JPS6133622B2 - - Google Patents
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- JPS6133622B2 JPS6133622B2 JP58025292A JP2529283A JPS6133622B2 JP S6133622 B2 JPS6133622 B2 JP S6133622B2 JP 58025292 A JP58025292 A JP 58025292A JP 2529283 A JP2529283 A JP 2529283A JP S6133622 B2 JPS6133622 B2 JP S6133622B2
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- ion exchange
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Description
本発明は、無機質で層状の結晶構造を有しカチ
オン中からLi+を選択的に捕捉する性質を備えた
Li+選択性イオン交換体に関するものである。
A2TioO2o+1(Aはアルカリ金属、nは3また
は4)で表わされる層状の結晶構造を有するチタ
ン酸アルカリ(以下「A型化合物」と略称する)
においては、層間のアルカリ金属イオン(A+)と
ホストの(TioO2o+1)2-層の酸素との結合が比較
的弱いために、A+には陽イオン交換能が認めら
れる。そして、本発明者は特にA型化合物を酸で
処理して、H2Ti3O7の組成を持つ化合物(以下
「NaH型化合物」と略称する)およびH2Ti4O9・
H2Oの組成を持つ化合物(以下「KH型化合物」
と略称する)に変えると、各種の陽イオン(無機
および有機陽イオン)を高い効率で
(TioO2o+1)2-が作る層間に取り込むことができる
という事実を見出している。つまり、これらの化
合物はイオン交換体としての機能を発揮し得ると
いうことが判明した。
本発明はかかる技術的背景を基に更に研究を推
し進め、特に陽イオン中からLi+を選択的に取り
込む性質を具備したイオン交換体を提供すること
に成功したものである。
すなわち、本発明はLi+選択性イオン交換体と
して、層状の結晶構造を有するNa2Ti3O7を酸処
理して得られるNaH型化合物を提供するものであ
る。
前記A型化合物、つまりA2TioO2o+1で表わさ
れる化合物におけるAには、一般にナトリウム
(Na)、カリウム(K)等の各種アルカリ金属が
含まれる。しかし、高い効率でイオン交換能を営
むものは、n=3の三チタン酸ナトリウムと、n
=4の四チタン酸カリウムを出発原料とするもの
に限られる。これは、この種のA型化合物が安定
な層状の結晶構造をなすからである。これらのA
型化合物は勿論そのままでも陽イオン交換体とし
て利用することができるが、一旦酸処理した化合
物、つまりNaH型およびKH型化合物として陽イ
オン交換体に用いるのは、A型化合物に直接地の
陽イオンを反応させたのでは(TioO2o+1)2-が作
る層間に前記イオンをうまく取り込むことができ
にくいという経験に基づくものである。そして、
三チタン酸ナトリウム又は四チタン酸カリウムを
酸処理して脱アルカリすると高い陽イオン交換能
を持つチタン酸アルカリ系イオン交換体が得られ
る理由は、H+と他の陽イオンの間に塩基性度の
差が生じる為に、これが反応の推進力となる為で
あると考えられる。なお、本発明者による研究
で、Na2Ti3O7を酸処理して得られる化合物が
H2Ti3O7の組成をもつことが明らかとされてい
る。
このように、層状の結晶構造を有するA型化合
物を酸処理し、その層間アルカリを脱アルカリし
て得られるNaH型化合物又はKH型化合物では、
その層間のプロトンと各種の陽イオンが容易にイ
オン交換し、高い効率のイオン交換体として利用
することができる。NaH型化合物の場合には、後
の実施例に示すように、アルカリ金属イオンとの
イオン交換反応において、反応速度が大きく異な
り、イオン半径の小さいイオン程速く層間に取込
まれ、Li+>Na+>K+の順に遅くなる。そのた
め、混合アルカリ水溶液からLi+を最も速く取り
込みLi+に対する選択性が発現する。他方、KH型
化合物においては、反応速度に大きな差は認めら
れず、そのため、無機イオンからイオン半径の最
も小さいLi+を選択的に吸着することを目的とす
る場合、KH型化合物では十分な選択性が得られ
ず、NaH型化合物即ちH2Ti3O7の組成を有する化
合物のみがLi+の選択性を有効に発現するものと
なる。
本発明はこのような知見を基にして、Li+選択
性を有するイオン交換体として、前記した
H2Ti3O7化合物を新たに提供し得たものである。
そして、本発明によると、各種の無機イオンや有
機イオンに混在するLi+を選択して回収すること
