JPH02144101A - Distillatory refining method - Google Patents

Distillatory refining method

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Publication number
JPH02144101A
JPH02144101A JP30001188A JP30001188A JPH02144101A JP H02144101 A JPH02144101 A JP H02144101A JP 30001188 A JP30001188 A JP 30001188A JP 30001188 A JP30001188 A JP 30001188A JP H02144101 A JPH02144101 A JP H02144101A
Authority
JP
Japan
Prior art keywords
container
solution
vessel
closed container
acid
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
JP30001188A
Other languages
Japanese (ja)
Other versions
JP2793208B2 (en
Inventor
Hideki Matsunaga
秀樹 松永
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.)
Toshiba Corp
Original Assignee
Toshiba 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 Toshiba Corp filed Critical Toshiba Corp
Priority to JP30001188A priority Critical patent/JP2793208B2/en
Publication of JPH02144101A publication Critical patent/JPH02144101A/en
Application granted granted Critical
Publication of JP2793208B2 publication Critical patent/JP2793208B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)

Abstract

PURPOSE:To obtain a high-purity reagent free of metallic impurities such as nitric acid, hydrochloric acid, and hydrofluoric acid by refining after previously adding one or both of sulfuric acid and phosphoric acid to a soln. material. CONSTITUTION:The injection part 6 and discharge part 7 for a soln. material 2 are connected to the side wall of a closed vessel 1 contg. the soln. material 2 in the vicinity of its bottom. A means 3 for heating the material 2 in the vessel 1 and a cooling vessel 8 with the lower part tapered are also furnished. In addition, a collecting duct 13 with the upper end arranged close to the bottom of the cooling vessel 8 and the lower end piercing the bottom of the vessel 1 and extending downward and a container 15 for collecting the liq. distillate into which the lower end of the duct 13 is inserted are provided. Filter plates 21a and 21b are arranged in the vessel 1 positioned above the liq. surface of the material 2, and shielding plates 22 and 23 are provided respectively at the lower part of the cooling vessel 8, the inner surface part of the vessel 1 positioned at the liq. surface of the material 2, and the outer surface part of the duct 13. One or both of sulfuric acid and phosphoric acid are previously added to the material 2.

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、酸等の溶液状の試薬を精製するための蒸溜精
製方法に関する。
Detailed Description of the Invention [Object of the Invention] (Industrial Application Field) The present invention relates to a distillation purification method for purifying a solution-like reagent such as an acid.

(従来の技術) 電子工業、原子カニ業或いは各種素材工業の進歩に伴い
材料の高純度化の要求が高まっている。
(Prior Art) With the progress of the electronics industry, the atomic industry, and various materials industries, the demand for highly purified materials is increasing.

また、材料評価技術においても超微量成分分析技術の向
上が望まれている。最近の分析装置の急速な発達により
湿式化学分析において超微量成分の分析が相当可能にな
ってきたが、分析に使用する試薬から分析目的成分が混
入する、いわゆるコンタミネーションの問題により分析
のブランク値が高くなり、必ずしも超@量成分を高精度
で分析できない場合があった。現在、電子工業用又は有
害金属測定用の高純度試薬が市販されているが、超微量
成分分析に用いるために充分な純度といえず、使用目的
に応じて更に精製する必要があった。
Furthermore, in material evaluation technology, there is a desire to improve ultratrace component analysis technology. The recent rapid development of analytical equipment has made it possible to analyze ultratrace components in wet chemical analysis, but due to the problem of so-called contamination, in which target components are mixed in with the reagents used for analysis, blank values for analysis are In some cases, it was not always possible to analyze ultra-quantity components with high accuracy. Currently, high-purity reagents for use in the electronics industry or for measuring hazardous metals are commercially available, but they are not of sufficient purity for use in ultratrace component analysis, and require further purification depending on the intended use.

