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Antimicrobial Agents and Chemotherapy, February 2005, p. 728-732, Vol. 49, No. 2
0066-4804/05/$08.00+0 doi:10.1128/AAC.49.2.728-732.2005
Copyright © 2005, American Society for Microbiology. All Rights Reserved.
Center for Biofilm Engineering and Department of Chemical Engineering, Montana State UniversityBozeman, Bozeman, Montana
Received 7 June 2004/ Returned for modification 10 August 2004/ Accepted 12 October 2004
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The objective of this study was to directly visualize the penetration of an antibiotic-sized tracer molecule into the interior of biofilm cell clusters, noninvasively and in real time. This was accomplished by using fluorescent dyes that were imaged by confocal scanning laser microscopy. Quantitative image analysis was performed to extract numerical values of the effective diffusion coefficient in the biofilm.
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Biofilm reactor. Biofilms were grown in glass capillary tubes (Friedrich and Dimmock, Millville, N.J.) under continuous-flow conditions. Glass tubes were used rather than a more clinically relevant material because glass provided an optically clear substratum for microscopy. In addition, these capillary tubes had a square cross-section, which facilitated microscopic observation of the biofilm through the capillary walls. The nominal inside dimension of the tube was 0.9 mm, and it was approximately 10 cm long. Autoclaved 1/10 strength TSB was delivered to the capillary by gravity feed from a 5-liter carboy. The head difference from the feed carboy to the waste outlet was approximately 1.5 m. The flow rate of medium, which was monitored by counting drops passing through a flow break between the feed carboy and capillary, was between 120 and 180 ml h1. This flow rate corresponds to a Reynolds number of 37 to 56 based on the hydraulic radius of the clean tube. The medium carboy and the reactor itself were placed inside separate 37°C incubators stacked on top of each other. The reactor was inoculated by injecting 1 to 2 ml of overnight culture into a septum just downstream of the glass capillary. The inoculated reactor was allowed to stand without flow for 2 h, after which flow was initiated. Biofilms were allowed to develop for 24 h in the continuous-flow mode. For microscope observations of biofilm, the capillary was placed in a holder (Biosurface Technologies, Bozeman, Mont.) that could be mounted on the microscope stage.
Tracer experiment and microscopy. Two fluorescent tracers, rhodamine B and fluorescein, were used to study diffusion in S. epidermidis biofilms. These dyes were chosen because they are similar in size to many antibiotics and because they are relatively inexpensive. There are a few commercially available fluorescent antibiotics, but their cost would be prohibitive when used in a continuous-flow system like the one we describe. Biofilms were imaged by a Leica NT confocal scanning laser microscope in transmission mode with excitation from a 488-nm laser. For imaging rhodamine B diffusion, a 568-nm laser line was used for excitation and the fluorescent signal was detected in a red channel (585- to 615-nm band pass filter). For imaging fluorescein, a 488-nm laser line was used for excitation and the fluorescence emission was detected in a green channel (500- to 550-nm band pass filter). A 20x oil immersion objective was used for these experiments. After a suitable cell cluster was located in the transmission mode, the focal plane was set approximately 10 to 20 µm below the glass and inside the cluster. The microscope settings were changed from transmission mode to fluorescence mode to image either rhodamine B or fluorescein. A time series was initiated in which an image was collected every 5 s. At the same time, the flow of phosphate-buffered saline through the capillary was changed to buffer containing 5 mg of rhodamine B (Eastman Organic Chemicals, Rochester, N. Y.) per liter or 50 mg of disodium fluorescein (Sigma Aldrich, Milwaukee, Wis.) per liter. The time series typically ran for 5 to 10 min. Images were analyzed in MetaMorph software (Universal Imaging Corporation, Downington, Pa.).
Some experiments were performed in which a biofilm was exposed to both rhodamine B and fluorescein. This was done sequentially. First the biofilm was stained with rhodamine B. Then buffer was pumped through, and the experimenter waited for the rhodamine B to desorb and diffuse out of the biofilm. The fluorescein penetration experiment was then performed while the same spot in the biofilm was examined.
Estimation of diffusion coefficient. The fluorescence intensity at the center of a biofilm cell cluster was extracted at each time point by using the MetaMorph software. The resulting intensity versus time data were exported to a spreadsheet. The solution to the diffusion equation in spherical coordinates (1) was fitted to the experimental data by adjusting the values of two parameters, the steady-state staining intensity and the effective diffusion coefficient, to minimize the sum or errors squared. The mean radius of the cell cluster was estimated from the transmission image of the cell cluster.
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FIG. 1. Transmission mode scanning laser microscopy of S. epidermidis biofilms grown in glass capillary tubes. Panel A shows a section of the tube at low magnification, and panel B shows a cell cluster used for a diffusion experiment. Flow was from left to right in panel A and top to bottom in panel B.
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FIG. 2. Transient diffusion of rhodamine B into a S. epidermidis biofilm cell cluster imaged by confocal scanning laser microscopy. The time indicated is the time, in seconds, after the first appearance of the dye in the flow cell. The cell cluster shown is the same as that shown in Fig. 1B. A movie of this sequence can be viewed at http://www.erc.montana.edu/Res-Lib99-SW/Movies/Database/MD_DisplayScript.asp.
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FIG. 3. Rhodamine B staining intensity at the center of a S. epidermidis biofilm cell cluster for the experiment dated 14 February 2003. Time zero corresponds to the first appearance of the dye in the flow cell. Open circles represent experimental data, and the line indicates the fitted diffusion equation in spherical coordinates.
