JPS5910924B2 - Manufacturing method of sodium hypochlorite - Google Patents

Manufacturing method of sodium hypochlorite

Info

Publication number
JPS5910924B2
JPS5910924B2 JP54028258A JP2825879A JPS5910924B2 JP S5910924 B2 JPS5910924 B2 JP S5910924B2 JP 54028258 A JP54028258 A JP 54028258A JP 2825879 A JP2825879 A JP 2825879A JP S5910924 B2 JPS5910924 B2 JP S5910924B2
Authority
JP
Japan
Prior art keywords
sodium hypochlorite
caustic soda
concentration
heavy metals
chlorine
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
Application number
JP54028258A
Other languages
Japanese (ja)
Other versions
JPS55121902A (en
Inventor
栄一 池田
邦彦 鈴木
秀樹 加藤
一彦 安藤
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.)
Toagosei Co Ltd
Original Assignee
Toagosei Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Toagosei Co Ltd filed Critical Toagosei Co Ltd
Priority to JP54028258A priority Critical patent/JPS5910924B2/en
Publication of JPS55121902A publication Critical patent/JPS55121902A/en
Publication of JPS5910924B2 publication Critical patent/JPS5910924B2/en
Expired legal-status Critical Current

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  • Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)

Description

【発明の詳細な説明】 本発明は隔膜法食塩電解により製造される苛性ソーダを
用いてその中に含まれる微量の重金属を除去し、これよ
り次亜塩素酸ソーダを製造する方法に関するものである
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing sodium hypochlorite by removing trace amounts of heavy metals contained in caustic soda produced by diaphragm salt electrolysis.

次亜塩素酸ソーダは強い酸化作用を持ち、漂白消毒及び
防臭用あるいは化学工業用原料として多量に使用されて
いる。
Sodium hypochlorite has a strong oxidizing effect and is used in large quantities for bleaching, disinfection, deodorization, and as a raw material for the chemical industry.

かかる次亜塩素酸ソーダの製造法としては、濃厚な苛性
ソーダを純水等で濃度調整し、これに塩素ガスを吸収反
応させ、濃度]−2%程度の次亜塩素酸ソーダとするか
、あるいは濃度25係程度の高濃度次亜塩素酸ソーダを
製造し、析出する食塩を分離し、濃度12%程度の次亜
塩素酸ソーダに希釈して市販されている。
The method for producing such sodium hypochlorite includes adjusting the concentration of concentrated caustic soda with pure water, etc., and then absorbing and reacting chlorine gas to obtain sodium hypochlorite with a concentration of about -2%, or Highly concentrated sodium hypochlorite with a concentration of about 25% is produced, precipitated salt is separated, and the product is diluted to sodium hypochlorite with a concentration of about 12% and sold commercially.

一般に隔膜法電解で得られる苛性ソーダは水銀法食塩電
解により得られる苛性ソーダに比べて濃縮工程に使用さ
れる蒸発缶の材質にニッケル、ステンレス鋼が用いられ
るため、ニッケル、クロム、鉄等の不純物が多く含まれ
ている。
In general, caustic soda obtained by diaphragm method electrolysis contains more impurities such as nickel, chromium, and iron than caustic soda obtained by mercury method salt electrolysis because nickel and stainless steel are used as materials for the evaporator used in the concentration process. include.

これら重金属を含有する苛性ソーダを原料に使用して製
造した次亜塩素酸ナトIJウムは分解性が大きく、有効
塩素酸濃度が減少し易くなるのみならず、これら不純物
を多く含有する次亜塩素酸ソーダを原料として各種製品
を製造する場合に悪影響を与え、最終的な製品の商品価
値をも低下させる原因となっている。
Sodium hypochlorite manufactured using caustic soda containing these heavy metals as a raw material is highly degradable, and not only does the effective chloric acid concentration easily decrease, but also the hypochlorous acid that contains many of these impurities. This has an adverse effect on the production of various products using soda as a raw material, and is a cause of lowering the commercial value of the final product.

従って従来は水銀法食塩電解による苛性ソーダが専ら原
料として使用されていたが、水銀法食塩電解の転換切換
えが推進されてきた現在隔膜法食塩電解による苛性ソー
ダから品質良好な次亜塩素酸ソーダを得ることが切望さ
れる。
Therefore, in the past, caustic soda produced by mercury-method salt electrolysis was used exclusively as a raw material, but now that a switch to mercury-method salt electrolysis has been promoted, it is now possible to obtain high-quality sodium hypochlorite from caustic soda produced by diaphragm-method salt electrolysis. is coveted.

