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Title: Recovery of mineral salts and potable water from desalting plant effluents by evaporation. Part II. Proposed simulation system for salt recovery

Journal Article · · Separation Science and Technology; (USA)
; ; ;  [1]
  1. King Fahd Univ. of Petroleum and Minerals, Dhahran (Saudi Arabia)

Salt recovery from rejected brines of the Al-Khobar Water Desalination Plant, Saudi Arabia, is studied through the simulation of a modified MSF system. Two phases of concentrations are planned: Phase I will concentrate the main effluent from 6.4 wt% total salt to 28.8%, while Phase II will use the effluents from Phase I as a feed to undergo further evaporation and cooling. NaCl and water are produced throughout this phase, while the end residue product will be essentially MgCl{sub 2}, since it is the most soluble. A mathematical model is developed and used to perform stage-to-stage material and heat balance calculations. Concentrations of NaCl and MgCl{sub 2} in the streams entering and leaving a stage are determined by using the solubility correlation developed in Part I. Simulation results show that by using 5,210 tons/h brine as a feed for Phase I, they can recover 4,430 tons/h fresh water, 277 tons/h NaCl, and 502 tons/h bittern (in which the ratio of MgCl{sub 2}/NaCl is increased to 12) as the very final products of the integrated scheme. This bittern provides 30 tons/h MgCl{sub 2} as an end product.

OSTI ID:
6278940
Journal Information:
Separation Science and Technology; (USA), Vol. 25:4, Issue 4; ISSN 0149-6395
Country of Publication:
United States
Language:
English