Previous Article | Next Article ![]()
Applied and Environmental Microbiology, May 2009, p. 2742-2749, Vol. 75, No. 9
0099-2240/09/$08.00+0 doi:10.1128/AEM.01790-08
Copyright © 2009, American Society for Microbiology. All Rights Reserved.

Center for Environmental Technology Research, Korea Institute of Science and Technology (KIST), Hawolgok-dong, Seongbuk-gu, Seoul 136-791, Republic of Korea,1 Public Health Microbiology Laboratory, Department of Environmental Health, Graduate School of Public Health, Seoul National University, Yeongeon-dong, Jongro-gu, Seoul 110-799, Republic of Korea,2 Aerosol and Bioengineering Laboratory, Department of Mechanical Engineering, Konkuk University, Hwayang-dong, Gwangjin-gu, Seoul 143-701, Republic of Korea,3 Aerosol and Particle Technology Laboratory, Department of Mechanical Engineering, Korea Advanced Institute of Science and Technology (KAIST), Guseong-dong, Yuseong-gu, Daejeon 305-701, Republic of Korea4
Received 3 August 2008/ Accepted 2 February 2009
|
|
|---|
3)-β-D-glucan concentration of fungal bioaerosols. More than 99% of the Aspergillus versicolor and Cladosporium cladosporioides bioaerosols lost their culturability in about 0.2 s when the surrounding temperature exceeded 350°C and 400°C, respectively. The instantaneous exposure to high temperature significantly changed the surface morphology of the fungal bioaerosols. |
|
|---|
Fungal bioaerosols constitute the major component of ambient airborne microorganisms (23, 50, 51). Several studies have reported that the concentration of fungal bioaerosols is relevant to the occurrence of human diseases and public health problems associated with acute toxic effects, allergies (3, 18), and asthma (4, 5, 13, 48). Fungal bioaerosols are of particular concern in healthcare facilities, where they can cause major infectious complications as opportunistic pathogens in patients with an immunodeficiency (9). For instance, invasive mycoses can affect patients undergoing high-dose chemotherapy for hematological malignancies associated with a prolonged period of neutropenia; they can also affect solid-organ transplant recipients. Despite all diagnostic and therapeutic efforts, the outcome of an invasive fungal infection is often fatal (with a mortality rate of around 50% for aspergillosis) (37). The main fungal genera responsible for these infections are as follows: Aspergillus spp., Fusarium spp., Scedosporium spp., and Mucorales spp. (10, 12, 20). However, virtually any filamentous fungus can be a pathogen (22, 41). In the hospital environment, possible sources of airborne nosocomial infection include ventilation or air-conditioning systems, decaying organic material, dust, water, food, ornamental plants, and building materials in and around hospitals (1).
One of the major bioaerosols of concern is (1
3)-β-D-glucans, which comprises up to 60% of the cell wall of most fungal organisms. The (1
3)-β-D-glucans are glucose polymers with a variable molecular weight and a degree of branching (49). The results of several studies about the exposure of subjects to airborne (1
3)-β-D-glucans suggest that these agents play a role in bioaerosol-induced inflammatory responses and resulting respiratory symptoms, such as a dry cough, phlegmy cough, hoarseness, and atopy (11, 44). In addition, given that many epidemiological studies have reported that (1
3)-β-D-glucan has strong immuno-modulating effects (42, 47), (1
3)-β-D-glucan is an important parameter for exposure assessment by itself and as a surrogate component for fungi (16).
To prevent the adverse health effects of fungal bioaerosols, we must ensure that control methods for airborne fungal spores are studied and developed. However, despite the necessity of controlling fungal bioaerosols, few studies have focused on such control mechanisms. The most common control methods are UV irradiation and electric ion emission. Given that UV irradiation is known to have a germicidal effect, several studies have examined how UV irradiation affects the viability of bioaerosols (35, 42). However, although UV irradiation can be easily applied by simply installing and turning on a UV lamp, the 254-nm-wavelength UV light produces ozone and radicals, which cause harmful effects to surrounding humans. Electric ion emission has also been studied as a means of controlling bioaerosols (21, 27). When the efficiency of the filter is increased, the efficacy of respiratory protection devices against bioaerosols can be enhanced. Although electric ions decrease the viability of airborne bacteria (25), the generation of the ions produces ozone, a pollutant, and also causes electric charges to accumulate on surrounding surfaces.
