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Greisner B, Mauer D, Rögener F, Lerch A. Predicting Water Flux in Forward Osmosis with Unknown Feed Solution Composition: An Empirical Approach Based on Thermodynamical Properties. MEMBRANES 2023; 13:427. [PMID: 37103854 PMCID: PMC10142923 DOI: 10.3390/membranes13040427] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Abstract] [Key Words] [Track Full Text] [Figures] [Subscribe] [Scholar Register] [Received: 02/10/2023] [Revised: 04/04/2023] [Accepted: 04/05/2023] [Indexed: 06/19/2023]
Abstract
This study investigated the predictability of forward osmosis (FO) performance with an unknown feed solution composition, which is important in industrial applications where process solutions are concentrated but their composition is unknown. A fit function of the unknown solution's osmotic pressure was created, correlating it with the recovery rate, limited by solubility. The osmotic concentration was derived and used in the subsequent simulation of the permeate flux in the considered FO membrane. For comparison, magnesium chloride and magnesium sulfate solutions were used since these show a particularly strong deviation from the ideal osmotic pressure according to Van't Hoff and are, thus, characterized by an osmotic coefficient unequal to 1. The simulation is based on the solution-diffusion model with consideration of external and internal concentration polarization phenomena. Here, a membrane module was subdivided into 25 segments of equal membrane area, and the module performance was solved by a numerical differential. Experiments in a laboratory scale for validation confirmed that the simulation gave satisfactory results. The recovery rate in the experimental run could be described for both solutions with a relative error of less than 5%, while the calculated water flux as a mathematical derivative of the recovery rate showed a bigger deviation.
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Affiliation(s)
| | | | - Frank Rögener
- TH Köln, Institute of Chemical Process Engineering and Plant Design, 50679 Köln, Germany
| | - André Lerch
- Institute of Urban and Industrial Water Management, Technische Universität Dresden, 01062 Dresden, Germany
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Bardhan A, Subbiah S, Mohanty K. Modeling and Experimental Validation for the Preparation of Concentrated Tea Extract Using a Forward Osmosis Process Using a Food-Grade Inorganic Draw Solute. Ind Eng Chem Res 2023. [DOI: 10.1021/acs.iecr.2c04219] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 02/11/2023]
Affiliation(s)
- Ananya Bardhan
- Department of Chemical Engineering, Indian Institute of Technology Guwahati, Guwahati 781039, India
| | - Senthilmurugan Subbiah
- Department of Chemical Engineering, Indian Institute of Technology Guwahati, Guwahati 781039, India
| | - Kaustubha Mohanty
- Department of Chemical Engineering, Indian Institute of Technology Guwahati, Guwahati 781039, India
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3
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Fuzzy logic control of a brackish water reverse osmosis desalination process. Comput Chem Eng 2022. [DOI: 10.1016/j.compchemeng.2022.108026] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/23/2022]
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Nematzadeh M, Samimi A, Mohebbi-Kalhori D, Shokrollahzadeh S, Bide Y. Forward osmosis dewatering of seawater and pesticide contaminated effluents using the commercial fertilizers and zinc-nitrate blend draw solutions. THE SCIENCE OF THE TOTAL ENVIRONMENT 2022; 820:153376. [PMID: 35077789 DOI: 10.1016/j.scitotenv.2022.153376] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Abstract] [Key Words] [MESH Headings] [Track Full Text] [Subscribe] [Scholar Register] [Received: 07/08/2021] [Revised: 12/16/2021] [Accepted: 01/20/2022] [Indexed: 06/14/2023]
Abstract
Fertilizer driven forward osmosis (FDFO) process would be feasible due to the possible prevention of the drainage of dewatered and concentrated pesticide effluent from agricultural pesticide industries to the environment. Instead, it would be possible to return the concentrated pesticide solution to the processing cycle, and on the other hand, employ directly the obtained diluted fertilizer draw solution for irrigation. This study investigated the performance of zinc-nitrate/amino-acids blends as fertilizer type draw solution, and distilled water, saline water (seawater), and synthetic wastewater containing pesticides as feed. The results indicated that the synergetic effect of blended type fertilizer presented significantly higher osmotic pressure and water flux than the sum of their individual ones, especially when the amount of amino acid increased. Conversely, an ignorable reverse flux of blended fertilizer draw solute was observed. The fertilizer blend with a molar ratio of 1:6 zinc-nitrate/amino-acid achieved the higher average fluxes of 34.7 and 23.92 L/m2h from distilled and saline waters compared to common draw solutions such as metal salts. Furthermore, the FDFO exhibited a high rejection (over 99%) of bentazon and imidacloprid in feed solutions compared to other agricultural pesticides due to their larger molecular weight and molecular size. The applied FDFO represented a significant reduction in specific energy consumption (from 0.17 to 0.049 kWh/m3) in a bench-scale setup as compared to the RO process almost at the same water permeation flux and the rejection of bentazon.
