A hybrid reverse osmosis/adsorption desalination plant for irrigation and drinking water

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The hybridisation of brackish water reverse osmosis (BWRO) desalination technology and an adsorption cycle (AD) are considered in this work as a means of producing large quantities of a) water for irrigation and; b) high quality water for domestic use. The RO process and the AD cycle are represented as numerical models and have been optimised to produce fresh water and cooling. An existing RO plant can be retrofitted to become an RO-AD process to improve its specific energy consumption and simultaneously produce a cooling effect which can be exploited for local process cooling or air conditioning. A pressure exchanger (PX) and AD are combined to recover the reject from the RO, resulting in reduction in power consumption. The hybridised RO-AD desalination processes can be considered as the optimum solution for rural areas due to its capability for the production of water for irrigation and drinking as well as cooling for air-conditioning. Nevertheless, the temperature and feed salinity may negatively effect on RO production, with the AD cycle producing more than 6 m3/tonne s.g of drinking water (<15 ppm) at 85 °C, additionally the AD evaporator is not effected significantly by salinity. The proposed plant could produce 24,000 m3/day for irrigation and 6.3 m3/tonne s.g for drinking as well as 75 RTon/tonne s.g. Another interesting finding was that the minimum specific energy for the combined RO-PX-AD plant with a capacity of 24,000 m3/day is 0.8 kWh/m3 at RO recovery = 45%. The small-scale combined system was also examined to produce 2000 m3/day and cost of different configurations was estimated as well. The results showed that the cost of the combined RO-AD system is the lowest, 0.44 £/m3 compares with other RO configurations.

Highlights

  • Despite three quarters of the earth surface being covered by water, 97.5% of the water on the earth surface is seawater with TDS higher than 35,000 ppm

  • The Reverse Osmosis (RO)-adsorption cycle (AD) combination can simultaneously produce a cooling effect which can be exploited for process cooling or air conditioning while retrofitting the existing RO plant to improve its specific energy consumption

  • A pressure exchanger (PX) and AD are combined to recover the reject from RO, resulting in reduction in power consumption

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Summary

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Despite three quarters of the earth surface being covered by water, 97.5% of the water on the earth surface is seawater with TDS higher than 35,000 ppm. The best and most practical desalination plants offer a cost-effective solution for removing suspended salt or solid from sea or brackish water to produce potable water while being environmentally friendly. The number of Reverse Osmosis (RO) processes in major desalination plants have expanded considerably in recent times [6]. The RO process is recommended by Al-Karaghouli and Kazmerski [10] to address a brackish water, and is considered more cost effective economically when TDS is > 5000 ppm. M/s Permeability coefficient m/s-Pa Pressure difference, Pa Water diffusivity, m2/s Water concentration, mol/m3 Water molar volume, m3. Pa Feed flow rate, m3/day Specific energy consumption, kWh/m3 Osmotic pressure difference, Pa Rejected flow rate, m3/day Permeate flow rate, m3/day. Pa Concentration of feed water, mol/m3 Uptake by adsorbent material, kg kg

E Epump A CrExpand/Collapse icon
15 Dsoe RT RP2Expand/Collapse icon
A numerical model for RO systemExpand/Collapse icon
The adsorption systemExpand/Collapse icon
Numerical model of combined RO-AD systemExpand/Collapse icon
ConclusionsExpand/Collapse icon
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CitationsShowing 10 of 67 papers
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This paper examines the viability of introducing solar thermal desalination technology as a means to supplement existing water production methods in the Republic of South Africa (RSA). The study provides an overview of the current state of desalination technology in the country. A key aspect of this study involves comparing the RSA with the Middle East and North Africa (MENA) region, using publicly available studies and reports. The focus of this comparison is to highlight the potential implementation of large-scale solar desalination in the RSA by evaluating the respective resources and environmental data that directly impact the input and output of a thermal desalination system. The study comparatively analyzes the environmental conditions and seawater salinity of the RSA and the MENA region. The RSA receives a higher solar irradiation range of 4.5–6.5 kWh/m2, whereas the MENA region experiences a range of 3.5–5.5 kWh/m2. Additionally, the salinity of the RSA’s seawater ranges between 35 and 35.5 parts per thousand, which is lower than the MENA region’s range of 36–40 parts per thousand. The study also reviews and proposes the adoption of an emerging thermal desalination method that has been successfully tested in the MENA region and other countries, based on its performance.

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Assessment of fixed, single-axis, and dual-axis photovoltaic systems applied to a reverse osmosis desalination process in northwest Mexico
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Toward a Sustainable Decentralized Water Supply: Review of Adsorption Desorption Desalination (ADD) and Current Technologies: Saudi Arabia (SA) as a Case Study
  • Apr 14, 2020
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Several regions are confronting a severe scarcity of fresh water due to the gap between supply and demand. They strive to bridge that gap by depleting nonrenewable water aquifers and expanding centralized energy-intensive desalination technologies. Continuing to adopt the same unsustainable approach could deplete the water aquifers and increase the consumption of fossil fuel and the ecological impact on air, water, and land. However, the traditional paradigm of centralized desalination systems could be shifted by increasing the utilization of renewable distributed generation, which can be coupled with emerging desalination technology such as adsorption desorption desalination (ADD), which has autonomous and resilient attributes that can contribute to the sustainability of decentralized fresh water supply in the future. In this work, three commercialized desalination technologies were reviewed and compared with emerging ones to explore the most economically and environmentally efficient systems within the context of decentralized water production. The well-known configurations of ADD were evaluated and compared with sea water reverse osmosis (SWRO), which is recognized as the principal commercialized desalination technology worldwide. The quantitative case study methodology was used by investigating four centralized seawater desalination plants in Saudi Arabia (SA) with their associated pipeline systems from the energy consumption point of view to determine the applicability of implementing ADD technology in SA and similar arid areas. The study reveals that adopting decentralized ADD technology coupled with renewable energy sources could reduce the specific energy consumption from 4 kWh/m3 to less than 1.38 kWh/m3. Combining reduced energy consumption from desalination plants and elimination of supply pipelines could potentially result in a significant reduction in energy consumption and carbon emissions. Finally, the study may be useful for researchers working on enhancing ADD processes, as well as technology users who would like to implement the most efficient ADD configurations. Additionally, it may initiate a direction of utilizing the results of original critical reviews as a methodology to develop the applied technologies.

