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A novel Forward osmosis membrane pretreatment of seawater for thermal desalination processes

机译:用于海水淡化的新型正渗透膜预处理

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The present work introduced a novel conceptual design of integrating Forward Osmosis (FO) membrane with the MuW Stage Flashing (MSF) or Multi Effect Distillation (MED) thermal desalination processes. A simple mathematical model was developed here to estimate the performance of the FO membrane system A previously developed program, VDS, for estimating the performance of thermal processes was updated to include the FO system. The verified VDS program [1 ] was applied to simulate the performance of the FO-MSF/MED hybrid system at different recovery rates varied from 16% to 32%. Brine reject from the thermal desalination processes was recycled and used as a draw solution to reduce the cost of FO membrane pretreatment Seawater was used as the donor solution in the FO membrane. The simulation results showed that the FO pretreatment, successfully, reduced the concentration of multivalent ions in the feed solution to the MSF and MED. It was found that the concentrations of Ca~(2+), Mg~(2+), and SO_4~(2-) ions, which are responsible for scale problem in MSF, decreased with increasing the recovery rate of FO membrane. In case of FO-MED hybrid system, the thickness of the CaCO3 scale layer was calculated at different FO recovery rates. The estimated thickness of CaCO3 scale layer was 74 μm, 43 μm, and 39 μm for 0%, 20%, and 32% FO recovery rate respectively. It was also found that the thickness of CaCO3 scale layer decreased in the direction from effect 1 to effect 6 due to temperature drop. Finally, the study demonstrated the feasible application of FO membrane in the pretreatment of seawater to reduce the concentration of multivalent ions which are responsible for the scale problem in the thermal desalination processes.
机译:本工作介绍了将正向渗透(FO)膜与MuW阶段闪蒸(MSF)或多效蒸馏(MED)热脱盐工艺相集成的新颖概念设计。这里开发了一个简单的数学模型来评估FO膜系统的性能。先前开发的用于评估热过程性能的程序VDS已更新为包括FO系统。经过验证的VDS程序[1]被用于模拟FO-MSF / MED混合系统在不同回收率(从16%到32%)下的性能。将来自热脱盐工艺的盐水废渣进行再循环,并用作抽取溶液,以降低FO膜预处理的成本。海水用作FO膜中的供体溶液。模拟结果表明,FO预处理成功地降低了MSF和MED进料溶液中多价离子的浓度。研究发现,导致MSF结垢的Ca〜(2 +),Mg〜(2+)和SO_4〜(2-)离子的浓度随着FO膜回收率的提高而降低。对于FO-MED混合系统,在不同的FO回收率下计算了CaCO3氧化皮层的厚度。 FO回收率分别为0%,20%和32%时,CaCO3氧化皮层的估计厚度分别为74μm,43μm和39μm。还发现由于温度下降,CaCO 3垢层的厚度在从效果1到效果6的方向上减小。最后,研究证明了FO膜在海水预处理中以降低多价离子的浓度的可行性,这是造成热脱盐过程中结垢的原因。

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