Submersible microbial fuel cell for electricity production from sewage sludge

A submersible microbial fuel cell (SMFC) was utilized to treat sewage sludge and simultaneously generate electricity. Stable power generation (145 +/- 5 mW/m2, 470 omega) was produced continuously from raw sewage sludge for 5.5 days. The maximum power density reached 190 +/- 5 mW/m2. The corresponding total chemical oxygen demand (TCOD) removal efficiency was 78.1 +/- 0.2% with initial TCOD of 49.7 g/L. The power generation of SMFC was depended on the sludge concentration, while dilution of the raw sludge resulted in higher power density. The maximum power density was saturated at sludge concentration of 17 g-TCOD/L, where 290 mw/m2 was achieved. When effluents from an anaerobic digester that was fed with raw sludge were used as substrate in the SMFC, a maximum power density of 318 mW/m2, and a final TCOD removal of 71.9 +/- 0.2% were achieved. These results have practical implications for development of an effective system to treat sewage sludge and simultaneously recover energy.     

Design through selection: a method that works

In this paper a practical approach to design, based on the concept of selection, is presented. The approach involves: first, the generation of alternative concepts using ideation tecniques; second, the selection of the ‘most-likely-to-succeed’ concepts for further development into feasible alternatives; third, the formulation and solution of selection-decision-support problems to rank the feasible alternatives in order of preference using multiple attributes.The method presented in this paper is a combination of the methods proposed by Pugh and by Mistree and Muster. The former method is appropriate for use in concept selection, which is characterized by many alternatives and essentially insight-based ‘soft’ information. The latter method is appropriate when there are few alternatives and a mix of science-based ‘hard’ and insight-based ‘soft’ information. The method presented by Mistree and Muster is therefore used to formulate and solve the selection-decision-support problem. The design example used in this paper is a modified version of that used by Pugh.     

Biohydrogen production from xylose at extreme thermophilic temperatures (70 °C) by mixed culture fermentation

Biohydrogen production from xylose at extreme thermophilic temperatures (70 °C) was investigated in batch and continuous-mode operation. Biohydrogen was successfully produced from xylose by repeated batch cultivations with mixed culture received from a biohydrogen reactor treating household solid wastes at 70 °C. The highest hydrogen yield of 1.62 ± 0.02 mol-H₂/mol-xylose_consumed was obtained at initial xylose concentration of 0.5 g/L with synthetic medium amended with 1 g/L of yeast extract. Lower hydrogen yield was achieved at initial xylose concentration higher than 2 g/L. Addition of yeast extract in the cultivation medium resulted in significant improvement of hydrogen yield. The main metabolic products during xylose fermentation were acetate, ethanol, and lactate. The specific growth rates were able to fit the experimental points relatively well with Haldane equation assuming substrate inhibition, and the following kinetic parameters were obtained: the maximum specific growth rate (μ_max) was 0.17 h⁻¹, the half-saturation constant (K_s) was 0.75 g/L, and inhibition constant (K_i) was 3.72 g/L of xylose. Intermittent N₂ sparging could enhance hydrogen production when high hydrogen partial pressure (>0.14 atm) was present in the headspace of the batch reactors. Biohydrogen could be successfully produced in continuously stirred reactor (CSTR) operated at 72-h hydraulic retention time (HRT) with 1 g/L of xylose as substrate at 70 °C. The hydrogen production yield achieved in the CSTR was 1.36 ± 0.03 mol-H₂/mol-xylose_sonsumed, and the production rate was 62 ± 2 ml/d·L_reactor. The hydrogen content in the methane-free mixed gas was approximately 31 ± 1%, and the rest was carbon dioxide. The main intermediate by-products from the effluent were acetate, formate, and ethanol at 4.25 ± 0.10, 3.01 ± 0.11, and 2.59 ± 0.16 mM, respectively.     

Anaerobic digestion of skim latex serum (SLS) for hydrogen and methane production using a two-stage process in a series of up-flow anaerobic sludge blanket (UASB) reactor

A series of up-flow anaerobic sludge blanket (UASB) reactors operated under thermophilic conditions was used to investigate the two-stage anaerobic process for continuous hydrogen and methane production from skim latex serum (SLS). The first reactor for producing hydrogen was operated by feeding 38 g-VS/L-SLS at various hydraulic retention times (HRTs) of 60, 48, 36, and 24 h. The optimum hydrogen production yield of 2.25 ± 0.09 L-H₂/L-SLS was achieved at a 36 h HRT. Meanwhile, the effluents containing mainly with acetate was fed to the second UASB reactor for methane production at 9-day HRT and could be converted to methane with the production yield of 6.41 ± 0.52 L-CH₄/L-SLS. The efficiency of organic matters removal obtained from this two-stage process was 62%. The present study shows high value fuel gases in a form of hydrogen and methane can be potentially generated by using a continuous two-stage anaerobic process, in which available organic matters is simultaneously degraded.     

Feasibility of bio-hythane production by co-digesting skim latex serum (SLS) with palm oil mill effluent (POME) through two-phase anaerobic process

Hydrogenogenic batch fermentation without nutrients addition was investigated at different SLS: POME mixing ratios of 100:0, 95:5, 90:10, 85:15, 80:20, 75:25, 70:30, 65:35, 60:40, 55:45,50:50, and 0:100 (Volatile Solid, VS basis) at initial organic concentrations of 21 and 7 g-VS/L. Satisfactory hydrogen yield of 84.5 ± 0.7 mL H₂/g-VS_added was achieved from 7 g-VS/L batch having SLS: POME-VS mixing ratio of 55:45. Adding NaHCO₃ 3 g/L or 0.43 g-NaHCO₃/g-VS) in the two-stage anaerobic system at 7 g-VS/L could provide sufficient buffering capacity. Hydrogenogenic effluent from 7 g-VS/L batch at SLS: POME mixing ratio of 55:45 (VS basis) could further generate rather high methane yield of 311.2 ± 8.0 mL- CH₄/g-VS_added in themethanogenic stage.According to the experimental results, bio-hythane approximately 55.5 × 10⁶ m³/year with 21% (V/V) of hydrogen, equivalent to51.0 × 10⁶ l-gasoline could be produced potentially from 3.88 × 10⁶ m³ of mixed SLS and POME through the two-stage anaerobic co-digestion.