Co-carbon Sources Research Articles

Dynamic flux balance analysis for pharmaceutical protein production by Pichia pastoris: Human growth hormone

The influence of methanol feeding rate on intracellular reaction network of recombinant human growth hormone (rhGH) producing Pichia pastoris was investigated at three different specific growth rates, namely, 0.02 (MS-0.02), 0.03 (MS-0.03), and 0.04h−1 (MS-0.04) where Period-I (33≤t<42h) includes the early exponential growth phase; Period-II (42≤t<48h) is the exponential growth phase where the specific cell growth rate decreases; Period-III (48≤t≤51h) is the exponential growth phase where rhGH concentration was the highest; and Period-IV (t>51h) is the diminution phase for rhGH and cell synthesis. In Period-I, almost all of the formaldehyde entered the assimilatory pathway, at MS-0.02 and MS-0.03, whereas, at MS-0.04 high methanol feeding rate resulted in an adaptation problem. In Period-III, only at MS-0.02 co-carbon source sorbitol uptake-flux was active showing that sorbitol uptake does not affected from the predetermined feeding rate of methanol at μ0>0.02h−1. The biomass synthesis flux value was the highest in Period-I, -II and -III, respectively at MS-0.03 & MS-0.04, MS-0.04 and MS-0.02; whereas, rhGH flux was the highest in Period-I, -II, and -III, respectively at MS-0.03, MS-0.02 and MS-0.03. Based on the fluxes, Period-I should start with MS-0.03 methanol feeding rate and starting from the middle of Period-II methanol feeding rate should be shifted to MS-0.02.

Biosynthesis and mobilization of a novel polyhydroxyalkanoate containing 3-hydroxy-4-methylvalerate monomer produced by Burkholderia sp. USM (JCM15050)

We attempted to synthesize a polyhydroxyalkanoate (PHA) containing newly reported 3-hydroxy-4-methylvalerate (3H4MV) monomer by using wild type Burkholderia sp . USM (JCM15050) and its transformed strain harboring the PHA synthase gene of Aeromonas caviae ( phaC Ac ). The introduction of 3H4MV as a second monomer will improve the material properties of 3HB-based polymers. To promote the accumulation of PHA containing 3H4MV monomer, isocaproic acid was provided as co-carbon source. Approximately 1 mol% of 3H4MV was detected in wild type Burkholderia sp. cultures when they were fed glucose or fructose together with isocaproic acid. Thus, the wild type strain can synthesize the 3H4MV monomer. High 3H4MV fractions, of about 40 mol%, were obtained when the transformed strain was cultivated on glucose or fructose together with isocaproic acid. In addition, the ability of the transformed strain to mobilize accumulated PHA containing 3H4MV monomer was demonstrated in this study. This is the first report on mobilization of the 3H4MV monomer.

Enhanced production of longer side-chain polyhydroxyalkanoic acid with ω-aromatic group substitution in phaZ-disrupted Pseudomonas fluorescens BM07 mutant through unrelated carbon source cometabolism and salicylic acid β-oxidation inhibition

The deletion of the intracellular polyhydroxyalkanoate (PHA) depolymerase gene (phaZ) in Pseudomonas fluorescens BM07 was found to increase more efficiently the levels of longer medium-chain-length (MCL) ω-aromatic monomer-units than in the wild-type strain when the cells were grown with a mixture of fructose and MCL ω-aromatic fatty acid in the presence of salicylic acid that is known as a β-oxidation inhibitor in BM07 strain. When 11-phenoxyundecanoic acid was used as co-carbon source, the longest monomer-unit 3-hydroxy-11-phenoxyundecanoate, not reported in literature yet, was incorporated into the polymer chain up to ∼10mol%. An advantage of salicylic acid inhibition technique is that salicylic acid is not metabolized in BM07 strain, thus, the effective concentration of the inhibitor remaining constant throughout the cultivation. In conclusion, this new technique could be exploited for the enhanced production of side-chain modulated functional MCL–PHA with improved physicochemical properties in P. fluorescens BM07.

