Toth Andras Jozsef
Environmental and Process Engineering Research Group, Department of Chemical and Environmental Process Engineering, Budapest University of Technology and Economics, H-1111, Hungary, Budapest, Műegyetem rkp. 3. And Institute of Chemistry, University of Miskolc, Egyetemváros C/1 108, H-3515 Miskolc, Hungary.
Membranes (Basel). 2020 Sep 28;10(10):265. doi: 10.3390/membranes10100265.
Nowadays, there is increasing interest in advanced simulation methods for desalination. The two most common desalination methods are multi-stage flash distillation (MSF) and reverse osmosis (RO). Numerous research works have been published on these separations, however their simulation appears to be difficult due to their complexity, therefore continuous improvement is required. The RO, in particular, is difficult to model, because the liquids to be separated also depend specifically on the membrane material. The aim of this study is to model steady-state desalination opportunities of saline process wastewater in flowsheet environment. Commercial flowsheet simulator programs were investigated: ChemCAD for thermal desalination and WAVE program for membrane separation. The calculation of the developed MSF model was verified based on industrial data. It can be stated that both simulators are capable of reducing saline content from 4.5 V/V% to 0.05 V/V%. The simulation results are in accordance with the expectations: MSF has higher yield, but reverse osmosis is simpler process with lower energy demand. The main additional value of the research lies in the comparison of desalination modelling in widely commercially available computer programs. Furthermore, complex functions are established between the optimized operating parameters of multi-stage flash distillation allowing to review trends in flash steps for complete desalination plants.
如今,人们对先进的海水淡化模拟方法越来越感兴趣。两种最常见的海水淡化方法是多级闪蒸(MSF)和反渗透(RO)。关于这些分离过程已经发表了大量的研究工作,然而由于其复杂性,它们的模拟似乎很困难,因此需要不断改进。特别是反渗透,很难进行建模,因为待分离的液体还特别取决于膜材料。本研究的目的是在流程环境中对含盐工艺废水的稳态海水淡化机会进行建模。研究了商业流程模拟程序:用于热法海水淡化的ChemCAD和用于膜分离的WAVE程序。基于工业数据对所开发的多级闪蒸模型的计算进行了验证。可以说,这两种模拟器都能够将含盐量从4.5 V/V%降低到0.05 V/V%。模拟结果符合预期:多级闪蒸产率更高,但反渗透是一种更简单的工艺,能源需求更低。该研究的主要附加价值在于在广泛使用的商业计算机程序中对海水淡化建模进行比较。此外,在多级闪蒸的优化操作参数之间建立了复杂的函数关系,从而能够审视完整海水淡化厂闪蒸步骤的趋势。