このようなことから、従来より高純度試薬を調製するた
めの蒸溜装置(特開昭80−183002号公報)が知
られている。この蒸溜装置は、仏性すべき溶液物質が収
容された仏性槽と、この仏性槽の底部に配設されたヒー
タと、前記仏性槽の上部に配設された下部が傾斜した形
状の冷却槽と、前記仏性槽の上部から底部を貫通して挿
入され、前記冷却槽で凝縮、滴下された仏性液を捕集ビ
ンに導くための導管とを具備した構造になっている。し
かしながら、かかる蒸溜装置では仏性槽内に収容した溶
液物質をヒータで加熱沸騰させる際、金属不純物を含ん
だミストが発生すると共に、該ミストが冷却槽に付着し
て溶液物質の蒸気の凝縮液と共に導管を通して捕集ビン
に導入されるため、高純度の仏性液を精製できない問題
があった。
For this reason, a distillation apparatus (Japanese Unexamined Patent Application Publication No. 80-183002) for preparing high-purity reagents has been known. This distillation apparatus includes a Buddhist tank containing a liquid substance to be made into Buddha, a heater disposed at the bottom of the Buddha tank, and a cooling tank with a sloped bottom disposed at the top of the Buddha tank. , and a conduit inserted through the top and bottom of the bath to guide the liquid condensed and dripped in the cooling tank to a collection bottle. However, in such a distillation apparatus, when the solution material contained in the distillation tank is heated to boiling with a heater, a mist containing metal impurities is generated, and the mist also adheres to the cooling tank and together with the condensate of the vapor of the solution material. Since the liquid is introduced into the collection bottle through a conduit, there was a problem in that it was not possible to purify the liquid to a high degree of purity.

(発明が解決し、ようとする課題) 本発明は、上記従来の問題点を解決するためになされた
もので、金属不純物の混入のない高純度の試薬等を精製
し得る仏性精製方法を提供しようとするものである。
(Problems to be Solved and Attempted by the Invention) The present invention has been made in order to solve the above-mentioned conventional problems, and provides a purification method capable of purifying high-purity reagents etc. without contamination with metal impurities. This is what I am trying to do.

[発明の構成] (課題を解決するための手段) 本発明は、底部付近に溶液物質が収容された密閉容器と
、この密閉容器の側壁に連結された溶液物質の注入部及
び排出部と、前記密閉容器内の溶液物質を加熱するため
の加熱手段と、前記密閉容器の上部に挿置され下部がテ
ーバ状をなす冷却槽と、上端が前記密閉容器内の冷却槽
下部に近接(7て配置され、かつ下端を該容器底面を貫
通して下方に延出させた捕集導管と、この捕集導管の下
端が挿入される仏性液の捕集容器と、前記溶液物質の液
面上方に位置する前記密閉容器内に配置された)、イル
タ板と、前記冷却槽下部と溶液物質液面の間に位置する
前記密閉容器の内面部分及び前記捕集導管の外面部分に
設けられた遮蔽板を具備した蒸溜装置を用いて溶液物質
を仏性精製する方法において、前記溶液物質に予め硫酸
及びリン酸のうちの一方又は両者を添加することを特徴
とする仏性精製方法である。
[Structure of the Invention] (Means for Solving the Problems) The present invention provides a closed container in which a solution substance is stored near the bottom, an injection part and a discharge part for the solution substance connected to the side wall of the closed container, a heating means for heating the solution substance in the sealed container; a cooling tank inserted in the upper part of the sealed container and having a tapered lower part; a collecting conduit having a lower end extending downwardly through the bottom of the container; a collection container for liquid liquid into which the lower end of the collecting conduit is inserted; a shielding plate provided on an inner surface portion of the sealed container and an outer surface portion of the collection conduit located between the lower part of the cooling tank and the liquid surface of the solution substance; This is a method for purifying a solution substance using a distillation apparatus equipped with the above method, characterized in that one or both of sulfuric acid and phosphoric acid is added to the solution substance in advance.

上記溶液物質としては、例えば塩酸、硝酸、弗化水素酸
、水等を挙げることができる。
Examples of the solution substance include hydrochloric acid, nitric acid, hydrofluoric acid, and water.

上記溶液物質に対する硫酸及びリン酸のうちの一方又は
両者の添加割合は、溶液物質中の金属不純物を含むミス
トの発生を抑1、すする観点から、0、L重量〇〇以上
とすることが望ましい。但し、前記硫酸等の添加上限に
ついては多くし過ぎると精製された溶液物質に硫酸等が
多量混入する恐れがあるため、実用上、5重量%とする
ことが望ましい。
The ratio of addition of one or both of sulfuric acid and phosphoric acid to the above solution material should be 0.L weight or more from the viewpoint of suppressing the generation of mist containing metal impurities in the solution material. desirable. However, regarding the upper limit of addition of sulfuric acid, etc., if it is added too much, there is a risk that a large amount of sulfuric acid, etc. will be mixed into the purified solution material, so it is practically desirable to set the upper limit to 5% by weight.

