JP2006232662A - Transportation method and transportation container - Google Patents

Transportation method and transportation container Download PDF

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JP2006232662A
JP2006232662A JP2006018038A JP2006018038A JP2006232662A JP 2006232662 A JP2006232662 A JP 2006232662A JP 2006018038 A JP2006018038 A JP 2006018038A JP 2006018038 A JP2006018038 A JP 2006018038A JP 2006232662 A JP2006232662 A JP 2006232662A
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iodine
liquid
container
concentration
concentrated
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JP4995465B2 (en
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Shigenobu Shoji
繁信 東海林
Makoto Takahashi
誠 高橋
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Nippoh Chemicals Co Ltd
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<P>PROBLEM TO BE SOLVED: To provide a method for inexpensively, stably and safely transporting a solution containing an iodine component and to provide a container to be used in the method for efficiently recovering the iodine component as a precious resource. <P>SOLUTION: The transportation method includes steps of: adding an alkali compound to a liquid having less than 10 mass% concentration of at least one kind selected from a group consisting of simple iodine, compounds containing iodine, iodine ion and ions containing an iodine element, so as to control the pH; concentrating the liquid obtained by the above step of controlling the pH so as to obtain a concentrated liquid having 10 to 40 mass% of at least one kind selected from a group consisting of simple iodine, compounds containing iodine, iodine ion and ions containing an iodine element; and transporting the concentrated liquid. The transportation container is used in the above method. <P>COPYRIGHT: (C)2006,JPO&NCIPI

Description

本発明は運搬方法および運搬容器に関し、詳細には単体ヨウ素、ヨウ素元素を含む化合物、ヨウ素イオン、およびヨウ素元素を含むイオンからなる群より選択される少なくとも1種を含有する液を安定にかつ安全に運搬する方法、およびこれに用いられる運搬容器に関する。   The present invention relates to a transport method and a transport container, and in particular, a stable and safe liquid containing at least one selected from the group consisting of simple iodine, a compound containing iodine element, iodine ion, and an ion containing iodine element. The present invention relates to a method for transporting to a container and a transport container used therefor.

ハロゲン元素であるヨウ素は、天然において他の元素と化合物を形成して存在することが多く、地殻、海水などに希薄に含まれる資源である。人に対する使用の例としては、生体反応を支える必須ミネラルとしての使用があり、工業資源としての使用の例は、ヨウ素が有する抗菌性や酸化力、反応性を利用した医薬用、工業用、農業用等の様々な製品の原料および中間体としての使用がある。その使用場面や使用量は増加する傾向にある。このように有用でニーズが多いヨウ素の供給に関しては、ヨウ素が自然界では水溶性の塩として存在する場合が多く、その分布の様子も希薄であるため、採掘には大規模な施設を必要とし、コスト高に繋がりうる。したがって、ヨウ素は産出量が限られる希少な資源として位置づけられる。   Iodine, which is a halogen element, often exists in the form of a compound with other elements in nature, and is a resource that is rarely contained in the crust, seawater, and the like. Examples of use for humans include use as essential minerals that support biological reactions, and examples of use as industrial resources include pharmaceutical, industrial, and agricultural uses of the antibacterial, oxidizing, and reactive properties of iodine. There are uses as raw materials and intermediates for various products such as for use. The usage scene and usage amount tend to increase. With regard to the supply of iodine that is useful and has many needs, iodine is often present as a water-soluble salt in nature, and its distribution is sparse, so mining requires large-scale facilities, This can lead to high costs. Therefore, iodine is positioned as a rare resource with limited output.

このように貴重な資源であるヨウ素の再使用は、増える需要を賄う意味、さらには、高濃度での排出を防止して環境負荷を軽減する意味として重要な課題となっている。   Thus, the reuse of iodine, which is a valuable resource, has become an important issue in terms of meeting increasing demand and further reducing the environmental burden by preventing discharge at high concentrations.

