Scale-up of ethanol production from sugarcane usingZymomonas mobilis

Summary TheZymomonas fermentation for industrial ethanol production has been successfully scaled up. Pilot plant experiments at 100 and 1,000 litre fermentation capacity gave 91–95% conversion efficiencies and up to 10% (v/v) ethanol yields within 17–20 hours using sugar cane syrup, A-, B-, and C-molasses with the addition of sucrose or syrup to a final 15% total sugar concentration.     

The kinetics of ethanol production by Zymomonas mobilis on fructose and sucrose media

Summary Z.mobilis is strain ZM4 was grown on 250 g/l fructose and sucrose media in batch culture and on 100 and 150 g/l sucrose media in continuous culture. With fructose, a significant reduction in the growth rate and the cell yield was apparent although the other kinetic parameters were similar to those previously reported for fermentation of glucose. With sucrose the major differences were a reduction in ethanol yield, (due to levan formation) and a lower final ethanol concentration. Ethanol inhibition of sucrose metabolism occurred at relatively low ethanol concentrations compared to those inhibiting glucose metabolism.     

High fructose formation from sugarcane syrup and molasses usingZymomonas mobilis mutants

High fructose recovery yields were obtained using sugarcane syrup and C-molasses (equal to blackstrap molasses) and a fructokinase negative mutant ofZymomonas mobilis. The fructose recovery was 95.7% with sugarcane syrup and 99.4% with 300 g/L C-molasses or mixtures of both. High fructose corn syrup of a 48/52 mixture of glucose and fructose gave only a 65–70% fructose recovery due to high sorbitol formation.     

Raisin: A suitable rav material for ethanol production usingZymomonas mobilis

Summary A batch fermentation process for the production of ethanol from raisin usingZymomonas mobilis is described. This process shows significant advantages in ethanol production compared with yeasts, such as, faster fermentation time and higher ethanol productivity and yield. Moreover, fermentation of the raisin extracts byZ. mobilis gave three-fold higher ethanol productivity than of standard synthetic media of the same invert-sugar concentration.     

The production of ethanol from sucrose using Zymomonas mobilis

Summary A new single-batch fermentation process for the commercial production of ethanol from refined sucrose, raw sugar, sugar cane juice and sugar cane syrup has been developed using a highly adapted and efficient strain of Zymomonas mobilis. The process gives a 94–98% sucrose hydrolysis efficiency and a 95–98% ethanol conversion efficiency. Within 24–30 h, 200 g/l sucrose is converted to produce 95.5 g/l ethanol. Reinoculation is carried out from the fermented broth without the need for centrifugation or membrane filtration.     

Simultaneous ethanol production from lactose byKluyveromyces fragilis andZymomonas mobilis

Ethanol production from lactose byKluyveromyces fragilis NRRL 665 in monoculture and coculture with strains ofZymomonas mobilis was studied. One of the strains,Z. mobilis NRRL 1960, when cocultured withK. fragilis, produed 55.2 g/l of ethanol, whereasK. fragilis in monoculture procuded only 36 g/l ethanol from 200 g/l lactose medium. Increased Qp (g ethanol produced/g biomass/h) and Qs (g substrate consumed/g biomass/h) were observed in coculture than in monoculture. However, the residual sugar concentration increased in coculture; this increase might be due to the slow utilization rate of galactose.     

Continuous production of ethanol from fructose by immobilized growing cells of Zymomonas mobilis

Immobilized growing cells of Zymomonas mobilis were found to ferment rapidly and efficiently media containing 100 g/L fructose in a continuous reactor. A volumetric ethanol productivity of 94.8 g/L h was achieved at a substrate conversion of 75.5%. With 97% conversion of substrate the productivity was 28.4 g/L h. At fructose concentrations of 150 and 200 g/L substrate and product inhibitions limited the performance of the reactor. Ethanol production was constant over a period of 55 days.     

The production of ethanol plus fructose sweetener using fructose utilization negative mutants of Zymomonas mobilis

Summary Two mutants, unable to utilize fructose (Fru^–) as a sole source of carbon and energy, were isolated fromZymomonas mobilis following ethyl methane sulfonate (EMS) mutagenesis. The frequency of stable Fru^– mutants among survivors of mutagenesis was 1 in 10⁴. The two Fru^– mutants were able to cleave sucrose to glucose and fructose, and then ferment only the glucose to ethanol while accumulating fructose close to the theoretical value. Under controlled fermentation conditions, sucrose was converted to ethanol plus 80% or higher purity fructose syrup in a single-stage batch fermentation process, improving the Sucrotech Process significantly.     