が可能となるから、貴重なLi資源の有効利用に資
するものとなる。
すなわち、Liの地殻中での存在度は僅か
20ppmの微量であるに対し、その用途は核融合
炉材料やリチウム電池材料などとして広汎であ
り、しかも今後益々その需要が増大すると予想さ
れる状況下において、その有効な回収手段が実用
化されることに伴なうメリツトは非常に大きいも
のと考えられる。
以下、本発明の実施例と比較例とを挙げて説明
する。
実施例
特級試薬の二酸化チタン(TiO2)と炭酸ナトリ
ウム(Na2CO3)を2.9:1のモル比で混合し、こ
れを磁製のるつぼに入れ電気炉により800℃の温
度下で20時間焼成した。これをよく粉砕・混合し
た後、再度800℃の温度下で20時間焼成し、白色
粉末状の三チタン酸ナトリウム(前記A形化合物
の1つでNa型化合物とよぶ)を得た。次に、こ
のNa型化合物1gを0.1規定、0.5規定および1.0
規定の塩酸200mlに浸し、60℃の温度下で3日間
反応させた。この際、反応水溶液は撹拌器にて3
時間撹拌し、その後静置し、上澄み液を除いた
後、新しい塩酸水溶液を加えるという操作を5回
繰り返し、反応の進行を完全なものにするように
した。結果、反応生成物はすべて同じ化合物
(NaH型化合物)であつた。
以下にNaH型化合物について述べる。NaH型化
合物はH2Ti3O7の組成を持つことが以下の実験結
果により確認された。NaH型化合物中にはアルカ
リ金属がほとんど含まれていないことが、その水
溶液の原子吸光分析により確認された。また、
Na型化合物は単斜晶系の化合物であり、NaH型
化合物については、発明者らが同じく単斜晶系で
指数付けした。それらの格子定数は、
Na型化合物a=8.571Å、b=3.804Å、
c=9.135Å、β=101.57゜
NaH型化合物a=8.080Å、b=3.752Å、
c=9.178Å、β=101.27゜
であり、酸処理により層間距離に対応するaの値
が小さくなり、b、c、βの値は大きく変化しな
かつた。このことはNaH型化合物の層間Na+が酸
処理により小さいH+に置き換わつたことおよび
その際ホストの(Ti3O7)2-層の構造は保たれてい
ることを示している。さらにNaH型化合物につい
て室温から800℃までの範囲で示差熱分析を行な
つたところ、250℃までは変化がなく、250〜360
℃に重量減少を伴う吸熱ピークがが認められた。
この重量減少よりNaH型化合物のH2O量を求め
た。また、さらにNaH型化合物の赤外吸収スペク
トルを測定すると3050〜3300cm-1にH−Oの伸縮
振動が認められH−Oの結合を示したが、1600cm
-1付近にあるH−O−Hの変角振動は認められ
ず、NaH型化合物は層間水を持たず、取り込まれ
たH+は層間で構造水となつていることがわかり
その組成はH2Ti3O7であることがわかつた。
また、このNaH型化合物の陽イオン交換特性を
調べた。
まず、NaH型化合物化合物0.5gに0.1MのACl
およびAOH(AはLi、NaまたはK)水溶液40ml
を第1表に示す組成せによつて加え、60℃の温度
下において3日間イオン交換反応を行なわせた。
The present invention is an inorganic material that has a layered crystal structure and has the property of selectively capturing Li + from cations.
It concerns Li + selective ion exchangers. Alkali titanate having a layered crystal structure represented by A 2 Ti o O 2o+1 (A is an alkali metal, n is 3 or 4) (hereinafter abbreviated as "A-type compound")
In , the bond between the alkali metal ion (A + ) between the layers and the oxygen in the (Ti o O 2o+1 ) 2- layer of the host is relatively weak, so A + has a cation exchange ability. The present inventors particularly treated the A-type compound with an acid to form a compound having the composition of H 2 Ti 3 O 7 (hereinafter abbreviated as "NaH-type compound") and H 2 Ti 4 O 9 .
