JPH0859205A - Production of hydroiodic acid - Google Patents

Production of hydroiodic acid

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Publication number
JPH0859205A
JPH0859205A JP19257394A JP19257394A JPH0859205A JP H0859205 A JPH0859205 A JP H0859205A JP 19257394 A JP19257394 A JP 19257394A JP 19257394 A JP19257394 A JP 19257394A JP H0859205 A JPH0859205 A JP H0859205A
Authority
JP
Japan
Prior art keywords
acid
iodine
reaction
solution
added
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
JP19257394A
Other languages
Japanese (ja)
Inventor
Sakaki Sasaki
佐々木  賢樹
Masahiro Omura
正弘 大村
Mitsuo Nakamura
光雄 中村
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 JP19257394A priority Critical patent/JPH0859205A/en
Publication of JPH0859205A publication Critical patent/JPH0859205A/en
Pending legal-status Critical Current

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Abstract

PURPOSE: To provide a method for producing hydroiodic acid in high conversion ratio of raw material iodine available even in production of highly concentrated hydroiodic acid, capable of extremely suppressing evaporation of raw material iodine during reaction. CONSTITUTION: Iodine is reacted with an aqueous solution of a reducing agent (e.g. phosphorous acid, hypophosphorous acid, pyrophosphoric acid, pyrophosphorous acid or isohypophosphoric acid) by continuously or intermittently adding iodine. After the reaction is over, hydroiodic acid is distilled from the reaction solution.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、ヨウ化水素酸の製造方
法に関する。ヨウ化水素酸は、各種ヨウ化物の合成原
料、医薬用中間体、又は還元剤として用いられる有用な
物質である。
TECHNICAL FIELD The present invention relates to a method for producing hydroiodic acid. Hydroiodic acid is a useful substance used as a raw material for synthesizing various iodides, a pharmaceutical intermediate, or a reducing agent.

【0002】[0002]

【従来の技術】ヨウ化水素の水溶液であるヨウ化水素酸
は、赤リンの懸濁液にヨウ素を加えるか、又はヨウ素の
懸濁液に硫化水素ガスを送入することで生成させること
ができるが、硫化水素は毒物であること、また赤リンは
危険物であり、かつ含有する不純物の影響を受けやすい
ことなどから、工業的には、通常、ヨウ素と水の混合液
あるいは懸濁液に、次亜リン酸などの還元剤を添加する
か、又はこれらの混合された液を加熱しながらヨウ素を
還元し、次いで、該反応液よりヨウ化水素酸を蒸留によ
り留出させて得るという方法が一般的に行なわれてい
る。
Hydroiodic acid, which is an aqueous solution of hydrogen iodide, can be produced by adding iodine to a suspension of red phosphorus or by feeding hydrogen sulfide gas into the suspension of iodine. However, since hydrogen sulfide is a poisonous substance, red phosphorus is a dangerous substance, and it is easily affected by impurities contained in it, industrially, it is usually a mixed solution or suspension of iodine and water. In addition, a reducing agent such as hypophosphorous acid is added, or iodine is reduced while heating a mixed solution of these, and then hydroiodic acid is distilled from the reaction solution by distillation. The method is commonly practiced.

【0003】しかし、従来より行なわれている上記した
製造方法においては、反応中にその液中よりヨウ素蒸気
が非常に発生しやすく、原料ヨウ素の損失を起こしやす
いという問題があり、その製造設備においても、有害な
ヨウ素の系外放散を防ぐために特別な除害設備が付帯さ
れるのが普通である。更に、還元反応時にあっては反応
溶液が急に発熱することが多く、これを制御することが
非常に困難であり、反応が暴走してしまうという危険性
をもはらんでいる。
However, in the above-mentioned conventional production method, there is a problem that iodine vapor is very likely to be generated from the liquid during the reaction, and iodine in the raw material is likely to be lost. However, special abatement equipment is usually attached to prevent harmful emission of iodine out of the system. Furthermore, during the reduction reaction, the reaction solution often generates abrupt heat, which is very difficult to control, and there is a risk that the reaction will run away.

