Extraction and characterization of triglycerides from coffeeweed and switchgrass seeds as potential feedstocks for biodiesel production.

BACKGROUND: Although switchgrass has been developed as a biofuel feedstock and its potential for bioethanol and bio-oil from fast pyrolysis reported in the literature, the use of the seeds of switchgrass as a source of triglycerides for biodiesel production has not been reported. Similarly, the potential for extracting triglycerides from coffeeweed (an invasive plant of no current economic value) needs to be investigated to ascertain its potential economic use for biodiesel production. RESULTS: The results show that coffeeweed and switchgrass seeds contain known triglycerides which are 983 and 1000 g kg(-1) respectively of the fatty acids found in edible vegetable oils such as sunflower, corn and soybean oils. In addition, the triglyceride yields of 53-67 g kg(-1) of the seed samples are in the range of commercial oil-producing seeds such as corn (42 g kg(-1) ). CONCLUSION: The results also indicate that the two non-edible oils could be used as substitutes for edible oil for biodiesel production. In addition, the use of seeds of switchgrass for non-edible oil production (as a feedstock for the production of biodiesel) further increases the total biofuel yield when switchgrass is cultivated for use as energy feedstock for pyrolysis oil and biodiesel production. © 2016 Society of Chemical Industry.

Kinetics of the pyrolysis of arundo, sawdust, corn stover and switch grass biomass by thermogravimetric analysis using a multi-stage model.

A new multi-stage kinetic model has been developed for TGA pyrolysis of arundo, corn stover, sawdust and switch grass that accounts for the initial biomass weight (W0). The biomass were decomposed in a nitrogen atmosphere from 23°C to 900°C in a TGA at a single 20°C/min ramp rate in contrast with the isoconversion technique. The decomposition was divided into multiple stages based on the absolute local minimum values of conversion derivative, (dx/dT), obtained from DTG curves. This resulted in three decomposition stages for arundo, corn stover and sawdust and four stages for switch grass. A linearized multi-stage model was applied to the TGA data for each stage to determine the pre-exponential factor, activation energy, and reaction order. The activation energies ranged from 54.7 to 60.9 kJ/mol, 62.9 to 108.7 kJ/mol, and 18.4 to 257.9 kJ/mol for the first, second and the third decomposition stages respectively.

Microbial oxidation of naphthalene to cis-1,2-naphthalene dihydrodiol using naphthalene dioxygenase in biphasic media.

The selective oxidation of aryl substrates to chiral cis-1,2-dihydrodiols is an industrially important reaction for the production of intermediates that can be used to produce fine chemicals, pharmaceuticals, and many other bioactive natural products. More specifically, the oxidation of naphthalene to produce optically pure (+)-cis-(1R,2S)-1,2-napthalene dihydrodiol (NDHD) to be used as a chiral synthon for specialty chemicals has gained much interest. Escherichia coli JM109(DE3) pDTG141 expresses naphthalene dioxygenase which catalyzes this reaction. Poor substrate solubility and substrate toxicity are barriers to using the power of these enzymes in large-scale aqueous whole cell systems. A biphasic reaction system was chosen to overcome these barriers. The optimal biphasic conditions for E. coli JM109(DE3) pDTG141 were determined to be 20% dodecane as the organic solvent containing 40 g/L naphthalene. The productivity of the biotransformation using resting cells was 1.75 g-diol/g-cdw/h for the first 6 h with 20% organic phase, which was increased from 0.59 g-diol/g-cdw/h for growing cells with 40% organic phase. The biocatalytic activity was retained for at least 12 h. The biocatalyst could be recycled for at least four runs in both suspended and immobilized form. The stability of the 12 h recycle was improved by immobilization in calcium alginate beads. The process has been improved both environmentally and economically by reducing the amount of solvent used and by recycling the biocatalyst.