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)     

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.     

pH influence on ethanol production and retained biomass in a passively immobilizedZymomonas mobilis system

Summary A broad pH range of 4.5–7.5 for maximum ethanol productivity and ethanol yield was observed with a passively immobilizedZ. mobilis system. Total retained biomass (as suspended flocs and entrapped cells) was >50 g/l for medium pH values between 4.0–8.0. The entrapped cells to suspended flocs ratio was highest at pH 4.0, whereas at pH above 5.2 it was close to 1.0. The observed enhancement of cell immobilization on the packing support at low pH seemed to be related to formation of bacterial filaments.     

Batch and membrane-assisted cell recycling in ethanol production byCandida shehatae

Summary During xylose fermentation byCandida shehatae ATCC 22984 with batch cell recycling, the volumetric ethanol fermentation rate increased two-fold, and the xylitol production rate increased three-fold as the cell density increased to ten-fold. In continuous fermentation with membrane-assisted cell recycle, the fermentation rates increased almost linearly with increasing agitation rates up to 300 rpm. The maximum continuous ethanol production rates obtained with 90 and 200 g L^–1 xylose were respectively 2.4 and 4.4 g L^–1h^–1. The cell density was 65–70 g (dry wt) L^–1. Ethanol yields ranged from 0.26 to 0.41 g g^–1.     

Direct fermentation of cellodextrins to ethanol byCandida wickerhamii andC. Lusitaniae

Summary Production of ethanol from cellodextrins, as large as cellohexose, byCandida lusitaniae andC. wickerhamii was studied.C. lusitaniae fermented only glucose and cellobiose, whereasC. wickerhamii efficiently fermented cellodextrins. Maximum ethanol yields of 29.2 g/liter from 54 g/liter cellodextrins were achieved byC. wickerhamii in 3–4 days.     

A simple culture method for Brassica hypototyl protoplasts

Hypocotyl protoplasts from oil rape, Brassica napus L. cv. Isuzu were cultured in the dark at 25°C in a modified Nitsch and Nitsch medium containing 13% sucrose, 5 g/l Ficoll, 0.5 mg/l BAP, 1 mg/l NAA and 0.5 mg/l 2–4 D. Protoplasts floated on the surface of the medium and developed into microcolonies 0.5 mm in diameter in 4–6 weeks. The microcolonies also remained on the surface of the medium. Transfer to MS medium supplemented with 200 mg/l casein hydrolysate, 5mg/l BAP, 0.5 mg/l NAA and solidified with 0.6% agarose induced shoot regeneration in 3–4 weeks.Abbreviations BAP 6-benzylaminopurine - NAA 1-naphthaleneacetic acid - 2,4-D 2,4 — dichlorophenoxyacetic acid     

Ethanol production by Zymomonas mobilis CP4 from sugar cane chips

Summary The fermentation of large sugar cane chips (1.0–1.5 in) to ethanol by Zymomonas mobilis CP4 (Z. mobilis) was studied in two glass fermentors operating with culture circulation for agitation (the EX-FERM type): a. A laboratory scale(2.5 liter) cylindrical vessel; b. A bench scale (8 liter) wide vessel. Z. mobilis cultures consumed 89–96% of the cane sucrose, converting it to ethanol by 90–97% of the theoretical yield in the laboratory scale fermentor and by 83–90% in the bench scale fermentor culture. Comparative Saccharomyces spp. cultures in laboratory fermentor consumed 96–98% of the cane sucrose, with ethanol conversion of only 75–79% of the theoretical yield.These preliminary results indicated that sucrose in agricultural size sugar cane chips was ethanol fermentable as compared to small size sugar cane chips or to sugar cane juice. Z. mobilis CP4 cultures converted sucrose more efficiently to ethanol than Saccharomyces spp. as shown in the laboratory scale fermentor studies.The ethanol yields in a wide bench scale fermentor cultures were slightly lower than in a laboratory fermentor.     

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 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.     

Ethanol production by recombinant Escherichia coli KO11 using crude yeast autolysate as a nutrient supplement

Summary Crude yeast autolysate (10 g/l; 5.8 g solubles/l) supplemented with minerals and vitamins served as a nutrient supplement for ethanol production by the recombinant bacterium, Escherichia coli KO11. Ethanol production in this medium (46±1.7 g ethanol/l) was equivalent to that obtained using 5–15 g/l of purified, soluble, commercial protein hydrolysates (44–48 g ethanol/l). On site production of autolysates from spent yeast offers the potential for synergy between grain-based and lignocellulose-based ethanol plants.     

Ethanol fermentation by flocculating yeast: Performance and stability dependence on a critical fermentation rate

Summary A system coupling fermentor and decantor permitted strong accumulation of yeast flocs that were homogeneously suspended in the reactional volume. At 100–190 g/l glucose feed practically total substrate conversion was attained. At 130 g/l glucose feed the highest productivity (18.4 g.l.h) and the highest ethanol yield (90.6%) were reached with biomass levels of 80–90 g/l. We observed that the stability of this system is limited when a critical fermentation rate (D.S_o) close to 39–40 g/l.h (with corresponding ethanol productivities of 19–20 g/l.h) is reached. Higher fermentation rates provoked de-flocculation and lost of biomass.Symbols D dilution rate (h^–1) - E ethanol (g/l) - S_r residual substrate (g/l) - S_o substrate in the feed (g/l) - X biomass (g/l) - ethanol yield (%) - DS_o fermentation rate (g/l.h) (for S_r0) - P_E ethanol productivity (g/l.h)     

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.     

