JP2733067B2 - Method for producing inorganic halogen compound powder - Google Patents

Method for producing inorganic halogen compound powder

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Publication number
JP2733067B2
JP2733067B2 JP22443888A JP22443888A JP2733067B2 JP 2733067 B2 JP2733067 B2 JP 2733067B2 JP 22443888 A JP22443888 A JP 22443888A JP 22443888 A JP22443888 A JP 22443888A JP 2733067 B2 JP2733067 B2 JP 2733067B2
Authority
JP
Japan
Prior art keywords
halogen compound
inorganic halogen
solution
bromide
vacuum
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.)
Expired - Fee Related
Application number
JP22443888A
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Japanese (ja)
Other versions
JPH0274501A (en
Inventor
純郎 天野
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MANATSUKU KK
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MANATSUKU KK
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Priority to JP22443888A priority Critical patent/JP2733067B2/en
Publication of JPH0274501A publication Critical patent/JPH0274501A/en
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Publication of JP2733067B2 publication Critical patent/JP2733067B2/en
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  • Inorganic Compounds Of Heavy Metals (AREA)
  • Compounds Of Alkaline-Earth Elements, Aluminum Or Rare-Earth Metals (AREA)

Description

【発明の詳細な説明】 [発明の目的] (産業上の利用分野) 本発明は、触媒、試薬、写真材料、電池材料などの用
途において工業的に有用な無機ハロゲン化合物粉末の製
造方法に関する。
DETAILED DESCRIPTION OF THE INVENTION [Object of the Invention] (Field of Industrial Application) The present invention relates to a method for producing an inorganic halogen compound powder which is industrially useful in applications such as catalysts, reagents, photographic materials, and battery materials.

(従来の技術) 従来、無機化合物粉末の一般的な製造方法としては、
無機ハロゲン化合物の精製液から、各種の方法により溶
媒を適度に蒸発せしめて再結晶を行い、分離した固形物
を乾燥する方法が適用されている(以下、この方法を
「再結晶法」という)。
(Prior art) Conventionally, as a general production method of inorganic compound powder,
From a purified solution of an inorganic halogen compound, a method is employed in which a solvent is appropriately evaporated by various methods to recrystallize, and a separated solid is dried (hereinafter, this method is referred to as "recrystallization method"). .

しかし、再結晶法の場合、無機ハロゲン化合物のなか
でも特に溶媒に対する溶解度が大きい塩類を製造する場
合には生産効率が極めて悪く、さらに固形分離工程で排
出される母液の保存や処理等が煩雑となり、時として重
金属塩類の場合には汚染源などになるという問題もあ
る。
However, in the case of the recrystallization method, the production efficiency is extremely low particularly when producing salts having high solubility in a solvent among inorganic halogen compounds, and furthermore, the storage and treatment of the mother liquor discharged in the solid separation step become complicated. However, there is also a problem that heavy metal salts sometimes become a source of pollution.

この再結晶法の問題点を解決する方法として、特公昭
52−38272号公報に記載の真空濃縮装置を用いる方法が
ある。この方法によれば無機ハロゲン化合物を含有する
溶液から1回の操作で目的とする無機ハロゲン化合物の
全量を固形物として得ることができることから、無機ハ
ロゲン化合物の効率的な製造が可能になる。さらには前
記溶液から単一の装置により無機ハロゲン化合物の固形
物を得ることができ、固形分離工程が不要になることか
ら再結晶法におけるような母液の発生がないために環境
保全面においても優れている方法である。
To solve the problem of this recrystallization method,
There is a method using a vacuum concentrator described in JP-A-52-38272. According to this method, the entire amount of the target inorganic halogen compound can be obtained as a solid from the solution containing the inorganic halogen compound in one operation, so that the inorganic halogen compound can be efficiently produced. Furthermore, a solid substance of the inorganic halogen compound can be obtained from the solution by a single apparatus, and a solid separation step is not required, so that there is no generation of a mother liquor as in the recrystallization method, and thus, the method is excellent in environmental protection. That's the way you are.

