JPH0742087B2 - Granulated refined iodine manufacturing method - Google Patents
Granulated refined iodine manufacturing methodInfo
- Publication number
- JPH0742087B2 JPH0742087B2 JP5046153A JP4615393A JPH0742087B2 JP H0742087 B2 JPH0742087 B2 JP H0742087B2 JP 5046153 A JP5046153 A JP 5046153A JP 4615393 A JP4615393 A JP 4615393A JP H0742087 B2 JPH0742087 B2 JP H0742087B2
- Authority
- JP
- Japan
- Prior art keywords
- iodine
- inert gas
- particle size
- temperature
- water
- 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.)
- Expired - Fee Related
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B7/00—Halogens; Halogen acids
- C01B7/13—Iodine; Hydrogen iodide
- C01B7/14—Iodine
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Glanulating (AREA)
Description
【0001】[0001]
【産業上の利用分野】本発明は、粒状化した精製沃素の
製法に関するものである。FIELD OF THE INVENTION The present invention relates to a method for producing granulated refined iodine.
【0002】[0002]
【従来の技術】固体の精製沃素は溶融沃素を冷却固化
し、フレーク状,粒状,球状などの特色ある形状にし
て、取り扱われている。しかし、最近の高品質化を要求
される時代においては、精製沃素も形状のみに特質化さ
れるだけでなく、より良い品質も要求されて来ている。
従来の方法では、固体精製沃素を製造する前工程の沃素
溶融操作において、水分及びその他の不純物をほとんど
除去しているにもかかわらず、沃素固化工程では、空気
中及び/又は水噴霧冷却を行い、水分及びその他の不純
物が付着及び/又は混入する様な状態で操作している。
その為、それらが、精製沃素の純度に大きく影響し、一
定した純度が得られない。更に、沃素は水1リットルに
約0.3g溶解する為、微量の水が付着及び/又は混入す
ると、沃素の一部が溶け、沃化水素酸に変化し、表面が
濡れた状態になり、包装材及び取扱機器等を汚したりす
る。又、精製沃素は、ほとんど国外に輸出されており、
その輸送に約2ケ月も要し、その間にケーキングを起こ
す事がある。これは、沃素が液体から固体になる時、容
積が約20%収縮するに伴い、沃素に空洞が生じる。冷
却方法により、大きな空洞になったり、ポーラス状の空
洞になったりするが、ポーラス状の空洞が多く出来る
と、表面積が増加し、それに伴い付着及び/又は混入す
る水分量も増える。それらが、沃素表面を覆い、張力及
び/又は毛管現象により、沃素間に引っ張り合いを生じ
させる事が、ケーキングを起こす主因であるが、前述の
沃化水素酸の生成も要因の一つに挙げられる。又、一般
的に腐食性、昇華性を有する沃素を精製する装置は、操
作が複雑で、高価な事が多い。2. Description of the Related Art Solid refined iodine is handled in the form of flakes, granules, spheres, etc., which are obtained by cooling and solidifying molten iodine. However, in the recent era in which high quality is required, refined iodine is not only characterized only by its shape, but also better quality is required.
In the conventional method, in the iodine melting operation in the previous step of producing solid purified iodine, water and other impurities are almost removed, but in the iodine solidification step, air and / or water spray cooling is performed. , The water and other impurities are attached and / or mixed in.
Therefore, they have a great influence on the purity of the purified iodine, and a constant purity cannot be obtained. Furthermore, since iodine dissolves in about 0.3 g in 1 liter of water, if a small amount of water adheres and / or mixes in, a part of iodine is dissolved and converted into hydroiodic acid, and the surface becomes wet. Soil packaging materials and handling equipment. Most of the refined iodine is exported overseas,
The transportation takes about two months, and during that time, caking may occur. This is because when the iodine changes from a liquid to a solid, the volume of the iodine shrinks by about 20%, and a void is formed in the iodine. Depending on the cooling method, a large cavity or a porous cavity may be formed. However, if there are many porous cavities, the surface area increases and the amount of water that adheres and / or mixes with it increases. The fact that they cover the surface of iodine and cause tension between iodine by tension and / or capillarity is the main cause of caking, but the formation of hydroiodic acid is also one of the factors. To be In addition, an apparatus for purifying iodine, which is generally corrosive and sublimable, is complicated in operation and often expensive.
