EX-FERM ethanol production using chipped sugarcane in packed bed fermenters

Summary The operation of packed bed fermenters for ethanol production using the EX-FERM technique with two cycles of 24 h each is described. Twelve Saccharomyces strains were tested with sugarcane particles which had been previously dried and stored as the substrate. All the strains showed acceptable sugar consumption, in some cases above 97%, and ethanol yield coefficients. Sugar consumption values differed, significantly among yeast strains for both cycles. Specific initial rates of ethanol production for the strains ranged from 0.75 to 0.82 g/g· h. Sugar extraction from the particles influenced the first 4 h period of each cycle; final sugar extraction was about 96%. The initial yeast biomass figures were low, within 2–4 g/l, and the final distribution of yeast between solids and circulating liquid varied according to the yeast strain employed. Hydrolysis of sucrose into its components was demonstrated for selected yeast strains during the EX-FERM concurrent extraction and fermentation. The results of the present study support the validity of the operation of packed bed fermenters in cycles for the EX-FERM technique, and suggest employment of smaller cane particles.     

Ethanol from Sugar Cane: Flask Experiments Using the EX-FERM Technique

Alcohol production at the laboratory scale from sugar cane pieces by the EX-FERM technique was studied with 37 strains of Saccharomyces spp. The EX-FERM process is novel in that it employs the simultaneous extraction and fermentation of the sucrose in a cane-water suspension. Two types of cane treatments were used: chips and shredded pith, either fresh or dried. A mother culture of the yeast was prepared in enriched cane juice and then added to the cane-water mixture. After static fermentation for 40 h at 30°C, the cane was removed, and fresh cane was added to the yeast-alcohol broth. After an additional 24 h, the cane was again removed and the liquor was analyzed. After the first 40-h cycle, sugar consumption was above 99% with 10 of the 37 yeast strains tested, and ethanol reached levels of 1.29 to 4.00 g per 100 ml, depending on the yeast strain. The final ethanol concentration reached 4.27 to 5.37 g per 100 ml, and sugar consumption was above 98% in three cases during a second EX-FERM cycle employing previously air-dried chips and pith. Product yields were within accepted values. Cane treatment did not appear to affect the results at this level.     

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.     

Continuous ethanol production by immobilized yeast in a fluidized reactor

Summary In order to minimize the adverse effect of CO₂ gas in a packed bed immobilized yeast reactor, a fluidized bed reactor was used for the continuous production of ethanol from glucose. Immobilized yeast was prepared by entrapping whole cells of Saccharomyces cerevisiae within a Caalginate matrix. It was found that the efficiency of the ethanol production in a fluidized bed reactor was 100% better than that for a packed bed reactor system. The alcohol productivity obtained was 21 g/l/hr in a fluidized bed reactor at 94% of conversion level.     

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.     

Novel supplements enhance the ethanol production in cane molasses fermentation by recycling yeast cell

Summary Eight alcohol producing yeast strains were screened for their sedimentation rates and it was found thatS.cerevisiae NCIM 3526 was a better flocculant strain. This strain was employed in cane molasses fermentation with yeast recycle, supplemented with skim milk, chitin and fungal mycelium individually or in combination, at 30°C, using fermentable sugars 15%. On the completion of ten 16 h cycles, 20–30% more ethanol was produced in presence of these supplements and the efficiency of the process was improved from 66 to 87%.     

Alkaloid formation by Catharanthus roseus cells in a packed column biofilm reactor

Summary Catharanthus roseus cells producing indole alkaloids were grown on surfaces of Ca-alginate beads within the interspacial volume of a packed column. Production media was circulated through the packed column in an upflow mode. Growth and indole alkaloid formation were quantified and compared with suspension culture of cells. Final alkaloid concentration and alkaloid yield obtained in the packed bed was superior to those obtained in suspension culture. This is thought to be due to improved cell-cell contact and interaction in the packed column.     

Microbial transformation of sucrose and glucose to erythritol

Summary Two strains of osmophilic yeast which were isolated from honey-comb, produced good yields of erythritol as a main product. These strains were identified as Trichosporonoides sp., 150-5 and 331-1.From the fermentation studies with these strains using glucose and sucrose as substrate, strain 331-1 produced more erythritol as the sole polyhydric product,with trace quantities of glycerol, than strain 150-5.     

Clonal propagation of Trifolium Pratense,T. Resupinatum and T. Subterraneum by direct somatic embryogenesis on cultured immature embryos

Direct somatic embryogenesis on immature zygotic embryos in vitro has been confirmed for Trifolium pratense and extended to T. resupinatum and T. subterraneum. For all species direct embryo cloning can be achieved on an appropriate basal medium supplemented with 1gl^–1 yeast extract and 0.05 mgl^–1 BAP. Basal medium/sucrose formulation, level of yeast extract and level of BAP affected the nature of in vitro responses. In particular, for T. pratense and T. subterraneum lowering of the yeast extract level suppressed embryoid initiation, and raising of the BAP level stimulated formation of nodular morphogenic callus. For T. resupinatum alteration of the basal medium/sucrose formulation changed the tissue site of embryoid initiation from hypocotyl to cotyledons or both. Control of embryoid initiation is briefly discussed.Abbreviation BAP 6-benzylaminopurine     

A novel Acinetobacter sp. for treating highly acidic rubber latex centrifugation effluent

Summary A novel Acinetobacter sp. BTJR-10 isolated from highly acidic (pH 2.5–4.5) rubber latex centrifugation effluent with high COD (22000 mg/L) and BOD (5000 mg/L). This strain could effect 39.5% COD reduction on free cell inoculation of effluent without incorporation of additional nutrients after 8 days. Calcium alginate immobilized cells showed 16.4% and 25% COD reduction after 6 hrs. without aeration and after 1 hr. with mild aeration under batch process respectively. Whereas 44.0% COD reduction could be achieved after 6 hrs. on continuous treatment in a packed bed reactor with mild aeration. Further, even after 3 cycles 37% COD reduction was recorded with continuous treatment.     