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Affiliation(s)
- Mohammad Nematzadeh
- Department of Chemical Engineering, University of Sistan and Baluchestan, Zahedan, Iran
| | - Abdolreza Samimi
- Department of Chemical Engineering, University of Sistan and Baluchestan, Zahedan, Iran.
| | - Davod Mohebbi-Kalhori
- Department of Chemical Engineering, University of Sistan and Baluchestan, Zahedan, Iran
| | - Soheila Shokrollahzadeh
- Department of Chemical Technologies, Iranian Research Organization for Science and Technology (IROST), Tehran, Iran
| | - Yasamin Bide
- Department of Chemical Technologies, Iranian Research Organization for Science and Technology (IROST), Tehran, Iran
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Sayyad S, Kamthe N, Sarvade S. Design and simulation of reverse osmosis process in a hybrid forward osmosis-reverse osmosis system. Chem Eng Res Des 2022. [DOI: 10.1016/j.cherd.2022.05.002] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/03/2022]
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Li Z, Xiao S, Xiong Q, Wu C, Huang J, Zhou R, Jin Y. Assessment of highly concentrated pear juice production through single-run forward osmosis using sodium lactate as the draw solute. J FOOD ENG 2022. [DOI: 10.1016/j.jfoodeng.2022.111122] [Citation(s) in RCA: 1] [Impact Index Per Article: 0.5] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 12/26/2022]
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Sarode SC, Sharma NK, Sarode G, Bhatkar D. Do osmotic pressure and hygroscopicity of areca nut related products drive extracellular fluid loss and condensation of collagen bundles in oral submucous fibrosis? Med Hypotheses 2022. [DOI: 10.1016/j.mehy.2022.110836] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 10/18/2022]
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Cai M, Zhong H, Chu H, Zhu H, Sun P, Liao X. Forward osmosis concentration of high viscous polysaccharides of
Dendrobium officinale
: Process optimisation and membrane fouling analysis. Int J Food Sci Technol 2021. [DOI: 10.1111/ijfs.15225] [Citation(s) in RCA: 2] [Impact Index Per Article: 0.7] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 12/20/2022]
Affiliation(s)
- Ming Cai
- Department of Food Science and Technology Zhejiang University of Technology Hangzhou Zhejiang 310014 China
- Key Laboratory of Food Macromolecular Resources Processing Technology Research (Zhejiang University of Technology) China National Light Industry Hangzhou Zhejiang 310014 China
| | - Huazhao Zhong
- Department of Food Science and Technology Zhejiang University of Technology Hangzhou Zhejiang 310014 China
- Key Laboratory of Food Macromolecular Resources Processing Technology Research (Zhejiang University of Technology) China National Light Industry Hangzhou Zhejiang 310014 China
| | - Haoqi Chu
- Department of Food Science and Technology Zhejiang University of Technology Hangzhou Zhejiang 310014 China
- Key Laboratory of Food Macromolecular Resources Processing Technology Research (Zhejiang University of Technology) China National Light Industry Hangzhou Zhejiang 310014 China
| | - Hua Zhu
- Department of Food Science and Technology Zhejiang University of Technology Hangzhou Zhejiang 310014 China
- Key Laboratory of Food Macromolecular Resources Processing Technology Research (Zhejiang University of Technology) China National Light Industry Hangzhou Zhejiang 310014 China
| | - Peilong Sun
- Department of Food Science and Technology Zhejiang University of Technology Hangzhou Zhejiang 310014 China
- Key Laboratory of Food Macromolecular Resources Processing Technology Research (Zhejiang University of Technology) China National Light Industry Hangzhou Zhejiang 310014 China
| | - Xiaojun Liao