【0004】また、ヨウ素を完全に水に溶解させた後に
還元剤を添加した場合には、上記したヨウ素蒸気の発
生、及び反応の暴走の危険性は緩和されるが、ヨウ素の
水に対する溶解度が非常に小さく(1.06g/リットル,
20℃)、容積効率が悪化する上、反応後の蒸留に際して
は大量の希薄なヨウ化水素酸が留出してしまい、高濃度
のヨウ化水素酸を得ることが非常に困難になるという欠
点が生ずる。
When the reducing agent is added after the iodine is completely dissolved in water, the above-mentioned risk of iodine vapor generation and reaction runaway is mitigated, but the solubility of iodine in water is reduced. Very small (1.06 g / l,
20 ° C), the volumetric efficiency deteriorates, and a large amount of dilute hydroiodic acid distills out during the distillation after the reaction, which makes it very difficult to obtain a high concentration of hydroiodic acid. Occurs.

【0005】[0005]

【発明が解決しようとする課題】本発明の目的は、ヨウ
化水素酸を製造するに際し、前述したような従来方法に
おける欠点のない製造方法を提供することである。すな
わち、反応中にヨウ素蒸気の発生することがなく、しか
も安全に高濃度のヨウ化水素酸を収率よく得られる製造
方法を提供することが目的である。
SUMMARY OF THE INVENTION It is an object of the present invention to provide a method for producing hydroiodic acid which does not have the drawbacks of the conventional methods described above. That is, it is an object to provide a production method in which iodine vapor is not generated during the reaction and a high concentration of hydroiodic acid can be safely obtained with a high yield.

【0006】[0006]

【課題を解決するための手段】上記の目的を達成するた
めに本発明者らは鋭意研究を行なったところ、従来方法
のようにヨウ素と水の混合液あるいは懸濁液に還元剤を
添加したり、又はこれらの混合された液を加熱して反応
させるのではなく、還元剤の水溶液にヨウ素を連続的又
は間欠的に添加して反応を行なわせるのが非常に有効な
方法であることを見出し、本発明を完成するに至った。
[Means for Solving the Problems] In order to achieve the above object, the inventors of the present invention have conducted diligent research and found that a reducing agent is added to a mixed solution or suspension of iodine and water as in the conventional method. Alternatively, it is a very effective method to carry out the reaction by continuously or intermittently adding iodine to an aqueous solution of a reducing agent, rather than heating the mixed solution to react. Heading out, the present invention has been completed.

【0007】すなわち、本発明は、還元剤の水溶液に、
ヨウ素を連続又は間欠的に添加して反応を行なわせ、反
応後に反応液よりヨウ化水素酸を蒸留により留出させる
ことを特徴とするヨウ化水素酸の製造方法である。
That is, the present invention provides an aqueous solution of a reducing agent,
A method for producing hydriodic acid is characterized in that iodine is continuously or intermittently added to carry out the reaction, and after the reaction, hydriodic acid is distilled from the reaction solution by distillation.