Ethanol production with Saccharomyces cerevisiae at potassium-limited aerobic growth conditions

Summary The specific ethanol productivity withSaccharomyces cerevisiae grown aerobically in a chemostat at a growth rate of 0.17 hr^–1 was found to increase from zero to 13 mmol/g cell dry matter·h when the potassium content in the substrate used was decreased to 0.05 mol/kg glucose. 78% of the glucose metabolized were converted to ethanol under these aerobic growth conditions.     

Production of ethanol by adsorbed yeast cells

Summary Various ion exchange resins were tested for their ability to adsorb cells of Saccharomyces cerivisiae with the ultimate intention of developing a packed bed immobilized cell reactor for the continuous production of ethanol. The resins varied greatly in their ability to adsorb cells - the least effective resins retained less than 1 mg S. cerivisiae cells (dry weight)/g of resin (dry weight), and the most effective, 130–140 mg cells/g of resin. A column reactor packed with adsorbed yeast cells was operated continuously for over 200 hours using a 12% (w/v) glucose medium at dilution rates of 1.1 h^-1 and 1.44 h^-1 (based on void volume). High ethanol productivities of 53.1 and 62.0 g ethanol/l-h were obtained.     

Ethanol production in a continuous fermentation/membrane pervaporation system

The productivity of ethanol fermentation processes, predominantly based on batch operation in the U.S. fuel ethanol industry, could be improved by adoption of continuous processing technology. In this study, a conventional yeast fermentation was coupled to a flat-plate membrane pervaporation unit to recover continuously an enriched ethanol stream from the fermentation broth. The process employed a concentrated dextrose feed stream controlled by the flow rate of permeate from the pervaporation unit via liquid-level control in the fermentor. The pervaporation module contained 0.1 m² commercially available polydimethylsiloxane membrane and consistently produced a permeate of 20%–23% (w/w) ethanol while maintaining a level of 4%–6% ethanol in a stirred-tank fermentor. The system exhibited excellent operational stability. During continuous operation with cell densities of 15–23 g/l, ethanol productivities of 4.9–7.8 gl^–1 h^–1 were achieved utilizing feed streams of 269–619 g/l glucose. Pervaporation flux and ethanol selectivities were 0.31–0.79 lm^–2 h^–1 and 1.8–6.5 respectively.     

In vitro propagation through axillary bud multiplication in different mulberry genotypes

Axillary buds from 5 genotypes of mulberry belonging to 4 species were cultured on modified MS basal medium. A total of 30 media combinations were tried for all the genotypes. The response of axillary buds and the requirement for growth regulators varied with genotype. In Morus indica BAP (0.25–0.5 mg/l), and in M. alba and M. rotondifolia GA₃ (0.5–1.0 mg/l)were found to induce sprouting. Two genotypes of M. bombycis, namely Schimanochi and Mizusawa, developed healthy shoots on the incorporation of 2,4-D (0.5–1.0 mg/l) and BAP (0.5–2.0 mg/l), respectively. IBA (0.5 mg/l), along with cytokinin/auxin/gibberellin, had no effect on bud growth but helped root induction. Shoots developed from the axillary buds were further multiplied as nodal explants. MS basal medium supplemented with 0.5 mg/l IBA and LS vitamins was found best to produce healthy plantlets in all the genotypes. An average 89% survival was observed on transferring the plantlets to soil.Abbreviations MS Murashige and Skoog (1962) - LS Linsmaier and Skoog (1965) - IBA 3-indole-butyric acid - GA₃ Gibberellic acid - BAP 6-Benzylaminopurine - Kn Kinetin - 2,4-D 2,4-Dichlorophenoxyacetic acid     

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.     

Effect of calcium and sodium salts on ethanol production in high sugar fermentation by free cells ofZymomonas mobilis

Summary Addition of calcium carbonate enhanced ethanol production byZymomonas mobilis ZM4 and a mutant (ZMI₂), especially at higher concentrations (200–400 g/L) of glucose and sucrose, as well as at higher temperature (42°C) by the mutant. Calcium and sodium carbonates neutralized the acid produced in the medium and enhanced the ethanol production. The Na salts were less effective in the parent strain and were not favourable for the mutant. Ca²⁺ ions played a direct role in augmenting ethanol production as evidenced by the effect of calcium chloride at controlled pH (5.5).     

Kinetics of repeated batch production of ethanol by immobilized growing yeast cells

Summary Kinetic and yield parameters for growth and ethanol production from sucrose (100 g/l) bySaccharomyces cerevisia entrapped in K-carrageenan and calcium alginate were identical to those of free cells. Cell leakage was minimum with calcium alginate gel. For the sixth batch, 4.51 g/lh ethanol productivity (94% conversion of sucrose) was obtained; 60.5 g/l of ethanol was obtained from 200 g/l sucrose with 83.2% conversion, indicating inhibition effects.     

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.