JPS6082102A - Refining apparatus of reagent - Google Patents

Refining apparatus of reagent

Info

Publication number
JPS6082102A
JPS6082102A JP19186183A JP19186183A JPS6082102A JP S6082102 A JPS6082102 A JP S6082102A JP 19186183 A JP19186183 A JP 19186183A JP 19186183 A JP19186183 A JP 19186183A JP S6082102 A JPS6082102 A JP S6082102A
Authority
JP
Japan
Prior art keywords
reagent
teflon
conduit
cooling
storage tank
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.)
Pending
Application number
JP19186183A
Other languages
Japanese (ja)
Inventor
Tsugio Shimono
下野 次男
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.)
NEC Corp
Original Assignee
NEC Corp
Nippon Electric Co Ltd
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 NEC Corp, Nippon Electric Co Ltd filed Critical NEC Corp
Priority to JP19186183A priority Critical patent/JPS6082102A/en
Publication of JPS6082102A publication Critical patent/JPS6082102A/en
Pending legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/02Apparatus characterised by being constructed of material selected for its chemically-resistant properties
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/02Apparatus characterised by their chemically-resistant properties
    • B01J2219/025Apparatus characterised by their chemically-resistant properties characterised by the construction materials of the reactor vessel proper
    • B01J2219/0295Synthetic organic materials

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)

Abstract

PURPOSE:To refine a quartz corrosive reagent with an inexpensive apparatus by using a ''Teflon'' material at the part of the apparatus in contact with the reagent. CONSTITUTION:An original liquid reagent 6 is charged into a reagent storage tank 4 made of ''Teflon'' which is placed on a hot plate 7 and heated. A gaseous nitrogen is blown into the reagent storage tank through a gas washing bottle 1 and a ''Teflon'' tube 3. The evaporated reagent is cooled by a cooler pipe 9 made of ''Teflon'' through a ''Teflon'' tube 8, and the refined reagent is collected in a collecting bottle 11 made of ''Teflon''.

Description

【発明の詳細な説明】 本発明は、酸などの溶液状の試薬を蒸留法により精製す
る装置に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an apparatus for purifying a solution-like reagent such as an acid by a distillation method.

電子工業、原子カニ業あるいは各種素材工業の進歩に伴
なう材料の高純度化の要求とともに、材料計測技術に右
いても超微量成分分析技術力の向上が一段と強く要求さ
れている。最近の分析装置の急速な発達により湿式化学
分析でも超微量成分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
くなり依然として超微量成分を分析できない場合が多い
。現在、電子工業用あるい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は
充分な純度であるとはいえず、使用目的に応じてさらに
精製する必要がある。従来、高純度試薬を調製するため
に石英製二段蒸留装置や石英製非沸騰蒸留装置が用いら
れているがこれらの装置は石英からできているためフッ
化水素酸のように石英腐食性の試薬の精製が難しい、装
置が高価である、広い設置スペースが必要であるなどの
欠点を有していた。
Along with the demand for higher purity materials due to advances in the electronics industry, atomic crab industry, and various materials industries, there is an even stronger need for improvements in ultratrace component analysis technology in material measurement technology. The recent rapid development of analytical equipment has made it possible to analyze ultratrace components using 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 high. In many cases, it is still not possible to analyze ultratrace components. Currently, high-purity reagents for 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 need to be further purified depending on the purpose of use. . Conventionally, quartz double-stage distillation equipment and quartz non-boiling distillation equipment have been used to prepare high-purity reagents, but since these equipment is made of quartz, it cannot be used with quartz corrosive substances such as hydrofluoric acid. It has drawbacks such as difficulty in purifying the reagent, expensive equipment, and the need for a large installation space.

本発明の目的は、石英腐食性の試薬の精製が行なえ、安
価に装置を組み立てられ、使用時以外には分解収納でき
る新規な試薬精製装置を提供することにある。
SUMMARY OF THE INVENTION An object of the present invention is to provide a new reagent purification apparatus that can purify quartz corrosive reagents, can be assembled at low cost, and can be disassembled and stored when not in use.

