工业安全与环保
工業安全與環保
공업안전여배보
INDUSTRIAL SAFETY AND ENVIRONMENTAL PROTECTION
2015年
1期
1-3
,共3页
EGSB%高浓度废水%有机负荷%VFA
EGSB%高濃度廢水%有機負荷%VFA
EGSB%고농도폐수%유궤부하%VFA
EGSB%high concentration wastewater%organic loading rate%VFA
在EGSB反应器中添加PVA凝胶颗粒处理高浓度废水。保持进水量一定,逐渐增加反应器内进水COD质量浓度,即2.2~12.9g/L,相应的有机负荷率是5.4~51.79g/(L?d)。观察反应器的运行情况,确定有机负荷率在30 g/(L?d )时,COD去除率最高可以达到96%。增大负荷,同时保证进水的pH值是7.0,观察反应器出水pH值与VFA的变化,确定适宜产甲烷菌生长的环境。从收集到的气体体积来看,在一定的范围内,气体产率随着进水负荷的提高而增加,当负荷达到30 g/(L?d )时,气体体积可达38 L (实验最大值)。
在EGSB反應器中添加PVA凝膠顆粒處理高濃度廢水。保持進水量一定,逐漸增加反應器內進水COD質量濃度,即2.2~12.9g/L,相應的有機負荷率是5.4~51.79g/(L?d)。觀察反應器的運行情況,確定有機負荷率在30 g/(L?d )時,COD去除率最高可以達到96%。增大負荷,同時保證進水的pH值是7.0,觀察反應器齣水pH值與VFA的變化,確定適宜產甲烷菌生長的環境。從收集到的氣體體積來看,在一定的範圍內,氣體產率隨著進水負荷的提高而增加,噹負荷達到30 g/(L?d )時,氣體體積可達38 L (實驗最大值)。
재EGSB반응기중첨가PVA응효과립처리고농도폐수。보지진수량일정,축점증가반응기내진수COD질량농도,즉2.2~12.9g/L,상응적유궤부하솔시5.4~51.79g/(L?d)。관찰반응기적운행정황,학정유궤부하솔재30 g/(L?d )시,COD거제솔최고가이체도96%。증대부하,동시보증진수적pH치시7.0,관찰반응기출수pH치여VFA적변화,학정괄의산갑완균생장적배경。종수집도적기체체적래간,재일정적범위내,기체산솔수착진수부하적제고이증가,당부하체도30 g/(L?d )시,기체체적가체38 L (실험최대치)。
PVA-gel beads are added to the EGSB reactor to treat high -concentration wastewater in this experiment .The influent COD level is increased stepwise from 2 .2 g/L to 12 .9 g/L under stable influent and the organic loading rate is changed relatively 5 .4~51 .79 g/(L?d) .The COD removal rate can reach 96% with an organic loading rate of 30 g/(L?d) in the reactor .While the organic loading rate is increased and the influent pH is kept at 7 .0 ,the changes of effluent pH and VFA are observed ,thus the appropriate growth environment for methanogens can be determined .In a certain range ,the gas production rate is increased with the increase of influent loading rate .When the organic loading rate reaches 30 g/(L?d ) , the gas volume can be increased to its peak (38 L ) .