- Beijing Advanced Innovation Center for Food Nutrition and Human Health College of Food Science and Nutritional Engineering China Agricultural University Beijing 100083 China
- Beijing Key Laboratory for Food Nonthermal Processing National Engineering Research Center for Fruit & Vegetable Processing Beijing 100083 China
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Manaure E, Olivera-Fuentes C, Wilczek-Vera G, Vera J. Pitzer Equations and a Model-Free Version of the Ion Interaction Approach for the Activity of Individual Ions. Chem Eng Sci 2021. [DOI: 10.1016/j.ces.2021.116619] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 10/21/2022]
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Xiao S, Li Z, Xiong Q, Wu C, Huang J, Zhou R, Jin Y. Exploration of sodium lactate as the draw solute of forward osmosis for food processing. J FOOD ENG 2021. [DOI: 10.1016/j.jfoodeng.2020.110465] [Citation(s) in RCA: 6] [Impact Index Per Article: 2.0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 12/26/2022]
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Gulied M, Al Nouss A, Khraisheh M, AlMomani F. Modeling and simulation of fertilizer drawn forward osmosis process using Aspen Plus-MATLAB model. THE SCIENCE OF THE TOTAL ENVIRONMENT 2020; 700:134461. [PMID: 31629261 DOI: 10.1016/j.scitotenv.2019.134461] [Citation(s) in RCA: 13] [Impact Index Per Article: 3.3] [Reference Citation Analysis] [Abstract] [Key Words] [Track Full Text] [Subscribe] [Scholar Register] [Received: 07/03/2019] [Revised: 09/11/2019] [Accepted: 09/13/2019] [Indexed: 06/10/2023]
Abstract
Although experimental studies on the impact of feed (FS) and draw solutions (DS) on the forward osmosis (FO) applications are reported in literature, systematic mathematical modeling considering the dynamic change in solution properties is lacking. In this study, asymmetric FO membrane simulation model was established using Aspen Plus-MATLAB subroutines algorithm to account for the effect of concentration polarization (CP), types of FS and DS and in their properties on FO performance. The developed model was validated by comparing the simulation with experimental results. The model successfully predict the performance of FO process under wide varieties of operational conditions, FS and DS flow rates and concentrations. The model showed that the variation of MCFDS concentration had a marked effect on water flux (WF) in contrast to flow rate. The WFs obtained from seawater (SW) increased from 5.28 L/m2.h to 42.08 L/m2.h as MCFDS changes from 150 g/L to 300 g/L which corresponding to 11.66% to 45.33% of water recovery. As for synthetic aquaculture wastewater (SAWW), 9.70 L/m2.h to 37.32 L/m2.h of WFs were exhibited with the increase of MCFDS concentration from 50 g/L to 200 g/L, respectively. The effect of concentrated external CP (CECP) was found to be significant in case of SW and negligible with SAWW. Whereas, increasing MCFDS concentration increases the severity effect of dilutive internal CP (DICP). The degree of DICP depends on the solute resistivity (KD) of porous layer, which were elevated (4.22-5.88 s/m) as MCFDS concentration increases (150-300 g/L). The study demonstrated the effectiveness and suitability of the developed Aspen Plus-MATLAB model simulating the FO process.
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Affiliation(s)
- Mona Gulied
- Department of Chemical Engineering, College of Engineering, Qatar University, P.O. Box 2713, Doha, Qatar
| | - Ahmed Al Nouss
- Department of Chemical Engineering, College of Engineering, Qatar University, P.O. Box 2713, Doha, Qatar
| | - Majeda Khraisheh
- Department of Chemical Engineering, College of Engineering, Qatar University, P.O. Box 2713, Doha, Qatar.
| | - Fares AlMomani
- Department of Chemical Engineering, College of Engineering, Qatar University, P.O. Box 2713, Doha, Qatar
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