Date of Graduation

12-2014

Document Type

Thesis

Degree Name

Bachelor of Science in Chemical Engineering

Degree Level

Undergraduate

Department

Chemical Engineering

Advisor/Mentor

Penney, William Roy

Committee Member/Reader

Hestekin, Jamie A

Abstract

In arid regions of the United States potable water is a valuable resource and is sometimes produced using energy intensive processes by removing salts from brackish water. Task 4 provides a solar option for producing potable water from brackish water; in competing in Task 4, H2OGS has developed a simple, cost effective solar desalination process to provide these regions with necessary, potable water. H2OGS’ design takes into account WERC requirements, including cost, energy usage, worker safety, and easily obtained materials. U.S. government regulatory requirements are also taken into account as the proposed location for this process is Alamogordo, New Mexico. H2OGS’ design consists of a thin plate-type solar evaporator and also a thin plate-type condenser. Black-painted corrugated galvanized steel panels were used to construct the evaporator and condenser. The black-painted evaporator panels are protected from atmospheric convection by a six mil polyethylene film, commonly used for greenhouses. Radiant energy from the sun passes through the polyethylene film and is absorbed by the black-painted panel. Brine is sprayed onto the back side of the panel via a nozzle located at the top of the unit. As the brine runs down the evaporating face, it is evaporated. The warmed, evaporated brine gravity drains to an insulated holding tank from which it moves to the next evaporating stage to be further concentrated. The evaporated water is condensed on additional corrugated steel plates located opposite the evaporating face. Because this plate is shielded from direct sunlight, the evaporated water is condensed by convection to the atmosphere and drained into a holding trough at the bottom of the unit where it is pumped to a potable water storage tank. The brine effluent that remains after leaving the final still unit is transported to a solar pond where salts crystalize and are removed by manual raking from the evaporation basin. This basin is designed to be 3’ deep by 45’ wide by 180’ long and will evaporate the remaining 20% of the bring effluent and allow for crystallization and recovery of the salts. After air drying, the salts are sold.

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