Study of the production of fructose and ethanol from sucrose media by Saccharomyces cerevisiae

The production of ethanol and enriched fructose syrups from a synthetic medium with various sucrose concentrations using the mutant Saccharomyces cerevisiae ATCC 36858 was investigated. In batch tests, fructose yields were above 90% of theoretical values for the sucrose concentrations between 35 g/l and 257 g/l. The specific growth rates and biomass yields were from 0.218 to 0.128 h(-1) and from 0.160 to 0.075 g biomass/g of glucose and fructose consumed, respectively. Ethanol yields were in the range of 72 to 85% of theoretical value when sucrose concentrations were above 81 g/l. The volumetric ethanol productivity was 2.23 g ethanol/(l h) in a medium containing 216 g/l sucrose. Fructo-oligosaccharides and glycerol were also produced in the process. A maximum fructo-oligosaccharides concentration (up to 9 g/l) was attained in the 257 g/l sucrose medium in the first 7 h of the fermentation. These sugars started to be consumed when the concentrations of sucrose in the media were less than 30% of its initial values. The fructo-oligosaccharides mixture was composed of 6-kestose (61.5%), neokestose (29.7%) and 1-kestose (8.8%). The concentration of glycerol produced in the process was less than 9 g/l. These results will be useful in the production of enriched fructose syrups and ethanol using sucrose-based raw materials.     

Effect of fructose and glucose supplementation on invertase mediated synthesis of oligosaccharides from sucrose

Summary The total amount of novel oligosaccharides synthesized by -D-fructofuranosidase at pH 7.5 increased three-fold using a medium composed of 1.2M sucrose, 0.5M fructose and 0.1M glucose, as compared to that with only 1.8M sucrose solution. Using 0.6M of the three sugars did not increase yield but reduced rate of sucrose hydrolysis by 72.7%. Synthesis of fructosyl/glucosyl oligosaccharides based on -fructofuranosidase mediated transglycosylation is enhanced by supplementation of sucrose solution with appropriate concentrations fructose and glucose.     

Ethanol production from sucrose by immobilizedZymomonas mobilis cells in polyurethane foam

Summary The possibility of using polyurethane foam as a support for the immobilization ofZymomonas mobilis cells to carry out sucrose conversion to ethanol was investigated. Sucrose hydrolysis efficiencies of 90% and higher, volumetric reactor productivity of 20 gL^–1h^–1 and final ethanol concentration of 6.3% (v/v) at a dilution rate of 0.4 h^–1 show the good performance of polyurethane foams for whole cell immobilization.     

Rapid ethanol production from sucrose without by-product formation

Summary Non-sorbitol-producing Zymomonas mobilis ACM 3963 was developed from Z. mobilis UQM 2716. This strain was co-immobilised with invertase in alginate and incubated on sucrose-based media. This combination allowed theoretical yields of ethanol to be produced from 100 and 150 g/l sucrose, using both semi-defined media and sugar-cane syrup. No sorbitol or fructo-oligosaccharides were formed in either fermentation. Increased biomass concentrations immobilised in alginate reduced the batch fermentation times of 100 and 150 g/l sucrose by 50–70%, to 3 and 5 hours respectively. This strain also improved the efficiency of the fed-batch fermentation of sucrose.     

Regulation of invertase levels in Avena stem segments by gibberellic Acid, sucrose, glucose, and fructose

Gibberellic acid and sucrose play significant roles in the increases in invertase and growth in Avena stem segments. About 80% of invertase is readily solubilized, whereas the rest is in the cell wall fraction. The levels of both types of invertase change in a similar manner in the response to gibberellic acid and sucrose treatment. The work described here was carried out with only the soluble enzyme. In response to a treatment, the level of invertase activity typically follows a pattern of increase followed by decrease; the increase in activity is approximately correlated with the active growth phase, whereas the decrease in activity is initiated when growth of the segments slows. A continuous supply of gibberellic acid retards the decline of enzyme activity. When gibberellic acid was pulsed to the segments treated with or without sucrose, the level of invertase activity increased at least twice as high in the presence of sucrose as in its absence, but the lag period is longer with sucrose present. Cycloheximide treatments effectively abolish the gibberellic acid-promoted growth, and the level of enzyme activity drops rapidly. Decay of invertase activity in response to cycloheximide treatment occurs regardless of gibberellic acid or sucrose treatment or both, and it is generally faster when the inhibitor is administered at the peak of enzyme induction than when given at its rising phase. Pulses with sucrose, glucose, fructose, or glucose + fructose elevate the level of invertase significantly with a lag of about 5 to 10 hours. The increase in invertase activity elicited by a sucrose pulse is about one-third that caused by a gibberellic acid pulse given at a comparable time during mid-phase of enzyme induction, and the lag before the enzyme activity increases is nearly twice as long for sucrose as for gibberellic acid. Moreover, the gibberellic acid pulse results in about three times more growth than the sucrose pulse. Our studies support the view that gibberellic acid, as well as substrate (sucrose) and end products (glucose and fructose), play a significant role in regulating invertase levels in Avena stem tissue, and that such regulation provides a mechanism for increasing the level of soluble saccharides needed for gibberellic acid-promoted growth.     

