Removing the by-products acetic acid and NH 4 + from the l -tryptophan broth by vacuum thin film evaporation during l -tryptophan production

Pulsed-Laser-Driven CO2 Reduction Reaction for the Control of the Photoluminescence Quantum Yield of Organometallic Gold Nanocomposites

Over the last decade, the CO2 reduction reaction (CO2RR) has been increasingly exploited for the synthesis of high-value raw materials in gaseous or liquid form, although no examples of CO2 fixation in nanoparticle systems have been demonstrated. Herein, CO2 fixation into solid nanomaterials by laser synthesis and processing of gold colloids in water, traditionally considered a green approach leading to ligand-free nanoparticles without the formation of by-products, is reported. If carbon monoxide-rich gold nanoparticles are observable even after synthesis in deionized water, the presence of CO2 derivatives in alkaline water environment leads to C 2 and C 3 coupling with the production of carboxylic acids as a typical CO2RR fingerprint. While laser processing of preformed gold colloids is selective for C 2 coupling, both C 2 and C 3 coupling to lactic acid are observed during pulsed laser ablation of a gold target. In the latter case, it is demonstrated that it is possible to synthesize photoluminescent organometallic nanocomposites in the blue spectral region with a quantum yield of about 20% under adequate experimental conditions. In this research, new pathways are offered to be explored in energetics, photonics, catalysis, and synthesis at the nanoscale.

Engineering for life in toxicity: Key to industrializing microbial synthesis of high energy density fuels

With the growing demand for air transportation combined with global concerns about environmental issues and the instability and lack of renewability of the oil market, microbial production of high energy density fuels for jets (bio-jet fuels) has received more attention in recent years. Bio-jet fuels can be derived from both isoprenoids and fatty acids, and, additionally, aromatic hydrocarbons derived from expanded shikimate pathways are also candidates for jet fuels. Compared to fatty acid derivatives, most of isoprenoids and aromatic hydrocarbons used for jet fuels have higher density energies. However, they are also highly toxic to host microbes. The cytotoxicity induced during the synthesis of isoprenoid or shikimate pathway-derived biofuels remains one of the major obstacles for industrial production even though synthetic and systems biology approaches have reconstructed and optimized metabolic pathways for production of these bio-jet fuels. Here, we review recent developments in the production of known and potential jet fuels by microorganisms, with a focus on alleviating cytotoxicity caused by the final products, intermediates, and metabolic pathways.

Effects of Methyl Donors on L-Tryptophan Fermentation

Methyl donors, a class of compounds that supply methyl groups to methyl acceptors, play important roles in the function, growth, and proliferation of cells; however, the methyl donor content in cells is not sufficient to meet their normal needs. In L-tryptophan production with E. coli, the growth and acid-producing ability of E. coli cells are weak due to the presence of exogenous plasmids that inhibit the growth of E. coli, and reduce the efficiency of exogenous gene expression. Therefore, the effect of methyl donors on L-tryptophan production was investigated. Among the methyl donors tested, choline chloride showed the most significant effect in promoting fermentation, followed by methionine. The optimum addition method involved the addition of 1.5 g/L methionine to the culture medium, combined with continuous feeding with a glucose solution containing 1 g/L choline chloride. The final tryptophan titer reached 53.5 g/L; the highest biomass of bacteria reached 51.8 g/L; and the main by-product, acetic acid, was reduced to 2.23 g/L, which had a significant impact on the fermentation results.

Using enzymatic hydrolyzate as new nitrogen source for L-tryptophan fermentation by E.coli

This study presents new methods for hydrolyzing bacterial cell in cyclic utilization of waste bacterial cell for L-tryptophan production by fermentation. Using enzymatic hydrolysis of the pre-treated bacterial cells which were collected from an L-tryptophan fermentation broth, trypsin was selected as the optimal protease for hydrolyzing the bacterial cell. The optimum conditions for hydrolysis were determined by the orthogonal test. Hydrolyzate was then dealt with a compound protease to further increase its content of free amino acids. With the optimum conditions of pH = 8, temperature of 37°C, treatment time of 6 h, and E/S of 4%, the final content of free amino acids in the hydrolyzate was 500.61 mg/g. The hydrolyzate and the yeast extract were added to the medium at the proportion of 1:1, which served as an organic nitrogen source for L-tryptophan production by fermentation. The production of L-tryptophan was 53.87 g/L, and the highest biomass was 53.45 g/L. As an organic nitrogen source, this hydrolyzate satisfies the requirements for L-tryptophan production by fermentation.

Hydrolysing the soluble protein secreted by Escherichia coli in trans-4-hydroxy-L-proline fermentation increased dissolve oxygen to promote high-level trans-4-hydroxy-L-proline production

Trans-4-hydroxy-L-proline (Hyp) production by Escherichia coli (E. coli) in fermentation is a high-oxygen-demand process. E. coli secretes large amounts of soluble protein, especially in the anaphase of fermentation, which is an important factor leading to inadequate oxygen supply. And acetic acid that is the major by-product of Hyp production accumulates under low dissolved oxygen (DO). To increase DO and achieve high-level Hyp production, soluble protein was hydrolysed by adding protease in Hyp fermentation. The optimal protease, concentration, and addition time were trypsin, 0.2 g/L, and 18 h, respectively. With the addition of trypsin, the soluble protein in Hyp fermentation decreased by 43.5%. The DO could be maintained at 20–30% throughout fermentation. Hyp production and glucose conversion rate were 45.3 g/L and 18.1%, which were increases of 24.1% and 8.4%, respectively. The accumulation of acetic acid was decreased by 52.1%. The metabolic flux of Hyp was increased by 44.2% and the flux of acetate was decreased by 51.0%.