本発明の試薬精製装置は、上ぶたに2本の導管を有する
試薬貯留槽部をホットプレート上で加熱し、発生した試
薬蒸気を一方の導管から導入した洗浄された不活性ガス
で追い出し他方の導管から冷却槽部に設置した冷却管部
に導き入れ、凝縮した精製試薬を捕集びん部に導く構造
を有し、試薬と接触する部分に全てテフロン製の部品を
用いることを特徴とする。
In the reagent purification device of the present invention, a reagent storage tank section having two conduits in the upper lid is heated on a hot plate, the generated reagent vapor is expelled with a cleaned inert gas introduced from one conduit, and the other conduit is expelled. It has a structure in which the condensed purified reagent is guided from a conduit to a cooling pipe installed in a cooling tank part to a collection bottle part, and all parts that come into contact with the reagent are made of Teflon.

以下、本発明について一実施例を示す図面を参照して説
明する。
DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be described below with reference to drawings showing one embodiment.

第1図は実施例を示す断面図である。テフロン製の試薬
貯留槽4に適量の試薬原液6を入れる。
FIG. 1 is a sectional view showing an embodiment. An appropriate amount of reagent stock solution 6 is put into a reagent storage tank 4 made of Teflon.

貯留槽の上ぶた5には2本のテフロン製導管が取り付け
られている。導管3は窒素ガスの洗気びん1に、導管8
は冷却管9に連結しており、各導管の先端は試薬液面の
下および上にある。貯留槽をホットプレート7にのせ加
熱し1発生した試薬蒸気を導管8からテフロン製冷却管
9に導入して凝縮させ、凝縮した精製試薬をテフロン製
捕集びん部11に集める。その場合、試薬が沸騰すると
試薬飛沫が発生し精製効率が悪くなるので沸騰しない程
度の温度で加熱する。発生した試薬蒸気を効率良く送り
出すために導管3から窒素ガスを吹き込む。窒素ガスに
も不純物が含有される可能性があるので洗気びんlを通
して洗浄する。洗気びんには濃硫酸などの洗浄液2が入
れである。冷却管9は冷却槽10に入っている。冷却槽
10には氷−水。
Two Teflon conduits are attached to the upper lid 5 of the storage tank. Conduit 3 connects to nitrogen gas washing bottle 1, and conduit 8
are connected to cooling tubes 9, the tips of each conduit being below and above the reagent liquid level. The storage tank is heated by placing it on a hot plate 7, and the generated reagent vapor is introduced from a conduit 8 into a Teflon cooling pipe 9 to be condensed, and the condensed purified reagent is collected in a Teflon collecting bottle 11. In this case, if the reagent boils, reagent droplets will be generated and the purification efficiency will deteriorate, so the reagent is heated at a temperature that does not boil. Nitrogen gas is blown through the conduit 3 in order to efficiently send out the generated reagent vapor. Nitrogen gas may also contain impurities, so it is washed through an air washing bottle. The air washing bottle contains a washing liquid 2 such as concentrated sulfuric acid. The cooling pipe 9 is placed in a cooling tank 10. The cooling tank 10 contains ice and water.

ドライアイス−エタノールなどの冷却剤が入っている。Dry ice - Contains a cooling agent such as ethanol.

冷却効率を高めるために冷却管はコイル状になっている
。外部からの汚染を防ぐために捕集びんの口はテフロン
シートなどでおおう。市販の最高純度の硝酸とフッ化水
素酸を第1図の装置で蒸留11″ij製した時の結果を
表1.2に示す。蒸留速度はホットプレートの温度にも
よるが約20fnl/時間であった。表1.2に示され
るように、蒸留精製により各不純物濃度が硝酸で1/1
.5〜IA8゜フッ化水素酸でl/1.1〜1/4に減
少した。
The cooling tubes are coiled to increase cooling efficiency. Cover the mouth of the collection bottle with a Teflon sheet to prevent contamination from the outside. Table 1.2 shows the results when commercially available highest purity nitric acid and hydrofluoric acid were distilled to 11"ij using the apparatus shown in Figure 1. The distillation rate was approximately 20 fnl/hour, although it depended on the temperature of the hot plate. As shown in Table 1.2, the concentration of each impurity was reduced to 1/1 with nitric acid by distillation purification.
.. It was reduced to 1/1.1 to 1/4 with 5 to IA 8° hydrofluoric acid.

