环境科学
環境科學
배경과학
CHINESE JOURNAL OF ENVIRONMENTAL SCIENCE
2015年
5期
1720-1726
,共7页
黄帅%刘宏波%殷波%马惠君%符波%刘和%白洁
黃帥%劉宏波%慇波%馬惠君%符波%劉和%白潔
황수%류굉파%은파%마혜군%부파%류화%백길
自生动态膜%滤布%形成%过滤模型%污泥发酵液%膜分离
自生動態膜%濾佈%形成%過濾模型%汙泥髮酵液%膜分離
자생동태막%려포%형성%과려모형%오니발효액%막분리
self-forming dynamic membrane%cloth filter%formation%filtration model%sludge fermentation liquid%membrane separation
采用自生生物动态膜分离高浓度污泥发酵液,研究了动态膜的形成过程及其对污泥发酵液的分离效果。结果表明,自生动态膜的形成过程受污泥浓度的影响较小,污泥浓度仅影响初始膜通量,不影响稳定时的膜通量。膜通量随着滤布孔径和搅拌速度的增大而增大。动态膜的形成过程符合死端过滤模型,分别由以下4个过程构成:先通过与膜基材孔径相似的污泥颗粒堵塞膜基材孔,其后在膜基材上形成单层污泥,进而在膜基材上形成多层污泥,最后,大颗粒污泥继续沉积到污泥层上。动态膜形成后,对污泥颗粒和溶解性 COD (SCOD)的截留率分别为98%和28%,对挥发性脂肪酸(volatile fatty acids, VFAs)的渗透率在82%以上,胞外聚合物(extracellular polymeric substances, EPS)中的蛋白质是动态膜的主要成分。
採用自生生物動態膜分離高濃度汙泥髮酵液,研究瞭動態膜的形成過程及其對汙泥髮酵液的分離效果。結果錶明,自生動態膜的形成過程受汙泥濃度的影響較小,汙泥濃度僅影響初始膜通量,不影響穩定時的膜通量。膜通量隨著濾佈孔徑和攪拌速度的增大而增大。動態膜的形成過程符閤死耑過濾模型,分彆由以下4箇過程構成:先通過與膜基材孔徑相似的汙泥顆粒堵塞膜基材孔,其後在膜基材上形成單層汙泥,進而在膜基材上形成多層汙泥,最後,大顆粒汙泥繼續沉積到汙泥層上。動態膜形成後,對汙泥顆粒和溶解性 COD (SCOD)的截留率分彆為98%和28%,對揮髮性脂肪痠(volatile fatty acids, VFAs)的滲透率在82%以上,胞外聚閤物(extracellular polymeric substances, EPS)中的蛋白質是動態膜的主要成分。
채용자생생물동태막분리고농도오니발효액,연구료동태막적형성과정급기대오니발효액적분리효과。결과표명,자생동태막적형성과정수오니농도적영향교소,오니농도부영향초시막통량,불영향은정시적막통량。막통량수착려포공경화교반속도적증대이증대。동태막적형성과정부합사단과려모형,분별유이하4개과정구성:선통과여막기재공경상사적오니과립도새막기재공,기후재막기재상형성단층오니,진이재막기재상형성다층오니,최후,대과립오니계속침적도오니층상。동태막형성후,대오니과립화용해성 COD (SCOD)적절류솔분별위98%화28%,대휘발성지방산(volatile fatty acids, VFAs)적삼투솔재82%이상,포외취합물(extracellular polymeric substances, EPS)중적단백질시동태막적주요성분。
Self-forming dynamic membrane was used to separate high-concentration sludge fermentation liquid, and the formation mechanism and separation efficiency of dynamic membrane were investigated. The results indicated that the impact of sludge concentrations was negligible on the formation of dynamic membrane. Though membrane flux could be influenced by sludge concentration at the initial stage of membrane formation process, the influence was not obvious at the stable stage. Membrane flux was improved with increasing filter cloth pore size and stirring speeds. Moreover, the results indicated that the formation process of dynamic membrane followed the dead-end filtration model, which could be divided into four stages. Firstly, filter cloth pore was blocked by those sludge particles with the diameter similar to the pore size of filter cloth. Secondly, sludge particles formed monolayer sludge on the filter cloth. Thirdly, sludge particles formed multilayer sludge on the filter cloth. Finally, large sludge particles deposited onto the sludge layer. After formation of the dynamic membrane, the retention efficiency of sludge particles and SCOD could reach 98% and 28% , respectively, and the permeation efficiency of VFAs was over 82% . Proteins in EPS were the main component of the dynamic membrane.