Abstract

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

Read more

Summary

Introduction

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 Cr
15 Dsoe RT RP2
A numerical model for RO system
The adsorption system
Numerical model of combined RO-AD system
Conclusions

Talk to us

Join us for a 30 min session where you can share your feedback and ask us any queries you have

Schedule a call

Disclaimer: All third-party content on this website/platform is and will remain the property of their respective owners and is provided on "as is" basis without any warranties, express or implied. Use of third-party content does not indicate any affiliation, sponsorship with or endorsement by them. Any references to third-party content is to identify the corresponding services and shall be considered fair use under The CopyrightLaw.