JP4875025B2 - Polyvinyl alcohol molding - Google Patents

Description

  The present invention relates to a polyvinyl alcohol molded product capable of efficiently removing a boron compound from boron-containing water, and a method for removing the boron compound from boron-containing water using the molded product.

  Boron compounds are used in various applications such as pharmaceuticals, cosmetics, soaps, electroplating, glass, etc., not only at the stage of producing boron compounds, but also at the stage of using boron compounds, and further by replacing the used boron compounds. In each stage such as the stage of incineration and disposal of the product containing it, water containing a boron compound is discharged into the natural world as waste water.

  The effect of boron on the human body is not clear, but it is said that there are health problems such as vomiting and abdominal pain by ingesting a high-concentration solution. It recognized.

  In addition, it has been reported that a high concentration of boron inhibits the growth of plants. From this background, the drainage standard for boron other than the sea area was set at 10 mg / L in 2001. However, there is no effective and inexpensive processing technology, and a temporary standard is set.

  Various methods for treating boron-containing water have been proposed as countermeasures. Basic removal means mainly include the following techniques, but none of them is satisfactory in terms of effect and price.

  For example, a method of treating boron-containing water using a rare earth element hydroxide (Patent Document 1) is disclosed, but in this method, the rare earth element hydroxide itself used as a treating agent has a moldability. Since it is difficult to handle, it is necessary to support a rare earth element hydroxide on a carrier such as a resin to form a granular material. As a result, the contact area between the rare earth element hydroxide and the liquid to be treated becomes small, and it becomes difficult to exhibit sufficient adsorption performance.

  Also disclosed is a method for adsorbing boron by using an ion exchange resin having an N-methylglucamine group, a type I or type II strong basic anion exchange resin, a weak basic anion exchange resin, or the like. (Patent Documents 2, 3, and 4). However, in order to use an ion exchange resin, the process which makes an ion exchange column into a dehydration state previously is required, and the operativity becomes complicated. Moreover, since these ion exchange resins are expensive, it is disadvantageous in terms of cost reduction to use for large capacity use such as waste water treatment.

  In Patent Document 5, in order to improve the performance of an adsorbent, a boron-adsorbing compound is supported on an open-cell structure having macropores connected to each other and mesopores having a specific pore diameter in the wall, A device for increasing the contact area is disclosed. However, since the adsorption principle is the same as that of the ion adsorption resin, it is considered that this method has the same problem as described above.

  Further, an adsorption sheet for adsorbing an airborne boron compound using a PVA fiber by utilizing the fact that a hydroxyl group of a polyvinyl alcohol (hereinafter abbreviated as PVA) fiber coordinates with boron in the boron compound to form a complex. (Patent Document 6) is also disclosed.

  However, since this adsorption sheet is produced by compound spinning of ethylene-modified PVA and a thermoplastic polymer and then leaching this PVA using hot water, the process for obtaining the sheet is long and the cost is high. In this case, it is necessary to leached PVA, so that it becomes difficult not only to control the residual amount and state of PVA after leaching, but also to reduce the weight of PVA itself having boric acid adsorption ability. As a result, the suction sheet has a problem that the suction capacity is reduced.

  Furthermore, a treatment agent for boron-containing water comprising a PVA gel (Patent Document 7) is also disclosed. However, this gel-like body repeats the operation of freezing a raw material solution obtained by dissolving 10 to 60 g of PVA in 1 liter of water at −20 to −70 ° C. for about 12 hours and then thawing at room temperature over 1 hour several times. Therefore, there is a problem that not only the mechanical strength is extremely low but also water resistance is low.

  Also disclosed is a boron adsorption gel (Patent Document 8) in which a polymer having stimuli response and a polymer having boron adsorption ability have a three-dimensional structure formed by crosslinking or the like. However, this method needs to be prepared by blending a boron-adsorbing polymer and a stimulus-responsive polymer from polymerization, so that a widely used polymer cannot be used, which is disadvantageous in terms of cost.

