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JPH0292802A - Extraction of fluorine and/or chlorine from inorganic substance - Google Patents

Extraction of fluorine and/or chlorine from inorganic substance

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Publication number
JPH0292802A
JPH0292802A JP24254288A JP24254288A JPH0292802A JP H0292802 A JPH0292802 A JP H0292802A JP 24254288 A JP24254288 A JP 24254288A JP 24254288 A JP24254288 A JP 24254288A JP H0292802 A JPH0292802 A JP H0292802A
Authority
JP
Japan
Prior art keywords
fluorine
chlorine
inorganic substance
reaction
reaction accelerator
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
JP24254288A
Other languages
Japanese (ja)
Other versions
JPH0617206B2 (en
Inventor
Michitaka Hidaka
道孝 日高
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.)
NGK Insulators Ltd
Original Assignee
NGK Insulators 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 NGK Insulators Ltd filed Critical NGK Insulators Ltd
Priority to JP63242542A priority Critical patent/JPH0617206B2/en
Publication of JPH0292802A publication Critical patent/JPH0292802A/en
Publication of JPH0617206B2 publication Critical patent/JPH0617206B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Investigating Or Analyzing Non-Biological Materials By The Use Of Chemical Means (AREA)

Abstract

PURPOSE:To enable easy and perfect extraction of fluorine and/or chlorine in inorganic substance by admixing a reaction accelerator to the inorganic substance, heating them in a steam at a specific temperature and collecting the formed HF and/or HCl in an alkaline solution. CONSTITUTION:An inorganic substance containing fluorine and/or chlorine such as a silicate salt containing magnesium fluoride and chloride is prepared. The inorganic substance is mixed with a reaction accelerator such as ferric oxide and the mixture is placed on a platinum boat, then inserted from the inlet 7 into the reaction tube 9. Then, the steam generated in the flask 1 is sent to the reaction tube 9 and the inorganic substance and the reaction accelerator is heated over 1,100 deg.C in the reaction tube 9 with an electric heater 6 so that the inorganic substance reacts with the reaction accelerator and the generated HF and/or HCl is cooled down with the cooling tube 8 and collected into an alkaline solution. This process enables accurate determination of fluorine and/or chlorine in inorganic substances.

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明はけい酸塩およびアルミナ等の無機物中のふっ素
及び/又は塩素を、パイロハイトロリシス(熱加水分解
)により抽出分離する方法に関するものである。
Detailed Description of the Invention (Industrial Application Field) The present invention relates to a method for extracting and separating fluorine and/or chlorine in inorganic substances such as silicates and alumina by pyrohydrolysis (thermal hydrolysis). It is.

(従来の技術) 一般に無機物中のふっ素及び/又は塩素の定量は、予じ
め蒸留法、パイロハイトロリシスによりふっ素及び/又
は塩素を抽出分離したのち、吸光光度法、イオン電極法
あるいはイオンクロマトグラフィー法等により行ってい
た。
(Prior art) In general, the determination of fluorine and/or chlorine in inorganic substances is performed by extracting and separating fluorine and/or chlorine in advance by distillation or pyrohydrolysis, and then using spectrophotometry, ion electrode method, or ion chromatography. This was done using the graphic method, etc.

このうち、パイロハイトロリシスによりふっ素及び/又
は塩素を抽出分離する方法の一例として、「反応促進剤
として酸化第二鉄を用いる熱加水分解」 (多田格三、
日本分析化学会、分析化学討論会、B73頁〜B74頁
、I B 12  (1970) )で開示された方法
が知られている。この方法は、対象となるオパールガラ
ス等の無機物を反応促進剤として酸化第二鉄を用いて1
050〜1100℃の温度で反応させて、ふっ素を抽出
分離していた。
Among these, one example of a method for extracting and separating fluorine and/or chlorine by pyrohydrolysis is ``thermal hydrolysis using ferric oxide as a reaction accelerator'' (Kakuzo Tada,
The method disclosed in Japanese Society of Analytical Chemistry, Analytical Chemistry Forum, pages B73 to B74, IB 12 (1970)) is known. This method uses ferric oxide as a reaction accelerator to treat inorganic substances such as opal glass.
Fluorine was extracted and separated by reaction at a temperature of 050 to 1100°C.