ヨウ素は高価であり反応性が高いことから、安易に使用できない物質である。そのため、ヨウ素の使用時、一度に使用するヨウ素の量は少ない。さらには環境負荷軽減への社会の認識が必ずしも高くなかったことから、ごくまれな例を除いて、使用後のヨウ素成分は、そのまま排水されるか、または産業廃棄物として処理されていた。これまでに知られているヨウ素成分の回収技術は、ヨウ素成分を含む液を燃焼し、得られた焼却灰などを精製処理することであり、有用な資源であるべきヨウ化物を含む液に関しては、ただ単に発生した排水として、処理施設へ送るための仕様があるに過ぎなかった(特許文献1および2参照)。   Iodine is a substance that cannot be easily used because it is expensive and highly reactive. Therefore, when using iodine, the amount of iodine used at a time is small. Furthermore, since the public's awareness of reducing the environmental burden was not necessarily high, except for rare cases, the iodine component after use was either drained as it was or treated as industrial waste. The iodine component recovery technology known so far is burning the liquid containing the iodine component and purifying the resulting incinerated ash, etc. Regarding the liquid containing iodide that should be a useful resource, However, there was only a specification for sending it to a treatment facility as wastewater generated (see Patent Documents 1 and 2).

資源回収を前提とした、ヨウ素成分を含む液の扱いに関しては、ヨウ素が昇華しやすい性質を有し、腐食性を有する劇物であることを念頭に置かなければならない。ヨウ素成分を含む溶液は、生物および環境への影響を考慮して、特に保管および運搬時の安定性・安全性に対する配慮をしなければならないが、安定にかつ安全に保管・運搬する手段を強いてあげれば、空気酸化によりヨウ素が発生しないように、密閉性が高い容器を用意し、その容器内を窒素置換して充填する方法がある。容器の密閉性を確保することは、コスト高を招き回収事業自体の存続性に不利であるのみならず、気温差による容器内の圧力変化が発生することから、容器の材質は金属など強度があるものに限られ、大重量になるがゆえに取り扱い上も不利な点が多い(特許文献3参照)。さらに、廃液が酸性であれば、容器の材質は、単に金属をつかえばよいというものではなく、ハステロイなどの特殊合金や、テフロン(登録商標)コーティング仕様など加工が煩雑で高価なものになる。
特開昭51−34896号公報 特開2004−35302号公報 特開2004−331155号公報
Regarding the handling of liquids containing iodine components on the premise of resource recovery, it must be kept in mind that iodine is a deleterious substance having the property of easily sublimating and corrosive. For solutions containing iodine components, consideration must be given to the stability and safety during storage and transportation in consideration of the impact on living organisms and the environment, but there must be a means for stable and safe storage and transportation. For example, there is a method of preparing a container with high hermeticity so that iodine is not generated by air oxidation, and filling the container with nitrogen. Ensuring the sealing of the container is not only disadvantageous for the sustainability of the collection business itself, but also increases the cost, and also changes in pressure in the container due to temperature differences. There are many disadvantages in handling because it is limited to certain things and becomes heavy (see Patent Document 3). Furthermore, if the waste liquid is acidic, the material of the container is not limited to simply using a metal, but processing such as a special alloy such as Hastelloy or Teflon (registered trademark) coating is complicated and expensive.
Japanese Patent Laid-Open No. 51-34896 JP 2004-35302 A JP 2004-331155 A

したがって、本発明の目的は、貴重な資源であるヨウ素成分の回収処理を効率的に行うために、安価で安定にかつ安全にヨウ素成分を含む溶液を運搬する方法、およびこれに用いられる容器を提供することにある。   Accordingly, an object of the present invention is to provide a method for transporting a solution containing an iodine component in an inexpensive, stable and safe manner, and a container used therefor, in order to efficiently recover a iodine component, which is a valuable resource. It is to provide.

上記の課題は、下記の(1)〜(7)により解決される。   Said subject is solved by following (1)-(7).

(1)単体ヨウ素、ヨウ素元素を含む化合物、ヨウ素イオン、およびヨウ素元素を含むイオンからなる群より選択される少なくとも1種の濃度が10質量%未満である液に、アルカリ化合物を添加してpHを調整する工程と、
単体ヨウ素、ヨウ素元素を含む化合物、ヨウ素イオン、およびヨウ素元素を含むイオンからなる群より選択される少なくとも1種の濃度が10〜40質量%である濃縮液を得るために、前記pHを調整する工程で得られた液を濃縮する工程と、
前記濃縮液を運搬する工程と、
を含むことを特徴とする、液の運搬方法。
(1) An alkaline compound is added to a solution having a concentration of at least one selected from the group consisting of simple iodine, a compound containing iodine element, iodine ion, and an ion containing iodine element of less than 10% by mass, and pH Adjusting the process,
In order to obtain a concentrated solution having a concentration of 10 to 40% by mass selected from the group consisting of simple iodine, a compound containing iodine element, iodine ion, and ion containing iodine element, the pH is adjusted. A step of concentrating the liquid obtained in the step;
Carrying the concentrated liquid;
A method for transporting a liquid, comprising:

(2)前記pHを調整する工程で得られる液のpHが7〜13であることを特徴とする、前記(1)に記載の方法。   (2) The method according to (1) above, wherein the pH of the liquid obtained in the step of adjusting the pH is 7 to 13.

