JPH01141803A - Production of iodine monochloride - Google Patents

Production of iodine monochloride

Info

Publication number
JPH01141803A
JPH01141803A JP29776787A JP29776787A JPH01141803A JP H01141803 A JPH01141803 A JP H01141803A JP 29776787 A JP29776787 A JP 29776787A JP 29776787 A JP29776787 A JP 29776787A JP H01141803 A JPH01141803 A JP H01141803A
Authority
JP
Japan
Prior art keywords
iodine
chlorine
monochloride
iodine monochloride
trichloride
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
JP29776787A
Other languages
Japanese (ja)
Other versions
JPH0735243B2 (en
Inventor
Atsushi Utsunomiya
宇都宮 淳
Yoshinori Tanaka
良典 田中
Kazuo Oguri
小栗 一男
Ryoichi Seki
亮一 関
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.)
Mitsui Toatsu Chemicals Inc
Original Assignee
Mitsui Toatsu Chemicals Inc
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 Mitsui Toatsu Chemicals Inc filed Critical Mitsui Toatsu Chemicals Inc
Priority to JP62297767A priority Critical patent/JPH0735243B2/en
Publication of JPH01141803A publication Critical patent/JPH01141803A/en
Publication of JPH0735243B2 publication Critical patent/JPH0735243B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B7/00Halogens; Halogen acids
    • C01B7/24Inter-halogen compounds

Abstract

PURPOSE:To produce a product of high, constant purity with little loss of chlorine when iodine and chlorine are brought into a reaction to produce iodine monochloride by absorbing excess chlorine in liq. iodine monochloride and adding solid iodine. CONSTITUTION:When iodine monochloride is produced with gaseous chlorine and solid iodine, excess chlorine is blown into liq. iodine monochloride. The liq. iodine monochloride reacts readily with the chlorine and becomes iodine trichloride. After part of the liq. iodine monochloride is converted into iodine trichloride, solid iodine is added. The iodine trichloride is rapidly converted into iodine monochloride and uniform iodine monochloride is obtd. in the liquefied state. The loss of chlorine is hardly caused and the amt. of iodine required can be calculated from the amt. of chlorine blown, so high purity iodine monochloride can be produced and distillation or other refining is made unnecessary.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、有機の沃素化剤、酸化剤として、また油脂の
沃素価の測定に盛んに用いられている一塩化沃素の製造
方法に関する。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention relates to a method for producing iodine monochloride, which is widely used as an organic iodinating agent, an oxidizing agent, and for measuring the iodine value of fats and oils.

〔従来の技術および発明が解決しようとする問題点〕[Problems to be solved by conventional technology and invention]

沃素と塩素を反応させて、一塩化沃素を製造することは
公知である。具体的な例として、■固体の沃素上に、乾
燥した気体の塩素を流す方法(イノガニツク・センセシ
ス(inorganic 5ynthesis )Vo
l、9.130〜133)、■沃素を、例えば四塩化炭
素、クロロホルム、メタノール、酢酸等の有機溶媒に溶
解、もしくは懸濁させて、気体の塩素を流す方法(西独
特許1961289) 、■液体塩素中に沃素を添加、
もしくは沃素に液体塩素を添加する方法(イノガニツク
・センセシス(inorganicsynthesis
)  Vol、1 +165〜167)がある、その他
に塩素を用いない一塩化沃素の製造方法としては、塩酸
ガスと沃素を用いる方法や、沃化カリウムと沃素酸塩(
沃素酸ナトリウム、沃素酸カリウム)を用いる方法(ジ
ャーナル・オブ・ゼ・アメリカン・ケミカル・ソサイア
ティ(Journal of theAmerican
 Chemical 5ociaty ) Vol、7
8.3210〜3216)が知られているが、沃化水素
酸の副生、原料が高価等の理由のために、塩素をmいる
方法と比べて工業的生産面では有用でない。
It is known to react iodine and chlorine to produce iodine monochloride. As a specific example, ■ a method of flowing dry gaseous chlorine over solid iodine (inorganic senthesis Vo.
l, 9.130-133), ■ A method of dissolving or suspending iodine in an organic solvent such as carbon tetrachloride, chloroform, methanol, acetic acid, etc., and flowing gaseous chlorine (West German Patent No. 1961289), ■ Liquid Adding iodine to chlorine,
Alternatively, a method of adding liquid chlorine to iodine (inorganic synthesis)
) Vol, 1 +165-167).Other methods for producing iodine monochloride that do not use chlorine include methods using hydrochloric acid gas and iodine, and methods using potassium iodide and iodate salts (
method using sodium iodate, potassium iodate) (Journal of the American Chemical Society)
Chemical 5ociety) Vol, 7
8.3210 to 3216) are known, but they are not as useful in industrial production as the method using chlorine because of the by-product of hydriodic acid and the high cost of raw materials.