Recently, heat treatment of indoor air using thermal processes has been considered a safe, effective, and environment-friendly method; it does not produce ozone or use ion or filter media. A thermal heating process has long been considered a suitable and reliable method for controlling microorganisms. Two types of heat are generally used, moist heat and dry heat. Moist heat utilizes steam under pressure, whereas dry heat involves high-temperature exposure without additional moisture. Several types of heat treatment are currently used for killing microorganisms. The treatments include incineration, Tyndallization, pasteurization, and autoclaving (32). However, most of these technologies were originally limited to controlling microorganisms in liquid or on material surfaces. In addition, they may not be adequate for controlling bioaerosols because the continuous surrounding environment of bioaerosols is significantly different from the conditions in liquid and on solid surfaces. Therefore, it is necessary to find adequate and practical conditions for controlling bioaerosols. Thus far, several investigations regarding the use of thermal processes against bioaerosols have been reported. Some of these studies have targeted airborne bacteria spores widely used as surrogates for biological warfare agents (8, 34), while others have focused on environmental parameters for the culture and survival of various vegetative cells (14, 29, 46). However, in these studies novel techniques for aerosols, such as measuring and analyzing aerosol particle size, distributions, and concentrations, were not utilized. In addition, to the best of our knowledge, there has been no study on the use of a thermal process for controlling fungal bioaerosols in continuous airflow. Fungal bioaerosols were found to be very resistant to a thermal environment in previous studies.
In this study, we investigated the thermal heating effects on the physical, chemical, and biological properties of fungal bioaerosols using a high-temperature, short-time (HTST) sterilization process. The HTST process, a type of thermal heating process, is based on high-temperature stresses for very short periods. Although this thermal process has been used for the microbial decontamination of seeds and dried, powdered products, such as pharmaceuticals and heat-sensitive drink and food, it can be also applied to the control of an airborne microorganism in a continuous-flow system, such as a heating, ventilation, and air-conditioning system (15, 33, 38). When the fungal bioaerosol was passed through a thermal electric heating system, the fungal spores were exposed to various temperatures for short periods. Then, we examined the bioaerosol and aerosol characteristics, including aerosol size distribution, culturability, (1
3)-β-D-glucan production, and surface morphology, using a novel technique for sampling and measuring aerosols.
|
|
|---|
![]() View larger version (31K): [in a new window] |
FIG. 1. Experimental setup. The fungal bioaerosols generated from the mold surface were transported by air flowing from the top outlet of the generator to the inlet of the sampling chamber. The sampling chambers were positioned at the inlet and the outlet of the thermal electric heating system. An airflow containing fungal bioaerosols was sampled in order to measure the total particle number concentration (QCPC) and the aerodynamic particle size distribution (QPSD) and to analyze the viability of the fungal bioaerosol (QBIO). MFC, mass flow controller.
|
Thermal electric heating system.
The designed thermal system consisted of a quartz tube (inner diameter, 29 mm; length, 700 mm; thickness, 1 mm) and an electric heating controller (MC-P; Poong Lim Co., Seoul, South Korea). The thermal heating system used electric heating coils of the ohm resistance type because the heating coils can be installed easily in existing air-conditioning systems. The heating coils were located outside the quartz tube and were covered with insulating materials of ceramic powder and glass fiber fabric so that passing bioaerosols could be exposed to a high-temperature environment without any obstruction of the bioaerosol flow stream. For experimental temperature conditions from 20°C (normal temperature) to 700°C, the residence time of the airflow between the inlet and outlet of the quartz tube in the thermal system was estimated to be from about 0.29 s (room temperature) to 0.17 s (700°C), with allowance for the air volume expansion due to the increase in temperature. Figure 2 shows the details of the thermal electric heating system.
![]() View larger version (41K): [in a new window] |
FIG. 2. Detail and center temperature distributions of the thermal electric heating system. Temp, temperature.
|
Aerosol measurement system.
The aerodynamic particle size distributions of the fungal bioaerosols were measured with a particle size distribution analyzer (PSD 3603; TSI Inc., MN). The PSD 3603 has 128 size channels ranging from 0.3 µm to 700 µm. While measuring the particle size distributions, we also used a condensation particle counter (CPC 4330; HCT Inc., South Korea) to measure the total particle number concentration of the fungal bioaerosols. The CPC 4330 has a maximum detectable concentration of 10,000 particles/cm3 and a minimum particle size of 15 nm, with 95% accuracy. Before the experiments with fungal spores, we used HEPA-filtered clean air to flush the system until the PSD 3603 and CPC 4330 could no longer detect any particles. The total fungal bioaerosol particle number concentrations in the inlet and outlet sampling chambers were used to calculate the viability of fungal bioaerosols.
