JP2001163618A - Production process of high purity zinc borofluoride hexahydrate - Google Patents

Production process of high purity zinc borofluoride hexahydrate

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Publication number
JP2001163618A
JP2001163618A JP35083999A JP35083999A JP2001163618A JP 2001163618 A JP2001163618 A JP 2001163618A JP 35083999 A JP35083999 A JP 35083999A JP 35083999 A JP35083999 A JP 35083999A JP 2001163618 A JP2001163618 A JP 2001163618A
Authority
JP
Japan
Prior art keywords
zinc
borofluoride
hexahydrate
water
zinc borofluoride
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP35083999A
Other languages
Japanese (ja)
Other versions
JP4559570B2 (en
Inventor
Toshiro Fukutome
敏郎 福留
Hirohisa Kikuyama
裕久 菊山
Yoji Yazaki
洋史 矢崎
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Stella Chemifa Corp
Original Assignee
Stella Chemifa Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Stella Chemifa Corp filed Critical Stella Chemifa Corp
Priority to JP35083999A priority Critical patent/JP4559570B2/en
Priority to TW089124088A priority patent/TW496788B/en
Priority to KR1020000074892A priority patent/KR100673874B1/en
Publication of JP2001163618A publication Critical patent/JP2001163618A/en
Application granted granted Critical
Publication of JP4559570B2 publication Critical patent/JP4559570B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Classifications

    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01GCOMPOUNDS CONTAINING METALS NOT COVERED BY SUBCLASSES C01D OR C01F
    • C01G9/00Compounds of zinc
    • C01G9/04Halides
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01GCOMPOUNDS CONTAINING METALS NOT COVERED BY SUBCLASSES C01D OR C01F
    • C01G9/00Compounds of zinc
    • C01G9/006Compounds containing, besides zinc, two ore more other elements, with the exception of oxygen or hydrogen

Abstract

PROBLEM TO BE SOLVED: To provide production process for a high purity zinc borofluoride hexahydrate by which a crystalline product of high purity zinc borofluoride hexahydrate can simply be produced at a low cost without requiring such operation as evaporation or concentration and also without using any expensive solvent such as alcohol, with only a stoichiometric means. SOLUTION: This production process comprises a step reacting zinc or a zinc compound with a borofluoride compound, wherein: the total amount of water participating to the reaction is equal to or slightly smaller than the amount of water required to form zinc borofluoride hexahydrate by hydrating zinc borofluoride; and as the above zinc compound, zinc fluoride tetrahydrate and/or anhydrous zinc fluoride can preferably be used.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】本発明は、高純度ホウフッ化亜鉛
6水塩の製造方法に係り、より詳細には、例えば、金属
製の缶の内面にエポキシ樹脂をコーティング施工する際
にエポキシ樹脂硬化剤として使用される高純度ホウフッ
化亜鉛6水塩の製造方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing high-purity zinc borofluoride hexahydrate, and more particularly to, for example, epoxy resin curing when coating an inner surface of a metal can with an epoxy resin. The present invention relates to a method for producing high-purity zinc borofluoride hexahydrate used as an agent.

【0002】[0002]

【従来の技術】ホウフッ化亜鉛6水塩は1809年Ga
y−Lussac等によって発明されて以来、多数の研
究がなされて来た。その製法は主に亜鉛化合物とホウフ
ッ酸とを反応させる方法である。
2. Description of the Related Art Zinc borofluoride hexahydrate has a 1809 Ga
Numerous studies have been made since it was invented by y-Lussac et al. The production method is mainly a method of reacting a zinc compound with borofluoric acid.

【0003】また、三フッ化ホウ素を用いる方法がMe
yerhoferによって研究され、Brit.Pat
ent 226,491(Dec,20,1923)に
なっている。
A method using boron trifluoride is known as Me.
studied by Yerhofer and described in Brit. Pat
ent 226, 491 (Dec, 20, 1923).

【0004】ホウフッ化亜鉛の用途は亜鉛メッキやWa
sh and wear加工用にエポキシ樹脂の硬化剤
として用いられている。
[0004] Zinc borofluoride is used for zinc plating and Wa.
It is used as a curing agent for epoxy resins for sh and wear processing.

【0005】これらの用途に対してはホウフッ化亜鉛六
水塩は水溶液として使用される。従って、結晶状の製品
ではなく、例えば、ホウフッ化亜鉛を40〜50%含有
する水溶液でよかった。
[0005] For these applications, zinc borofluoride hexahydrate is used as an aqueous solution. Therefore, instead of a crystalline product, an aqueous solution containing, for example, 40 to 50% of zinc borofluoride was preferred.

【0006】近年になり、ホウフッ化亜鉛六水塩は、缶
内面にエポキシ樹脂をコーティングする際のエポキシ樹
脂の硬化剤として使用されている。かかる用途に対して
は水分の少ないホウフッ化亜鉛6水塩の結晶状の製品が
重用される。
In recent years, zinc borofluoride hexahydrate has been used as a curing agent for an epoxy resin when coating the inside of a can with an epoxy resin. For such applications, a crystalline product of zinc borofluoride hexahydrate having a low water content is frequently used.

【0007】この結晶状の製品は従来の製法による水溶
液から得るのは極めて困難である。水溶液を濃縮すれ
ば、やがてシロップ状になり、なかなか結晶化するに至
らない。濃縮液を冷却して結晶を得ても収率が極めて低
く、不経済である。反応系に余分な水分があれば、生成
物がその水分に溶解して結晶が析出しないとか析出して
もなかなか乾燥しにくいとかなどの問題がある。
[0007] This crystalline product is very difficult to obtain from aqueous solutions by conventional manufacturing methods. When the aqueous solution is concentrated, it eventually becomes a syrup and does not readily crystallize. Even if the concentrated solution is cooled to obtain crystals, the yield is extremely low and uneconomical. If there is excess water in the reaction system, there is a problem that the product is dissolved in the water and crystals do not precipitate, or even if it precipitates, it is difficult to dry.