沃素と塩素を反応させる方法のうち、■は塩素の溶媒に
対する溶解度を高めるために、反応温度を比較的低温に
保たなくてはならず、溶解度以上の塩素は未反応のまま
、反応系外へと流出してしまう、そのため塩素量からの
反応の制御が困難となる、また一定の溶媒を用いるため
に、他の溶媒への転用が困難になり、汎用性という面で
は好ましくない。■の方法は、液体塩素を用いるため、
加圧操作もしくは塩素の沸点以下の温度が必要となり、
製造装置が特殊なものとなる。
Among the methods for reacting iodine and chlorine, method (2) requires keeping the reaction temperature relatively low in order to increase the solubility of chlorine in the solvent, and chlorine exceeding the solubility remains unreacted and is removed from the reaction system. This makes it difficult to control the reaction based on the amount of chlorine, and since a certain solvent is used, it is difficult to use it for other solvents, which is not desirable in terms of versatility. Method ■ uses liquid chlorine, so
Pressurized operation or a temperature below the boiling point of chlorine is required.
The manufacturing equipment will be special.

沃素と塩素の反応は、極めて急速に発熱を伴いながら進
行する。そのために気体と固体でも十分に一塩化沃素の
製造ができる。しかし■の方法では、固体の沃素上に乾
燥した塩素を流し、反応を行わせるため、一定量以上の
塩素は消費され難くなる。なぜならば沃素の塩素化は、
一塩化沃素の段階で止まることなく、さらに塩素化が進
み、固体の三塩化沃素が形成され、完全に液化していな
い沃素と一塩化沃素の混合物上に固体である三塩化沃素
層を作る。そのために未反応の沃素の塩素化を阻害する
。この状態になると流入した塩素量による一塩化沃素の
純度の調整が困難となる。
The reaction between iodine and chlorine proceeds extremely rapidly and exothermically. For this reason, iodine monochloride can be sufficiently produced in both gas and solid form. However, in method (2), dry chlorine is poured over solid iodine to cause the reaction to occur, making it difficult for more than a certain amount of chlorine to be consumed. Because chlorination of iodine is
Without stopping at the iodine monochloride stage, chlorination proceeds further to form solid iodine trichloride, creating a solid iodine trichloride layer on the mixture of iodine and iodine monochloride that has not completely liquefied. Therefore, chlorination of unreacted iodine is inhibited. In this state, it becomes difficult to adjust the purity of iodine monochloride depending on the amount of chlorine introduced.

一塩化沃素の製造上、高純度で、かつ一定純度で得るこ
とは、非常に重要である。流入した塩素量が少なすぎる
と、沃素過剰の状態を生じ、多すぎると、塩素過剰とな
り、容易に三塩化沃素を生じる。特に塩素過剰の状態で
生じる三塩化沃素の存在は、一塩化沃素を沃素化剤とし
て用いる場合には、多大な弊害を生じる。なぜならば三
塩化沃素は、塩素化剤として、また一塩化沃素よりさら
に強力な酸化剤として働くためである。
In the production of iodine monochloride, it is very important to obtain it in high purity and at a constant purity. If the amount of chlorine introduced is too small, an excess of iodine will occur; if it is too large, an excess of chlorine will occur, easily producing iodine trichloride. In particular, the presence of iodine trichloride produced in a state of excess chlorine causes great harm when iodine monochloride is used as an iodizing agent. This is because iodine trichloride acts as a chlorinating agent and as an oxidizing agent even stronger than iodine monochloride.