(3)前記pHを調整する工程で、アルカリ化合物が添加される前の液が、単体ヨウ素、アルカリ金属およびヨウ素元素を含む化合物、アルカリ土類金属およびヨウ素元素を含む化合物、ならびにヨウ化アンモニウムからなる群より選択される少なくとも1種の物質を含むことを特徴とする、前記(1)または(2)に記載の方法。   (3) In the step of adjusting the pH, the solution before the alkali compound is added is composed of simple iodine, a compound containing an alkali metal and an iodine element, a compound containing an alkaline earth metal and an iodine element, and ammonium iodide. The method according to (1) or (2) above, comprising at least one substance selected from the group consisting of:

(4)前記アルカリ化合物が水酸化アルカリであることを特徴とする、前記(1)〜(3)のいずれか1つに記載の方法。   (4) The method according to any one of (1) to (3), wherein the alkali compound is an alkali hydroxide.

(5)前記(1)〜(4)のいずれか1つに記載の方法に含まれる、液を濃縮する工程で得られた濃縮液を収容して、保管および運搬するための容器。   (5) A container for storing and transporting the concentrated liquid obtained in the process of concentrating liquid, which is included in the method according to any one of (1) to (4).

(6)前記容器は、圧力調整穴を備えていることを特徴とする、前記(5)に記載の容器。   (6) The container according to (5), wherein the container includes a pressure adjustment hole.

(7)前記容器の形態がドラム缶、タンク、またはコンテナーであることを特徴とする、前記(5)または(6)に記載の容器。   (7) The container according to (5) or (6) above, wherein the container is in the form of a drum, a tank, or a container.

本発明によれば、回収すべきヨウ素成分を含む液を安価で、安定にかつ安全に運搬することができる。   According to the present invention, a liquid containing an iodine component to be recovered can be transported inexpensively, stably and safely.

図1は、回収すべきヨウ素成分を含む液(以後、回収液と呼ぶ)を安定に保管し、安全に運搬するための処理工程を示したフローシートである。回収液は、単体ヨウ素、ヨウ素元素を含む化合物、ヨウ素イオン、およびヨウ素元素を含むイオンからなる群より選択される少なくとも1種(以後、ヨウ素分と呼ぶ)を含む。詳細には、ヨウ素分としては、単体ヨウ素、ヨウ化ナトリウム、ヨウ化カリウム、ヨウ化リチウム、ヨウ素酸ナトリウム、ヨウ素酸カリウム等のアルカリ金属およびヨウ素元素を含む化合物、ヨウ化カルシウム、ヨウ化マグネシウム、ヨウ化バリウム、ヨウ素酸カルシウム、ヨウ素酸マグネシウム等のアルカリ土類金属およびヨウ素元素を含む化合物、ヨウ化アンモニウム、ヨウ化ユウロピウム、ヨウ化銅、ヨウ化亜鉛、ヨウ素酸バリウム、またはこれらの水和物等のヨウ素元素を含む無機化合物、ヨウ化メチル、ヨウ化エチル等のヨウ素元素を含む有機化合物などが好ましく、単体ヨウ素、アルカリ金属およびヨウ素元素を含む化合物、アルカリ土類金属およびヨウ素元素を含む化合物、ならびにヨウ化アンモニウムがより好ましい。また、回収液中のヨウ素分の濃度は10質量%未満、好ましくは2〜8質量%である。   FIG. 1 is a flow sheet showing processing steps for stably storing a liquid containing an iodine component to be recovered (hereinafter referred to as a recovered liquid) and transporting it safely. The recovered liquid contains at least one selected from the group consisting of simple iodine, a compound containing iodine element, iodine ion, and ion containing iodine element (hereinafter referred to as iodine content). Specifically, the iodine content includes simple iodine, sodium iodide, potassium iodide, lithium iodide, sodium iodate, potassium iodate and other compounds containing an alkali metal and iodine element, calcium iodide, magnesium iodide, Compounds containing alkaline earth metals and elemental iodine such as barium iodide, calcium iodate, magnesium iodate, ammonium iodide, europium iodide, copper iodide, zinc iodide, barium iodate, or hydrates thereof Inorganic compounds containing iodine element such as iodine, organic compounds containing iodine element such as methyl iodide, ethyl iodide, etc. are preferable, simple iodine, compounds containing alkali metal and iodine element, compounds containing alkaline earth metal and iodine element And ammonium iodide is more preferred. The concentration of iodine in the recovered liquid is less than 10% by mass, preferably 2-8% by mass.

