Continuous Fermentative Hydrogen Production from Brown Sugar Using EGSB Reactor

2010 ◽  
Vol 113-116 ◽  
pp. 1132-1137 ◽  
Author(s):  
Yong Feng Li ◽  
Yong Ming Hui ◽  
Xin Yao ◽  
Lu Wang ◽  
Qian Wen Song ◽  
...  
Keyword(s):  
Hydrogen Production ◽  
Hydraulic Retention Time ◽  
Loading Rate ◽  
Granular Sludge ◽  
Organic Loading Rate ◽  
Organic Loading ◽  
Hydrogen Production Rate ◽  
Brown Sugar ◽  
Fermentative Hydrogen Production ◽  
Fermentative Hydrogen

In this experiment, brown sugar was chosen as the substrate of continuous operation. A lab-scale expanded granular sludge blanket (EGSB) reactor was employed. Stable ethanol-type fermentation was formed by controlling the organic loading rate (OLR). The results showed a maximum hydrogen production rate of 5.73L / L reactor•d was achieved, under the condition that the hydraulic retention time (HRT) = 2h, OLR = 97.2kg COD/m3 reactor•d. The average hydrogen content in the biogas during the 73-day operation was 41.27%.

Impact of Hydraulic Retention Time at Constant Organic Loading Rate in a Two-Stage Expanded Granular Sludge Bed Reactor

2014 ◽  
Vol 31 (6) ◽  
pp. 317-323 ◽  
Author(s):  
Mahyar Ghorbanian ◽  
Robert M. Lupitskyy ◽  
Jagannadh V. Satyavolu ◽  
R. Eric Berson
Keyword(s):  
Retention Time ◽  
Hydraulic Retention Time ◽  
Loading Rate ◽  
Granular Sludge ◽  
Organic Loading Rate ◽  
Organic Loading ◽  
Two Stage

Properties of Anaerobic Activated Sludge in Biohydrogen Production Reactor

2014 ◽  
Vol 884-885 ◽  
pp. 503-506
Author(s):  
Zhi Qin ◽  
Guang Yu Bai ◽  
Qi Zhang ◽  
Yong Yan Cui ◽  
Chao Yu Zhang
Keyword(s):  
Hydrogen Production ◽  
Activated Sludge ◽  
Retention Time ◽  
Hydraulic Retention Time ◽  
Loading Rate ◽  
Biohydrogen Production ◽  
Organic Loading Rate ◽  
Organic Loading ◽  
Mixture Volume ◽  
Total Mixture

For the properties of activated sludge studies, three kinds of activated sludge were obtained from continuous hydrogen production reactor. Activated sludge was got under organic loading rate (OLR) of 3, 7 and 25 kgCOD/m3·d condition, respectively. Sedimentation performance and activities of sludge were investigated. When OLR was 3 kgCOD/m3·d, activated sludge showed good sedimentation performance. After 30 minutes sedimentation, the volume of activated sludge in total mixture volume was about 39%. When OLR was 7 and 25kgCOD/m3·d, after 30 minutes sedimentation, the volume of activated sludge in total mixture volume was 80% and 83%, respectively. The increase of biomass is the main reason for increase of sedimentation performance. MLVSS/MLSS of activated sludge was 37.7% and 79.6% under OLR of 3 and 25kgCOD/m3·d condition, therefore, activities of activated sludge was high under high OLR condition. Since sedimentation performance of sludge is high under high OLR condition, hydraulic retention time should controlled carefully in engineering operation.

Enhanced Treatment of CSTR Anaerobic Digested Effluent from Poultry Wastewater by IC Reactor

2012 ◽  
Vol 433-440 ◽  
pp. 1239-1244
Author(s):  
Zhan Guang Liu ◽  
Xue Fei Zhou ◽  
Ya Lei Zhang ◽  
Hong Guang Zhu
Keyword(s):  
Hydraulic Retention Time ◽  
Loading Rate ◽  
Biogas Production ◽  
Granular Sludge ◽  
Anaerobic Treatment ◽  
Controlling Factors ◽  
Organic Loading Rate ◽  
Organic Loading ◽  
Internal Circulation ◽  
Poultry Wastewater

The feasibility of applying internal circulation (IC) reactor anaerobic treatment for effluent from a CSTR plant treating poultry wastewater was examined and the key controlling factors were explored. A continuous-flow IC reactor of 12.3L capacity inoculated with anaerobic granular sludge was operated for 98 days at 35±1°C. With corresponding organic loading rate of 1.5-3.5 kgCOD/m3•d at hydraulic retention time of 1.5d, the maximum volumetric biogas production rate of 1.2 m3/m3•d and tCOD (total COD) removal efficiency in the range of 70-80% was achieved. Therefore, IC reactor is competent to treat CSTR effluent from poultry wastewater. The decrease of sCOD (soluble COD) relative to tCOD and ammonia inhibition may lead to deterioration of IC reactor anaerobic treatment.

