JP2005041743A5 - - Google Patents

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JP2005041743A5
JP2005041743A5 JP2003278643A JP2003278643A JP2005041743A5 JP 2005041743 A5 JP2005041743 A5 JP 2005041743A5 JP 2003278643 A JP2003278643 A JP 2003278643A JP 2003278643 A JP2003278643 A JP 2003278643A JP 2005041743 A5 JP2005041743 A5 JP 2005041743A5
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alkali metal
slurry
crystallizer
producing
taken out
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JP2003278643A
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JP4539047B2 (en
JP2005041743A (en
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Claims (13)

所定の反応器内でアルカリ金属イオンを含む水溶液と二酸化炭素とを反応させてアルカリ金属炭酸水素塩の結晶を晶析させる方法において、前記水溶液の前記結晶を含むスラリーの一部を前記晶析装置から取り出し、前記結晶の一部を溶解させた後で前記晶析装置に戻すことを特徴とするアルカリ金属炭酸水素塩の製造方法。   In the method of reacting an aqueous solution containing alkali metal ions and carbon dioxide in a predetermined reactor to crystallize alkali metal hydrogencarbonate crystals, a part of the slurry containing the crystals of the aqueous solution is crystallized in the crystallizer A method for producing an alkali metal hydrogen carbonate, wherein a part of the crystal is dissolved and then returned to the crystallizer. 前記晶析装置から取り出された前記スラリーの圧力を前記晶析装置の圧力よりも低くすることにより、該スラリー中に含まれる前記結晶の一部を溶解させることを特徴とする、請求項1に記載のアルカリ金属炭酸水素塩の製造方法。   The part of the crystals contained in the slurry is dissolved by making the pressure of the slurry taken out from the crystallizer lower than the pressure of the crystallizer. The manufacturing method of alkali metal hydrogencarbonate of description. 前記晶析装置から取り出された前記スラリーに、該スラリーの流量に対して標準状態0.2〜20倍の体積の空気を吹き込むことにより、該スラリー中に含まれる前記結晶の一部を溶解させることを特徴とする、請求項1または2に記載のアルカリ金属炭酸水素塩の製造方法。   A part of the crystals contained in the slurry is dissolved by blowing air having a volume of 0.2 to 20 times the standard state with respect to the flow rate of the slurry into the slurry taken out from the crystallizer. The method for producing an alkali metal hydrogen carbonate according to claim 1 or 2, wherein 前記晶析装置から取り出された前記スラリーに、アルカリ金属の炭酸塩および/または水酸化物を含む水溶液を添加することにより、該スラリー中に含まれる前記結晶の一部を溶解させることを特徴とする、請求項1〜3のうちいずれか一項に記載のアルカリ金属炭酸水素塩の製造方法。   A part of the crystals contained in the slurry is dissolved by adding an aqueous solution containing an alkali metal carbonate and / or hydroxide to the slurry taken out from the crystallizer. The manufacturing method of the alkali metal hydrogencarbonate as described in any one of Claims 1-3. 前記晶析装置から取り出された前記スラリーに、水を添加することにより、該スラリー中に含まれる前記結晶の一部を溶解させることを特徴とする、請求項1〜4のうちいずれか一項に記載のアルカリ金属炭酸水素塩の製造方法。   5. A part of the crystals contained in the slurry is dissolved by adding water to the slurry taken out from the crystallizer. The manufacturing method of the alkali metal hydrogencarbonate described in 2. 前記晶析装置から取り出された前記スラリーを加熱することにより、該スラリー中に含まれる前記結晶の一部を溶解させることを特徴とする、請求項1〜5のうちいずれか一項に記載のアルカリ金属炭酸水素塩の製造方法。   The part of the crystals contained in the slurry is dissolved by heating the slurry taken out from the crystallizer, The method according to any one of claims 1 to 5, A method for producing an alkali metal bicarbonate. 前記晶析装置から取り出される前記スラリーの量が、前記晶析装置中のスラリー全量を基準として1時間当たり30〜200質量%であることを特徴とする、請求項1〜6のうちいずれか一項に記載のアルカリ金属炭酸水素塩の製造方法。   The amount of the slurry taken out from the crystallizer is 30 to 200% by mass per hour based on the total amount of slurry in the crystallizer. The manufacturing method of the alkali metal hydrogencarbonate of item. 前記水溶液がアルカリ金属の炭酸塩および/または水酸化物を含有することを特徴とする、請求項1〜7のうちいずれか一項に記載のアルカリ金属炭酸水素塩の製造方法。   The method for producing an alkali metal hydrogencarbonate according to any one of claims 1 to 7, wherein the aqueous solution contains an alkali metal carbonate and / or a hydroxide. 前記アルカリ金属がナトリウムまたはカリウムであることを特徴とする、請求項1〜8のうちいずれか一項に記載のアルカリ金属炭酸水素塩の製造方法。   The method for producing an alkali metal hydrogencarbonate according to any one of claims 1 to 8, wherein the alkali metal is sodium or potassium. 前記晶析装置から取り出された前記スラリー中に含まれる結晶の全部または一部を粉砕することを特徴とする、請求項1〜9のうちいずれか一項に記載のアルカリ金属炭酸水素塩の製造方法。   The production of an alkali metal hydrogen carbonate according to any one of claims 1 to 9, wherein all or part of crystals contained in the slurry taken out from the crystallizer is pulverized. Method. 前記晶析装置から取り出された前記スラリーの母液の組成が、アルカリ金属炭酸水素塩が飽和未満の濃度であることを特徴とする、請求項10記載のアルカリ金属炭酸水素塩の製造方法。   The method for producing an alkali metal hydrogen carbonate according to claim 10, wherein the composition of the mother liquor of the slurry taken out from the crystallizer has a concentration of the alkali metal hydrogen carbonate below saturation. 前記反応器内の温度が50〜90℃であることを特徴とする、請求項1〜11のうちいずれか一項に記載のアルカリ金属炭酸水素塩の製造方法。   The method for producing an alkali metal hydrogen carbonate according to any one of claims 1 to 11, wherein the temperature in the reactor is 50 to 90 ° C. 前記晶析装置から前記スラリーの一部を取り出すにあたって、前記晶析装置内のより大きな結晶を抜き出して溶解させることを特徴とする、請求項1〜12のうちのいずれか一項に記載のアルカリ金属炭酸塩の製造方法。The alkali according to any one of claims 1 to 12, wherein, when taking out a part of the slurry from the crystallizer, larger crystals in the crystallizer are extracted and dissolved. A method for producing a metal carbonate.

