Inactivation of Pseudomonas fluorescens and Streptococcus thermophilus in Trypticase® Soy Broth and total bacteria in milk by continuous-flow ultrasonic treatment and conventional heating
Introduction
During the last years, ultrasonic treatment and other alternative food technologies have been studied due to consumers’ continuing demand for products with improved quality and safety.
High-intensity ultrasound (10–1000 W/cm2 and ⩽0.1 MHz) Povey & McClements, 1988, McClements, 1995 has been used for some dairy process applications such as cleaning (Kivelä, 1996), inactivation of bacteria Ordóñez et al., 1987, Garcı́a et al., 1989, Wrigley & Llorca, 1992 and enzymes (Vercet, López & Burgos, 1997), extraction of chymosin Kim & Zayas, 1991a, Kim & Zayas, 1991b and β-galactosidase (Sakakibara, Wang, Ikeda & Suzuki, 1994) and homogenisation of milk (Gaffney, 1997), even increasing the cheese yield (Müller, 1992). Although the bactericidal effect of ultrasound is known, especially when combined with heat Ordóñez et al., 1984, Ordóñez et al., 1987, Garcı́a et al., 1989 and static pressure (Raso, Pagán, Condón & Sala, 1998), the dairy industry does not currently use this technique for preservation purposes. This could be due to the fact that detailed studies, including energy consumption aspects, about continuous-flow ultrasonic milk processing are scarce. It is evident that continuous processes are easier to scale-up than batch treatments.
During ultrasonic treatment the main active force is mechanical in nature, resulting in the formation and implosion of bubbles in a liquid (cavitation) (Shukla, 1992). However, the action of cavitation is a heat-generating process, since input of mechanical energy causes molecular motion, raising the temperature (Berliner, 1984). Moreover, part of the energy can be absorbed for the heating of the sample (Floros & Liang, 1994). As the heating is within the sample, the equipment wall temperature is lower than the liquid temperature. This could offer some advantages over conventional heating systems in terms of better temperature distribution and less fouling formation, and thus the product quality might be improved Jong de et al., 1992, Jong de, 1996.
On the other hand, Pseudomonas fluorescens (Gram-negative) is one of the most important psychrotrophic bacteria responsible for undesirable flavours in milk and dairy products. The heat treatment applied during conventional pasteurisation (72–78°C, 10–20 s) is sufficient to destroy large numbers of vegetative cells of this microorganism (Nickerson & Sinskey, 1972). Streptococcus thermophilus (Gram-positive) is a thermoduric bacterium which may appear in large numbers in pasteurised milk, giving the false impression that the milk has not been properly pasteurised (Frobisher, 1968).
The effectiveness of ultrasound in killing Gram-negative and Gram-positive microorganisms is still unclear. Ahmed and Russell (1975) stated that Gram-negative cells are less resistant to ultrasound than Gram-positive. However, Scherba, Weigel and O’Brien (1991) did not find any difference in the killing rate of the two kinds of microorganisms by ultrasonic treatment.
The aim of this research was to evaluate the effects of continuous-flow ultrasonic treatment using the heating produced by ultrasound on P. fluorescens and S. thermophilus in Trypticase® Soy Broth (TSB), and on total bacterial counts of milk. A comparative study has been made using a conventional heating system (heat exchanger) under similar process conditions. In addition, the shelf life of milk subjected to a mild continuous-flow ultrasonic and conventional treatment has been evaluated by microbiological and proteolytic indices.
Section snippets
Bacteria and culture conditions
Experiments were performed using P. fluorescens NIZO B337 (isolated from raw milk) and S. thermophilus B8 (isolated from a cheese factory from the Netherlands). Stock cultures of 1% in litmus milk were stored at −80°C. Prior to use, these cultures of P. fluorescens and S. thermophilus were maintained overnight at 30°C and 45°C, respectively. A small inoculum (1.8 ml) was transferred into 1 l of fresh 3% TSB (Becton Dickinson) and incubated at 30°C for 8 h in the case of P. fluorescens and at
Set-up of the equipment: selection of the processing conditions
In order to determine the equilibrium temperature at several flow rates (from 11 to 174 ml/min), previous experiments with distilled water were performed at the maximum output intensity level (10). After 20 min of treatment the system was in equilibrium as indicated by constant outlet temperatures. Once the steady state was achieved, the outlet temperature was maintained with coefficients of variations less than 1%. Flow rates from 11 to 50 ml/min and output intensity values of 10 and 5
Acknowledgements
M. Villamiel thanks the Spanish Ministry of Education and Culture for a postdoctoral grant.
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