そこで、高純度かつ一定純度の一塩化沃素を得るために
、蒸留もしくは高純度の一塩化沃素を溶媒とした再結晶
を行わなければならず、操作上好ましいとはいえない。
Therefore, in order to obtain iodine monochloride of high purity and constant purity, it is necessary to perform distillation or recrystallization using high purity iodine monochloride as a solvent, which is not convenient from an operational point of view.

また昇華性の高い三塩化沃素は、容易に未反応の塩素に
運ばれて、反応系外へ流出し、沃素及び塩素の損失を生
じる。
Furthermore, iodine trichloride, which has a high sublimability, is easily carried by unreacted chlorine and flows out of the reaction system, resulting in loss of iodine and chlorine.

〔問題点を解決するための手段および作用]本発明者ら
は、上記問題点を解決するために鋭意検討した結果、一
塩化沃素に過剰の塩素を流入し、一部、三塩化沃素に変
え、その後に固体の沃素を投入することにより本発明の
目的を達成できることを見出し本発明を完成させるに至
った。
[Means and effects for solving the problems] As a result of intensive studies to solve the above problems, the inventors of the present invention have found that by injecting excess chlorine into iodine monochloride, some of it is converted to iodine trichloride. The present inventors discovered that the object of the present invention could be achieved by subsequently introducing solid iodine, leading to the completion of the present invention.

即ち本発明は、気体の塩素と固体の沃素とからなる、一
塩化沃素の製造において、液体の一塩化沃素に過剰の塩
素を吸収させた後、固体の沃素を添加することを特徴と
する一塩化沃素の製造方法である。
That is, the present invention provides a method for producing iodine monochloride consisting of gaseous chlorine and solid iodine, which is characterized in that after excess chlorine is absorbed into liquid iodine monochloride, solid iodine is added. This is a method for producing iodine chloride.

一塩化沃素と塩素は容易に反応して、三塩化沃素となる
。前述したように一塩化沃素中に三塩化沃素が存在する
と、一塩化沃素使用時に弊害を化シル。シカシ、液体の
一塩化沃素中では、三塩化沃素は均一に存在し、固体の
沃素の添加に′より、速やかに一塩化沃素となる。この
場合、三塩化沃素1モルが沃素分子1モルにより、3モ
ルの一塩化沃素となる。そのために、一塩化沃素の50
%を三塩化沃素にし、沃素を添加するだけで初期仕込み
の倍量の一塩化沃素を容易に得ることができる。
Iodine monochloride and chlorine easily react to form iodine trichloride. As mentioned above, the presence of iodine trichloride in iodine monochloride causes adverse effects when using iodine monochloride. In liquid iodine monochloride, iodine trichloride exists uniformly, and upon addition of solid iodine, it quickly becomes iodine monochloride. In this case, 1 mole of iodine trichloride becomes 3 moles of iodine monochloride due to 1 mole of iodine molecules. For this purpose, 50% of iodine monochloride
% to iodine trichloride, and by simply adding iodine, it is possible to easily obtain twice the amount of iodine monochloride as initially charged.

また攪拌可能な液体の一塩化沃素中に塩素を三塩化沃素
の形で吸収させ、沃素を投入することにより、液化した
状態のままで均一な一塩化沃素を得ることができる。
Further, by absorbing chlorine in the form of iodine trichloride into a stirrable liquid iodine monochloride and adding iodine, uniform iodine monochloride can be obtained in a liquefied state.

具体的には、一塩化沃素が液体として存在しうる濃度、
望ましくは50%以上の一塩化沃素に塩素を流入する。
Specifically, the concentration at which iodine monochloride can exist as a liquid,
Preferably, 50% or more of iodine monochloride is injected with chlorine.

流入する際の温度は一塩化沃素が液体として存在しろる
温度、望ましくは20〜40°Cの範囲で行う。適当な
乾燥剤、例えば硫酸中を通過させた塩素を適当量攪拌し
つつ吸収させ、一塩化沃素の一部を三塩化沃素とする。
The temperature at which the mixture is introduced is such that iodine monochloride exists as a liquid, preferably in the range of 20 to 40°C. An appropriate amount of chlorine passed through a suitable drying agent, such as sulfuric acid, is absorbed while stirring to convert a portion of iodine monochloride into iodine trichloride.

