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Applied and Environmental Microbiology, August 2007, p. 4791-4796, Vol. 73, No. 15
0099-2240/07/$08.00+0 doi:10.1128/AEM.00120-07
Copyright © 2007, American Society for Microbiology. All Rights Reserved.

INRA, AgroParisTech, UMR 763 Bioadhésion et Hygiène des Matériaux, 25 Avenue de la République, 91 300 Massy, France,1 Université de Rouen, Laboratoire d'Electrochimie et de Chimie Analytique, UFR de Sciences et Technologies, 76 821 Mont Saint-Aignan, France,2 Université de Yaoundé I, Laboratoire de Chimie Minérale, Département de Chimie Inorganique, B.P. 812, Yaoundé, Cameroon,3 AgroParisTech, INRA, UMR763 Bioadhésion et Hygiène des Matériaux, 1 Avenue des Olympiades, 91 300 Massy, France4
Received 17 January 2007/ Accepted 15 May 2007
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The gliding electric discharge ("glidarc") device in humid air is an efficient and inexpensive source of nonthermal plasma which operates close to atmospheric pressure (it does not require a vacuum) and at room temperature. This plasma exhibits characteristics of both thermal and nonthermal plasma so that its interactions with matter are those of quenched plasma (16). With humid air as the working gas, °OH and NO° were identified by emission spectroscopy measurements as the principal radical species present in the glidarc plasma plume (2), and they are probably precursors of other active species. Such species endow the medium with very high, enhanced chemical reactivity. As a result, the gliding discharge device was first studied successfully for the treatment of gases (5) and liquids (24) to abate chemical pollutants. More recently, it was also tested successfully for decontamination of microorganisms (12, 22), which represents one of the most interesting applications of atmospheric pressure plasmas in recent years.
This work dealt with inactivation of bacterial suspensions using gliding arc plasma. In aqueous solution, a so-called temporal postdischarge phenomenon was recently highlighted in a chemical pollutant abatement setting. This phenomenon can simply be defined as the overall reactions that continue after the discharge is switched off, and it probably involves the presence of long-lived reactive species. The postdischarge phenomenon may be of great value in terms of environmental and industrial applications because the target continues to be treated without any contribution of energy. Costs are thus reduced. Although this phenomenon has been observed in the oxidation of inorganic aqueous solutions (7) and in plasma chemical nucleophilic substitution reactions (6), no attempts to use plasma temporal postdischarge disinfection have been reported previously, as far as we know. In this study, as a first step toward full evaluation of the viability of glidarc technology for industrial microbial decontamination, after characterizing the destruction of bacterial cells by classical gliding electric discharges, we focused on the study of temporal postdischarge treatment. Postdischarge efficiency was evaluated for cells that were present or not present in the fluid exposed to the discharge. In the latter case, treatment consisted of disinfection by plasma-activated water, the properties of which were studied. The entire study was conducted with Hafnia alvei, which was selected as a bacterial model. This gram-negative bacterium belongs to the family Enterobacteriaceae. It has been found in a number of foods, such as milk products and meats, and in humans it may be associated with several intestinal disorders, including gastroenteritis (31).
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Gliding discharge treatments.
The plasma device utilized was a nonthermal quenched plasma device of the gliding arc type operating at atmospheric pressure with humid air as the plasma gas. The design of the device and the procedure for gas discharge have previously been described (22). Under operating conditions, the feed gas was provided by an air compressor. The air supplied (550 liters h–1) was bubbled through a water-filled Duran flask in order to saturate it with water vapor. The gap between the plasma source electrodes was kept constant at 3.5 mm. The distance between the electrode tips and the top of the liquid target was 13 cm. The reactor was fitted with a circulating water jacket to prevent any thermal effect, so that the temperature of the treated suspensions remained below 30°C. Valves and filters were adjusted to the reactor in order to allow sampling during plasma treatment, when necessary. For each series of experiments, 200-ml portions of stirred liquid samples (1.5 x 10–1 M NaCl or diluted suspensions) were exposed to the plasma discharge. The treatment time under plasma discharge was designated t*.
Temporal postdischarge treatments.
For temporal postdischarge treatments, diluted bacterial suspensions were initially treated for various t* with the glidarc reactor, as described above. Once the discharge was stopped, the bacterial suspension was left at the ambient temperature for various postdischarge times (tp) before sampling and determination of surviving cells.
During other experiments, 1.5 x 10–1 M NaCl solutions without bacterial cells were treated with the glidarc reactor for various t* and then referred to as "activated water." Concentrated bacterial suspensions (12 ml) were diluted in activated water (188 ml) immediately after plasma treatment or after a period of storage. Thereafter, the suspensions were left at the ambient temperature for a variety of postdischarge periods (referred to as "contact time" [tc]) before samples were removed and survivors were counted.