しかし、この方法は、目的とする製品によってはその
品質面で不十分な点があり、さらに検討の余地がある。
However, this method has an insufficient quality depending on a target product, and there is room for further study.

(発明が解決しようとする課題) 本願発明は上記の問題点を解決し、効率よく、残存溶
媒量が非常に少なく、高品質の無機ハロゲン化合物粉末
を得ることができる、無機ハロゲン化合物粉末の製造方
法を提供することを目的とする。
(Problems to be Solved by the Invention) The present invention solves the above-mentioned problems and efficiently produces an inorganic halogen compound powder capable of obtaining a high-quality inorganic halogen compound powder with a very small amount of residual solvent. The aim is to provide a method.

[発明の構成] (課題を解決しようとする手段および作用) 本願発明者らは、前記特公昭52−38272号公報に記載
の真空濃縮装置に着目し、無機ハロゲン化合物溶液の濃
縮乾燥方法について検討を行った。その結果、前記装置
を用いて単に無機ハロゲン化合物の溶液の濃縮乾燥を行
った場合には、得られた無機ハロゲン化合物を水もしく
はアルコール等の溶媒に溶解して行う溶状の品質試験に
おいて「濁り」が著しいことから工業用材料として不適
であることが判明した。そこでさらに検討を重ねた結
果、無機ハロゲン化合物の溶液のpHを調整することによ
り、「濁り」のない高品質の無機ハロゲン化合物粉末を
効率よく製造し得ることを見出し、本発明を完成するに
至った。
[Constitution of the Invention] (Means for Solving the Problems and Action) The inventors of the present application focused on the vacuum concentrator described in JP-B-52-38272, and studied a method for concentrating and drying an inorganic halogen compound solution. Was done. As a result, when the concentration of the solution of the inorganic halogen compound is simply dried using the above-described apparatus, "turbidity" is generated in a solution quality test performed by dissolving the obtained inorganic halogen compound in a solvent such as water or alcohol. Was remarkable, it was found to be unsuitable as an industrial material. Therefore, as a result of further study, they found that by adjusting the pH of the solution of the inorganic halogen compound, it was possible to efficiently produce a high-quality inorganic halogen compound powder without "turbidity", and completed the present invention. Was.

本願発明の無機ハロゲン化合物粉末の製造方法は、pH
4以下に調整した無機ハロゲン化合物溶液を、長管状加
熱器、真空蒸発機および前記真空蒸発機に連結管を介し
て連結された受器、さらに前記受器に結合された真空ポ
ンプを具備してなる真空濃縮装置により濃縮乾燥するこ
とを特徴とする。
The production method of the inorganic halogen compound powder of the present invention is pH
The inorganic halogenated compound solution adjusted to 4 or less, a long tubular heater, a vacuum evaporator and a receiver connected to the vacuum evaporator via a connecting pipe, and further comprising a vacuum pump connected to the receiver. It is characterized by being concentrated and dried by a vacuum concentrator.

本発明で用いる無機ハロゲン化合物溶液は、公知の方
法で製造された無機ハロゲン化合物溶液を、必要に応じ
て過、活性炭吸着処理などの方法により適宜精製した
ものを用いることができる。さらには予備的に溶媒を蒸
発させたもの、またはさらに溶媒を蒸発させて結晶が一
部析出したスラリー状のものも用いることができる。本
発明でいう溶液は、水を初めとする無機ハロゲン化合物
を溶解できる溶媒の溶液である。
As the inorganic halogen compound solution used in the present invention, a solution obtained by appropriately purifying an inorganic halogen compound solution produced by a known method by a method such as excess or activated carbon adsorption treatment as necessary can be used. Further, a solvent in which the solvent is preliminarily evaporated, or a slurry in which crystals are partially precipitated by further evaporating the solvent can be used. The solution referred to in the present invention is a solution of a solvent capable of dissolving an inorganic halogen compound such as water.