第1図の装置を改良した装置の試薬貯留槽部分の断面図
を第2図に示す。第2図では第1図の導管3と導管8が
改良されている。導管3では先端表1.蒸留前後での硝
酸中の不純物含有濃度が円筒のため窒素ガスを吹き込む
と大傘な気泡がifr続的に発生するため試薬飛沫が発
生しやすく精製効率が低下する。導管12の先端は多数
の細孔の空いた恰】21を有しており、気泡が連続的に
発生するため窒素ガスを穏やかに吹き込める。そのため
試薬飛沫の発生を抑えられる。尋′98に入った試薬飛
沫はそのまま冷却管に送り込まれるため精製効率が低下
する。導管13には途甲にテフロンくずを冗填したトラ
ップ14がついているため、試薬飛沫はここで捕集され
、試薬蒸気だけが1′肯却看に送り込まれ、商い精製効
率を得ることがでさる。、第2図に示すように専管を救
民することにより、第1図の装置に較べで、数倍精製効
率を高めることができた。
FIG. 2 shows a sectional view of the reagent storage tank portion of the device that is an improved version of the device shown in FIG. In FIG. 2, the conduits 3 and 8 of FIG. 1 have been improved. In conduit 3, tip table 1. Since the concentration of impurities in nitric acid before and after distillation is cylindrical, large bubbles are continuously generated when nitrogen gas is blown into the nitric acid, which tends to generate reagent droplets and reduces purification efficiency. The tip of the conduit 12 has a hole 21 with a large number of pores, and since bubbles are continuously generated, nitrogen gas can be gently blown into the conduit 12. Therefore, generation of reagent droplets can be suppressed. Since the reagent droplets that entered the tube '98 are directly sent to the cooling tube, the purification efficiency decreases. Since the conduit 13 is equipped with a trap 14 redundantly filled with Teflon scraps, the reagent droplets are collected here, and only the reagent vapor is sent to the 1' container, thereby achieving commercial purification efficiency. Monkey. As shown in FIG. 2, by using a dedicated system, the purification efficiency could be increased several times compared to the device shown in FIG.

冷却′U部や冷却槽部iこけ第1図に示されたもの以外
に、各種のものが考えらnる。その−実施例の断面図を
第3図に示す。第3因のものは二重管構造を有している
。冷却管部■5は透明な材質のもので作らn、た帝却倍
部I6に組み込ま孔ている。冷却槽s16の中では冷却
剤17が循環している。この冷却管部を使うと凝縮した
試薬が滞留しないため蒸留速度が速かった。
Various types of cooling parts other than those shown in FIG. 1 are conceivable for the cooling section and cooling tank section. A sectional view of this embodiment is shown in FIG. The third factor has a double tube structure. The cooling pipe part 5 is made of a transparent material and is incorporated into the cooling pipe part I6. A coolant 17 is circulating in the cooling tank s16. By using this cooling tube section, the distillation rate was faster because the condensed reagents did not stagnate.

第1図および第2図に示した装置は、各部品が分解でき
るため必要な時だけ装置を組み立てれば良く、使用しな
い時は分解して収納できる。そのため特別に設置スペー
スを必要としない。また、石英製蒸留装置より安価に組
み立てられる。
In the apparatus shown in FIGS. 1 and 2, each part can be disassembled, so the apparatus need only be assembled when necessary, and can be disassembled and stored when not in use. Therefore, no special installation space is required. It is also cheaper to assemble than a quartz distillation device.