【0008】そのため、より蒸発しやすいアルコールで
脱水・乾燥する手段がとられる。この場合、溶媒として
アルコールを使用せざるを得ず、また、脱水・乾燥など
の操作に手間がかかりる。従って、この方法はコストア
ップになる。さらに、この方法では最終的な収率は精々
70〜75%にとどまるため原価が高くなってしまう。
また溶媒のアルコールは回収再利用しないかぎり、環境
汚染の原因になる。
For this reason, means for dehydrating and drying with alcohol which is more easily evaporated is used. In this case, alcohol must be used as a solvent, and operations such as dehydration and drying are troublesome. Therefore, this method increases the cost. Furthermore, this method results in a high cost since the final yield is at most 70-75%.
In addition, unless the solvent alcohol is collected and reused, it causes environmental pollution.

【0009】[0009]

【発明が解決しようとする課題】本発明は、ホウフッ化
亜鉛6水塩の結晶状製品を、蒸発濃縮などの操作にたよ
ることなく、またアルコールなどの高価な溶媒を使用せ
ずに、単に化学量論的手段を用いるだけで簡便かつ安価
に製造することができる高純度ホウフッ化亜鉛6水塩の
製造方法を提供することを目的とする。
SUMMARY OF THE INVENTION The present invention provides a method for producing a crystalline product of zinc borofluoride hexahydrate without resorting to operations such as evaporation and concentration, and without using expensive solvents such as alcohol. An object of the present invention is to provide a method for producing high-purity zinc borofluoride hexahydrate that can be produced simply and inexpensively simply by using stoichiometric means.

【0010】[0010]

【課題を解決するための手段】上記課題は、亜鉛または
亜鉛化合物とホウフッ化化合物とを反応させることによ
りホウフッ化亜鉛6水塩を製造するホウフッ化亜鉛6水
塩の製造方法において、反応に関与する水の総量がホウ
フッ化亜鉛が水和して6水和物になる量に等しいかわず
かに少なくなるようにして反応させることを特徴とする
高純度ホウフッ化亜鉛6水塩の製造方法により解決され
る。
An object of the present invention is to provide a method for producing zinc borofluoride hexahydrate by reacting zinc or a zinc compound with a borofluoride compound to produce zinc borofluoride hexahydrate. A method for producing high purity zinc borofluoride hexahydrate, characterized in that the reaction is carried out so that the total amount of water to be formed is equal to or slightly less than the amount of hydrated zinc borofluoride to hexahydrate. Is done.

【0011】また、該亜鉛化合物がフッ化亜鉛4水塩お
よび/または無水フッ化亜鉛であることが好ましい。
Further, the zinc compound is preferably zinc fluoride tetrahydrate and / or anhydrous zinc fluoride.

【0012】[0012]

【作用】本発明者は、ホウフッ化亜鉛6水塩の晶出に際
して、その物性を克明に観察検討した結果、亜鉛やホウ
素、フッ素などの物量バランスはしっかりと合わせるこ
とは言うまでもないが、反応に関与する水の存在が大き
く影響していることを見い出した。反応に関与する水の
総量がホウフッ化亜鉛が水和して6水和物になる量に等
しいかわずかに少なくなるようにして反応させる。原料
に由来する水や反応によって生成する水の総量を把握し
て反応させるのがこの製法のポイントである。
The present inventor has carefully observed and studied the physical properties of zinc borofluoride hexahydrate when crystallizing it, and as a result, it was needless to say that the balance of the quantities of zinc, boron, fluorine, etc. was tightly adjusted. It was found that the presence of the water involved had a significant effect. The reaction is performed such that the total amount of water involved in the reaction is equal to or slightly less than the amount of zinc borofluoride hydrated to hexahydrate. The point of this production method is to grasp the total amount of water derived from the raw materials and the water generated by the reaction and to cause the reaction.

【0013】反応系に存在する水の総量は、ホウフッ化
亜鉛1モルに対して、6モルか6モルよりやや少ない程
度が限度である。
The total amount of water present in the reaction system is limited to 6 mol or slightly less than 6 mol per mol of zinc borofluoride.

【0014】原料に含まれる水分と反応生成水の和が
5.5〜6モルになるように原料を組み合わせ、不足量
は水を加えて補えばよい。
The raw materials are combined so that the sum of the water contained in the raw materials and the reaction water is 5.5 to 6 mol, and the shortage may be compensated by adding water.