本発明者らはこの様な情勢において税意研究の結果、隔
膜法苛性ソーダ中の重金属除去と重金属除去を行った隔
膜法苛性ソーダを使用して品質良好な次亜塩素酸ソーダ
を製造する方法を見出し本発明を完成するに至った。
Under these circumstances, the inventors of the present invention conducted tax-conscious research and discovered a method for producing high-quality sodium hypochlorite using the diaphragm-method caustic soda that had undergone the removal of heavy metals and the heavy metals removed. The present invention has now been completed.

本発明は隔膜法食塩電解により得られた苛性ソーダを、
次亜塩素酸ソーダ濃度として0.001〜5%の範囲で
部分塩素化して含有する重金属類を析出させ、沢過によ
って該重金属類を除去した部分塩素化液を塩素ガスと反
応させることを特徴とする次亜塩素酸ソーダの製造法で
ある。
The present invention uses caustic soda obtained by diaphragm method salt electrolysis,
It is characterized by partially chlorinating the sodium hypochlorite concentration in the range of 0.001 to 5% to precipitate the contained heavy metals, and then reacting the partially chlorinated liquid from which the heavy metals have been removed by filtration with chlorine gas. This is a method for producing sodium hypochlorite.

本発明力法において隔嘆法苛性ソーダを部分塩素化し沢
過する工程では、苛性ソーダ濃度に制限はないが特に高
濃度の苛性ソーダを部分塩素化する場合、苛性ソーダ濃
度は殆んど希釈されることなく、苛性ソーダ中のニッケ
ル化合物を選択的に除去することができるので有利であ
る。
In the process of partially chlorinating and filtering caustic soda in the method of the present invention, there is no limit to the concentration of caustic soda, but especially when partially chlorinating caustic soda with a high concentration, the concentration of caustic soda is hardly diluted, This is advantageous because the nickel compounds in the caustic soda can be selectively removed.

塩素化率は次亜塩素酸ソーダ濃度o.oo1.%以七で
あれば良く過剰に塩素化することは重金属除去の目的か
らは意味がなくその上限は5%までが好ましい。
The chlorination rate is determined by the concentration of sodium hypochlorite o. oo1. Excessive chlorination is meaningless from the purpose of removing heavy metals, and the upper limit is preferably 5%.

一般に次亜塩素酸ソーダを製造する場合、原料中に重金
属が含有されていると苛性ソーダに塩素を吸収反応させ
る際に次亜塩素酸ソーダの分解が促進され、又製造工程
中の分解及び製品の安定性を悪くシ、製品当りの塩素の
量が多くなる。
Generally, when producing sodium hypochlorite, if heavy metals are contained in the raw materials, the decomposition of the sodium hypochlorite will be accelerated when chlorine is absorbed and reacted with caustic soda, and the decomposition during the manufacturing process and product damage will occur. Stability deteriorates and the amount of chlorine per product increases.

特に隔膜法苛性ソーダを使用して次亜塩素酸ソーダを製
潰する場合には上記の現象が著しい。
The above phenomenon is particularly noticeable when crushing sodium hypochlorite using diaphragm method caustic soda.

従って本発明者らはこれらの欠点を除くため隔膜法苛性
ソーダの部分塩素化を行い重金属特にニッケル化合物を
除去した苛性ソーダを使用することにより上述のような
分解もなく、製品当りの使用塩素量も水銀法電解で得ら
れる苛性ソーダと同等の結果が得られることを知った。
Therefore, in order to eliminate these drawbacks, the present inventors partially chlorinated caustic soda using a diaphragm method to remove heavy metals, especially nickel compounds, thereby eliminating the decomposition described above and reducing the amount of chlorine used per product from mercury. I learned that results comparable to those obtained by electrolyzing caustic soda can be obtained.

又高濃度次亜塩素酸ソーダを製造する場合、析出する食
塩は隔膜法苛性ソーダを部分塩素化せず使用した場合に
は粒径が小さく、食塩の結晶の分離には付着母液量が多
く、上述の次亜塩素酸ソーダの分解も著しいが、本発明
力法によって部分塩素化し涙過した隔嘆法精製苛性ソー
ダを用いた場合には析出する食塩の粒径も大きく分解も
少ない1以下に実施例及び比較例を挙げて本発明を説明
する。
In addition, when producing high-concentration sodium hypochlorite, the precipitated salt has a small particle size when the diaphragm method caustic soda is used without partial chlorination, and the amount of adhering mother liquor is large for the separation of salt crystals. The decomposition of sodium hypochlorite is also significant, but when using the separated method purified caustic soda that has been partially chlorinated and filtered by the method of the present invention, the particle size of the precipitated common salt is large and the decomposition is small. The present invention will be explained with reference to and comparative examples.

これらの中で「部」および「係」はいずれも重量による
ものである。
In these, "department" and "department" are both based on weight.