Culturability determination.
A BioSampler (SKC Inc., PA) was used for fungal bioaerosol sampling before and after the thermal heating treatment. The fungal bioaerosols were collected into 20 ml of phosphate-buffered saline (pH 7.0) water at a nominal flow rate of 12.5 liters/min. The sampling time of the BioSampler was 15 min for each test. Stainless steel tubing, which can sufficiently cool the sampled air to avoid heat shock when hot spores reach a cold sampler medium, was used as sampling tubing. The sample from the BioSamplers was serially diluted and plated on 2% MEA culture plates. The plates were incubated at 25°C ± 2°C for 7 days. The number of colonies was enumerated, and the CFU concentrations (CFUInlet or CFUOutlet) were calculated per milliliter (CFU/ml) of sampled suspension by taking into account the measured fungal spore number concentration. The relative culturability of the bioaerosols was determined as the ratio of the culturability of the bioaerosols in the outlet BioSampler to the culturability of the bioaerosols in the inlet BioSampler, and the culturability loss was obtained from the relative culturability according to the following equations:
![]() | (1) |
![]() | (2) |
Assay of (1
3)-β-D-glucan.
A portion of the fungal particle suspension was analyzed for (1
3)-β-D-glucan by using the kinetic chromogenic Limulus amebocyte lysate method (Glucatell Associates of Cape Cod, East Falmouth, MA). For analysis, we added 0.5 ml of 0.6 M NaOH to each 0.5-ml suspension of fungal particles. This suspension was shaken with a mechanical shaker for 1 h so that we could extract the (1
3)-β-D-glucan from the suspended fungal particles by unwinding its triple-helix structure and making it water soluble. Next, we transferred 25-µl aliquots of the suspension samples to 96-microwell plates and added 50 µl of specific (1
3)-β-D-glucan lysate. The plates were incubated in an absorbance microplate reader (Infinite M200 microplate reader and Magellan, version 6, software; Tecan Ltd., Männedorf, Switzerland), and the kinetics of the ensuing color reaction were read at 405 nm. The (1
3)-β-D-glucan results were expressed as concentrations (ng/m3 of air) based on the sampling flow rate and the sampling time of the BioSampler. This ratio is also calculated by taking into account the fungal spore number concentrations of fungal bioaerosols during the sampling time. Finally, the (1
3)-β-D-glucan removal rate by the HTST process was obtained from the relative (1
3)-β-D-glucan ratio according to the following formulas:
![]() | (3) |
![]() | (4) |
SEM analysis.
The morphology of fungal bioaerosols was investigated with the aid of scanning electron microscope (SEM) analysis (XL30S FEG; Phillips, The Netherlands). For this purpose, fungal bioaerosols exposed to various temperatures were sampled onto a 13-mm mixed cellulose ester filter with a pore size of 1.2 µm (Millipore Corporation, MA) downstream from the outlet sampling chamber for 5 min. After the sampling process, the mixed cellulose ester filters were coated with an osmium coater by means of a chemical vapor deposition method (HPC-1SW; Vacuum Device Inc., Japan) and then analyzed with a SEM.
Statistical analysis.
All the experimental data were analyzed statistically in terms of analysis of variance, a t test, and linear regression by using the software package SAS, version 9.1, of Microsoft Windows.
|
|
|---|
Aerodynamic size distribution and morphology.
Figure 3 shows the variations in the normalized aerodynamic particle size distributions of A. versicolor and C. cladosporioides fungal bioaerosols under conditions of elevated surrounding temperatures. The aerodynamic diameter, of an aerosol particle is equivalent to the diameter of standard density sphere particles that have the same gravitational settling velocities as the original particles (23). The number concentration of particles in the air, which was recorded for each channel size of the instrument (PSD 3603; TSI Inc., MN), was divided by the logarithmic interval of the corresponding particle size range and plotted as a function of the aerodynamic diameter for the experimental conditions of each fungus. The particle number concentrations were then normalized in terms of the values of the highest concentration under each condition. From this figure, the increase of the surrounding temperature inside the thermal heating tube was found to shift the aerosol particle size distributions of the fungal bioaerosols. As shown in Fig. 3 and 4, the geometric mean aerodynamic diameter (GMD) of the two species of fungal bioaerosols decreased as the surrounding temperature increased, and the geometric standard deviation (GSD) increased as the surrounding temperature increased. Compared with normal temperature conditions (17°C to 21°C), the GMD reduction ratio [1 – (outlet GMD/inlet GMD)] of the A. versicolor fungal bioaerosol was about 7.7% at 400°C and about 34.5% at 700°C. In the case of C. cladosporioides, the GMD reduction ratio was about 9.2% at 400°C and about 30.1% at 700°C. There was little variation in the GSD (<0.6% for A. versicolor and <1.5% for C. cladosporioides) of the fungal bioaerosols until 500°C, and their respective GSD values increased when the temperature exceeded 500°C.