【0003】[0003]
【発明が解決しようとする課題】本発明の目的は、前述
の様な精製沃素の欠点を改善し、ケーキングを起こしに
くい、高品質の粒状化精製沃素を経済的に製造する事で
ある。SUMMARY OF THE INVENTION An object of the present invention is to improve the above-mentioned drawbacks of refined iodine and to economically produce high-quality granular refined iodine that is unlikely to cause caking.
【0004】[0004]
【課題を解決するための手段】前述の問題を有利に解決
するために、本発明の粒状化精製沃素の製法において
は、溶融沃素を噴射ノズルで噴射し、これを冷却,乾
燥,清浄処理した不活性気体に接触させ、溶融沃素を冷
却固化させる事により、水分及び不純物の混入が非常に
少ない粒状化精製沃素を製造する。In order to advantageously solve the above-mentioned problems, in the method for producing granulated refined iodine of the present invention, molten iodine is injected by an injection nozzle, and this is cooled, dried and cleaned. By bringing the molten iodine into contact with an inert gas and cooling and solidifying the molten iodine, granular refined iodine containing very little water and impurities is produced.
【0005】次に本発明について詳細に説明する。溶融
沃素とは、粗製沃素を精製する工程で得られる、純度の
高い液体沃素である。これは、固体粗製沃素を沃素に腐
食されない容器に仕込み、密閉後、容器温度115〜1
30℃で溶融し、一定時間静置した後、不純物を分離し
たものである。Next, the present invention will be described in detail. Molten iodine is high-purity liquid iodine obtained in the step of refining crude iodine. This is because solid crude iodine is charged into a container which is not corroded by iodine, and after sealing, the container temperature is 115 to 1
It was obtained by melting at 30 ° C., leaving it for a certain period of time, and then separating impurities.
【0006】噴射ノズルとは、ノズル径0.5〜3.0mm
で、一定の圧力を要する噴霧ノズルの事である。溶融沃
素を噴射させるときは、導管温度を115〜120℃に
調節し、噴射角度を水平線より、上向き55〜75°、
噴射圧力を1.0〜3.0kg/cm2にする。The injection nozzle is a nozzle having a diameter of 0.5 to 3.0 mm.
It is a spray nozzle that requires a certain pressure. When injecting molten iodine, the conduit temperature is adjusted to 115 to 120 ° C., and the injection angle is 55 to 75 ° above the horizontal line.
The injection pressure is set to 1.0 to 3.0 kg / cm 2 .
【0007】冷却とは、不活性気体の温度を水冷又は空
冷により下げる操作で、15℃以下にする事が好まし
い。Cooling is an operation of lowering the temperature of the inert gas by water cooling or air cooling, and it is preferably set to 15 ° C. or lower.
【0008】乾燥とは、冷却した不活性気体の湿度を乾
燥剤等で下げる操作で、20%以下にする事が好まし
い。Drying is an operation of lowering the humidity of the cooled inert gas with a desiccant or the like, and is preferably set to 20% or less.
【0009】清浄とは、冷却及び乾燥操作の終了した不
活性気体中の微粒子をエアクリーナー等で除去する操作
で、出来るだけ、除去する事が好ましい。The term "cleaning" refers to an operation of removing fine particles in an inert gas which has been cooled and dried by an air cleaner or the like, and it is preferable to remove the particles as much as possible.
【0010】不活性気体とは、液体沃素と反応しない気
体の事で、窒素、ヘリウム、空気等種々あるが、取扱易
さ及び経済性から、空気が好ましい。The inert gas is a gas that does not react with liquid iodine, and there are various kinds such as nitrogen, helium and air, but air is preferred from the viewpoint of easy handling and economy.
