used can be reduced.

  In addition, the sediment containing the aluminum compound obtained in the third step contains a trace amount of fluorine removed from the waste water, and there is a concern that fluorine may be concentrated in the process system by repeating this sediment. Although it is basically a fluorine compound that does not contain boron, even if the fluorine contained in the porridge is dissolved again in the first step, it is surely converted into calcium fluoride in the second step. Since it is removed, there is no risk of concentration.

  The temple obtained in this way contains aluminum. By using this deposit as the aluminium compound, it is possible to perform highly efficient removal by reducing the input amount of a new chemical against the decomposition of borofluoride. It can be used as a substitute for all or part of the aluminum drug, and preferably is used as a substitute for the whole amount. A new aluminum agent may be used only when Al / F (mol) = 0.3 or less as a result of using the entire amount. Although it depends on the wastewater content of the borofluoride, the use of about 1% by mass to 20% by mass with respect to the inflowing wastewater basically simplifies operational management.

  In any stage of the first process to the third process, the liquid temperature is about 40 ° C. to 80 ° C. at the time of addition or reaction, or 40 when the temperature at the time of generation such as waste incineration wastewater is high. It is better to keep the temperature below ℃. This is to improve the reactivity and precipitation. The liquid temperature is preferably 50 ° C to 80 ° C.

  Note that a flocculant may be added after the generation of the porridge to further improve the filterability and precipitation. There is no restriction | limiting in particular as this flocculant, According to the objective, it can select suitably, For example, a commercially available polymer additive can be used.

Due to the large amount of wastewater generated in the industry, the amount of shrine generated is also large. For this reason, a thickener having a necessary and sufficient cross-sectional area as equipment to be used is used for solid-liquid separation from the generation of temples. If the thickener is used, the temple is settled at the bottom to form a sediment sedimentation layer, and the temple can be collected by extracting the temple from this layer. Thickeners can be easily collected from the underflow port. The porridge collected from the third step may be transferred to the first step by a pump or the like and added.
The thickener by the thickener in the second step and the supernatant liquid in the third step can be appropriately post-processed, discarded and discharged.

  Examples of the present invention will be described below, but the present invention is not limited to these examples.

The Example of the decomposition processing method of the borofluoride containing waste_water | drain by this invention is described in detail. First, the smoke ash in the waste incineration plant is washed with industrial water, the smoke-washed waste water after washing is guided to the first reaction tank, and controlled to pH 2-3 with calcium carbonate milk (first step), In the second reaction tank, the mixture was neutralized with lime milk to pH 9.3 and settled and separated by the first thickener (second step).
Next, the supernatant was introduced into a third reaction vessel, and aluminum chloride was added at a ratio of 187 ppm to the supernatant, and after stirring and mixing for 15 minutes, caustic soda was added to adjust the pH to 6.7. Next, the generated agglomerates were settled and separated by the second thickener, and the starch precipitated at the bottom was collected from the underflow (third step).
In addition, since the borofluoride concentration of the smoke washing wastewater in the first reaction tank is low, in order to clarify the effect of adding starch and make it easy to evaluate, the smoke washing wastewater is collected so that the concentration of borofluoride is 22 ppm. A simulated solution to which a sodium borofluoride solution was added was prepared.

  Next, in order to change the Al / F ratio, three types A, B, and C having different total F concentrations were prepared as the smoke-washing waste water. Table 1 shows the analysis result of each waste water. The total F concentration was measured according to JIS K0102. The amount of Al was measured according to JIS K0102 (1998) 58,4.

<No. 1 and no. 3-8>
A sodium borofluoride solution was added to a BF ₄ concentration of 22 ppm, and each effluent was poured therein to a total volume of 500 ml. As shown in Table 3, the reaction temperature was set to 50 ° C to 75 ° C and held for a predetermined time.
Next, as shown in Table 3, 25 to 75 ml of aluminum-containing residue A or B was added, and lime milk was further added and adjusted so that the pH of the waste water was 2 to 4. Table 2 shows the components of the aluminum-containing articles A and B.

Next, after stirring for 5 to 10 minutes with a stirrer, the mixture was stirred for 20 minutes while adding lime milk again to adjust the pH to 9 to 10.
Thereafter, filtration under reduced pressure was performed using a filter paper having a retained particle diameter of 1 μm, and the total F concentration in the filtrate was measured according to JIS K0102. Further, the BF ₄ concentration in the filtrate was measured by an absolute calibration curve method using a BF ₄ ion selective electrode.
The BF ₄ decomposition rate was calculated by the following formula. The results are shown in Table 3.
BF ₄ {(BF ₄ concentration of BF ₄ concentration / pretreatment after treatment) 1} decomposition rate = × 100

<No. 2>
Since aluminum in the aluminum-containing deposit is gel aluminum hydroxide, an experiment was conducted using a commercially available aluminum hydroxide reagent having the same form.
The aluminum hydroxide reagent was added to the wastewater A (218 mg) so that Al / F (mol) = 0.3, which is the same as the Al / F ratio when 37 ml of aluminum-containing residue was added to the wastewater A. The subsequent experimental procedure is the same as above. The decomposition rate of BF ₄ was measured in the same manner. The results are shown in Table 3.

  From the results in Table 3, it was found that borofluoride can be decomposed when the molar ratio of aluminum to total fluorine in the wastewater is 0.3 or more in Al / F.

  The method for treating borofluoride-containing water of the present invention enables efficient decomposition and removal of borofluoride with a reduced amount of chemical compared to conventional methods, so that borofluoride in wastewater is efficiently decomposed and removed. can do.

Claims (5)

Adding an aluminum compound to borofluoride-containing water, which is a compound of fluorine and boron, and decomposing the borofluoride;
A second step of adding a calcium compound to treat fluorine generated by decomposition, and solid-liquid separation;
Adding an aluminum salt to the liquid obtained by the solid-liquid separation, and obtaining a porridge containing aluminum by solid-liquid separation, and
A method for treating borofluoride-containing water, wherein the residue containing aluminum obtained in the third step is used for decomposition of the borofluoride-containing water in the first step.   2. The borofluoride-containing water according to claim 1, wherein an aluminum compound is used as the aluminum compound in a treatment method of a borofluoride-containing water that is decomposed by adding an aluminum compound to borofluoride-containing water that is a compound of fluorine and boron. Processing method.   The method for treating borofluoride-containing water according to any one of claims 1 to 2, wherein the aluminum-containing product in the third step is precipitated by a thickener and collected from an underflow port of the thickener. The aluminum compound is aluminum hydroxide that can be dissolved as aluminum ions in the acidic region or alkaline region,
The method for treating borofluoride-containing water according to any one of claims 1 to 3, wherein the calcium compound is at least one of slaked lime or calcium carbonate, and the aluminum salt is at least one of aluminum chloride and aluminum sulfate.   Aluminum compound is added to borofluoride-containing water to pH 2-4, then calcium compound is added to pH 9-10, and aluminum salt is added to the supernatant to adjust pH 6-7, and the residue is separated into solid and liquid. A process for producing a borofluoride decomposing agent characterized by the following.