Multi-component linkage extraction separation flow design system and design method
A design system, multi-component technology, applied in design optimization/simulation, liquid solution solvent extraction, calculation, etc., can solve problems such as heavy workload and shortage
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Embodiment 1
[0220] For a GdCl-containing 3 , EuCl 3 and SmCl 3 The aqueous phase feed liquid of the three components to be separated, the separation goal is to obtain SmCl with a purity of 99.99% 3 , EuCl 3 and GdCl 3 Three products. P507-kerosene is used as the extracted organic phase. During the separation process, the saponification of the extracted organic phase needs to consume alkali, and the washing process in the washing section needs to consume acid. By adopting the present invention, an extraction total separation process with the theoretical minimum consumption of acid and alkali can be quickly designed and obtained, that is, the designed total separation process has the theoretical minimum extraction amount and the minimum washing amount.
[0221] In the data input module, input the components to be separated as Gd, Eu and Sm; the flow rate of Gd, Eu and Sm in the feed liquid is f Gd,a , f Eu,a , f Sm,a Input 0.3000, 0.1000 and 0.6000 respectively, the total flow f a ...
Embodiment 2
[0265] The feed liquid to be separated contains NdCl 3 , PrCl 3 , CeCl 3 and LaCl 3 The water phase of the four components to be separated, the separation goal is to obtain LaCl with a purity of 99.99% 3 , CeCl 3 , PrCl 3 and NdCl 3 Four products. P507-kerosene is used as the extracted organic phase. During the separation process, the saponification of the extracted organic phase requires the consumption of alkali, and the washing process requires the consumption of acid. By adopting the invention, an extraction and complete separation process with the theoretical minimum consumption of acid and alkali can be quickly designed and obtained.
[0266] Input the components to be separated into Nd, Pr, Ce and La in the data input module; their flow f in the feed liquid Nd,a , f Pr,a , f Ce,a , f La,a Enter 0.1500, 0.0500, 0.5000 and 0.3000 respectively, the total flow f a 1.0000; Ce / La, Pr / Ce, Nd / Pr separation coefficient β Ce / La , β Pr / Ce and beta Nd / Pr The input is...
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