【0011】接触させとは、噴射された溶融沃素が、不
活性気体と接触して、急冷される事なく、効率良く徐々
に冷却される操作を言う。The term "contact" means an operation in which the injected molten iodine is efficiently cooled gradually without coming into contact with an inert gas and being rapidly cooled.
【0012】冷却固化とは、噴射された溶融沃素が不活
性気体空間中で、冷却され、固体の粒子に変化する操作
を言う。Cooling and solidification refers to an operation in which the injected molten iodine is cooled in an inert gas space and converted into solid particles.
【0013】ここで言う粒状化とは、固化された沃素が
丸い及び細長いとかと言う形状等を問わず、一定の粒度
分布範囲に存在する粒径の粒子の事を言う。この方法で
は、0.2〜2.5mmの粒度分布範囲の粒子である。The term "granulation" as used herein refers to particles having a particle size within a certain particle size distribution range regardless of the shape of the solidified iodine, such as round or elongated. In this method, the particles have a particle size distribution range of 0.2 to 2.5 mm.
【0014】本発明の方法を実施する工程の一例を図1
に基づいて説明する。固体である粗製沃素13を沃素溶
融容器2に入れて密閉し、温度を上昇させて溶融する。
そのまま、一定時間静置し、不純物及び水分を分離した
液体沃素を準備して置く。沃素溶融容器2内の圧力は粒
径に合わせて適当に調節する。造粒塔1内には、不活性
気体吸入口5より、不活性気体14を冷却器8、乾燥器
7及びエアクリーナ6を通過させた後、吸入する。排風
機11により、造粒塔1内の排気口9から、排ガス15
を排ガス吸収塔10及び排風機11を通過させて排気す
る。次に溶融した沃素を、温度調節器3で温度を調節
し、噴射ノズル4より造粒塔内に噴射する。噴射ノズル
4は、上向きに造粒塔1内の不活性気体空間に噴射す
る。造粒塔1内の空間で冷却固化された粒状精製沃素
は、造粒塔底部の製品受口12に受けられる。製品受口
12は、粒径により分割する事が出来る。An example of steps for carrying out the method of the present invention is shown in FIG.
It will be described based on. The crude iodine 13 which is a solid is put in the iodine melting vessel 2 and sealed, and the temperature is raised to melt.
As it is, it is allowed to stand for a certain period of time, and liquid iodine from which impurities and water are separated is prepared and placed. The pressure in the iodine melting vessel 2 is appropriately adjusted according to the particle size. The inert gas 14 is sucked into the granulating tower 1 through the inert gas inlet 5 after passing through the cooler 8, the dryer 7 and the air cleaner 6. The exhaust gas 11 is discharged from the exhaust port 9 in the granulation tower 1 by the exhaust fan 11.
Is passed through the exhaust gas absorption tower 10 and the exhaust fan 11 to be exhausted. Next, the temperature of the molten iodine is adjusted by the temperature controller 3, and the molten iodine is injected from the injection nozzle 4 into the granulating tower. The injection nozzle 4 injects upward into the inert gas space in the granulation tower 1. The refined granular iodine that has been cooled and solidified in the space inside the granulation tower 1 is received by the product receiving port 12 at the bottom of the granulation tower. The product receiving port 12 can be divided according to the particle size.
【0015】本発明においては、前記の様な装置を採用
し、粒状化精製沃素の製法を実施する事により、次の利
点が認められる。この方法で得られた粒状化精製沃素
は、非常に乾燥された状態であるため、微量水分の影響
による装置への沃素の汚れ及び包装後におけるケーキン
グの発生が非常に少ない。これは粒子の表面積が従来法
より小さくなり、更に不活性気体中での操作により、水
分等が混入されにくい為と推定される。In the present invention, the following advantages are recognized by adopting the apparatus as described above and carrying out the method for producing granulated refined iodine. Since the granulated purified iodine obtained by this method is in a very dried state, the generation of iodine stains on the device and the occurrence of caking after packaging due to the influence of a trace amount of water are very small. It is presumed that this is because the surface area of the particles becomes smaller than that of the conventional method, and further, it is difficult for water and the like to be mixed in by the operation in an inert gas.
