JP2017131883A - Heavy metal ion absorbent - Google Patents

Abstract

PROBLEM TO BE SOLVED: To provide an absorbent containing crystalline silico-titanate effective for absorbing heavy metal ions.SOLUTION: There is provided an absorbent of heavy metal ions containing crystalline silico-titanate having crystalline particle diameter of 150 Å or more and represented by the general formula: ATiSiOnHO, where A is one or two alkali metal selected from Na and K and preferably potassium content has weight ratio to AO in terms of KO of 0<KO/AO≤50 mass% and n is 0 to 8, wherein the crystalline silico-titanate preferably has crystalline diameter of 150 to 250 Å.SELECTED DRAWING: None

Description

  The present invention relates to an adsorbent containing crystalline silicotitanate that can be suitably used for selectively and efficiently separating and recovering heavy metal ions.

Crystalline silicotitanate is one of the inorganic adsorbents studied so far for the adsorptivity of cesium and / or strontium. Crystalline silicotitanates are known to have a plurality of types of compositions such as those with a Ti / Si ratio of 1: 1, 5:12, and 2: 1. It is known that there is crystalline silicotitanate in which is 4: 3. In Non-Patent Document 1, products 3B and 3C produced by hydrothermal treatment using an alkoxide of Ti (OET) ₄ as a Ti source and colloidal silica as a Si source are three-dimensional from the X-ray diffraction pattern. It has a typical 8-membered ring structure, and the crystalline silicotitanate having this structure ideally has a composition represented by M ₄ Ti ₄ Si ₃ O ₁₆ (M is Na, K, etc.). The crystalline silicotitanate having this structure is named Grace titanium silicate (GTS-1). Non-Patent Document 2 discloses a hydrothermal treatment of a crystalline silicotitanate having a Ti / Si ratio of 4: 3, titanium tetrachloride as a Ti source, and a highly dispersed SiO ₂ powder as a Si source. The fact that it was manufactured by applying is described. This document describes that the synthesized crystalline silicotitanate has ion exchange capacity with Mg, Ca, Sr and Co.
In addition, the present applicants previously described crystalline silicotitanate having a Ti / Si ratio of 4: 3 as an adsorbent capable of adsorbing both cesium and strontium, and A ′ ₄ Ti ₉ O ₂₀ .mH ₂ O (formula Wherein A ′ represents one or two alkali metals selected from Na and K. In the formula, m represents a number of 0 or more. (See Patent Document 1 below).

Japanese Patent No. 5696244

ZEOLITES, 1990, Vol 10, November / December Keiko Fujiwara, “Modification and evaluation of microporous crystals as heat pump adsorbents”, [online], [March 3, 2014 search], Internet <URL: http://kaken.nii.ac.jp/pdf /2011/seika/C-19/15501/21560846seika.pdf>

Heavy metal ions are known to cause significant damage to ecosystems. For this reason, an adsorbent having an excellent adsorption capacity for heavy metal ions is also required.
Accordingly, an object of the present invention is to provide an adsorbent containing crystalline silicotitanate that is effective for adsorption of heavy metal ions.

The present inventor has conducted extensive studies in view of the above circumstances, and as a result, a general formula having a crystallite diameter in a specific range; A ₄ Ti ₄ Si ₃ O ₁₆ .nH ₂ O (where A is selected from Na and K) The crystalline silicotitanate represented by the formula 1 or 2 alkali metal, wherein n is 0 to 8, has been found to be particularly excellent in the ability to adsorb heavy metal ions, The present invention has been completed.

That is, the adsorbent to be provided by the present invention is an adsorbent for heavy metal ions,
A ₄ Ti ₄ Si ₃ O ₁₆ .nH ₂ O (wherein A represents one or two alkali metals selected from Na and K. In the formula, the crystallite diameter is 150 Å or more; n represents 0-8.) It contains crystalline silicotitanate.

  ADVANTAGE OF THE INVENTION According to this invention, the adsorption agent containing the crystalline silicotitanate excellent in especially the adsorption removal characteristic of heavy metal ions, such as Pb, Cu, Zn, Cd, and Hg, can be provided.

1 is an X-ray diffraction chart of an adsorbent containing crystalline silicotitanate obtained in Examples 1 and 2 and Reference Example 1. FIG. 2 is an X-ray diffraction chart of an adsorbent containing crystalline silicotitanate obtained in Comparative Example 1. FIG. FIG. 3 is an X-ray diffraction chart of the adsorbent containing crystalline silicotitanate obtained in Example 4.

