scholarly journals Biohydrogen production by Clostridium butyricum EB6 from palm oil mill effluent

2009 ◽  
Vol 34 (2) ◽  
pp. 764-771 ◽  
Author(s):  
M CHONG ◽  
R RAHIM ◽  
Y SHIRAI ◽  
M HASSAN
Keyword(s):  
Palm Oil ◽  
Clostridium Butyricum ◽  
Biohydrogen Production ◽  
Palm Oil Mill Effluent ◽  
Palm Oil Mill

scholarly journals Optimization of biohydrogen production by Clostridium butyricum EB6 from palm oil mill effluent using response surface methodology

2009 ◽  
Vol 34 (17) ◽  
pp. 7475-7482 ◽  
Author(s):  
Mei-Ling Chong ◽  
Nor' Aini Abdul Rahman ◽  
Raha Abdul Rahim ◽  
Suraini Abdul Aziz ◽  
Yoshihito Shirai ◽  
...  
Keyword(s):  
Response Surface Methodology ◽  
Response Surface ◽  
Palm Oil ◽  
Clostridium Butyricum ◽  
Biohydrogen Production ◽  
Palm Oil Mill Effluent ◽  
Palm Oil Mill

Biohydrogen production from palm oil mill effluent using immobilized Clostridium butyricum EB6 in polyethylene glycol

2013 ◽  
Vol 48 (2) ◽  
pp. 294-298 ◽  
Author(s):  
Lakhveer Singh ◽  
Zularisam A. Wahid ◽  
Muhammad Faisal Siddiqui ◽  
Anwar Ahmad ◽  
Mohd Hasbi Ab. Rahim ◽  
...  
Keyword(s):  
Polyethylene Glycol ◽  
Palm Oil ◽  
Clostridium Butyricum ◽  
Biohydrogen Production ◽  
Palm Oil Mill Effluent ◽  
Palm Oil Mill

scholarly journals Acclimatization Study for Biohydrogen Production from Palm Oil Mill Effluent (POME) in Continuous-flow System

2018 ◽  
Vol 34 ◽  
pp. 02054 ◽  
Author(s):  
N. Idris ◽  
N.A. Lutpi ◽  
Y. S. Wong ◽  
T.N. Tengku Izhar
Keyword(s):  
Steady State ◽  
Palm Oil ◽  
Continuous Flow ◽  
Flow System ◽  
Oxygen Demand ◽  
Biohydrogen Production ◽  
Palm Oil Mill Effluent ◽  
Continuous Flow System ◽  
Thermophilic Fermentation ◽  
Palm Oil Mill

This research aims to study the acclimatization phase for biohydrogen production from palm oil mill effluent (POME) by adapting the microorganism to the new environment in continuous-flow system of thermophilic bioreactor. The thermophilic fermentation was continuously loaded with 0.4 L/day of raw POME for 35 days to acclimatize the microorganism until a steady state of biohydrogen production was obtained. The significance effect of acclimatization phase on parameter such as pH, microbial growth, chemical oxygen demand (COD), and alkalinity were also studied besides the production of biogas. This study had found that the thermophilic bioreactor reach its steady state with 1960 mL/d of biogas produced, which consist of 894 ppm of hydrogen composition.

Ozonation aided mesophilic biohydrogen production from palm oil mill effluent

2019 ◽  
Vol 44 (11) ◽  
pp. 5182-5188 ◽  
Author(s):  
Pinanong Tanikkul ◽  
Siriorn Booyawanich ◽  
Nipon Pisutpaisal
Keyword(s):  
Palm Oil ◽  
Biohydrogen Production ◽  
Palm Oil Mill Effluent ◽  
Palm Oil Mill

Appropriate mixing speeds of Rushton turbine for biohydrogen production from palm oil mill effluent in a continuous stirred tank reactor

Energy ◽  
2019 ◽  
Vol 179 ◽  
pp. 823-830 ◽  
Author(s):  
Tanawat Srirugsa ◽  
Suteera Prasertsan ◽  
Thanansak Theppaya ◽  
Theerayut Leevijit ◽  
Poonsuk Prasertsan
Keyword(s):  
Palm Oil ◽  
Biohydrogen Production ◽  
Palm Oil Mill Effluent ◽  
Stirred Tank ◽  
Continuous Stirred Tank Reactor ◽  
Stirred Tank Reactor ◽  
Rushton Turbine ◽  
Tank Reactor ◽  
Continuous Stirred Tank ◽  
Palm Oil Mill

Kinetics of Biohydrogen Production from Ozonated Palm Oil Mill Effluent Using C. butyricum and C. acetobutylicum Co-Culture

2012 ◽  
Vol 512-515 ◽  
pp. 1515-1519 ◽  
Author(s):  
Nipon Pisutpaisal ◽  
Saowaluck Hoasagul
Keyword(s):  
Hydrogen Production ◽  
Palm Oil ◽  
Biohydrogen Production ◽  
Palm Oil Mill Effluent ◽  
Batch Reactors ◽  
Fermentation Products ◽  
Ozone Pretreatment ◽  
Palm Oil Mill ◽  
Kinetics Of ◽  
Mesophilic Condition

Kinetics of mesophilic biohydrogen production from ozone-pretreated palm oil mill effluent (POME) using C. butyricum and C. acetobutylicum co-culture was investigated. All experiments were setup in 0.5-L batch reactors under mesophilic condition (37°C), pH 6, and POME concentration of 5,000-30,000 mg COD L-1. At the concentration of 15,000 mg COD L-1, maximum hydrogen production yield for non-ozone pretreated POME and ozone pretreated POME were 318 and 122 mL g-1 CODremoved, respectively. Acetic and butyric acids were dominant fermentation products in liquid phase. Ozone-pretreatment of POME showed no significant improvement on the hydrogen production by the co-culture.

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