  In addition to these, methods of coagulating sedimentation using sulfate bands, ferrous salts of inorganic acids, or aluminum salts and slaked lime have been proposed, but all require the addition of a large amount of chemicals, resulting in a large amount of sludge. Not only occurs, but also a considerable concentration of boron remains after the treatment.

JP2004-50069 JP 2001-247305 A JP 2001-33531 A JP 2004-298738 JP2004-66153 JP2007-32152A JP2002-186976 JP 2004-292479 A

An object of the present invention is to provide a PVA molded product that has not only excellent portability and handling properties but also high boron adsorption.
Another object of the present invention is to provide an inexpensive and reusable PVA molded article that is not only excellent in boron adsorptivity.

Still another object of the present invention is to provide a PVA molded product that can be processed at low cost and efficiently even for a large volume of boron-containing water.
Another object of the present invention is to provide a method capable of efficiently removing a boron compound from boron-containing water using such a PVA molded product.

  In order to solve the above-mentioned problems, the present inventors have made extensive studies, and as a result, even when the polyvinyl alcohol molded product has a water resistance and a reduced hydrophilicity, The adsorbent structure having a boron adsorbing seat can be realized by the above, and it has been found that handling efficiency and boron adsorbing ability, both of which have been difficult in the past, can be achieved by setting the elution rate to 10% or less. I let you.

That is, the present invention is a PVA molding used for removing a boron compound from boron-containing water, wherein the molding is composed of at least polyvinyl alcohol and a basic nitrogen-containing substance , and the polyvinyl alcohol is The nitrogen-containing substance is supported and the degree of swelling is 80% or more and the elution rate is 10% or less. The polyvinyl alcohol may have a saponification degree of 88 mol% or more, and an average polymerization degree of about 500 to 5,000.

Also, such nitrogen-containing materials, for example, amine compounds, may be at least one kind selected from nitrogen-containing substance consisting of imine compounds and amide compounds. Further, the ratio of the nitrogen-containing substance to 100 parts by weight of polyvinyl alcohol may be about 5 to 50 parts by weight.

  Moreover, although a granular material and a powdery material may be sufficient as a PVA molded object, it is preferable that it has a fiber shape, for example.

  Furthermore, the present invention is a method for treating boron-containing water, wherein the polyvinyl alcohol molded product is brought into contact with boron-containing water under a pH of 6 or more (for example, about pH 6 to 14). Is included.

In this specification, the degree of swelling and the dissolution rate are defined as follows.
The weight of the PVA molded product dried at 105 ° C. for 4 hours was weighed as A (g), and then this molded product was immersed in 30 ° C. water at a bath ratio of 100 or more for 30 minutes, and then rotated at 3000 rpm for 5 minutes. When the weight weighed by centrifugal dewatering for 5 minutes is B (g), and the weight of the dehydrated molding dried at 105 ° C. for 4 hours and weighed is C (g), the degree of swelling (%) and The dissolution rate (%) can be expressed by the following formulas (1) and (2), respectively.

Swelling degree = (B−A) / A × 100 (1)
Dissolution rate = (AC) / A × 100 (2)
However, when a salt such as sodium sulfate is adhered to the PVA molded product as a sample, the adhesion rate of the salt is obtained by a roasting method, and the initial weight is corrected to the polymer amount.

  Here, the degree of swelling is used as an index that expresses the ratio of moisture taken into the molded body, excluding moisture adhering to the surface of the molded product. In addition, when this numerical value is large, when processing a boric acid solution, it means that it can be utilized as an adsorption seat even inside a molded object.

  According to the present invention, a molded article formed of PVA is formed by forming a molded article for adsorbing and removing a boron compound from boron-containing water using PVA having a specific swelling degree and dissolution rate. In addition, since the boron compound can be adsorbed to a high degree, both the boron adsorption performance and the handleability, portability, and / or storage stability derived from the water-resistant PVA molded product can be achieved.

