Provision of Desalinated Irrigation Water by the Desalination of Groundwater Abstracted from a Saline Aquifer

Globally, about 54 million ha of cropland are irrigated with saline water. Globally, the soils associated with about 1 billion ha are affected by salinization. A small decrease in irrigation water salinity (and soil salinity) can result in a disproportionally large increase in crop yield. This study...

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Main Author: David D. J. Antia
Format: Article
Language:English
Published: MDPI AG 2022-07-01
Series:Hydrology
Subjects:
Online Access:https://www.mdpi.com/2306-5338/9/7/128
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author David D. J. Antia
author_facet David D. J. Antia
author_sort David D. J. Antia
collection DOAJ
description Globally, about 54 million ha of cropland are irrigated with saline water. Globally, the soils associated with about 1 billion ha are affected by salinization. A small decrease in irrigation water salinity (and soil salinity) can result in a disproportionally large increase in crop yield. This study uses a zero-valent iron desalination reactor to effect surface processing of ground water, obtained from an aquifer, to partially desalinate the water. The product water can be used for irrigation, or it can be reinjected into a saline aquifer, to dilute the aquifer water salinity (as part of an aquifer water quality management program), or it can be injected as low-salinity water into an aquifer to provide a recharge barrier to protect against seawater intrusion. The saline water used in this study is processed in a batch flow, bubble column, static bed, diffusion reactor train (0.24 m<sup>3</sup>), with a processing capacity of 1.7–1.9 m<sup>3</sup> d<sup>−1</sup> and a processing duration of 3 h. The reactor contained 0.4 kg Fe<sup>0</sup>. A total of 70 batches of saline water (average 6.9 g NaCl L<sup>−1</sup>; range: 2.66 to 30.5 g NaCl L<sup>−1</sup>) were processed sequentially using a single Fe<sup>0</sup> charge, without loss of activity. The average desalination was 24.5%. The reactor used a catalytic pressure swing adsorption–desorption process. The trial results were analysed with respect to Na<sup>+</sup> ion removal, Cl<sup>−</sup> ion removal, and the impact of adding trains. The reactor train was then repurposed, using n-Fe<sup>0</sup> and emulsified m-Fe<sup>0</sup>, to establish the impact of reducing particle size on the amount of desalination, and the amount of n-Fe<sup>0</sup> required to achieve a specific desalination level.
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spelling doaj.art-8778103076404eb09446f48af07af2ce2023-11-30T21:02:11ZengMDPI AGHydrology2306-53382022-07-019712810.3390/hydrology9070128Provision of Desalinated Irrigation Water by the Desalination of Groundwater Abstracted from a Saline AquiferDavid D. J. Antia0DCA Consultants Ltd., The Bungalow, Castleton Farm, Falkirk, Stirlingshire FK2 8SD, UKGlobally, about 54 million ha of cropland are irrigated with saline water. Globally, the soils associated with about 1 billion ha are affected by salinization. A small decrease in irrigation water salinity (and soil salinity) can result in a disproportionally large increase in crop yield. This study uses a zero-valent iron desalination reactor to effect surface processing of ground water, obtained from an aquifer, to partially desalinate the water. The product water can be used for irrigation, or it can be reinjected into a saline aquifer, to dilute the aquifer water salinity (as part of an aquifer water quality management program), or it can be injected as low-salinity water into an aquifer to provide a recharge barrier to protect against seawater intrusion. The saline water used in this study is processed in a batch flow, bubble column, static bed, diffusion reactor train (0.24 m<sup>3</sup>), with a processing capacity of 1.7–1.9 m<sup>3</sup> d<sup>−1</sup> and a processing duration of 3 h. The reactor contained 0.4 kg Fe<sup>0</sup>. A total of 70 batches of saline water (average 6.9 g NaCl L<sup>−1</sup>; range: 2.66 to 30.5 g NaCl L<sup>−1</sup>) were processed sequentially using a single Fe<sup>0</sup> charge, without loss of activity. The average desalination was 24.5%. The reactor used a catalytic pressure swing adsorption–desorption process. The trial results were analysed with respect to Na<sup>+</sup> ion removal, Cl<sup>−</sup> ion removal, and the impact of adding trains. The reactor train was then repurposed, using n-Fe<sup>0</sup> and emulsified m-Fe<sup>0</sup>, to establish the impact of reducing particle size on the amount of desalination, and the amount of n-Fe<sup>0</sup> required to achieve a specific desalination level.https://www.mdpi.com/2306-5338/9/7/128catalysischloride ion removalNaClpartial desalinationpressure swing adsorptionsaline irrigation
spellingShingle David D. J. Antia
Provision of Desalinated Irrigation Water by the Desalination of Groundwater Abstracted from a Saline Aquifer
Hydrology
catalysis
chloride ion removal
NaCl
partial desalination
pressure swing adsorption
saline irrigation
title Provision of Desalinated Irrigation Water by the Desalination of Groundwater Abstracted from a Saline Aquifer
title_full Provision of Desalinated Irrigation Water by the Desalination of Groundwater Abstracted from a Saline Aquifer
title_fullStr Provision of Desalinated Irrigation Water by the Desalination of Groundwater Abstracted from a Saline Aquifer
title_full_unstemmed Provision of Desalinated Irrigation Water by the Desalination of Groundwater Abstracted from a Saline Aquifer
title_short Provision of Desalinated Irrigation Water by the Desalination of Groundwater Abstracted from a Saline Aquifer
title_sort provision of desalinated irrigation water by the desalination of groundwater abstracted from a saline aquifer
topic catalysis
chloride ion removal
NaCl
partial desalination
pressure swing adsorption
saline irrigation
url https://www.mdpi.com/2306-5338/9/7/128
work_keys_str_mv AT daviddjantia provisionofdesalinatedirrigationwaterbythedesalinationofgroundwaterabstractedfromasalineaquifer