微藻测序间歇式生物膜反应器(SBBR)在污水处理中的应用

S. Elystia, Rika Kristin, D. Andrio
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引用次数: 0

摘要

灰水含有有机物,未经任何处理就直接排放到环境中,会造成污染并影响水中的生命。可以进行的治疗是使用微生物。其中一种是微藻小球藻,它利用有机物作为生长的营养来源。在本研究中,使用序批式生物膜反应器(SBBR)工艺添加Kaledness 1(K1)生物载体作为附着微生物的培养基。研究目的是(1)了解序批式生物膜反应器(SBBR)中附着和悬浮的小球藻的最大数量。(2)获得去除灰水中COD、氨和MLSS的最佳循环时间和稳定时间。该研究通过在四个循环中改变每个循环中的稳定时间(1.5;2和2.5小时)进行,充电时间30分钟、反应120分钟、45分钟、分离45分钟不变,并进行四个循环,搅拌速度为60rpm,SBBR中藻类悬浮液的浓度为25%,Kaledness K1培养基的体积为20%。结果表明,小球藻悬浮并附着的微藻细胞数分别为1.85×106和1.46×106个/ml。对COD、氨和MLSS的最佳去除是在4个循环中稳定时间变化1.5小时,去除效率分别为84%和76%,悬浮和附着的MLSS浓度分别增加4780mg/l和4720mg/l。可以得出的结论是,稳定时间越快,去除效率就越高。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Application of Sequencing Batch Biofilm Reactor (SBBR) Using Microalgae Chorella sp. to Removal Nutrient in Grey Water
Grey water contains organic matter that is directly disposed to the environment without any treatment previously, will cause pollution and impacting life in the water. Treatment that can be done is using microorganisms. One of its kind is the microalgae Chlorella sp. which utilizes organic matter as a source of nutrients for its growth. In this study, the Kaldness 1 (K1) bio carrier was added as a medium for attaching microorganisms using the Sequencing Batch Biofilm Reactor (SBBR) process. The research objectives were (1) to know the maximum number of Chlorella sp. both attached and suspended in the Sequencing Batch Biofilm Reactor (SBBR), (2) to obtain the best cycle time and stabilization time in the removal of COD, Ammonia, and MLSS in grey water. The research was conducted by varying the stabilization time (1.5; 2 and 2.5 hours) in each cycle for four cycles with a constant variation of charging time 30 minutes, reaction 120 minutes, 45 minutes, separation 45 minutes, and carried out with four cycles, stirring speed at 60 rpm, the concentration of algae suspension in SBBR was 25% and the volume of Kaldness K1 medium was 20%. The results showed the number of microalgae cells Chlorella sp. was suspended and attached to 1.85 x 106 and 1.46 x 106 cells/ml. The best removal of COD, ammonia, and MLSS was found in the stabilization time variation of 1.5 hours in 4 cycles with a removal efficiency of 84% and 76%, respectively, and an increase in the concentration of suspended and attached MLSS by 4780 mg/l and 4720 mg/l. It can be concluded that the faster stabilization time, the more removal efficient will be.
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