無機ハロゲン化合物としては、臭化亜鉛、臭化第二
銅、臭化ルビジウム、臭化カルシウム、沃化カリウム、
沃化ナトリウムなどを例示することができる。無機ハロ
ゲン化合物としてはこれらのなかでも臭化亜鉛、臭化第
二銅または臭化ルビジウムであることが本発明の製造方
法を適用する場合に濃縮効率をより高め、得られた製品
の品質がよいことから好ましく、同様の理由で臭化亜鉛
であることがさらに好ましい。
As inorganic halogen compounds, zinc bromide, cupric bromide, rubidium bromide, calcium bromide, potassium iodide,
Examples thereof include sodium iodide. Among these inorganic zinc compounds, zinc bromide, cupric bromide or rubidium bromide among these are more concentrated when applying the production method of the present invention, and the quality of the obtained product is good. Therefore, zinc bromide is more preferable for the same reason.

無機ハロゲン化合物溶液のpHは4以下であることが必
要であり、好ましくは3以下である。pHが4を超えると
得られた製品の水溶液またはアルコール溶液が濁りを生
じ、製品として不適となる。
The pH of the inorganic halogen compound solution needs to be 4 or less, and preferably 3 or less. If the pH exceeds 4, the aqueous solution or alcohol solution of the obtained product becomes turbid and becomes unsuitable as a product.

pHは4以下であれば下限は特に制限されるものではな
いが、収率を考慮すると用いる酸の量が無機ハロゲン化
合物溶液中において5重量%量以下になることが好まし
く、3重量%量以下になることがさらに好ましい。
Although the lower limit is not particularly limited as long as the pH is 4 or less, the amount of the acid used is preferably 5% by weight or less, preferably 3% by weight or less in the inorganic halogen compound solution in consideration of the yield. More preferably,

pHの調整に用いる酸としては臭化水素酸、塩酸または
沃化水素酸などの鉱酸を例示することができる。
Examples of the acid used for adjusting the pH include mineral acids such as hydrobromic acid, hydrochloric acid and hydroiodic acid.

本発明で用いる真空濃縮装置は、長管状加熱器、真空
蒸発機および前記真空蒸発機に連結管を介して連結され
た受器、さらに前記受器に結合された真空ポンプを具備
してなるものである。
The vacuum concentrator used in the present invention comprises a long tubular heater, a vacuum evaporator, a receiver connected to the vacuum evaporator via a connecting pipe, and a vacuum pump connected to the receiver. It is.

この真空濃縮装置としては、具体的には特公昭52−38
272号公報に記載の真空濃縮装置を用いることができ
る。図に前記公報記載の装置の概略を示す。図中1は無
機ハロゲン化合物溶液の貯留タンク、2は前記溶液、3
は前記溶液の供給ポンプ、4は長尺式加熱器、5は真空
蒸発器、6は中間弁、7は連結管、8は受器、9は取り
出し弁、10〜12は弁、13はパイプ(真空系)および14は
補助真空ポンプである。
As this vacuum concentrator, specifically, JP-B-52-38
No. 272, a vacuum concentrating device can be used. The figure shows an outline of the device described in the above publication. In the figure, 1 is a storage tank of an inorganic halogen compound solution, 2 is the solution, 3
Is a supply pump of the solution, 4 is a long heater, 5 is a vacuum evaporator, 6 is an intermediate valve, 7 is a connecting pipe, 8 is a receiver, 9 is a take-out valve, 10 to 12 are valves, and 13 is a pipe. (Vacuum system) and 14 are auxiliary vacuum pumps.

