会员体验
专利管家(专利管理)
工作空间(专利管理)
风险监控(情报监控)
数据分析(专利分析)
侵权分析(诉讼无效)
联系我们
交流群
官方交流:
QQ群: 891211   
微信请扫码    >>>
现在联系顾问~
热词
    • 1. 发明授权
    • Process for producing sodium percarbonate
    • 生产过碳酸钠的方法
    • US06231828B1
    • 2001-05-15
    • US09142940
    • 1998-12-23
    • Alun P. JamesGraham R. HorneRichard RoeslerLido SignoriniRobert OwenSoraya ParvanehRomano PardiniStefano BiginiManfred MathesUwe DrostePier-Luigi Deli
    • Alun P. JamesGraham R. HorneRichard RoeslerLido SignoriniRobert OwenSoraya ParvanehRomano PardiniStefano BiginiManfred MathesUwe DrostePier-Luigi Deli
    • C01B1510
    • C11D3/3942C01B15/103C11D3/128
    • Sodium percarbonate is traditionally made in a crystallization process from aqueous hydrogen peroxide and sodium carbonate with recycle of mother liquor in the presence of a substantial concentration of a salting-out agent, conventionally sodium chloride. The invention provides a process intended to be conducted without addition of chloride salting-out agent in which the dissolution step (1) is controlled to restrict the sodium carbonate concentration to below 95%; preferably 60 to 90% of its saturated concentration at a temperature preferably controlled to at most 35° C. and the mole ratio of hydrogen peroxide: sodium carbonate in the reaction vessel is controlled to between 0.7 to 1.2:1, and preferably about 1:1. In some embodiments at least a fraction of the mother liquor introduced into the dissolution tank (1) is obtained by extraction from the reaction vessel (6) and in other embodiments a fraction of the sodium percarbonate (2) is introduced in solution in the mother liquor (4) and a fraction is introduced in particulate form (8) directly into the reaction vessel (6). Large particle sodium percarbonate is provided which has a 7 day aged heat emission at 40° C. of not more than 3 &mgr;W/g measured in a microcalorimeter over 16 hours that is lower than the heat emission from conventionally produced sodium percarbonate employing a chloride salting-out agent.
    • 传统上,过碳酸钠通过过氧化氢和碳酸钠水溶液的结晶过程在母液中,在大量浓度的盐析剂,常规氯化钠存在下进行。 本发明提供了一种在不加入氯化物盐析剂的情况下进行的方法,其中控制溶解步骤(1)以将碳酸钠浓度限制在95%以下; 优选其饱和浓度的60至90%,优选控制在至多35℃,反应容器中过氧化氢:碳酸钠的摩尔比控制在0.7至1.2:1之间,优选约1: 1。 在一些实施方案中,通过从反应容器(6)中提取,获得引入溶解槽(1)的至少一部分母液,在其它实施方案中,将过量碳酸钠(2)的一部分引入母体溶液中 液体(4)和一部分颗粒形式(8)直接引入反应容器(6)。 提供大颗粒过碳酸钠,其在40℃下具有7天以上的热释放度,其在微量热计中在16小时内测量的不超过3μW/ g,低于常规制备的过碳酸钠使用氯化物盐析 -out代理。
    • 2. 发明授权
    • Sodium percarbonate and process for producing sodium percarbonate
    • 过碳酸钠和生产过碳酸钠的方法
    • US06482385B2
    • 2002-11-19
    • US09794122
    • 2001-02-28
    • Alun P. JamesGraham R. HorneRichard RoeslerLido SignoriniRobert OwenSoraya ParvanehRomano PardiniStefano BiginiManfred MathesUwe DrostePier-Luigi Deli
    • Alun P. JamesGraham R. HorneRichard RoeslerLido SignoriniRobert OwenSoraya ParvanehRomano PardiniStefano BiginiManfred MathesUwe DrostePier-Luigi Deli
    • C01B1510
    • C11D3/3942C01B15/103C11D3/128
    • Sodium percarbonate is traditionally made in a crystallization process from aqueous hydrogen peroxide and sodium carbonate with recycle of mother liquor in the presence of a substantial concentration of a salting out agent, conventionally sodium chloride. The invention provides a process intended to be conducted without addition of chloride salting-out agent in which the dissolution step is controlled to restrict the sodium carbonate concentration to below 95%, preferably 60 to 90% of its saturated concentration at a temperature preferably controlled to at most 35C. and the mole ratio of hydrogen peroxide:sodium carbonate in the reaction vessel is controlled to between 0.7 to 1.2:1, and preferably about 1:1. In some embodiments at least a fraction of the mother liquor introduced into the dissolution tank is obtained by extraction from the reaction vessel and in other embodiments a fraction of the sodium percarbonate is introduced in solution in the mother liquor and a fraction is introduced in particulate form directly into the reaction vessel. Large particle sodium percarbonate is provided which has a 7 day aged heat emission at 40C. of not more than 3 &mgr;W/g measured in a microcalorimeter over 16 hours that is lower than the heat emission from conventionally produced sodium percarbonate employing a chloride salting-out agent.
    • 传统上,过碳酸钠通过过氧化氢水溶液和碳酸钠的结晶过程进行,在过量的盐析剂(常规氯化钠)存在下,再循环母液。 本发明提供一种在不加入氯化物盐析剂的情况下进行的方法,其中控制溶解步骤以将碳酸钠浓度限制在其饱和浓度的95%以下,优选60%至90%,优选控制在 最多35℃。 并且将反应容器中过氧化氢:碳酸钠的摩尔比控制在0.7至1.2:1之间,优选约1:1。 在一些实施方案中,通过从反应容器中萃取而获得引入溶解槽的至少一部分母液,在其它实施方案中,将过碳酸钠的一部分引入母液中的溶液中,并将一部分以颗粒形式 直接进入反应容器。 提供了大颗粒过碳酸钠,其在40℃下具有7天的发热。 在微量热计中在16小时内测量的,不超过3微瓦/克,低于使用氯化物盐析剂的常规生产的过碳酸钠的散热。