(発明が解決しようとするi1題) 上述した方法は、オパールガラス、リシア雲母等に対し
て有効な手段であるが、無機物中でもアルミニウムやマ
グネシウムのぶつ化物及び/又は塩化物を含むけい酸塩
やアルミナ中のふっ素を定量しようとすると、ふっ素及
び/又は塩素を完全には抽出できず、正確な分析が実施
できない場合があった。
(I1 Problem to be Solved by the Invention) The above-mentioned method is effective for opal glass, spodium mica, etc., but it is also effective for treating opal glass, sulfur mica, etc., but it also applies to silicates containing aluminum and magnesium lumps and/or chlorides, among other inorganic substances. When trying to quantify fluorine in alumina, fluorine and/or chlorine could not be completely extracted, making accurate analysis impossible in some cases.

本発明の目的は上述した課題を解消して、アルミニラム
やマグネシウムのぶつ化物及び/又は塩化物を含むけい
酸塩やアルミナ中のふっ素及び/又は塩素を正確に抽出
分離することが可能なふっ素及び/又は塩素の抽出方法
を提供しようとするものである。
The purpose of the present invention is to solve the above-mentioned problems, and to make it possible to accurately extract and separate fluorine and/or chlorine in silicates and alumina containing aluminum ram and magnesium chloride and/or chloride. /Or to provide a method for extracting chlorine.

(課題を解決するための手段) 本発明のふっ素及び/又は塩素の抽出方法は、無機物中
のふっ素及び/又は塩素を抽出する方法であって、無機
物に反応促進剤を混合して水蒸気中、1100℃を越え
る温度で加熱し、発生するぶつ化水素及び/又は塩化水
素をアルカリ溶液に捕集することを特徴とするものであ
る。
(Means for Solving the Problems) The method for extracting fluorine and/or chlorine of the present invention is a method for extracting fluorine and/or chlorine from an inorganic substance, in which a reaction accelerator is mixed with an inorganic substance, It is characterized by heating at a temperature exceeding 1100° C. and collecting generated hydrogen fluoride and/or hydrogen chloride in an alkaline solution.

(作 用) 上述した構成において、抽出すべき無機物と反応促進剤
との反応温度を1100℃を越えた従来よりも高い温度
に設定することにより、従来の1100℃以下の反応温
度では完全には抽出できなかったアルミニウムやマグネ
シウムのぶつ化物及び/又は塩化物を含むけい酸塩やア
ルミナ中のふっ素及び/又は塩素を完全に抽出分離でき
ることを見出したことによる。アルミニウム、マグネシ
ウムはふっ素及び/又は塩素との結合力が強く、加熱温
度を高くすることによって、それらの結合を分解するこ
とができ、ぶつ化水素及び/又は塩化水素として抽出で
きる。
(Function) In the above-mentioned configuration, by setting the reaction temperature between the inorganic substance to be extracted and the reaction accelerator at a temperature higher than 1100°C than the conventional one, the conventional reaction temperature of 1100°C or lower can not be used completely. This is based on the discovery that it is possible to completely extract and separate fluorine and/or chlorine in silicates and alumina containing aluminum and magnesium fragments and/or chlorides, which could not be extracted. Aluminum and magnesium have strong bonds with fluorine and/or chlorine, and by increasing the heating temperature, these bonds can be decomposed and extracted as hydrogen fluoride and/or hydrogen chloride.

ここで、反応温度を1100 ’Cを越えた温度と規定
したのは、1100’Cを越えることにより、後述する
実施例から明らかなようにアルミニウム又はマグネシウ
ムのぶつ化物及び/又は塩化物を含むけい酸塩やアルミ
ナ中のふっ素及び/又は塩素も完全に抽出分離できるた
めである。なお、実使用にあたっては、反応管の材質が
透明石英ガラスであること等の制約をうけ、加熱温度は
1200〜1300’Cであると好ましい。
Here, the reason why the reaction temperature was specified as a temperature exceeding 1100'C is that by exceeding 1100'C, silicon containing aluminium or magnesium chloride and/or This is because fluorine and/or chlorine in acid salts and alumina can be completely extracted and separated. In actual use, the heating temperature is preferably 1200 to 1300'C, subject to restrictions such as the fact that the material of the reaction tube is transparent quartz glass.

なお、反応促進剤としては、従来から公知のU3011
+ WOi+ V2O5+ (X −A jl! 20
31 Fe2O3等のいずれでも使用できるが、取扱い
等の点からはFe2O3の使用が好ましい。
In addition, as a reaction accelerator, conventionally known U3011
+ WOi+ V2O5+ (X -A jl! 20
31 Fe2O3 and the like can be used, but from the viewpoint of handling etc., it is preferable to use Fe2O3.