Compounds with the composition H 2 O (hereinafter referred to as "KH type compounds")
It has been discovered that various cations (inorganic and organic cations) can be incorporated between the layers formed by (Ti o O 2o+1 ) 2- with high efficiency. In other words, it has been found that these compounds can function as ion exchangers. The present invention has further advanced research based on this technical background, and has succeeded in providing an ion exchanger having the property of selectively taking in Li + from cations in particular. That is, the present invention provides a NaH type compound obtained by acid treatment of Na 2 Ti 3 O 7 having a layered crystal structure as a Li + selective ion exchanger. A in the type A compound, ie, the compound represented by A 2 Ti o O 2o+1 , generally includes various alkali metals such as sodium (Na) and potassium (K). However, sodium trititanate with n=3 and n
It is limited to those using potassium tetratitanate of =4 as a starting material. This is because this type of A-type compound has a stable layered crystal structure. These A
Of course, type compounds can be used as cation exchangers as they are, but compounds that have been treated with an acid, that is, NaH type and KH type compounds, are used as cation exchangers when directly adding cations to the A type compounds. This is based on the experience that it is difficult to properly incorporate the ions between the layers formed by (Ti o O 2o+1 ) 2- when reacted with (Ti o O 2o+1 ) 2-. and,
The reason why an alkaline titanate ion exchanger with a high cation exchange capacity is obtained when sodium trititanate or potassium tetratitanate is treated with acid to dealkalize it is due to the basicity between H + and other cations. This is thought to be due to the fact that a difference occurs, which becomes the driving force for the reaction. In addition, in research by the present inventor, a compound obtained by acid treatment of Na 2 Ti 3 O 7 was found to be
It is clear that it has a composition of H 2 Ti 3 O 7 . In this way, NaH type compounds or KH type compounds obtained by acid-treating an A type compound having a layered crystal structure and dealkalizing the interlayer alkali,
Protons between the layers and various cations can be easily ion-exchanged, and it can be used as a highly efficient ion exchanger. In the case of NaH-type compounds, as shown in the examples below, the reaction rate differs greatly in the ion exchange reaction with alkali metal ions, and the ions with smaller ionic radius are incorporated into the layer faster, resulting in Li + >Na It becomes slower in the order of + > K + . Therefore, Li + is taken up from the mixed alkaline aqueous solution the fastest, and selectivity for Li + is expressed. On the other hand, with KH-type compounds, there is no significant difference in reaction rate, and therefore, when the purpose is to selectively adsorb Li + with the smallest ionic radius from inorganic ions, KH-type compounds are a sufficient selection. Therefore, only NaH type compounds, that is, compounds having a composition of H 2 Ti 3 O 7 effectively exhibit Li + selectivity. Based on this knowledge, the present invention uses the above-mentioned ion exchanger as an ion exchanger having Li + selectivity.
This allows us to provide a new H 2 Ti 3 O 7 compound.
According to the present invention, it is possible to selectively recover Li + mixed in various inorganic ions and organic ions, which contributes to the effective use of valuable Li resources. In other words, the abundance of Li in the earth's crust is small.
Although the amount is only 20ppm, its uses are wide-ranging, such as as materials for nuclear fusion reactors and lithium batteries, and as the demand for it is expected to increase in the future, an effective means of recovering it will be put into practical use. The benefits associated with this are considered to be very large. Examples of the present invention and comparative examples will be described below. Example Titanium dioxide (TiO 2 ) and sodium carbonate (Na 2 CO 3 ), which are special grade reagents, were mixed at a molar ratio of 2.9:1, and the mixture was placed in a porcelain crucible and heated at 800°C in an electric furnace for 20 hours. Fired. After thoroughly pulverizing and mixing this, it was calcined again at a temperature of 800° C. for 20 hours to obtain a white powder of sodium trititanate (one of the A-type compounds mentioned above, referred to as an Na-type compound). Next, 1 g of this Na-type compound was added to 0.1N, 0.5N and 1.0N.