かかる真空濃縮装置を構成する材質は特に制限される
ものでははいが、無機ハロゲン化合物溶液と直接接触す
る部位には特に高い耐食性の材質を選択することが好ま
しい。高耐食性の材質としては、ガラス、セラミック
ス、フッ素樹脂系などの合成樹脂、高耐食性の金属およ
びこれらの材質で表面加工したものを例示することがで
きる。
Although the material constituting such a vacuum concentrator is not particularly limited, it is preferable to select a material having a particularly high corrosion resistance at a portion which comes into direct contact with the inorganic halogen compound solution. Examples of the material having high corrosion resistance include glass, ceramics, synthetic resins such as fluororesins, metals having high corrosion resistance, and materials surface-treated with these materials.

本発明で用いる真空濃縮装置の大きさ、使用条件など
は目的とする生産能力や、無機ハロゲン化合物溶液の溶
媒の種類などにより適宜決定することができる。
The size, use conditions, and the like of the vacuum concentrator used in the present invention can be appropriately determined depending on the intended production capacity, the type of the solvent of the inorganic halogen compound solution, and the like.

無機ハロゲン化合物粉末の製造は、例えば次のように
して行うことができる。
The production of the inorganic halogen compound powder can be performed, for example, as follows.

まず、無機ハロゲン化合物溶液2を供給ポンプ3によ
り一定流量で長尺式加熱器4へ送り、ここで予備加熱す
る。この際の加熱温度は特に制限されるものではない
が、溶液の沸点以上にまで加熱することが好ましい。次
に予備加熱された前記溶液を真空蒸発器5に送り水分を
蒸発させる。蒸発させた溶媒はパイプ13から除去し、無
機ハロゲン化合物粉末は受器8に蓄積される。なお、こ
の一連の操作を乾燥させた空気や窒素などの雰囲気中で
行うことにより、さらに一層濃縮効率を高めることがで
きることから好ましい。
First, the inorganic halogen compound solution 2 is sent to the long heater 4 at a constant flow rate by the supply pump 3, where it is preheated. The heating temperature at this time is not particularly limited, but it is preferable to heat the solution to the boiling point or higher. Next, the preheated solution is sent to a vacuum evaporator 5 to evaporate water. The evaporated solvent is removed from the pipe 13, and the inorganic halogen compound powder is accumulated in the receiver 8. It is preferable to perform this series of operations in an atmosphere of dried air, nitrogen, or the like, because the concentration efficiency can be further increased.

本発明の製造方法により、水などの溶媒に溶解した場
合の溶状が澄明であり、かつ残存溶媒量が著しく少ない
無機ハロゲン化合物を得ることができる機構の詳細は不
明であるが、無機ハロゲン化合物溶液中にやや過剰に存
在する酸が脱水を進行させるとともに、製品の品質安定
化に寄与するものと推定される。
According to the production method of the present invention, the details of the mechanism capable of obtaining an inorganic halogen compound in which the solution when dissolved in a solvent such as water is clear and the amount of the residual solvent is extremely small are unknown, but the inorganic halogen compound solution It is presumed that the acid present in the medium in excess slightly promotes dehydration and contributes to the stabilization of product quality.

(実施例) 以下、具体的に実施例を掲げて本発明を説明するが、
本発明はこれらの実施例によって何ら限定されるもので
はない。なお、以下において「%」は「重量%」を表
す。また、pHの測定、残存溶媒量および溶状試験は次の
方法によった。
(Examples) Hereinafter, the present invention will be described specifically with reference to Examples.
The present invention is not limited by these examples. In the following, “%” represents “% by weight”. In addition, the measurement of pH, the amount of the remaining solvent and the dissolution test were performed by the following methods.

pH測定 pH測定は、サンプル50mlを容量50mlのガラス製ビーカ
ーにとり、JIS Z 8802(pH測定方法)により測定し
た。
pH Measurement The pH was measured by placing a 50 ml sample in a 50 ml glass beaker and measuring according to JIS Z 8802 (pH measurement method).