【0015】この条件を満たす原料を次の群から選んで
組み合わせればよい。 Zn原料:亜鉛未,酸化亜鉛,フッ化亜鉛4水塩,無水
フッ化亜鉛 ホウフッ化物原料:BF3(ガス),BF3・H2O,2
BF3・3H2O,BF3・2H2O,CH3OH・BF3
25OH・BF3,(CH32O・BF3,(C25
2O・BF3
Materials satisfying this condition may be selected from the following group and combined. Zn raw material: zinc not, zinc oxide, zinc fluoride tetrahydrate, anhydrous zinc fluoride borofluoride raw material: BF 3 (gas), BF 3 .H 2 O, 2
BF 3 · 3H 2 O, BF 3 · 2H 2 O, CH 3 OH · BF 3,
C 2 H 5 OH.BF 3 , (CH 3 ) 2 O.BF 3 , (C 2 H 5 )
2 O ・ BF 3

【0016】これらの組み合わせの数例を化学式で例示
する。 Zn+2HF+2BF3・3H2O+3H2O→Zn(B
42・6H2O+H2 ZnO+2HF+2(BF3・2H2O)+H2O→Zn
(BF42・6H2O ZnF2・4H2O+2(BF3・H2O)→Zn(B
42・6H2O ZnF2+2BF3・3H2O+3H2O→Zn(BF42
・6H2O ZnF2・4H2O+2(CH3OH・BF3)+2H2
→Zn(BF42・6H2O+2CH3OH ZnF2+2{(C252O・BF3}+6H2O→Zn
(BF4)・6H2O+2(C252
Several examples of these combinations are illustrated by chemical formulas. Zn + 2HF + 2BF 3 · 3H 2 O + 3H 2 O → Zn (B
F 4) 2 · 6H 2 O + H 2 ZnO + 2HF + 2 (BF 3 · 2H 2 O) + H 2 O → Zn
(BF 4 ) 2 .6H 2 O ZnF 2 .4H 2 O + 2 (BF 3 .H 2 O) → Zn (B
F 4) 2 · 6H 2 O ZnF 2 + 2BF 3 · 3H 2 O + 3H 2 O → Zn (BF 4) 2
6H 2 O ZnF 2 .4H 2 O + 2 (CH 3 OH.BF 3 ) + 2H 2 O
→ Zn (BF 4 ) 2 .6H 2 O + 2CH 3 OH ZnF 2 +2 {(C 2 H 5 ) 2 O.BF 3 } + 6H 2 O → Zn
(BF 4 ) · 6H 2 O + 2 (C 2 H 5 ) 2 O

【0017】Znの原料としてはフッ化亜鉛4水塩やこ
の化合物を110℃で加熱・脱水して得た無水フッ化亜
鉛が純度の高い製品を得るのに好適である。
As a raw material of Zn, zinc fluoride tetrahydrate or anhydrous zinc fluoride obtained by heating and dehydrating this compound at 110 ° C. is suitable for obtaining a product of high purity.

【0018】亜鉛末や酸化亜鉛とフッ化水素酸でフッ化
亜鉛を合成して、これに三フッ化ホウ素を添加してホウ
フッ化亜鉛を得る方法では、反応が緩慢であり、前記方
法に比べると高純度の製品が得られにくい。
In the method of synthesizing zinc fluoride with zinc powder or zinc oxide and hydrofluoric acid and adding boron trifluoride to this to obtain zinc borofluoride, the reaction is slow and compared with the above method. And high purity products are difficult to obtain.

【0019】ホウフッ化物原料としては、三フッ化ホウ
素ガスのほか、BF3・H2O,2BF3・3H2O、BF
3・2H2Oなどの水錯塩が好適である。
Borofluoride raw materials include BF 3 .H 2 O, 2BF 3 .3H 2 O, and BF 3 in addition to boron trifluoride gas.
Water complex salts such as 3 · 2H 2 O are preferred.

【0020】アルコールやエーテルなどの三フッ化ホウ
素錯塩はフッ化亜鉛とよく反応するが、BF3を離した
のちアルコールやエーテルが遊離して来る。副生したア
ルコールやエーテルにはホウフッ化亜鉛が多量にとける
ので、結晶状のホウフッ化亜鉛6水塩を得るには、加熱
してアルコールやエーテルを蒸発・濃縮冷却して晶析さ
せる必要があり、好ましくない。
A boron trifluoride complex salt such as alcohol or ether reacts well with zinc fluoride, but after releasing BF 3 , alcohol or ether is liberated. Since a large amount of zinc borofluoride dissolves in the by-produced alcohol or ether, it is necessary to crystallize by heating, evaporating, concentrating and cooling the alcohol or ether to obtain crystalline zinc borofluoride hexahydrate. Is not preferred.

【0021】本発明者はホウフッ化亜鉛6水塩を調製す
る際の水の影響について詳細に検討した。
The present inventors have studied in detail the effect of water when preparing zinc borofluoride hexahydrate.

【0022】フッ化亜鉛4水塩を脱水して得た無水フッ
化亜鉛と2BF3・3H2Oの組成を持つ三フッ化ホウ素
水錯塩とを反応させてホウフッ化亜鉛6水塩1モルを調
整するに際し、水の存在量を5モル〜6.25モルの範
囲で0.25モルづつ変化させて影響を検討した結果、
表1に示すとおりであった。
The anhydrous zinc fluoride obtained by dehydrating the zinc fluoride tetrahydrate is reacted with a boron trifluoride water complex having a composition of 2BF 3 .3H 2 O to form 1 mol of zinc borofluoride hexahydrate. As a result of examining the effect by changing the amount of water in the range of 5 mol to 6.25 mol by 0.25 mol at the time of adjustment,
As shown in Table 1.

【0023】ホウフッ化亜鉛6水塩の生成反応は水の過
不足に大きく左右される。水が不足すれば反応が完全に
は進行せず、生成物からはガスが盛んに発生する。その
程度は水が少なければ少ないほど多くなる。
The formation reaction of zinc borofluoride hexahydrate largely depends on the excess or deficiency of water. If water is insufficient, the reaction does not proceed completely, and gas is generated from the product. The lower the water, the greater the degree.