【0008】一般に、ヨウ素を還元してヨウ化水素酸を
製造するに際し、還元剤の水溶液にヨウ素を一括で添加
し反応させた場合には、激しく発熱するとともに、溶液
より未反応のヨウ素が蒸発しやすい。この現象は、ヨウ
素が大量に存在する水溶液又は懸濁液に還元剤を添加し
た場合にもほぼ同様に起こる。しかしながら、本発明の
方法のごとく、還元剤の水溶液にヨウ素を連続又は間欠
的に添加した場合には、急に発熱することがなく、穏和
な条件において添加されたヨウ素がごく速やかに還元さ
れ、ヨウ素の蒸発することを大幅に抑制することが可能
である。従って、ヨウ素の損失を抑制できる効果がとり
わけ顕著であり、所定量の原料を添加し反応させるのみ
で純度のよいヨウ化水素酸を収率よく得ることができ
る。
In general, when iodine is reduced to produce hydroiodic acid, when iodine is added all at once to an aqueous solution of a reducing agent and reacted, heat is generated violently and unreacted iodine is evaporated from the solution. It's easy to do. This phenomenon occurs almost similarly when a reducing agent is added to an aqueous solution or suspension containing a large amount of iodine. However, as in the method of the present invention, when iodine is continuously or intermittently added to an aqueous solution of a reducing agent, heat is not suddenly generated, and iodine added under mild conditions is reduced very quickly, It is possible to significantly suppress the evaporation of iodine. Therefore, the effect of suppressing the loss of iodine is particularly remarkable, and hydriodic acid having a high purity can be obtained in a high yield only by adding a predetermined amount of the raw materials and reacting them.

【0009】本発明の方法に使用可能な還元剤として
は、亜リン酸、次亜リン酸、次二リン酸、二亜リン酸、
亜硫酸、ピロリン酸、ピロ亜リン酸、イソ次リン酸、二
リン酸、次リン酸、シュウ酸、蟻酸、マロン酸、乳酸、
ピルビン酸、アスコルビン酸など、還元性のある化合物
であればその広い範囲で挙げることができ、二種以上が
用いられても構わない。これらのうちでも、亜リン酸、
次亜リン酸、ピロリン酸、ピロ亜リン酸、イソ次リン酸
を用いた場合は製品を高収率で得られる効果が高く、ま
た更には、次亜リン酸、亜リン酸、ピロリン酸を用いた
場合、還元反応に際して反応温度がより容易に制御可能
であり、ヨウ素の損失を抑制できる効果がとりわけ顕著
である。
The reducing agents usable in the method of the present invention include phosphorous acid, hypophosphorous acid, hypodiphosphoric acid, diphosphorous acid,
Sulfurous acid, pyrophosphoric acid, pyrophosphorous acid, isohypophosphoric acid, diphosphoric acid, hypophosphoric acid, oxalic acid, formic acid, malonic acid, lactic acid,
A wide range of reducing compounds such as pyruvic acid and ascorbic acid can be mentioned, and two or more compounds may be used. Among these, phosphorous acid,
When hypophosphorous acid, pyrophosphoric acid, pyrophosphorous acid, or isophosphoric acid is used, it is highly effective to obtain the product in high yield, and further, hypophosphorous acid, phosphorous acid, or pyrophosphoric acid is used. When used, the reaction temperature during the reduction reaction can be controlled more easily, and the effect of suppressing the loss of iodine is particularly remarkable.

【0010】本発明の方法における還元剤の使用量は、
反応に用いられるヨウ素に対し、当量以上であればよ
く、好ましくは 1.0〜1.5 当量の範囲である。この量が
1.0当量未満では反応液中に未反応のヨウ素が残り、収
率が悪化する。また、 1.5当量を越えて使用しても特に
問題はないが、それ以上の効果がなく不経済である。
The amount of reducing agent used in the method of the present invention is
It may be equivalent or more, preferably 1.0 to 1.5 equivalents, with respect to iodine used in the reaction. This amount
If it is less than 1.0 equivalent, unreacted iodine remains in the reaction solution, resulting in a poor yield. Further, although there is no particular problem even if it is used in excess of 1.5 equivalents, it is uneconomical because it has no further effect.

【0011】本発明の製造方法における反応液の量とし
ては、反応に用いるヨウ素の濃度が1〜57重量%、望ま
しくは40〜57重量%となるような量を用いるのが適当で
ある。これが57重量%以上の濃度となってしまうような
量であっては、蒸留時に共沸せず、ガスとして損失する
ヨウ化水素の割合が多くなるため好ましくない。
The amount of the reaction solution used in the production method of the present invention is appropriately such that the concentration of iodine used in the reaction is 1 to 57% by weight, preferably 40 to 57% by weight. If the amount is such that the concentration becomes 57% by weight or more, it is not preferable because it does not azeotrope during distillation and the proportion of hydrogen iodide lost as a gas increases.

