摘要抗生素废水的特点是COD、BOD、SS（悬浮物）含量较高，且水质成

摘要
抗生素废水的特点是COD、BOD、SS（悬浮物）含量较高，且水质成分复杂，因此处理起来较为困难。
本设计为2000m3/d抗生素废水处理工程设计，处理水量为1200m3/d，PH为7.5，COD为20000mg/L，BOD为10000mg/L，油为300mg/L，SS为500mg/L，SO42-为150mg/L的溶媒废水和水量为800m3/d，PH为7，COD为2200mg/L，BOD为800mg/L，油为0mg/L，SS为900mg/L，SO42-为0mg/L的板框废水。根据其水质特征和污水特点，经过方案比较后确定采用“UASB+氧化沟+曝气生物滤池工艺”。
工艺流程是：平流式隔油池——UASB——调节池——平流式初沉池——水解酸化池——氧化沟——竖流式二沉池——曝气生物滤池，经本工艺处理后，排放水质达到《发酵类制药工业水污染物排放标准》（GB21903-2008）的标准。
根据主体工艺，通过详细的设计计算确定各处理构筑物的尺寸和布置形式，并通过AutoCAD完成各主要构筑物的平剖面图的绘制，对各附属设备进行选型。然后开始高程计算并完成了高程的CAD绘制。最后进行经济预算，完成设计。
关键词：抗生素废水 UASB 氧化沟 曝气生物滤池

結果 (英文) 1:

SummaryAntibiotics waste water characteristics of the COD, BOD, SS (suspended solids) content is high, and water quality components, thus more difficult to deal with.The design for the 2000m3/d antibiotic wastewater treatment engineering, 1200m3/d,PH for 7.5,COD for 20000mg/L,BOD for 10000mg/L of water, the solvent oil for 300mg/L,SS for 500mg/L,SO42-for 150mg/L waste water and 800m3/d,PH for 7,COD for 2200mg/L,BOD for 800mg/L of water and oil 0mg/L, SS-900mg/L,SO42--0mg/L frame of wastewater. According to the water quality and wastewater characteristics, after a comparison using "+ Biological Aerated Filter technology of UASB+ oxidation ditch".Process are: flat grease--UASB--adjust the tank – beginning of horizontal-flow sedimentation-hydrolytic acidification-oxidation ditch-pool-vertical-flow secondary sedimentation tank – Biological Aerated Filter by this process, discharge water quality of the fermented water discharge standards of pollutants for pharmaceutical industry (GB21903-2008) standard.According to the main process, through detailed design calculations to determine the size and layout of the structure and AutoCAD to complete the main structure of flat profile drawing, selection of subsidiary equipment. Then start elevation calculation and CAD drawing of the finished height. Final budget to complete the design.Key words: antibiotic wastewater by UASB oxidation ditch in Biological Aerated Filter

結果 (英文) 3:

abstractAntibiotic wastewater is characterized by high content of COD, BOD and SS (suspended matter), and the water quality is complex, so it is difficult to deal with.The design / D of antibiotic wastewater treatment engineering design, the water treatment for 1200m3/d, pH is 7.5, cod is 20000mg /, BOD is 10000mg / L, the oil is 300mg / L, SS is 500mg / L, SO42 - 150mg / L solvent waste water and water for 800m3 / D, pH is 7, cod is 2 200mg, BOD is 800 mg / L, the oil is mg / L SS 900MG / L, SO42 - wastewater for mg / L of the frame. According to the characteristics of water quality and sewage, after the comparison of the scheme, the UASB+ oxidation ditch and biological aerated filter process was adopted ".Process: advection oil separation tank - UASB - regulation pool -- flat flow primary sedimentation tank, pool acid hydrolysis oxidation ditch, vertical flow type secondary sedimentation tank -- biological aerated filter, after this process, discharge water quality reached the fermentation pharmaceutical industrial water pollutant discharge standard "(GB21903-2008) standard.According to the main process, through the detailed design calculation to determine the size and layout of each processing structure, and through the AutoCAD to complete the main structures of the flat profile drawing, the various ancillary equipment selection. Then start elevation calculation and completed the elevation of CAD rendering. At the end of the budget, the completion of the design.Key words: Antibiotic Wastewater UASB oxidation ditch biological aerated filter