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A method of concentrating dilute sulfuric acid in a three-stage forced-circulation vacuum evaporation plant plant using forced circulation.

机译:一种使用强制循环在三级强制循环真空蒸发设备中浓缩稀硫酸的方法。

摘要

The process of concentrating a dilute sulfuric acid in a three-stage vacuum evaporation plant includes feeding an entry dilute sulfuric acid to a first evaporation stage of a vacuum evaporation plant to form an overhead vapor (6), withdrawing a finally concentrated sulfuric acid from the third evaporation stage (3), using steam or the overhead vapor (6) of the first evaporation stage as a heating fluid in the three-stage vacuum evaporation plant, maintaining the entry dilute sulfuric acid under a pressure of 0.4 to 0.7 bar and at a temperature of 80 DEG to 120 DEG C. in the first evaporation stage (1), maintaining the partially concentrated sulfuric acid under a pressure of 0.02 to 0.06 bar and at a temperature of 50 DEG to 90 DEG C. in the second evaporation stage (2), maintaining the further concentrated sulfuric acid under a pressure of 0.02 to 0.06 bar and at a temperature of 80 DEG to 120 DEG C. in the third evaporation stage (3), and condensing overhead vapors (8,8a) formed in the second and third evaporation stages. Each evaporation stage (1,2,3) includes an evaporation vessel (1b,2b,3b) and a connected recycle line including a shell-tube heat exchanger (1a,2a,3a) and pump. The process also includes continuously feeding about 30 to 95% of the entry dilute sulfuric acid (4) to the first evaporation vessel in the first evaporation stage (1) and continuously feeding the balance of the entry dilute sulfuric acid to the second evaporation vessel in the second evaporation stage (2).
机译:在三级真空蒸发设备中浓缩稀硫酸的过程包括:将进入的稀硫酸进料到真空蒸发设备的第一蒸发步骤中以形成塔顶蒸气(6),然后从蒸馏塔中抽出最终浓缩的硫酸。第三蒸发阶段(3),使用第一蒸发阶段的蒸汽或塔顶蒸气(6)作为三阶段真空蒸发设备中的加热流体,将进入的稀硫酸保持在0.4至0.7 bar的压力下并保持在在第一蒸发阶段(1)中的温度为80-120℃,在第二蒸发阶段中将部分浓缩的硫酸保持在0.02-0.06bar的压力下和50-90℃的温度下。 (2),在第三蒸发阶段(3)中,将进一步的浓硫酸保持在0.02至0.06巴的压力和80至120℃的温度下,并冷凝形成的塔顶蒸气(8,8a)。在第二和第三蒸发阶段。每个蒸发阶段(1,2,3)都包括一个蒸发容器(1b,2b,3b)和一个连接的循环管线,该循环管线包括壳管式热交换器(1a,2a,3a)和泵。该方法还包括在第一蒸发阶段(1)中将进料稀硫酸(4)的约30%至95%连续进料到第一蒸发容器中,并在第二蒸发器中连续进料剩余的进料稀硫酸到第二蒸发容器中。第二蒸发阶段(2)。

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