【0012】本発明の製造方法では、還元剤の水溶液に
ヨウ素を添加しながら反応を行なわせるが、反応温度
は、通常、常圧下において40〜100 ℃で十分可能であ
り、より好ましくは50〜70℃である。反応温度が40℃未
満では反応の進行が極端に遅くなり、また、 100℃を越
えて反応させた場合には反応液よりヨウ素蒸気が発生し
やすくなるため好ましくない。
In the production method of the present invention, the reaction is carried out while adding iodine to the aqueous solution of the reducing agent, but the reaction temperature is usually 40-100 ° C. under normal pressure, and more preferably 50-100 ° C. 70 ° C. If the reaction temperature is lower than 40 ° C, the reaction progresses extremely slowly, and if the reaction temperature is higher than 100 ° C, iodine vapor is likely to be generated from the reaction solution, which is not preferable.

【0013】本発明の方法において、還元剤水溶液への
ヨウ素の添加は、連続的でもあるいは間欠的でもどちら
でも構わない。また、その添加速度は、製造量、反応温
度、又は反応容器などにより変わるため、一概には記載
できないが、通常は、精々速くとも反応溶液が濃褐色を
呈しないような速度で加えていくことがよく、一般的に
は、少なくとも1時間以上をかけて添加することが好ま
しい。
In the method of the present invention, iodine may be added to the reducing agent aqueous solution continuously or intermittently. In addition, the rate of addition varies depending on the production amount, reaction temperature, reaction vessel, etc., so it cannot be stated unconditionally, but usually it should be added at such a rate that the reaction solution does not show a dark brown color even at best. It is generally preferable to add it for at least 1 hour or more.

【0014】ヨウ素の添加終了後は、更に反応溶液を熟
成させ、反応を完結させることが好ましい。この熟成に
要する時間はその温度により左右され一定しないが、通
常は10分以上、好ましくは30分以上である。また、還元
剤として亜リン酸、次亜リン酸、ピロリン酸、ピロ亜リ
ン酸、又はイソ次リン酸を使用した場合には、反応溶液
を70〜100 ℃の温度で熟成させることがより好ましい。
これはこれらの自己分解に伴う還元作用が、この範囲の
温度でとりわけ顕著であるからである。
After the addition of iodine is completed, the reaction solution is preferably aged to complete the reaction. The time required for this aging depends on the temperature and is not constant, but it is usually 10 minutes or longer, preferably 30 minutes or longer. When phosphorous acid, hypophosphorous acid, pyrophosphoric acid, pyrophosphorous acid, or isophosphorous acid is used as the reducing agent, it is more preferable to age the reaction solution at a temperature of 70 to 100 ° C. .
This is because the reducing action associated with these self-decompositions is particularly remarkable at temperatures in this range.

【0015】また、反応後に未反応のヨウ素が存在する
場合、すなわち、反応溶液が着色している場合などに
は、還元剤を更に添加することにより、この未反応のヨ
ウ素を容易にヨウ化水素とすることができる。
When unreacted iodine is present after the reaction, that is, when the reaction solution is colored, the unreacted iodine can be easily converted into hydrogen iodide by adding a reducing agent. Can be

【0016】反応溶液の熟成後は、該溶液を蒸留し目的
物を留出させることにより、夾雑物又は不純物のないヨ
ウ化水素酸が収率よく得られる。反応溶液の蒸留は、減
圧下〜加圧下の広い範囲の条件で可能であるが、通常は
20〜760 mmHg程度で行なうことが一般的である。
After the reaction solution is aged, the solution is distilled to distill the desired product, whereby hydroiodic acid free from impurities or impurities can be obtained in good yield. Distillation of the reaction solution is possible under a wide range of conditions from reduced pressure to increased pressure.
Generally, it is performed at about 20 to 760 mmHg.

