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Chemical pre-treatment of waste water from the Morcinek Mine in Poland

Technical Report ·
DOI:https://doi.org/10.2172/10177952· OSTI ID:10177952
This report presents a treatment strategy for brine that is recovered from the Morcinek mine near the city of Kartowice in Upper Silesia, Poland. The purpose of the study is to provide sufficient chemical composition and solubility data to permit selection of equipment for a pilot scale waste water processing plant. The report delineates: (1) the pre-treatment steps necessary before the brine is delivered to a reverse osmosis unit; (2) the composition of the brine solution at various stages in the pretreatment process and during the reverse osmosis step; (3) the types and amounts of chemicals that need to be added to the brine during pre-treatment. Analysis of the composition of the brine slurry from the submerged combustion evaporator that follows the reverse osmosis unit and the composition of brine elements that might be carried into the exhaust stack of the evaporator will be dealt with later. The pretreatment process will consist of four steps: (1) aeration and addition of sodium carbonate, (2) multimedia filtration, (3) addition of hydrochloric acid, and (4) ultrafiltration. On the basis of one m{sup 3} of the brine that has a density of 1.03 g/cm{sup 3}, approximately 800 grams (1.7 lbs.) of sodium carbonate monohydrate (Na{sub 2}CO{sub 3}{center_dot}H{sub 2}O) and 60 grams (0.12 lbs.) of concentrated hydrochloric acid (HCI) will need to be added to the brine during pre-treatment. The goal of the pre-treatment is to produce a fluid that is always undersaturated with respect to all mineral phases. However, only the minimum amount of pre-treatment chemicals should be added in order to minimize costs. Therefore the overall goal is to generate a fluid that approaches but does not exceed saturation at the end of the reverse osmosis process. The suggested amounts of chemicals reported here are therefore the minimum amounts that need to be added during pre-treatment to keep all salts in solution during the reverse osmosis process.
Research Organization:
Lawrence Livermore National Lab., CA (United States)
Sponsoring Organization:
USDOE, Washington, DC (United States)
DOE Contract Number:
W-7405-ENG-48
OSTI ID:
10177952
Report Number(s):
UCRL-ID--117927; ON: DE94017937
Country of Publication:
United States
Language:
English

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