Enhanced cutinase production of Thermobifida fusca by a two-stage batch and fed-batch cultivation strategy

In this study, cutinase production by Thermobifida fusca WSH03-11 was investigated with mixed short-chain organic acids as co-carbon sources to demonstrate the possibility of producing high value-added products from organic wastes. T. fusca WSH03-11 was cultured with different combinations of butyrate, acetate, and lactate with a purpose of increasing cutinase activity. The optimum proportion of butyrate, acetate, and lactate was 4:1:3. In batch cultivation, acetate and lactate were consumed quickly, while the consumption of butyrate was depressed in the presence of acetate with a concentration higher than 0.5 g/L. Based on these results, a two-stage batch and fed-batch cultivation strategy was proposed: a batch culture with acetate and lactate as the co-carbon sources in the first 10 h, and then a fed-batch culture with a constant butyrate feeding rate of 12 mL/h during 11∼20 h. By this two-stage cultivation strategy, cutinase activity, dry cell weight, and consumption rate of butyrate were increased by 70%, 103.4%, and 4.3-fold, respectively, compared to those of the batch cultivation. These results provided a novel and efficient way to produce high value-added products from organic wastes.

Bacterial synthesis of poly(hydroxybutyrate- co-hydroxyvalerate) using carbohydrate-rich mahua (Madhuca sp.) flowers

The objective of the present work was to utilize an unrefined natural substrate namely mahua (Madhuca sp.) flowers, as a carbon source for the production of bacterial polyhydroxyalkanoate (PHA) copolymer by Bacillus sp-256. In the present work, three bacterial strains were tested for PHA production on mahua flower extract (to impart 20 g l(-1) sugar) amongst which, Bacillus sp-256 produced higher concentration of PHA in its biomass (51%) compared with Rhizobium meliloti (31%) or Sphingomonas sp (22%). Biosynthesis of poly(hydroxybutyrate-co-hydroxyvalerate) - P(HB-co-HV)--of 90 : 10 mol% by Bacillus sp-256 was observed by gas chromatographic analysis of the polymer. Major component of the flower is sugars (57% on dry weight basis) and additionally it also contains proteins, vitamins, organic acids and essential oils. The bacterium utilized malic acid present in the substrate as a co-carbon source for the copolymer production. The flowers could be used in the form of aqueous extract or as whole flowers. PHA content of biomass (%) and yield (g l(-1)) in a 3.0-l stirred tank fermentor after 30 h of fermentation under constant pH (7) and dissolved oxygen content (40%) were 54% and 2.7 g l(-1), respectively. Corresponding yields for control fermentation with sucrose as carbon source were 52% and 2.5 g l(-1). The polymer was characterized by proton NMR. Utilization of mahua flowers, a natural substrate for bacterial fermentation aimed at PHA production, had additional advantage, as the sugars and organic acids present in the flowers were metabolized by Bacillus sp-256 to synthesize P(HB-co-HV) copolymer. Literature reports on utilization of suitable cheaper natural substrate for PHA copolymer production is scanty. Mahua flowers used in the present experiment is a cheaper carbon substrate compared with several commercial substrates and it is rich in main carbon as well as co-carbon sources that can be utilized by bacteria for PHA copolymer production.

Speculations on industrial electrochemistry

Large-scale electrochemical processes are commonly used where ionic raw materials are converted into finished products that are either metals or covalently bound. Examples are aluminium production and the chlor-alkali industry. In a few cases they are used to carry out chemically difficult processes such as acrylonitrile dimerization. The advances in electrochemistry and the related electrochemical engineering, coupled with sharply increased energy costs, have led to a new appraisal of electrochemistry in the chemical process industries. It seems likely that the novel electrochemical routes will emerge in situations where the special advantages of electrochemistry such as energy specificity, absence of toxic and reactive intermediates, chemical selectivity, and specific activation of small molecules can be applied. Examples of this will possibly come in the production of chlorine chemicals, nitrogen chemicals, use of CO and CO 2 as carbon sources, and in selective oxidation processes that permit combined production of chemical intermediates and electrical energy.