(実施例) 第1図は本発明の抽出方法を実施する装置の一構成を示
す図である。第1図において、フラスコ1、マントルヒ
ータ2、導入ロート(コック付)3、コック4により構
成した蒸気供給装置5と、電気炉6内に設置され一端に
試料挿入ロアを有するとともに他端に冷却管8を有する
透明石英ガラス製の反応管9とから、本発明の抽出方法
を実施する装置が構成されている。
(Example) FIG. 1 is a diagram showing the configuration of an apparatus for carrying out the extraction method of the present invention. In Fig. 1, there is shown a steam supply device 5 consisting of a flask 1, a mantle heater 2, an introduction funnel (with a cock) 3, and a cock 4, and an electric furnace 6, which is installed in an electric furnace 6 and has a sample insertion lower at one end and cooling at the other end. A reaction tube 9 made of transparent quartz glass having a tube 8 constitutes an apparatus for carrying out the extraction method of the present invention.

上述した装置によりふっ素及び/又は塩素の抽出を実施
する場合は、以下のようになる。まず、抽出すべき無機
物と酸化第二鉄やα−アルミナ等の反応促進剤の混合物
を白金ボートに載せ、試料挿入ロアから反応管9内に挿
入し、試料挿入ロアを塞ぐ。次に、コック4を閉じ、フ
ラスコ1で発生した水蒸気を反応管9内に流しながら、
電気炉6により反応管9内の無機物および反応促進剤の
温度を1100“Cを越える所定の温度に保持する。
When extracting fluorine and/or chlorine using the above-mentioned apparatus, the procedure is as follows. First, a mixture of an inorganic substance to be extracted and a reaction accelerator such as ferric oxide or α-alumina is placed on a platinum boat, inserted into the reaction tube 9 through the sample insertion lower, and the sample insertion lower is closed. Next, the cock 4 is closed, and while the water vapor generated in the flask 1 is flowing into the reaction tube 9,
The temperature of the inorganic substance and reaction promoter in the reaction tube 9 is maintained at a predetermined temperature exceeding 1100"C by the electric furnace 6.

すると、無機物と反応促進剤とが反応してぶつ化水素及
び/又は塩化水素が発生し、冷却管8により留出させ、
アルカリ溶液に捕集することができる。
Then, the inorganic substance and the reaction accelerator react to generate hydrogen fluoride and/or hydrogen chloride, which is distilled out through the cooling pipe 8.
Can be collected in alkaline solution.

抽出分離されたふっ化水素、塩化水素は、公知のイオン
クロマトグラフ法や吸光光度法等により定量され、ふっ
素及び/又は塩素の定量分析が可能となる。
The extracted and separated hydrogen fluoride and hydrogen chloride are quantified by known ion chromatography, spectrophotometry, etc., making it possible to quantitatively analyze fluorine and/or chlorine.

以下、本発明の方法によりふっ素及び/又は塩素を抽出
分離してイオンクロマトグラフ法により分析する方法に
ついて説明する。
Hereinafter, a method of extracting and separating fluorine and/or chlorine by the method of the present invention and analyzing it by ion chromatography will be explained.

なお、イオンクロマトグラフ法によりふっ素及び/又は
塩素を定量する場合は、ナトリウムイオンが妨害となる
ので捕集に用いる水酸化ナトリウム溶液は、ふっ素及び
/又は塩素の捕集後において大過剰とならない程度の濃
度が好ましい。具体的には、捕集後の水酸化ナトリウム
濃度は0.1 g/100dが好ましく、0.025 
g/100 mR,がより好ましい。
In addition, when quantifying fluorine and/or chlorine by ion chromatography, the sodium hydroxide solution used for collection should be adjusted to an extent that does not result in a large excess after collecting fluorine and/or chlorine, since sodium ions will interfere. A concentration of is preferred. Specifically, the sodium hydroxide concentration after collection is preferably 0.1 g/100d, and 0.025
g/100 mR, is more preferred.

16  試薬および装置 1.1.試薬 ことわりのない限りJIS試薬試薬特売
品いた。
16 Reagents and Equipment 1.1. Reagents Unless otherwise specified, JIS reagents are on sale.

