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    • 14. 发明授权
    • Process for the preparation of crystalline sodium silicates having a
sheet structure
    • 制备具有片状结构的结晶硅酸钠的方法
    • US5211930A
    • 1993-05-18
    • US693782
    • 1991-04-26
    • Gunther SchimmelReinhard GradlMartin Schott
    • Gunther SchimmelReinhard GradlMartin Schott
    • C01B33/38
    • C01B33/38
    • For the preparation of crystalline sodium silicates having a sheet structure and an SiO.sub.2 /Na.sub.2 O molar ratio of 1.9:1 to 3.5:1 from waterglass solutions having a solids content of 20 to 65% by weight, the waterglass solutions are first treated in a spray-drying zone. This gives a pulverulent amorphous sodium silicate having a maximum ignition loss of 20% by weight, while the waste gas leaving the spray-drying zone is at a temperature of at least 140.degree. C. Thereafter, the spray-dried sodium silicate is heated in an ignition zone containing an agitated solid bed at temperatures of 500.degree. to 800.degree. C. for 1 to 60 minutes in the presence of at least 10% by weight of recycled material. This recycled material was obtained by mechanical comminution of crystalline sodium silicate discharged from the ignition zone.
    • 对于具有固体含量为20至65重量%的水玻璃溶液,具有片状结构和SiO 2 / Na 2 O摩尔比为1.9:1至3.5:1的结晶硅酸钠的制备,先将水玻璃溶液以喷雾 干燥区 这产生了具有20重量%的最大灼烧损失的粉状无定形硅酸钠,而离开喷雾干燥区的废气处于至少140℃的温度。此后,将喷雾干燥的硅酸钠加热 在至少10重量%的再循环材料的存在下,在500℃至800℃的温度下含有搅拌的固体床1分钟至60分钟的点火区域。 该回收材料通过从点火区域排出的结晶硅酸钠的机械粉碎获得。
    • 15. 发明授权
    • Process for the preparation of alkali metal phosphate solutions
    • 制备碱金属磷酸盐溶液的方法
    • US5124137A
    • 1992-06-23
    • US676862
    • 1991-03-28
    • Gunther SchimmelThomas StaffelReinhard Gradl
    • Gunther SchimmelThomas StaffelReinhard Gradl
    • C01B25/30
    • C01B25/308
    • Alkali metal phosphate solutions having a fluorine content of less than 20 ppm, based on P.sub.2 O.sub.5, are prepared by first digesting crude phosphate using sulfuric acid, and separating the calcium sulfate from the crude phosphoric acid. An alkali metal compound is then added to the crude phosphoric acid, and the precipitated solid is filtered off. The prepurified crude phosphoric acid is neutralized to a pH of at least 7, and the solid produced during this operation is separated off. The resultant alkali metal phosphate solutions having a P.sub.2 O.sub.5 content of from 10 to 30% by weight are adjusted to a pH of between 4.8 and 6.0 using phosphoric acid. The solutions are heated to from 60.degree. to 120.degree. C., and from 1 to 6% by weight, based on the weight of the solution, of an alkaline earth metal oxygen compound are added to the alkali metal phosphate solutions with stirring. Finally, the precipitated solid is filtered off from the alkali metal phosphate solutions after a residence time of from 0.5 to 4 hours.
    • 通过首先使用硫酸消化粗磷酸酯,并从粗磷酸中分离硫酸钙,制备基于P 2 O 5的氟含量小于20ppm的碱金属磷酸盐溶液。 然后向粗磷酸中加入碱金属化合物,滤出沉淀的固体。 将预纯化的粗磷酸中和至至少7的pH,并且在该操作期间产生的固体被分离出来。 使用磷酸将所得的具有10-30重量%的P2O5含量的碱金属磷酸盐溶液调节至4.8至6.0的pH。 在搅拌下将溶液加热至60〜120℃,以溶液重量为1〜6重量%的碱土金属氧化合物加入到碱金属磷酸盐溶液中。 最后,在0.5-4小时的停留时间后,将沉淀的固体从碱金属磷酸盐溶液中滤出。
    • 17. 发明授权
    • Process for making alkali metal phosphate solutions containing little
fluorine
    • 制造含少量氟的碱金属磷酸盐溶液的方法
    • US4640824A
    • 1987-02-03
    • US682053
    • 1984-12-14
    • Gunther SchimmelReinhard Gradl
    • Gunther SchimmelReinhard Gradl
    • C01B25/237C01B25/30C01B25/46C01B25/16
    • C01B25/46C01B25/308
    • The disclosure relates to a process for making alkali metal phosphate solutions containing little fluorine from pre-purified alkali metal phosphate solutions obtained from crude phosphoric acid by extracting the acid with an organic solvent being immiscible or only partially miscible with water, scrubbing the crude extract with water or an alkali metal solution, re-extracting the phosphoric acid from the scrubbed extract with the use of an aqueous alkali metal solution while establishing an alkali metal/P-molar ratio equal to or larger than 1:1, and separating the resulting organic phase from the pre-purified alkali metal phosphate solution obtained.To this end, the disclosure provides:(a) for the pre-purified alkali metal phosphate solution to be stirred at 60.degree.-120.degree. C. into a compound of an alkaline earth metal Me.sup.2+ with a solubility in water at 20.degree. C. of more than 0.01 mol Me.sup.2+ /1, alkaline earth metal compounds with a solubility in water of less than 5 g/l being used in the form of particles of which more than 50% have a size of less than 8 .mu.m, for the whole to be reacted over a period of 0.5 to 4 hours, and for the resulting precipitate to be separated from the alkali metal phosphate solution so purified, and(b) for the alkaline earth metal compound necessary for effecting the defluorination to be suspended or dissolved in the alkali metal phosphate solution needed for effecting the re-extraction, and for the reaction between the alkali metal phosphate solution and alkaline earth metal compound to be effected in the mixing zone of the re-extraction unit.