Ethanol fermentation by immobilized cells in a trickle bed reactor

A modified discontinuous packed bed reactor with CO₂ ventilation ports, resembling a trickle bed reactor was employed to overcome gas holdup and bed compaction problems which are commonly encountered in cell immobilized packed bed reactors for ethanol fermentation. The reactor consisting of yeast cells entrapped in alginate matrix was operated by varying the substrate concentration, bed volume and inlet flow rates. The number of recirculation cycles (passes) and total stages were dependent upon the liquid flow rate, though the total contact time for complete conversion remains the same for a particular initial substrate level. The total contact time was 1.5, 3 and 4.5 h for initial substrate concentrations of 0.555, 0.933 and 1.3 kmol/m³ respectively. The number of cycles and in turn stages increased with the increase in initial sugar level. A graphical method for predicting the number of stages required for complete conversion was proposed based on material balance equation and evaluated for the operating variables of the present study. The reactor was operated continuously for 30 days producing 1.05– 1.15 kmol/m³.     

The metabolism of lactose byClostridium acetobutylicum

Summary Acetone and butanol biosynthesis byClostridium acetobutylicum ATCC 824 was affected by lactose concentration and by agitation during the fermentation. At 1% and 3% lactose concentrations acid production predominated, while butanol production predominated at 5% lactose concentration. Higher solvent production was observed in fermentors without agitation than in fermentors with agitation.     

Alkali Protease and Alcohol Dehydrogenase Immobilized to Weakly Basic Anion Exchange Resins Using 2-Car-boxymethylamino-4,6-dichloro-s-triazine

Alkali protease partially purified from a strain of Bacillus subtilis and yeast alcohol dehydrogenase were immobilized to weakly basic anion exchange resins using a bifunctional reagent, 2-carboxymethyIamino-4,6-dichloro-s-triazine.

Properties of these immobilized enzymes were studied both in batchwise operation and in packed bed reactor systems.     

New yeast strains for alcoholic fermentation at higher sugar concentration

Summary New yeast strains for alcoholic fermentation were isolated from samples collected from Brazilian alcohol factories at the end of the sugar cane crop season. They were selected by their capacity of fermenting concentrated sugar cane syrup as well as high sucrose concentrations in synthetic medium with a conversion efficiency of 89–92%. The strains were identified asSaccharomyces cerevisiae.     

A comparison of methods for assessing yeast viability

Summary Eight different methods were used to assess the cell viability of four strains of Saccharomyces. Staining with Mg-ANS, primuline yellow, FITC and methylene blue gave a good index of yeast cell viability. The standard plate count technique and microcolony formation also gave a good measure of cell viability. Fluorescent staining with acridine orange was the least useful of the methods tested. INT dye reduction gave a good index of respiring cells depending upon the yeast strain tested.     

Electrical aspects of division control inSaccharomyces

Readily discernable changes in electrical character take place during the division cycle of the yeast,Saccharomyces cerevisiae. By using the technique of cellular spin resonance, the electrical polarizability of individual cells can be seen to change with the life cycle, as determined by cell morphology. The polarizability changes indicate that during the advance through the life cycle, the ionic double layers associated with the outer cell wall gradually tighten.     

Screening of yeast strains capable of hyperproducing amylolytic enzymes

Summary Fifteen strains of yeast, which produced an extracellular amylolytic enzymes, were isolated from nature. One of them produced more than 100 times the enzyme activity in comparison with the 14 strains and the extremely hyperproducing strain of yeast was identified asCandida sp. 347. Paper chromatograms of the amylolytic enzyme demonstrated activity of amyloglucosidase. The optimum pH for activity of the enzyme was 5.5–6.0 and optimum temperature was 60°C.     

Yeast cells entrapped in low-gelling temperature agarose for the continuous production of ethanol

Summary Continuous ethanol production byS. uvarum immobilized in a low-gelling temperature agarose namely SeaPlaque agarose was studied in a packed bed reactor at 30°C using sugarcane molasses containing 13.5% fermentable sugars as feed. The productivity at 95% conversion was 23 g/l.h (on reactor volume basis). The bioreactor was run continuously at a fixed dilution rate and it retained 60% of its initial activity upto 80 days.     

Solid state fermentation of dried citrus peel byAspergillus niger

Summary Solid state fermentation of dried citrus peel was studied in a packed bed reactor withAspergillus niger QH-2. When no nitrogen source was added the growth was limited. When urea and/or ammonium sulphate were added in the proportion of 0.63 g N/100 g solid dry substrate a diauxie was observed and the final content of crude protein was higher than 10%. The results of a factorial design show that ammonium sulphate has a significant effect on the specific growth rate.     

Regulated production of recombinant echistatin by yeast

Summary The -mating factor pre-pro-leader sequence under the regulation of theGAL10 promoter was used to direct the secretion of echistatin by recombinant yeasts. Optimization of the culture medium and host strain increased the productivity of shake flask cultures twenty-fold to 8 mg/L. In fermentors, the production of echistatin was greater than 40 mg/L.