pH調整工程2では、アルカリ化合物、好ましくは水酸化カリウム、水酸化ナトリウム等の水酸化アルカリであるpH調整剤3を回収液に添加して、pHを7以上に調整する工程である。回収液が次工程で濃縮される間または回収液の保管および運搬中の液温上昇や液性変化などにより、昇華性のあるヨウ素単体が発生および飛散して回収されるべきヨウ素量が減少すること、人に対する毒性、ならびに装置および容器の素材の劣化などを防ぐために、ヨウ素分が含まれている液のpHを、昇華性のあるヨウ素単体が発生しやすい酸性条件からアルカリ性条件に変えることが必要となる。アルカリ化合物を添加した後の液のpHは、7〜13が好ましく、より好ましくは7.5〜13、さらに好ましくは8〜12である。過度のアルカリ化は無用にアルカリを消費するため好ましくない。ヨウ化アンモニウムにおいては、液の温度変化や液の物性変化で容易に分解することが知られている。ヨウ化アンモニウムが含まれている液に、予め強い塩基を作用させれば、本発明の効果のみならず、保管や運搬に先立ってヨウ化アンモニウムからアンモニアをガスとして追い出し、このアンモニアガスを、スクラバーなどで安全に除去でき、保管や運搬中の予期せぬガス発生を防止できる効果もある。この際、回収液のヨウ素分の濃度が例えば、10質量%以上あり、特に濃縮を実施しなくてもよい場合はそのまま濃縮回収液6として扱うことが可能である。   In the pH adjusting step 2, a pH adjusting agent 3 which is an alkali compound, preferably an alkali hydroxide such as potassium hydroxide or sodium hydroxide is added to the recovered liquid to adjust the pH to 7 or more. While the recovered liquid is concentrated in the next step or due to a rise in liquid temperature or a change in liquid properties during storage and transportation of the recovered liquid, sublimable iodine is generated and scattered, reducing the amount of iodine to be recovered In order to prevent toxicity to humans and deterioration of the materials of the device and container, the pH of the liquid containing iodine can be changed from acidic conditions where sublimable iodine is easily generated to alkaline conditions. Necessary. The pH of the liquid after adding the alkali compound is preferably 7 to 13, more preferably 7.5 to 13, and still more preferably 8 to 12. Excessive alkalization is undesirable because it consumes alkali unnecessarily. It is known that ammonium iodide is easily decomposed by a change in liquid temperature or a change in physical properties of the liquid. If a strong base is allowed to act on a solution containing ammonium iodide in advance, not only the effect of the present invention but also ammonia is expelled from ammonium iodide as a gas prior to storage and transportation. It can be removed safely, and can prevent unexpected gas generation during storage and transportation. At this time, the concentration of iodine in the recovered liquid is, for example, 10% by mass or more, and when the concentration does not need to be performed, it can be handled as the concentrated recovered liquid 6 as it is.