  Moreover, in this invention, since the molded product excellent in boron adsorption | suction performance is obtained using PVA currently mass-produced, it is advantageous in terms of cost.

  Moreover, when PVA has a specific saponification degree and average polymerization degree, the said handling property, carrying property, and preservability can be improved.

  Furthermore, when a nitrogen-containing substance is supported on PVA, the boron adsorption performance of PVA can be further improved without reducing the boron adsorption locus of PVA.

  Moreover, when a PVA molding has a fiber shape, a contact area with the boron compound of a molding can be increased, and the boron adsorption | suction performance of PVA can be improved.

[PVA molded product]
The PVA molding of the present invention is used for removing boron compounds from boron-containing water. And in the PVA molded product used in the present invention, from the viewpoint of adsorbing boron compounds, the degree of swelling needs to be 80% or more, preferably about 85-400%, more preferably 90-300%. It may be a degree. Further, the elution rate of the PVA molded article needs to be 10% or less, preferably 5% or less, and more preferably 3% or less.
The PVA molded product of the present invention is not only excellent in handleability, portability, and storage stability, but can be reused without destroying its shape even when washed with water.

(PVA polymer)
The PVA molded product is composed of polyvinyl alcohol (that is, a PVA polymer). The PVA polymer is not particularly limited as long as it has a vinyl alcohol unit as a main component, and may have other constituent units (modified units) as desired as long as the effects of the present invention are not impaired. Examples of such a structural unit include olefins (for example, ethylene, propylene, butylene, etc.), acrylic acids (for example, acrylic acid and salts thereof, acrylic esters such as methyl acrylate, etc.), methacrylic acids (for example, Methacrylic acid and salts thereof, methacrylic acid esters such as methyl methacrylate), acrylamides (for example, acrylamide, N-methylacrylamide, etc.), methacrylamides (for example, methacrylamide, N-methylol methacrylamide, etc.), N -Vinyl lactams (for example, N-vinyl pyrrolidone, etc.), N-vinyl amides (for example, N-vinyl formamide, N-vinyl acetamide, etc.), vinyl ethers (for example, allyl ethers having a polyalkylene oxide in the side chain, Mechi Vinyl ether), nitriles (e.g., acrylonitrile, etc.), halogenated vinyl compound (vinyl chloride), unsaturated dicarboxylic acids (e.g., maleic acid and salts or anhydrides or esters thereof) and the like. These denaturing units can be used alone or in combination. Such a modified unit may be introduced by copolymerization or post-reaction.

  The ratio (molar ratio) of the modified unit to the vinyl alcohol unit is (vinyl alcohol unit) / (modified unit) = about 85/15 to 100/0, preferably about 88/12 to 99/1, and more preferably 90 / It is about 10 to 98/2. Of course, as long as the effect of the present invention is not impaired, addition of a flame retardant, an antioxidant, an antifreezing agent, a pH adjusting agent, a concealing agent, a coloring agent, an oil agent, a special functional agent, etc. in the polymer depending on the purpose. An agent may be included. These additives may be included alone or in combination.

  The degree of polymerization of the PVA polymer can be appropriately selected according to the purpose and is not particularly limited. However, from the viewpoint of imparting water resistance to PVA, the average degree of polymerization obtained from the viscosity of the 30 ° C. aqueous solution is 500 or more (for example, About 500 to 5000), preferably about 750 to 4000, and more preferably about 900 to 3000.

  Further, the saponification degree of the PVA polymer can be appropriately selected according to the purpose and is not particularly limited. However, from the viewpoint of imparting mechanical strength to the PVA molded product, for example, 88 mol% or more, preferably 90 It may be at least mol%, more preferably at least 95 mol%.

