Reagent-Free Methods for Reducing the Amount of Concentrate from Reverse Osmosis Plants

封面

如何引用文章

全文:

开放存取 开放存取
受限制的访问 ##reader.subscriptionAccessGranted##
受限制的访问 订阅存取

详细

Of all developed water desalination processes, reverse osmosis takes the leading place - 69% of the world’s fresh water production is attributed to reverse osmosis plants, one of the efficiency criteria of which is the amount of concentrate produced. The article describes some modern baromembrane reagentless methods of reducing the amount of concentrate of reverse osmosis plants, the main criterion for the selection of which is the experience of their industrial application. Such processes as forward osmosis, pressure assisted forward osmosis, osmotically assisted reverse osmosis, semi-batch reverse osmosis, pulse flow reverse osmosis are considered, their working principle and results of practical application in industry or large-scale pilot tests are given.

全文:

受限制的访问

作者简介

A. Smirnov

National Research University „MPEI“

编辑信件的主要联系方式.
Email: SmirnovAlAlex@mpei.ru
俄罗斯联邦, Krasnokazarmennaya, 14, Moscow, 111250

V. Smirnov

Mediana-Filter Research and Production Company JSC

Email: Smirnov@mediana-filter.ru
俄罗斯联邦, 1 Tkatskaya St., Moscow, 105318

参考

  1. Jones E., Qadir M., van Vliet M.T.H., Smakhtin V., Kang S. The state of desalination and brine production: A global outlook // Sci. Total Environ. 2019. V. 657. P. 1343.
  2. McGinnis R.L., Elimelech M. Energy requirements of ammonia–carbon dioxide forward osmosis desalination // Desalination. 2007. V. 207. P. 370.
  3. Xu Y., Zhu Y., Chen Z., Zhu J., Chen G. A Comprehensive Review on Forward Osmosis Water Treatment: Recent Advances and Prospects of Membranes and Draw Solutes // Int. J. Environ. Res. Public Health. 2022. V. 19. P. 8215.
  4. Abounahia N., Ibrar I., Kazwini T., Altaee A., Samal A.K., Zaidi S.J., Hawari A.H. Desalination by the forward osmosis: Advancement and challenges // Sci. Total Environ. 2023. V. 886. P. 163901.
  5. FO plant completes 1-year of operation. Water Desalination Report: 2–3. 15 Nov 2010. URL: https://www.desalination.com/articles/fo-plant-completes-1-year-of-operation (дата обращения: 15.09.2024).
  6. Altaee A., Braytee A., Millar G.J., Naji O. Energy efficiency of hollow fibre membrane module in the forward osmosis seawater desalination process // J. Membr. Sci. 2019. V. 587. P. 117165.
  7. Forward Osmosis – A Brief Introduction. Water Today. 2017. URL: https://idadesal.org/wp-content/uploads/2018/11/140824-Nicoll-IDA-Whte-Paper-Forward-Osmosis-A-Brief-Introduction.pdf (дата обращения: 30.09.2024).
  8. Андрианов А.П., Янцен О.В., Ефремов Р.В. Прямой осмос сегодня: перспективы и ограничения // Мембраны и мембранные технологии. 2023. Т. 13. № 4. С. 312.
  9. Blandin G., Verliefde A., Tang C.Y., Childress A.E., Le-Clech P. Validation of assisted forward osmosis (AFO) process: impact of hydraulic pressure // Journal of membrane science. 2013. V. 447. P. 1.
  10. FilmTec™ Reverse Osmosis Membranes Technical Manual. URL: https://www.dupont.com/content/dam/dupont/amer/us/en/water-solutions/public/documents/en/RO-NF-FilmTec-Manual-45-D01504-en.pdf (дата обращения: 04.10.2024).
  11. Toray sea water reverse osmosis membranes. URL: https://www.water.toray/products/ro/#sea-water (дата обращения: 30.09.2024).
  12. Toyobo MC membrane module for brine concentration. URL: https://www.toyobo-mc.jp/wordpress/wp-content/uploads/2023/10/TMC-Brochure_BC_2305.pdf (дата обращения: 07.10.2024).
  13. Innovative brine concentration using osmotically assisted reverse osmosis (OARO) process and advanced hollow fiber membrane. URL: http://worldwatersummit.in/presentation/2023/Day-1/Takahhito_nako.pdf (дата обращения: 15.10.2024).
  14. Ju J., Lee S., Kim Y., Cho H., Lee S. Theoretical and Experimental Analysis of Osmotically Assisted Reverse Osmosis for Minimum Liquid Discharge // Membranes. 2023. V. 13. P. 814.
  15. Пантелеев А.А., Пантелеев А.А., Рябчиков Б.Е., Сидоров А.Р., Смирнов В.Б. Высокоэффективные УОО с мембранными элементами рулонного типа // Новое в российской электроэнергетике. 2024. № 8. С. 15.
  16. Boyd М. Twenty-first century reverse osmosis disrupts traditional technology // World Water. 2019. V. 4. P. 26.
  17. Матусевич Л.Н. Кристаллизация из растворов в химической промышленности. М.: Химия, 1968. C. 304.
  18. Qian L., Guo-Rong X., Rasel D. Inorganic scaling in reverse osmosis (RO) desalination: Mechanisms, monitoring, and inhibition strategies // Desalination. 2019. V. 468. P. 114065.
  19. Elimelech M., Phillip W.A. The future of seawater desalination: energy, technology, and the environment // Science. 2011. V. 333. P. 712.
  20. Gal Z., Efraty A. CCD series no. 18: record low energy in closed-circuit desalination of ocean seawater with NanoH2O elements without ERD // Desalinаtion Water Treatment. 2015. V. 57. P. 9180.
  21. Jungbin K., Linyinxue D., Ho S., Kiho P. Current progress in semi-batch reverse osmosis for brackish water desalination // Desalination. 2024. V. 578 P. 117434.
  22. Liberman B. Three methods of forward osmosis cleaning for RO membranes // Desalination. 2018. V. 431. P. 22.
  23. Liberman B., Lior E., Greenberg G. Pulse Flow RO–The new RO technology for waste and brackish water applications // Desalination. 2020. V. 479. P. 114336.
  24. Смирнов А.А., Смирнов В.Б. Повышение эффективности двухступенчатых установок обратного осмоса // Новое в российской электроэнергетике. 2024. № 7. С. 24.