【0017】[0017]

【実施例】以下、実施例により本発明の製造方法を更に
詳細に説明する。以下において「%」は全て重量基準で
ある。
EXAMPLES Hereinafter, the production method of the present invention will be described in more detail with reference to examples. In the following, all "%" are based on weight.

【0018】実施例1 34%次亜リン酸水溶液 101.9g(0.52モル)と水 144.2
gを 500mlフラスコに入れ、攪拌下50℃に加熱した後、
溶液の温度を50〜60℃に保ちながらこれにヨウ素 253.8
g(1モル)を 1.5時間かけ、連続的に添加した。添加
終了後、溶液を80℃で2時間放置した。このとき溶液が
黄色く着色していたので次亜リン酸1gを添加し透明に
した。次に、溶液を圧力50mmHg下で蒸留し、60〜63℃の
間の留分を得、製品とした。得られた製品は、濃度57%
のヨウ化水素酸 424.3gであり、収率は添加したヨウ素
に対し92.8%であった。
Example 1 101.9 g (0.52 mol) of 34% aqueous solution of hypophosphorous acid and water 144.2
g in a 500 ml flask and heated to 50 ° C with stirring,
Add 253.8% iodine to this while maintaining the temperature of the solution at 50-60 ° C.
g (1 mol) was added continuously over 1.5 hours. After the addition was complete, the solution was left at 80 ° C. for 2 hours. At this time, since the solution was colored yellow, 1 g of hypophosphorous acid was added to make it transparent. Next, the solution was distilled under a pressure of 50 mmHg to obtain a fraction between 60 and 63 ° C, which was used as a product. The product obtained has a concentration of 57%
Of hydroiodic acid of 424.3 g, and the yield was 92.8% with respect to the added iodine.

【0019】実施例2 実施例1において、ヨウ素 253.8gを5回に分け、15分
間隔で等量ずつ投入した。すなわち、 50.76gずつを15
分間隔で投入した他は全て同様に操作した。その結果、
得られた製品は、濃度57%のヨウ化水素酸 420.6gであ
り、収率は92.0%であった。
Example 2 In Example 1, 253.8 g of iodine was divided into 5 portions and added in equal amounts at 15-minute intervals. That is, 50.76 g each for 15
All were operated in the same manner except that they were charged at minute intervals. as a result,
The obtained product was 420.6 g of hydroiodic acid having a concentration of 57%, and the yield was 92.0%.

【0020】実施例3 亜リン酸93.0g(1.13モル)と水 195.0gを 500mlフラ
スコに入れ、攪拌下50℃に加熱した後、溶液の温度を50
〜60℃に保ちながらこれにヨウ素 253.8g(1モル)を
1.5時間かけ、連続的に添加した。添加終了後、溶液を
80℃で2時間放置した。このとき溶液が黄色く着色して
いたので亜リン酸1gを添加し透明にした。次に、溶液
を圧力50mmHg下で蒸留し、60〜63℃の間の留分を得、製
品とした。得られた製品は、濃度57%のヨウ化水素酸 4
12.0gであり、収率は添加したヨウ素に対し91.8%であ
った。
Example 3 93.0 g (1.13 mol) of phosphorous acid and 195.0 g of water were placed in a 500 ml flask and heated to 50 ° C. with stirring, and then the temperature of the solution was adjusted to 50.
While maintaining the temperature at -60 ℃, add 253.8g (1 mol) of iodine to it.
Added continuously over 1.5 hours. After the addition is complete,
It was left at 80 ° C for 2 hours. At this time, since the solution was colored yellow, 1 g of phosphorous acid was added to make it transparent. Next, the solution was distilled under a pressure of 50 mmHg to obtain a fraction between 60 and 63 ° C, which was used as a product. The product obtained had a hydroiodic acid concentration of 57%.
It was 12.0 g, and the yield was 91.8% with respect to the added iodine.