Hereinafter, the present invention will be described based on preferred embodiments.
The adsorbent according to the present invention adsorbs heavy metal ions. Examples of heavy metal ions adsorbed by the adsorbent of the present invention include one or more of Pb, Cu, Zn, Cd, Hg, Co, Ni, Fe, Mn, Ag, and the like. Among these, Particularly preferred is one or two selected from Pb, Cu, Zn, Cd and Hg.

The crystalline silicotitanate contained in the adsorbent according to the present invention has a general formula: A ₄ Ti ₄ Si ₃ O ₁₆ .nH ₂ O (wherein A is one or two alkali metals selected from Na and K). In the formula, n represents 0 to 8.)

The crystallinity represented by the general formula: A ₄ Ti ₄ Si ₃ O ₁₆ .nH ₂ O (wherein A represents an alkali metal of Na and K. In the formula, n represents 0 to 8). In silicotitanate (hereinafter, sometimes simply referred to as “crystalline silicotitanate”), a more detailed composition is not clear, but when A in the formula contains Na and K, the general formula; Na ₄ Ti _{4 Si 3 O 16 · nH 2} O and _{K 4 Ti 4 Si 3 O 16} · nH or containing ₂ O, or _{(Na x K (1-x} )) 4 Ti 4 Si 3 O 16 · nH 2 O ( wherein The present inventors presume that x is more than 0 and less than 1.

  The crystalline silicotitanate contained in the adsorbent according to the present invention is subjected to X-ray diffraction analysis using Cu-Kα rays with the crystalline silicotitanate as a radiation source, and a diffraction peak of 2θ = 10 ° to 13 ° ( One feature is that the crystallite diameter determined from the Scherrer equation from the half width of the main peak (B1) is 150 angstroms or more, preferably 160 to 250 angstroms, particularly preferably 180 to 230 angstroms.

  In addition to having the above characteristics, the adsorbent according to the present invention has 2θ = 10 ° of crystalline silicotitanate when X-ray diffraction measurement is performed using Cu-Kα rays with the crystalline silicotitanate as a radiation source. The half-value width of the diffraction peak (main peak (B1)) of the lattice plane (100 plane) of 13 ° or less is 0.3 to 0.7 °, preferably 0.3 to 0.55 °. It is one feature.

In Non-Patent Document 2, titanium tetrachloride is used as a titanium source, and the crystallite diameter obtained by adding the silicic acid source and titanium tetrachloride to the mixed solution in such an amount that Ti / Si is 0.32 is 80 to 80. A crystalline silicotitanate that is 130 Å is disclosed.
The inventors of the present invention are concerned with the crystallite size determined from the diffraction peak (main peak (B1)) of 2θ = 10 ° or more and 13 ° or less of the crystalline silicotitanate contained in the adsorbent for the adsorption ability of heavy metal ions. And it discovered that it became the adsorbent which the adsorption capacity of heavy metal ion improved compared with the nonpatent literature 2 by making a crystallite diameter into a specific range larger than a nonpatent literature.

Further, in the adsorbent according to the present invention, crystalline Shirikochitaneto to be contained is in a content of potassium K ₂ O in terms of, 0 in a weight ratio to the _{A 2 O (K 2 O /} A 2 O) Ultra 50 Weight % Or less, preferably 5% by mass or more and 40% by mass or less, from the viewpoint of further improving the adsorption ability of heavy metal ions.

In the adsorbent according to the present invention, the crystalline silicotitanate may be used alone, but the general formula; A ′ ₄ Ti ₉ O ₂₀ · mH ₂ O (where A ′ is selected from Na and K 1 It represents a seed or two kinds of alkali metals, wherein m represents a number of 0 or more. In the present invention, when the crystalline silicotitanate and 9 titanate are used in combination, for example, the adsorption performance of Hg heavy metal ions can be dramatically improved.

_{Incidentally, A '4 Ti 9 O 20} · mH 2 O ( wherein, A' is. In formula indicating one or two alkali metal selected from Na and K, m represents a number of 0 or more.) In the case of 9 titanate represented by the formula (hereinafter, sometimes simply referred to as “9 titanate”), the detailed composition is not clear, but when A in the formula contains Na and K Or a general formula; Na ₄ Ti ₉ O ₂₀ · mH ₂ O and K ₄ Ti ₉ O ₂₀ · mH ₂ O, or (Na _x K _(1-x) ) ₄ Ti ₉ O ₂₀ · mH ₂ O ( In the formula, the present inventors presume that x is more than 0 and less than 1.