JP2003278643A 2003-07-23 2003-07-23 Method for producing alkali metal hydrogen carbonate Expired - Fee Related JP4539047B2 (en)

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JP2005041743A JP2005041743A (en) 2005-02-17
JP2005041743A5 true JP2005041743A5 (en) 2006-06-01
JP4539047B2 JP4539047B2 (en) 2010-09-08

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Publication number Priority date Publication date Assignee Title
FR2918575B1 (en) * 2007-07-09 2009-08-28 Crystal Evap Consult Sarl FORCED CIRCULATION CRYSTALLIZATION APPARATUS.
JP6442014B1 (en) * 2017-09-13 2018-12-19 株式会社流機エンジニアリング Processing apparatus and processing method for liquid to be processed
KR102002479B1 (en) * 2018-11-20 2019-07-23 탑에코에너지주식회사 Manufacturing system of High-purity NaHCO3
CN110282638B (en) * 2019-07-30 2024-05-17 武汉德泽环保科技有限公司 Method and device for preparing baking soda by double decomposition

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JPS5560021A (en) * 1978-10-27 1980-05-06 Toyo Soda Mfg Co Ltd Production of sodium bicarbonate
JPS62247802A (en) * 1986-03-18 1987-10-28 Daicel Chem Ind Ltd Crystallization method
SE8700213L (en) * 1987-01-21 1988-07-22 Nobel Kemi Ab SET TO MAKE CRYSTALLINE SUBSTANCES
JP2890881B2 (en) * 1990-06-27 1999-05-17 味の素株式会社 Crystallization of amino acids or nucleic acids
JPH05184805A (en) * 1992-01-16 1993-07-27 Shin Nippon Kagaku Kogyo Co Ltd Circulative crystallization method
US5445805A (en) * 1993-05-06 1995-08-29 Church & Dwight Co., Inc. Large potassium bicarbonate crystals and process for the preparation thereof

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