工业水处理
工業水處理
공업수처리
INDUSTRIAL WATER TREATMENT
2009年
11期
56-58
,共3页
张晓辉%皮科武%胡林%崔建宇%曹奇光
張曉輝%皮科武%鬍林%崔建宇%曹奇光
장효휘%피과무%호림%최건우%조기광
氰酚废水%好氧工艺%厌氧工艺%混凝
氰酚廢水%好氧工藝%厭氧工藝%混凝
청분폐수%호양공예%염양공예%혼응
phenol and cyanide wastewater%aerobic process%anoxic process%flocculation
采用后继混凝沉淀的A/O工艺对含酚、氰的焦化废水进行了处理,运行结果表明:废水中酚质量浓度从287~681 mg/L降至1.0 mg/L以下,氰化物质量浓度从0.72~11.4 mg/L降至0.5 mg/L以下,完全达到了<污水综合排放标准>(GB 8978-1996)的二级排放标准;COD_(Cr)从3 879~6 378 mg/L降至116.1~184.2 mg/L.氨氮从145.6~200 mg/L降至11.64~25.26 mg/L.大多数时间达到排放标准.
採用後繼混凝沉澱的A/O工藝對含酚、氰的焦化廢水進行瞭處理,運行結果錶明:廢水中酚質量濃度從287~681 mg/L降至1.0 mg/L以下,氰化物質量濃度從0.72~11.4 mg/L降至0.5 mg/L以下,完全達到瞭<汙水綜閤排放標準>(GB 8978-1996)的二級排放標準;COD_(Cr)從3 879~6 378 mg/L降至116.1~184.2 mg/L.氨氮從145.6~200 mg/L降至11.64~25.26 mg/L.大多數時間達到排放標準.
채용후계혼응침정적A/O공예대함분、청적초화폐수진행료처리,운행결과표명:폐수중분질량농도종287~681 mg/L강지1.0 mg/L이하,청화물질량농도종0.72~11.4 mg/L강지0.5 mg/L이하,완전체도료<오수종합배방표준>(GB 8978-1996)적이급배방표준;COD_(Cr)종3 879~6 378 mg/L강지116.1~184.2 mg/L.안담종145.6~200 mg/L강지11.64~25.26 mg/L.대다수시간체도배방표준.
Aerobic/anoxic(A/O) process followed by flocculation-sedirnentation has been used for treating coking wastewater containing highly concentrated phenol and cyanide. The result indicates that the mass concentration of phenol decreases from 287-681 mg/L to 1.0 mg/L, mass concentration of cyanide decreases from 0.72-11.4 mg/L to 0.5 mg/L. The effluent quality can meet the second class criteria specified in Integrated Wastewater Discharge Standard (GB 8978-1996).The COD_(Cr) decreases from 3 879-6 378 mg/L to 116.1-184.2 mg/L, NH_4~+-N decrease from 145.6-200 mg/L to 11.64-25.26 mg/L. The effluent quality can meet the second class criteria in most time.