  In the adsorbent according to the present invention, the content of the 9 titanate is 2θ = 8 to 10 derived from 9 titanate when the adsorbent is measured using Cu—Kα ray as an X-ray source. The height ratio (A1 / B1) of the main peak (A1) at 0 ° to the main peak (B1) at 2θ = 10-13 ° of crystalline silicotitanate is in the range of 5-40%, preferably 5-30% It is particularly preferable from the viewpoint of improving the adsorption performance of heavy metal ions such as Hg.

  In the adsorbent of the present invention, the molar ratio of the 9 titanate to the crystalline silicotitanate obtained by composition analysis (the former: the latter) is preferably 1: 0.25 to 0.45, It is more preferable that it is 1: 0.30-0.40, and it is still more preferable that it is 1: 0.35-0.38.

（ｄ）得られた結晶性シリコチタネートのモル数及びチタン酸塩のモル数から上記の比を得る。 <How to find the molar ratio of crystalline silicotitanate: 9 titanate>
(A) The adsorbent is put in a suitable container (aluminum ring or the like), sandwiched between dies, and pelletized by applying a pressure of 10 MPa with a press machine to obtain a measurement sample. This sample was subjected to a fluorescent X-ray apparatus (device name: ZSX100e, tube: Rh (4 kW), atmosphere: vacuum, analysis window: Be (30 μm), measurement mode: SQX analysis (EZ scan), measurement diameter: 30 mmφ, (stock ) All elements are measured with Rigaku). The content (mass%) of SiO ₂ and TiO ₂ in the adsorbent is calculated by calculating by the SQX method which is a semi-quantitative analysis method.
(B) the obtained content of SiO ₂ and TiO ₂ (mass%) divided by the respective molecular weight, obtaining the number of moles of SiO ₂ and TiO ₂ in the adsorbent 100 g.
(C) One third of the number of moles of SiO _{2 in} the adsorbent determined above is used as the crystalline silicotitanate (Na ₄ Ti ₄ Si ₃ O ₁₆ .nH ₂ O, (Na _x K _{( 1-x)} ) ₄ Ti ₄ Si ₃ O ₁₆ .nH ₂ O and K ₄ Ti ₄ Si ₃ O ₁₆ .nH ₂ O are assumed to be the number of moles. Moreover, since the number of moles of Ti atoms in 1 mole of the crystalline silicotitanate is 4, the number of moles of the titanate in the adsorbent is determined by the following formula (1).

(D) The above ratio is obtained from the number of moles of the obtained crystalline silicotitanate and the number of moles of titanate.

  The adsorbent of the present invention was obtained by, for example, a first step of mixing a silicic acid source, a sodium compound and / or potassium compound, titanium tetrachloride, and water to obtain a mixed gel, and the first step. A second step of hydrothermally reacting the mixed gel, and in the first step, the molar ratio of Ti and Si contained in the mixed gel is Ti / Si = 0.5 to 3.0, It can be produced by adding a silicic acid source and titanium tetrachloride.

  According to the method for producing an adsorbent, an adsorbent containing only crystalline silicotitanate and an adsorbent containing both crystalline silicotitanate and 9 titanate can be produced.

Hereinafter, the manufacturing method of the adsorbent of this invention is demonstrated.
As a silicic acid source which concerns on a 1st process, sodium silicate is mentioned, for example. Moreover, the active silicic acid obtained by carrying out cation exchange of the alkali silicate (namely, alkali metal salt of silicic acid) is also mentioned.

  The activated silicic acid is obtained by cation exchange by bringing an aqueous alkali silicate solution into contact with, for example, a cation exchange resin. As a raw material for the alkali silicate aqueous solution, a sodium silicate aqueous solution usually called water glass (water glass No. 1 to No. 4 etc.) is preferably used. This is relatively inexpensive and can be easily obtained. For semiconductor applications that dislike Na ions, an aqueous potassium silicate solution is suitable as a raw material. There is also a method of preparing an alkali silicate aqueous solution by dissolving solid alkali silicate in water. Alkali metasilicates are produced through a crystallization process, so some of them have few impurities. The aqueous alkali silicate solution is diluted with water as necessary.

  The cation exchange resin used when preparing the active silicic acid can be appropriately selected from known ones and is not particularly limited. In the contacting step between the alkali silicate aqueous solution and the cation exchange resin, for example, the alkali silicate aqueous solution is diluted with water so that the silica has a concentration of 3% by mass or more and 10% by mass or less. Contact with a strong acidic or weakly acidic cation exchange resin to dealkalize. Further, if necessary, it can be deanioned by contacting with an OH type strongly basic anion exchange resin. By this step, an active silicic acid aqueous solution is prepared. Regarding the details of the contact conditions between the aqueous alkali silicate solution and the cation exchange resin, various proposals have already been made, and any known contact conditions can be adopted in the present invention.

