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Procedure for operating a gypsum sulphuric acid plant

机译:石膏硫酸装置的运行程序

摘要

In this process, conversion of the gypsum serving as feedstock into anhydrite in a separate plant is omitted. Instead, the gypsum is first subjected only to partial dehydration down to a surface water content of 10-15% by weight. A two-step drying and calcining of the gypsum is then carried out in which the SO2-containing waste gas of the furnace is used as heat-transfer medium. At the same time, dust is removed from this waste gas to such an extent that it can be passed without any further gas treatment into the gas scrubber of the sulphuric acid plant. After passing the second drying step, the dried and calcined gypsum still has a total water content of about 6% by weight and is passed directly together with the addition materials via a conveying element into the heat-exchanger of the furnace, so that the furnace powder is mixed in the conveying element and/or heat-exchanger.
机译:在该方法中,省略了在单独的工厂中将用作原料的石膏转化为硬石膏。相反,首先仅将石膏部分脱水至表面水含量为10-15重量%。然后进行石膏的两步干燥和煅烧,其中将炉子中的含SO 2的废气用作传热介质。同时,从该废气中去除灰尘的程度应使它无需进一步的气体处理就可以通过而进入硫酸装置的气体洗涤器。在经过第二干燥步骤之后,干燥并煅烧的石膏的总水含量仍为约6重量%,并且与附加材料一起经由输送元件直接进入炉子的热交换器中,使得炉子粉末在输送元件和/或热交换器中混合。

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