补充文件

附件文件
动作
1. JATS XML
下载
2. Fig. 1. Illustration of the forward osmosis mechanism (a) and a typical application scheme (b).

下载 (440KB)
索引源数据
3. Fig. 2. Illustration of the pressure assisted forward osmosis (PAFO) mechanism.

下载 (295KB)
索引源数据
4. Fig. 3. Illustration of the mechanism of reverse osmosis (a) and reverse osmosis with osmotic support (b).

下载 (256KB)
索引源数据
5. Fig. 4. Stages of the semi-batch reverse osmosis process.

下载 (316KB)
索引源数据
6. Fig. 5. Flows of feed water, concentrate, permeate and filtration pressure at the stages of operation of a semi-batch reverse osmosis plant.

下载 (236KB)
索引源数据
7. Fig. 6. Connection diagram of membrane devices in a continuous reverse osmosis unit (a) and in a pulsating flow reverse osmosis unit (b).

下载 (245KB)
索引源数据
8. Fig. 7. The mechanism of cleaning the membrane surface in a reverse osmosis system with a pulsating flow.

下载 (326KB)
索引源数据
9. Fig. 8. Dependence of the saturation index of poorly soluble substances (LSI) in the concentrate (a) and the quality of the permeate of the second stage of reverse osmosis (b) on the degree of permeate extraction in the first stage reverse osmosis unit at different salt content of the source water: the Volkhov River (Veliky Novgorod) - 195.6 mg/l, the Sochi River (Sochi) - 490.6 mg/l, Lake Balkhash (Balkhash) - 1877.6 mg/l.

下载 (299KB)
索引源数据

版权所有 © Russian Academy of Sciences, 2025