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Process for preparing nitric acid with a concentration in the range from 50 to 77.8 by weight
Process for preparing nitric acid with a concentration in the range from 50 to 77.8 by weight
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机译:制备浓度范围为50-77.8%(重量)的硝酸的方法
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摘要
A process for preparing nitric acid by: catalytically oxidizing ammonia, to obtain a gas mixture containing NO and O2; cooling and condensing the gas mixture, thereby further oxidizing NO with O2, to obtain a gas stream containing NO2/N2O4 and an aqueous solution containing nitric acid; and countercurrently absorbing the NO2/N2O4 from the gas stream in an absorber with process water (H2O), to obtain nitric acid and an NOx-containing absorber offgas, wherein the water content of the nitric acid is regulated to a concentration in the range from 50 to 77.8% by weight and the NOx content of the absorber offgas to a concentration in the range from 20 to 500 ppm, by continuously measuring the water content of the process air supplied to the catalytic gas phase oxidation and, as a function of this, adjusting the amount of process water (Q-H2O) fed to the absorber.
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机译:一种制备硝酸的方法,该方法是:将氨催化氧化,得到含有NO和O 2 Sub>的气体混合物;冷却并冷凝该气体混合物,从而进一步用O 2 Sub>氧化NO,以获得包含NO 2 Sub> / N 2 Sub> O 4 Sub>和含硝酸的水溶液;并在吸收塔中用工艺水(H 2 Sub> / N 2 Sub> O 4 Sub>)从气流中逆流吸收Sub> O),以获得硝酸和含NO x Sub>的吸收塔尾气,其中将硝酸的水含量调节至50-77.8%重量范围内的浓度,通过连续测量供应给催化气相氧化的工艺空气的水含量,并以此来确定吸收器废气中NO x Sub>的含量,使其浓度范围为20至500 ppm ,调整送入吸收塔的工艺水(QH 2 Sub> O)的量。
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