Abstract:
The effluent from a large-scale coking plant in Shandong treated by a conventional biochemical method has been used as raw water,and treated in depth by multi-medium filter-hollow fiber UF membrane-DEC adsorption resin filter-reverse osmosis membrane process. The results show that the effluent COD from DEC adsorption resin filter is less than 60 mg/L,removing rate higher than 69%,total cyanide less than 0.2 mg/L,NH3-N less than 5 mg/L, chroma less than 20 times,and stable operation cycle longer than 36 h. It can meet the discharge requirements specified in the Discharge Standard of Pollutants from Coking Chemical Industry(GB 16171-2012). DEC absorption resin filter rinsing and reclaimed water are recovered by nanofiltration(NF) membrane. The produced water can be used for DEC rinsing and resin regeneration make-up water. The RO system wastewater recovery rate is higher than 65%,stable operation cycle longer than 70 d. The produced water conductivity is less than 100 μS/cm,removing rate higher than 98%,turbidity less than 0.1 NTU,COD less than 10 mg/L. It can meet the requirements for water quality standard of circulating water,cooling water,and make-up water,specified in the Wastewater Recycling Engineering Design Specification(GB 50335-2002) and being reused in coking production.
Key words:
coking wastewater,
adsorption resin,
RO membrane,
COD,
chrome
摘要:
以山东某大型焦化厂焦化废水常规生化处理出水为原水,采用多介质过滤器-中空纤维超滤膜-DEC吸附树脂过滤器-反渗透膜工艺进行深度处理。结果表明:DEC吸附树脂过滤器出水COD小于60 mg/L,COD去除率大于69%,总氰化物 < 0.2 mg/L,NH3-N < 5 mg/L,SS < 5 mg/L,色度 < 20倍,稳定运行周期大于36 h,出水满足GB 16171-2012《炼焦化学工业污染物排放标准》排放要求。DEC吸附树脂过滤器冲洗和再生废水采用纳滤膜回收,产水用于DEC冲洗和树脂再生补水。反渗透膜处理系统水回收率大于65%,稳定运行周期大于70 d。产水电导率小于100μS/cm,浊度小于0.1 NTU,COD小于10 mg/L,满足《污水再生利用工程设计规范》(GB 50335-2002)中循环水冷却水补水水质标准要求,可回用焦化生产。
关键词:
焦化废水,
吸附树脂,
反渗透膜,
化学需氧量(COD),
色度
CLC Number:
Fu Jiangtao, Wang Li, Wang Wei, Ma Li. Advancement treatment and reuse of coking wastewater by adsorption resin[J]. INDUSTRIAL WATER TREATMENT, 2017, 37(5): 109-112.
付江涛, 王黎, 王伟, 马力. 焦化废水树脂吸附及深度处理回用[J]. 工业水处理, 2017, 37(5): 109-112.