なお、仏性精製に用いる上記蒸溜装置としては強磁性金
属不純物を含むミストの発生をより低減させる観点から
密閉容器内の溶液物質に磁界を与えるための磁界発生手
段を付設することが望ましい。
In addition, from the viewpoint of further reducing the generation of mist containing ferromagnetic metal impurities, it is desirable that the above-mentioned distillation apparatus used for purification be equipped with a magnetic field generating means for applying a magnetic field to the solution substance in the closed container.

(作用) 本発明によれば、溶液物質の液面上方に位置する密閉容
器内にフィルタ板を配置した蒸溜装置を用いて精製する
ことによって、密閉容器内の溶液物質を加熱、蒸気化す
る際、突沸によるミスト発生を抑制でき、かつ冷却槽下
部と溶液物質液面の間に位置する前記密閉容器の内面部
分及び前記捕集導管の外面部分に遮蔽板を夫々設けるこ
とによって、加熱手段により密閉容器内の溶液物質を加
熱、蒸気化する際、溶液物質が密閉容器内面や捕集導管
外面に沿って上昇するのを前記各遮蔽板によって防止で
き、溶液物質そのものが導管の上端からその内部に流入
するのを防止できる。(7かも、溶液物質に硫酸及びリ
ン酸のうちの一方又は両名を添加することによって、溶
液物質中のU、Th、Fe等の金属不純物イオンと反応
して高沸点の硫酸化合物もしくはリン酸化合物が生成す
るため、金属不純物の蒸発を低下でき、これら不純物を
含むミストの発生を抑制できる。
(Function) According to the present invention, when a solution substance in a closed container is heated and vaporized by purification using a distillation apparatus in which a filter plate is arranged in a closed container located above the liquid level of the solution substance. The generation of mist due to bumping can be suppressed, and by providing shielding plates on the inner surface of the sealed container and the outer surface of the collection conduit located between the lower part of the cooling tank and the liquid surface of the solution material, the heating means can be used to seal the container. When the solution substance in the container is heated and vaporized, the above-mentioned shielding plates can prevent the solution substance from rising along the inner surface of the sealed container or the outer surface of the collection conduit, and the solution substance itself can be prevented from rising inside the conduit from the upper end. It can prevent the inflow. (Option 7) By adding one or both of sulfuric acid and phosphoric acid to the solution material, it reacts with metal impurity ions such as U, Th, and Fe in the solution material to form a high boiling point sulfuric acid compound or phosphoric acid. Since the compound is generated, the evaporation of metal impurities can be reduced, and the generation of mist containing these impurities can be suppressed.

従って、溶液物質の高純度の蒸気のみを冷加槽で凝縮し
、液滴として捕集導管を通して捕集容器に導くことによ
って、金属不純物の混入が極めて少ない高純度の仏性液
を得ることかできる。
Therefore, by condensing only the high-purity vapor of the solution substance in a cooling tank and guiding it as droplets through a collection conduit to a collection container, it is possible to obtain a high-purity liquid with very little metal impurities. .

(実施例) 以下、本発明の実施例を第1図を参照して詳細に説明す
る。
(Example) Hereinafter, an example of the present invention will be described in detail with reference to FIG.

実施例】 図中の1は、底部付近に仏性精製するための溶液物質2
が収容された例えば空間体積が約1500Oct+lの
密閉容器である。この密閉容器1の底面には、前記溶液
物質2を加熱するためのヒータ3が配設されている。こ
のヒータ3の底面には、例えばポリテトラフルオロエチ
レンでコートされた直径25cm、厚さ0.5 cmで
g K Gaussの永久磁石からなる磁界発生部材4
が配設されている。こうしたヒータ3、磁界発生部材4
を底面に順次配設した密閉容器lは、支持台5上に設置
されている。
Example] 1 in the figure shows a solution material 2 for purifying Buddha nature near the bottom.
For example, it is a closed container with a space volume of about 1500 Oct+l. A heater 3 for heating the solution substance 2 is disposed on the bottom of the closed container 1. On the bottom of the heater 3, there is a magnetic field generating member 4 made of a permanent magnet coated with polytetrafluoroethylene and having a diameter of 25 cm and a thickness of 0.5 cm and a g K Gauss.
is installed. These heaters 3 and magnetic field generating members 4
A closed container l, in which the following are sequentially arranged on the bottom surface, is placed on a support stand 5.