(1)水酸化ナトリウム溶液(5−ハχ)(2)標準ふ
っ素溶液(10kgF/蔵):105℃で2時間乾燥し
、デシケータ−で放冷したぶつ化ナトリウム2.210
0.g  を水に溶かし、11とし、ポリエチレン容器
に保存する。使用の都度、この溶液20m!を水で薄め
て22とする。
(1) Sodium hydroxide solution (5-Haχ) (2) Standard fluorine solution (10 kgF/store): Sodium fluoride 2.210 dried at 105°C for 2 hours and left to cool in a desiccator
0. Dissolve g in water to make 11 and store in a polyethylene container. 20ml of this solution each time you use it! Dilute with water to make 22.

(3)標準塩素溶液(10μg /d)  : 105
℃で2時間乾燥し、デシケータ−で放冷した塩化ナトリ
ウム1.6489 gを水に溶かし、II!、とし、ポ
リエチレン容器に保存する。使用の都度、この溶液20
m1を水で薄めて21とする。
(3) Standard chlorine solution (10μg/d): 105
1.6489 g of sodium chloride, which had been dried at ℃ for 2 hours and left to cool in a desiccator, was dissolved in water, and II! , and store in a polyethylene container. 20 minutes of this solution before each use.
Dilute m1 with water to make 21.

(4)溶離液(1,OmM/Na)ICOz溶液)二炭
酸水素ナトリウム0.050 gを水に溶かして11と
する。
(4) Eluent (1, OmM/Na) ICOz solution) Dissolve 0.050 g of sodium bicarbonate in water to obtain 11.

(5)酸化第二鉄;純度99.9%のγ−Fe2O3を
使用する。
(5) Ferric oxide: γ-Fe2O3 with a purity of 99.9% is used.

(6)アルミナ標準試料:住友化学工業(株)製、保証
値S−2;51±5μg F/g、 S−4; 220
±16μg P/gである。
(6) Alumina standard sample: manufactured by Sumitomo Chemical Co., Ltd., guaranteed value S-2; 51 ± 5 μg F/g, S-4; 220
±16 μg P/g.

(7)セメント標準試料:  NBS SRM 633
ポルトランドセメント、保証値F O,08%。
(7) Cement standard sample: NBS SRM 633
Portland cement, guaranteed value FO, 08%.

(8)霞石閃長岩標準試料: 5ABS SARM3 
LUSAVRITE保証値 Cl3 0.12% 1.2.装 置 (1)  イオンクロマトグラフ (2)電気炉 2、定量操作 (1)試料 0.220 gと酸化第二鉄0.440 
gをとり、めのう乳鉢で混合し、その0.600 gを
とり、白金ポートに移す。
(8) Nepheline syenite standard sample: 5ABS SARM3
LUSAVRITE guaranteed value Cl3 0.12% 1.2. Apparatus (1) Ion chromatograph (2) Electric furnace 2, quantitative operation (1) Sample 0.220 g and ferric oxide 0.440 g
Mix in an agate mortar, then take 0.600 g and transfer to a platinum port.

(2)受器(250++f!メスフラスコ)に水約5m
fl。
(2) Approximately 5 m of water in the receiver (250++f! volumetric flask)
fl.

水酸化ナトリウム溶液0 、5 mlを入れ、冷却器の
先端を液中に浸したのち、白金ボートを炉心管中央部ま
で入れる。
Pour 0.5 ml of sodium hydroxide solution, immerse the tip of the cooler in the solution, and then insert the platinum boat up to the center of the core tube.

(3)電気炉を指定の温度に調節後、留出速度を毎分8
〜9 mlに調整して水蒸気を発生させ、留出液量が2
50++4!になるまで捕集する。
(3) After adjusting the electric furnace to the specified temperature, reduce the distillation rate to 8/min.
Adjust the volume to ~9 ml and generate water vapor until the distillate volume reaches 2.
50++4! Collect until

(4)留出液の一部を取り、イオンクロマトグラフによ
りふっ素イオン量を求める。
(4) Take a portion of the distillate and determine the amount of fluorine ions using an ion chromatograph.

(5)空試験は酸化第二鉄0.400 gを白金ボード
に取り、(2)〜(4)の操作に従い、指定の温度で、
250 mlになるまで捕集する。
(5) For a blank test, place 0.400 g of ferric oxide on a platinum board, follow steps (2) to (4), and test at the specified temperature.
Collect up to 250 ml.

