Chromium removal by a bipolar electro-chemical precipitation process
Удаление хрома методом биполярного электрохимического осаждения
1996-01-01
SCID: 54.1/4j27wzbm
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X-ray fluorescence and X-ray diffractionbipolar electro-chemical precipitationchromium removalelectroplating wastewatermaghemite and chromite sludge
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Abstract (AI)
This research was conducted in laboratory to investigate an alternative for Cr removal from an electroplating wastewater using the electro-chemical precipitation (ECP) process. The ECP unit, operated in the bipolar mode, had six steel plates including the anode and cathode and was supplied with DC power. The electroplating wastewater used in the experiments contained Cr concentrations in the range of 570-2100 mg/l. The Cr removal efficiencies in the bipolar ECP units were higher than 99% and the Cr concentrations in the treated effluent were less than 0.5 mg/l. The acceptable conditions of the bipolar ECP unit treating the electroplating wastewater were found to be: I - 1.0 amp (or i - 6.70 amp/m2) and initial pH (pHi) of 4.5. At these acceptable conditions, the electric power and steel electrode plate consumptions were 20.0 kWh/m3 and 1.1-2.8 kg-Fe/kg Cr removed, respectively. X-ray fluorescence and X-ray diffractometric analysis performed on the precipitated sludge revealed the main compounds to be maghemite (Fe2O3) and chromite (FeCr2O4). The percent Fe2O3 and FeCr2O4 contents of the dried ECP sludge were 68% and 25%, respectively. From the mass balance analysis, the percent of Cr removal by precipitation in the ECP unit and adsorption on the ECP sludge were 85.1 and 14.8%, respectively.
Key Findings
1
A bipolar electro-chemical precipitation unit with six steel plates removed more than 99% of chromium from electroplating wastewater.
2
Acceptable operating conditions were 1.0 amp (6.70 amp/m²) current and initial pH 4.5.
3
For influent chromium concentrations of 570–2100 mg/l, treated effluent chromium concentrations remained below 0.5 mg/l.
4
The precipitated sludge mainly contained maghemite (68% Fe₂O₃) and chromite (25% FeCr₂O₄); chromium removal occurred through precipitation (85.1%) and sludge adsorption (14.8%).
5
Under these conditions, electricity consumption was 20.0 kWh/m³ and steel consumption was 1.1–2.8 kg-Fe per kg chromium removed.
Research Object
Chromium-containing electroplating wastewater treated in a bipolar electrochemical precipitation unit
Research Subject
Cr removal efficiency, operating conditions, energy and steel-electrode consumption, precipitated-sludge composition, and removal mechanisms by precipitation and adsorption
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1996-01-01
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