(Basic nitrogen-containing substances)
PVA molded product of the present invention, for improving the adsorption of the boron compound, it is carrying a basic nitrogen-containing materials. The reason why the addition of such a nitrogen-containing substance is advantageous in adsorbing boron compounds is not necessarily clear, but it is probably possible to create a basic atmosphere with a nitrogen-containing substance around the PVA molecule, It is expected that the interaction with boron compounds will increase.

  For example, examples of such nitrogen-containing substances include nitrogen-containing substances such as amine compounds, imine compounds, and amide compounds. In addition, you may use these nitrogen-containing substances individually or in combination of 2 or more types.

Specifically, the nitrogen-containing substance may be either a high-molecular nitrogen-containing substance or a low-molecular nitrogen-containing substance. For example, examples of the polymer nitrogen-containing substance include water-soluble nitrogen-containing polymers such as polyallylamine, polyvinylamine, polyethyleneimine, polytrimethyleneimine, polyacrylamide, polymethacrylamide, and polyaniline. As the low molecular-type nitrogen-containing _{substance, C 1-6} alkyl amines (ethylamine, etc.), hydroxylamine, methanol amine, ethanol amine, _{di-C 1-3} alkylamine (diethylamine, etc.), tri _{C 1-3} alkylamine (Such as triethylamine), low molecular weight amines such as ethylenediamine, propylenediamine, diethylenetriamine, triethylenetetramine; low molecular weight imines such as ethyleneimine, monoimine of propyleneimine, piperazine; urea, acetamide, formamide, dimethylformamide, dimethylacetamide, And low molecular weight amides such as ethanediamide and N-methylacetamide.

  Among these nitrogen-containing substances, particularly preferable substances include water-soluble nitrogen-containing polymers such as polyallylamine.

  In addition, from the viewpoint of achieving both the moldability of the PVA molded product and the adsorptivity of the boron compound, the ratio of the nitrogen-containing substance to 100 parts by weight of polyvinyl alcohol may be, for example, about 5 to 50 parts by weight, preferably It may be about 7.5 to 40 parts by weight.

  Furthermore, you may put various additives (A crosslinking agent, a pore formation agent, various stabilizers, a pH adjuster, a disinfectant, a coloring agent, a fragrance | flavor etc.) in a PVA molding as needed.

  Among these, the cross-linking agent is not particularly limited as long as the molecular chain of polyvinyl alcohol can be cross-linked. Dialdehydes), epoxy compounds (eg, ethylene glycol glycidyl ether, bisphenol A diglycidyl ether), methylol compounds (eg, urea resin initial condensate, melamine resin initial condensate, etc.), metal compounds (eg, titanium) , Aluminum, zirconium, tin, vanadium, chromium, copper, or a divalent metal salt such as cobalt). These crosslinking agents may be used alone or in combination of two or more. Of these crosslinking agents, dialdehydes such as glyoxal and glutaraldehyde are preferred.

  Examples of the porous forming agent include sodium chloride, sodium acetate, sodium phosphate, calcium carbonate, and calcium hydroxide. These porous forming agents may be used alone or in combination of two or more.

(Method for producing polyvinyl alcohol molded product)
The manufacturing method of the PVA molded product of the present invention can be appropriately selected according to the shape. For example, when the PVA molded product is in a fiber shape, the molded product can be manufactured by the following method.

  First, a spinning stock solution in which a PVA polymer is dissolved in a solvent is prepared. As the solvent for the spinning dope, various polar solvents can be used, for example, water, organic solvents [sulfoxides such as dimethyl sulfoxide (hereinafter referred to as DMSO); nitrogen such as dimethylacetamide, dimethylformamide, N-methylpyrrolidone, etc. Containing polar solvents; polyhydric alcohols such as glycerin and ethylene glycol], and mixtures thereof with swellable metal salts such as rhodan salts, lithium chloride, calcium chloride, and zinc chloride. These solvents can be used alone or in combination. Among these, water and DMSO are preferable in terms of process passability such as cost and recoverability.

