Kinetic studies on alac-containing strain ofZymomonas mobilis

Summary Batch and continuous culture studies have been carried out on a strain ofZ.mobilis (ZM6306) which can convert lactose directly to ethanol. Previous strain development has established that thelac operon encoded on the transposon Tn951 can be expressed inZ.mobilis. Using a medium containing 80 g/l glucose and 40 g/l lactose, it was found that strain ZM6306 could convert about 13 g/l lactose to 4 g/l ethanol and 6 g/l galactose in continuous culture. Further lactose conversion is likely with increased cell concentration using a cell recycle system.     

The effect of temperature,pH, and initial glucose concentration on the kinetics of ethanol production by Zymomonas mobilis in batch fermentation

Summary Zymomonas mobilis, strain ATCC 10988, was used to evaluate the effects of pH (5.0 to 8.0), temperature (30°C to 40°C), and initial glucose concentration (75 g/l to 150 g/l) on the kinetics of ethanol production from glucose using batch fermentation. Specific ethanol production rate was maximum and nearly constant over a pH range of 6.0 to 7.5. End-of-batch ethanol yield and specific growth rate were insensitive to pH in the range of 5.0 to 7.5. End-of-batch ethanol yield was maximum and nearly constant between 30°C and 37°C but decreased by 24% between 37°C and 40°C. All other kinetic parameters are greatest at 34°C. End-of-batch ethanol yield is maximum at an initial glucose concentration of 100 g/l. Specific growth rate reaches a maximum at 75 g/l, but specific ethanol production rate decreases throughout the range. The optimum initial glucose concentration of 100 g/l gives the highest ethanol yield at a specific ethanol production rate less than 10% below the maximum observed.     

Influence of pH and undissociated butyric acid on the production of acetone and butanol in batch cultures of Clostridium acetobutylicum

Summary The kinetics of growth and acid and solvent production are examined in batch fermentation of Clostridium acetobutylicum at pH between 4.5 and 6.0. At the lower pH, growth occurs in two consecutive phases and solvents are the main excreted metabolites. At the higher pH, there is a single growth phase with only acid formation. The influence of the pH can be correlated with a critical role of the concentration of undissociated butyric acid in the medium: cellular growth is inhibited above 0.5 g/l and solvent production starts at an undissociated acid level of 1.5 g/l. Reducing the intracellular acid dissociation by lowering the intracellular pH also favours the production of acetone and butanol.     

Vertical Rotating Immobilized Cell Reactor of the bacteriumZymomonas mobilis for stable long-term continuous ethanol production

Summary Vertical Rotating Immobilized Cell Reactor was designed and built for glucose conversion into ethanol. Immobilized biomass units withZ. mobilis cells attached into polyurethane foam discs were fixed along a rotating shaft inside the bioreactor. The effect of rotation speed on the concentration of immobilized biomass was studied. Stability of the bioreactor over long-term operation was dependent on the concentration of the immobilized biomass. With fermentation carried out at 6 rpm a constant active immobilized cell concentration of only 34.5 g/l was maintained and used to convert up to 140 g glucose/l into more than 70 g ethanol/l with a volumetric ethanol productivity of 63 g/l/h.     

An investigation of ethanol inhibition and other limitations occurring during the fermentation of concentrated whey permeate byKluyveromyces fragilis

Based on the well-known fact thatKluyveromyces fragilis strains show sub-optimal performance when grown in concentrated whey permeate, previously optimized medium was investigated for possible limitations appearing at high concentrations. Shaken flask cultures showed that no additional vitamin or mineral sources were required when the optimized amount of yeast extract was added to the concentrated permeate. Several aspects of the ethanol inhibition of the growth ofK. fragilis NRRL 665 were investigated in continuous culture. The maximum ethanol concentration tolerated by this yeast, i.e. 45 g/l, was much lower than commonly reported for other strains. Ethanol and biomass production were also influenced by the increased ethanol concentration of the medium. At 31 g/l of alcohol product yield was reduced to 0.23 g/g whereas biomass yield was 0.05 g/g. Some evidence suggested that residence time and residual lactose concentration played a significant role in modulating the toxic effect of ethanol.     

Fermentation of starch to ethanol by a complementary mixture of an amylolytic yeast andSaccharomyces cerevisiae

Summary Synergistic coculture of an amylolytic yeast (Saccharomycopsis fibuligera) andS. cerevisiae, a non-amylolytic yeast, fermented unhydrolyzed starch to ethanol with conversion efficiencies over 90% of the theoretical maximum. Fermentation was optimal between pH 5.0 to 6.0. Using a starch concentration of 10% (w/v) and a 5% (v/v) inoculum ofS. fibuligera, increasingS. cerevisiae inoculum from 4% to 12% (w/v) resulted in 35–40% (w/v) increase in ethanol yields. Anaerobic or limited aerobic incubation almost doubled ethanol yields.     