この三塩化沃素と一塩化沃素の混合物中に塩素量から計
算された沃素量を添加し、一塩化沃素を調整する。この
方法による一塩化沃素の製造では塩素の損失が殆どなく
、流入した塩素量から沃素の必要量が計算できるため、
沃素添加後に高純度の一塩化沃素を得ることができる。
An amount of iodine calculated from the amount of chlorine is added to the mixture of iodine trichloride and iodine monochloride to adjust the amount of iodine monochloride. In the production of iodine monochloride using this method, there is almost no loss of chlorine, and the required amount of iodine can be calculated from the amount of chlorine flowing in.
High purity iodine monochloride can be obtained after iodine addition.

そのため通常、沃素と塩素による一塩化沃素の製造の際
に必要とされる蒸留その他の精製が不要となり、工程の
簡略化を行うことができる。さらに製造後の一塩化沃素
を次回の反応に必要な量だけ反応器に残すことにより連
続的に一塩化沃素の製造を行うことができる。
Therefore, distillation and other purifications that are normally required when producing iodine monochloride using iodine and chlorine are not necessary, and the process can be simplified. Further, by leaving only the amount of iodine monochloride required for the next reaction in the reactor after production, iodine monochloride can be produced continuously.

〔実施例] 以下、実施例により本発明を具体的に説明する。〔Example] Hereinafter, the present invention will be specifically explained with reference to Examples.

実施例1 攪拌機付の51の反応器に徐々に固体の沃素を添加しつ
つ、乾燥した塩素を導入し、粗一塩化沃素6.35Kg
を得た。粗一塩化沃素は27〜40°Cにおいて液体と
して存在した。沃素滴定より、一塩化沃素の純度は90
.3%であった。この一塩化沃素を27〜40℃に保温
しながら、更に乾燥した塩素を1.56Kg(22,O
mol)流入し、塩素過剰状態とした。過剰に流入した
塩素量から計算された、必要量の沃素5.08Kg(2
0,Omol)を反応器に投入し、1時間攪拌した。沃
素滴定より、純度99.8%の高純度一塩化沃素を13
.0X得ることができた。沃素と塩素の損失は2%以下
であった。
Example 1 While gradually adding solid iodine to a 51 reactor equipped with a stirrer, dry chlorine was introduced to produce 6.35 kg of crude iodine monochloride.
I got it. Crude iodine monochloride existed as a liquid at 27-40°C. According to iodometric titration, the purity of iodine monochloride is 90.
.. It was 3%. While keeping this iodine monochloride at a temperature of 27 to 40°C, 1.56 kg of dried chlorine (22,0
mol) to create an excess chlorine state. The required amount of iodine, calculated from the excess amount of chlorine, was 5.08 kg (2
0,0mol) was charged into the reactor and stirred for 1 hour. Highly purified iodine monochloride with a purity of 99.8% was determined by iodometric titration.
.. I was able to get 0X. The loss of iodine and chlorine was less than 2%.

実施例2 実施例1と同様の方法により、粗一塩化沃素6.12K
gを得た。沃素滴定より、一塩化沃素の純度は74.0
%であった。この粗一塩化沃素に乾燥した塩素1.79
Kg(25,2mol)を流入し、塩素過剰状態とした
。実施例1と同様に沃素5.08Kg(20,0+wo
l)を投入した結果、99.7%の高純度の一塩化沃素
13.0Kgを得た。沃素と塩素の損失は2%以下であ
った。
Example 2 Crude iodine monochloride 6.12K was prepared in the same manner as in Example 1.
I got g. According to iodometric titration, the purity of iodine monochloride is 74.0.
%Met. 1.79 chlorine dried to this crude iodine monochloride
Kg (25.2 mol) was introduced to create an excess chlorine state. As in Example 1, 5.08 kg of iodine (20,0+wo
1), 13.0 kg of iodine monochloride with a high purity of 99.7% was obtained. The loss of iodine and chlorine was less than 2%.