【0024】[0024]

【表1】ホウフッ化亜鉛6水塩調製時の水の過不足の影
Table 1 Influence of excess or deficiency of water when preparing zinc borofluoride hexahydrate

【0025】この生成物に不足分の水を補填してやる
と、直ちに反応して正常な粉状製品になる。このとき発
熱を伴うがこの熱は水和熱と推測される。水和の不完全
な生成物は不安定な状態でガス化しやすいものと考えら
れる。
When this product is supplemented with a shortage of water, it reacts immediately and becomes a normal powdery product. At this time, heat is generated, but this heat is presumed to be heat of hydration. Incompletely hydrated products are considered to be unstable and prone to gasification.

【0026】一方、余剰な水分があれば、その水分に結
晶が溶解して一部シロップ状を呈し湿潤状態になり、乾
燥してもなかなか粉状製品をえるのが難しくなる。
On the other hand, if there is excess water, the crystals dissolve in the water and become partially syrup-like and become wet, making it difficult to obtain a powdery product even when dried.

【0027】以上のとおり高純度ホウフッ化亜鉛6水塩
を得るキイポイントは水の管理である。原料に含まれる
水や反応生成水など反応系に存在する水総量がホウフッ
化亜鉛1モルに対して好ましくは5.5〜6.25モ
ル、より好ましくは5.75〜6モルになるように制御
する。
As described above, the key point for obtaining high-purity zinc borofluoride hexahydrate is water management. The total amount of water present in the reaction system, such as water contained in the raw materials and reaction product water, is preferably 5.5 to 6.25 mol, more preferably 5.75 to 6 mol, per mol of zinc borofluoride. Control.

【0028】本発明の製造方法は溶解・濾過精製、再結
晶などの手間のかかる操作を省き、一工程で高純度の製
品を得る方法を提供するものであるが、厳正な条件下で
行っても製品中に精々1.5%程度ではあるがエチルア
ルコール不溶解分を含む。この不溶解分はX線回折分析
の結果、フッ化亜鉛であることが確認された。
The production method of the present invention provides a method for obtaining a high-purity product in one step by eliminating troublesome operations such as dissolution / filtration / purification and recrystallization, but it is carried out under strict conditions. However, the product contains ethyl alcohol-insoluble components at about 1.5% at most. As a result of X-ray diffraction analysis, this insoluble matter was confirmed to be zinc fluoride.

【0029】このエチルアルコール不溶解分は、製品を
保管養生することによって、徐々に低減することがわか
った。保管養生の条件は60℃程度の保温下で行えばよ
り短時間で促進されるが、それだけコストがかかるの
で、常温下で充分である。常温下で行ったエチルアルコ
ール不溶解分低減試験結果の例を図1に示す。保管養生
は、製品をビンなどに入れ、蓋をした状態で行うことが
好ましい。ホウフッ化亜鉛6水塩は、水との親和性が高
く、吸湿性が高いため水分を含む雰囲気から遮断するた
めビンなどの容器に入れ蓋をした状態で保管養生を行う
ものである。
It has been found that the insoluble content of ethyl alcohol is gradually reduced by curing the product after storage. The condition of storage curing can be accelerated in a shorter time if the condition is kept at a temperature of about 60 ° C., but the cost is high, so that the condition at room temperature is sufficient. FIG. 1 shows an example of the results of a test for reducing ethyl alcohol insolubles conducted at room temperature. The storage curing is preferably performed with the product placed in a bottle or the like and covered. Zinc borofluoride hexahydrate has a high affinity for water and has high hygroscopicity, so that it is stored and cured in a container such as a bottle in order to shield it from an atmosphere containing moisture.

【0030】この結果によれば、調製当日1%前後あっ
たエチルアルコール不溶解分は養生熟成することによっ
て、1日経過時に急激に低下し、3日でさらに低下し、
以降次第に低下して来る。エチルアルコールに溶けるホ
ウフッ化亜鉛分が99.5%以上の高純度に仕上げるに
は常温においてさえおよそ3日あれば充分である。
According to the results, the ethyl alcohol insoluble content, which was about 1% on the day of preparation, decreased rapidly after one day due to curing and aging, and further decreased after three days.
Then it gradually decreases. About three days is enough even at room temperature to achieve a high purity of 99.5% or more of zinc borofluoride dissolved in ethyl alcohol.

【0031】[0031]

【実施例】以下に実施例を示して本発明の方法を具体的
に開示する。
The following examples are provided to further illustrate the method of the present invention.

【0032】(実施例1)フッ化亜鉛4水塩を脱水して
得た無水フッ化亜鉛12.5gを容積1L(リットル)
のPFAビンにとり純水13.0gを加えて懸濁状とし
た。
(Example 1) 12.5 g of anhydrous zinc fluoride obtained by dehydrating zinc fluoride tetrahydrate was added in a volume of 1 L (liter).
And 13.0 g of pure water was added to the PFA bottle to form a suspension.

【0033】三フッ化ホウ素ガス16.5gを加えたと
ころ激しく発熱反応し、温度は112℃まで上った。三
フッ化ホウ素ガスが僅かに残ったので窒素ガスを通じて
パージした。生成物は粉状結晶で、収量は41.8gで
理論値に等しかった。
When 16.5 g of boron trifluoride gas was added, a vigorous exothermic reaction occurred, and the temperature rose to 112 ° C. Since a small amount of boron trifluoride gas remained, the gas was purged through nitrogen gas. The product was powdery crystals with a yield of 41.8 g, equivalent to theory.

【0034】生成物を分析したところエタノール不溶解
分0.62%、含量(Znから)99.8%であった。
The product was analyzed and found to have an ethanol-insoluble content of 0.62% and a content (from Zn) of 99.8%.

