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A process for producing a as a delustering agent in paints suitable silica filler

机译:一种在涂料中合适的二氧化硅填料中用作消光剂的方法

摘要

1,229,125. Spray drying silica. FARBENFABRIKEN BAYER A.G. 16 May, 1969 [2 July, 1968], No. 24984/69. Heading C1A A silica filler is obtained by spray drying an aqueous suspension of precipitated silica with a specific surface of from 50-200 m.SP2/SP/g. (according to BET) and a salt content of less than 1 % by weight, based on SiO 2 , the solids concentration being less than 12% by weight and the outlet temperature of the heating gases being between 250‹ and 700‹ C. The preferred conditions are a turbulent gas stream so that at least 100 kg. of water are evaporated per m.SP3/SP of drier volume per hour; a residence time of 1 second or less and an outlet temperature of 450-700‹ C. The silica suspension may be obtained by removing metal cations by hydrogen ion exchange from a suspension of filter cake after washing the latter. In an example sulphuric acid is added to a waterglass solution over a period of 3 hrs. at 70‹ C., the mixture boiled for 1 hr., adjusted to pH 7 and finally filtered. The filter cake was washed, suspended in salt free water and delivered to the spray drier.
机译:1,229,125。喷雾干燥二氧化硅。 FARBENFABRIKEN BAYER A.G.,1969年5月16日[1968年7月2日],第24984/69号。标题C1A通过喷雾干燥比表面积为50-200 m。 2 / g的沉淀二氧化硅水悬浮液来获得二氧化硅填料。 (根据BET),盐含量小于SiO 2的1重量%,固体浓度小于12重量%,加热气体的出口温度在250℃至700℃之间。优选的条件是湍流,以使至少100kg。每干燥器每小时 3 蒸发量的水;停留时间为1秒或更短,出口温度为450-700℃。二氧化硅悬浮液可通过在洗涤滤饼后通过氢离子交换从滤饼悬浮液中除去金属阳离子而获得。在一个实例中,在3小时内将硫酸添加到水玻璃溶液中。在70℃下,将混合物煮沸1小时,调节至pH 7,最后过滤。洗涤滤饼,将其悬浮在无盐水中并输送至喷雾干燥器。

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