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From the silicon treatment foul solution you recover and reuses nitric acid the manner

机译:从硅处理污垢溶液中,您可以回收并重复使用硝酸

摘要

PURPOSE: To improve recovering efficiency by removing silicon dioxide deposited on a cooling condensing part by dissolving with fluoric acid and recovering nitric acid by distillation when recovering nitric acid from a washing waste liquid or the like of poly crystalline silicon or the like. ;CONSTITUTION: A waste water bottle 11 in a oil bath 10 is connected to a cooling part 13 and a collecting vessel 14 with a branching pipe 12 and is connected to a fluoric acid supply pipe 15. And the waste water is heated to equal or above b.p. of a fluoric acid water and a nitric acid water, usually 100-125°C, and is distilled. Water-fluoric acid group is distilled on a low b.p. side. In the process, hydrosilicofluoric acid is decomposed and silicon fluoride is distilled with fluoric acid and reacts with water to deposit silicon dioxide in the cooling part 13. And distilled fluoric acid flows down to the cooling part 13 through the supply pipe 15 to dissolve and remove silicon dioxide. Supply of fluoric acid is stopped when deposition is out. And when the distillation on the side of low b.p. group is completed, the distillation is transferred to the side of high b.p. group for distilling nitric acid to recover nitric acid.;COPYRIGHT: (C)1993,JPO&Japio
机译:目的:当从多晶硅等的洗涤废液等中回收硝酸时,通过溶解于氟中并除去氟沉积在冷却冷凝部分上的二氧化硅并通过蒸馏回收硝酸来提高回收效率。 ;组成:油浴10中的废水瓶11通过分支管12与冷却部件13和收集容器14连接,并与氟酸供给管15连接。废水被加热到等于或等于高于bp通常在100-125°C的温度范围内蒸馏水,然后蒸馏。水氟酸基团在低沸点下蒸馏。侧。在该过程中,氢氟硅酸分解,氟硅酸与氟酸蒸馏并与水反应以在冷却部分13中沉积二氧化硅。并且蒸馏的氟酸通过供应管15向下流到冷却部分13以溶解和除去。二氧化硅。沉积结束后,停止供应氟酸。而当蒸馏在低b.p.组完成后,将蒸馏转移至高沸点侧。蒸馏硝酸回收硝酸组。版权所有:(C)1993,日本特许厅

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