【0035】(実施例2)フッ化亜鉛4水塩131.6
gと、フッ化亜鉛4水塩を脱水して得た無水フッ化亜鉛
25.9gとを容積1LのPFAビンにとり、2BF3
・3H2Oの組成を持つ三フッ化ホウ素水錯塩191.
5gを加えたところ激しく反応して発熱し80℃まで昇
温した。よく振ってさらに反応をすすめたところ、1時
間後に固体粉状の製品348.3gを得た(収率99.
8%)。含量(Znから)100.2%であった。
(Example 2) 131.6 zinc fluoride tetrahydrate
g and 25.9 g of anhydrous zinc fluoride obtained by dehydrating zinc fluoride tetrahydrate are placed in a 1 L PFA bottle, and 2BF 3
· 3H boron trifluoride water complexes 191 having the composition 2 O.
When 5 g was added, the mixture violently reacted and generated heat, and the temperature was raised to 80 ° C. The mixture was further shaken to further promote the reaction, and after 1 hour, 348.3 g of a solid powdery product was obtained (yield: 99.9%).
8%). Content (from Zn) 100.2%.

【0036】室温において7日熟成後同様に分析したと
ころエタノール不溶解分0.20%、含量(Znから)
100.6%であった。
After aging at room temperature for 7 days, the same analysis was carried out to find that the content insoluble in ethanol was 0.20% and the content (from Zn)
It was 100.6%.

【0037】(実施例3)フッ化亜鉛4水塩を脱水して
得た無水フッ化亜鉛103.8gを容積1LのPFAビ
ンにとり、BF3・H2Oの組成を持つ三フッ化ホウ素水
錯塩171gを徐々に加えたところ少し反応して70℃
まで昇温した。この混合物に純水72gを少しづつ加え
て混合、反応したところ、激しく反応して発熱し、11
7℃まで昇温した。反応後8時間して分析したところエ
タノール不溶解分1.35%、含量(Znから)10
1.8%であった。
Example 3 103.8 g of anhydrous zinc fluoride obtained by dehydrating zinc fluoride tetrahydrate was placed in a 1 L PFA bottle, and boron trifluoride water having a composition of BF 3 .H 2 O was used. When 171 g of a complex salt was gradually added, a little
Temperature. When 72 g of pure water was added little by little to the mixture and mixed and reacted, the mixture vigorously reacted and generated heat.
The temperature was raised to 7 ° C. Analysis was conducted 8 hours after the reaction, whereupon ethanol insoluble content was 1.35%, content (from Zn) 10
1.8%.

【0038】常温において7日間保管養生して同様に分
析したところエタノール不溶解分0.16%、含量(Z
nから)101.3%であった。
After storage and curing at room temperature for 7 days and analysis in the same manner, 0.16% of an ethanol-insoluble content and a content (Z
(from n) 101.3%.

【0039】(実施例4)フッ化亜鉛4水塩を脱水して
得た無水フッ化亜鉛830.4gを容積5LのPFAビ
ンに入れ、2BF3・3H2Oの組成を持つ三フッ化ホウ
素水錯塩1532gを加えたところ温度60℃のスラリ
ーになった。この混合物に純水418gを徐々に加えて
混合撹拌したところ、激しく反応して125℃まで昇温
した。製品2773g(収率99.8%)を得た。8時
間後分析したところ、エタノール不溶解分1.16%、
含量(Znから)101.1%であった。室温で7日間
保管熟成したのち、同様に分析したところ、エタノール
不溶解分0.1%、含量(Znから)100.0%であ
った。
Example 4 830.4 g of anhydrous zinc fluoride obtained by dehydrating zinc fluoride tetrahydrate was put into a 5 L PFA bottle, and boron trifluoride having a composition of 2BF 3 .3H 2 O was used. When 1532 g of a water complex salt was added, a slurry having a temperature of 60 ° C. was obtained. When 418 g of pure water was gradually added to this mixture and mixed and stirred, the mixture vigorously reacted and the temperature was raised to 125 ° C. 2773 g (yield 99.8%) of the product was obtained. When analyzed after 8 hours, ethanol insoluble content 1.16%,
Content (from Zn) 101.1%. After storage and aging at room temperature for 7 days, the same analysis revealed that the ethanol-insoluble content was 0.1% and the content (from Zn) was 100.0%.

【0040】(実施例5)フッ化亜鉛4水塩を脱水して
得た無水フッ化亜鉛103.8gに、BF3・H2Oの組
成を持つ三フッ化ホウ素水錯塩209.5gを混合し
た。混合すると少し反応し温度は65℃になった。
Example 5 209.5 g of an aqueous complex of boron trifluoride having a composition of BF 3 .H 2 O was mixed with 103.8 g of anhydrous zinc fluoride obtained by dehydrating zinc fluoride tetrahydrate. did. Upon mixing, the temperature slightly increased to 65 ° C.

【0041】この混合物に水36gを加えよく混合した
ところ激しく反応して発熱し、112℃まで昇温した。
When 36 g of water was added to the mixture and mixed well, the mixture vigorously reacted and generated heat, and the temperature was raised to 112 ° C.

【0042】8時間後分析したところエタノール不溶解
分1.45%、含量(Znから)100.6%であっ
た。
When analyzed after 8 hours, the ethanol-insoluble content was 1.45% and the content (from Zn) was 100.6%.

【0043】室温で7日保管熟成したのち、同様に分析
したところエタノール不溶解分0.32%含量(Znか
ら)100.9%であった。
After storage and aging at room temperature for 7 days, the same analysis revealed that the content of ethanol-insoluble matter was 0.32% (from Zn) 100.9%.

