JPH0617221B2 - Crystal growth method of sodium bicarbonate - Google Patents

Crystal growth method of sodium bicarbonate

Info

Publication number
JPH0617221B2
JPH0617221B2 JP9355985A JP9355985A JPH0617221B2 JP H0617221 B2 JPH0617221 B2 JP H0617221B2 JP 9355985 A JP9355985 A JP 9355985A JP 9355985 A JP9355985 A JP 9355985A JP H0617221 B2 JPH0617221 B2 JP H0617221B2
Authority
JP
Japan
Prior art keywords
sodium bicarbonate
sodium
crystals
crystal growth
crystal
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
Application number
JP9355985A
Other languages
Japanese (ja)
Other versions
JPS61256919A (en
Inventor
圭一 中矢
末一 平田
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.)
AGC Inc
Original Assignee
Asahi Glass 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 Asahi Glass Co Ltd filed Critical Asahi Glass Co Ltd
Priority to JP9355985A priority Critical patent/JPH0617221B2/en
Publication of JPS61256919A publication Critical patent/JPS61256919A/en
Publication of JPH0617221B2 publication Critical patent/JPH0617221B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Crystals, And After-Treatments Of Crystals (AREA)

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は、水溶液中から重炭酸ソーダを析出させる際に
その母液中に酒石酸ソーダまたはその誘導体を添加する
ことを特徴とする重炭酸ソーダの結晶成長法に関するも
のである。
TECHNICAL FIELD The present invention relates to a sodium bicarbonate crystal growth method characterized by adding sodium tartrate or a derivative thereof to a mother liquor when precipitating sodium bicarbonate from an aqueous solution. It is a thing.

[従来の技術] 純度の高いカセイソーダまたは炭酸ソーダと炭酸ガスか
ら重炭酸ソーダを製造する際に析出する結晶は、針状に
近い微細なものになりやすく、これが濾過工程における
目ずまりや水切りの悪さ、乾燥工程における微粉の飛散
による歩留りの低下、乾燥温度の上昇による重炭酸ソー
ダの熱分解、結晶塊の生成、スケールの付着など種々の
トラブルの原因となっている。また製品重炭酸ソーダも
その結果として粒度が小さく、かつ固結しやすく、水
分、炭酸ソーダ分が多いなど、品質上問題があり、さら
に使用に際して微粉の飛散、流動性の悪さ、固結などの
難点を含んでいる。
[Prior Art] Crystals that precipitate during the production of sodium bicarbonate from high-purity caustic soda or sodium carbonate and carbon dioxide gas are likely to become fine needle-like particles, which may cause clogging in the filtration process, poor drainage, and dryness. This causes various problems such as a decrease in yield due to scattering of fine powder in the process, thermal decomposition of sodium bicarbonate due to increase in drying temperature, formation of crystal lumps, and scale adhesion. In addition, as a result, the product sodium bicarbonate has a small particle size and is easy to congeal, and there are problems in quality such as a large amount of water and sodium carbonate, and there are problems such as scattering of fine powder, poor fluidity, and congealing during use. Contains.

粒度を大きくする試みとして、従来、結晶成長時間を長
くすること、結晶種を添加すること、炭酸ガス濃度を変
えること等の試みがなされているが、いずれも決定的を
解決を得るに至っていない。また、この他に媒晶剤を添
加する方法も知られている(例えば、特公昭48−17160
号公報)。しかし、例えば、特公昭48−17160号公報に
記載されるようなポリアクリル酸塩を用いた場合には、
得られる重炭酸ソーダを例えば酸性下で使用する時、製
品中に残存したポリアクリル酸塩が水不溶性物質として
浮上する等の問題がある。
As attempts to increase the grain size, attempts have been made to lengthen the crystal growth time, add crystal seeds, change the carbon dioxide gas concentration, etc., but none of them have reached a definitive solution. . In addition, a method of adding a habit modifier is also known (for example, Japanese Patent Publication No. 48-17160).
Issue). However, for example, when using a polyacrylate as described in JP-B-48-17160,
When the obtained sodium bicarbonate is used, for example, under acidic conditions, there is a problem that the polyacrylic acid salt remaining in the product floats up as a water-insoluble substance.

[発明の解決しようとする問題点] 本発明は水溶液から、結晶の大きな、かつ立方体に近い
形状を有する重炭酸ソーダを得るために有効な媒晶剤を
提供すべく研究された結果見出されたものである。
[Problems to be Solved by the Invention] The present invention was found as a result of research to provide an effective habit modifier for obtaining sodium bicarbonate having large crystals and a shape close to a cube from an aqueous solution. Is.