    • 本公开涉及通过用与水不混溶或仅与水部分混溶的有机溶剂萃取酸来从粗磷酸获得的预纯化碱金属磷酸盐溶液中制备含少量氟的碱金属磷酸盐溶液的方法,用 水或碱金属溶液,使用碱金属水溶液从洗涤的提取物中再次提取磷酸,同时确定等于或大于1:1的碱金属/ P摩尔比,并分离所得的有机物 从预纯化的碱金属磷酸盐溶液获得。 为此,本公开内容提供:(a)将预纯化的在60-120℃下搅拌的碱金属磷酸盐溶液转变成在20℃在水中溶解度的碱土金属Me2 +的化合物。 大于0.01mol Me2 + / 1,在水中的溶解度小于5g / l的碱土金属化合物以超过50%的尺寸小于8μm的颗粒的形式使用,对于 整个反应0.5至4小时,并将所得沉淀物从纯化的碱金属磷酸盐溶液中分离出来,(b)对于实现脱氟所必需的碱土金属化合物悬浮或溶解 在进行再提取所需的碱金属磷酸盐溶液中,以及在再提取单元的混合区域中进行的碱金属磷酸盐溶液和碱土金属化合物之间的反应。
    • 18. 发明授权
    • Multistage column for countercurrent extraction of liquids
    • 用于逆流提取液体的多级柱
    • US4444729A
    • 1984-04-24
    • US393695
    • 1982-06-30
    • Reinhard GradlGunther Schimmel
    • Reinhard GradlGunther Schimmel
    • B01D11/04A01D17/00
    • B01D11/043
    • The disclosure relates to a multistage column for countercurrent extraction of two liquids of different specific density therein. The column is comprised of a housing in upright position provided at its upper end with an upper inlet and upper outlet and, at its lower end, with a lower inlet and lower outlet, the upper inlet and lower outlet permitting specifically denser liquid to be introduced into the column and to be taken therefrom, and the lower inlet and upper outlet permitting specifically less dense liquid to be introduced into the column and to be taken therefrom. Arranged centrally within the housing so as to extend vertically downward therein is a shaft and a plurality of stirring means which are spaced apart from each other are secured to the shaft, perpendicularly with respect thereto. A plurality of annular stator collars are mounted within the region of the inside wall of the housing, the individual stator collars being arranged downstream of, and spaced apart from, each other. Each stirring means has at least one disk with a diameter sufficient to cover the inner free area of the respective stator collar, secured thereto, at at least one place thereof. The stirring means and/or the stator collars are vertically movable against each other at a separation L. Encircling packings permitting the disks and stator collars to be sealed are provided at at least on position between disks and stator collars.
    • 本公开涉及一种用于逆流提取两种不同比重密度的液体的多级柱。 该柱由直立位置的壳体组成,其上端具有上部入口和上部出口,并且在其下端具有下部入口和下部出口,上部入口和下部出口允许引入更密集的液体 进入该塔并从其中取出,并且下部入口和上部出口允许将较不致密的液体引入该塔并从其中取出。 在壳体中央布置成在其中垂直向下延伸的是轴和彼此间隔开的多个搅拌装置,其相对于其垂直地固定到轴上。 多个环形定子环安装在壳体的内壁的区域内,各个定子套环布置在彼此的下游并且彼此间隔开。 每个搅拌装置具有至少一个盘,其直径足以覆盖固定在其上的相应定子环的内部自由区域,其至少一个位置处。 搅拌装置和/或定子套环在分离L处可彼此上下移动。允许盘和定子套环密封的环形填料至少在盘和定子套环之间的位置处提供。