【0044】(比較例1)フッ化亜鉛4水塩175.4
gを容積1LのPFAビンにとり2BF3・3H2Oの組
成を持つ三フッ化ホウ素水錯塩191.5gを加えたと
ころ反応して発熱し85%まで昇温した。反応物はシロ
ップ状を呈した。
Comparative Example 1 Zinc Fluoride Tetrahydrate 175.4
g was placed in a 1 L PFA bottle, and 191.5 g of a boron trifluoride water complex salt having a composition of 2BF 3 .3H 2 O was added. The reaction was syrupy.

【0045】80℃湯浴上で窒素ガスを通じて5時間処
理したが、乾燥固体製品は得られなかった。
After treating with a nitrogen gas in an 80 ° C. water bath for 5 hours, a dry solid product was not obtained.

【0046】(比較例2)フッ化亜鉛4水塩175.4
gを容積1LのPFAビンにとり、2BF3・3H2Oの
組成を持つ三フッ化ホウ素水錯塩191gを加えて反応
させたところ反応して発熱し84℃まで昇温した。
Comparative Example 2 Zinc Fluoride Tetrahydrate 175.4
g was placed in a 1 L PFA bottle, and 191 g of a boron trifluoride water complex salt having a composition of 2BF 3 .3H 2 O was added and reacted. When the reaction occurred, a heat was generated and the temperature was raised to 84 ° C.

【0047】このものにエタノール200mlを加えて
濾過した。
This was added with 200 ml of ethanol and filtered.

【0048】未反応フッ化亜鉛の固体を濾別し澄明な濾
液を得た。
The unreacted zinc fluoride solid was filtered off to obtain a clear filtrate.

【0049】この濾液を100℃の湯浴上で窒素を通じ
ながら8時間濃縮した。
The filtrate was concentrated for 8 hours in a 100 ° C. water bath while passing nitrogen through.

【0050】冷却後晶出した結晶を濾別したところエチ
ルアルコールを含む湿潤結晶が得られた。
After cooling, the crystallized crystals were filtered off to obtain wet crystals containing ethyl alcohol.

【0051】このものを100℃湯浴上で窒素ガスを通
じながら乾燥したところ211gのホウフッ化亜鉛6水
塩を得た。収率60.8%製品を分析したところエタノ
ール不溶解分0.22%、含量(Znから)100.0
%であった。
This was dried on a 100 ° C. water bath while passing nitrogen gas to obtain 211 g of zinc borofluoride hexahydrate. Yield 60.8% The product was analyzed and found to be ethanol-insoluble 0.22%, content (from Zn) 100.0%
%Met.

【0052】この製法では濾過・濃縮・乾燥に手間がか
かり高価なアルコールを溶媒にする上に、収率が低い欠
点がある。
In this method, filtration, concentration and drying are troublesome, expensive alcohol is used as a solvent, and the yield is low.

【0053】(比較例3)三フッ化ホウ素のアルコール
錯塩と、フッ化亜鉛4水塩を脱水して得た無水フッ化亜
鉛とを反応させてホウフッ化亜鉛6水塩を得る。次式の
ような反応式に従って反応させる。
(Comparative Example 3) An alcohol complex salt of boron trifluoride is reacted with anhydrous zinc fluoride obtained by dehydrating zinc fluoride tetrahydrate to obtain zinc borofluoride hexahydrate. The reaction is performed according to the following reaction formula.

【0054】ZnF2+2CH3OH・BF3+6H2O→
Zn(BF42・6H2O+2CH3OH ZnF2+2C25OH・BF3+6H2O→Zn(B
42・6H2O+2C25OH
ZnF 2 + 2CH 3 OH.BF 3 + 6H 2 O →
Zn (BF 4 ) 2 .6H 2 O + 2CH 3 OH ZnF 2 + 2C 2 H 5 OH.BF 3 + 6H 2 O → Zn (B
F 4) 2 · 6H 2 O + 2C 2 H 5 OH

【0055】無水フッ化亜鉛51.8gと、BF3含量
52%の三フッ化ホウ素メタノール錯塩130.4gと
を混合した。
51.8 g of anhydrous zinc fluoride and 130.4 g of a boron trifluoride methanol complex salt having a BF 3 content of 52% were mixed.

【0056】この混合物に純水54.0gを加えて混合
撹拌したところ激しく反応して発熱し、95℃まで昇温
した。
When 54.0 g of pure water was added to this mixture and mixed and stirred, the mixture violently reacted to generate heat, and the temperature was raised to 95 ° C.

【0057】得られた反応生成物は透明な液体であり、
生成したホウフッ化亜鉛は全て副生するメタノールに溶
解しており、結晶を得るには更にメタノールやエタノー
ルを蒸発・濃縮する必要がある。
The reaction product obtained is a transparent liquid,
All the generated zinc borofluoride is dissolved in the by-produced methanol, and it is necessary to further evaporate and concentrate methanol and ethanol to obtain crystals.

【0058】(比較例4)三フッ化ホウ素のエーテル錯
塩とフッ化亜鉛4水塩を脱水して得た無水フッ化亜鉛と
を反応させてホウフッ化亜鉛六水塩を得る。次式のよう
な反応式に従って反応させる。
(Comparative Example 4) An ether complex salt of boron trifluoride and anhydrous zinc fluoride obtained by dehydrating zinc fluoride tetrahydrate are reacted to obtain zinc borofluoride hexahydrate. The reaction is performed according to the following reaction formula.

