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Journal articles on the topic 'Reverse osmosis'

Author: Grafiati

Published: 4 June 2021

Last updated: 25 July 2025

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1

Rao, Sudhakar M. "Reverse osmosis." Resonance 12, no. 5 (2007): 37–40. http://dx.doi.org/10.1007/s12045-007-0048-8.

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2

Rao, Sudhakar M. "Reverse Osmosis." Resonance 16, no. 12 (2011): 1333–36. http://dx.doi.org/10.1007/s12045-011-0151-8.

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3

Fill, Marc, Flavio Muff, and Mirko Kleingries. "Evaluation of a new air water generator based on absorption and reverse osmosis." Heliyon 6, no. 9 (2020): 1–9. https://doi.org/10.5281/zenodo.5769412.

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The evaluation of a new air water generator (AWG) based on absorption and reverse osmosis is described. For the evaluation, an aqueous lithium bromide solution has been selected from a wide range of liquids as the absorbent. At high salt mass fractions, the aqueous lithium bromide solution has a low vapour pressure and a high osmotic pressure. The low vapour pressure ensures that the water vapour can be absorbed from the air, but the high osmotic pressure leads to high pressures over the membrane. Due to the high osmotic pressures, several reverse osmosis membrane modules are necessary and sal

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4

Altaee, Ali, Guillermo Zaragoza, and H. Rost van Tonningen. "Comparison between Forward Osmosis-Reverse Osmosis and Reverse Osmosis processes for seawater desalination." Desalination 336 (March 2014): 50–57. http://dx.doi.org/10.1016/j.desal.2014.01.002.

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5

Abdella, Dana L. "Reverse Osmosis Desalination." Marine Technology and SNAME News 31, no. 03 (1994): 195–200. http://dx.doi.org/10.5957/mt1.1994.31.3.195.

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Reverse osmosis (RO) desalination is a method of producing fresh water from seawater by a process similar to filtration, rather than by traditional evaporative distillation. A semipermeable membrane allows water molecules to pass through while blocking the passage of most other ions. The qualities of RO which make it attractive for naval and marine applications are its ability to operate on electric power alone, requiring no heat source; its comparatively low system weight to other methods of freshwater production at sea; and its ability to operate automatically, requiring minimal operator att

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6

Dukhin, S. S., Nikolai V. Churaev, V. N. Shilov, and Viktor M. Starov. "Modelling Reverse Osmosis." Russian Chemical Reviews 57, no. 6 (1988): 572–84. http://dx.doi.org/10.1070/rc1988v057n06abeh003374.

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7

McCray, Scott B. "Reverse osmosis technology." Journal of Membrane Science 49, no. 3 (1990): 352–53. http://dx.doi.org/10.1016/s0376-7388(00)80649-3.

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8

Sagiv, Abraham, Neta Avraham, Carlos G. Dosoretz, and Raphael Semiat. "Osmotic backwash mechanism of reverse osmosis membranes." Journal of Membrane Science 322, no. 1 (2008): 225–33. http://dx.doi.org/10.1016/j.memsci.2008.05.055.

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9

García, Andreina, B. Rodríguez, D. Ozturk, et al. "Desalination Performance of Antibiofouling Reverse Osmosis Membranes." Modern Environmental Science and Engineering 2, no. 07 (2016): 481–89. http://dx.doi.org/10.15341/mese(2333-2581)/07.02.2016/007.

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10

Shah, Tapan N., Yeomin Yoon, Cynthia L. Pederson, and Richard M. Lueptow. "Rotating reverse osmosis and spiral wound reverse osmosis filtration: A comparison." Journal of Membrane Science 285, no. 1-2 (2006): 353–61. http://dx.doi.org/10.1016/j.memsci.2006.09.004.

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11

Touati, Khaled, Fernando Tadeo, and Hamza Elfil. "Osmotic energy recovery from Reverse Osmosis using two-stage Pressure Retarded Osmosis." Energy 132 (August 2017): 213–24. http://dx.doi.org/10.1016/j.energy.2017.05.050.

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12

Dickel, Gerhard, and Abdeslam Chabor. "Osmosis and reverse osmosis. Part 2.—The separation factor of reverse osmosis and its connection with isotonic osmosis." Journal of the Chemical Society, Faraday Transactions 1: Physical Chemistry in Condensed Phases 82, no. 11 (1986): 3293. http://dx.doi.org/10.1039/f19868203293.

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13

Salahudeen, Nurudeen. "Process simulation of modelled reverse osmosis for desalination of seawater." Water Practice and Technology 17, no. 1 (2021): 175–90. http://dx.doi.org/10.2166/wpt.2021.127.