実施例3 実施例2により得られた、高純度の一塩化沃素6.5K
g(40mol)を51の反応器に残した。これに乾燥
した塩素1.42Kg(20mol)を流入し、実施例
2と同様に沃素5.08Kg(20mol)を投入した
ところ、純度99.7Xの一塩化沃素13.00Kgを
得ることができた。更に一塩化沃素6.5に、を釜に残
し、5回同様の操作を行ったところ、純度99,6〜9
9.9%の一塩化沃素を得ることができた。5回繰り返
した場合の沃素と塩素の損失は2%であった。
Example 3 High purity iodine monochloride 6.5K obtained in Example 2
g (40 mol) remained in reactor 51. When 1.42 kg (20 mol) of dried chlorine was introduced into this and 5.08 kg (20 mol) of iodine was added in the same manner as in Example 2, 13.00 kg of iodine monochloride with a purity of 99.7X could be obtained. . Furthermore, when 6.5% of iodine monochloride was left in the pot and the same operation was repeated 5 times, the purity was 99.6-9.
It was possible to obtain 9.9% iodine monochloride. The loss of iodine and chlorine when repeated five times was 2%.

〔発明の効果〕〔Effect of the invention〕

本発明の方法によれば、塩素の損失がほとんどな(、流
入した塩素量から沃素の必要量が計算できるため、沃素
添加後に高純度の一塩化沃素を製造することができる。
According to the method of the present invention, there is almost no loss of chlorine (and the required amount of iodine can be calculated from the amount of chlorine introduced, so high purity iodine monochloride can be produced after adding iodine.

また蒸留、その他の精製が不要となり、工程の簡略化が
できる。
Further, distillation and other purification are not required, and the process can be simplified.

特許出願人 三井東圧化学株式会社Patent applicant: Mitsui Toatsu Chemical Co., Ltd.

Claims (1)

【特許請求の範囲】[Claims] 1 気体の塩素と固体の沃素とからなる、一塩化沃素の
製造において、液体の一塩化沃素に過剰の塩素を吸収さ
せた後、固体の沃素を添加することを特徴とする一塩化
沃素の製造方法。
1 Production of iodine monochloride consisting of gaseous chlorine and solid iodine, characterized in that after excess chlorine is absorbed into liquid iodine monochloride, solid iodine is added. Method.
JP62297767A 1987-11-27 1987-11-27 Method for producing iodine monochloride Expired - Lifetime JPH0735243B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP62297767A JPH0735243B2 (en) 1987-11-27 1987-11-27 Method for producing iodine monochloride

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP62297767A JPH0735243B2 (en) 1987-11-27 1987-11-27 Method for producing iodine monochloride

Publications (2)

Publication Number Publication Date
JPH01141803A true JPH01141803A (en) 1989-06-02
JPH0735243B2 JPH0735243B2 (en) 1995-04-19

Family

ID=17850912

Family Applications (1)

Application Number Title Priority Date Filing Date
JP62297767A Expired - Lifetime JPH0735243B2 (en) 1987-11-27 1987-11-27 Method for producing iodine monochloride

Country Status (1)

Country Link
JP (1) JPH0735243B2 (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2011003894A1 (en) 2009-07-07 2011-01-13 Bracco Imaging Spa Process for the preparation of a iodinating agent
JP2011236087A (en) * 2010-05-11 2011-11-24 Toho Earthtech Inc Method for producing iodine monochloride aqueous solution
US9193659B2 (en) 2008-02-20 2015-11-24 Bracco Imaging S.P.A. Process for the iodination of aromatic compounds
CN110577191A (en) * 2019-08-20 2019-12-17 中船重工(邯郸)派瑞特种气体有限公司 Method for directly preparing iodine monochloride from iodine-containing salt

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US9193659B2 (en) 2008-02-20 2015-11-24 Bracco Imaging S.P.A. Process for the iodination of aromatic compounds
WO2011003894A1 (en) 2009-07-07 2011-01-13 Bracco Imaging Spa Process for the preparation of a iodinating agent
JP2012532983A (en) * 2009-07-07 2012-12-20 ブラッコ・イメージング・ソシエタ・ペル・アチオニ Method for producing iodinating agent
US9157156B2 (en) 2009-07-07 2015-10-13 Bracco Imaging S.P.A. Process for the preparation of a iodinating agent
JP2011236087A (en) * 2010-05-11 2011-11-24 Toho Earthtech Inc Method for producing iodine monochloride aqueous solution
CN110577191A (en) * 2019-08-20 2019-12-17 中船重工(邯郸)派瑞特种气体有限公司 Method for directly preparing iodine monochloride from iodine-containing salt

Also Published As

Publication number Publication date
JPH0735243B2 (en) 1995-04-19

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