Evaluation of surviving cells.
Before and after treatment (discharge and/or postdischarge), the numbers of surviving cells were determined by duplicate plate counting on Trypticase soy agar (bioMérieux). In order to prevent any destruction after sampling, the lethal effect of active species generated by glidarc plasma discharge was stopped with a universal neutralizing solution (3 g liter–1 L-
-phosphatidylcholine, 30 g liter–1 Tween 80, 5 g liter–1 sodium thiosulfate, 1 g liter–1 L-histidine, 30 g liter–1 saponine), as recommended in the NF EN 1040 European standard (1) with respect to disinfection. For this purpose, 1 ml of the suspension to be analyzed was diluted in 9 ml of neutralizing solution at each time point. Thereafter, classic 1/10 dilution in 1.5 x 10–1 M NaCl was performed prior to plating. As described in the European standard, control experiments were performed to verify the inactivity of the neutralization procedure with microbial cells and its efficiency against active species generated by glidarc plasma discharge. The number of cultivable bacteria (expressed as CFU) was counted after 2 days of incubation at 30°C. The limit of detection under our experimental conditions was 5 CFU ml–1. Each determination of the kinetics of destruction was performed with at least three independently grown cultures. The data presented below are the means of decimal logarithm CFU ml–1 values ± standard deviations.
Modeling of bacterial destruction.
GinaFiT, a freeware add-in for Microsoft Excel (9), was utilized to model inactivation kinetics. This tool enables testing of nine different types of microbial survival models, and the choice of the best fit depends on five statistical measures (i.e., sum of squared errors, mean sum of squared errors and its root, R2, and adjusted R2). During this study, the different models were applied to the mean values obtained from experimental data. The "shoulder + log-linear" inactivation model exhibited the best fit with our experimental data and was thus considered. It took account of a latency time before a decrease in the population size. The kinetics of destruction were expressed as follows (9):
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FIG. 1. Survival curve for H. alvei treated with gliding arc plasma discharge (x). The values are the means ± standard deviations for at least three experiments conducted with independently grown cultures. +, blank (treatment with un-ionized humid air); solid line, GInaFiT inactivation model; dashed and dotted line, detection threshold.
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Figure 2 shows the survival curves for H. alvei planktonic cells subjected to temporal postdischarge for different periods of glidarc plasma treatment. All these curves presented the same profile, which is similar to that obtained with direct discharge, with an initial lag phase followed by decay of the cultivable population. For all the different curves, the "shoulder + log-linear" GInaFiT model fitted the data relatively satisfactorily (R2 > 0.9733). Inactivation constants, as well as the lengths of the shoulder phase, are shown in Table 1. All the conditions tested made it possible to achieve more than 7 decimal logarithm units of destruction, but the efficiency of postdischarge treatments was clearly affected by the discharge duration. Postdischarge treatment was more efficient after a longer t*, and no detectable cells (from the initial population containing 4 x 107 bacteria per ml) remained after 13 min for a t* of 5 min, after 16 min for a t* of 4 min, after 21 min for a t* of 3 min, and after 28 min for a t* of 2 min. As illustrated in Fig. 2 and Table 1, both the length of the lag phase and the inactivation rate depended on t*. More precisely, it could even be considered that there was a positive linear correlation between kmax and t* and a negative linear correlation between Sl and t* (Fig. 3). Within the domain studied, the kmax and the Sl could then be expressed as kmax = 0.37t* + 0.56 (R2 = 0.9776) and Sl = –3.36t* + 21.68 (R2 = 0.9654), respectively.
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FIG. 2. Survival curves for H. alvei subjected to temporal postdischarge time (tp) after different t*, including ( ) 5 min, ( ) 4 min, ( ) 3 min, and () 2 min. For each curve, the open symbol indicates the beginning of postdischarge treatment. The values are means ± standard deviations for at least three experiments conducted with independently grown cultures. Solid lines, GInaFiT; dashed and dotted line, detection threshold.
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TABLE 1. "Shoulder + log-linear" model parameters for survival curves for H. alvei subjected to temporal postdischarge after different t*a
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FIG. 3. Correlation between model temporal postdischarge kinetic parameters, including kmax ( ) and Sl ( ), and t*.
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FIG. 4. Kinetics of destruction of H. alvei cells exposed for a t* of 5 min to the glidarc plasma discharge and then to postdischarge (during tp; ) or exposed to activated water for a contact time (tc; ). In the latter case, activation was achieved by exposure for 5 min of 1.5 x 10–1 M NaCl without cells to gliding arc plasma discharge. The values are means ± standard deviations for at least three experiments conducted with independently grown cultures. Dotted and dashed line, detection threshold. tc, contact time; tp, postdischarge time.