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Abstract Model equations for prediction of process parameters of reverse osmosis for desalination of seawater were developed via mathematical derivation from basic equations for the reverse osmosis process. A model equation relating the interfacial solute concentration () with the process pressure difference () was developed. Taking the of reverse osmosis as the basic independent variable, further model equations relating other process parameters such as the solute concentration polarity , water flux , osmotic pressure , water output rate (q), power density (Pd) and specific energy consumption

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14

Vyas, Prabhanshu, and Smriti G. Solomon. "Knowledge regarding reverse osmosis (R.O) waste water utilization among general public in urban areas." Southeast Asian Journal of Case Report and Review 10, no. 1 (2023): 13–19. http://dx.doi.org/10.18231/j.sajcrr.2023.003.

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Reverse osmosis (RO) is a water purification process that uses a partial permeable membrane to remove ions, unwanted molecules and larger particles from drinking water. In reverse osmosis, an applied pressure is used to overcome osmotic pressure, a colligative property that is driven by chemical potential differences of the solvent, a thermodynamic parameter. In the process of reverse osmosis the amount of water that is drained is a concern area for the people using the R.O. filtration device in their household because it wasted about 70% of the water to purify just one liter of water. This R.

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15

Liu, Mu. "A Review on Reverse Osmosis Membrane Fouling Diagnosis." International Journal of Oceanography & Aquaculture 7, no. 2 (2023): 1–8. http://dx.doi.org/10.23880/ijoac-16000238.

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During long-term operation, reverse osmosis (RO) membrane fouling is an inevitable occurrence that leads to a decline in membrane performance. When the water quality fails to meet specific application requirements, it becomes necessary to replace the deteriorated membranes. Membrane autopsy is widely recognized as the most direct and effective method for studying and identifying membrane fouling. By analyzing the results of membrane autopsy and membrane fouling diagnosis, valuable insights can be gained to optimize the operation of the membrane system, maintain the membrane elements through re

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16

Karode, Sandeep. "COUPLING REVERSE OSMOSIS AND OSMOTIC DEHYDRATION: FURTHER INVESTIGATIONS." Separation Science and Technology 36, no. 14 (2001): 3091–103. http://dx.doi.org/10.1081/ss-100107761.

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17

Kurihara, Masaru. "Seawater Reverse Osmosis Desalination." Membranes 11, no. 4 (2021): 243. http://dx.doi.org/10.3390/membranes11040243.

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18

Das, Abhimanyu, and David M. Warsinger. "Batch counterflow reverse osmosis." Desalination 507 (July 2021): 115008. http://dx.doi.org/10.1016/j.desal.2021.115008.

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19

Flemming, Hans-Curt. "Reverse osmosis membrane biofouling." Experimental Thermal and Fluid Science 14, no. 4 (1997): 382–91. http://dx.doi.org/10.1016/s0894-1777(96)00140-9.

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20

Watson, BruceM. "High recovery reverse osmosis." Desalination 78, no. 1 (1990): 91–97. http://dx.doi.org/10.1016/0011-9164(90)80032-7.

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21

Rautenbach, R. "Reverse osmosis technology edited." Chemical Engineering and Processing: Process Intensification 25, no. 1 (1989): 56. http://dx.doi.org/10.1016/0255-2701(89)85010-x.

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22

Kumar, Manish, Samer Adham, and James DeCarolis. "Reverse osmosis integrity monitoring." Desalination 214, no. 1-3 (2007): 138–49. http://dx.doi.org/10.1016/j.desal.2006.10.021.

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23

Francis, Roger. "Seawater Reverse Osmosis Desalination." Materials Performance 59, no. 11 (2020): 44–47. https://doi.org/10.5006/mp2020_59_11-44.

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It is estimated that by the year 2025, more than 60% of the world population living in 88 countries is expected to face serious water shortage. Severe water shortages are mainly due to explosive population growth, extensive changes in human lifestyle, increased industrial activities, and pollution.

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24

Prior, F. G. R., V. Morecroft, T. Gourlay, and K. M. Taylor. "The Therapeutic Significance of Pulse Reverse Osmosis." International Journal of Artificial Organs 19, no. 8 (1996): 487–92. http://dx.doi.org/10.1177/039139889601900810.

