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Method for the purification of a liquid by membrane distillation, in particular for the production of desalinated water from seawater or brackish water or process water

机译:通过膜蒸馏纯化液体的方法,特别是用于从海水或微咸水或工艺用水生产脱盐水的方法

摘要

The following process steps are carried out in order to purify a liquid by membrane distillation, in particular to produce desalinated water from seawater or brackish water or process water:passing a relatively warn vaporising stream of liquid (retentate stream) over a porous membrane, vapour flowing via the pores of the membrane to the other side of said membrane, andcondensing said vapour on a relatively cool condenser surface to give a distillate stream, said condenser surface forming the non-porous separation between a feed stream to be purified and said distillate steam, which feed stream is in counter-current with the retentate stream so that an appreciable proportion of the latent heat will be transferred via vapour to the feed stream, and a gas gap with a width of less than 5 mm being present between the porous membrane and the condenser surface.In order to improve the distillate flow rate per unit driving force, a pressure which is lower than the atmospheric pressure and higher than the vapor pressure of the feed stream is maintained in the gas gap, the porosity epsilon of the porous membrane is higher than 0.7, porosity being understood to be the ratio of the open volume to the total volume of the porous membrane, the surface area of the condenser surface is 1.2 to 6 times, preferably 2 to 3 times, the surface area of the porous membrane, the effective local vapour pressure difference between the retentate seam and the condensing stream is less than 10 kPa (0.1 bar), preferably less than 5 kPa (0.05 bar) and the perceptible heat of the distillate stream is released by heat exchange to the feed stream and/or the retentate stream, with preference for the retentate stream.
机译:进行以下工艺步骤以通过膜蒸馏来纯化液体,特别是从海水或微咸水或工艺用水中生产脱盐水:使相对警告的液体汽化流(截留物流)流过多孔膜,蒸气经由膜的孔流至所述膜的另一侧,并将所述蒸气冷凝在相对凉的冷凝器表面上以产生馏出物流,所述冷凝器表面在待纯化的进料流和所述馏出蒸汽之间形成无孔分离。 ,该进料流与截留物流成逆流,因此相当一部分潜热将通过蒸气转移到进料流,并且多孔膜之间存在宽度小于5 mm的气隙为了提高每单位驱动力的馏出流量,压力要比大气压低而高。相对于在气隙中保持进料流的蒸气压,多孔膜的孔隙率ε高于0.7,孔隙率应理解为开口率与多孔膜总表面积,表面积之比。冷凝器表面的面积为多孔膜表面积的1.2至6倍,优选为2至3倍,截留物接缝与冷凝流之间的有效局部蒸气压差小于10 kPa(0.1 bar),优选为小于5kPa(0.05bar),并且馏出物流的可察觉的热量通过热交换释放至进料流和/或渗余物流,优选渗余物流。

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