It was immersed in 200 ml of specified hydrochloric acid and allowed to react at a temperature of 60°C for 3 days. At this time, the reaction aqueous solution was stirred with a stirrer for 3
The procedure of stirring for a certain period of time, then allowing it to stand, removing the supernatant liquid, and adding fresh aqueous hydrochloric acid solution was repeated five times to complete the progress of the reaction. As a result, all reaction products were the same compound (NaH type compound). NaH type compounds will be described below. The following experimental results confirmed that the NaH type compound has a composition of H 2 Ti 3 O 7 . It was confirmed by atomic absorption spectrometry of the aqueous solution that NaH-type compounds contain almost no alkali metals. Also,
The Na-type compound is a monoclinic compound, and the inventors also indexed the NaH-type compound based on the monoclinic system. Their lattice constants are: Na type compound a = 8.571 Å, b = 3.804 Å, c = 9.135 Å, β = 101.57° NaH type compound a = 8.080 Å, b = 3.752 Å, c = 9.178 Å, β = 101.27° The value of a, which corresponds to the interlayer distance, decreased due to the acid treatment, but the values of b, c, and β did not change significantly. This indicates that the interlayer Na + of the NaH type compound was replaced by small H + by the acid treatment, and that the structure of the host (Ti 3 O 7 ) 2- layer was maintained. Furthermore, when differential thermal analysis was performed on NaH-type compounds in the range from room temperature to 800℃, there was no change up to 250℃, and between 250 and 360℃.
An endothermic peak accompanied by weight loss was observed at °C.
From this weight loss, the amount of H 2 O in the NaH type compound was determined. Furthermore, when the infrared absorption spectrum of the NaH type compound was measured, stretching vibrations of H-O were observed at 3050 to 3300 cm -1 , indicating a H-O bond, but at 1600 cm
Bending vibration of H-O-H near -1 was not observed, indicating that NaH-type compounds do not have interlayer water, and the incorporated H + becomes structural water between the layers. Its composition is H It turned out to be 2 Ti 3 O 7 . We also investigated the cation exchange properties of this NaH type compound. First, add 0.1M ACl to 0.5g of NaH type compound.
and AOH (A is Li, Na or K) aqueous solution 40ml
were added according to the composition shown in Table 1, and an ion exchange reaction was carried out at a temperature of 60° C. for 3 days.
【表】
反応生成物はX線回折法、原子吸光法、比色分
析法、示差熱分析法等を用いて分析を行なつた。
それらの結果に基いて計算した各反応生成物の化
学式を第2表に示す。[Table] The reaction products were analyzed using X-ray diffraction, atomic absorption spectrometry, colorimetry, differential thermal analysis, etc.
Table 2 shows the chemical formulas of each reaction product calculated based on these results.
【表】
このように、NaH型化合物化合物は塩化物水溶
液に浸漬中ほとんどイオン交換反応を起こさない
ことがわかつた。他方、水酸化物水溶液に浸漬す
るとA+の種類によつて異なるが、NaH型化合物
の層間H+のうち15〜63%がA+にイオン交換され
ることがわかつた。
このように、塩化物水溶液中と水酸化物水溶液
中でイオン交換率に大きな差があることから、次
にこの反応のPH依存性を調べた。0.1MのNaClと
NaOH水溶液を混合して、PHが8.0、9.0、10.0、
11.0、12.0および12.5の水溶液を調整し、これら
の水溶液40mlに、それぞれNaH型化合物0.5gを
加え、60℃の温度下において3日間イオン交換反
応を行なわせた。結果を第1図に示す。このよう
に、イオン交換率はPHが11〜12付近に急激な立ち
上がりを持つ曲線で表わされ、PHの高い領域でイ
オン交換率が高くなることを示した。
次に、高い交換率を示す水酸化物水溶液中での
NaH型化合物のイオン交換反応の経時変化を調べ
た。NaH型化合物0.5gに0.1MのAOH(AはLi、
NaおよびK)水溶液40mlを加え60℃の温度下に
おいて、1時間、3時間、6時間、1日間、2日
間および3日間それぞれイオン交換反応を行なわ
せた。結果を第2図に示す。イオン交換率は、