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Pulse reverse osmosis (1) is a new theory of fluid balance and exchange which suggests that the mean blood pressure and osmotic gradient control fluid balance and that the pulse controls fluid exchange. In vitro testing has confirmed some of the physico chemical principles underlying the theory (2). The hypothesis suggests a relationship between mean capillary blood pressure and osmotic gradient. Imbalance in this relationship can be related to the development of hypertension, hypotension, oedema and shock. In an attempt to test this concept mean blood pressures and colloid osmotic pressures w

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25

Wulan, Wulansari, Dwi Savitri Nur Hidayah, Ragil Johanda, et al. "PENGOLAHAN AIR ASIN MENJADI AIR TAWAR MENGGUNAKAN METODE REVERSE OSMOSIS DI KELURAHAN MENDAHARA ILIR." Jurnal Pengabdian Masyarakat Pinang Masak 2, no. 2 (2021): 54–61. http://dx.doi.org/10.22437/jpm.v2i2.15331.

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Air mempunyai peranan yang sangat penting dalam kehidupan manusia sehari-hari. Di Indonesia, banyak daerah mengalami permasalahan sumber air. Salah satunya di Kelurahan Mendahara Ilir, Kecamatan Mendahara, Kabupaten Tanjung Jabung Timur, Provinsi Jambi yang mengalami kesulitan mendapatkan air bersih. Masyarakat daerah Mendahara Ilir biasanya mendapatkan air bersih dengan cara menampung air hujan dan sumur bor yang dapat menyebabkan masalah lingkungan seperti penurunan tingkat permukaan tanah. Air laut yang sangat berlimpah dapat dimanfaatkan dan diolah menjadi air bersih dengan menggunakan tek

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26

Contreras-Martínez, Jorge, Carmen García-Payo, Paula Arribas, et al. "Recycled reverse osmosis membranes for forward osmosis technology." Desalination 519 (December 2021): 115312. http://dx.doi.org/10.1016/j.desal.2021.115312.

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27

Khramtsov, A. G. "Technological breakthrough of the agrarian-and-food innovations in dairy case for example of universal agricultural raw materials. Reverse osmosis." Agrarian-And-Food Innovations 14 (June 29, 2021): 7–20. http://dx.doi.org/10.31208/2618-7353-2021-14-7-20.

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Aim. Consideration of the membrane technology process – reverse osmosis – by directed and controlled processing of whey and its filtrates through special semipermeable partitions (filter membranes) with a pore size from 0.1 to 1.0 nm, carried out at a pressure of 3.0 - 10.0 MPa with the release of particles (cutting off) with a molecular weight of 100 Daltons. Reverse osmosis allows you to concentrate all the compounds of whey and filtrates, separating almost distilled water (condensate). Discussion. In the molecular sieve separation system, reverse osmosis logically continues the membrane tre

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28

Minhas, Muhammad B., Yusufu A. C. Jande, and Woo-Seung Kim. "Hybrid Reverse Osmosis-Capacitive Deionization versus Two-Stage Reverse Osmosis: A Comparative Analysis." Chemical Engineering & Technology 37, no. 7 (2014): 1137–45. http://dx.doi.org/10.1002/ceat.201300681.

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29

Tu, Qingsong, Tiange Li, Ao Deng, Kevin Zhu, Yifei Liu, and Shaofan Li. "A scale-up nanoporous membrane centrifuge for reverse osmosis desalination without fouling." TECHNOLOGY 06, no. 01 (2018): 36–48. http://dx.doi.org/10.1142/s2339547818500024.

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A scale-up nanoporous membrane centrifuge is designed and modeled. It can be used for nanoscale scale separation including reverse osmosis desalination. There are micron-size pores on the wall of the centrifuge and nanoscale pores on local graphene membrane patches that cover the micron-size pores. In this work, we derived the critical angular velocity required to counter-balance osmosis force, so that the reverse-osmosis (RO) desalination process can proceed. To validate this result, we conducted a large scale (four million atoms) full atom molecular dynamics (MD) simulation to examine the cr

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30

Sambeyano, Roby Nyoman. "OPTIMALISASI BLOWDOWN COOLING WATER MELALUI VARIASI PENGOLAHAN AIR MAKE-UP." Jurnal Teknologi Kimia Unimal 14, no. 1 (2025): 13–24. https://doi.org/10.29103/jtku.v14i1.21102.

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Sistem cooling water memiliki peran kritis dalam industri, namun menghadapi tantangan signifikan terkait akumulasi mineral, pengendapan, dan korosi yang dapat menurunkan efisiensi perpindahan panas. Penelitian ini bertujuan mengoptimalkan proses blowdown cooling water melalui variasi pengolahan air make-up. Studi dilakukan dengan menganalisis tiga variasi air make-up yaitu make-up tanpa reverse osmosis (RO), make-up campuran air tanpa reverse osmosis dan dengan reverse osmosis dengan perbandingan 50:50, dan make-up dengan pengolahan reverse osmosis sepenuhnya. Metodologi penelitian mencakup pe

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31

Magara, Y., M. Kawasaki, M. Sekino, and H. Yamamura. "Development of reverse osmosis membrane seawater desalination in Japan." Water Science and Technology 41, no. 10-11 (2000): 1–8. http://dx.doi.org/10.2166/wst.2000.0594.