Hydrolysis of cellulose in fed-batch culture by Cl. thermocellum: A way to increase speed of cellulose hydrolysis

Summary Fed batch fermentation ofClostridium thermocellum gives improved conversion rates and high ethanol concentration in the broth; 8.5 g/l of ethanol were obtained in 60 hours with a maximum ethanol productivity of 1.0 g/l h.     

Ethanol production from Jerusalem artichoke juice using flocculent cells of Kluyveromyces marxianus

Summary Flocculent cells ofKluyveromyces marxianus SM 16-10 were used for batch production of ethanol from the inulin sugars derived from Jerusalem artichoke tubers. Using 20% initial sugar concentration, a maximum ethanol concentration of 92 g/l was achieved in 7 h, when the flocculent cell concentration was 30 g dry wt./l bioreactor volume. The same flocculent cells were used repeatedly for 7 batch runs starting with fresh medium at the beginning of each run. The ethanol yield was found to be almost constant at about 94% of the theoretical for all the 7 batch cycles, while the maximum ethanol production rate increased from 17.21 g ethanol/1/h during the first batch run to 21 g ethanol/1/h during the last batch run.     

Glycerol production by immobilised cells of Pichia farinosa

Summary Cells ofPichia farinosa were immobilised in calcium alginate and K-Carrageenan and their ability to produce glycerol from glucose under aerobic conditions with acidic as well as alkaline pH was investigated. An average glycerol production rate of 0.07 g/l.h was obtained with immobilised cells (IMC) in shake flasks. Continuous glycerol production in a fluidised bed reactor (FBR) under steady state operation gave a glycerol concentration of 13.5 g/l in the product stream.     

Ethanol production byClostridium thermocellum SS8, a newly isolated thermophilic bacterium

Summary Clostridium thermocellum SS8, has a broad substrate spectrum. It produced 0.25–0.29 g. of ethanol per g. of cellulose consumed. Cellulose fermentation was repressed by both glucose and cellobiose. pH had an effect on ethanol productivity at high substrate concentration. Best results were obtained at 30 g/l with an E/S and E/A ratios of 0.29 and 2.4 respectively.     

Optimisation of L-lysine production byCorynebacterium sp in fed-batch cultures

Summary The influence of initial concentration of glucose from 60 to 233 g/l on the production of L-lysine byCorynebacterium sp was studied first in batch culture. The maximum conversion rate into L-lysine was obtained at 165 g/l and the best specific production rate for L-lysine was observed at 65 g/l of glucose. In fed-batch fermentations, better conversion and the specific production rates were obtained. Maintaining of a high glucose concentration in the fed-batch technique allowed a 54% increase of the L-lysine production compared to the batch culture.     

High productivity continuous ethanol fermentation with a flocculating mutant strain of Zymomonas mobilis

High fermenter (volumetric) ethanol productivities (80 g/lh^–1) were attained in a simple single-stage continuous-stirred-tank-reactor (CSTR) employing a flocculent mutant of Zymomonas mobilis with a feed containing 100g/l glucose. Under these conditions a final ethanol concentration of 47.6 g/l was obtained, representing a maximum conversion efficiency of 97% of theoretical.Nomenclature SR = Medium glucose concentration (g/l)X Biomass concentration (g/l) - P Ethanol concentration (g/l) - VP Volumetric productivity (g ethanol/l/h) - Yp/s Product yield coefficient (g ethanol/g glucose consumed) - Qp Specific rate of ethanol formation (g ethanol/g cells/h) - D Dilution rate (h^–1) - Dmax Maximum dilution rate: ie., highest dilution rate at which the effluent glucose concentration 4g/l (h^–1)     

Selective production of phenylalanine from phenylpyruvate using growing cells ofCorynebacterium glutamicum

Summary Phenylalanine was produced from phenylpyruvate by growing cells of a mutant strain ofCorynebacterium glutamicum over-producing valine. A defined medium was used to minimize the accumulation of valine. The maximum phenylalanine concentration achieved was 44.5 mM (7.5 g/l) with a phenylpyruvate molar conversion of 75%.     