残存溶媒量 残存溶媒量の測定はJIS K 0 0 6 8(化学
製品の水分試験方法)の方法に準拠して行った。なお測
定に際しては、サンプル1gをメスフラスコにとり、メチ
ルアルコールを加えて100mlとし、均一にした後、この
溶液2mlを用いて試験を行い残存溶媒量を求め、同時に
メチルアルコール2mlを用いてブランク試験を行い溶媒
量を求め、両者の差から製品中の残存溶媒量を求めた。
Residual solvent amount The residual solvent amount was measured in accordance with the method of JIS K068 (method for testing moisture of chemical products). When measuring, take 1 g of the sample in a volumetric flask, add methyl alcohol to make 100 ml, homogenize, then test using 2 ml of this solution to determine the amount of residual solvent, and simultaneously perform a blank test using 2 ml of methyl alcohol. The amount of the solvent was determined, and the amount of the residual solvent in the product was determined from the difference between the two.

溶状試験 溶状試験は、溶媒として水およびエタノールを用いて
両者に対する溶状試験をJIS K8001(試薬試験方法通
則)5−2溶状、の方法に準拠して行った。なお測定に
際しては、サンプル5gを用い、溶媒を加えて50mlとして
サンプルが溶解た後行った。なお、評価方法は次のとお
りである。
Dissolution test The dissolution test was performed according to JIS K8001 (General rules for reagent test method) 5-2 dissolution test using water and ethanol as a solvent. Note that the measurement was performed after dissolving the sample using a 5 g sample to make 50 ml by adding a solvent. The evaluation method is as follows.

◎:澄明 ○:ほとんど澄明 △:わずかに澄明 ×:微濁 ××:混濁 実施例1 まず、臭化亜鉛、臭化第二銅および臭化ルビジウムの
各精製水溶液を次の方法により調製した。すなわち、酸
合亜鉛、酸化第二銅および一酸化ルビジウムの各々と、
臭化水素酸水溶液(48%)とを所定のモル引で反応さ
せ、その後、pH4〜6とした反応後の溶液を自然過
(紙:東洋紙No.5Cを使用)した。次に、これらの
精製水溶液の無機ハロゲン化合物濃度をいずれも50重量
%濃度に調整し、さらにそのpHをそれぞれ第1表に示す
ように調整した。得られた各水溶液1について真空濃
縮装置により濃縮乾燥を行い、無機ハロゲン化合物粉末
を得た。
:: clear ○: almost clear △: slightly clear ×: slightly turbid XX: turbid Example 1 First, each purified aqueous solution of zinc bromide, cupric bromide and rubidium bromide was prepared by the following method. That is, each of zinc oxide, cupric oxide and rubidium monoxide,
The resulting solution was allowed to react with a hydrobromic acid aqueous solution (48%) at a predetermined molar ratio, and the solution after the reaction was adjusted to pH 4 to 6, and the solution was naturally filtered (paper: using Toyo Paper No. 5C). Next, the concentration of the inorganic halogen compound in each of these purified aqueous solutions was adjusted to a concentration of 50% by weight, and the pH thereof was further adjusted as shown in Table 1. Each obtained aqueous solution 1 was concentrated and dried by a vacuum concentrator to obtain an inorganic halogen compound powder.

真空乾燥機として特公昭52−38272号公報に記載の装
置を用いた。
The apparatus described in JP-B-52-38272 was used as a vacuum dryer.

濃縮乾燥は、前記各水溶液を供給ポンプ8により連続
的に0.11/分の割合で供給しながら行った。なお、各
溶液を供給する長尺式加熱器4の温度は180℃、受器8
のジャケットの加熱温度は120℃および受器8における
減圧度は10mmHgに設定した。また、濃縮乾燥した製品
は、各水溶液を送液終了後にさらに10分間受器中での乾
燥を継続したのちに取り出した。濃縮乾燥に要した時間
は20分間であった。
The concentration and drying were performed while continuously supplying the aqueous solutions by the supply pump 8 at a rate of 0.11 / min. The temperature of the long heater 4 for supplying each solution is 180 ° C.
The heating temperature of the jacket was set at 120 ° C., and the degree of reduced pressure in the receiver 8 was set at 10 mmHg. The concentrated and dried product was taken out after continuing the drying in the receiver for another 10 minutes after the completion of sending each aqueous solution. The time required for concentration and drying was 20 minutes.