【0059】ZnF2+2(CH32O・BF3+6H2
O→Zn(BF42・6H2O+2(CH32O ZnF2+2(C2H5)2O・BF3+6H2O→Zn
(BF42・6H2O+2(C252
ZnF 2 +2 (CH 3 ) 2 O.BF 3 + 6H 2
O → Zn (BF 4 ) 2 .6H 2 O + 2 (CH 3 ) 2 O ZnF 2 +2 (C 2 H 5) 2 O.BF 3 + 6H 2 O → Zn
(BF 4) 2 · 6H 2 O + 2 (C 2 H 5) 2 O

【0060】無水フッ化亜鉛22.0gに、BF3含量
48.3%の三フッ化ホウ素エチルエーテル錯塩59.
5gを加えて混合した。
22.0 g of anhydrous zinc fluoride was mixed with a boron trifluoride ethyl ether complex salt having a BF 3 content of 48.3%.
5 g was added and mixed.

【0061】この混合物に純水22.9gを加えて混合
撹拌したところ、激しく反応して発熱した反応熱によっ
て副生したエチルエーテルの約半量が揮散したが、残り
の半量が反応系に残って、生成したホウフッ化亜鉛を溶
解して液状の生成物を得た。結晶を得るには残存するエ
ーテルを蒸発乾涸する必要がある。
When 22.9 g of pure water was added to this mixture and mixed and stirred, about half of the by-product ethyl ether was volatilized by the reaction heat generated by the vigorous reaction, but the remaining half remained in the reaction system. The resulting zinc borofluoride was dissolved to obtain a liquid product. To obtain crystals, the remaining ether must be evaporated to dryness.

【0062】(比較例5)亜鉛未32.7gと50%フ
ッ化水素酸40gおよび純水7gとを混合した。反応は
徐々にしか進行せず、湯浴上で2時間反応させたが、未
反応の亜鉛未が残った。 この混合物に2BF3
3H2Oの組成を持つ三フッ化ホウ素水錯塩95.8g
を加えた。この反応は次式に示すような関係になる。 Zn+2HF+3H2O+2BF3・3H2O→Zn(B
42・6H2O+H2
Comparative Example 5 32.7 g of zinc-free, 40 g of 50% hydrofluoric acid and 7 g of pure water were mixed. The reaction proceeded only slowly, and the reaction was carried out on a hot water bath for 2 hours, but unreacted zinc remained. 2BF 3
95.8 g of boron trifluoride water complex salt having a composition of 3H 2 O
Was added. This reaction has the relationship shown in the following equation. Zn + 2HF + 3H 2 O + 2BF 3 · 3H 2 O → Zn (B
F 4) 2 · 6H 2 O + H 2

【0063】24時間放置したのち分析したところエタ
ノール不溶解分3.8%、含量(Znから)86.1%
であり、とても実用になるような製品は得られなかっ
た。
After standing for 24 hours, analysis was carried out to find 3.8% ethanol-insoluble content and 86.1% content (from Zn).
Therefore, a very practical product could not be obtained.

【0064】(比較例6)酸化亜鉛20.35gと50
%フッ化水素酸20.0gとを混合したのち、2BF3
・3H2Oの組成を持つ三フッ化ホウ素水錯塩47.4
gを反応させた。
(Comparative Example 6) 20.35 g of zinc oxide and 50
% Hydrofluoric acid and 2BF 3
· Boron trifluoride water complex having a composition of 3H 2 O 47.4
g was reacted.

【0065】この反応は次式に示すような関係になる。 ZnO+2HF+2BF3・3H2O+2H2O→Zn
(BF42・6H2
This reaction has the relationship shown in the following equation. ZnO + 2HF + 2BF 3 · 3H 2 O + 2H 2 O → Zn
(BF 4) 2 · 6H 2 O

【0066】この反応は思ったより進行しにくく、60
℃湯浴上で10時間反応させたのち、分析したところエ
タノール不溶解分3.23%、含量(Znから)81.
5%を得た。純度が低く実用に供し得ないものであっ
た。
This reaction is less likely to proceed than expected,
After reacting in a hot water bath for 10 hours, analysis showed that the ethanol-insoluble content was 3.23% and the content (from Zn) was 81.degree.
5% was obtained. The purity was so low that it could not be put to practical use.

【0067】[0067]

【発明の効果】例えば缶内面の樹脂コーティング用のエ
ポキシ樹脂硬化剤として重用されるホウフッ化亜鉛6水
塩の固体製品を化学量論的手段で簡便に安価に調製・供
給することができる。
According to the present invention, for example, a solid product of zinc borofluoride hexahydrate, which is frequently used as an epoxy resin hardener for coating a resin on the inner surface of a can, can be easily and inexpensively prepared and supplied by stoichiometric means.

【図面の簡単な説明】[Brief description of the drawings]

【図1】養生時間とエチルアルコール不溶解分のとの関
係を示すグラフである。
FIG. 1 is a graph showing the relationship between curing time and ethyl alcohol insoluble matter.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 矢崎 洋史 大阪府泉大津市臨海町1丁目41番ステラケ ミファ株式会社内 Fターム(参考) 4G047 AA05 AB02 AC03 AD03 4J036 AA01 GA20  ────────────────────────────────────────────────── ─── Continuing from the front page (72) Inventor Hiroshi Yazaki 1-41 Rinkai-cho, Izumiotsu-shi, Osaka

Claims (9)