濃縮工程4では、比較的ヨウ素分の濃度が低い回収液を濃縮して、保管や運搬の利便性の向上を図る。濃縮方法は、通常行われている液の濃縮方法を行えばよいが、昇華性のあるヨウ素単体の発生を防止するために、本発明の方法は、濃縮の前にアルカリ化合物を添加する工程を含む。本発明の方法では、常圧下または減圧下での蒸発濃縮方法が好ましい。アルカリ化合物の添加を行うことで、装置および容器の材質、特に金属への腐食性が軽減され、熱伝導性に優れた金属素材を装置類に使用できる利点がある。また、この濃縮の際に副生する凝縮水5は、蒸留水として直ちに再利用が可能となる利点がある。回収液の濃縮の程度は、ヨウ素分の濃度として10〜40質量%となるように行う。過度の濃縮は、濃縮液の粘度および比重の上昇による取り扱い上の不利、結晶成分の析出による濃縮液の突沸などの事態を招きやすいことから、濃縮後の液のヨウ素分の濃度を、好ましくは20〜30質量%とする。回収液が有機溶剤を含む場合には、濃縮の工程で除去が可能であり、有機溶剤を含まない場合には、濃縮の工程で得られる凝縮水5が良質な工業用水として再利用が可能である。濃縮回収液6は、その後の工程となる保管7、または運搬8に供すべく管理される。   In the concentration step 4, the recovered liquid having a relatively low iodine content is concentrated to improve the convenience of storage and transportation. The concentration method may be a conventional method for concentrating liquids, but in order to prevent generation of sublimable iodine alone, the method of the present invention includes a step of adding an alkali compound before concentration. Including. In the method of the present invention, an evaporation concentration method under normal pressure or reduced pressure is preferable. By adding an alkali compound, the corrosiveness to the material of the apparatus and the container, particularly the metal is reduced, and there is an advantage that a metal material having excellent thermal conductivity can be used for the apparatus. Further, the condensed water 5 by-produced during the concentration has an advantage that it can be reused immediately as distilled water. The degree of concentration of the collected liquid is 10 to 40% by mass as the iodine content. Excessive concentration is likely to cause disadvantages in handling due to an increase in the viscosity and specific gravity of the concentrate, and bumping of the concentrate due to precipitation of crystal components, so the concentration of iodine in the concentrated liquid is preferably 20 to 30% by mass. If the recovered liquid contains an organic solvent, it can be removed in the concentration step. If it does not contain the organic solvent, the condensed water 5 obtained in the concentration step can be reused as high-quality industrial water. is there. The concentrated recovery liquid 6 is managed so as to be used for storage 7 or transportation 8 as a subsequent process.

図2には、前記にて得られた濃縮回収液6を安全に保管および運搬するための容器を示す。図中で示すものは、容量が1m程度のコンテナー10である。濃縮回収液6を、本体と同じ高さに調整した上部蓋11から、液面がコンテナー10の側面上部に設けてある圧力調整穴12を超えることのないようにポンプ等(図示せず)で充填する。保管・運搬に供する場合に、コンテナー10を積載したり、隙間なく並べたりできるように、突起部を極力減らした構造を有する上部蓋11、圧力調整穴12、および下部バルブ13が、コンテナー本体に対して窪んだ位置に設けてある。その後に液の回収処理を行うに当たっては、上部蓋11または下部バルブ13を経由して、回収処理装置に送液する。図3は、車載タンク20の概略図である。濃縮回収液6を、マンホール21または液入口バルブ22からポンプ等(図示せず)で車載タンク20に充填する。圧力調整穴24は、雨水などが直接入らないように、ノズルが下を向く形でタンク上部に設けてある。保管および運搬後に液の回収処理を行うに当たっては、マンホール21または液出口バルブ23を経由して送液する。コンテナーの素材としてはステンレスなどの金属、ポリエチレンなどの樹脂等が用いられうるが、特に制限はない。ポリエチレンなどの樹脂をコンテナーの素材としたときは、強度を保つために外周を金属枠などで覆うことが好ましい。 FIG. 2 shows a container for safely storing and transporting the concentrated and recovered liquid 6 obtained as described above. What is shown in the figure is a container 10 having a capacity of about 1 m 3 . From the upper lid 11 adjusted to the same height as the main body, the concentrated recovery liquid 6 is pumped or the like (not shown) so that the liquid level does not exceed the pressure adjustment hole 12 provided in the upper side of the container 10. Fill. An upper lid 11, a pressure adjusting hole 12, and a lower valve 13 having a structure in which protrusions are reduced as much as possible so that the containers 10 can be loaded or arranged without gaps when being stored and transported are provided on the container body. On the other hand, it is provided in a recessed position. Thereafter, when the liquid recovery process is performed, the liquid is sent to the recovery processing apparatus via the upper lid 11 or the lower valve 13. FIG. 3 is a schematic diagram of the in-vehicle tank 20. The concentrated recovery liquid 6 is filled into the in-vehicle tank 20 with a pump or the like (not shown) from the manhole 21 or the liquid inlet valve 22. The pressure adjustment hole 24 is provided in the upper portion of the tank so that the nozzle faces downward so that rainwater or the like does not enter directly. In performing the liquid recovery process after storage and transportation, the liquid is sent via the manhole 21 or the liquid outlet valve 23. As a material of the container, a metal such as stainless steel, a resin such as polyethylene can be used, but there is no particular limitation. When a resin such as polyethylene is used as the material of the container, it is preferable to cover the outer periphery with a metal frame or the like in order to maintain strength.