【0021】実施例4 ピロリン酸 210.4g(1.18モル)と水 195.0gを 500ml
フラスコに入れ、攪拌下50℃に加熱した後、溶液の温度
を50〜60℃に保ちながらこれにヨウ素 253.8g(1モ
ル)を 1.5時間かけ、連続的に添加した。添加終了後、
溶液を80℃で2時間放置した。このとき溶液が黄色く着
色していたのでピロリン酸1gを添加し透明にした。次
に、溶液を圧力50mmHg下で蒸留し、60〜63℃の間の留分
を得、製品とした。得られた製品は、濃度57%のヨウ化
水素酸 413.3gであり、収率は添加したヨウ素に対し9
2.1%であった。
Example 4 500 ml of 210.4 g (1.18 mol) of pyrophosphoric acid and 195.0 g of water
The mixture was placed in a flask and heated to 50 ° C. with stirring, and then 253.8 g (1 mol) of iodine was continuously added to this while keeping the temperature of the solution at 50 to 60 ° C. over 1.5 hours. After the addition is complete
The solution was left at 80 ° C. for 2 hours. Since the solution was colored yellow at this time, 1 g of pyrophosphoric acid was added to make it transparent. Next, the solution was distilled under a pressure of 50 mmHg to obtain a fraction between 60 and 63 ° C, which was used as a product. The obtained product was 413.3 g of hydroiodic acid with a concentration of 57%, and the yield was 9 based on the added iodine.
It was 2.1%.

【0022】実施例5 34%次亜リン酸水溶液 101.9g(0.52モル)と水 144.2
gを 500mlフラスコに入れ、攪拌下40℃に加熱した後、
溶液の温度を40〜50℃に保ちながらこれにヨウ素 253.8
g(1モル)を 1.5時間かけ、連続的に添加した。添加
終了後、溶液を70℃で2時間放置した。このとき反応液
が黄色く着色していたので次亜リン酸1gを追加し透明
にした。次に、溶液を圧力50mmHg下で蒸留し、60〜63℃
の間の留分を得、製品とした。得られた製品は、濃度57
%のヨウ化水素酸 424.3gであり、収率は添加したヨウ
素に対し90.8%であった。
Example 5 101.9 g (0.52 mol) of 34% aqueous solution of hypophosphorous acid and 144.2 of water
g into a 500 ml flask and heating to 40 ° C with stirring,
Add iodine 253.8 to this while maintaining the temperature of the solution at 40-50 ° C.
g (1 mol) was added continuously over 1.5 hours. After the addition was complete, the solution was left at 70 ° C. for 2 hours. Since the reaction solution was colored yellow at this time, 1 g of hypophosphorous acid was added to make it transparent. Next, the solution is distilled under a pressure of 50 mmHg and 60-63 ° C.
The fraction between the two was obtained and used as the product. The product obtained has a concentration of 57
% Hydroiodic acid was 424.3 g, and the yield was 90.8% based on the added iodine.

【0023】実施例6 実施例1において、フラスコに仕込んだ水 144.2gを 2
44.2gとして行なった他は全て同様に操作した。その結
果、得られた製品は、濃度44.9%のヨウ化水素酸 530.2
gであり、収率は添加したヨウ素に対し93.8%であっ
た。
Example 6 In Example 1, 24.2 g of 144.2 g of water charged in a flask was added.
The same operation was performed except that the amount was 44.2 g. As a result, the obtained product was 530.2% hydroiodic acid with a concentration of 44.9%.
The yield was 93.8% with respect to the added iodine.