  The polymer concentration in the spinning dope varies depending on the composition, degree of polymerization, and solvent. For example, if the average degree of polymerization of the PVA polymer is 1500 to 2500, it is about 10 to 20% by weight (preferably about 12 to 18% by weight). Is preferable from the viewpoint of spinning tension.

  When the additive is added, the additive may be added in advance to the solvent of the spinning dope before dissolving the PVA, or a solution or dispersion in which the additive is dissolved or dispersed in water is added to the PVA. You may add and mix in the melt | dissolution stock solution. Furthermore, you may add an additive with methods, such as immersion and spraying, to the fiber which finished the drying process once.

  When a cross-linking agent is used as an additive, the cross-linking agent may be added to the spinning dope, spun into a coagulation bath containing a reaction catalyst, and subjected to a cross-linking process until drying, or coagulation. It is also possible to apply a reaction catalyst in a subsequent process after the bath (for example, a stretching bath) and to perform a crosslinking treatment in the process up to drying. Furthermore, even if the fiber is once dried, a cross-linking treatment may be performed by adding a liquid containing a cross-linking agent to the fiber by a technique such as dipping or spraying, if necessary.

  In addition, when a porous forming agent such as calcium carbonate particles is used as an additive, the porous forming agent is extracted in the molding process or a subsequent process, and the fibers are made porous, thereby increasing the adsorption capacity of the boron compound of the PVA molded body. Can be bigger. For example, in this case, the calcium carbonate particles may be mixed with the spinning stock solution and once spun, and then the calcium carbonate particles in the raw yarn may be extracted with sulfuric acid.

  The obtained spinning dope is usually discharged from a nozzle into a solidified liquid having a solidifying ability with respect to the PVA polymer or a gas. Examples of the spinning method include wet spinning, dry wet spinning, and dry spinning.

  The coagulation bath used in wet spinning or dry wet spinning differs depending on whether the stock solvent is an organic solvent or water (or an aqueous solution). When the spinning dope is an aqueous solution, the solidification solvent constituting the coagulation bath is not particularly limited as long as it has a solidification ability for the PVA polymer, and examples thereof include inorganic salts such as sodium sulfate (sodium sulfate), ammonium sulfate, and sodium carbonate. An aqueous solution; an aqueous sodium hydroxide solution can be used. Alternatively, an alkaline coagulation bath may be used by adding boric acid to the stock solution.

  On the other hand, in the case of an undiluted solution using an organic solvent, it has a solidifying ability for PVA polymers such as alcohols such as methanol, ethanol, propanol and butanol, and ketones such as acetone, methyl ethyl ketone and methyl isobutyl ketone. An organic solvent can be used.

  The mixing method of the nitrogen-containing substance and PVA is not particularly limited in the polyvinyl alcohol molded product, but as such a method, for example, (I) the nitrogen-containing substance is added to the stock solution in which PVA is dissolved. Or a method of supporting a nitrogen-containing substance on PVA by dissolving or dispersing the resin, or (II) a method of allowing a nitrogen-containing substance to permeate and support a molded product in the steps after spinning. Good.

  Furthermore, in the case of a low molecular weight nitrogen-containing substance, the low molecular weight nitrogen-containing substance is once adsorbed on an adsorbent such as zeolite or activated carbon in order to prevent the pH from increasing due to this substance and inhibiting the moldability. Then, together with the adsorbent, it may be supported on PVA by the method described above.

  After such a coagulation bath, an extraction bath may be passed through in order to extract and remove the solvent of the spinning dope from the solidified yarn. For example, an organic solvent such as DMSO may be removed from the raw yarn by washing the fiber with an alcohol such as methanol.

  Furthermore, you may perform processes, such as wet extending | stretching by a well-known or usual method as needed. The raw yarn or drawn yarn that has undergone these treatment steps is usually subjected to a drying step.

