TY - JOUR
T1 - Evaluation of the rotational speed and carbon source on the biological removal of free cyanide present on gold mine wastewater, using a rotating biological contactor
AU - Guamán Guadalima, Mónica Paola
AU - Nieto Monteros, Diego Alejandro
N1 - Publisher Copyright:
© 2018 Elsevier Ltd
PY - 2018/6
Y1 - 2018/6
N2 - Wastewater streams generated during the leaching process of precious metals recovery (e.g. gold, silver) contain high concentrations of toxic compounds, being free cyanide (CN−) one of the most important among them. Free cyanide is a toxic compound that affects cellular respiration and causes irreversible environment problems. Thus, effective wastewater treatment processes should be applied to reduce CN− without producing other contaminants. This study evaluated the effect of rotational speed and carbon source on the biological removal of CN− present on gold mine wastewater, using a rotating biological contactor (RBC). A factorial design (23) was developed by triplicate (N = 24) to evaluate: carbon source concentration (commercial sugar cane, 99% sucrose), free cyanide concentration (CN−), and rotational speed (ω) on the biological removal of free cyanide (%B.R.). The bioreactor worked on continuous system under the following conditions: VRBC = 4.2L, FI = 0.42L/h (gold mine wastewater at 10 or 300 mg CN−/L, liquid culture media with or without carbon source, final pH = 10.5 ± 0.5), HRT = 10 h, and ω = 5 or 10 rpm. According to the factorial analysis: free cyanide concentration ([CN−]i), carbon source concentration ([FC]i), and rotational speed (ω) affected significantly (p < 0.05) during the biological removal of CN−. Furthermore, the highest biological removal percentage (96.89%) was achieved when the RBC worked under the following conditions: [CN−]i = 300 mg/L, [FC]i = 3.8 g/L, and ω = 5 rpm; even though dissolved oxygen reached levels below 2 mg/L. Thus, biological removal increased when free cyanide and carbon source concentrations were at their highest level 300 mg/L and 3.8 g/L, respectively; however rotational speed (10 rpm) diminished the bioprocess.
AB - Wastewater streams generated during the leaching process of precious metals recovery (e.g. gold, silver) contain high concentrations of toxic compounds, being free cyanide (CN−) one of the most important among them. Free cyanide is a toxic compound that affects cellular respiration and causes irreversible environment problems. Thus, effective wastewater treatment processes should be applied to reduce CN− without producing other contaminants. This study evaluated the effect of rotational speed and carbon source on the biological removal of CN− present on gold mine wastewater, using a rotating biological contactor (RBC). A factorial design (23) was developed by triplicate (N = 24) to evaluate: carbon source concentration (commercial sugar cane, 99% sucrose), free cyanide concentration (CN−), and rotational speed (ω) on the biological removal of free cyanide (%B.R.). The bioreactor worked on continuous system under the following conditions: VRBC = 4.2L, FI = 0.42L/h (gold mine wastewater at 10 or 300 mg CN−/L, liquid culture media with or without carbon source, final pH = 10.5 ± 0.5), HRT = 10 h, and ω = 5 or 10 rpm. According to the factorial analysis: free cyanide concentration ([CN−]i), carbon source concentration ([FC]i), and rotational speed (ω) affected significantly (p < 0.05) during the biological removal of CN−. Furthermore, the highest biological removal percentage (96.89%) was achieved when the RBC worked under the following conditions: [CN−]i = 300 mg/L, [FC]i = 3.8 g/L, and ω = 5 rpm; even though dissolved oxygen reached levels below 2 mg/L. Thus, biological removal increased when free cyanide and carbon source concentrations were at their highest level 300 mg/L and 3.8 g/L, respectively; however rotational speed (10 rpm) diminished the bioprocess.
KW - Biological removal
KW - Dissolved oxygen
KW - Free cyanide
KW - Rotating biological contactor
KW - Sucrose
UR - http://www.scopus.com/inward/record.url?scp=85044159381&partnerID=8YFLogxK
U2 - 10.1016/j.jwpe.2018.03.008
DO - 10.1016/j.jwpe.2018.03.008
M3 - Artículo
AN - SCOPUS:85044159381
SN - 2214-7144
VL - 23
SP - 84
EP - 90
JO - Journal of Water Process Engineering
JF - Journal of Water Process Engineering
ER -