【0024】実施例7 34%次亜リン酸水溶液 200.0g(1.03モル)と水 100.1
gを 500mlフラスコに入れ、攪拌下50℃に加熱した後、
溶液の温度を50〜60℃に保ちながらこれにヨウ素 253.8
g(1モル)を 1.5時間かけ、連続的に添加した。添加
終了後、溶液を80℃で2時間放置した。次に、溶液を実
施例1同様蒸留し、製品を得た。得られた製品は、濃度
57%のヨウ化水素酸 419.7gであり、収率は91.8%であ
った。
Example 7 200.0 g (1.03 mol) of 34% aqueous solution of hypophosphorous acid and 100.1 of water
g in a 500 ml flask and heated to 50 ° C with stirring,
Add 253.8% iodine to this while maintaining the temperature of the solution at 50-60 ° C.
g (1 mol) was added continuously over 1.5 hours. After the addition was complete, the solution was left at 80 ° C. for 2 hours. Next, the solution was distilled as in Example 1 to obtain a product. The resulting product has a concentration
It was 419.7 g of 57% hydroiodic acid, and the yield was 91.8%.

【0025】比較例1 実施例1において、ヨウ素を連続的に添加することな
く、当初よりヨウ素をもフラスコ中に入れ、そのまま80
℃に昇温し、その温度を維持させながら2時間反応させ
た。この間には、溶液中より蒸発するヨウ素蒸気が大量
に見られた。次に、溶液を実施例1同様蒸留し、製品を
得た。得られた製品は、濃度57%のヨウ化水素酸 424.3
gであり、収率は79.7%であった。
Comparative Example 1 In Example 1, iodine was also added to the flask from the beginning without continuously adding iodine, and the iodine was directly added to the flask.
The temperature was raised to 0 ° C., and the reaction was performed for 2 hours while maintaining the temperature. During this period, a large amount of iodine vapor that was evaporated from the solution was observed. Next, the solution was distilled as in Example 1 to obtain a product. The product obtained has a hydroiodic acid content of 424.3
The yield was 79.7%.

【0026】比較例2 ヨウ素 253.8g(1モル)と水 144.2gを 500mlフラス
コに入れ、攪拌下50〜60℃に保ちながらこれに34%次亜
リン酸水溶液 101.9g(0.52モル)を 1.5時間かけ、連
続的に添加した(すなわち、実施例1における次亜リン
酸とヨウ素の添加の形態を逆にして行なった。)。この
添加中においても、比較例1同様溶液中より蒸発するヨ
ウ素蒸気が大量に見られた。次に、溶液を実施例1同様
蒸留し、製品を得た。得られた製品は、濃度57%のヨウ
化水素酸 181.1gであり、収率は70.8%であった。
Comparative Example 2 253.8 g (1 mol) of iodine and 144.2 g of water were placed in a 500 ml flask and 101.9 g (0.52 mol) of 34% aqueous solution of hypophosphorous acid was added thereto while maintaining the temperature at 50 to 60 ° C. for 1.5 hours. And added continuously (that is, the mode of addition of hypophosphorous acid and iodine in Example 1 was reversed). Even during this addition, a large amount of iodine vapor evaporated from the solution was observed as in Comparative Example 1. Next, the solution was distilled as in Example 1 to obtain a product. The obtained product was 181.1 g of hydroiodic acid having a concentration of 57%, and the yield was 70.8%.

【0027】[0027]

【発明の効果】以上詳述したように、還元剤の水溶液に
ヨウ素を連続的又は間欠的に添加し反応させた後に反応
液を蒸留する本発明のヨウ化水素酸の製造方法によれ
ば、高濃度の目的物を得る際にも、使用されるヨウ素の
損失はほとんどなく、高い転化率で製品を得ることがで
きる。また、ヨウ素の系外に放散することも防止できる
ことになるので、その除害設備も大幅に縮小することが
可能である。従って、工業的にヨウ化水素酸を製造する
場合には、本発明の製造方法が好適に用いられる。
As described in detail above, according to the method for producing hydroiodic acid of the present invention, iodine is continuously or intermittently added to an aqueous solution of a reducing agent to cause a reaction, and then the reaction solution is distilled. Even when obtaining a high-concentration target product, there is almost no loss of iodine used, and a product can be obtained with a high conversion rate. Further, since it is possible to prevent the release of iodine out of the system, it is possible to greatly reduce the equipment for removing the harm. Therefore, when industrially producing hydroiodic acid, the production method of the present invention is preferably used.