  Examples of the sodium compound used in the first step include sodium hydroxide and sodium carbonate. Among these sodium compounds, when sodium carbonate is used, carbon dioxide gas is generated. Therefore, it is preferable to use sodium hydroxide that does not generate such gas from the viewpoint of smoothly promoting the neutralization reaction.

  Examples of the potassium compound include potassium hydroxide and potassium carbonate. Among these potassium compounds, when potassium carbonate is used, carbon dioxide gas is generated. Therefore, it is preferable to use potassium hydroxide that does not generate such gas from the viewpoint of smoothly promoting the neutralization reaction.

  When using a sodium compound and a potassium compound in the first step, the ratio of the number of moles of the potassium compound to the total number of moles of the sodium compound and the potassium compound is preferably more than 0% and 50% or less, preferably 5% or more More preferably, it is 30% or less.

  The addition amount of the silicic acid source and titanium tetrachloride is such that Ti / Si, which is the molar ratio of Ti derived from titanium tetrachloride and Si derived from the silicic acid source in the mixed gel, has a specific ratio. For example, in Non-Patent Document 3, titanium tetrachloride is used as the titanium source, but the silicate source and titanium tetrachloride are added to the mixed solution in such an amount that the Ti / Si ratio is 0.32. On the other hand, in this manufacturing method, a silicic acid source and titanium tetrachloride are added in such an amount that the Ti / Si ratio is 0.5 or more and 3.0 or less. As a result of the study by the present inventors, by setting the Ti / Si ratio in the mixed gel to the above molar ratio range, as a crystalline silicotitanate, the crystallinity is high, and the crystallite diameter and the half width are in the above range. It becomes easy to obtain. The Ti / Si ratio in the mixed gel is preferably 1.0 or more and 3.0 or less.

  When obtaining an adsorbent containing only crystalline silicotitanate, the molar ratio of Ti / Si is 1.2 or more and 1.5 or less, and an adsorbent containing crystalline silicotitanate and 9 titanate is used. When obtained, the molar ratio of Ti / Si is preferably 1.8 or more and 2.2 or less.

Further, the total amount of the SiO ₂ equivalent silicic acid source concentration and the TiO ₂ equivalent titanium tetrachloride concentration in the mixed gel is 2.0 mass% or more and 40 mass% or less, and A ₂ O / SiO _{2 in the} mixed gel. It is desirable to add the silicic acid source and titanium tetrachloride so that the molar ratio of the above becomes 0.5 to 3.0. Here, A represents Na and K. By adjusting the addition amount of the silicic acid source and titanium tetrachloride within the above range, the yield of the target crystalline silicotitanate can be increased to a satisfactory level.

The number of moles of A ₂ O is the number of ions of sodium and potassium in the mixed gel expressed in terms of oxide, in other words, used by the neutralization reaction between alkali such as sodium or potassium and titanium tetrachloride. It is obtained excluding the amount of sodium and potassium.

When obtaining an adsorbent containing only crystalline silicotitanate, a molar ratio of A ₂ O / SiO ₂ = 0.5 or more and 2.5 or less, an adsorbent containing crystalline silicotitanate and 9 titanate is used. When obtaining, it is desirable to add a silicic acid source and titanium tetrachloride so that it may become 1.0-1.8.

  The titanium tetrachloride used in the first step can be used without particular limitation as long as it is industrially available.

  In the first step, the silicic acid source, sodium compound, potassium compound, and titanium tetrachloride can be added to the reaction system in the form of an aqueous solution, respectively. In some cases, it can be added in solid form. Further, in the first step, the concentration of the mixed gel can be adjusted using pure water if necessary for the obtained mixed gel.

  In the first step, the silicic acid source, sodium compound, potassium compound, and titanium tetrachloride can be added in various addition orders. For example, (1) a mixed gel can be obtained by adding titanium tetrachloride to a mixture of a silicate source, a sodium compound and / or a potassium compound, and water (this addition order is simply referred to as “additional order” hereinafter). (It may be called “Implementation of (1)”.) The implementation of (1) is preferable in that the generation of chlorine from titanium tetrachloride is suppressed.