A new biosensor for specific determination of sucrose using an oxidoreductase of Zymomonas mobilis and invertase

A new biosensor for specific determination of sucrose was developed using an oxidoreductase of Zymomonas mobilis and invertase. Cells of Z. mobilis were permeabilized with toluene in order to utilize the enzymes of glucose-fructose oxidoreductase and gluconolactonase inside the intact cells. Permeabilized cells and invertase were coimmobilized in a gelatin membrane, and a whole cell enzyme electrode was constructed by fixing the membrane on a pH electrode. The production of hydrogen ion was detected using the biosensor-connected microcomputer, and the concentration of sucrose was determined by using both the initial rate and the steady-state methods. Optimum conditions for biosensor response were pH 6.2 and temperature 35 degrees C. The effect of interfering compounds on the electrode response was investigated, and the interference by various sugars was eliminated by determining sucrose concentration using the steady-state method. The biosensor developed is simple and reproducible, and the calibration curve for sucrose is linear up to 70 g/L.     

Continuous ethanol production from sago starch using immobilized amyloglucosidase and Zymomonas mobilis

To produce ethanol more economically than in a conventional process, it is necessary to attain high productivity and low production cost. To this end, a continuous ethanol production from sago starch using immobilized amylogucosidase (AMG) and Zymomonas mobilis cells was studied. Chitin was used for immobilization of AMG and Z. mobilis cells were immobilized in the form of sodium alginate beads. Ethanol was produced continuously in an simultaneous saccharification and ethanol fermentation (SSF) mode in a pacekd bed reactor. The maximum ethanol productivity based on the void volume, V_v, was 37 g/l/h with ethanol yield, Y_p/s, 0.43 g/g (84% of the theoretical ethanol yield) in this system. The steady-state concentration of ethanol (46 g/l could be maintained in a stable manner over two weeks at the dilution rate of 0.46 h⁻.     

Comparison of ethanol production by Zymomonas mobilis from sugar beet substrates

Summary The potential of four sugar beet substrates from the sugar industry [syrup (S), crystallizer effluent 1 (CE1), crystallizer effluent 2 (CE2) and molasses (M)] were compared for ethanol production using an osmotolerant mutant strain of the bacterium Zymomonas mobilis. Sucrose of the substrates was enzymatically hydrolysed to avoid levan formation during fermentation. Nutrient supplementation experiments have shown that reproducible growth and ethanol production could be obtained on the four substrates supplemented only with magnesium sulphate (CE2 and M) or additionally with ammonium sulphate (S and CE1). Thus, addition of costly yeast extract could be avoided. All 20% (w/v) substrates showed nearly complete sugar conversion (>94.9%), good growth (0.16 h^–1) and ethanol production (>40 g 1^–1). However, sorbitol formation reduced the ethanol yield (73–79% of the theoretical value) significantly. Batch kinetic parameters and studies of instantaneous parameters showed that enhanced osmolality of substrates (SZ. mobilis with appropriate supplementation. Offprint requests to: J. Baratti     

Kinetic control of ethanol production by Zymomonas mobilis

Summary Zymomonas mobilis UQM 2716 was grown anaerobically in continuous culture (D = 0.1/h; 30° C) 3nder glucose or nitrogen limitation at pH 6.5 or 4.0. The rates of glucose consumption and ethanol production were lowest during glucose-limited growth at pH 6.5, but increased during growth at pH 4.0 or under nitrogen limitation, and were highest during nitrogen-limited growth at pH 4.0. The uncoupling agent CCCP substantially increased the rate of glucose consumption by glucose-limited cultures at pH 6.5, but had much less effect at pH 4.0. Washed cells also metabolised glucose rapidly, irrespective of the conditions under which the original cultures were grown, and the rates were variably increased by low pH and CCCP. Broken cells exhibited substantial ATPase activity, which was increased by growth at low pH. It was concluded that the fermentation rates of cultures growing under glucose or nitrogen limitation at pH 6.5, or under glucose limitation at pH 4.0, are determined by the rate at which energy is dissipated by various cellular activities (including growth, ATP-dependent proton extrusion for maintenance of the protonmotive force and the intracellular pH, and an essentially constitutive ATP-wasting reaction that only operates in the presence of excess glucose). During growth under nitrogen limitation at pH 4.0 the rate of energy dissipation is sufficiently high for the fermentation rate to be determined by the inherent catalytic activity of the catabolic pathway.Abbreviations CCCP carbonyl cyanide p-trifluoromethoxyphenylhydrazone - qG rate of glucose consumption (g glucose/g dry wt cells/h) - qE rate of ethanol production (g ethanol/g dry wt cells/h) - Y growth yield (g dry wt cells/g glucose) - D dilution rate Offprint requests to: C. W. Jones