Article ID | Journal | Published Year | Pages | File Type |
---|---|---|---|---|
7715471 | International Journal of Hydrogen Energy | 2015 | 10 Pages |
Abstract
A two-stage thermophilic fermentation and mesophilic methanogenic process for biohythane production from palm oil mill effluent (POME) was investigated. The hydrogen and methane potential from POME were 170-200 L H2 kgCODâ1 and 210-292 L CH4 kgCODâ1, respectively. A continuous two-stage process with hydraulic retention time (HRT) of 2 d for hydrogen reactor and 15 d for methane reactor, obtained 34% higher energy yield than single stage methane production. The hydrogen and methane yields from two-stage were 210 L H2 kgCODâ1 and 315 L CH4 kgCODâ1, respectively with total energy yield of 15.34 MJ kgCODâ1. Mixed hydrogen and methane (biohythane) production rate was 4.4 L biogas Lâ1dâ1 with containing of 51% CH4, 14% H2 and 35% CO2. Hydrogen reactor was dominated with hydrogen producing bacteria of Thermoanaerobacterium thermosaccharolyticum, while acetoclastic Methanoculleus sp. was the dominant methanogen in methane reactor. Two-stage process for biohythane production could efficiently for energy recovery from POME.
Keywords
Related Topics
Physical Sciences and Engineering
Chemistry
Electrochemistry
Authors
Chonticha Mamimin, Apinya Singkhala, Prawit Kongjan, Benjaporn Suraraksa, Poonsuk Prasertsan, Tsuyoshi Imai, Sompong O-Thong,