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PROCESS FOR PRODUCING POLYPHOSPHATES OF ALKALI METALS
PROCESS FOR PRODUCING POLYPHOSPHATES OF ALKALI METALS
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机译:碱金属多磷酸盐的生产方法
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1414369 Alkali metal polyphosphates RHONE-PROGIL 30 July 1973 [31 July 1972 14 June 1973] 36145/73 Heading C1A A process for preparing alkali metal polyphosphates having a predetermined crystalline form comprises, in a first stage, joining a mixture of alkali metal orthophosphates into spherical granules in the presence of water, the granules obtained having a molar ratio of alkali metal oxide/P 2 O 5 of from 1 to 2, drying the spherical granules at a temperature less than 120‹ C. and, in a second stage, heating the granules to form polyphosphates. It is preferred to prepare the granules from a mixture of mono and disodium orthophosphates, having a molar ratio of Na 2 O/P 2 O 5 close to 5/3, using a 50% by wt. aqueous solution of these salts to give granules of an average grain size of 0À1-3À15 mm. which are dried at 100‹ C. in, for example, a fluidized bed. The second stage of the process in which polyphosphates are formed is carried out either by (a) heating the dried granules in a fluidized bed or (b) introducing the dried granules into a fluidized bed by means of a pneumatic conveyer at a high temperature, in the presence in both cases of water vapour. In the case of processes (a) the average residence time of the granules in the bed is 5-30 mins. At a temperature of 300-400‹ C. in the bed granules of phase II tripolyphosphates are attained, whilst at temperatures of at least 480‹ C. phase I tripolyphosphates are obtained. The use of intermediate temperatures allows the formation of both phases in a predetermined manner. In the case of process (b) the dried granules are introduced into a pneumatic conveyer at a high temperature, e.g. 550‹ C. to give a residence time of a few seconds in the conveyer and 1-10 mins. in the following fluidized bed. The ranges of temperature in which phase I and phase II are formed are less high than in process (a). The water vapour content of the bed gases is preferably 14-100% by weight.
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机译:1414369碱金属多磷酸盐RHONE-PROGIL 1973年7月30日[1972年7月31日,1973年6月14日]标题C1A制备具有预定晶体形式的碱金属多磷酸盐的方法包括,在第一步中,将碱金属正磷酸盐的混合物加入球形颗粒在水的存在下,所获得的颗粒的碱金属氧化物/ P 2 O 5的摩尔比为1至2,在小于120°C的温度下干燥球形颗粒,并在第二步中,加热颗粒以形成多磷酸盐。优选由Na 2 O / P 2 O 5的摩尔比接近5/3的正磷酸单磷酸钠和磷酸二氢钠的混合物制备颗粒,使用50重量%的Na 2 O / P 2 O 5。将这些盐的水溶液制成平均粒径为0到1-3 15毫米的颗粒。将其在例如100℃的流化床中干燥。形成多磷酸盐的方法的第二阶段是通过以下方式进行的:(a)在流化床中加热干燥的颗粒,或(b)借助于气动输送机在高温下将干燥的颗粒引入流化床中,在两种情况下都存在水蒸气。在方法(a)的情况下,颗粒在床中的平均停留时间为5-30分钟。在300-400℃的温度下,获得了II相三聚磷酸盐的颗粒,而在至少480℃的温度下,获得了I相的三聚磷酸盐。使用中间温度允许以预定方式形成两相。在方法(b)的情况下,将干燥的颗粒在高温下例如在20℃下引入气动输送机中。 550 ‹C.给出在传送带中停留几秒和1-10分钟的时间。在以下流化床中。形成相I和相II的温度范围比方法(a)中的温度范围低。床气体的水蒸气含量优选为14-100重量%。
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