このようにして得られた各無機ハロゲン化合物粉末の
残存溶媒量等を測定した。結果を第1表に示す。
The residual solvent amount and the like of each of the inorganic halogen compound powders thus obtained were measured. The results are shown in Table 1.

比較例1 実施例1の臭化亜鉛、臭化第二銅および臭化ルビジウ
ムの各精製溶液のpHを第1表に示すように調整したほか
は実施例1と同様にして各無機ハロゲン化合物粉末を得
た。この粉末の品質の測定結果を第1表に示す。
Comparative Example 1 Each inorganic halogen compound powder was prepared in the same manner as in Example 1 except that the pH of each purified solution of zinc bromide, cupric bromide and rubidium bromide in Example 1 was adjusted as shown in Table 1. I got Table 1 shows the measurement results of the quality of the powder.

比較例2 再結晶法による無機ハロゲン化合物粉末の製造を行っ
た。
Comparative Example 2 An inorganic halogen compound powder was produced by a recrystallization method.

まず、実施例1で用いた臭化亜鉛、臭化第二銅および
臭化リビジウムの水溶液のうちpHを第1表に示すように
調整したもの各500mlを擦り付きなす形フラスコに入れ
た。次に、このなす形フラスコを減圧エバポレーターに
取り付け、減圧度を5mmHgとした後、なす形フラスコを
回転させながら加熱した。加熱はオイルバスを用い、な
す形フラスコ内の溶液が突沸しないように徐々に昇温し
て70〜140℃で水分を蒸発させた。最終的に溶媒をほと
んど認めなくなった段階でなす形フラスコ内のスラリー
状の溶液を減圧過により固液分離した。その後得られ
た固形物を減圧度5mmHg、温度120℃で1時間または2時
間乾燥させて、各無機ハロゲン化合物の粉末を得た。
First, 500 ml each of the aqueous solutions of zinc bromide, cupric bromide and lividium bromide used in Example 1 whose pH was adjusted as shown in Table 1 were placed in a rubbed flask. Next, the eggplant-shaped flask was attached to a reduced-pressure evaporator, the degree of reduced pressure was set to 5 mmHg, and the eggplant-shaped flask was heated while rotating. Heating was performed using an oil bath, and the temperature was gradually raised so that the solution in the eggplant-shaped flask did not boil off, and water was evaporated at 70 to 140 ° C. Finally, at the stage when almost no solvent was recognized, the slurry-like solution in the formed flask was subjected to solid-liquid separation by applying reduced pressure. Thereafter, the obtained solid was dried at a reduced pressure of 5 mmHg and a temperature of 120 ° C. for 1 hour or 2 hours to obtain a powder of each inorganic halogen compound.

各粉末についての品質の測定結果を第1表に示す。 Table 1 shows the quality measurement results for each powder.

実施例2 臭化カルシウム、臭化コバルト、沃化ナトリウムおよ
び沃化カリウムの各水溶液のpHを第2表に示すように調
整したものを用い、実施例1と同様にして無機ハロゲン
化合物粉末を得た。
Example 2 Inorganic halogen compound powders were obtained in the same manner as in Example 1 by using aqueous solutions of calcium bromide, cobalt bromide, sodium iodide and potassium iodide, each of which had the pH adjusted as shown in Table 2. Was.

この粉末についての品質の測定結果を第2表に示す。 Table 2 shows the quality measurement results for this powder.