以上、実施例に示したように、本発明の試薬精製装置に
より、従来の石英製蒸留器で行なえなかった石英腐食性
の試薬の蒸留器で行なえなかった石英腐食性の試薬の蒸
留精製が可能になった。さらに、本装置は安価に組み立
てられるとともに、分解が容易なため特別な設置スペー
スがいらないなどの利点を有する。
As shown in the examples above, the reagent purification apparatus of the present invention enables distillation purification of quartz corrosive reagents, which could not be performed with conventional quartz distillers. Became. Furthermore, this device has the advantage of being inexpensive to assemble and easy to disassemble, requiring no special installation space.

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

第1図は本発明の装置の一実施例を示す断面図である。 図において。 1・・・洗気びん、2・・・濃硫酸などの洗浄液、3・
・・テフロン製導管、4・・・テフロン製酸貯留槽、5
・・・上ぶた。6・・・酸原液、7・・・ホットプレー
ト、8・・・テフロン製導管、9・・・テフロン製冷却
管、10・・・冷却槽、 11・・・テフロン製捕集び
ん、第2図は他の実施例を示す装置の酸貯留槽部分の断
面図である。図において、 12 、13・・・テフロン製導管、14・・・トラッ
プ、第3図は冷却管部および冷却槽部の他の実施例を示
す断面図である。図において。 15・・・テフロン製冷却管、16・・・冷却槽、17
・・・冷却剤。 オ l 図 :/P 2 図 オ 3 図
FIG. 1 is a sectional view showing an embodiment of the device of the present invention. In fig. 1...Air washing bottle, 2...Cleaning liquid such as concentrated sulfuric acid, 3.
...Teflon conduit, 4...Teflon acid storage tank, 5
...upper lid. 6... Acid stock solution, 7... Hot plate, 8... Teflon conduit, 9... Teflon cooling pipe, 10... Cooling tank, 11... Teflon collection bottle, 2nd The figure is a sectional view of an acid storage tank portion of a device showing another embodiment. In the figure, 12, 13... Teflon conduit, 14... trap, and FIG. 3 is a sectional view showing another embodiment of the cooling pipe section and the cooling tank section. In fig. 15... Teflon cooling pipe, 16... Cooling tank, 17
...coolant. O l Figure: /P 2 Figure O 3 Figure

Claims (1)

【特許請求の範囲】[Claims] 上ぶたに2本の導管を有する試薬貯留槽部をボ、ドブレ
ート上で加熱し、発生した試薬蒸気を一方の導管から導
入した洗浄された不活性ガスで追い出し、他方の導管か
ら冷却槽部に設置した冷却管部に導き入れ、凝縮した積
装試薬を冷却管部から捕集びん部に導くように構成され
、かつ、試薬と接触する部分が全てテフロン材を用いて
構成されることを特徴とする試薬精製装置。
The reagent storage tank section, which has two conduits in the upper lid, is heated on a vent plate, and the generated reagent vapor is expelled with a cleaned inert gas introduced from one conduit, and then transferred to the cooling tank section from the other conduit. It is configured to introduce the condensed loaded reagent into the installed cooling pipe section and guide it from the cooling pipe section to the collection bottle section, and is characterized in that all parts that come into contact with the reagent are constructed using Teflon material. Reagent purification equipment.
JP19186183A 1983-10-14 1983-10-14 Refining apparatus of reagent Pending JPS6082102A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP19186183A JPS6082102A (en) 1983-10-14 1983-10-14 Refining apparatus of reagent

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP19186183A JPS6082102A (en) 1983-10-14 1983-10-14 Refining apparatus of reagent

Publications (1)

Publication Number Publication Date
JPS6082102A true JPS6082102A (en) 1985-05-10

Family

ID=16281712

Family Applications (1)

Application Number Title Priority Date Filing Date
JP19186183A Pending JPS6082102A (en) 1983-10-14 1983-10-14 Refining apparatus of reagent

Country Status (1)

Country Link
JP (1) JPS6082102A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6508915B1 (en) 1996-12-20 2003-01-21 Fujitsu Limited Apparatus and method for distilling waste liquids

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6508915B1 (en) 1996-12-20 2003-01-21 Fujitsu Limited Apparatus and method for distilling waste liquids
US7232504B2 (en) 1996-12-20 2007-06-19 Fujitsu Limited Apparatus and method for distilling waste liquids

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