【0016】不活性気体の温度、湿度をコントロールす
る事により、精製沃素の純度が向上し、非常に安定して
いる。又、清浄度をコントロールする事により、不揮発
残査等の分析値も非常に小さく、安定しているので品質
管理も容易であり、それに伴いケーキングの発生も非常
に少なく、長期保存に耐え得る為、出荷管理も容易であ
る。By controlling the temperature and humidity of the inert gas, the purity of the purified iodine is improved and is very stable. In addition, by controlling the cleanliness, the analysis values such as non-volatile residue are also very small and stable, so quality control is easy, and the occurrence of caking is very small, and it can withstand long-term storage. Shipping management is also easy.
【0017】不活性気体のみを冷却媒体としているの
で、操作及びコントロールもし易く、又、装置も安価な
材質で簡単に製作可能であり、沃素以外の物質が混入し
にくい。Since only the inert gas is used as the cooling medium, the operation and control are easy, and the device can be easily manufactured with a cheap material, and substances other than iodine are not easily mixed.
【0018】[0018]
【実施例】次に、実施例により本発明の方法を具体的に
説明する。 実施例1 添付図面の図1に従って、粒状化精製沃素の製造を実施
した。圧力2.0kg/cm2、温度120℃に調節した15リ
ットルの沃素溶融容器2から、溶融沃素を温度調節器3
で温度115℃に調節して、造粒塔1の上部に向け60
°の角度にした噴射ノズル4より、液体沃素を毎時50
kgで噴射する。噴射ノズル4の口径は0.6mmである。造
粒塔1は、高さ2m,長さ3m,幅1mの透明塩化ビニ
ール樹脂製で、造粒塔1の不活性気体吸入口5より、温
度10℃,湿度20%の空気が吸入される。排気口9か
らは毎分10m3で排ガスが排ガス吸収塔10を経て、排
風機11によって排気される。製品は造粒塔1の底部の
製品受口12に受ける。EXAMPLES Next, the method of the present invention will be specifically described by way of examples. Example 1 Granulated purified iodine was produced according to FIG. 1 of the accompanying drawings. The molten iodine was heated from a 15 liter iodine melting vessel 2 adjusted to a pressure of 2.0 kg / cm 2 and a temperature of 120 ° C. by a temperature controller 3.
The temperature is adjusted to 115 ° C. with 60 ° C. toward the upper part of the granulation tower 1.
Liquid iodine is sprayed from the spray nozzle 4 at an angle of 50
Jet in kg. The diameter of the injection nozzle 4 is 0.6 mm. The granulating tower 1 is made of a transparent vinyl chloride resin having a height of 2 m, a length of 3 m and a width of 1 m, and the inert gas suction port 5 of the granulating tower 1 sucks air having a temperature of 10 ° C. and a humidity of 20%. . The exhaust gas is exhausted from the exhaust port 9 at a rate of 10 m 3 per minute through the exhaust gas absorption tower 10 and by the exhaust fan 11. The product is received in the product receiving port 12 at the bottom of the granulating tower 1.
【0019】前述の操作を5回繰り返し実施した結果、
沃素の純度は平均値が99.85%,最低値が99.80
%,最高値が99.91%であった。不純物である不揮発
残査は平均で0.0041%,最低値が0.0035%,最
高値が0.0052%であった。平均粒径は0.52mmで、
粒度分布は0.2〜0.8mmの範囲に95.5%が存在した。
温度20℃でガラス製サンプル瓶に保存した結果、60
日後でもケーキングは見られなかった。又、サンプル瓶
の内部に汚れは生じなかった。As a result of repeating the above operation five times,
The average purity of iodine is 99.85% and the minimum is 99.80.
%, And the maximum value was 99.91%. The non-volatile residue as an impurity was 0.0041% on average, the minimum value was 0.0035%, and the maximum value was 0.0052%. The average particle size is 0.52 mm,
The particle size distribution was 95.5% in the range of 0.2 to 0.8 mm.
As a result of storing in a glass sample bottle at a temperature of 20 ° C., 60
I could not see caking even after a day. Moreover, the inside of the sample bottle was not soiled.