検量線の作成 標準ふっ素溶液及び標準塩素溶液を0〜
50mfl、ふっ素及び塩素として(O〜500μg)
を250 mlのメスフラスコに段階的にとり、水酸化
ナトリウム溶液0.5−を加え水で薄める。
Creating a calibration curve Standard fluorine solution and standard chlorine solution from 0 to
50mfl, as fluorine and chlorine (O~500μg)
Stepwise take the solution into a 250 ml volumetric flask, add 0.5-ml of sodium hydroxide solution, and dilute with water.

指定の温度ニジリカーマグネシア系鉱物、セメント及び
アルミナは1300℃1それ以外は1200℃0 3、実験および結果 3.1パイロハイトロリシスにおける加熱温度の影響 各種けい酸塩及びアルミナ原料を用いて加熱温度を95
0〜1300’Cまで変化させてふっ素及び/又は塩素
を定量し影響を調べた。結果を第1表(a)、(b)に
示す。加熱温度以外の条件はこの定量操作に従った。
Specified temperature Nijirikar Magnesia minerals, cement and alumina: 1300℃ 1 Others: 1200℃ 0 3. Experiments and results 3.1 Effect of heating temperature in pyrohydrolysis Heating using various silicate and alumina raw materials temperature to 95
Fluorine and/or chlorine were determined by varying the temperature from 0 to 1300'C to examine their effects. The results are shown in Tables 1 (a) and (b). Conditions other than heating temperature followed this quantitative operation.

第1表(a)、(b)の結果から、シリカマグネシア系
鉱物、セメント及びアルミナ中のふっ素の抽出は950
℃では不完全であるが1300℃で最高値でかつ、はぼ
一定値となり、それ以外は1200’Cで一定値となっ
た。
From the results in Table 1 (a) and (b), the extraction of fluorine from silica-magnesia minerals, cement, and alumina is 950.
At 1300°C, the value was the highest and almost constant, although it was incomplete, and at 1200'C the other values were constant.

3.2留出液量 ふっ素定量値に対し、加熱温度の影響が大きい第1表(
a)中のシリカ−マグネシア系鉱物−2を用いて、20
0 mlまでの留出液量及び200瀬以上は50滅毎の
留出液量とふっ素定量値の関係を調べた結果を第2表に
示す。
3.2 Distillate Volume Table 1 (Table 1) where the heating temperature has a large effect on the fluorine quantitative value
a) Using the silica-magnesia mineral-2 in
Table 2 shows the results of investigating the relationship between the amount of distillate up to 0 ml and the amount of distillate every 50 ml and the fluorine quantitative value for 200 ml or more.

第 表 第2表の結果からシリカ−マグネシア鉱物の場合は13
00℃で250 ml留出までで抽出が終了した。これ
に対し、パイロハイトロリシス温度が750℃の場合は
留出液量を450 mlと増しても回収率は46.1%
である。1050″Cでも留出液量が250mfでは回
収率が94.4%であり、なおふっ素の抽出が続いてい
る。
From the results in Table 2, in the case of silica-magnesia mineral, it is 13
The extraction was completed when 250 ml was distilled at 00°C. On the other hand, when the pyrohydrolysis temperature is 750°C, the recovery rate is 46.1% even if the distillate volume is increased to 450 ml.
It is. Even at 1050″C, the recovery rate was 94.4% when the distillate volume was 250mf, and fluorine extraction continued.

3.3実際試料の繰り返し分析結果 第3表は本性によるふっ素定量値である。第3表におい
て、アルミナ、セメントは1300℃で、陶磁器−1は
1200℃でパイロハイトロリシスを実施した後、イオ
ンクロマトグラフ法によりふっ素を定量した。
3.3 Results of repeated analysis of actual samples Table 3 shows the quantitative values of fluorine according to its nature. In Table 3, alumina and cement were subjected to pyrohydrolysis at 1300°C, and ceramic-1 was subjected to pyrohydrolysis at 1200°C, and then fluorine was determined by ion chromatography.

本発明は上述した実施例にのみ限定されるものではなく
、幾多の変形、変更が可能である。例えば、上述した実
施例では反応促進剤として酸化第二鉄(r  F ez
ch)を使用したが、他の公知の反応促進剤例えばα−
アルミナ、 U:1O11等でも同様な本発明の効果を
得ることができることはいうまでもない。
The present invention is not limited only to the embodiments described above, and numerous modifications and changes are possible. For example, in the embodiments described above, ferric oxide (r F ez
ch) was used, but other known reaction accelerators such as α-
It goes without saying that the same effects of the present invention can be obtained with alumina, U:1O11, etc.