さらに、製品中に微量の媒晶剤が残存しても爾後の使用
に際して何ら問題にならない媒晶剤を提供することも本
発明の目的である。
Further, it is an object of the present invention to provide a habit modifier which does not cause any problem in subsequent use even if a trace amount of habit modifier remains in the product.

[問題点を解決するための手段] 本発明者等は、上述の目的を達するのに酒石酸ソーダま
たは、その誘導体が有効であることを見出し、本発明を
完成されたもので、かくして、本発明は、蒸発、冷却、
反応による析出等の方法で水溶液から重炭酸ソーダ結晶
を析出させるにあたり、母液中に少量の酒石酸ソーダま
たはその誘導体を添加することを特徴とする重炭酸ソー
ダ結晶の成長法を要旨とするものである。
[Means for Solving Problems] The present inventors have found that sodium tartrate or a derivative thereof is effective in achieving the above-mentioned object, and completed the present invention. Thus, the present invention Evaporates, cools,
A method for growing a sodium bicarbonate crystal is characterized in that a small amount of sodium tartrate or a derivative thereof is added to a mother liquor when a sodium bicarbonate crystal is precipitated from an aqueous solution by a method such as precipitation by reaction.

酒石酸ソーダまたはその誘導体の使用量の範囲は使用す
る物質による差はあるが、通常1ppmから50000ppmの広範
囲にわたって有効でかつ得られる結晶型、粒度分布は濃
度によって連続的に変化するが、製品への混入や、製品
コスト等の関係から上限は5000ppm位とするのが好まし
い。また、5000ppmより多量に存在させても立方体とし
ての形状はほとんど変らない。
Although the range of the amount of sodium tartrate or its derivative to be used varies depending on the substance used, it is usually effective over a wide range from 1 ppm to 50,000 ppm, and the obtained crystal form and particle size distribution continuously change depending on the concentration. It is preferable to set the upper limit to about 5000 ppm in consideration of mixing and product cost. Also, even if it is present in an amount of more than 5000 ppm, the shape of the cube remains almost unchanged.

酒石酸ソーダの濃度が減少するにつれて、得られる結晶
は、縦長のものになる。そして、酒石酸ソーダの濃度が
500ppmでは、結晶の縦横比(柱状結晶の高さと、柱の断
面の有効直径との比)は10〜20、100ppmでは50〜100と
なる(ここで有効直径とは柱の断面積と同面積の円の直
径をいう。)。従って、酒石酸ソーダ濃度の下限も用途
によるが500ppm程度が適当である。
As the concentration of sodium tartrate decreases, the resulting crystals become elongated. And the concentration of sodium tartrate
At 500 ppm, the aspect ratio of the crystal (the ratio of the height of the columnar crystal to the effective diameter of the cross section of the column) is 10 to 20, and at 100 ppm it is 50 to 100 (where the effective diameter is the same area as the cross section of the column. The diameter of the circle. Therefore, the lower limit of the sodium tartrate concentration is about 500 ppm, although it depends on the application.

また、本発明の方法により、重炭酸ソーダの比較的細い
結晶を得、これを種晶として、好ましくは、酒石酸ソー
ダの存在しない水溶液から結晶成長させることも可能で
ある。
It is also possible to obtain a relatively fine crystal of sodium bicarbonate by the method of the present invention, and use this as a seed crystal, and preferably perform crystal growth from an aqueous solution free of sodium tartrate.

このようにすれば、得られる大粒径重炭酸ソーダ結晶は
不純物の極めて少ないものとなるため特に高純度の製品
を得るのに適している。
By doing so, the obtained sodium bicarbonate crystal having a large particle size has very few impurities, which is particularly suitable for obtaining a high-purity product.

なお、酒石酸ソーダまたはその誘導体による媒晶作用
は、共存する塩素イオンやアンモニウムイオン等によつ
て妨害されることはないから本発明の方法がアンモニア
ンソーダ法の重炭酸ソーダ製造工程にも利用し得ること
は勿論であり、その他水溶液からの重炭酸ソーダ結晶析
出法には、蒸発によるもの、冷却によるもの、あるいは
反応によるものがあるが、それらに応用し得ることを見
い出した。
In addition, since the habit crystallization effect of sodium tartrate or its derivative is not disturbed by coexisting chlorine ions, ammonium ions, etc., the method of the present invention can be used in the sodium bicarbonate production process of the ammoniacal soda method. Of course, other methods for precipitating sodium bicarbonate crystals from an aqueous solution include evaporation, cooling, and reaction, and they have been found to be applicable.