前記密閉容器■の下部側壁には、溶液物質の注入部6が
連結され、かつ該注入部6と対向する該密閉容器1の下
部側壁には上下に折れ曲がった溶液物質の排出部7が連
結されている。
An injection part 6 for the solution substance is connected to the lower side wall of the closed container (2), and a discharge part 7 for the solution substance bent up and down is connected to the lower side wall of the closed container 1 facing the injection part 6. ing.

また、+T;を2密閉容器Iの上部には、冷却槽8が挿
置されている。この冷却槽8は、下部がテーバ状をなす
と共に上下封じられた外筒体9と、この外筒体9の上部
から挿置された内筒体10と、前記外筒体9の上部側壁
に開口された冷却水入口1.1と、前記内筒体重0の上
端に形成された冷却水出口12とから構成されている。
Further, a cooling tank 8 is inserted in the upper part of the +T;2 sealed container I. The cooling tank 8 includes an outer cylinder 9 whose lower part is tapered and sealed vertically, an inner cylinder 10 inserted from the upper part of the outer cylinder 9, and an upper side wall of the outer cylinder 9. It consists of an open cooling water inlet 1.1 and a cooling water outlet 12 formed at the upper end of the zero weight inner cylinder.

こうした冷却槽8において、冷却水人口1.1から冷却
水を導入することにより冷却水は外筒体9と内筒体lO
の間の環状空間を通って下方に移動して外筒体9を冷却
し、この後内筒体10内に流入して冷却水出口12から
排出される。
In such a cooling tank 8, by introducing cooling water from a cooling water population 1.1, the cooling water is distributed between the outer cylinder body 9 and the inner cylinder body lO.
The cooling water moves downward through the annular space between them to cool the outer cylinder body 9, after which it flows into the inner cylinder body 10 and is discharged from the cooling water outlet 12.

前記密閉容器1内には、捕集導管13がその上端を前記
冷却槽8のテーバ状下部に近接して配置され、かつ該捕
集導管13の下端は該密閉容器lの底面、ヒータ3、磁
界発生部材4及び支持台5を貫通して下方に延出されて
いる。前記冷却槽8のテーバ状下部に近接する捕集導管
13の上端には、漏斗形状の捕集部14が形成されてい
る。前記捕集導管13の下端は、捕集容器15の口部に
挿入されている。
Inside the hermetic container 1, a collection conduit 13 is arranged with its upper end close to the tapered lower part of the cooling tank 8, and the lower end of the collection conduit 13 is connected to the bottom surface of the hermetic container l, the heater 3, It passes through the magnetic field generating member 4 and the support base 5 and extends downward. A funnel-shaped collection portion 14 is formed at the upper end of the collection conduit 13 close to the tapered lower portion of the cooling tank 8 . The lower end of the collection conduit 13 is inserted into the mouth of the collection container 15.

この捕集容器15は、冷却容器17内に配置され、かつ
該冷却容器17内には冷却水18が満たされている。
This collection container 15 is arranged within a cooling container 17, and the cooling container 17 is filled with cooling water 18.

前記冷却容器17の下部側壁には、冷却水導入部19が
設けられ、かつ同容器17の」一部側壁には冷却水I8
のオーバーフロ一部20が設けられている。
A cooling water introduction part 19 is provided on the lower side wall of the cooling container 17, and a cooling water I8 is provided on a part of the side wall of the cooling container 17.
An overflow portion 20 is provided.

更に、前記密閉容器1内の溶液物質2が収容された部分
及び該溶液物質2の液面上方には、フィルタ板21a 
、 21bが夫々設けられている。これらフィルタ板2
1a 、 21bは、多数の穴が穿設された円板状をな
すと共に中央に前記捕集導管13が貫通ずる穴を開口し
た形状になっており、具体的には直径24mm、厚さ0
.2cmの穴が約5000個くり抜かれたポリテトラフ
ルオロエチレン製板から形成されている。なお、前記各
フィルタ21a 、 21bは夫々1枚で形成しても、
曵数枚所定の間隔をあけて積層し、て形成してもよい。
Further, a filter plate 21a is provided in the portion of the closed container 1 where the solution substance 2 is accommodated and above the liquid level of the solution substance 2.
, 21b are provided, respectively. These filter plates 2
1a and 21b are in the shape of a disk with a large number of holes, and have a hole in the center through which the collection conduit 13 passes, and specifically have a diameter of 24 mm and a thickness of 0.
.. It is made of a polytetrafluoroethylene plate with approximately 5,000 2 cm holes punched out. Note that even if each of the filters 21a and 21b is formed of one piece,
It may also be formed by stacking several sheets at a predetermined interval.

