Bioforest S. A., Camino Coronel Km 15, Coronel, 4190000, Chile; Department of Civil Engineering, Universidad de Concepción, P.O. Box 160-C, Concepción, 4030000, Chile.
Department of Civil Engineering, Universidad de Concepción, P.O. Box 160-C, Concepción, 4030000, Chile.
J Environ Manage. 2022 Feb 1;303:114104. doi: 10.1016/j.jenvman.2021.114104. Epub 2021 Nov 22.
We evaluated percrystallization at laboratory scale to determine its suitability as core technology for achieving Zero Liquid Discharge (ZLD) in a Kraft effluent desalination process. Compared with conventional evaporation/crystallization techniques, percrystallization allows to operate at room temperature and with barely pressurized fluids, using relatively unexpensive membranes and vacuum to allow evaporation of aqueous brine solutions. For further comprehension of the technology before experimentation, a computational fluid dynamics model was developed, showing how temperature affects the performance of percrystallization in terms of transmembrane flux. Additionally, we performed experiments with single and double salt solutions (NaCl and NaCl/NaSO) and concentrated industrial effluent from a Kraft pulp mill (brine from the effluent desalination with electrodialysis). Percrystallization of the concentrated industrial effluent was successfully achieved at laboratory scale, showing no signs of fouling on the membrane surface. However, high energy consumptions (above 3000 kWh/ton of evaporated water) were measured. Theoretical power consumptions of an optimized industrial percrystallization system were therefore computed. Percrystallization showed a more efficient performance compared with similar membrane systems, such as vacuum membrane distillation, but higher energy consumptions than conventional ZLD technologies (mechanical vapor compression), having an estimated energy consumption of around 110-150 kWh/ton of removed water, depending on the feed fluid temperature. Nevertheless, percrystallization could be suitable for ZLD applications where low-cost heating (e.g., solar) is available, since the vacuum energy demand is only 32-140 kWh/ton. Alternatively, it could be applied to low scale processes where the temperature of the solution must remain low (e.g., less than 40 °C).
我们在实验室规模上评估了预结晶,以确定其作为实现 Kraft 废水脱盐过程零液体排放 (ZLD) 的核心技术的适用性。与传统的蒸发/结晶技术相比,预结晶允许在室温下操作,使用几乎无压力的流体,使用相对廉价的膜和真空来允许蒸发盐水溶液。为了在实验前进一步理解该技术,我们开发了一个计算流体动力学模型,展示了温度如何影响预结晶在跨膜通量方面的性能。此外,我们还进行了单盐和双盐溶液 (NaCl 和 NaCl/Na2SO4) 以及 Kraft 纸浆厂浓缩工业废水 (电渗析脱盐后的废水) 的实验。浓缩工业废水的预结晶在实验室规模上成功实现,膜表面没有结垢迹象。然而,测量到的能耗很高(蒸发水每吨超过 3000 kWh)。因此,计算了优化的工业预结晶系统的理论能耗。与类似的膜系统(如真空膜蒸馏)相比,预结晶表现出更高效的性能,但比传统的 ZLD 技术(机械蒸汽压缩)的能耗更高,估计能耗约为 110-150 kWh/吨去除的水,具体取决于进料流体的温度。然而,预结晶可能适用于需要低成本加热(例如太阳能)的 ZLD 应用,因为真空的能源需求仅为 32-140 kWh/吨。或者,它可以应用于需要保持低温的小规模过程(例如低于 40°C)。