  Further, the dried raw yarn or drawn yarn may be subjected to a heat treatment such as dry heat drawing, if necessary. The most important point here is that the PVA molded product has practical water resistance (that is, an elution rate of 10% or less) so that it does not dissolve or deteriorate during use as an adsorbent. At the same time, the degree of swelling is controlled to be 80% or more. As a method for satisfying both the water resistance and the swelling property, for example, the following treatment conditions can be mentioned.

  The treatment conditions can be divided according to, for example, the saponification degree of PVA. When the saponification degree of PVA is 99 mol% or more, the elution rate of the PVA molded product is 10% or less due to crystallization of PVA itself. Therefore, almost no heat stretching after drying is necessary.

  Further, when the saponification degree of PVA is 97 to 99 mol%, the crystallinity degree of PVA itself is not sufficient to suppress elution, so that the raw yarn or under the predetermined temperature condition (for example, about 220 to 230 ° C.) The drawn yarn needs to be drawn and heat treated.

Furthermore, when the degree of saponification of PVA is lower than that, or even if it is 97 mol% or more, in the case of modified PVA copolymerized with monomers such as maleic acid, crosslinking is important from the viewpoint of suppressing elution. It becomes.
In this case, crosslinking may be performed with the above-described crosslinking agent, or radicals may be generated and crosslinked by irradiation with an electron beam or radiation.

Thereafter, stretching and heat treatment can be performed as necessary.
When heat treatment is performed, the heat treatment conditions are generally 100 ° C or higher, preferably 150 ° C to 240 ° C. If the temperature is too low, the effect of improving the physical properties of the fiber is insufficient. On the other hand, if the temperature is too high, partial melting of the fiber occurs, and even in this case, the mechanical properties are lowered.

  In addition, the PVA molded product does not necessarily have to be in a fiber form, and may be a molded product such as a granule or a powder. For example, a stock solution containing PVA and (if necessary, a nitrogen-containing substance and a crosslinking agent) is prepared according to the above-described method for producing a spinning stock solution, and then this stock solution is dropped into a coagulation bath containing a crosslinking catalyst. By solidifying and drying the obtained solidified product, a granular molded product can be formed. If necessary, the solidified product may be cross-linked by irradiation with an electron beam or radiation.

  From the viewpoint of increasing the surface area of the molded product, the PVA molded product preferably has a fiber shape. For example, when it has a fiber shape, it can be used in any form such as a shortcut fiber, non-woven fabric, spun yarn or filament. Further, these molded products may be further packed in a cartridge or column for use.

[Method of treating boron-containing water]
In the method for treating boron-containing water according to the present invention, the PVA molded product described above is brought into contact with boron-containing water at pH 6 to 14 to adsorb the boron compound contained in the boron-containing water by the PVA molded product. Can be made.
Since the PVA molded product of the present invention has water resistance, it is excellent not only in portability and handling properties but also in storage stability.

In the boron-containing water to be treated in the present invention, the boron compound is usually present as a boron compound such as boric acid or borate in the boron-containing water. Examples of such a boron compound or borate include molecular forms of boron such as orthoboric acid (H ₃ BO ₃ ), metaboric acid (HBO ₂ ), and tetraboric acid (H ₂ B ₄ O ₇ ). Acids: orthoborate ion (BO ₃ ³⁻ ), diborate ion ([B ₂ O ₅ ] ⁴⁻ ), metaborate ion ([B ₃ O ₆ ] ³⁻ ), tetraborate ion ([B ₄ O _7] ^2), pentaborate ion _{([B 5 H 4 O 10} ] -), Monohou acid ion (B ^(OH) present in ionic form of borate derived from boric acid salt such as ^4-) It may be. These boron compounds may be in an associated state.

  The pH condition needs to be pH 6 or more from the point of adsorption equilibrium between PVA and boric acid, and may be preferably pH 9 or more. Moreover, although an upper limit can be suitably determined according to the kind of waste_water | drain, for example, pH14 or less, Preferably pH12 or less may be sufficient.

