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
    • 7. 发明申请
    • POWDERS AND GRANULES AND PROCESS FOR MAKING SUCH POWDERS AND GRANULES
    • 粉末和颗粒以及制造这种粉末和颗粒的方法
    • WO2017220308A1
    • 2017-12-28
    • PCT/EP2017/063285
    • 2017-06-01
    • BASF SE
    • MUELLER, Michael KlemensSTAMM, ArminJAEKEL, FrankSUELING, Carsten
    • C11D3/33C07C227/00C07C229/16C11D11/00C11D11/02
    • Process for making a powder or granule containing at least one chelating agent selected from alkali metal salts of methyl glycine diacetic acid (MGDA) and glutamic acid diacetate (GLDA) and iminodisuccinic acid (IDS), said process comprising the steps of (a) introducing an aqueous solution or aqueous slurry of the respective chelating agent (A) into a spray-dryer or spray-granulator, and removing most of said water by spray-drying or spray granulation using a gas with an inlet temperature of 125 to 250°C, (b) withdrawing powder or granules, respectively, from the spray-dryer or spray-granulator, respectively, (c) separating off fines from said powder or granules, wherein said fines have a maximum particle diameter of 350 µm, (d) separating off lumps from said powder or granules, wherein said lumps have a particle diameter of 1,500 µm or more, (e) milling said lumps to a maximum particle diameter of 500 µm, (f) re-introducing said fines from step (c) and milled lumps from step (e) into the spray-dryer or spray-granulator, wherein the share of fines is in the range of from 0.5 to 20 % by weight of the total chelating agent (A) withdrawn in step (b) and the share of milled lumps is in the range of from 5 to 60% by weight of the total chelating agent (A) withdrawn in step (b).
    • 制备含有至少一种选自甲基甘氨酸二乙酸(MGDA)和谷氨酸二乙酸(GLDA)和亚氨基二琥珀酸(IDS)的碱金属盐的螯合剂的粉末或颗粒的方法,所述方法 包括以下步骤:(a)将各自螯合剂(A)的水溶液或含水浆料引入喷雾干燥器或喷雾造粒机中,并且通过喷雾干燥或使用气体喷雾造粒除去大部分所述水 (b)分别从喷雾干燥器或喷雾造粒机中分别取出粉末或颗粒,(c)分离所述粉末或颗粒中的细粒,其中所述细粒具有最大颗粒 (d)从所述粉末或颗粒中分离出块状物,其中所述块状物的粒径为1,500微米或更大,(e)将所述块状物研磨至最大粒径为500微米 ,(f)将来自步骤(c)的所述细粒再次引入, 并将来自步骤(e)的块状物研磨到喷雾干燥器或喷雾造粒机中,其中细粒的份额为在步骤(b)中提取的总螯合剂(A)的0.5-20重量% 研磨块的份额在步骤(b)中提取的总螯合剂(A)的5至60重量%的范围内。