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Updated: Jun 26, 2026

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Protocol for Biofilm Streamer Formation in a Microfluidic Device with Micro-pillars
Published on: August 20, 2014
[Biofilm formation in an external loop three phase fluidized bed reactor]
Jin-Sheng Zhang1, Xing-Zhong Yuan, Guang-Ming Zeng
1(College of Environmental Science and Technology, Hunan University, Changsha 410082, China. jecalsamy@163.com
Huan Jing Ke Xue= Huanjing Kexue
|January 16, 2009
Summary
Optimal biofilm formation in fluidized bed reactors occurs with specific sludge addition (2 g/L) and C/N ratios (8-12). Hydraulic residence time (HRT) between 1-3 hours also promotes biofilm growth.
Area of Science:
- Environmental Engineering
- Biotechnology
- Water Treatment
Context:
- Biofilm formation is crucial for wastewater treatment processes.
- Fluidized bed reactors offer advantages in handling biomass.
- Controlling operational parameters is key to optimizing biofilm development.
Purpose:
- To investigate the impact of sludge addition, C/N ratio, and hydraulic residence time (HRT) on biofilm formation in a three-phase fluidized bed reactor.
- To determine optimal conditions for rapid and stable biofilm development.
- To understand the relationship between suspended and attached sludge under varying HRT.
Summary:
- The study found that a sludge addition of 2 g/L and a C/N ratio of 8-12 were optimal for biofilm formation in granular activated carbon (GAC) fluidized beds (0.125-0.5 mm diameter) at 20-30°C.
- High C/N ratios (≥14) led to filamentous bulking sludge.
- Biofilm increased with HRT from 1-3 hours, stabilized between 4-5 hours, and decreased beyond 5 hours, correlating with suspended sludge levels.
Impact:
- Provides critical data for optimizing the design and operation of fluidized bed reactors for enhanced wastewater treatment.
- Offers insights into managing sludge characteristics and preventing operational issues like filamentous bulking.
- Contributes to the development of more efficient and stable biological treatment systems.
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