Production of L-DOPA from pyrocatechol and DL-serine by bioconversion using immobilized Erwinia herbicola cells

Summary Immobilized cells of Erwinia herbicola were used for L-DOPA production from pyrocatechol and DL-serine. Optimal conditions have been defined and utilized in batch and continuous reactors. A maximal volumetric productivity of 0.46 g/l.h in L-DOPA was obtained with a conversion yield of 18% (L-DOPA concentration 2.3 g/l).     

Microbial production of 2,3-butanediol from whey permeate

Summary Of four organisms tested in semi-synthetic medium for the production of 2,3-butanediol from lactose, Klebsiella pneumoniae N.C.I.B. 8017 proved to be the most promising. When tested using rennet whey permeate as substrate, a butanediol concentration of 7.5 g/l, representing a yield of 0.46 g/g lactose utilized, was observed after 96 h incubation. In whey permeate where the lactose had been hydrolysed enzymatically prior to the fermentation, a butanediol concentration of 13.7 g/l, representing a yield of 0.39 g/g sugar utilized was obtained. These results indicate that lactose utilization may be a limiting step in the fermentation process.     

Continuous production of ethanol from a glucose,xylose and arabinose mixture by a flocculent strain ofPichia stipitis

Summary Enhanced rates of continuous ethanol production by a flocculent strain ofPichia stipitis from a sugar mixture (xylose 75%, glucose 20%, arabinose 5%) were attained using a single-stage gas lift tower fermentor. With a substrate feed of 50g/l, the biomass accumulated at a level near 50g/l, showed a maximum and stable ethanol productivity of 10.7 g/l.h, with a substrate conversion of 80%; the ethanol yield reached 0.41g/g. In these operating conditions, similar performances were obtained when D.xylose alone was supplied.     

D-malic acid production from DL-malic acid by enantiospecific assimilation with Acinetobacter lwofii

Summary Acinetobacter lwofii ATCC 9036 assimilated L-malic acid eantiospecifically and left D-malic acid when grown in a medium containing DL-malic acid. The optical purity of the D-malic acid isolated from the culture filtrate was 100%. When the organism was incubated at 26°C, 220 r.p.m. in a Erlenmeyer flask containing 100g/l of disodium maleate, L-malic acid was completely consumed during 7 days incubation and D-malic acid remained at the concentration of 35g/l.     

Growth ofSchizosaccharomyces sp. HL on supernatant from anaerobically fermented pig waste: Effects of VFA concentration and pH

Summary Schizosaccharomyces sp. HL utilized almost all of the volatile fatty acids (VFA) up to concentrations of 9.3 g/l in the surface culture using supernatant from anaerobically fermented pig waste as medium. The maximum yield of dry matter (DM) was 5.8 g/l in the optimum conditions of 9.3 g/l VFA, pH 5.1 and 29°C. Lowering of pH was required to obtain the maximum yield of yeast DM, and the optimum pH value rose as the VFA concentration increased.     

The effect of aeration on D-xylose fermentation byPachysolen tannophilus,Pichia stipitis,Kluyveromyces marxianus andCandida shehatae

Summary The fermentation of D-xylose byPachysolen tannophilus Y2460,Pichia stipitis Y7124,Kluyveromyces marxianus Y2415 andCandida shehatae Y12878 was investigated in aerobic, anaerobic and microaerophilic batch cultures. The aeration rate greatly influenced the fermentations; growth, rate of ethanol production and oxidation of ethanol are affected. Of the strains tested,Pichia stipitis appears superior; under anaerobic conditions it converts D-xylose (20 g/l) to ethanol with a yield of 0.40 g/l and it exhibits the highest ethanol specific productivity (3.5 g of ethanol per g dry cell per day) under microaerophilic conditions.     

Potential of Datura innoxia cell suspension cultures for glucosylating hydroquinone

The efficiency of glucosylation of hydroquinone by Datura innoxia cell suspension cultures was investigated. The yield of arbutin was 2.4 g/l medium when 10 mM of hydroquinone was added to a suspension culture that was then incubated for 24 h, but the yield decreased at a higher concentration. This decrease, which could not be overcome by changing the growth phase or increasing the cell density used, could be avoided by the repeated addition of a low concentration of hydroquinone over 3 days. This increased the yield of arbutin to 4.2 g/l at the usual cell density and to 7.1 g/l at a high density. The kinetics of this reaction were explained by the Michaelis-Menten formula. The theoretical maximum velocity of the arbutin-forming reaction was estimated as 0.77 mg/h/g. The velocity increased linearly up to a cell density of 300 g/l under standard aeration, the theoretical maximum yield of arbutin being calculated to be 5.5 g/l/day.