前記冷却Vj8下部と溶液物質2液而の間に位置する前
記密閉容器lの内面部分には、互いに平行して下方に傾
斜した複数枚の第1の遮蔽板22が夫々設けられている
。また、前記冷却)fl 8上部と溶液物質2液面の間
に位置する前記捕集導管13の4而部分には複数枚の第
2の遮蔽板23が下方に傾斜するように夫々設けられて
いる。前記密閉容器lの側壁には、吸排気管24が連結
されており、かつ該吸排気管24にはバルブ25が介装
されている。なお、前記溶液物質2、その蒸発物質及び
仏性液が接触する密閉容器1、捕集導管13、捕集容器
15及び遮蔽板22.23は夫々高純度石英により形成
されている。
A plurality of first shielding plates 22 parallel to each other and tilted downward are provided on the inner surface of the closed container l located between the lower part of the cooling Vj8 and the solution substance 2, respectively. Furthermore, a plurality of second shielding plates 23 are provided at four parts of the collection conduit 13 located between the upper part of the cooling fl 8 and the liquid surface of the solution substance 2, respectively, so as to be inclined downward. There is. An intake/exhaust pipe 24 is connected to the side wall of the closed container 1, and a valve 25 is interposed in the intake/exhaust pipe 24. The closed container 1, the collection conduit 13, the collection container 15, and the shielding plates 22 and 23, with which the solution substance 2, its evaporated substance, and liquid come into contact, are each made of high-purity quartz.

次に、前述した第1図図示の仏性装置を用いて硝酸の仏
性精製方法を説明する。
Next, a method for purifying nitric acid will be explained using the above-described apparatus shown in FIG.

まず、硝酸1oooo−にリン酸を50−添加した溶液
物質2を注入部6から密閉容器1内に注入し、排出部7
から排出して該容器1内に一定量の溶液物質2を貯蔵し
た。つづいて、磁界発生部材4から溶液物質2に8 K
 Gaussの磁界を与え、かつ冷却槽8の冷却水人口
11から冷却水を供給して冷却水出口12から排出17
て該冷却槽8の外筒体9を冷却し、更にヒータ3により
密閉容器I内の溶液物質2を119℃に加熱した。こう
したヒータ3による加熱によって、密閉容器1内の溶液
物質2が沸騰、蒸気化される。この場合、溶液物質2の
表面でミストの発生が起こるが、該溶液物質2中及びそ
の上方にフィルタ板21a 、 21bが夫々配置され
ているため、ミストが溶液物質の蒸気26と共に密閉容
器1の上部に上昇するのを抑制される。また、前記磁界
発生部材4からの磁界の作用によりミスト中にFe5C
o、N1等の強磁性金属不純物が混入するのを防止でき
る。更に、溶液物質2には予めリン酸が添加されている
ため、硝酸中のUlTh、Fe等の金属不純物イオンが
該リン酸と反応して高沸点のリン酸化合物を生成するた
め、金属不純物の蒸発が少なくなり、これち金属不純物
を含むミストの発生が抑制される。その上、溶液物質2
を加熱、蒸気化する際して該溶液物質2が密閉容器1内
面や捕集導管13外面に沿って上昇する、いわゆるクリ
ーピングを密閉容器1内面及び捕集導管13外面に夫々
設けられた遮蔽板22.23によって阻止され、溶液物
質2そのものが捕集導管13上端の捕集部14からその
内部に流入するのを防止される。
First, a solution substance 2 obtained by adding 50 - of phosphoric acid to 100 - of nitric acid is injected into the closed container 1 from the injection part 6, and then
A quantity of solution substance 2 was stored in the container 1 by discharging it from the container. Subsequently, 8 K is applied from the magnetic field generating member 4 to the solution substance 2.
A Gaussian magnetic field is applied, and cooling water is supplied from the cooling water port 11 of the cooling tank 8 and discharged from the cooling water outlet 12 17
The outer cylinder 9 of the cooling tank 8 was cooled, and the solution substance 2 in the closed container I was further heated to 119° C. by the heater 3. By heating with the heater 3, the solution substance 2 in the closed container 1 is boiled and vaporized. In this case, mist is generated on the surface of the solution material 2, but since the filter plates 21a and 21b are arranged in and above the solution material 2, the mist is generated in the closed container 1 together with the vapor 26 of the solution material. It is restrained from rising to the top. In addition, due to the effect of the magnetic field from the magnetic field generating member 4, Fe5C is added to the mist.
It is possible to prevent ferromagnetic metal impurities such as O and N1 from being mixed in. Furthermore, since phosphoric acid is added to the solution material 2 in advance, metal impurity ions such as UlTh and Fe in nitric acid react with the phosphoric acid to produce a high boiling point phosphoric acid compound. Evaporation is reduced, and the generation of mist containing metal impurities is suppressed. Moreover, solution substance 2
When the solution substance 2 is heated and vaporized, it rises along the inner surface of the closed container 1 and the outer surface of the collection conduit 13, which is called creeping. The plates 22,23 prevent the solution substance 2 itself from flowing into its interior from the collecting section 14 at the upper end of the collecting conduit 13.

