Abstract
The feasibility and operation characteristics of anaerobic fermentation biohydrogen production in a continuous stirred-tank reactor (CSTR) were investigated for treating beet-sugar processing wastewater. The research indicates that the reactor has the capacity of continuously producing hydrogen in an initial biomass (as volatile suspension solids) of 17.74 g/L, temperature of (35±1)°C, hydraulic retention time (HRT) of 6 h, and the reactor can start up the ethanol-type fermentation with COD organic loading rate (OLR) in 12 d and realize stable hydrogen production. Furthermore, the CSTR reactor enjoys a favorable stability even with an organic shock loading. When the organic loading rate (as COD) rises from 8 kg/(m3·d) to 24 kg/(m3·d), the CSTR system can reach a new steady state within 9 d. COD removal rate increases from 8% to 20%, the biogases yield increases from 3 L/d to 12 L/d, and the hydrogen volume fraction in the biogas is 67%.
| Original language | English |
|---|---|
| Pages (from-to) | 75-78 |
| Number of pages | 4 |
| Journal | Huaxue Gongcheng/Chemical Engineering (China) |
| Volume | 38 |
| Issue number | 2 |
| State | Published - Feb 2010 |
UN SDGs
This output contributes to the following UN Sustainable Development Goals (SDGs)
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SDG 7 Affordable and Clean Energy
Keywords
- Anaerobic fermentation
- CSTR
- Hydrogen production
- Organic loading rate
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