Methodological approaches to conducting pilot and proof tests on reverse-osmosis systems: Results of comparative studies
- 作者: Panteleev A.A.1, Bobinkin V.V.2, Larionov S.Y.2, Ryabchikov B.E.2, Smirnov V.B.2, Shapovalov D.A.1
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隶属关系:
- Moscow Power Engineering Institute
- Scientific Production Company Mediana-Fil’tr
- 期: 卷 64, 编号 10 (2017)
- 页面: 781-786
- 栏目: Water Treatment and Water-Chemistry Conditions
- URL: https://journals.rcsi.science/0040-6015/article/view/172846
- DOI: https://doi.org/10.1134/S0040601517100093
- ID: 172846
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详细
When designing large-scale water-treatment plants based on reverse-osmosis systems, it is proposed to conduct experimental-industrial or pilot tests for validated simulation of the operation of the equipment. It is shown that such tests allow establishing efficient operating conditions and characteristics of the plant under design. It is proposed to conduct pilot tests of the reverse-osmosis systems on pilot membrane plants (PMPs) and test membrane plants (TMPs). The results of a comparative experimental study of pilot and test membrane plants are exemplified by simulating the operating parameters of the membrane elements of an industrial plant. It is concluded that the reliability of the data obtained on the TMP may not be sufficient to design industrial water-treatment plants, while the PMPs are capable of providing reliable data that can be used for full-scale simulation of the operation of industrial reverse-osmosis systems. The test membrane plants allow simulation of the operating conditions of individual industrial plant systems; therefore, potential areas of their application are shown. A method for numerical calculation and experimental determination of the true selectivity and the salt passage are proposed. An expression has been derived that describes the functional dependence between the observed and true salt passage. The results of the experiments conducted on a test membrane plant to determine the true value of the salt passage of a reverse-osmosis membrane are exemplified by magnesium sulfate solution at different initial operating parameters. It is shown that the initial content of a particular solution component has a significant effect on the change in the true salt passage of the membrane.
作者简介
A. Panteleev
Moscow Power Engineering Institute
Email: ShapovalovDA2010@mail.ru
俄罗斯联邦, Moscow, 111250
V. Bobinkin
Scientific Production Company Mediana-Fil’tr
Email: ShapovalovDA2010@mail.ru
俄罗斯联邦, Moscow, 105318
S. Larionov
Scientific Production Company Mediana-Fil’tr
Email: ShapovalovDA2010@mail.ru
俄罗斯联邦, Moscow, 105318
B. Ryabchikov
Scientific Production Company Mediana-Fil’tr
Email: ShapovalovDA2010@mail.ru
俄罗斯联邦, Moscow, 105318
V. Smirnov
Scientific Production Company Mediana-Fil’tr
Email: ShapovalovDA2010@mail.ru
俄罗斯联邦, Moscow, 105318
D. Shapovalov
Moscow Power Engineering Institute
编辑信件的主要联系方式.
Email: ShapovalovDA2010@mail.ru
俄罗斯联邦, Moscow, 111250
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