上記ヒータ3の加熱により蒸気化され、ミスト等の混入
が抑制された溶液物質の蒸気2Bは、密閉容器l内を上
昇し、その上部に配置された冷却槽8の外表面に接触し
て凝縮する。こうして冷却槽8で凝縮された溶液物質の
仏性液滴27は、該冷却槽8のテーパ部に沿って下部に
集り、落下する。
The vapor 2B of the solution substance, which is vaporized by the heating of the heater 3 and whose contamination with mist etc. is suppressed, rises inside the closed container 1, contacts the outer surface of the cooling tank 8 disposed above it, and condenses. do. The liquid droplets 27 of the solution material thus condensed in the cooling tank 8 gather at the bottom along the tapered part of the cooling tank 8 and fall.

落下した仏性液滴27は、冷却槽8の下部に近接して配
置された捕集部14をから捕集導管13内に導入される
。捕集導管I3を伝わって落下する仏性液滴27は、該
導管13の下端から予め冷却容器17内で冷却水18に
より冷却された捕集容器15に落下して硝酸の仏性液2
8として捕集される。
The fallen liquid droplets 27 are introduced into the collection conduit 13 through the collection section 14 arranged close to the lower part of the cooling tank 8 . The liquid droplets 27 falling through the collection conduit I3 fall from the lower end of the conduit 13 into the collection container 15, which has been cooled in advance with the cooling water 18 in the cooling container 17, and collect the liquid 2 of nitric acid.
Collected as 8.

比較例1 硝酸にリン酸を添加しない溶液物質を用いた以外、前記
実施例1と同様な方法により硝酸の蒸溜を行なった。
Comparative Example 1 Nitric acid was distilled in the same manner as in Example 1, except that a solution material in which phosphoric acid was not added to nitric acid was used.

しかして、本実施例1及び比較例1により得られた硝酸
仏性液中のU及びThを誘導結合プラズマ質量分析装置
、Fc及びCaをフレームレス原子吸光装置により夫々
分析した。その結果を下記第1表に示す。なお、第1表
中には蒸溜する前の硝酸(原液)の分析値を併記した。
Therefore, U and Th in the nitric acid solution obtained in Example 1 and Comparative Example 1 were analyzed using an inductively coupled plasma mass spectrometer, and Fc and Ca were analyzed using a flameless atomic absorption spectrometer. The results are shown in Table 1 below. In Table 1, the analytical values of nitric acid (undiluted solution) before distillation are also listed.

第   1   表 第2表に示す。なお、第2表中には蒸溜する前の塩酸(
原液)の分析値を併記した。
Shown in Table 1 and Table 2. Furthermore, in Table 2, hydrochloric acid (
The analytical values of the stock solution) are also listed.

第   2   表 実施例2 溶液物質として塩酸10000−に硫酸を50−を添加
したものを用い、かつ蒸溜温度を107℃とした以外、
実施例1と同様な方法により塩酸の蒸溜を行なった。
Table 2 Example 2 Except that 50% of sulfuric acid was added to 10,000% of hydrochloric acid as the solution material, and the distillation temperature was 107°C.
Hydrochloric acid was distilled in the same manner as in Example 1.

比較例2 塩酸に硫酸を添加しない溶液物質を用いた以外、前記実
施例2と同様な方法により塩酸の蒸溜を行なった。
Comparative Example 2 Hydrochloric acid was distilled in the same manner as in Example 2, except that a solution material in which sulfuric acid was not added to the hydrochloric acid was used.