(発明の効果) 以上の説明から明らかなように、本発明のふっ素及び/
又は塩素の抽出方法によれば、試料と反応促進剤を11
00’Cを越える温度で反応させることにより、無機物
質のうち従来法ではふっ素及び/又は塩素の抽出が難し
かったけい酸塩やアルミナ中のふっ素及び/又は塩素を
完全に抽出分離することが可能となり、その結果正確な
ふっ素及び/又は塩素の定量を実施することができる。
(Effect of the invention) As is clear from the above explanation, the fluorine and/or
Or, according to the chlorine extraction method, the sample and reaction accelerator are separated into 11
By reacting at temperatures exceeding 00'C, it is possible to completely extract and separate fluorine and/or chlorine from silicates and alumina, which were difficult to extract using conventional methods among inorganic substances. As a result, accurate determination of fluorine and/or chlorine can be performed.

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

第1図は本発明のふっ素の抽出方法を実施する装置の一
構成を示す図である。 1・・・フラスコ     2・・・マントルヒータ・
・・導入ロート(コンク付) ・・・コック ・・・藤気供給装置 ・・・試料挿入口 ・・・反応管 6・・・電気炉 8・・・冷却管
FIG. 1 is a diagram showing the configuration of an apparatus for implementing the fluorine extraction method of the present invention. 1...Flask 2...Mantle heater・
...Introduction funnel (with conch) ...Cook ...Wisteria air supply device ...Sample insertion port ...Reaction tube 6 ...Electric furnace 8 ...Cooling pipe

Claims (1)

【特許請求の範囲】[Claims] 1、無機物中のふっ素及び/又は塩素を抽出する方法で
あって、無機物に反応促進剤を混合して水蒸気中、11
00℃を越える温度で加熱し、発生したフッ化水素及び
/又は塩化水素をアルカリ溶液に捕集することを特徴と
する無機物中のふっ素及び/又は塩素の抽出方法。
1. A method for extracting fluorine and/or chlorine from inorganic substances, in which a reaction accelerator is mixed with the inorganic substance and 11
A method for extracting fluorine and/or chlorine from inorganic substances, which comprises heating at a temperature exceeding 00°C and collecting generated hydrogen fluoride and/or hydrogen chloride in an alkaline solution.
JP63242542A 1988-09-29 1988-09-29 Method for extracting fluorine and / or chlorine from inorganic matter Expired - Lifetime JPH0617206B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP63242542A JPH0617206B2 (en) 1988-09-29 1988-09-29 Method for extracting fluorine and / or chlorine from inorganic matter

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP63242542A JPH0617206B2 (en) 1988-09-29 1988-09-29 Method for extracting fluorine and / or chlorine from inorganic matter

Publications (2)

Publication Number Publication Date
JPH0292802A true JPH0292802A (en) 1990-04-03
JPH0617206B2 JPH0617206B2 (en) 1994-03-09

Family

ID=17090658

Family Applications (1)

Application Number Title Priority Date Filing Date
JP63242542A Expired - Lifetime JPH0617206B2 (en) 1988-09-29 1988-09-29 Method for extracting fluorine and / or chlorine from inorganic matter

Country Status (1)

Country Link
JP (1) JPH0617206B2 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007101504A (en) * 2005-10-07 2007-04-19 Kagoshima Univ Quantitative determination of fluorine in coal
US8593830B2 (en) 2010-06-29 2013-11-26 Maxim Integrated Products, Inc. Reverse current limit protection for active clamp converters
US8638170B2 (en) 2002-01-24 2014-01-28 Maxim Integrated Products, Inc. Single supply headphone driver/charge pump combination

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5542930A (en) * 1978-09-19 1980-03-26 Mitsubishi Chem Ind Method of coating sheet on house

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5542930A (en) * 1978-09-19 1980-03-26 Mitsubishi Chem Ind Method of coating sheet on house

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8638170B2 (en) 2002-01-24 2014-01-28 Maxim Integrated Products, Inc. Single supply headphone driver/charge pump combination
JP2007101504A (en) * 2005-10-07 2007-04-19 Kagoshima Univ Quantitative determination of fluorine in coal
US8593830B2 (en) 2010-06-29 2013-11-26 Maxim Integrated Products, Inc. Reverse current limit protection for active clamp converters

Also Published As

Publication number Publication date
JPH0617206B2 (en) 1994-03-09

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