図4は、図2で説明した容器の使用形態の一例を示す概略図である。図で示すものは、図2に示したコンテナー10と同様の構造である、容器30の配置である。濃縮回収液6を、配管31を介してポンプ等(図示せず)で屋内または屋外に設置した容器30に送る。図5は、図2で説明したものと同様の構造を有する、コンテナー40による濃縮回収液の運搬の一実施形態であるが、例えばトラック42に積載した形で運ぶことができる。図6は、図3に示しているタンクローリーでの濃縮回収液の運搬を示す一実施形態であり、配管51を経由して、濃縮回収液が車載タンク50に送られる。   FIG. 4 is a schematic view showing an example of a usage pattern of the container described in FIG. What is shown in the figure is the arrangement of the container 30 having the same structure as the container 10 shown in FIG. The concentrated recovery liquid 6 is sent to a container 30 installed indoors or outdoors via a pipe 31 with a pump or the like (not shown). FIG. 5 shows an embodiment of transporting the concentrated recovery liquid by the container 40 having the same structure as that described with reference to FIG. FIG. 6 is an embodiment showing the transport of the concentrated recovery liquid in the tank lorry shown in FIG. 3, and the concentrated recovery liquid is sent to the in-vehicle tank 50 via the pipe 51.

このようにして得られた濃縮回収液は、必要によりヨウ素の回収工程に移される。例えば、濃縮回収液に塩素ガスを吹き込んで、その酸化作用によりヨウ素単体を析出させ、常法により回収することができる。   The concentrated recovery solution thus obtained is transferred to an iodine recovery step as necessary. For example, chlorine gas is blown into the concentrated recovery liquid, and simple iodine can be precipitated by its oxidizing action, and can be recovered by a conventional method.

つぎに、実施例を挙げて本発明をさらに詳細に説明する。なお、ヨウ素イオンの濃度の測定は、JIS規格 K8913 「よう化カリウム(試薬)」中の、「6.試験方法 (1)純度(乾燥後)」に記載されている測定方法を基に、ヨウ素酸カリウム滴定法により測定した。   Next, the present invention will be described in more detail with reference to examples. The measurement of iodine ion concentration is based on the measurement method described in “6. Test method (1) Purity (after drying)” in JIS standard K8913 “Potassium iodide (reagent)”. It measured by the acid potassium titration method.

(実施例1)
ヨウ素イオン濃度が8質量%であるヨウ化ナトリウム水溶液に水酸化ナトリウムを添加して、pHを9に調整した。ついで、得られた液を、蒸発缶を用いて濃縮して、ヨウ素イオン濃度が24質量%である濃縮液を得た。このようにして得られた濃縮液を、図3に示したものと同様のタンクローリーでヨウ素回収装置へ運搬した。
Example 1
Sodium hydroxide was added to an aqueous sodium iodide solution having an iodine ion concentration of 8% by mass to adjust the pH to 9. Next, the obtained liquid was concentrated using an evaporator to obtain a concentrated liquid having an iodine ion concentration of 24% by mass. The concentrated solution thus obtained was transported to an iodine recovery device by a tank lorry similar to that shown in FIG.

この濃縮液をヨウ素回収装置内に移し、濃縮液1kgに対して70gの割合で、塩素ガスを供給した。その後に生成した析出物をメルター釜へ移し、メルター釜の下部よりヨウ素を回収した。ヨウ素の回収率は、蒸発濃縮する前のヨウ化ナトリウム水溶液に含まれていたヨウ素イオンに対して95%であった。   This concentrated liquid was transferred into an iodine recovery apparatus, and chlorine gas was supplied at a rate of 70 g with respect to 1 kg of the concentrated liquid. Thereafter, the generated precipitate was transferred to a melter kettle, and iodine was collected from the lower part of the melter kettle. The iodine recovery rate was 95% with respect to iodine ions contained in the sodium iodide aqueous solution before being evaporated and concentrated.

(実施例2)
ヨウ素イオン濃度が約2質量%であるヨウ化カリウム溶液100gを作製した後、5質量%の水酸化カリウム水溶液を加え、ヨウ化カリウム溶液のpHを約12とした。その後は実施例1と同様にヨウ化カリウム溶液を蒸発濃縮し、ヨウ化カリウム溶液のヨウ素イオン濃度を測定した。結果を下記表1に示す。
(Example 2)
After preparing 100 g of a potassium iodide solution having an iodine ion concentration of about 2% by mass, a 5% by mass aqueous potassium hydroxide solution was added to adjust the pH of the potassium iodide solution to about 12. Thereafter, the potassium iodide solution was evaporated and concentrated in the same manner as in Example 1, and the iodine ion concentration of the potassium iodide solution was measured. The results are shown in Table 1 below.