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The seawater desalination facilities by reverse osmosis membranes in the world are reviewed. The largest seawater desalination facility using reverse osmosis started its operation at Chatan water purification plant in Okinawa prefectural water works. The high-efficiency seawater desalination technology which improves the recovery ratio of fresh water up to 60% developed by a manufacturing company of reverse osmosis membranes in Japan is explained. Finally the state of the art of desalination technology development using reverse osmosis membranes is discussed.

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32

Shen, Tianyi. "The advantages and future development trends of reverse seawater osmosis compared with other desalination methods." Highlights in Science, Engineering and Technology 21 (December 4, 2022): 398–404. http://dx.doi.org/10.54097/hset.v21i.3197.

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Global freshwater resources are not evenly distributed in regions and time, and with economic development and population growth, the world's water consumption is also increasing year by year. The world is facing a crisis of insufficient freshwater resources, which will become more and more serious in the future. In order to solve this problem, various countries are vigorously developing seawater desalination technology. Seawater reverse osmosis is one of the important methods of seawater desalination. The advantages and disadvantages of the seawater reverse osmosis method were obtained by comp

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33

Kůdela, Vlastimil, Klaus Richau, Olen Ryba, and Hans-Hartmuth Schwarz. "Orientation dependent concentration potentials of asymmetrical cellulose acetate membranes." Collection of Czechoslovak Chemical Communications 51, no. 7 (1986): 1419–29. http://dx.doi.org/10.1135/cccc19861419.

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Orientation dependent (asymmetrical) membrane potentials were observed on both reverse osmosis and ultrafiltration cellulose acetate and polymer sulfone membranes in contact with electrolyte solutions. It was shown that this phenomenon can be observed only on asymmetrical membranes with a gradient of fixed charge molality in the active layer (skin), provided that the activity of the more concentrated solution is comparable with or higher than the fixed charge molality in the active layer. This holds also for partly hydrolyzed reverse osmosis membranes. The origin of the orientation dependence

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34

Hulienko, S., and S. Virych. "RESISTANCE TO CONCENTRATION POLARISATION AT THE MEMBRANE: INFLUENCE OF OPERATING PARAMETERS AND MATHEMATICAL MODELLING." Znanstvena misel journal, no. 78 (May 29, 2023): 16–21. https://doi.org/10.5281/zenodo.7980576.

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This Research and Analysis paper presents a review of research related to reverse osmosis and concentration polarisation. In the introductory section, the general context and relevance of the problem are discussed, and the main aspects of reverse osmosis, its principle of operation and use are reviewed. Recent research aimed at studying the phenomenon of concentration polarisation in the context of reverse osmosis is described. Experimental and theoretical approaches are presented that allow for a more detailed understanding and quantification of this phenomenon. An overview of the results obt

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35

Sun, Xiao Ming, Jing Yang Liu, Qi Qiao, Yue Zhang, Na Zhang, and Li Hong Meng. "Application of Reverse Osmosis Membrane in Wastewater Treatmente." Applied Mechanics and Materials 737 (March 2015): 661–63. http://dx.doi.org/10.4028/www.scientific.net/amm.737.661.

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Reverse osmosis membrane is usually used to desalination. With the development of membrane materials and technology, the performance of reverse osmosis membrane is improved continuously, and the interception rate of organic matter is higher, the separation rate of the organic matter is obviously improved. The research progress and application status of separating organics in aqueous solution by reverse osmosis membrane is presented in this paper. The future research direction and application of reverse osmosis membrane for separating organics from aqueous solution were also analyzed and prospe

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36

Al-Alalawy, Ahmed Faiq, Talib Rashid Abbas, and Hadeer Kadhim Mohammed. "Comparative Study for Organic and Inorganic Draw Solutions in Forward Osmosis." Al-Khwarizmi Engineering Journal 13, no. 1 (2017): 94–102. http://dx.doi.org/10.22153/kej.2017.08.007.