The method for contacting the PVA molded product with the boron-containing water is not particularly limited as long as the PVA molded product can adsorb the boron compound, and various methods can be used. For example, as such a contact method, (i) after the PVA molded product is put into an adsorption tank containing boron-containing water, the PVA molded product is stirred in the adsorption tank to adsorb the boron compound to the PVA molded product. And (ii) a method in which boron-containing water is passed through an adsorption tower pre-filled with a PVA molded product, and a boron compound is adsorbed on the PVA molded product.
In addition, since the PVA molded product is formed from water-resistant PVA, it can be reused through a regeneration process after adsorption of the boron compound. In the regeneration step, for example, boron adsorbed in the PVA molding by washing the PVA molding adsorbing the boron compound with an acid solution (for example, mineral acid such as hydrochloric acid and nitric acid; organic acid such as acetic acid). The compound can be desorbed and the adsorbent can be regenerated.

  EXAMPLES Hereinafter, although an Example demonstrates this invention in detail, this invention is not limited at all by this Example. In the examples, the boric acid adsorption rate, the average degree of polymerization of PVA, the degree of swelling of the PVA molded product, and the dissolution rate are determined by the following methods.

(Boric acid adsorption rate%)
A sample of 0.5 g was immersed at 20 ° C. in 100 mL of an aqueous solution of orthoboric acid (hereinafter simply referred to as boric acid) having a concentration of 200 ppm. The sample was allowed to stand for 30 minutes without stirring, and then the concentration of the boric acid solution was measured. The concentration difference before the test was regarded as adsorbed, and the adsorption amount was divided by the sample weight to express the adsorption rate. . The pH of the boric acid solution during the adsorption test was adjusted to a predetermined pH using hydrochloric acid or an aqueous sodium hydroxide solution.

(Average polymerization degree of PVA)
The average degree of polymerization of PVA was measured according to JIS K6726.

(Swelling degree and dissolution rate of PVA molded product)
A sample of the PVA molded product dried at 105 ° C. for 4 hours was weighed, and its weight was defined as A (g). Next, this sample was immersed in 30 ° C. water at a bath ratio of 100 or more for 30 minutes, and then centrifuged and dehydrated at 3000 rpm for 5 minutes. The dehydrated sample was weighed, and its weight was defined as B (g). . Further, the dehydrated sample was dried at 105 ° C. for 4 hours, the dried sample was weighed, and its weight was defined as C (g). And swelling degree (%) and elution rate (%) were calculated | required by following formula (1) and (2), respectively.
Swelling degree = (B−A) / A × 100 (1)
Dissolution rate = (AC) / A × 100 (2)

( Reference Examples 1 and 2 )
A spinning stock solution was prepared by dissolving PVA having a saponification degree of 98.5 mol% and an average polymerization degree of 1750 in water at a concentration of 14%. This spinning solution was wet-spun through a nozzle having a diameter of 0.08 mm into a saturated sodium sulfate bath at 40 ° C. and 400 g / L, and taken up at a speed of 10 m / min. Subsequently, the film was wet-stretched 2.5 times and then dried at 130 ° C. The PVA molded product in the form of fibers thus obtained had a fineness of 1.3 dtex, a swelling degree of 145%, and an elution rate of 5%. The amount of boric acid adsorbed on the obtained PVA molded product was measured under pH 6.5 ( Reference Example 1 ) or pH 11 ( Reference Example 2 ). The results are shown in Table 1.

( Example 1 )
PVA having a saponification degree of 96 mol% and an average polymerization degree of 1750 was dissolved in water at a concentration of 16%, and polyallylamine (Nittobo PAA-15C) having an average molecular weight of 15000 was dissolved in water to a concentration of 15% by weight with respect to PVA. A stock solution for spinning was prepared by adding and mixing.