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 還元剤の水溶液に、ヨウ素を連続又は間
欠的に添加して反応を行なわせ、反応後に反応液よりヨ
ウ化水素酸を蒸留により留出させることを特徴とするヨ
ウ化水素酸の製造方法。
1. A hydroiodic acid characterized in that iodine is continuously or intermittently added to an aqueous solution of a reducing agent to carry out a reaction, and hydroiodic acid is distilled from the reaction solution by distillation after the reaction. Manufacturing method.
【請求項2】 還元剤が亜リン酸、次亜リン酸、ピロリ
ン酸、ピロ亜リン酸、イソ次リン酸から選ばれる一種又
は二種以上である請求項1記載のヨウ化水素酸の製造方
法。
2. The production of hydriodic acid according to claim 1, wherein the reducing agent is one or more selected from phosphorous acid, hypophosphorous acid, pyrophosphoric acid, pyrophosphorous acid and isohypophosphoric acid. Method.
【請求項3】 反応を40〜100 ℃の温度で行なわせる請
求項1又は2記載のヨウ化水素酸の製造方法。
3. The method for producing hydroiodic acid according to claim 1, wherein the reaction is carried out at a temperature of 40 to 100 ° C.
JP19257394A 1994-08-16 1994-08-16 Production of hydroiodic acid Pending JPH0859205A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP19257394A JPH0859205A (en) 1994-08-16 1994-08-16 Production of hydroiodic acid

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP19257394A JPH0859205A (en) 1994-08-16 1994-08-16 Production of hydroiodic acid

Publications (1)

Publication Number Publication Date
JPH0859205A true JPH0859205A (en) 1996-03-05

Family

ID=16293535

Family Applications (1)

Application Number Title Priority Date Filing Date
JP19257394A Pending JPH0859205A (en) 1994-08-16 1994-08-16 Production of hydroiodic acid

Country Status (1)

Country Link
JP (1) JPH0859205A (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8268284B2 (en) 2008-01-31 2012-09-18 Nippoh Chemicals Co., Ltd. System and method for producing iodine compound
CN102674253A (en) * 2012-05-22 2012-09-19 太仓沪试试剂有限公司 Preparation method of hydroiodic acid
CN104085857A (en) * 2014-06-26 2014-10-08 周海军 New method for preparing high-purity hydroiodic acid
US9272922B2 (en) 2008-01-31 2016-03-01 Nippoh Chemicals Co., Ltd. Inorganic iodide, production method thereof, and production system thereof
JP6330064B1 (en) * 2017-01-10 2018-05-23 伊勢化学工業株式会社 Method for producing hydroiodic acid and method for producing aqueous metal iodide solution
CN113753859A (en) * 2021-10-15 2021-12-07 太仓沪试试剂有限公司 Method for purifying high-purity iodide

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8268284B2 (en) 2008-01-31 2012-09-18 Nippoh Chemicals Co., Ltd. System and method for producing iodine compound
US9272922B2 (en) 2008-01-31 2016-03-01 Nippoh Chemicals Co., Ltd. Inorganic iodide, production method thereof, and production system thereof
CN102674253A (en) * 2012-05-22 2012-09-19 太仓沪试试剂有限公司 Preparation method of hydroiodic acid
CN104085857A (en) * 2014-06-26 2014-10-08 周海军 New method for preparing high-purity hydroiodic acid
JP6330064B1 (en) * 2017-01-10 2018-05-23 伊勢化学工業株式会社 Method for producing hydroiodic acid and method for producing aqueous metal iodide solution
JP2018111618A (en) * 2017-01-10 2018-07-19 伊勢化学工業株式会社 Method for producing hydriodic acid and method for producing aqueous metal iodide solution
CN113753859A (en) * 2021-10-15 2021-12-07 太仓沪试试剂有限公司 Method for purifying high-purity iodide

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