  As another order of addition in the first step, (2) an aqueous solution of activated silicic acid (hereinafter sometimes simply referred to as “activated silicic acid”) obtained by cation exchange of alkali silicate, titanium tetrachloride and water, A mode in which a sodium compound and / or a potassium compound is added to a mixture of these can be employed. Even if this order of addition is adopted, a mixed gel can be obtained in the same manner as in the embodiment of (1) (this order of addition may hereinafter be simply referred to as “execution of (2)”). Titanium tetrachloride can be added in the form of an aqueous solution or solid form. Similarly, sodium compounds and potassium compounds can also be added in the form of their aqueous solutions or solid forms.

In the implementation of (1) and (2), the sodium compound and / or potassium compound has a total concentration of sodium and potassium (A ₂ O concentration) in the mixed gel of 0.5% by mass or more in terms of Na ₂ O. It is preferable to add so that it may become 0 mass% or less, especially 0.7 mass% or more and 13 mass% or less. The total Na ₂ O equivalent mass of sodium and potassium in the mixed gel and the total Na ₂ O equivalent concentration of sodium and potassium in the mixed gel (hereinafter referred to as “total concentration of sodium and potassium (the potassium compound is used in the first step) If not, it is referred to as “sodium concentration”).

Total Na ₂ O equivalent mass (g) of sodium and potassium in the mixed gel = (number of moles of A above−number of moles of chloride ions derived from titanium tetrachloride) × 0.5 × Na ₂ O molecular weight

Concentration (mass%) of total sodium and potassium in mixed gel in terms of Na ₂ O = total mass of sodium and potassium in mixed gel converted to Na ₂ O / {water content in mixed gel + sodium in mixed gel And potassium total Na ₂ O equivalent mass} × 100

Suppressing the formation of crystalline silicotitanate other than crystalline silicotitanate with a molar ratio of Ti: Si of 4: 3 by combining the selection of the silicate source with the adjustment of the total concentration of sodium and potassium in the mixed gel Can do. When sodium silicate or potassium silicate is used as the silicic acid source, the molar ratio of Ti: Si is set to 2.0% by mass or more in terms of Na ₂ O in terms of the total concentration of sodium and potassium in the mixed gel. It becomes possible to effectively suppress the formation of 5:12 crystalline silicotitanate, while the total concentration of sodium and potassium in the mixed gel is 6.0% by mass or less in terms of Na ₂ O, The molar ratio of Ti: Si is 1:
The production of 1 crystalline silicotitanate can be effectively suppressed. Also, when using the active silicic acid obtained by the alkali silicate to cation exchange as silicic acid source, by setting more than 1.0 mass% in terms of Na ₂ O, Ti: molar ratio of Si 5: It is possible to effectively suppress the formation of 12 crystalline silicotitanate, while the total concentration of sodium and potassium in the mixed gel is 6.0% by mass or less in terms of Na ₂ O, so that Ti: Production of crystalline silicotitanate having a Si molar ratio of 1: 1 can be effectively suppressed.

When sodium silicate is used as the silicate source, the sodium component in the sodium silicate simultaneously becomes the sodium source in the mixed gel. Therefore, the “Na ₂ O equivalent mass (g) of sodium in the mixed gel” mentioned here is counted as the sum of all sodium components in the mixed gel. Similarly, “Na ₂ O equivalent mass (g) of potassium in the mixed gel” is also counted as the sum of all potassium components in the mixed gel.

  In the implementation of (1) and (2), it is desirable to add titanium tetrachloride stepwise or continuously as an aqueous titanium tetrachloride solution over a certain period of time in order to obtain a uniform gel. For this reason, a peristaltic pump etc. can be used suitably for addition of titanium tetrachloride.

  The mixed gel obtained in the first step may be aged at 10 ° C. or higher and 100 ° C. or lower for a time period of 0.1 hour or longer and 5 hours or shorter before performing a hydrothermal reaction which is the second step described later. From the viewpoint of obtaining a uniform product. The aging step may be performed, for example, in a stationary state, or may be performed in a stirring state using a line mixer or the like.

  In the present invention, the mixed gel obtained in the first step is subjected to a hydrothermal reaction as the second step to obtain crystalline silicotitanate. The hydrothermal reaction is not particularly limited as long as the crystalline silicotitanate can be synthesized. Usually, in an autoclave, the temperature is preferably 120 ° C. or higher and 200 ° C. or lower, more preferably 140 ° C. or higher and 180 ° C. or lower, preferably 6 hours or longer and 120 hours or shorter, more preferably 12 hours or longer and 100 hours or shorter. React under pressure. The reaction time can be selected according to the scale of the synthesizer.