(比較例)
ヨウ素イオン濃度が約2質量%であるヨウ化カリウム溶液100gを作製した後、5質量%の硫酸水溶液を加え、ヨウ化カリウム溶液のpHを約2とした。その後は実施例1と同様にヨウ化カリウム溶液を蒸発濃縮し、ヨウ化カリウム溶液のヨウ素イオン濃度を測定した。結果を下記表1に示す。
(Comparative example)
After preparing 100 g of a potassium iodide solution having an iodine ion concentration of about 2% by mass, a 5% by mass sulfuric acid aqueous solution was added to adjust the pH of the potassium iodide solution to about 2. Thereafter, the potassium iodide solution was evaporated and concentrated in the same manner as in Example 1, and the iodine ion concentration of the potassium iodide solution was measured. The results are shown in Table 1 below.

Figure 2006232662
Figure 2006232662

表1からわかるように、ヨウ化カリウム溶液を酸性とした場合、pH調整時から、遊離ヨウ素による液の着色が見られた。また、蒸発濃縮後のヨウ化カリウム溶液の理論値は20.12質量%であるが、これと比べて比較例は、ヨウ素イオン濃度が少ないことから、蒸発濃縮時にヨウ素が空気中に放出したものと考えられる。   As can be seen from Table 1, when the potassium iodide solution was acidified, the liquid was colored by free iodine from the time of pH adjustment. The theoretical value of the potassium iodide solution after evaporation and concentration is 20.12% by mass. Compared to this, the comparative example has a low iodine ion concentration, so that iodine was released into the air during evaporation and concentration. it is conceivable that.

一方、ヨウ化カリウム溶液をアルカリ性とした実施例2では、pH調整時の液の色変化がないことから、ヨウ素の遊離はないと考えられる。また、蒸発濃縮後のヨウ化カリウム溶液の濃度の値も、理論値とほぼ同じであることから、蒸発濃縮時のヨウ素の空気中への放出はほとんどないと考えられる。   On the other hand, in Example 2 in which the potassium iodide solution was made alkaline, there is no change in the color of the solution during pH adjustment, so it is considered that iodine is not liberated. Further, since the concentration value of the potassium iodide solution after evaporation and concentration is almost the same as the theoretical value, it is considered that there is almost no release of iodine into the air during evaporation and concentration.

本発明は、ヨウ素分を使用した後、ヨウ素分を回収する技術に係る分野に好適に用いられうる。   The present invention can be suitably used in the field related to a technique for recovering iodine after using iodine.

本発明の運搬方法の一実施形態を示すフローシートである。It is a flow sheet which shows one embodiment of the transportation method of the present invention. 本発明の運搬容器の一実施形態を示す概略図である。It is the schematic which shows one Embodiment of the conveyance container of this invention. 本発明の運搬容器の、他の実施形態を示す概略図である。It is the schematic which shows other embodiment of the conveyance container of this invention. 図2に示した本発明の運搬容器の、配置の一実施形態を示す概略図である。It is the schematic which shows one Embodiment of arrangement | positioning of the conveyance container of this invention shown in FIG. 本発明の運搬容器の、他の実施形態を示す概略図である。It is the schematic which shows other embodiment of the conveyance container of this invention. 本発明の運搬容器の、他の実施形態を示す概略図である。It is the schematic which shows other embodiment of the conveyance container of this invention.

符号の説明Explanation of symbols

1・・・回収液、
2・・・pH調整工程、
3・・・pH調整剤、
4・・・濃縮工程、
5・・・凝縮水、
6・・・濃縮回収液、
7・・・保管、
8・・・運搬、
10、40・・・コンテナー、
20、50・・・車載タンク、
30・・・容器、
11・・・上部蓋、
12、24・・圧力調整穴、
13・・・下部バルブ、
21・・・マンホール、
22・・・液入口バルブ、
23・・・液出口バルブ、
31、51・・・配管、
42・・・トラック。
1 ... recovered liquid,
2 ... pH adjustment step,
3 ... pH adjuster,
4 ... Concentration process,
5 ... condensed water,
6 ... concentrated recovery liquid,
7 ... Storage,
8 ... transport,
10, 40 ... container,
20, 50 ... Car tank,
30 ... container,
11 ... Upper lid,
12, 24 ... Pressure adjusting hole,
13 ... Lower valve,
21 ... Manhole,
22 ... Liquid inlet valve,
23 ... Liquid outlet valve,
31, 51 ... piping,
42 ... Track.