【0020】比較例1 比較例1として、次の事を試験した。不活性気体吸入口
5より、温度20℃,湿度70%の空気を取り入れ、実
施例1と同様に操作し、その操作を5回繰り返し実施し
た結果、沃素の純度は平均値が99.75%,最低値が9
9.62%,最高値が99.82%であった。不揮発残査は
平均で0.0053%,最低値が0.0035%,最高値が
0.0073%であった。平均粒径は0.54mmで粒度分布
は0.2〜0.8mmの範囲に95.2%が存在した。温度20
℃でガラス製サンプル瓶に保存した結果、20日後に全
てがケーキングした。又、サンプル瓶内部の所々に薄茶
色の汚れが生じていた。この比較例では空気中の湿度が
高いため、沃素の純度が低く、尚且つ、ケーキングしや
すい事がわかった。Comparative Example 1 As Comparative Example 1, the following was tested. Air having a temperature of 20 ° C. and a humidity of 70% was taken in through the inert gas inlet port 5, and the same operation as in Example 1 was carried out. As a result of repeating the operation 5 times, the average purity of iodine was 99.75%. , The lowest value is 9
The maximum value was 9.62%, and the maximum was 99.82%. Nonvolatile residue is 0.0053% on average, the lowest value is 0.0035%, and the highest value is
It was 0.0073%. The average particle size was 0.54 mm, and the particle size distribution was 95.2% in the range of 0.2 to 0.8 mm. Temperature 20
Storage in glass sample bottles at 0 ° C. resulted in all caking after 20 days. In addition, light brown stains were found in various places inside the sample bottle. It was found that in this comparative example, the humidity in the air was high, so that the purity of iodine was low and the cake was easily caked.
【0021】比較例2 比較例2として、次の事を試験した。添付図面の図1の
エアクリーナ6及び乾燥器7をとりはずし、実施した例
を示す。不活性気体吸入口5より、温度20℃、湿度9
0%の空気を吸入する。この空気中に蒸留水を毎分10
0ミリリットルで噴射し、50ミクロンの水滴が含まれ
る様にし、実施例1と同様に操作した。その操作を5回
繰り返し実施した結果、沃素の純度は平均値が99.30
%,最低値が99.00%,最高値が99.52%であっ
た。不揮発残査は、平均で0.0080%,最低値が0.0
050%,最高値が0.0110%であった。平均粒径
は、0.51mmで粒度分布は0.2〜0.8mmの範囲に94.1
%が存在した。温度20℃でガラス製サンプル瓶に保存
した結果、10日後に全てがケーキングした。又、サン
プル瓶内部全面が茶褐色になり、液滴が付着していた。
この比較例では沃素の純度及び不揮発残査も悪く、品質
が不安定であり、ケーキングも非常に早かった。これ
は、水で急冷された為に、粒子中にポーラスな空洞が多
くでき、その中に水が吸着された為に起こるものと考え
られる。又、この製品を乾燥しても、純度は比較例1の
純度にも達しなかった。Comparative Example 2 As Comparative Example 2, the following was tested. An example is shown in which the air cleaner 6 and the dryer 7 shown in FIG. From inert gas inlet 5, temperature 20 ℃, humidity 9
Inhale 0% air. Distilled water 10 minutes per minute in this air
The same operation as in Example 1 was carried out by injecting 0 ml so as to contain a water droplet of 50 microns. As a result of repeating the operation 5 times, the average purity of iodine was 99.30.
%, The lowest value was 99.00%, and the highest value was 99.52%. Nonvolatile residue is 0.0080% on average, and the minimum value is 0.0
The maximum value was 050% and 0.0110%. The average particle size is 0.51 mm, and the particle size distribution is 94.1 in the range of 0.2 to 0.8 mm.
% Was present. After storage in a glass sample bottle at a temperature of 20 ° C., all were caked after 10 days. In addition, the entire inside of the sample bottle became dark brown and droplets were attached.