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Reverse Osmosis Modeling Study of Lead and Arsenic Removal from Drinking Water in Tarija and La Paz, Bolivia
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In areas with inadequate improved water supply, irrigation water serves as an alternative water source for domestic uses in addition to its prime purpose of agricultural production. This increased water availability for the household can generate positive hygiene and health impacts, but poor irrigation water quality can be a source of domestic water contamination and can be harmful to human health. Using primary household survey data from two rural districts of Ethiopia, this study seeks to disentangle these opposite effects: the results show that irrigation is associated with poor household water quality (adjusted odds ratio 1.68, 95%, CI 1.07–2.66) and a lower risk of diarrheal disease (adjusted odds ratio 2.07, 95%, CI 1.24–3.44). Domestic use of irrigation water, however, does not further degrade the microbial quality of household water. On the other hand, the domestic use of irrigation water reduces the burden of water collection (p < 0.01). Providing education and training programs to foster behavioral change towards sustainable improvements in water resource management, such as the safe use of irrigation water for domestic purposes through appropriate point-of-use water treatment, would be crucial to maximize the benefits of the domestic use of irrigation water and to minimize adverse environmental and health risks.

  • Preprint Article
  • 10.5194/egusphere-egu25-673
Evaluation of Wheat Yield and Water Productivity for Drip and Flood Irrigated Treatments Based on Maximum Allowable Deficit, Crop Evapotranspiration, and Conventional Practices
  • Apr 1, 2025
  • Ghanshyam Giri + 2 more

Assessing grain yield (GY), irrigation water productivity (IWP), and irrigation crop water use efficiency (ICWUE) provides valuable insights into optimizing irrigation water use while maintaining crop yield. For this purpose, irrigation is varied either in crop phenological stages or based on the maximum allowable depletion/deficit (MAD) or crop evapotranspiration (ETC) or ratio of irrigation water to cumulative pan evaporation. No study has been identified that analyzed and compared GY, IWP, and ICWUE for drip and flood irrigated treatments based on MAD, ETC, and conventional practices for wheat. This study analyzed and compared GY, IWP, and ICWUE among drip-irrigated (DI) and flood-irrigated (FI) treatments based on MAD, ETC, and conventional practices by conducting field experiments for the wheat crop during 2023-24. The treatments were 50% MAD (DI), 50% MAD (FI), 100% ETC (DI), 80% ETC (DI), 80% ETC (FI), 60% ETC (DI), 40% ETC (DI), and conventional practice replication (referred to as farmers’ field replication). Compared to farmers’ field replication, GY increased by 30.5%, 16.9%, 23.2%, 15.6%, 9.6%, and 0.4% in 50% MAD (DI), 50% MAD (FI), 100% ETC (DI), 80% ETC (DI), 80% ETC (FI), 60% ETC (DI) treatments, respectively. Furthermore, compared to the farmers’ field replication, the irrigation amount in 50% MAD (DI), 50% MAD (FI), 100% ETC (DI), 80% ETC (DI), 80% ETC (FI), 60% ETC (DI), and 40% ETC (DI) reduced by 16.4%, 7.9%, 18.3%, 36.8%, 33.9%, 52.4%, and 65.5%, respectively. IWP values in 50% MAD (DI), 50% MAD (FI), 100% ETC (DI), 80% ETC (DI), 80% ETC (FI), 60% ETC (DI), 40% ETC (DI), and farmers’ field replication were 29, 23.6, 28, 34, 39.2, 50.3, and 18.6 kg/ha-mm, respectively. For the same level of irrigation, IWP and ICWUE were higher in DI treatments compared to FI treatments. The values of IWP and ICWUE in 50% MAD (DI) increased by 23.1% and 41.5%, respectively compared to 50% MAD (FI). Similarly, IWP and ICWUE in 80% ETC (DI) increased by 20% compared to 80% ETC (FI). Among the treatments, the 50% MAD (DI) and 100% ETC (DI) produced significantly higher GY of 5336.2 kg/ha and 5036.3 kg/ha, respectively. Between these two treatments, GY was higher in 50% MAD (DI). This can be attributed to the MAD in the 100% ETC (DI) treatment reaching 67% during the high-water demand growth stage, which exceeded the MAD level in the 50% MAD (DI) treatment. This study suggested that with the priority to produce the higher grain yield and save irrigation water (16.4 to 18.3%) as compared to existing irrigation practices followed by the farmers in the study region, 50% MAD (DI) or 100% ETC (DI) treatment must be employed. With the priority of saving the highest irrigation amount (52.4 %) without compensating for the GY, 60% ETC (DI) can be utilized by the farmers in the local region.

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