Biomass for Energy and the Environment -  P. Chartier,  G.L. Ferrero,  U.M. Henius,  S. Hultberg,  J. Sachau,  M. Wiinblad

Biomass for Energy and the Environment (eBook)

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2012 | 1. Auflage
630 Seiten
Elsevier Science (Verlag)
978-0-08-098382-0 (ISBN)
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Biomass is set to play an increasing role in the supply of energy, both in the industrialised world and in developing countries, as concern for the state of the global environment grows. The possibility for the acceleration of commercial production has received support from the increasing involvement of the large power producers and the growing political commitments of several European countries.The 9th European Bioenergy Conference was held in Copenhagen, 24-27 June 1996. Interest in this conference series continues to grow and the event attracted around 700 delegates from 45 countries. In contrast to previous events, more emphasis was placed on demonstrating bioenergy technology in the marketplace. Overviews on recent achievements in commercial or near commercial activities formed the main focus of the event, but highlights of advancesin science and technological development were also presented, in addition to papers covering environmental aspects of bioenergy.The proceedings contain 350 state-of-the-art papers addressing the following areas; primary production of biomass; provision and production of solid biomass fuels; processes for large power plants; processes for decentralised heat and power production; processes for production of transportation fuels; market, economic and environmental aspects of bioenergyand policy measures to overcome non-technical barriers
Biomass is set to play an increasing role in the supply of energy, both in the industrialised world and in developing countries, as concern for the state of the global environment grows. The possibility for the acceleration of commercial production has received support from the increasing involvement of the large power producers and the growing political commitments of several European countries.The 9th European Bioenergy Conference was held in Copenhagen, 24-27 June 1996. Interest in this conference series continues to grow and the event attracted around 700 delegates from 45 countries. In contrast to previous events, more emphasis was placed on demonstrating bioenergy technology in the marketplace. Overviews on recent achievements in commercial or near commercial activities formed the main focus of the event, but highlights of advancesin science and technological development were also presented, in addition to papers covering environmental aspects of bioenergy.The proceedings contain 350 state-of-the-art papers addressing the following areas; primary production of biomass; provision and production of solid biomass fuels; processes for large power plants; processes for decentralised heat and power production; processes for production of transportation fuels; market, economic and environmental aspects of bioenergyand policy measures to overcome non-technical barriers

PRODUCTION OF ETHANOL AND INVERTASE BY S.cerevisiae GROWN IN BLACKSTRAP MOLASSES


MICHELE VITOLO,     Department of Biochemical and Pharmaceutical Technology, University of São Paulo, 05508-900, São Paulo, SP, Brazil

ABSTRACT


S.cerevisiae was grown in blackstrap molasses without aeration and at different pH (4.0, 4.5, 5.0, 5.5, 6.0 and 6.5). The highest production of etha nol (8.5 g/L.h) and invertase (238 U/L) were attained at 4.5 and 5.5, respectively. The invertase formation would be subjected to carbohydrate repression/derepression mechanism and to the culture conditions employed, such as pH.

KEYWORDS

Ethanol

invertase

molasses

yeast

S.cerevisiae

INTRODUCTION


Renewable biomass such as sugar cane, sugar beet and molasses are among the most important raw materials for alcohol production, using the fermentative yeast Saccharomyces cerevisiae. At the end of alcoholic fermentation, a significant amount of residual cells are attained, which, in turn, could become a source for several products of economic interest (yeast extract enzymes, nucleic acid, among others) (Buentemeyer et al., 1989). One commercially valuable by-product is invertase (EC.3.2.1.26), an enzyme employed in analytical probes, confectionary and sucrose hydrolysis for inverted syrup production (Barlikova et al., 1991; Vitolo and Yassuda, 1991). This communication deals with the effect of pH of culture medium on the ethanol production and invertase activity of S.cerevisiae.

METHODOLOGY


Inoculum Preparation


S.cerevisiae (isolated from pressed yeast), maintained on slant tubes containing (per liter) nutrient agar Difco 23.0g and glucose 1.0g, was transferred to test tubes containing 5.0 mL of growth medium (peptone 5.0g, glucose 10.0g, yeast extract 3.0g and distilled water 1.0L; pH adjusted to 4.5) and incubated at 33°C for 48 h. Nine 250 mL-erlenmeyer flasks containing 50 mL molasses medium were inoculated with five tubes of cell suspension, and left incubating at 33°C for 22 h in a rotary shaker (frequency of 120 min−1).

Batch Fermentation


Tests were carried out in a 5-L bench fermenter (NBS-MF 200 coupled with a NBS-dissolved oxygen controller, D0-81) filled with 2.55 L of sterilized blackstrap molasses (Total Reducing Sugars (TRS): 145-150 g/L, clarified (Vitolo et al., 1985) and supplemented with 5.1 g/L (NH4)2SO4, 2.4 g/L Na2HP04.12H2O and 0.075 g/L MgS04.7H2O). The following standard culture conditions were adopted: Impeller speed = 500 min−1; Antifoam: 0.1 mg/L dimethylpolysiloxane (added dropwise as needed); Temperature = 30°C. The mash was inoculated with 0.45 L of S.cerevisiae suspension (10.Og dry matter/L) and left fermenting until TRS was negligible. The pH was controlled during fermentation at 4.0, 4.5, 5.0, 5.5, 6.0 or 6.5. At regular time intervals (1 hour) aliquots (10.0 mL) of the culture medium were drawn for analytical purposes. The cells used for invertase activity determination and protein release from the cell wall were separated by centri fugation (5,000 xg; 15 min) and rinsed twice with distilled water. Then, the cells were resuspended in distilled water in order to obtain a known volume.