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TABLE 2. Effects of the length of plasma activation of 1.5 x 10–1 M NaCl solutions on the temporal postdischarge destruction of H. alvei cells
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TABLE 3. Effects of the resting time of activated water on the temporal postdischarge destruction of H. alvei cellsa
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The kinetics of destruction were studied under various conditions, including direct discharge followed or not followed by temporal postdischarge. In both cases, the kinetics of destruction fitted well with the "shoulder + log-linear" GInaFiT model (Fig. 1 and 2). In previous studies, the kinetics of plasma treatment were often polyphasic (14, 20). Biphasic curves with a lag phase were previously observed during the destruction of planktonic cells by direct discharges using the same type of plasma equipment (22), as well as with other types of discharges (17), and the reported values for shoulder lengths and inactivation rates were comparable to those obtained during the present study. For example, Maeda et al. (17) obtained a lag phase of 14 min and an inactivation rate of 1 min–1. Our study showed that these two parameters were contrastingly linearly modified with discharge time t*. This situation can be compared with the results of thermal destruction, where biphasic curves have also been observed, and both shoulder lengths and inactivation rates have been clearly related to the destruction temperature by some authors (4, 8). Thus, the quantity of energy injected (as heat or electricity) is a key parameter in bacterial inactivation, as it is for chemical compound abatement using glidarc techniques (13). The energy provided to the discharge was used to create active (and/or lethal) species. In this context, we can assume that the lag phase was a manifestation of accumulated damage which became irreparable (and thus lethal) above a critical level. However, from results shown in Fig. 4, it can be deduced that this level depended not only on the amount of active species but also on the contact time between cells. This corresponds to the CT parameter (concentration x contact time) frequently employed in the case of disinfection with classical chemical compounds (25).
The course of the kinetics of destruction of microorganisms by any lethal agent can be related to the rate of the reaction between the agent and the microorganism under study and also to the variable resistance of individual cells in a given population (25, 27). For example, the fact that a small fraction of any population can survive treatments that kill the majority of that population has frequently been reported (which leads to a survival curve with a tail, as shown in Fig. 4), and intrapopulation diversity has been postulated to be a mechanism to ensure survival following exposure to stress (3). Moreover, in the specific case of plasma treatment, polyphasic curves could result from the successive actions of several lethal agents that depend on the plasma device (15, 19). In the present study, the pH of H. alvei suspensions fell from 6.1 to 3.6 with only 1 min of treatment, and HNO3 was detected in the suspended fluids. But acidification alone cannot explain the cell mortality observed during discharge and postdischarge treatments, as immersion for 30 min of an H. alvei suspension in acidified NaCl (HNO3, pH 3.6) induced a reduction in the number of cultivable cells which was less than 2 decimal logarithm units (data not shown). Glidarc destruction is probably also based on the chemical processes of oxidation. As parallel experiments conducted in NaCl solutions and deionized water produced the same level of destruction (data not shown), plasma treatment could not be suspected to induce the formation of chlorine active species, which are potent oxidizers used as sanitizers (18). On the other hand, various free radicals (e.g., °OH and NO°) are formed in the plasma plume (2). These radicals are highly active in the inactivation of microorganisms (20, 29) and possibly involved in direct discharge treatments. Through recombination and collisions, these labile free radicals may give rise to new longer-life-span species that would be responsible for the lethal effects of temporal postdischarge. In agreement, H2O2 (a molecule derived from °OH) was proposed to be the principal agent for oxidation in the temporal postdischarge of chemical compounds (7), and NO° was oxidized to HNO2 and subsequently to HNO3, both of which were detected in plasma-treated fluids (data not shown). The evolution over time of discharge-generated active species led to evolution of activated water efficiency (Table 2). Together with lesions induced directly by plasma discharges on bacterial cells (due to, for example, an electric field, as in the case of destruction by a pulsed electric field [28]), the evolution of active species was also probably responsible for the difference in efficiency observed when the cells were in the fluid or not in the fluid during the discharge (Fig. 4).
To summarize, for discharge alone or under in postdischarge conditions, the efficiency probably results from a combination of different effects, principally of a chemical nature. We plan to pursue our studies to determine the implications for different chemical active species, particularly in the setting of the lethal postdischarge effect of glidarc. Even though preliminary studies have shown that the glidarc treatment of water does not generate genotoxic compounds (21), the production of potential toxic by-products also needs to be carefully examined before any practical applications can be proposed, especially in the food and water industries.
Georges Kamgang-Youbi's thesis received financial support from the "Service de la Coopération et d'Action Culturelle (SCAC)" at the French Embassy in Cameroon via an EGIDE scholarship.
Published ahead of print on 8 June 2007. ![]()
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