0.1MのLiOH水溶液中では1時間で約45%とな
り、その後時間とともに増加し2日間で約63%と
なり、その後ほぼ一定となる。0.1MのNaOH水溶
液中では、1時間で約18%となり、その後時間と
ともに増加し、3日間で約44%に達する。0.1M
のKOH水溶液中では1時間で約5%で、その後
3日間で約11%まで増加する。このようにLi+と
の反応が最も速いので、混合アルカリ水溶液中か
らLi+を最も速く取り込み、それに起因するLi+選
択性が発現するのではないかと考えて以下の実験
を行なつた。
Li+、Na+およびK+に対するイオン交換反応の
イオン選択性について調べた。0.1MのLiOH、
NaOHおよびKOH水溶液をそれぞれ40mlずつ混
合した水溶液にNaH型化合物0.5gを加えて、60
℃の温度下において3日間イオン交換反応を行な
わせた。結果、反応生成物中のLi:Na:Kのモ
ル比は1.00:0.26:0.01となり最もイオン半径の
小さいLi+が最も多く取り込まれるることがわか
つた。すなわち、Li+の交換量が2番目に多い
Na+の4倍と非常に高いLi+選択性を示してい
る。
比較例
特級試薬の二酸化チタンと炭酸カリウム
(K2CO3)を3.5:1のモル比で混合し、実施例と
同じ条件で焼成し、白色粉末状の四チタン酸カリ
ウム(前記A型化合物の1つでK型化合物と呼
ぶ)を得た。次に、このK型化合物1gを実施例
と同じ条件で酸処理した。結果、反応生成物はす
べて同じ化合物(KH型化合物)であつた。
以下にKH型化合物について述べる。KH型化
合物はH2Ti4O9・H2Oの組成を持つことが以下の
実験結果により確認された。KH型化合物中には
アルカリ金属イオンが含まれていないことが、そ
の水溶液の原子吸光分析により確認された。ま
た、K型化合物は単斜晶系の化合物であり、KH
型化合物については、発明者らが同じく単斜晶系
で指数付けした。それらの格子定数は、
K型化合物a=18.25Å、b=3.791Å、
c=12.01Å、β=106.4゜
KH型化合物a=18.77Å、b=3.750Å、
c=11.62Å、β=104.6゜
であり、酸処理により層間距離に対応するaの値
が大きくなり、他のb、c、βは大きく変化しな
かつた。このことは、K型化合物の層間K+(半
径1.33Å)が少し大きいヒドロニウムイオン
H3O+(1.40Å)に置き換わつたこととその際ホ
ストの(Ti4O9)2-層の構造は保たれたままであつ
たことを示している。さらに、KH型化合物につ
いて室温から800℃までの範囲で示差熱分析を行
なつたところ、40〜90℃および90〜250℃に重量
減少を伴なう吸熱ピークが認められた。この重量
減少よりKH型化合物のH2O量を求めた。またさ
らに、KH型化合物の赤外吸収ベクトルを測定す
ると、3050〜3300cm-1のH−Oの伸縮振動および
1600cm-1付近のH−O−Hの変角振動に認めら
れ、H2Oの存在を示した。以上のことよりKH型
化合物に取り込まれたH3O+は層間で自由水(層
間水)となつていることがわかり、その組成は
H2Ti4O9・H2Oであることがわかつた。
また、このKH型化合物の陽イオン交換特性を
調べた。
まず、KH型化合物0.5gに0.1MのACLおよび
AOH(AはLi、NaまたはK)水溶液40mlを第3
表に示す組合せによつて加え、60度の温度下にお
いて3日間イオン交換反応を行なわせた。[Table] Thus, it was found that the NaH type compound hardly undergoes an ion exchange reaction while immersed in an aqueous chloride solution. On the other hand, it was found that when immersed in an aqueous hydroxide solution, 15 to 63% of the interlayer H + of the NaH type compound was ion-exchanged to A + , although this differed depending on the type of A + . Since there is a large difference in the ion exchange rate between chloride and hydroxide aqueous solutions, we next investigated the PH dependence of this reaction. 0.1M NaCl
Mix NaOH aqueous solution, pH is 8.0, 9.0, 10.0,
Aqueous solutions of 11.0, 12.0 and 12.5 were prepared, and 0.5 g of the NaH type compound was added to 40 ml of each of these aqueous solutions, and an ion exchange reaction was carried out at a temperature of 60° C. for 3 days. The results are shown in Figure 1. Thus, the ion exchange rate was expressed by a curve with a sharp rise around pH 11 to 12, indicating that the ion exchange rate was high in the high pH range. Next, in a hydroxide aqueous solution showing a high exchange rate,
We investigated the time course of the ion exchange reaction of NaH-type compounds. 0.5g of NaH-type compound and 0.1M AOH (A is Li,
40 ml of an aqueous solution (Na and K) was added and ion exchange reactions were carried out at a temperature of 60° C. for 1 hour, 3 hours, 6 hours, 1 day, 2 days and 3 days, respectively. The results are shown in Figure 2. The ion exchange rate is
In a 0.1M LiOH aqueous solution, it becomes about 45% in 1 hour, increases with time, reaches about 63% in 2 days, and then remains almost constant. In a 0.1M NaOH aqueous solution, it becomes about 18% in 1 hour, then increases with time, reaching about 44% in 3 days. 0.1M