In this comparative example, the purity and non-volatile residue of iodine were poor, the quality was unstable, and caking was very fast. It is considered that this is because a large number of porous cavities are formed in the particles due to the rapid cooling with water, and the water is adsorbed therein. Moreover, even when this product was dried, the purity did not reach the purity of Comparative Example 1.
【0022】[0022]
【発明の効果】本発明の粒状化精製沃素の製法により、
従来品よりも純度が高く、不揮発残査の少ない、高品質
な安定したものが得られ、尚且つ、粒径が小さいにもか
かわらずケーキングの発生率が非常に少なく、長期保存
に対しても、ほとんどケーキングが発生しないものが得
られる。更に、包装材内部の汚れ等もないので、品質管
理および出荷管理が安定化するので能率向上が計られ、
又、使用に際しては、粒径が粒度分布の一定した小さい
範囲におさまるので、溶解速度も早く、均一な溶解速度
をもつものが得られる。加えて、装置も複雑ではなく、
安価な材質で簡単に製作可能であり、冷却固化も単一の
気体で良いので保守管理が容易になる。Industrial Applicability According to the method for producing granular refined iodine of the present invention,
Higher purity and less non-volatile residue than conventional products, stable and high quality can be obtained.Although the particle size is small, the incidence of caking is very low, and even for long-term storage. It is possible to obtain a cake that hardly causes caking. Furthermore, since there is no dirt inside the packaging material, quality control and shipping control are stabilized, improving efficiency.
In use, since the particle size falls within a small range where the particle size distribution is constant, the dissolution rate is fast and a uniform dissolution rate can be obtained. In addition, the device is not complicated,
It can be easily manufactured with an inexpensive material, and since it can be cooled and solidified with a single gas, maintenance and management is easy.
【図1】本発明の方法を実施するプロセスの一例を示す
フローシートである。FIG. 1 is a flow sheet showing an example of a process for carrying out the method of the present invention.
1 造粒塔 2 沃素溶融容器 3 温度調節器 4 噴射ノズル 5 不活性気体吸入口 6 エアクリーナ 7 乾燥器 8 冷却器 9 排気口 10 排ガス吸収塔 11 排風機 12 製品受口 13 粗製沃素 14 不活性気体 15 排ガス 1 Granulation Tower 2 Iodine Melting Container 3 Temperature Controller 4 Injection Nozzle 5 Inert Gas Intake Port 6 Air Cleaner 7 Dryer 8 Cooler 9 Exhaust Port 10 Exhaust Gas Absorption Tower 11 Exhaust Fan 12 Product Receptor 13 Crude Iodine 14 Inert Gas 15 Exhaust gas
Claims (1)
し、これを冷却,乾燥,清浄処理した不活性気体14に
接触させ、冷却固化させることを特徴とする粒状化精製
沃素の製法。1. A method for producing granular refined iodine, which comprises injecting molten iodine with an injection nozzle 4, bringing the molten iodine into contact with an inert gas 14 which has been cooled, dried, and cleaned, and then cooled and solidified.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP5046153A JPH0742087B2 (en) | 1993-02-12 | 1993-02-12 | Granulated refined iodine manufacturing method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP5046153A JPH0742087B2 (en) | 1993-02-12 | 1993-02-12 | Granulated refined iodine manufacturing method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH06239602A JPH06239602A (en) | 1994-08-30 |
| JPH0742087B2 true JPH0742087B2 (en) | 1995-05-10 |
Family
ID=12739045
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP5046153A Expired - Fee Related JPH0742087B2 (en) | 1993-02-12 | 1993-02-12 | Granulated refined iodine manufacturing method |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0742087B2 (en) |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH03163054A (en) * | 1989-08-14 | 1991-07-15 | Nippon Shokubai Kagaku Kogyo Co Ltd | Production of granular cysteamine hydrochloride |
| JPH07109401B2 (en) * | 1990-05-16 | 1995-11-22 | 鹿島建設株式会社 | Ground improvement area detection method using improved material |
-
1993
- 1993-02-12 JP JP5046153A patent/JPH0742087B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPH06239602A (en) | 1994-08-30 |
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