Measurement of Invertase Activity


The determination of invertase activity was carried out at 37°C in a mixture of 1.5 mL 0.01M acetate-acetic acid buffer (pH 4.6), 2.5 mL 0.3M sucrose solution and 0.5 mL invertase solution or cell suspension (both adequately diluted to assure that less than 2.0% of the sucrose present in the solution would be hydrolyzed). After 3 min, the hydrolysis was stopped by adding 1.0 mL of the Somogyi alkaline reagent (Somogyi, 1952), quickly followed by immersion in a boiling water bath for 10 min. The TRS concentration was then measured as described previously (Vitolo and Borzani, 1983). One invertase unit (U) was defined as the amount of enzyme catalyzing the formation of 1g of TRS per hour at pH 4.6 and 37°C. Specific invertase activities were expressed as U/mg of protein (soluble invertase, released from yeast cell wall) and U/g dry cell (insoluble invertase).

Measurement of Cell and Ethanol Concentrations


The determination of ethanol and cell concentrations were carried out as described previously (Vitolo et al., 1991).

Protein Release from Cell Wall


Induced release of extracellular protein from the cell wall was achieved as follows: 200mg of cells were suspended in 5mL of a 50mM potassium phosphate buffer (pH 7.0) containing 15 mM 2-mercaptoethanol and 15 mM dithiothreitol. The suspension was incubated for 2 h at 35°C, followed by centrifugation (10,000xg; 15 min) at 4°C. The protein content in the supernatant phase was measured (Bradford, 1976).

RESULTS AND DISCUSSION


Data of Table 1 show that invertase activity of intact cells (v) increased markedly when the TRS concentration in the mash was lower than 10.0 g/L, thus indicating that invertase biosynthesis could be regulated by the carbohydrate repression/derepression mechanism (Patkar and Seo, 1992). Taking into account the variation of v against time (dv/dt), it is clear that invertase accumulated into the cell wall even at TRS concentration higher than 10.0 g/L.

Table 1

Variation of invertase activity (v), cell (X) and TRS concentrations in a batch culture carried out at pH 5.5.

This is confirmed by the observed increase of protein concentration and specific invertase activity (v′) released from the wall of cells harvested during fermentation (Table 2). This finding suggests that invertase could be subjected not only to a repressive/derepressive mechanism but also to the culture conditions employed.

Table 2

The specific invertase activity (v’) and protein concentration in the cell-free extract (the cells were harvested from batch culture carried out at pH 5.5).

t (h) protein (mg/mL) v’ (U/mg of protein)
0 1.02 0.20
1 1.12 0.26
3 1.20 0.34
5 1.64 0.86
7 1.93 1.02

Ethanol (E) and invertase (P) productions were affected by the pH of the cul ture medium, being the highest P (237.6 U/L) and E (8.5 g/L.h) attained at pH 5.5 and 4.5, respectively (Table 3).

Table 3

Variation of invertase and ethanol production against the pH of the culture medium. The protein concentration and v’ in the cell-free extract are also presented (the cells were harvested at the end of fermentation).

Since the protein released from wall of cells harvested at the end of batch fermentations, carried out at different pH, varied only 8% whereas v’ varied 25% (Table 3), one could state that the effect of pH on the invertase activity of intact cells could be due to modifications in the tertiary and quaternary structures of invertase as consequence of the external pH, leading to an anomalous insertion of the enzyme inside the cell wall network (Reddy et al., 1990). Of course, perturbations at the level of the invertase biosynthesis pathway can not be totally disregarded. The result related to ethanol production fairly well agree with evidences of the literature (Vitolo et al., 1991). It might be also possible to speculate that the external pH would change in some extention the intracellular pH, interfering on the glycolytic pathway, and in turn, ou ethanol biosynthesis (Weitzel et al., 1987).

The observation that invertase activity of intact yeast cells is enhanced at low TRS concentration (molasses diluted ten times, at least), opens the possibility to sugar industries interested to invertase, as by-product, to divert only a fraction of its available molasses for this purpose. The largest part of substrate could be still funnelled to the more common applications, such as ethanol fermentation.

REFERENCES


Barlikova, A., Svorc, J., Miertus, S. Hybrid biosensor for determination of sucrose. Analyt. Chim. Acta. 1991; 247:83–87.

Bradford, M.M. A rapid and sensitive method for the quantitation of microgram quantities of protein using the principle of protein-dye binding. Analyt. Biochem. 1976; 72:248–254.

Buentemeyer, K., Kroner, K.H., Husted, H., Deckwer, W.D. Process for large-scale recovery of intracellular yeast invertase. Process Biochem. 1989; 24:212–216.

Patkar, A., Seo, J.H. Fermentation kinetics of recombinant yeast in batch and fed-batch cultures. Biotechnol. Bioeng....

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