Wanna Choorit

Effect of temperature on the anaerobic digestion of palm oil mill effluent

Two continuous stirred tank reactors (CSTRs) each fed with palm oil mill effluent (POME), operated at 37oC and 55oC, respectively, were investigated for their performance under varies organic loading rates (OLRs). The 37oC reactor operated successfully at a maximum OLR of 12.25 g[COD]/L/day and a hydraulic retention time (HRT) of 7 days. The 55oC reactor operated successfully at the higher loading rate of 17.01 g[COD]/L/day and had a HRT of 5 days. The 37oC reactor achieved a 71.10% reduction of chemical oxygen demand (COD), a biogas production rate of 3.73 L of gas/L[reactor]/day containing 71.04% methane, whereas the 55oC reactor achieved a 70.32% reduction of COD, a biogas production rate of 4.66 L of gas/L[reactor]/day containing 69.53% methane. An OLR of 9.68 g[COD]/L/day, at a HRT of 7 days, was used to study the effects of changing the temperature by 3oC increments. The reactor processes were reasonably stable during the increase from 37oC to 43oC and the decrease from 55oC to 43oC. When the temperature was increased from 37oC to 46oC, the total volatile fatty acid (TVFA) concentration and biogas production was 2,059 mg as acetic acid/L and 1.49 L of gas/L[reactor]/day at day 56, respectively. When the temperature was reduced from 55oC to 40oC, the TVFA concentration and biogas production was 2,368 mg as acetic acid/L and 2.01 L of gas/L[reactor]/day at day 102, respectively. By first reducing the OLR to 4.20 g[COD]/L/day then slowly increasing the OLR back to 9.68 g[COD]/L/day, both reactors were restored to stable conditions at 49oC and 37oC respectively. The initial 37oC reactor became fully acclimatized at 55oC with an efficiency similar to that when operated at the initial 37oC whereas the 55oC reactor also achieved stability at 37oC but with a lower efficiency

Use of response surface method for the determination of demineralization efficiency in fermented shrimp shells

A Box-Behnken design with three variables (sucrose concentration, initial pH value and soaking time) and three levels were used for studying the demineralization efficiency in fermented shrimp shells by Pediococcus sp. L1/2. First, the bacterial cells were inoculated into the media with various concentrations of sucrose and initial pH values, and fermentation took place under static conditions at 37 degrees C for 24h. Significant differences in the levels of total titratable acid were observed. This was followed by adding shrimp shells and soaking them in the fermentation media for 12, 24 and 36 h. The results showed that when the sucrose concentration was 50 g/L, and the initial pH value was 6.00, soaking for 36 h gave a demineralization efficiency of 68.38%. By solving the equation and also analyzing the response surface contour plots, optimum conditions occurred when the sucrose concentration was 50 g/L, the initial pH value was 7.00 and the soaking time was 36 h with a predicted value of demineralization of 83.03% whereas our experiment gave 83.47%.

Carbon-to-nitrogen ratio affects the biomass composition and the fatty acid profile of heterotrophically grown Chlorella sp. TISTR 8990 for biodiesel production

Chlorella sp. TISTR 8990 was cultivated heterotrophically in media with various initial carbon-to-nitrogen ratios (C/N ratio) and at different agitation speeds. The production of the biomass, its total fatty acid content and the composition of the fatty acids were affected by the C/N ratio, but not by agitation speed in the range examined. The biomass production was maximized at a C/N mass ratio of 29:1. At this C/N ratio, the biomass productivity was 0.68gL(-1)d(-1), or nearly 1.6-fold the best attainable productivity in photoautotrophic growth. The biomass yield coefficient on glucose was 0.62gg(-1) during exponential growth. The total fatty acids (TFAs) in the freeze-dried biomass were maximum (459mgg(-1)) at a C/N ratio of 95:1. Lower values of the C/N ratio reduced the fatty acid content of the biomass. The maximum productivity of TFAs (186mgL(-1)d(-1)) occurred at C/N ratios of 63:1 and higher. At these conditions, the fatty acids were mostly of the polyunsaturated type. Allowing the alga to remain in the stationary phase for a prolonged period after N-depletion, reduced the level of monounsaturated fatty acids and the level of polyunsaturated fatty acids increased. Biotin supplementation of the culture medium reduced the biomass productivity relative to biotin-free control, but had no effect on the total fatty acid content of the biomass.

Production of biomass and extracellular 5-aminolevulinic acid by Rhodopseudomonas palustris KG31 under light and dark conditions using volatile fatty acid.

Kinetic parameters for growth and extracellular 5-aminolevulinic acid (ALA) production of Rhodopseudomonas palustris KG31 under light and dark conditions in a medium containing volatile fatty acids (VFA) as the carbon sources were estimated using a Gompertz model. The lag phase for growth and the maximum specific growth rate under microaerobic-light cultivations were 7.29-12.49 h and 0.038-0.094 h(-1), respectively, whereas under aerobic-dark cultivations, they were 2.03-14.25 h and 0.016-0.022 h(-1), respectively. The lag phase for extracellular ALA production and the maximum specific extracellular ALA production rate under microaerobic-light cultivations (15.72-24.74 h and 0.222-0.299 h(-1), respectively) were better than those obtained under aerobic-dark cultivations (24.57-44.84 h and 0.103-0.215 h(-1), respectively). The biomass and the extracellular ALA yields of 39.66-56.25 gDCW/l/mol C, and 148.47-245.75 μM/mol C, respectively, under microaerobic-light cultivations were higher than of those obtained under aerobic-dark conditions. An enhancement of extracellular ALA production under aerobic-dark conditions revealed that the ALA yield was markedly increased 8-fold (48.36 μM) by the addition of 10mM succinate, 4.5mM glycine, and 15 mM levulinic acid (LA). By controlling dissolved oxygen (DO) and pH values, a maximum extracellular ALA yield of 66.38 μM was found. The degradation rate of ALA in the culture broth was closely related to the pH value.