しかして、本実施例2及び比較例2により得られた塩酸
仏性液中のU及びThを誘導結合プラズマ質量分析装置
、Fe及びCaをフレームレス原子吸光装置により夫々
分析した。その結果を下記実施例3 第1図図示の仏性装置における溶液物質2、その蒸発物
質及び仏性液が接触する密閉容2″A1、捕集導管13
、捕集容器15及び遮蔽板22.23をポリテトロフル
オロエチレンにより形成し、溶液物質として弗化水素酸
toooo−に硫酸を50−添加したしのを用い、かつ
蒸溜温度を110℃とした以外、実施例1と同様な方法
により弗化水素酸の蒸溜を行なった。
Therefore, U and Th in the hydrochloric acid solution obtained in Example 2 and Comparative Example 2 were analyzed using an inductively coupled plasma mass spectrometer, and Fe and Ca were analyzed using a flameless atomic absorption spectrometer. The results are shown below in Example 3. In the apparatus shown in FIG.
, except that the collection container 15 and the shielding plates 22 and 23 were made of polytetrofluoroethylene, the solution material was hydrofluoric acid to which 50% of sulfuric acid had been added, and the distillation temperature was 110°C. , Hydrofluoric acid was distilled in the same manner as in Example 1.

比較例3 弗化水素酸に硫酸を添加しない溶液物質を用いた以外、
前記実施例3と同様な方法により弗化水素酸の蒸溜を行
なった。
Comparative Example 3 Except for using a solution material in which sulfuric acid was not added to hydrofluoric acid,
Hydrofluoric acid was distilled in the same manner as in Example 3 above.

しかして、本実施例3及び比較例3により得られた弗化
水素酸仏性液中のU及びThを誘導結合プラズマ質ff
i+)折装置、Fc及びCaをフレームレス原子吸光装
置により夫々分析した。その結果を下記第3表に示す。
Therefore, U and Th in the hydrofluoric acid solution obtained in Example 3 and Comparative Example 3 were transferred to the inductively coupled plasma ff.
Fc and Ca were analyzed using a frameless atomic absorption spectrometer. The results are shown in Table 3 below.

なお、第3表中には蒸溜する前の弗化水素酸(原液)の
分析値を併記した。
Additionally, Table 3 also shows the analytical values of hydrofluoric acid (undiluted solution) before distillation.

第  3  表 上記第1表〜第3表から明かなように、本実施例の蒸溜
精製方法によれば比較例1〜3に比べて極めて高純度の
硝酸、塩酸、弗化水素酸を蒸溜、精製できることがわか
る。
Table 3 As is clear from Tables 1 to 3 above, the distillation purification method of this example distilled nitric acid, hydrochloric acid, and hydrofluoric acid with extremely high purity compared to Comparative Examples 1 to 3. It turns out that it can be purified.

なお、上記実施例で用いた蒸溜装置において捕集導管1
3として直線状のものを使用したが、仏性液滴の捕集効
果を向上させるために途中をコイル状とした捕集導管を
用いてもよい。
In addition, in the distillation apparatus used in the above example, the collection conduit 1
Although a straight pipe was used as No. 3, a collection pipe with a coiled part in the middle may be used to improve the collection effect of the droplets.

上記実施例で用いた蒸溜装置において、溶液物質2の上
方にフィルタ21bを配置するのみならず、溶液物質2
中にもフィルタ21aを配置したが、該フィルタ21a
を省略してもよい。
In the distillation apparatus used in the above embodiment, not only the filter 21b is disposed above the solution substance 2, but also the filter 21b is disposed above the solution substance 2.
A filter 21a is also arranged inside, but the filter 21a
may be omitted.

