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    • 2. 发明专利
    • Production method for hardly caking sodium hydrogencarbonate
    • 生产氢化钠的生产方法
    • JP2004203673A
    • 2004-07-22
    • JP2002374581
    • 2002-12-25
    • Asahi Glass Co Ltd旭硝子株式会社
    • KIKUCHI SHINTAROYOKOYAMA KOICHIHIRANO HACHIROSAKURAI SHIGERU
    • C01D7/42
    • PROBLEM TO BE SOLVED: To provide a method for producing hardly caking sodium hydrogencarbonate (sodium bicarbonate) suitable in the fields of food, medicine, and bath salts and requiring no addition of an anticaking agent.
      SOLUTION: (1) Wet sodium hydrogencarbonate particles are kept in contact, for 1-20 min, with a drying gas containing at least 5 vol% carbon dioxide gas, having a water content corresponding to a dew point of 50°C or lower, and being kept at 50-400°C. Otherwise, (2) wet sodium hydrogencarbonate particles are kept in contact, for 1-120 min, with a first drying gas containing at least 5 vol% carbon dioxide gas, having a water content corresponding to a dew point of 55°C or lower, and being kept at 50-400°C and then are brought into contact, for 1-120 min, with a second drying gas containing at least 3 vol% carbon dioxide gas, having a water content corresponding to a dew point not higher than that of the first drying, and being kept at 350°C or lower and at a temperature lower than that of the first drying gas.
      COPYRIGHT: (C)2004,JPO&NCIPI
    • 待解决的问题:提供一种适用于食品,药物和浴盐领域的不结块碳酸氢钠(碳酸氢钠)的方法,并且不需要添加抗结块剂。 <1>解决方案:(1)将湿碳酸氢钠颗粒与含有至少5体积%二氧化碳气体的干燥气体保持接触1-20分钟,其含水量相当于露点为50℃ 或更低,并保持在50-400℃。 否则,(2)湿碳酸氢钠颗粒与含有至少5体积%二氧化碳气体的第一干燥气体保持接触1-120分钟,其含水量相当于露点为55℃或更低 并保持在50-400℃,然后与含有至少3体积%二氧化碳气体的第二干燥气体接触1-120分钟,其含水量不高于 第一次干燥,并保持在350℃以下且温度低于第一干燥气体的温度。 版权所有(C)2004,JPO&NCIPI
    • 3. 发明专利
    • Method for producing sodium hydrogencarbonate crystal particle having low caking property
    • 用于生产具有低开关性能的氢氧化钠晶体颗粒的方法
    • JP2010159208A
    • 2010-07-22
    • JP2010049663
    • 2010-03-05
    • Asahi Glass Co Ltd旭硝子株式会社
    • HIRANO HACHIROYOKOYAMA KOICHIYAMAMOTO KIYOSHINARIZUKA TEIJI
    • C01D7/42C01D7/00
    • C01D7/42
    • PROBLEM TO BE SOLVED: To provide a method for producing and packaging sodium hydrogencarbonate (baking soda) crystal particles having a low caking property, which do not need the addition of a caking inhibitor thereto and are suitable for use in the fields of food, pharmaceuticals and bath agents.
      SOLUTION: Sodium hydrogencarbonate crystal particles having a mean particle diameter of 50-500 μm are produced by deposition from mother liquor of an aqueous solution containing sodium hydrogencarbonate having potassium concentration of ≤400 mass ppm, and the sodium hydrogencarbonate crystal particles are dried using a dry gas having carbon dioxide concentration of ≥3 vol.% to produce sodium hydrogencarbonate crystal particles having potassium concentration of ≤50 mass ppm and carbonate ion concentration of ≤1 mass% in terms of sodium carbonate.
      COPYRIGHT: (C)2010,JPO&INPIT
    • 要解决的问题:提供一种生产和包装具有低结块性的碳酸氢钠(小苏打)晶体颗粒的方法,其不需要在其上添加结块抑制剂,并且适用于 食品,药品和浴剂。 解决方案:平均粒径为50-500μm的碳酸氢钠晶体颗粒是通过从含有钾浓度≤400质量ppm的碳酸氢钠的水溶液的母液中沉积而生成的,并且将碳酸氢钠晶体颗粒干燥 使用二氧化碳浓度≥3体积%的干燥气体,制成钾浓度≤50质量ppm的碳酸氢钠结晶粒子,碳酸钠的碳酸根离子浓度≤1质量%。 版权所有(C)2010,JPO&INPIT
    • 10. 发明专利
    • PRODUCTION OF SODIUM BICARBONATE
    • JPH01208315A
    • 1989-08-22
    • JP3194888
    • 1988-02-16
    • ASAHI GLASS CO LTD
    • NAKAYA KEIICHIYOKOYAMA KOICHI
    • C01D7/18
    • PURPOSE:To obtain sodium bicarbonate particles having large particle size in high efficiency, by returning a part of mother liquor left after the separation of sodium bicarbonate to a feeding liquid system in the production of NaHCO3 from ammoniacal saline water and a CO2-containing gas and recycling the mother liquor. CONSTITUTION:Ammoniacal saline water 1 is supplied to a preliminary carbonation column A and carbonated to a neutralized ammoniacal saline water 2 with a CO2- containing exhaust gas 9 discharged from a carbonation column C composed of a reaction zone having plural stages. A feeding liquid composed of said neutralized ammoniacal saline water 2 is mixed with a part of mother liquor 7 left after the separation of sodium bicarbonate to obtain a liquid mixture 3. The volume ratio of the mother liquor left after the separation of sodium bicarbonate to the feeding liquid is selected to 0.2-1.5. The liquid mixture is cooled to a prescribed temperature with a cooler B and the obtained feeding liquid 4 is supplied to the carbonation column C. The slurry 5 containing precipitated sodium bicarbonate is separated into sodium bicarbonate 6 and the separated mother liquor 7 with a separator D. As mentioned above, a part of the separated mother liquor 7 is mixed with neutralized ammoniacal saline water and the remaining part of the liquor is sent to a distillation stage.