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Process for the purification and treatment of nitrous exhaust gases containing at least one additional acid compound

机译:包含至少一种其他酸化合物的含氮废气的净化和处理方法

摘要

The invention relates to a process for purifying and working up nitrous exhaust gases which contain at least one additional acidic compound, such as hydrofluoric acid, sulfur oxides, hydrochloric or phosphoric acid, individually or in combination. Starting from the disadvantages of the known prior art, a method is to be provided with which an exhaust gas of high purity and a mixed acid which can be used again for pickling or etching are obtained. The following procedure is proposed for this: The exhaust gas is gradually, in at least three washing stages with washing columns K1, K2, K3 connected in series with a packed bed FS with a surface area of 180 to 980 m2 / m3, a space load of 30 to 180 m3 / m3h each Washing column in countercurrent brought into contact with fresh water as a washing solution with a temperature of 5 to 30 ° C, with the addition of an oxidizing agent. In the first washing stage K1, at least 60% of the NOx components contained in the exhaust gas and 90% of the further acid components contained in the exhaust gas are washed out. The washing cycle is continued until a concentration ratio of mixed or thin acid in the sequence K1: K2: K3 of 500: 50: 5 to 500: 10: 0.2 is established in the column bottoms KS of the washing columns K1, K2, K3 , Immediately thereafter, mixed acid is removed from the first column K1, and then, in each case, thin acid from the second column K2 is metered into the first column K1 and from the third column K3 into the second column K2, and fresh water is fed to the third column K3 as compensation. The space load of the individual wash columns K1, K2, K3 among one another is set so that the ratio of the space load of the first wash column K1 to that of the subsequent wash columns K2, K3 is from 1: 1.5 to 1:10.
机译:本发明涉及一种单独地或组合地净化和处理含至少一种另外的酸性化合物的亚硝酸废气的方法,该酸性化合物例如氢氟酸,硫氧化物,盐酸或磷酸。从已知的现有技术的缺点出发,将提供一种方法,利用该方法可获得可再次用于酸洗或蚀刻的高纯度废气和混合酸。为此,建议采取以下程序:在至少三个洗涤阶段中,将废气逐步洗净,将洗净塔K1,K2,K3与填充床FS串联,其表面积为180至980 m2 / m3,空间每个洗涤塔以30到180 m3 / m3h的负荷逆流与温度为5到30℃的新鲜水作为洗涤溶液接触,并加入氧化剂。在第一洗涤阶段K1中,洗涤掉废气中至少60%的NOx成分和废气中90%的其他酸成分。继续洗涤循环,直到在洗涤塔K1,K2,K3的塔底KS中建立了混合酸或稀酸的浓度比为500:50:5至500:10:0.2的K1:K2:K3之后,立即从第一塔K1中除去混合酸,然后分别将来自第二塔K2的稀酸计量加入第一塔K1并将从第三塔K3的稀酸计量加入第二塔K2和淡水被馈送到第三列K3作为补偿。各个洗涤塔K1,K2,K3彼此之间的空间负载被设置成使得第一洗涤塔K1与随后的洗涤塔K2,K3的空间负载的比为1:1.5至1:1。 10。

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