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The present work aims to study forward osmosis process using different kinds of draw solutions and membranes. Three types of draw solutions (sodium chloride, sodium formate, and sodium acetate) were used in forward osmosis process to evaluate their effectiveness with respect to water flux and reverse salt flux. Experiments conducted in a laboratory-scale forward osmosis (FO) unit in cross flow flat sheet membrane cell. Three types of membranes (Thin film composite (TFC), Cellulose acetate (CA), and Cellulose triacetate (CTA)) were used to determine the water flux under osmotic pressure as a dr

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37

Kim, Jung Eun, Sherub Phuntsho, Syed Muztuza Ali, Joon Young Choi, and Ho Kyong Shon. "Forward osmosis membrane modular configurations for osmotic dilution of seawater by forward osmosis and reverse osmosis hybrid system." Water Research 128 (January 2018): 183–92. http://dx.doi.org/10.1016/j.watres.2017.10.042.

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38

Shabalin, V. V. "Evaluation of the selectivity of reverse osmotic membranes in separation of binary sodium chloride solutions." Вестник гражданских инженеров 19, no. 3 (2022): 110–19. http://dx.doi.org/10.23968/1999-5571-2022-19-3-110-119.

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Manufacturers of reverse osmosis filter membranes provide their products with computer programs that allow for technological evaluation calculations for solutions with different concentrations of impurities. The description of the programs does not include the computer methods and algorithms which are necessary for calculating traffic flows. Consequently, it is not possible to evaluate the selectivity of the reversely osmotic stages of membranes. The development of computer algorithms and techniques that would evaluate the operation of reverse osmosis plants taking into account external and in

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39

Parra, Abdon, Mario Noriega, Lidia Yokoyama, and Miguel Bagajewicz. "Does Pressure-Retarded Osmosis Help Reverse Osmosis in Desalination?" Industrial & Engineering Chemistry Research 60, no. 11 (2021): 4366–74. http://dx.doi.org/10.1021/acs.iecr.0c04382.

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40

Murad, S., and J. G. Powles. "Computer simulation of osmosis and reverse osmosis in solutions." Chemical Physics Letters 225, no. 4-6 (1994): 437–40. http://dx.doi.org/10.1016/0009-2614(94)87108-6.

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41

Bilstad, T., and M. V. Madland. "Leachate Minimization by Reverse Osmosis." Water Science and Technology 25, no. 3 (1992): 117–20. http://dx.doi.org/10.2166/wst.1992.0084.

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Leachates from chemical and domestic landfills are defined as hazardous wastewater. Quantitative and qualitative control of leachate can be performed by membrane separation of the total produced leachate volume. Dissolved and suspended solids in the leachate are removed from the major portion of the water phase and either returned to the landfill or further treated. The particle - free permeate meets the effluent requirements for direct discharge to virtually any watercourse. An untreated leachate flow is concentrated thirteen times by tubular type reverse osmosis. The separation efficiencies

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42

Ishibashi, Ryo. "Fouling Resistant Reverse Osmosis Elements." MEMBRANE 44, no. 3 (2019): 136–39. http://dx.doi.org/10.5360/membrane.44.136.

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43

KISO, Yoshiaki, and Takane KITAO. "Reverse osmosis and liquid chromatography." membrane 12, no. 5 (1987): 272–80. http://dx.doi.org/10.5360/membrane.12.272.

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44

Henthorne, Lisa. "Trends in Seawater Reverse Osmosis." IDA Journal of Desalination and Water Reuse 2, no. 3 (2010): 12–13. http://dx.doi.org/10.1179/ida.2010.2.3.12.

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45

zum Kolk, Christian, Wolfgang Hater, and Niclas Kempken. "Cleaning of reverse osmosis membranes." Desalination and Water Treatment 51, no. 1-3 (2012): 343–51. http://dx.doi.org/10.1080/19443994.2012.715424.

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46

Isaias, Nicos P. "Experience in reverse osmosis pretreatment." Desalination 139, no. 1-3 (2001): 57–64. http://dx.doi.org/10.1016/s0011-9164(01)00294-6.

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47

Ning, Robert Y. "Arsenic removal by reverse osmosis." Desalination 143, no. 3 (2002): 237–41. http://dx.doi.org/10.1016/s0011-9164(02)00262-x.

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48

Dababneh, Awwad J., and M. A. Al-Nimr. "A reverse osmosis desalination unit." Desalination 153, no. 1-3 (2003): 265–72. http://dx.doi.org/10.1016/s0011-9164(02)01145-1.

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49

Kryvoruchko, Antonina P., and Boris Yu Kornilovich. "Water deactivation by reverse osmosis." Desalination 157, no. 1-3 (2003): 403–7. http://dx.doi.org/10.1016/s0011-9164(03)00423-5.

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50

Kahdim, Abdul Sattar, Saleh Ismail, and Alaa' Abdulrazaq Jassim. "Modeling of reverse osmosis systems." Desalination 158, no. 1-3 (2003): 323–29. http://dx.doi.org/10.1016/s0011-9164(03)00471-5.

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