化工学报
化工學報
화공학보
JOURNAL OF CHEMICAL INDUSY AND ENGINEERING (CHINA)
2015年
7期
2678-2685
,共8页
李宁%苗志加%李再兴%王忠东%秦学%黄娟
李寧%苗誌加%李再興%王忠東%秦學%黃娟
리저%묘지가%리재흥%왕충동%진학%황연
生物反应器%废水%降解%生物转鼓反应器%氧转移特性%分段进水%后置反硝化
生物反應器%廢水%降解%生物轉鼓反應器%氧轉移特性%分段進水%後置反硝化
생물반응기%폐수%강해%생물전고반응기%양전이특성%분단진수%후치반초화
bioreactors%waste water%degradation%rotating drum biological contactor%oxygen transfer characteristics%step feed%post-denitrification
采用一种研制的新型生物转鼓反应器(RDBC),内部装填 MBBR 悬浮填料,通过调节浸没深度和转速可实现厌氧、缺氧、好氧等工况条件下运行,其氧总体积传质系数 KLa 可达25.87 h?1,动力效率可达228.62 g·(kW·h)?1。利用生物转鼓分段进水后置反硝化工艺处理模拟生活污水,结果表明:在进水流量6 L·h?1(HRT=18 h),好氧生物转鼓反应器浸没高度比2/3、转速8 r·min?1、DO 3.0 mg·L?1,缺氧生物转鼓反应器浸没高度比5/6、转速4 r·min?1、DO 1.0 mg·L?1,进水流量分配比3:1,进水COD、4NH+-N和TN浓度平均值分别为385.0、38.0和38.0 mg·L?1时,COD、4NH+-N和TN去除率分别达到90.4%、93.7%和80.9%,出水水质可满足我国《城镇污水处理厂污染物排放标准》(GB 18918—2002)一级A排放标准要求。
採用一種研製的新型生物轉鼓反應器(RDBC),內部裝填 MBBR 懸浮填料,通過調節浸沒深度和轉速可實現厭氧、缺氧、好氧等工況條件下運行,其氧總體積傳質繫數 KLa 可達25.87 h?1,動力效率可達228.62 g·(kW·h)?1。利用生物轉鼓分段進水後置反硝化工藝處理模擬生活汙水,結果錶明:在進水流量6 L·h?1(HRT=18 h),好氧生物轉鼓反應器浸沒高度比2/3、轉速8 r·min?1、DO 3.0 mg·L?1,缺氧生物轉鼓反應器浸沒高度比5/6、轉速4 r·min?1、DO 1.0 mg·L?1,進水流量分配比3:1,進水COD、4NH+-N和TN濃度平均值分彆為385.0、38.0和38.0 mg·L?1時,COD、4NH+-N和TN去除率分彆達到90.4%、93.7%和80.9%,齣水水質可滿足我國《城鎮汙水處理廠汙染物排放標準》(GB 18918—2002)一級A排放標準要求。
채용일충연제적신형생물전고반응기(RDBC),내부장전 MBBR 현부전료,통과조절침몰심도화전속가실현염양、결양、호양등공황조건하운행,기양총체적전질계수 KLa 가체25.87 h?1,동력효솔가체228.62 g·(kW·h)?1。이용생물전고분단진수후치반초화공예처리모의생활오수,결과표명:재진수류량6 L·h?1(HRT=18 h),호양생물전고반응기침몰고도비2/3、전속8 r·min?1、DO 3.0 mg·L?1,결양생물전고반응기침몰고도비5/6、전속4 r·min?1、DO 1.0 mg·L?1,진수류량분배비3:1,진수COD、4NH+-N화TN농도평균치분별위385.0、38.0화38.0 mg·L?1시,COD、4NH+-N화TN거제솔분별체도90.4%、93.7%화80.9%,출수수질가만족아국《성진오수처리엄오염물배방표준》(GB 18918—2002)일급A배방표준요구。
A novel rotating drum biological contactor (RDBC) was operated with MBBR packing particles inside, by which anaerobic, anoxic and aerobic operating modes can be achieved by adjusting immersion level or rotating speed. The volume oxygen transfer coefficient (KLa) and power efficiency can reach 25.87 h?1 and 228.62 g·(kW·h)?1, respectively. Synthetic domestic sewage was treated with step feed post-denitrification process. The results showed that the optimal operating conditions were immersion level 2/3, rotating speed 8 r·min?1 and DO 3.0 mg·L?1 in aerobic tank, and immersion level 5/6, rotating speed 8 r·min?1 and DO 1.0 mg·L?1 in anoxic tank. In above conditions, when the influent average COD was 385.0 mg·L?1, 4NH+-N 38.0 mg·L?1, TN 38.0 mg·L?1, total inflow 6 L·h?1 (HRT=18 h) and flow distribution ratio 3:1, the remove rate of effluent COD, 4NH+-N and TN can reach 90.4%, 93.7% and 80.9%, respectively, which can meet the first level A discharge standards in China (GB18918—2002).