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    • 1. 发明授权
    • Process for the preparation of dicalcium phosphate
    • 磷酸二钙的制备方法
    • US5024825A
    • 1991-06-18
    • US521737
    • 1990-05-10
    • Horst BuhlJosef HolzFranz-Josef Dany
    • Horst BuhlJosef HolzFranz-Josef Dany
    • C01B25/32
    • C01B25/322
    • For the preparation of dicalcium phosphate dihydrate stabilized with dimagnesium phosphate trihydrate and sodium pyrophosphate, an aqueous suspension of calcium carbonate is introduced into a reactor and recirculated by pumping through a high-speed mixer at 3,500 to 8,000 rpm which is in flow connection with the lower and upper portion of the reactor. Into the mixer an amount of phosphoric acid is introduced which is at least sufficient for the quantitative formation of dicalcium phosphate dihydrate and then an oxygen-containing magnesium compound is introduced into the reactor. Finally, lime milk is metered into the reactor up to a maximum pH of 6.9, before the sodium pyrophosphate is added to the reactor. The resulting suspension which has a stabilized dicalcium phosphate dihydrate content of 20 to 33% by weight is spray-dried.An apparatus for carrying out the process comprises besides a stirred reactor 1 two stirrer-equipped slurry containers (6, 7) and an intermediate container 16 from which a line 17 leads into a spray tower 18 where it ends above an atomizer wheel 19. The spray tower 18 is also the end point for hot air lines 20 and is in flow connection with a filter 22. The bottom of filter 22 is the starting point for a product line 24 via which highly adsorbent dicalcium phosphate dihydrate can be withdrawn.
    • 为了制备用磷酸三氢镁和焦磷酸钠稳定的磷酸二钙二水合物,将碳酸钙的水性悬浮液引入反应器中,并通过泵送通过高速混合器以3,500至8,000rpm再循环,该高速混合器与下部流动相连 和反应器的上部。 向混合器中加入一定量的磷酸,其至少足以定量形成磷酸二钙二水合物,然后将含氧的镁化合物引入反应器中。 最后,在将焦磷酸钠加入到反应器中之前,将石灰乳计量加入反应器直至最高pH为6.9。 所得到的具有稳定的磷酸二钙二水合物含量为20至33重量%的悬浮液被喷雾干燥。 用于进行该方法的装置除了具有搅拌反应器1的两个装有搅拌器的浆料容器(6,7)和中间容器16之外,其中管线17从该搅拌反应器引入喷雾塔18,在该喷雾塔18中它结束在雾化器轮19的上方。 喷雾塔18也是热空气管线20的终点,并且与过滤器22流动连接。过滤器22的底部是产物线24的起始点,通过该产物线24可以抽出高吸附性磷酸二钙二水合物。
    • 2. 发明授权
    • Process for the preparation of phosphorous acid
    • 制备磷酸的方法
    • US5147625A
    • 1992-09-15
    • US739873
    • 1991-08-02
    • Alexander TapperHorst BuhlJosef Holz
    • Alexander TapperHorst BuhlJosef Holz
    • C01B7/03C01B25/163
    • C01B7/035C01B25/163
    • In a continuous process for the preparation of phosphorous acid with simultaneous production of hydrochloric acid, a reaction zone is provided which is in open communication with a first scrubbing zone. A portion of the reaction product is recycled from the bottom of the reaction zone into the top of the scrubbing zone and phosphorous acid is removed from the circulation. Hydrogen chloride gas escaping from the top of the first scrubbing zone is brought into contact, in a cooled, second scrubbing zone, with an overstoichiometric amount of water. Hydrochloric acid is obtained which is passed as starting material into the reaction zone or into the top of the first scrubbing zone. The external cooling of the second scrubbing zone is controlled such that the temperature in the reaction zone is kept constant at a desired value between 90.degree. and 130.degree. C. without adding any external cooling or heating energy. Pure hydrochloric acid is recovered in an absorption zone.
    • 在以同时生产盐酸制备亚磷酸的连续方法中,提供了与第一洗涤区开放连通的反应区。 反应产物的一部分从反应区的底部再循环到洗涤区的顶部,并且从循环中除去亚磷酸。 从第一洗涤区的顶部排出的氯化氢气体在冷却的第二洗涤区中与化学计量的水接触。 得到的盐酸作为原料进入反应区或进入第一洗涤区的顶部。 控制第二洗涤区的外部冷却,使得反应区中的温度保持恒定在90℃至130℃之间的期望值,而不增加任何外部冷却或加热能量。 在吸收区中回收纯盐酸。