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FIG. 4. Profiles of rhodamine B staining intensity along radial transects through a S. epidermidis biofilm cell cluster for the experiment dated 14 February 2003. Zero on the x axis corresponds to the center of the cell clusters. Each curve is labeled with a time, in seconds, where time zero corresponds to the first appearance of the dye in the flow cell. Data were smoothed by the Lowess function to obtain the curves shown.
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The time scale for diffusive penetration of rhodamine B into S. epidermidis cell clusters, defined as the time required to attain 90% of the equilibrium staining intensity at the center of the cell cluster, ranged from 1.1 to 6.7 min for cell clusters ranging in diameter from about 240 to 590 µm (Table 1). The effective diffusion coefficients derived from these data ranged from 2.0 x 107 to 6.5 x 107 cm2 s1, or 6 to 18% of the diffusion coefficient in pure water (Table 1). The mean relative effective diffusion coefficient (the value in biofilm divided by the value in water) was 0.11 ± 0.05. The uncertainty indicated is the standard deviation. The diffusion coefficient of rhodamine B in water at 21.5°C, as calculated from the Wilke-Chang correlation, is 3.6 x 106 cm2 s1. There was no apparent trend of diffusion coefficient with cluster size.
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TABLE 1. Summary of measured effective diffusion coefficients of rhodamine B in S. epidermidis biofilma
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FIG. 5. A hollow S. epidermidis biofilm cell cluster stained with rhodamine B (red) and negatively stained by fluorescein (green).
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In several cell clusters with such hollow centers, the diffusive penetration of fluorescein was measured by time lapse microscopy by using the same protocols used for rhodamine B. The time required to attain 90% of the equilibrium staining intensity at the center of the cell cluster ranged from 1.4 to 2.2 min for cell clusters ranging in diameter from about 360 to 590 µm (Table 2). The effective diffusion coefficients derived from these data ranged from 1.0 x 106 to 2.1 x 106 cm2 s1, or 20 to 43% of the diffusion coefficient in pure water (Table 2). The mean relative effective diffusion coefficient for fluorescein was 0.32 ± 0.10, where the uncertainty indicated is the standard deviation. The diffusion coefficient of fluorescein in water at 21.5°C, as calculated from the Wilke-Chang correlation, is 4.9 x 106 cm2 s1.
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TABLE 2. Summary of measured effective diffusion coefficients of fluorescein in S. epidermidis biofilma
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FIG. 6. Rhodamine B () and fluorescein ( ) staining intensity at the center of the same S. epidermidis cell cluster. Time zero corresponds to the first appearance of the dye in the flow cell.
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The relative diffusion coefficients for rhodamine B (0.32) and fluorescein (0.11) in a staphylococcal biofilm measured in this investigation agree with reported relative effective diffusion coefficients for solutes of similar size in biofilms. The MW of rhodamine B is 442 and of fluorescein is 376. The mean relative effective diffusion coefficient for sucrose (MW, 342) in various biofilms is 0.19 (5). The relative diffusivity of the antibiotic ciprofloxacin (MW, 330) in Pseudomonas aeruginosa biofilms was reported to be 0.31 (8). The relative diffusion coefficient of chlorhexidine digluconate (MW, 898) in Candida albicans biofilms was approximately 0.2 (7). Tatevossian (9) reported a relative effective diffusion coefficient of inulin (MW,
5,200) of 0.12 in dental plaque. Together these measurements suggest that solutes with MWs in the range of a few hundred to a few thousand diffuse in biofilms at 10 to 35% of the rate they do in pure water.
Our conclusion that antibiotic-sized solutes penetrate S. epidermidis biofilms is consistent with the few reports in which antibiotic penetration has been experimentally measured in biofilms formed by this microorganism (2, 3, 10, 11). The rapid penetration we observed is also in agreement with the work of Stone et al. (6), who used confocal scanning laser microscopy to demonstrate tetracycline permeation throughout Escherichia coli biofilms within 3 min.
The progressive pattern of inward diffusion (Fig. 2) was symmetric in every experiment. More specifically, there was no difference in the permeation of dyes on the upstream and downstream edges of a cell cluster. If convective flow within the cell cluster contributed to the transport of the tracer, then one would expect to see greater penetration of dyes on the upstream edge of the cluster than on the downstream edge. The fact that this was not observed confirms that convective transport inside the cell cluster was insignificant.
The slower diffusion of rhodamine B compared to fluorescein was likely due to adsorbtion of rhodamine B to the biofilm matrix. Sorption is predicted, on theoretical grounds, to retard the penetration of a solute diffusing in a heterogeneous medium (4). While rhodamine B clearly bound to the biofilm, there was no indication that fluorescein interacted with the biofilm matrix (Fig. 5).
The inability of antimicrobial agents to control microorganisms in biofilms is often attributed to the failure of these agents to penetrate the biofilm. This explanation is simple and intuitive and could apply to antimicrobial agents of diverse chemistries. But this hypothesis is probably incorrect. As the visual and quantitative data reported in this article demonstrate, there is no generic physical barrier to the permeation of solutes the size of most biocides and antibiotics into microbial biofilm. Antimicrobial agents likely do penetrate biofilms in most cases, except when subject to rapid neutralizing reactions in the biofilm (4, 5). Mechanisms of biofilm protection that derive from the biology of microorganisms in biofilms should be pursued.
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