  The water-containing product containing the crystalline silicotitanate obtained in the second step can be dried, and the obtained dried product can be pulverized or pulverized as necessary to form a powder (including granules). Alternatively, a hydrous material containing crystalline silicotitanate may be extruded from an aperture member in which a plurality of apertures are formed to obtain a rod-shaped molded body, and the obtained rod-shaped molded body may be dried to form a columnar shape. The dried rod-shaped molded body may be formed into a spherical shape, or may be pulverized or pulverized into particles.

  Examples of the shape of the hole formed in the opening member include a circle, a triangle, a polygon, and a ring shape. The true circle equivalent diameter of the opening is preferably 0.1 mm or more and 10 mm or less, and more preferably 0.3 mm or more and 5 mm or less. The true circle equivalent diameter here is a diameter of a circle calculated from the area when the area of one hole is a circle area. The drying temperature after extrusion molding can be, for example, 50 ° C. or more and 200 ° C. or less. The drying time can be 1 hour or more and 120 hours or less.

  The dried rod-shaped molded body can be used as an adsorbent as it is, or can be used after lightly loosening. Moreover, you may grind | pulverize and use the rod-shaped molded object after drying. It is preferable from the viewpoint of increasing the adsorption efficiency of heavy metal ions that the powdery material containing crystalline silicotitanate obtained by these various methods is further classified and then used as an adsorbent. For the classification, for example, it is preferable to use a first sieve having a nominal opening prescribed in JISZ8801-1 of 1000 μm or less, particularly 710 μm or less.

According to the above production method, an industrial advantage that adsorbents containing not only crystalline silicotitanate but also crystalline silicotitanate and 9 titanate can be produced all at once by selecting reaction conditions as appropriate. Have.
In addition, in the case of the adsorbent containing crystalline silicotitanate and 9 titanate according to the present invention, a single-phase crystalline silicotitanate is produced by X-ray diffraction by the above-described method, and is separately commercially available or publicly known. Needless to say, the 9 titanate produced by the production method may be mixed later.

  The adsorbent characterized in that it contains the crystalline silicotitanate according to the present invention may be molded according to a conventional method as necessary, and the resulting molded product may be used as an adsorbent for heavy metal ions.

  As the molding process, for example, a powdery adsorbent containing crystalline silicotitanate is granulated and a powdery adsorbent containing crystalline silicotitanate is slurried to form calcium chloride. A method of encapsulating a powdery adsorbent containing crystalline silicotitanate by dropping it into a liquid containing a curing agent such as, and attaching a powdery adsorbent containing crystalline silicotitanate to the surface of a resin core material A method of coating treatment, a method of adhering a powdery adsorbent containing crystalline silicotitanate to the surface and / or inside of a sheet-like base material formed of natural fibers or synthetic fibers, and fixing it to a sheet shape, etc. Can be mentioned. Examples of the granulation method include known methods such as stirring and mixing granulation, rolling granulation, extrusion granulation, crushing granulation, fluidized bed granulation, spray drying granulation (spray drying), and compression granulation. A grain etc. can be mentioned. In the granulation process, a binder and a solvent may be added and mixed as necessary. As the binder, known ones such as polyvinyl alcohol, polyethylene oxide, hydroxyethylcellulose, hydroxypropylcellulose, hydroxypropylmethylcellulose, hydroxyethylmethylcellulose, carboxymethylcellulose, hydroxypropylmethylcellulose, methylcellulose, ethylcellulose, starch, cornstarch, molasses, lactose, gelatin , Dextrin, gum arabic, alginic acid, polyacrylic acid, glycerin, polyethylene glycol, polyvinylpyrrolidone and the like. As the solvent, various solvents such as an aqueous solvent and an organic solvent can be used.

    In addition, a granular product obtained by granulating a water-containing material containing crystalline silicotitanate is preferably used as an adsorbent in a water treatment system having an adsorption vessel and an adsorption tower filled with an adsorbent. I can do it.

  In this case, the shape and size of the granular material obtained by granulating the water-containing material containing crystalline silicotitanate is filled in an adsorption vessel or a packed tower, and the treated water containing heavy metal ions is passed through. It is preferable to appropriately adjust the shape and size so as to adapt to watering.

  In addition, a granular product obtained by granulating water-containing material containing crystalline silicotitanate is used as an adsorbent that can be recovered by magnetic separation from water containing heavy metal ions by further containing magnetic particles. I can do it. Examples of magnetic particles include metals such as iron, nickel, and cobalt, or powders of magnetic alloys based on these metals, metal oxides such as iron trioxide, iron sesquioxide, cobalt-added iron oxide, barium ferrite, and strontium ferrite. Examples thereof include powders of magnetic system.