The stock solution was spun, wet-drawn and dried in the same manner as in Reference Example 1 to obtain a fiber having a fineness of 1.7 dtex. Next, this fiber was immersed in a bath of glutaraldehyde / sulfuric acid / sodium sulfate = 0.5 / 1/130 g / L at 40 ° C. for 30 minutes, dehydrated, dried at 80 ° C., and subjected to crosslinking treatment. The PVA molded product in the form of fibers thus obtained had a fineness of 1.7 dtex, a swelling degree of 95%, and an elution rate of 0.3%. The boric acid adsorption amount of the obtained PVA molded product was measured under pH 6.5. The results are shown in Table 1.

(Comparative Example 1)
The wet stretch-dried yarn of PVA obtained in Reference Example 1 was further heat-stretched 1.8 times under hot air at 230 ° C., the fineness was 0.7 dtex, the swelling degree was 57%, and the dissolution rate was 2%. A PVA molded product was obtained. The boric acid adsorption amount of the obtained PVA molded product was measured in the same manner as in Reference Example 1 . The results are shown in Table 1.

( Reference Example 3 )
PVA having a saponification degree of 99 mol% and a polymerization degree of 1000 was dissolved in water at a concentration of 15%, adjusted to pH 8 with sodium hydroxide, and then 2% by weight of glyoxal was added to PVA to prepare a stock solution.

  This undiluted solution is dropped from a nozzle with a diameter of 1 mm into a sulfuric acid bath having a concentration of 10 g / L at 40 ° C. to obtain particulate spheres, which are further washed with water and dried to form a PVA molded article having a granular form. Got. The obtained molded product was a granular material having a diameter of about 0.6 mm, the degree of swelling was 250%, and the elution rate was 0.1%. The amount of boric acid adsorbed under pH 11 of this molded product was measured. The results are shown in Table 1.

As shown in Table 1, the PVA molded product having a high degree of swelling showed excellent boric acid adsorption, and the amount of boric acid adsorbed tended to increase as the degree of swelling increased. Moreover, when the elution of PVA in water was confirmed, in all the reference examples and Example 1 , it was a level which is satisfactory practically. Therefore, it is considered that such a PVA molded product can be reused by a predetermined process.
Further, when the PVA molded product contained a nitrogen-containing substance (Example 1) , boric acid adsorption was higher than that of Reference Example 1 having a swelling degree of 145%, even though the swelling degree was 95%.
On the other hand, in the comparative example having a swelling degree of 57%, although the shape did not collapse visually, the boric acid adsorption amount was less than half that of Example 1 and did not show high boric acid adsorption.

Claims (7)

A polyvinyl alcohol molding used for removing boron compounds from boron-containing water,
The molded article is composed of at least polyvinyl alcohol and a basic nitrogen-containing substance , the polyvinyl alcohol carries the nitrogen-containing substance , and the molded article has a degree of swelling of 80% or more and an elution rate. Polyvinyl alcohol molded product that is 10% or less.   The polyvinyl alcohol molded product according to claim 1, wherein the saponification degree of polyvinyl alcohol is 88 mol% or more.   The polyvinyl alcohol molded product according to claim 1 or 2, wherein the average degree of polymerization of polyvinyl alcohol is 500 to 5,000. The polyvinyl alcohol molded product according to any one of claims 1 to 3, wherein the nitrogen-containing material is at least one selected from nitrogen-containing materials composed of an amine compound, an imine compound, and an amide compound. The polyvinyl alcohol molded product according to any one of claims 1 to 4, wherein a ratio of the nitrogen-containing substance to 100 parts by weight of polyvinyl alcohol is 5 to 50 parts by weight. The polyvinyl alcohol molded product according to any one of claims 1 to 5 , wherein the molded product has a fiber shape. A method for treating boron-containing water, wherein the polyvinyl alcohol molded product according to any one of claims 1 to 6 is brought into contact with boron-containing water at a pH of 6 or more.