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首页> 外文期刊>Brazilian journal of chemical engineering >EVALUATION OF SODIUM CHLORIDE CRYSTALLIZATION IN MEMBRANE DISTILLATION CRYSTALLIZATION APPLIED TO WATER DESALINATION
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EVALUATION OF SODIUM CHLORIDE CRYSTALLIZATION IN MEMBRANE DISTILLATION CRYSTALLIZATION APPLIED TO WATER DESALINATION

机译:膜脱盐法中氯化钠结晶法在水脱盐中的应用

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Crystallization in a Direct Contact Membrane Distillation (DCMD) process was studied both theoretically and experimentally. A mathematical model was proposed in order to predict the transmembrane flux in DCMD. The model fitted well experimental data for the system NaCl-H 2 O from undersaturated to supersaturated conditions in a specially designed crystallization setup at a bench scale. It was found that higher transmembrane fluxes induce higher temperature and concentration polarizations, as well as higher supersaturation in the vicinity of the solution-vapor interface. In this region, the supersaturation ratio largely exceeded the metastable limit for NaCl crystallization for the whole range of transmembrane fluxes of 0.37 to 1.54 kg/ (m 2 h), implying that heterogeneous primary nucleation occurred close to such interface either in solution or on the membrane surface. Solids formed in solution accounted for 14 to 36% of the total solids, whereas solid formed on the membrane surface (fouling) was responsible for 6 to 19%. The remaining solids deposited on other surfaces such as in pumps and pipe fittings. It was also discovered that, by increasing the supersaturation ratio, heterogeneous nucleation in solution increased and on the membrane surface decreased. Heterogeneous nuclei in solution grew in size both by a molecular mechanism and by agglomeration. Single crystals were cubic shaped with well-formed edges and dominant size of about 40 ?μm whereas agglomerates were about 240 ?μm in size. The approach developed here may be applied to understanding crystallization phenomena in Membrane Distillation Crystallization (MDC) processes of any scale.
机译:理论上和实验上都研究了直接接触膜蒸馏(DCMD)过程中的结晶。为了预测DCMD中的跨膜通量,提出了一个数学模型。该模型在专门设计的结晶试验台上,从不饱和状态到过饱和状态,很好地拟合了NaCl-H 2 O系统的实验数据。发现较高的跨膜通量引起较高的温度和浓度极化,以及溶液-蒸汽界面附近较高的过饱和度。在该区域,过饱和比在整个跨膜通量范围为0.37至1.54 kg /(m 2 h)的范围内大大超过了NaCl结晶的亚稳态极限,这表明在溶液中或在界面上靠近该界面发生了不均匀的一次成核。膜表面。溶液中形成的固体占总固体的14%至36%,而在膜表面(结垢)形成的固体占6%至19%。剩余的固体沉积在其他表面上,例如泵和管道配件中。还发现,通过增加过饱和比,溶液中的异相成核增加而膜表面上的异种成核减少。溶液中的异质核通过分子机理和附聚而增大。单晶呈立方体状,边缘形成良好,主要尺寸约为40?μm,而附聚物的尺寸约为240?μm。本文开发的方法可用于了解任何规模的膜蒸馏结晶(MDC)过程中的结晶现象。

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