【特許請求の範囲】[Claims] 【請求項1】 亜鉛または亜鉛化合物とホウフッ化物と
を反応させることによりホウフッ化亜鉛6水塩を製造す
るホウフッ化亜鉛6水塩の製造方法において、反応に関
与する水の総量がホウフッ化亜鉛が水和して6水和物に
なる量に等しいかわずかに少なくなるようにして反応さ
せることを特徴とする高純度ホウフッ化亜鉛6水塩の製
造方法。
1. A method for producing zinc borofluoride hexahydrate by reacting zinc or a zinc compound with a borofluoride, wherein the total amount of water involved in the reaction is such that zinc borofluoride is produced. A method for producing high-purity zinc borofluoride hexahydrate, wherein the reaction is carried out so as to be equal to or slightly less than the amount of hydrated hexahydrate.
【請求項2】 前記亜鉛化合物がフッ化亜鉛4水塩およ
び/または無水フッ化亜鉛であることを特徴とする請求
項1記載の高純度ホウフッ化亜鉛6水塩の製造方法。
2. The method for producing high-purity zinc borofluoride hexahydrate according to claim 1, wherein the zinc compound is zinc fluoride tetrahydrate and / or anhydrous zinc fluoride.
【請求項3】 無水フッ化亜鉛はフッ化亜鉛4水塩を脱
水して得られる無水フッ化亜鉛であることを特徴とする
請求項1または2に記載の高純度ホウフッ化亜鉛6水塩
の製造方法。
3. The high-purity zinc borofluoride hexahydrate according to claim 1, wherein the anhydrous zinc fluoride is anhydrous zinc fluoride obtained by dehydrating zinc fluoride tetrahydrate. Production method.
【請求項4】 前記ホウフッ化化合物は三フッ化ホウ素
および/または三フッ化ホウ素錯塩であることを特徴と
する請求項1ないし3のいずれか1項に記載の高純度ホ
ウフッ化亜鉛6水塩の製造方法。
4. The high-purity zinc borofluoride hexahydrate according to claim 1, wherein the borofluoride compound is boron trifluoride and / or a boron trifluoride complex salt. Manufacturing method.
【請求項5】 前記三フッ化ホウ素水錯塩はBF3・H2
O,2BF3・3H2O,BF3・2H2Oであることを請
求項4記載の高純度ホウフッ化亜鉛6水塩の製造方法。
5. The boron trifluoride water complex salt is BF 3 .H 2
O, 2BF 3 · 3H 2 O , the method of producing a high-purity zinc borofluoride hexahydrate according to claim 4, wherein it is a BF 3 · 2H 2 O.
【請求項6】 反応系に存在する水の総量がホウフッ化
亜鉛1モルに対し、5.5モル以上6.25モル未満で
あることを特徴とする請求項1ないし5のいずれか1項
記載の高純度ホウフッ化亜鉛6水塩の製造方法。
6. The method according to claim 1, wherein the total amount of water present in the reaction system is at least 5.5 mol and less than 6.25 mol per 1 mol of zinc borofluoride. A method for producing high-purity zinc borofluoride hexahydrate according to claim 1.
【請求項7】 反応系に存在する水の総量がホウフッ化
亜鉛1モルに対し、5.75モル以上6モル以下である
ことを特徴とする請求項6に記載の高純度ホウフッ化亜
鉛6水塩の製造方法。
7. The high-purity zinc borofluoride 6 water according to claim 6, wherein the total amount of water present in the reaction system is 5.75 mol or more and 6 mol or less per 1 mol of zinc borofluoride. Method for producing salt.
【請求項8】 請求項1〜7のいずれか1項に記載の方
法で得たホウフッ化亜鉛6水塩をさらに、60℃以下で
3日以上保管熟成してエチルアルコール不溶解分0.5
%以下の高純度ホウフッ化亜鉛6塩を得ることを特徴と
するホウフッ化亜鉛6水塩の製造方法。
8. The zinc borofluoride hexahydrate obtained by the method according to any one of claims 1 to 7, which is further stored and aged at 60 ° C. or lower for 3 days or more to obtain an ethyl alcohol insoluble content of 0.5%.
% Or less of high purity zinc borofluoride hexahydrate.
【請求項9】 常温で保管熟成することを特徴とする請
求項8記載の高純度ホウフッ化亜鉛6水塩の製造方法。
9. The method for producing high-purity zinc borofluoride hexahydrate according to claim 8, wherein the storage aging is performed at room temperature.
JP35083999A 1999-12-09 1999-12-09 Method for producing high purity zinc borofluoride hexahydrate Expired - Fee Related JP4559570B2 (en)

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KR1020000074892A KR100673874B1 (en) 1999-12-09 2000-12-09 The method of preparing high purity ZnBF42 6H2O

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JPS6133791A (en) * 1984-07-24 1986-02-17 Hitachi Ltd Flux for brazing
JPS61151024A (en) * 1984-12-25 1986-07-09 Hashimoto Kasei Kogyo Kk Production of high purity lithium fluoride complex salt
JPS61151023A (en) * 1984-12-25 1986-07-09 Hashimoto Kasei Kogyo Kk Purification of lithium fluoride complex salt
JPH0781903A (en) * 1993-09-20 1995-03-28 Kanto Denka Kogyo Co Ltd Production of inorganic fluoride being in gaseous state at ordinary temperature

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB226491A (en) * 1923-12-20 1925-11-02 Albert Fritz Meyerhofer Process of producing metal compounds
JPS6133791A (en) * 1984-07-24 1986-02-17 Hitachi Ltd Flux for brazing
JPS61151024A (en) * 1984-12-25 1986-07-09 Hashimoto Kasei Kogyo Kk Production of high purity lithium fluoride complex salt
JPS61151023A (en) * 1984-12-25 1986-07-09 Hashimoto Kasei Kogyo Kk Purification of lithium fluoride complex salt
JPH0781903A (en) * 1993-09-20 1995-03-28 Kanto Denka Kogyo Co Ltd Production of inorganic fluoride being in gaseous state at ordinary temperature

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