In a KOH aqueous solution of , it is about 5% in 1 hour, and increases to about 11% over the next 3 days. In this way, since the reaction with Li + is the fastest, Li + is taken up from the mixed alkaline aqueous solution the fastest, and the following experiment was conducted based on the assumption that the Li + selectivity caused by this would be expressed. The ion selectivity of ion exchange reactions for Li + , Na + and K + was investigated. 0.1M LiOH,
Add 0.5 g of NaH type compound to a mixed aqueous solution of 40 ml each of NaOH and KOH aqueous solutions,
The ion exchange reaction was carried out for 3 days at a temperature of .degree. As a result, the molar ratio of Li:Na:K in the reaction product was 1.00:0.26:0.01, and it was found that Li + with the smallest ionic radius was incorporated the most. In other words, the exchange amount of Li + is the second largest
It shows extremely high Li + selectivity, four times that of Na + . Comparative Example Titanium dioxide and potassium carbonate (K 2 CO 3 ), which are special grade reagents, were mixed at a molar ratio of 3.5:1 and calcined under the same conditions as in the example. One of them was called a K-type compound). Next, 1 g of this K-type compound was acid-treated under the same conditions as in the example. As a result, all reaction products were the same compound (KH type compound). The KH type compounds will be described below. It was confirmed from the following experimental results that the KH type compound has a composition of H 2 Ti 4 O 9.H 2 O. It was confirmed by atomic absorption spectrometry of the aqueous solution that the KH type compound does not contain alkali metal ions. In addition, K-type compounds are monoclinic compounds, and KH
For type compounds, the inventors also indexed them based on the monoclinic system. Their lattice constants are: K type compound a = 18.25 Å, b = 3.791 Å, c = 12.01 Å, β = 106.4° KH type compound a = 18.77 Å, b = 3.750 Å, c = 11.62 Å, β = 104.6° The acid treatment increased the value of a corresponding to the interlayer distance, but the other values of b, c, and β did not change significantly. This means that the interlayer K + (radius 1.33 Å) of the K-type compound is slightly larger than the hydronium ion.
This shows that H 3 O + (1.40 Å) was substituted, and the structure of the host (Ti 4 O 9 ) 2- layer was maintained. Furthermore, when differential thermal analysis was performed on the KH type compound in the range from room temperature to 800°C, endothermic peaks accompanied by weight loss were observed at 40-90°C and 90-250°C. From this weight loss, the amount of H 2 O in the KH type compound was determined. Furthermore, when the infrared absorption vector of the KH type compound is measured, the H - O stretching vibration and
The bending vibration of H-O-H near 1600 cm -1 was observed, indicating the presence of H 2 O. From the above, it is clear that H 3 O + incorporated into the KH type compound becomes free water (interlayer water) between the layers, and its composition is
It was found to be H 2 Ti 4 O 9 ·H 2 O. We also investigated the cation exchange properties of this KH type compound. First, 0.5g of KH type compound, 0.1M ACL and
Add 40ml of AOH (A is Li, Na or K) aqueous solution to the third
The combinations shown in the table were added and an ion exchange reaction was carried out at a temperature of 60 degrees for 3 days.
【表】【table】
【表】
反応生成物は実施例2と同じ方法で分析を行な
つた。それらの結果に基づいて計算した各反応生
成物の化学式を第4表に示す。[Table] The reaction products were analyzed in the same manner as in Example 2. Table 4 shows the chemical formulas of each reaction product calculated based on those results.