Claims (7)

単体ヨウ素、ヨウ素元素を含む化合物、ヨウ素イオン、およびヨウ素元素を含むイオンからなる群より選択される少なくとも1種の濃度が10質量%未満である液に、アルカリ化合物を添加してpHを調整する工程と、
単体ヨウ素、ヨウ素元素を含む化合物、ヨウ素イオン、およびヨウ素元素を含むイオンからなる群より選択される少なくとも1種の濃度が10〜40質量%である濃縮液を得るために、前記pHを調整する工程で得られた液を濃縮する工程と、
前記濃縮液を運搬する工程と、
を含むことを特徴とする、液の運搬方法。
The pH is adjusted by adding an alkali compound to a liquid having a concentration of at least one selected from the group consisting of simple iodine, a compound containing iodine element, iodine ions, and ions containing iodine element being less than 10% by mass. Process,
In order to obtain a concentrated solution having a concentration of 10 to 40% by mass selected from the group consisting of simple iodine, a compound containing iodine element, iodine ion, and ion containing iodine element, the pH is adjusted. A step of concentrating the liquid obtained in the step;
Carrying the concentrated liquid;
A method for transporting a liquid, comprising:
前記pHを調整する工程で得られる液のpHが7〜13であることを特徴とする、請求項1に記載の方法。   The method according to claim 1, wherein the pH of the liquid obtained in the step of adjusting the pH is 7 to 13. 前記pHを調整する工程で、アルカリ化合物が添加される前の液が、単体ヨウ素、アルカリ金属およびヨウ素元素を含む化合物、アルカリ土類金属およびヨウ素元素を含む化合物、ならびにヨウ化アンモニウムからなる群より選択される少なくとも1種の物質を含むことを特徴とする、請求項1または2に記載の方法。   In the step of adjusting the pH, the liquid before the alkali compound is added is selected from the group consisting of simple iodine, a compound containing an alkali metal and an iodine element, a compound containing an alkaline earth metal and an iodine element, and ammonium iodide. 3. The method according to claim 1 or 2, characterized in that it comprises at least one selected material. 前記アルカリ化合物が水酸化アルカリであることを特徴とする、請求項1〜3のいずれか1項に記載の方法。   The method according to claim 1, wherein the alkali compound is an alkali hydroxide. 請求項1〜4のいずれか1項に記載の方法に含まれる、液を濃縮する工程で得られた濃縮液を収容して、保管および運搬するための容器。   A container for storing, transporting, and storing the concentrated liquid obtained in the process of concentrating the liquid, which is included in the method according to claim 1. 前記容器は、圧力調整穴を備えていることを特徴とする、請求項5に記載の容器。   The container according to claim 5, wherein the container includes a pressure adjusting hole. 前記容器の形態がドラム缶、タンク、またはコンテナーであることを特徴とする、請求項5または6に記載の容器。   The container according to claim 5 or 6, wherein the container is in the form of a drum, a tank, or a container.
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KR20230138498A (en) 2021-03-05 2023-10-05 오르가노 코포레이션 Water treatment method and water treatment agent composition

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH01108101A (en) * 1987-10-22 1989-04-25 Nippo Kagaku Kk Separation and recovery of iodine
JP2002531358A (en) * 1998-11-27 2002-09-24 ブラッコ イメージング エッセ ピ ア Method for the recovery of iodine from aqueous solutions containing iodinated organic compounds
JP2004331155A (en) * 2003-05-07 2004-11-25 Kyowa Hakko Kogyo Co Ltd Container for storing/transporting liquid and method for storing/transporting liquid using the same

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH01108101A (en) * 1987-10-22 1989-04-25 Nippo Kagaku Kk Separation and recovery of iodine
JP2002531358A (en) * 1998-11-27 2002-09-24 ブラッコ イメージング エッセ ピ ア Method for the recovery of iodine from aqueous solutions containing iodinated organic compounds
JP2004331155A (en) * 2003-05-07 2004-11-25 Kyowa Hakko Kogyo Co Ltd Container for storing/transporting liquid and method for storing/transporting liquid using the same

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20230138498A (en) 2021-03-05 2023-10-05 오르가노 코포레이션 Water treatment method and water treatment agent composition

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