  As a method of adding magnetic particles to a granulated product obtained by granulating a water-containing material containing crystalline silicotitanate, for example, the above-described granulation processing operation may be performed in a state where magnetic particles are contained. .

  The adsorbent according to the present invention can also be used as a heavy metal ion adsorbent for tap water in combination with activated carbon.

  EXAMPLES Hereinafter, although an Example demonstrates this invention in detail, this invention is not limited to these Examples.

  EXAMPLES The present invention will be specifically described below with reference to examples and comparative examples, but the present invention is not limited to these examples. Unless otherwise specified, “%” represents “mass%”. Evaluation devices and materials used in Examples and Comparative Examples are as follows.

<Evaluation equipment>
X-ray diffraction: Bruker D8 AdvanceS was used. Cu-Kα was used as the radiation source. The measurement conditions were a tube voltage of 40 kV, a tube current of 40 mA, and a scanning speed of 0.1 ° / sec.
ICP-AES: Varian 720-ES was used.

<Materials used>
Potassium silicate: manufactured by Nippon Chemical Industry Co., Ltd. (SiO ₂ : 26.5%, K ₂ O: 13.5%, H ₂ O: 60.00%, SiO ₂ / K ₂ O = 3.09).
Sodium silicate: manufactured by Nippon Chemical Industry Co., Ltd. (SiO ₂ : 28.96%, Na ₂ O: 9.37%, H ₂ O: 61.67%, SiO ₂ / Na ₂ O = 3.1).
Silica sol: manufactured by Nippon Chemical Industry Co., Ltd. (SiO ₂ : 30%, particle size 15 angstrom)
・ Caustic potash: solid reagent potassium hydroxide (KOH: 85%)
・ Caustic soda aqueous solution; industrial 25% sodium hydroxide (NaOH: 25%, H ₂ O: 75%)
-Titanium tetrachloride aqueous solution: 36.48% aqueous solution manufactured by Osaka Titanium Technologies Co., Ltd.-Titanium dioxide: Ishihara Sangyo ST-01

[Examples 1 and 2 and Reference Example 1]
<Synthesis of crystalline silicotitanate>
(1) First Step Using sodium silicate, 25% caustic soda, 85% caustic potash and pure water, they were mixed in the amounts shown in Table 1 and stirred to obtain a mixed aqueous solution. To this mixed aqueous solution, the amount of titanium tetrachloride aqueous solution shown in Table 1 was continuously added with a peristaltic pump over 0.5 hours to produce a mixed gel. The mixed gel was aged by standing at room temperature (25 ° C.) for 1 hour after the addition of the aqueous titanium tetrachloride solution.

(2) Second Step The mixed gel obtained in the first step was put in an autoclave and heated to the temperature shown in Table 1 over 1 hour, and then the reaction was carried out with stirring while maintaining this temperature. The slurry after the reaction was filtered, washed and dried to obtain massive crystalline silicotitanate.

The composition judged from the X-ray diffraction structure of the obtained crystalline silicotitanate is shown in Table 2 below. Further, elemental analysis of the crystalline silicotitanate was performed by ICP, and the amounts of Na and K were expressed in terms of Na ₂ O and K ₂ O, respectively, and the results are also shown in Table 2. Moreover, the X-ray-diffraction chart of the crystalline silicotitanate obtained in Examples 1-2 and Reference Example 1 is shown in FIG.
Moreover, about the crystalline silicotitanate sample obtained in Examples 1-2 and Reference Example 1, the full width at half maximum and the crystallite diameter were determined as follows, and the results are shown in Table 3.
The half-value width was obtained by performing X-ray diffraction measurement using Cu-Kα ray as a radiation source and obtaining a value on the lattice plane (100 plane) of the main peak (B1) of 2θ = 10 ° to 13 °.
The crystallite diameter was determined from Scherrer's equation based on the value obtained by calculating the half width of the diffraction peak.

[Comparative Example 1]
After adding NaOH aqueous solution to silica sol with the addition amount shown in Table 1 and stirring, titanium tetrachloride aqueous solution was added, and it stirred at 25 degreeC for 40 minutes, and prepared the mixed gel. Next, the obtained mixed gel was put into an autoclave and heated to the temperature shown in Table 1 over 1 hour, and then the reaction was carried out at 170 ° C. for 48 hours with stirring while maintaining this temperature. The slurry after the reaction was filtered, washed and dried to obtain massive crystalline silicotitanate. An X-ray diffraction chart of the obtained crystalline silicotitanate is shown in FIG. In addition, the composition determined from the X-ray diffraction structure is shown in Table 2 below. Further, the full width at half maximum and the crystallite diameter were measured in the same manner as in Examples 1 and 2, and the results are shown in Table 3.