Influence of Precursors and Inhibitor on the Production of Extracellular 5-Aminolevulinic Acid and Biomass by Rhodopseudomonas palustris KG31

5-Aminolevulinic acid (ALA) and the biomass of photosynthetic bacteria, Rhodopseudomonas palustris KG31, have very high potential for development and exploitation as bioherbicide and biofertilizer respectively. In this work, the effects of two precursors and an inhibitor of aminolevulinic dehydratase (ALAD) added to the VFA culture medium on the production of ALA and biomass were investigated. The experimental runs were carried out according to a Box-Behnken design. The precursors were added to the medium at the beginning of cultivation, while the inhibitor was added after 24 h. Statistical analysis indicated that levulinic acid (LA) has a positive effect on ALA production while glycine has a negative effect on biomass production. In order to enhance both ALA and biomass products, the most suitable medium was VFA medium supplemented with 3.0 mM glycine and 10 mM LA, giving ALA and biomass of 182.91 μM and 3.1 gDCW/l within 54 h.

Cellulose and hemicellulose recovery from oil palm empty fruit bunch (EFB) fibers and production of sugars from the fibers

A sequential two-step treatment with peracetic acid (PA) and alkaline peroxide (AP) at mild temperatures (20-35°C) removed more than 98% of the lignin from oil palm empty fruit bunch (EFB) fiber. For each kilogram of EFB fiber treated, 200-250g of a solids fraction and 120-170g of a precipitate fraction were recovered after the treatment. Subsequent enzymatic hydrolysis (45°C, 72h) of the recovered solids (excluding the precipitate) resulted in a glucose yield of 629.8±0.5g per kg of the original dry EFB biomass. Enzymatic hydrolysis of untreated EFB yielded only 3.0±0.0g glucose per kg of dry EFB. Therefore, the PA-AP pretreatment enhanced glucose recovery from EFB by nearly 210-fold. The total treatment time was 93h (a 9h PA treatment at 35°C, a 12h treatment with AP (20°C, 4% NaOH), 72h of enzymatic hydrolysis).

In-vitro assessment of probiotic potential of Lactobacillus plantarum WU-P19 isolated from a traditional fermented herb

Samples of fermented herbs were used to isolate lactic acid bacteria (LAB). Of a total of 19 isolates, eight were resistant both to gastric acid and bile salts (glycocholic acid, GCA; taurocholic acid, TCA; glycodeoxycholic acid, GDCA; and taurodeoxycholic acid, TDCA). Most isolates exhibited a pH-dependent surface hydrophobicity: a pH of 4 conferred a greater hydrophobicity compared to a pH of 7. Based on the hydrophobicity characteristics, the LAB isolate WU-P19 from the traditional fermented herb Oroxylum indicum was selected for further study. WU-P19 was identified as Lactobacillus plantarum WU-P19. The presence of bile salts GCA and GDCA in the culture medium induced production of the relevant bile salt hydrolase. Relative to controls, the presence of the bile salts in the culture medium affected the carbon and nitrogen contents of the cells and their hydrophobicity. Cells grown in a medium free of bile salts were morphologically different to cells grown in the presence of GCA and GDCA. WU-P19 was resistant to several antibiotics. It produced β-galactosidase and inhibited growth of the tested pathogenic bacteria at various levels. In vitro, L. plantarum WU-P19 adapted well to conditions typical of the various zones of the human gastrointestinal tract. In view of the promising results, in vivo evaluations are planned for the isolate WU-P19.

Heterotrophic production of Chlorella sp. TISTR 8990—biomass growth and composition under various production conditions

The green microalga Chlorella sp. TISTR 8990 was grown heterotrophically in the dark using various concentrations of a basal glucose medium with a carbon‐to‐nitrogen mass ratio of 29:1. The final biomass concentration and the rate of growth were highest in the fivefold concentrated basal glucose medium (25 g L−1 glucose, 2.5 g L−1 KNO3) in batch operations. Improving oxygen transfer in the culture by increasing the agitation rate and decreasing the culture volume in 500‐mL shake flasks improved growth and glucose utilization. A maximum biomass concentration of nearly 12 g L−1 was obtained within 4 days at 300 rpm, 30°C, with a glucose utilization of nearly 76% in batch culture. The total fatty acid (TFA) content of the biomass and the TFA productivity were 102 mg g−1 and 305 mg L−1 day−1, respectively. A repeated fed‐batch culture with four cycles of feeding with the fivefold concentrated medium in a 3‐L bioreactor was evaluated for biomass production. The total culture period was 11 days. A maximum biomass concentration of nearly 26 g L−1 was obtained with a TFA productivity of 223 mg L−1 day−1. The final biomass contained (w/w) 13.5% lipids, 20.8% protein and 17.2% starch. Of the fatty acids produced, 52% (w/w) were saturated, 41% were monounsaturated and 7% were polyunsaturated (PUFA). A low content of PUFA in TFA feedstock is required for producing high quality biodiesel.