【表】
このように、KH型化合物は塩化物水溶液に浸
漬中に殆どイオン交換反応を起こさないことがわ
かつた。他方、水酸化物水溶液に浸漬すると、
A+の種類によつて異なるが、KH型化合物の層間
H+およびH3O+のち75〜85%がA+にイオン交換さ
れることがわかつた。
次に実施例と同様、反応のPH依存性を調べた。
0.1MのKClとKOHの各水溶液を混合して、PHが
8.0、9.0、10.0、11.0、12.0および12.5の水溶液を
調製し、これらの水溶液40mlに、それぞれKH型
化合物0.5gを加え、60℃の温度下において3日
間イオン交換反応を行なわせた。結果を第3図に
示す。このようにイオン交換率はPHが11〜12付近
に急激な立上がりを持つ曲線で表わされ、PHの高
い領域でイオン交換率が高くなることを示した。
次に高い交換率を示す水酸化物水溶液中での
KH型化合物のイオン交換反応の経時変化を調べ
た。KH型化合物0.5gに0.1MのAOH(AはLi、
NaおよびK)水溶液40mlを加え、60℃の温度下
において、1時間、3時間、6時間、1日、2日
間および3日間それぞれイオン交換反応を行なわ
せた。結果を第4図に示す。イオン交換率は、
0.1MのLiOH水溶液中では1時間で約75%に達
し、その後もほぼこの値で一定となる。0.1Mの
NaOH水溶液中では1時間で約60%、2時間で約
65%、その後約70%まで達しほぼ一定となる。
0.1MのKOH水溶液中では1時間で約82%に達
し、その後もほぼこの値で一定となる。このよう
に、KH型化合物においては、Li+、Na+およびK+
との反応はすべて速やかで、反応速度差は認めら
れなかつた。
最後の、Li+、Na+およびK+に対するイオン交
換反応のイオン選択性について調べた。0.1Mの
LiOH、NaOHおよびKOH水溶液をそれぞれ40ml
ずつ混合した水溶液にKH型化合物0.5gを加え
て、60℃の温度下において3日間イオン交換反応
を行なわせた。結果、反生成物中のLi:Na:K
のモル日は1.00:0:0.51となりNaH型と同じ
く、最もイオン半径の小さいLi+が最も多く取り
込まれることがわかつた。しかし、この場合Li+
以下のイオン量が略倍増し、Li+の交換量が2番
目に多いK+の約2倍しかなく、Li+選択性は不十
分である。[Table] Thus, it was found that the KH type compound hardly caused an ion exchange reaction while immersed in an aqueous chloride solution. On the other hand, when immersed in an aqueous hydroxide solution,
Although it depends on the type of A + , the interlayer of KH type compound
It was found that 75-85% of H + and H 3 O + was ion-exchanged to A + . Next, the PH dependence of the reaction was investigated in the same manner as in the examples.
Mix 0.1M KCl and KOH aqueous solutions and adjust the pH.
Aqueous solutions of 8.0, 9.0, 10.0, 11.0, 12.0 and 12.5 were prepared, and 0.5 g of the KH type compound was added to each of 40 ml of these aqueous solutions, and an ion exchange reaction was carried out at a temperature of 60° C. for 3 days. The results are shown in Figure 3. In this way, the ion exchange rate was expressed by a curve with a sharp rise around pH 11 to 12, indicating that the ion exchange rate was high in the high pH range. In hydroxide aqueous solution showing the next highest exchange rate
We investigated the time course of the ion exchange reaction of KH type compounds. 0.1M AOH (A is Li,
40 ml of an aqueous solution (Na and K) was added, and the ion exchange reaction was carried out at a temperature of 60° C. for 1 hour, 3 hours, 6 hours, 1 day, 2 days, and 3 days, respectively. The results are shown in Figure 4. The ion exchange rate is
In a 0.1M LiOH aqueous solution, it reaches about 75% in one hour and remains almost constant at this value thereafter. 0.1M
In NaOH aqueous solution, about 60% in 1 hour, about 60% in 2 hours
65%, then reaches about 70% and remains almost constant.