[発明の効果] 以上詳述した如く、本発明によれば金属不純物の混入の
ない高純度の硝酸、塩酸、弗化水素酸等の試薬を精製し
得る蒸溜精製方法を提供できる。
[Effects of the Invention] As detailed above, according to the present invention, it is possible to provide a distillation purification method capable of purifying highly pure reagents such as nitric acid, hydrochloric acid, and hydrofluoric acid without contamination with metal impurities.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は、本発明の実施例で使用した蒸溜装置の一形態
を示す概略図である。 l・・・密閉容器、2・・・溶液物質、3・・・ヒータ
、4・・・磁界発生部材、8・・・冷却槽、13・・・
捕集導管、15・・・捕集容器、17・・・冷却容器、
21a 、21b・・・フィルタ、22.23・・・遮
蔽板、26・・・蒸気、27・・・仏性液滴、28・・
・仏性液。 出願人代理人  弁理士 鈴江武彦
FIG. 1 is a schematic diagram showing one form of a distillation apparatus used in an example of the present invention. l... Airtight container, 2... Solution substance, 3... Heater, 4... Magnetic field generating member, 8... Cooling tank, 13...
Collection conduit, 15... Collection container, 17... Cooling container,
21a, 21b... Filter, 22. 23... Shielding plate, 26... Steam, 27... Buddhist droplet, 28...
・French sexual fluid. Applicant's agent Patent attorney Takehiko Suzue

Claims (1)

【特許請求の範囲】[Claims] 底部付近に溶液物質が収容された密閉容器と、この密閉
容器の側壁に連結された溶液物質の注入部及び排出部と
、前記密閉容器内の溶液物質を加熱するための加熱手段
と、前記密閉容器の上部に挿置され下部がテーパ状をな
す冷却槽と、上端が前記密閉容器内の冷却槽下部に近接
して配置され、かつ下端を該容器底面を貫通して下方に
延出させた捕集導管と、この捕集導管の下端が挿入され
る蒸溜液の捕集容器と、前記溶液物質の液面上方に位置
する前記密閉容器内に配置されたフィルタ板と、前記冷
却槽下部と溶液物質液面の間に位置する前記密閉容器の
内面部分及び前記捕集導管の外面部分に設けられた遮蔽
板を具備した蒸溜装置を用いて溶液物質を蒸溜精製する
方法において、前記溶液物質に予め硫酸及びリン酸のう
ちの一方又は両者を添加することを特徴とする蒸溜精製
方法。
a closed container containing a solution substance near the bottom; an injection part and a discharge part for the solution substance connected to a side wall of the closed container; a heating means for heating the solution substance in the closed container; A cooling tank is inserted into the upper part of the container and has a tapered lower part, and the upper end is arranged close to the lower part of the cooling tank in the closed container, and the lower end extends downward through the bottom of the container. a collection conduit, a distillate collection container into which the lower end of the collection conduit is inserted, a filter plate disposed in the closed container located above the liquid level of the solution substance, and a lower part of the cooling tank. In a method for distilling and purifying a solution substance using a distillation apparatus equipped with a shielding plate provided on an inner surface of the closed container and an outer surface of the collection conduit located between the liquid surface of the solution substance, the solution substance is purified by distillation. A distillation purification method characterized by adding in advance one or both of sulfuric acid and phosphoric acid.
JP30001188A 1988-11-28 1988-11-28 Distillation purification method Expired - Fee Related JP2793208B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP30001188A JP2793208B2 (en) 1988-11-28 1988-11-28 Distillation purification method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP30001188A JP2793208B2 (en) 1988-11-28 1988-11-28 Distillation purification method

Publications (2)

Publication Number Publication Date
JPH02144101A true JPH02144101A (en) 1990-06-01
JP2793208B2 JP2793208B2 (en) 1998-09-03

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ID=17879644

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Country Status (1)

Country Link
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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5603811A (en) * 1990-03-21 1997-02-18 Cogema -Compagnie Generale Des Matieres Nucleaires Process for the treatment of an aqueous solution mainly containing nitric acid and hydrofluoric acid
JP2012062300A (en) * 2010-09-16 2012-03-29 Shanghai Chemical Reagent Research Inst Method for producing ultra-high purity electronic grade chemical reagent
CN102921180A (en) * 2011-08-08 2013-02-13 四川西陇化工有限公司 Preparation method of inorganic ultra-clean highly-pure reagent acid

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5603811A (en) * 1990-03-21 1997-02-18 Cogema -Compagnie Generale Des Matieres Nucleaires Process for the treatment of an aqueous solution mainly containing nitric acid and hydrofluoric acid
JP2012062300A (en) * 2010-09-16 2012-03-29 Shanghai Chemical Reagent Research Inst Method for producing ultra-high purity electronic grade chemical reagent
CN102921180A (en) * 2011-08-08 2013-02-13 四川西陇化工有限公司 Preparation method of inorganic ultra-clean highly-pure reagent acid

Also Published As

Publication number Publication date
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