Improvement of Organic Loading Rate on Hydrogen Production Using Continuous Stirred Tank

2013 ◽  
Vol 805-806 ◽  
pp. 1382-1386
Author(s):  
Jian Hui Zhao ◽  
Ning Li ◽  
Yong Feng Li
Keyword(s):  
Hydrogen Production ◽  
Production Rate ◽  
Gas Production ◽  
Stirred Tank ◽  
Organic Loading Rate ◽  
Organic Loading ◽  
Hydrogen Production Rate ◽  
Brown Sugar ◽  
High Hydrogen ◽  
Continuous Stirred Tank

The influence of organic loading rates (OLRs) on the production of fermentation hydrogen was investigated in a continuous stirred tank reactor (CSTR) with brown sugar water as the fermentation substrate, and sewage sludge as the initiation of reaction. Six OLRs were examined, ranging from 12 kg/m3·d to 32 kg/m3·d. The biogas and hydrogen production rates continuously increased with increasing OLR (12 kg/m3·d to 32 kg/m3·d).It reached a maximum production rate of 18.6L/d and a hydrogen production rate of 6.4L/d at OLR= 32 kg/m3·d. Compared with the initial 12kg/m3·d, gas production improved by 89% and 87%, respectively. During system operation, the reactor could maintain a high hydrogen production rate of ethanol-type fermentation by adding a certain amount of NaOH in the reactor to regulate the pH level.

scholarly journals Effects of Carrier Materials on Anaerobic Hydrogen Production by Continuous Mixed Immobilized Sludge Reactors

2020 ◽  
Vol 65 (1) ◽  
pp. 124-132
Author(s):  
Qiaoyan Li ◽  
Yikun Cao ◽  
Yongfeng Li
Keyword(s):  
Hydrogen Production ◽  
Loading Rate ◽  
Anaerobic Fermentation ◽  
Utilization Efficiency ◽  
Organic Loading Rate ◽  
Organic Loading ◽  
Hydrogen Production Rate ◽  
Treatment Performance ◽  
Ceramic Ring ◽  
Carrier Materials

To enhance hydrogen production rate and increase substrate utilization efficiency of anaerobic fermentation, three carrier materials, Granular Activated Carbon (GAC), Zeolite Molecular Sieve (ZMS) and Biological Ceramic Ring (BCR), were used as carrier materials in Continuous Mixed Immobilized Sludge Reactors (CMISRs). The effects of carrier materials and substrate organic loading rate (OLR, OLR = 12, 24, 36, 48 kg/m3/d) on biohydrogen production were investigate, respectively. The highest HPRs of ZMS, GAC and BCR were achieved under the OLR of 36 kg COD/m3/d, and were 2.01, 1.81, and 2.86 L/L/d, respectively. The highest COD removal efficiencies of ZMS, GAC and BCR were 38.95 % (OLR = 24 kg COD/m3/d), 36.47 % (OLR = 36 kg COD/m3/d), and 41.03 % (OLR = 36 kg COD/m3/d), respectively. The best substrate degradation rate of ZMS, GAC and BCR were 40.33 % (OLR = 24 kg COD/m3/d), 38.30 % (OLR = 24 kg COD/m3/d) and 45.60 % (OLR = 12 kg COD/m3/d). The results indicated that biological ceramic ring get better hydrogen production and wastewater treatment performance as sludge carrier material for hydrogen production in immobilized bioprocesses.

Performance of an anaerobic baffled reactor (ABR) as a hydrolysis-acidogenesis unit in treating landfill leachate mixed with municipal sewage

2000 ◽  
Vol 42 (12) ◽  
pp. 115-121 ◽  
Author(s):  
B. Wang ◽  
Y. Shen
Keyword(s):  
Landfill Leachate ◽  
Loading Rate ◽  
Granular Sludge ◽  
Operational Performance ◽  
Municipal Sewage ◽  
Organic Loading Rate ◽  
Stable Operation ◽  
Organic Loading ◽  
Anaerobic Baffled Reactor ◽  
Biological Treatability

A study on the performance of an Anaerobic Baffled Reactor(ABR) as a hydrolysis-acidogenesis unit in treating the mixed wastewater of landfill leachate and municipal sewage in different volumetric ratios was carried out. The results showed that ABR substantially improved the biological treatability of the mixed wastewater by increasing its BOD5/COD ratio to 0.4–0.6 from the initial values of 0.15–0.3. The formation of bar-shaped granular sludge of 0.5–5 mm both in diameter and length with an SVI of 7.5–14.2 ml/g was observed in all compartments of the ABR when the organic loading rate reached 4.71 kgCOD/m3 · d. The effects of the ratios of NH4+-N/COD and COD/TP in mixed wastewater on the operational performance were also studied, from which it was found that a reasonable NH4+-N/COD ratio should be lower than 0.02, and the phosphorus supplement was needed when the volumetric ratio was higher than 4:6 for stable operation of ABR.

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