比較例3 実施例2の臭化カルシウム、臭化コバルト、沃化ナト
リウムおよび沃化カリウムの各水溶液のpHを第2表に示
すように調整したものを用い、実施例2と同じにして無
機ハロゲン化合物粉末を得た。
Comparative Example 3 An inorganic halogen solution was prepared in the same manner as in Example 2 except that the pH of each aqueous solution of calcium bromide, cobalt bromide, sodium iodide and potassium iodide was adjusted as shown in Table 2. Compound powder was obtained.

この粉末についての品質の測定結果を第2表に示す。 Table 2 shows the quality measurement results for this powder.

[発明の効果] 本発明の製造方法によれば効率よく、水等の溶媒に対
する溶状が良好であり、かつ残存溶媒量が非常に少な
い、高品質の無機ハロゲン化合物粉末を得ることができ
る。
[Effects of the Invention] According to the production method of the present invention, it is possible to efficiently obtain a high-quality inorganic halogen compound powder having a good solubility in a solvent such as water and a very small amount of a residual solvent.

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

図は真空濃縮装置の概略図である。 The figure is a schematic diagram of a vacuum concentrator.

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 C01F 11/34 C01F 11/34 C01G 3/04 C01G 3/04 9/04 9/04 51/08 51/08 ──────────────────────────────────────────────────続 き Continued on the front page (51) Int.Cl. 6 Identification code Agency reference number FI Technical indication location C01F 11/34 C01F 11/34 C01G 3/04 C01G 3/04 9/04 9/04 51/08 51/08

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】pH4以下に調整した無機ハロゲン化合物溶
液を、長管状加熱器、真空蒸発機および前記真空蒸発機
に連結管を介して連結された受器、さらに前記受器に結
合された真空ポンプを具備してなる真空濃縮装置により
濃縮乾燥することを特徴とする無機ハロゲン化合物粉末
の製造方法。
1. An inorganic halogenated compound solution adjusted to pH 4 or less is supplied to a long tube heater, a vacuum evaporator, a receiver connected to the vacuum evaporator via a connecting pipe, and a vacuum connected to the receiver. A method for producing an inorganic halogen compound powder, comprising concentrating and drying with a vacuum concentrator equipped with a pump.
【請求項2】無機ハロゲン化合物が臭化亜鉛、臭化第二
銅および臭化ルビジウムから選ばれる1の化合物である
請求項1記載の無機ハロゲン化合物粉末の製造方法。
2. The method for producing an inorganic halogen compound powder according to claim 1, wherein the inorganic halogen compound is one compound selected from zinc bromide, cupric bromide and rubidium bromide.
JP22443888A 1988-09-09 1988-09-09 Method for producing inorganic halogen compound powder Expired - Fee Related JP2733067B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP22443888A JP2733067B2 (en) 1988-09-09 1988-09-09 Method for producing inorganic halogen compound powder

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP22443888A JP2733067B2 (en) 1988-09-09 1988-09-09 Method for producing inorganic halogen compound powder

Publications (2)

Publication Number Publication Date
JPH0274501A JPH0274501A (en) 1990-03-14
JP2733067B2 true JP2733067B2 (en) 1998-03-30

Family

ID=16813773

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Country Status (1)

Country Link
JP (1) JP2733067B2 (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005047764A (en) * 2003-07-30 2005-02-24 Nippo Kagaku Kk Manufacturing method of particulate metal iodide
JP5260019B2 (en) * 2007-10-11 2013-08-14 合同資源産業株式会社 Method for producing granular sodium iodide
KR101262362B1 (en) * 2012-01-31 2013-05-08 (주) 골프존 Virtual golf simulation apparatus for supporting generation of virtual putting green and method therefor
CN103265423B (en) * 2013-05-31 2015-05-27 重庆龙瑞化工有限公司 Resourceful treatment method for industrial wastes containing acetic anhydride, zinc bromide and the like
JP6173931B2 (en) * 2014-01-23 2017-08-02 日宝化学株式会社 Method for producing alkali metal iodide or alkaline earth metal iodide

Also Published As

Publication number Publication date
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