以下に本発明の実施例を示すが、これに限定されるもの
ではない。
Examples of the present invention will be shown below, but the invention is not limited thereto.

[実施例] 実施例1 60℃の重炭酸ソーダ飽和溶液200mlに酒石酸ソーダ1gを
溶解し、10℃/時の速さで10℃まで冷却し、約300μ程
度の正立方状結晶を得た。これに対し酒石酸ソーダを加
えなかた場合は、60μ×10μ程度の微細な針状結晶しか
得られなかった。
Example 1 1 g of sodium tartrate was dissolved in 200 ml of a saturated sodium bicarbonate solution at 60 ° C., and the mixture was cooled to 10 ° C. at a rate of 10 ° C./hour to obtain a cubic crystal of about 300 μm. On the other hand, when sodium tartrate was not added, only fine needle-like crystals of about 60 μ × 10 μ were obtained.

実施例2 15%カセイソーダ溶液200mlに酒石酸アンモニウム0.5g
を溶解し、温度を70℃に保ちつつ炭酸ガスを吹き込み、
重炭酸化が充分進行した時点でなおも炭酸ガスを吹き込
みつつ10℃/時の速さで10℃まで冷却した。得られた結
晶は500μ×300μの柱状結晶および約300μ立方の結晶
を多数含み、酒石酸アンモニウムを添加しない場合に比
べ著しく結晶が成長した。
Example 2 0.5 g of ammonium tartrate was added to 200 ml of 15% caustic soda solution.
Is dissolved and carbon dioxide is blown in while maintaining the temperature at 70 ° C.
When the bicarbonate was sufficiently advanced, the carbon dioxide gas was still blown in, and the mixture was cooled to 10 ° C at a rate of 10 ° C / hour. The obtained crystals contained many columnar crystals of 500 μ × 300 μ and many crystals of about 300 μ cubic, and the crystals grew remarkably as compared with the case where ammonium tartrate was not added.

実施例3 酒石酸ソーダ1000ppmを添加したカセイソーダ溶液を用
意し、これに炭酸ガスを吹き込みつつ重炭酸化を行った
後徐冷し、結晶を得た。得られた結晶は500μ×100μの
柱状結晶で酒石酸ソーダを添加しない場合に比べて著し
い成長を示した。
Example 3 A caustic soda solution containing 1000 ppm of sodium tartrate was prepared, and bicarbonate was blown into the caustic soda solution, followed by slow cooling to obtain crystals. The obtained crystals were columnar crystals of 500μ × 100μ and showed remarkable growth as compared with the case where sodium tartrate was not added.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】蒸発、冷却、反応による析出等の方法で水
溶液から重炭酸ソーダ結晶を析出させるにあたり、母液
中に少量の酒石酸ソーダまたはその誘導体を添加するこ
とを特徴とする重炭酸ソーダ結晶の成長法。
1. A method for growing sodium bicarbonate crystals, which comprises adding a small amount of sodium tartrate or a derivative thereof to a mother liquor when precipitating sodium bicarbonate crystals from an aqueous solution by a method such as evaporation, cooling and precipitation by reaction.
【請求項2】酒石酸ソーダまたはその誘導体が水溶液に
対し、1〜50000ppm添加される特許請求の範囲第1項の
重炭酸ソーダの結晶成長法。
2. The crystal growth method of sodium bicarbonate according to claim 1, wherein 1 to 50,000 ppm of sodium tartrate or its derivative is added to the aqueous solution.
JP9355985A 1985-05-02 1985-05-02 Crystal growth method of sodium bicarbonate Expired - Fee Related JPH0617221B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP9355985A JPH0617221B2 (en) 1985-05-02 1985-05-02 Crystal growth method of sodium bicarbonate

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP9355985A JPH0617221B2 (en) 1985-05-02 1985-05-02 Crystal growth method of sodium bicarbonate

Publications (2)

Publication Number Publication Date
JPS61256919A JPS61256919A (en) 1986-11-14
JPH0617221B2 true JPH0617221B2 (en) 1994-03-09

Family

ID=14085603

Family Applications (1)

Application Number Title Priority Date Filing Date
JP9355985A Expired - Fee Related JPH0617221B2 (en) 1985-05-02 1985-05-02 Crystal growth method of sodium bicarbonate

Country Status (1)

Country Link
JP (1) JPH0617221B2 (en)

Also Published As

Publication number Publication date
JPS61256919A (en) 1986-11-14

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