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Biological removal of cyanide compounds from electroplating wastewater (EPWW) by sequencing batch reactor (SBR) system

机译:通过顺序批处理反应器(SBR)系统从电镀废水(EPWW)中生物去除氰化物

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摘要

Biological treatment system especially, sequencing batch reactor (SBR) system could not be applied to treat the raw electroplating wastewater (EPWW) due to the low organic matter concentration of 10 ± 3 mg-BOD_5/L and toxic of high cyanide concentration of 23.0 ± 2.2 mg-CN/L. However, EPWW could be used as the nitrogen source for the bio-sludge of SBR system. And 10% of EPWW (the final cyanide concentration of 2.3 ± 0.2 mg/L) was most suitable to supplement into the wastewater as the nitrogen source. SBR system showed the highest COD, BOD_5, TKN and cyanide removal efficiencies of 79 ± 2%, 85 ± 3%, 49.0 ± 2.1% and 97.7 ± 0.7%, respectively with 4-times diluted Thai-rice noodle wastewater (TRNWW) containing 10% EPWW and 138 mg/L NH_4Cl (BOD_5: TN of 100:10) at SRT of 72 ± 13 days (under organic and cyanide loadings of 0.40 kg-BOD_5/m~3 d and 0.0023 kg-CN/m~3 d, respectively). However, the effluent ammonia was still high of 22.6 ± 0.4 mg-N/L while the effluent nitrate and nitrite was only 9.9 ± 0.4 and 1.2 ± 0.9 mg-N/L, respectively. And SVI and effluent SS of the system were higher than 95 and 75 mg/L, respectively.
机译:尤其是生物处理系统,由于有机物浓度低至10±3 mg-BOD_5 / L,且氰化物浓度高至23.0±,因此无法应用于顺序电镀反应器(SBR)系统来处理原电镀废水(EPWW)。 2.2 mg-CN / L。但是,EPWW可以用作SBR系统生物污泥的氮源。 10%的EPWW(最终氰化物浓度为2.3±0.2 mg / L)最适合作为氮源添加到废水中。 SBR系统显示出最高的COD,BOD_5,TKN和氰化物去除效率分别为79±2%,85±3%,49.0±2.1%和97.7±0.7%,其中含有4倍稀释的泰国米粉废水(TRNWW) 10%EPWW和138 mg / L NH_4Cl(BOD_5:TN为100:10),SRT为72±13天(在有机和氰化物负载量为0.40 kg-BOD_5 / m〜3 d和0.0023 kg-CN / m〜3的情况下) d)。但是,氨的出水量仍然很高,为22.6±0.4 mg-N / L,而硝酸盐和亚硝酸盐的出水量分别仅为9.9±0.4和1.2±0.9 mg-N / L。系统的SVI和废水SS分别高于95和75 mg / L。

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