注）表中の「−」は未測定を示す。

Note) "-" in the table indicates unmeasured.

{Example 3}
(1) First Step 90 g of sodium silicate No. 3, caustic soda aqueous solution 667, 49 g and 84.38 g of pure water were mixed and stirred to obtain a mixed aqueous solution. To this mixed aqueous solution, 443.90 g of titanium tetrachloride aqueous solution was continuously added over 1 hour and 20 minutes with a peristaltic pump to produce a mixed gel. The mixed gel was aged at room temperature for 1 hour after the addition of the aqueous titanium tetrachloride solution. At this time, the molar ratio of Ti and Si in the mixed gel was Ti: Si = 2: 1. Further, the concentration of SiO _{2 in} the mixed gel was 2%, the concentration of TiO ₂ was 5.3%, and the sodium concentration in terms of Na ₂ O was 3.22%.
(2) Second Step The mixed gel obtained in the first step was placed in an autoclave, heated to 170 ° C. over 1 hour, and then reacted for 24 hours with stirring while maintaining this temperature. The slurry after the reaction was filtered, washed and dried to obtain an adsorbent. The composition judged from the X-ray diffraction structure of the obtained adsorbent is shown in Table 4 below. An X-ray diffraction chart of the obtained adsorbent is shown in FIG.
In the X-ray diffraction chart, the main peak (B1) of crystalline silicotitanate (derived from Na ₄ Ti ₄ Si ₃ O ₁₆ .6H ₂ O) is detected in the range of 2θ = 10 to 13 °, and 2θ = Main peak (A1) of sodium titanate which is 9 titanate at 8 to 10 ° (derived from Na ₄ Ti ₉ O ₂₀ · 5 to 7H ₂ O) was detected.
The ratio of the height of the main peak of sodium titanate to the height of the main peak of crystalline silicotitanate was determined. Moreover, the molar ratio of crystalline silicotitanate and sodium titanate was determined by the method described above. Moreover, Na amount, K amount, a half value width, and a crystallite diameter were calculated | required similarly to Examples 1-2.

<Adsorption test of heavy metal ions>
The obtained massive adsorbent was pulverized and classified with a 100 μm sieve to obtain powder under the sieve. Take 0.1 g of this granular adsorbent in a 100 ml container, add 100 ml of a test solution in which heavy metal ions are dissolved, stir at room temperature (25 ° C.) for 1 hour, filter through 5C filter paper, The heavy metal ion concentration was quantified with an ICP emission spectrometer. The results are shown in Table 6 below. The test solutions in which heavy metal ions were dissolved were those shown in Table 5 below.

Claims (7)

An adsorbent for heavy metal ions,
A ₄ Ti ₄ Si ₃ O ₁₆ .nH ₂ O (wherein A represents one or two alkali metals selected from Na and K. In the formula, the crystallite diameter is 150 Å or more; n represents 0 to 8.) An adsorbent characterized by containing a crystalline silicotitanate represented by:   The adsorbent according to claim 1, wherein the crystalline silicotitanate has a crystallite diameter of 150 to 250 angstroms.   The adsorbent according to claim 1, wherein the crystalline silicotitanate has a half-value width of a diffraction peak on a lattice plane (100 plane) of 0.3 to 0.7 °. Crystalline Shirikochitaneto is a potassium content of K ₂ O in terms, A ₂ weight ratio _{O (K 2 O / A 2} O) at 0 claims 1 to 3, characterized in that ultra-50 wt% or less Adsorbent as described in any one of these. Furthermore, A ′ ₄ Ti ₉ O ₂₀ · mH ₂ O (wherein A ′ represents one or two alkali metals selected from Na and K. In the formula, m represents a number of 0 or more. The adsorbent according to claim 1, comprising 9 titanate represented by:   When the adsorbent was measured using Cu—Kα ray as an X-ray source, the main peak (A1) of 2θ = 8 to 10 ° derived from 9 titanate and 2θ = 10 to 10 of crystalline silicotitanate The adsorbent according to claim 5, wherein the height ratio (A1 / B1) of the 13 ° main peak (B1) is 5 to 40%. The adsorbent according to any one of claims 1 to 6, wherein the heavy metal ions to be adsorbed are one or more selected from Pb, Cu, Zn, Cd and Hg.

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