実施例1,2および比較例1ならびに参考例1隔嘆法苛
性ソーダ(濃度48弼)に塩素を吹込み部分塩素化した
のち、これを溶液の重量に対し15%の珪藻十をボディ
ーコ−1・シた沢布パレイン(中尾フィルターエ業■製
)にて加圧瀘過し、得られた溶液の重金属濃度次亜塩素
酸濃度を測定した。
Examples 1 and 2 and Comparative Example 1 and Reference Example 1 After partially chlorinating chlorine by blowing chlorine into caustic soda (concentration: 48 sq.), this was mixed with 15% of the weight of diatoms based on the weight of the solution. The solution was filtered under pressure using Shitazawa Cloth Parein (manufactured by Nakao Filter Engineering), and the heavy metal concentration and hypochlorous acid concentration of the resulting solution were measured.

次いでこれらの沖液を純水で調整し濃度19070の苛
性ソーダ溶液となし、その1953部に塩素ガス277
部を反応させ、12.9%濃度の次亜塩素酸ソーダ溶液
222部を得た。
Next, these Oki liquids were adjusted with pure water to make a caustic soda solution with a concentration of 19070, and 277 parts of chlorine gas was added to 1953 parts of the solution.
222 parts of a 12.9% sodium hypochlorite solution were obtained.

この溶液に更に48係苛性ソーダ260部を加え、塩素
ガス99.6部を徐々に加えて反応させ、反応終了後析
出食塩を分離し25.2%の次亜塩素酸ソーダ溶液を得
た4尚反応温度は20℃に保持した。
Further, 260 parts of 48% caustic soda was added to this solution, and 99.6 parts of chlorine gas was gradually added to react. After the reaction, precipitated salt was separated to obtain a 25.2% sodium hypochlorite solution. The reaction temperature was maintained at 20°C.

これらの結果を第1表に示す。These results are shown in Table 1.

尚、隔嘆法苛性ソーダについてこれを部分塩素化せずに
沖過し、上記と同様に塩素と反応させて次亜塩素酸ソー
ダを製造した場合(比較例1)および水銀法苛性ソーダ
を用いて同様に部分塩素化せずに沖過し塩素との反応で
次亜塩素酸ソーダを製造した場合(参考例1)について
の結果も併せて第1表に示す。
In addition, when sodium hypochlorite was produced by filtrating caustic soda without partial chlorination and reacting with chlorine in the same manner as above (Comparative Example 1), and when using mercury method caustic soda, the same results were obtained. Table 1 also shows the results for the case where sodium hypochlorite was produced by reaction with offshore chlorine without partial chlorination (Reference Example 1).

Claims (1)

【特許請求の範囲】[Claims] 1 隔膜法食塩電解により得られた苛性ソーダを、次亜
塩素酸ソーダ濃度として0.001〜5係の範囲で部分
塩素化して含有する重金属類を析出させ、濾過によって
該重金属類を除去した部分塩素化液を塩素ガスと反応さ
せることを特徴とする次亜塩素酸ソーダの製造法。
1 Caustic soda obtained by diaphragm method salt electrolysis is partially chlorinated to a concentration of sodium hypochlorite in the range of 0.001 to 5 parts to precipitate the heavy metals contained, and the heavy metals are removed by filtration.Partial chlorination A method for producing sodium hypochlorite, which is characterized by reacting a chemical solution with chlorine gas.
JP54028258A 1979-03-13 1979-03-13 Manufacturing method of sodium hypochlorite Expired JPS5910924B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP54028258A JPS5910924B2 (en) 1979-03-13 1979-03-13 Manufacturing method of sodium hypochlorite

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP54028258A JPS5910924B2 (en) 1979-03-13 1979-03-13 Manufacturing method of sodium hypochlorite

Publications (2)

Publication Number Publication Date
JPS55121902A JPS55121902A (en) 1980-09-19
JPS5910924B2 true JPS5910924B2 (en) 1984-03-12

Family

ID=12243535

Family Applications (1)

Application Number Title Priority Date Filing Date
JP54028258A Expired JPS5910924B2 (en) 1979-03-13 1979-03-13 Manufacturing method of sodium hypochlorite

Country Status (1)

Country Link
JP (1) JPS5910924B2 (en)

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4947292A (en) * 1972-08-31 1974-05-07
JPS5288598A (en) * 1976-01-21 1977-07-25 Toagosei Chem Ind Co Ltd Production of sodium hypochlorite

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4947292A (en) * 1972-08-31 1974-05-07
JPS5288598A (en) * 1976-01-21 1977-07-25 Toagosei Chem Ind Co Ltd Production of sodium hypochlorite

Also Published As

Publication number Publication date
JPS55121902A (en) 1980-09-19

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