In a 0.1M KOH aqueous solution, it reaches approximately 82% in 1 hour and remains approximately constant at this value thereafter. Thus, in KH type compounds, Li + , Na + and K +
All reactions were rapid, and no difference in reaction rate was observed. Finally, the ion selectivity of the ion exchange reaction for Li + , Na + and K + was investigated. 0.1M
40ml each of LiOH, NaOH and KOH aqueous solutions
0.5 g of the KH type compound was added to the mixed aqueous solution, and an ion exchange reaction was carried out at a temperature of 60° C. for 3 days. As a result, Li:Na:K in the reaction product
The molar day of is 1.00:0:0.51, and it was found that, like the NaH type, Li + with the smallest ionic radius is taken in the most. But in this case Li +
The amount of the following ions almost doubles, and the exchange amount of Li + is only about twice that of K + , which is the second largest, so the Li + selectivity is insufficient.
第1図と第2図は本発明の実施例を示し、第1
図はNaH型化合物のイオン交換反応PH依存性を示
すグラフ、第2図はNaH型化合物の水酸化アルカ
リ水溶液中でのイオン交換反応の経時変化を示す
グラフである。第3図と第4図は比較例を示し、
第3図はKH型化合物のイオン交換反応のPH依存
性を示すグラフ、第4図はKH型化合物の水酸化
アルカリ水溶液中でのイオン交換反応の経時変化
を示すグラフである。
1 and 2 show embodiments of the present invention;
The figure is a graph showing the pH dependence of the ion exchange reaction of the NaH type compound, and Figure 2 is a graph showing the time course of the ion exchange reaction of the NaH type compound in an aqueous alkali hydroxide solution. Figures 3 and 4 show comparative examples;
FIG. 3 is a graph showing the pH dependence of the ion exchange reaction of the KH type compound, and FIG. 4 is a graph showing the time course of the ion exchange reaction of the KH type compound in an aqueous alkali hydroxide solution.
Claims (1)
して得られるH2Ti3O7の組成を有する化合物から
なることを特徴とするLi+選択性イオン交換体。1. A Li + selective ion exchanger comprising a compound having a composition of H 2 Ti 3 O 7 obtained by acid treatment of Na 2 Ti 3 O 7 having a layered crystal structure.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP58025292A JPS59150543A (en) | 1983-02-16 | 1983-02-16 | Synthesis of alkali titanate type ion exchange material |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP58025292A JPS59150543A (en) | 1983-02-16 | 1983-02-16 | Synthesis of alkali titanate type ion exchange material |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS59150543A JPS59150543A (en) | 1984-08-28 |
| JPS6133622B2 true JPS6133622B2 (en) | 1986-08-02 |
Family
ID=12161937
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP58025292A Granted JPS59150543A (en) | 1983-02-16 | 1983-02-16 | Synthesis of alkali titanate type ion exchange material |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS59150543A (en) |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP5164131B2 (en) * | 2006-02-27 | 2013-03-13 | 独立行政法人産業技術総合研究所 | Active material for lithium secondary battery, method for producing the same, and lithium secondary battery using the same |
| JP5438891B2 (en) * | 2007-08-23 | 2014-03-12 | 株式会社東芝 | Non-aqueous electrolyte secondary battery negative electrode material, non-aqueous electrolyte secondary battery negative electrode material manufacturing method, non-aqueous electrolyte secondary battery, and battery pack |
| JP5551483B2 (en) * | 2010-03-25 | 2014-07-16 | 国立大学法人信州大学 | Filtration material and purification device |
| CN103483897B (en) * | 2013-10-17 | 2015-09-09 | 盐城工学院 | Preparation method of self-healing coating based on corrosion inhibitor intercalation nano titanate carrier |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS553371A (en) * | 1978-06-23 | 1980-01-11 | Natl Inst For Res In Inorg Mater | Production of titania hydrate fiber, titania glass fiber and titania fiber |
| JPS5617928A (en) * | 1979-07-23 | 1981-02-20 | Natl Inst For Res In Inorg Mater | Manufacture of titania hydrate fiber, titania glass fiber and titania fiber |
| JPS5820300B2 (en) * | 1979-12-17 | 1983-04-22 | 科学技術庁無機材質研究所長 | Adsorption and ion exchange material for cesium in aqueous solution |
-
1983
- 1983-02-16 JP JP58025292A patent/JPS59150543A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS59150543A (en) | 1984-08-28 |
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