水处理技术
水處理技術
수처리기술
2010年
2期
44-48
,共5页
李庆%徐高田%秦哲%赵朋卫
李慶%徐高田%秦哲%趙朋衛
리경%서고전%진철%조붕위
水力特性%气含率%液相循环速度
水力特性%氣含率%液相循環速度
수력특성%기함솔%액상순배속도
hydrodynamic characteristics%gas holdup%liquid circulation rate
通过清水试验,确定了喷射环流膜生物反应器的最大吸气量,探讨吸气量、循环水量等因素对气含率、液相循环速度的影响,测定膜组件加入前后的气含率、液相循环速度大小,并与已有的生化反应器进行了比较.结果表明,装置的最大吸气量可达到0.67 m~3·h~(-1)吸气量是影响气含率的主要因素,并且随着吸气量的增加,气含率也随着增加;循环水量是影响液相循环速度的主要因素,随着循环水量的升高循环液速升高;膜组件的加入对气舍率、液相循环速度的影响非常小,与已有的生化反应器比较,JLMBR在水力特性方面具有明显的优势.所得结果可以为该类反应器的放大设计提供借鉴.
通過清水試驗,確定瞭噴射環流膜生物反應器的最大吸氣量,探討吸氣量、循環水量等因素對氣含率、液相循環速度的影響,測定膜組件加入前後的氣含率、液相循環速度大小,併與已有的生化反應器進行瞭比較.結果錶明,裝置的最大吸氣量可達到0.67 m~3·h~(-1)吸氣量是影響氣含率的主要因素,併且隨著吸氣量的增加,氣含率也隨著增加;循環水量是影響液相循環速度的主要因素,隨著循環水量的升高循環液速升高;膜組件的加入對氣捨率、液相循環速度的影響非常小,與已有的生化反應器比較,JLMBR在水力特性方麵具有明顯的優勢.所得結果可以為該類反應器的放大設計提供藉鑒.
통과청수시험,학정료분사배류막생물반응기적최대흡기량,탐토흡기량、순배수량등인소대기함솔、액상순배속도적영향,측정막조건가입전후적기함솔、액상순배속도대소,병여이유적생화반응기진행료비교.결과표명,장치적최대흡기량가체도0.67 m~3·h~(-1)흡기량시영향기함솔적주요인소,병차수착흡기량적증가,기함솔야수착증가;순배수량시영향액상순배속도적주요인소,수착순배수량적승고순배액속승고;막조건적가입대기사솔、액상순배속도적영향비상소,여이유적생화반응기비교,JLMBR재수력특성방면구유명현적우세.소득결과가이위해류반응기적방대설계제공차감.
The biggest suction of bioreactor was examined by using tap water. The influence of suction and liquid circulation on gas holdup and liquid circulation rate was discussed. Compared with existing bioreactor and measured gas holdup and liquid circulation velocity with membrane in the biore-actor or not. The results showed that the biggest suction could reach 0.67 m~3·h~(-1).The suction was primary factor which effected gas holdup, gas holdup would increase gradually as suction increased. The liquid circulation was primary factor which effected liquid circulation velocity, as liquid circulation increased; liquid circulation velocity would increase rapidly. Membrane had little effect to gas holdup and liquid circulation velocity. JLMBR has shown the comparative advantage in hydrodynamic characteristics to existing bioreactor. It provides a theoretical basis and base data for design and scaling up of the reactor.