![]() View larger version (45K): [in a new window] |
FIG. 3. Variation in the aerodynamic particle size distribution of A. versicolor and C. cladosporioides with surrounding temperature conditions. N, number concentration of particles in the air; da, aerodynamic diameter; Max, maximum. Temperature is in °C.
|
![]() View larger version (26K): [in a new window] |
FIG. 4. Variation in the GMD and GSD of A. versicolor (a) and C. cladosporioides (b) with surrounding temperature conditions. The error bars indicate standard deviations (n = 3).
|
![]() View larger version (131K): [in a new window] |
FIG. 5. SEM images (magnification, x30,000) at temperatures of 20°C (a), 400°C (b), and 700°C (c) of A. versicolor spores and at temperatures of 20°C (d), 400°C (e), and 700°C (f) of C. cladosporioides spores. The surface morphology of the sampled fungal particles becomes smoother at elevated temperature conditions.
|
![]() View larger version (22K): [in a new window] |
FIG. 6. Culturability loss of the A. versicolor and C. cladosporioides bioaerosols in relation to the surrounding temperature. The error bars indicate standard deviations (n = 5).
|
Use of the HTST process to remove (1
3)-β-D-glucan.
Thermal heating is one of the most effective depyrogenation methods. We tested the efficiency of the thermal heating process on the removal of (1
3)-β-D-glucan in A. versicolor bioaerosols. As seen in Fig. 7, an increase in the surrounding temperature produced a significant decline in the A. versicolor (1
3)-β-D-glucan concentration. The removal ratio (equation 4) of (1
3)-β-D-glucan ranged from 4.8% ± 6.11% (200°C) to 32.2% ± 2.27% (700°C). We conducted a linear regression analysis, which showed that the total (1
3)-β-D-glucan removal ratio was significantly correlated with the combined GMD reduction ratio of the fungal particles (P value of <0.05; R2 = 0.9196) (Fig. 8).
![]() View larger version (28K): [in a new window] |
FIG. 7. Removal ratio (percent) of (1 3)-β-D-glucan from the thermal HTST process. The error bars indicate standard deviations (n = 3).
|
![]() View larger version (20K): [in a new window] |
FIG. 8. Linear regression analysis of the (1 3)-β-D-glucan removal ratio (percent) versus the GMD reduction ratio (percent) by exposure to high temperature conditions. The dashed line is 1:1.
|
|
|
|---|
3)-β-D-glucan because the oxidation process partially vaporizes and melts materials such as the (1
3)-β-D-glucan of fungal bioaerosols. As seen in Fig. 6, more than 99% of the A. versicolor and C. cladosporioides bioaerosols lost their culturability at 350°C and 400°C, respectively, in this HTST process. The growth of a microorganism on a material surface can be inactivated by general dry heat treatment at 140°C for approximately 3 h (36), at 180°C for 15 min (6), or at 400°C for 20 s to 30 s (7). However, our results demonstrate that fungal bioaerosols in a continuous airflow can be inactivated by exposure to a high temperature in a thermal electric heating system at 350°C (A. versicolor) and 400°C (C. cladosporioides) for about 0.2 s. This result supports the view that the inactivation conditions for airborne microorganisms differ from those for microorganisms in food or water.
Prolonged exposure to conditions of dry air can affect the viability of microorganisms. The relative humidity in a continuous airflow with an atmospheric pressure condition drops to almost 0% when the temperature exceeds 100°C. Hong et al. (24) used the model to predict the effect of temperature and moisture on various conidia fungi. At a relative humidity of almost 0% and a temperature range of 4°C to 37°C, the time required to yield 50% survival is approximately 10 days to 1,000 days. In our HTST process, the exposure time was always less than 0.3 s. In addition, as shown in Fig. 6, the culturability loss data at 50°C for the two fungal species confirm much lower culturability losses of only 5.5% for A. versicolor and 6.12% for C. cladosporioides. Therefore, for these study conditions, we think the dry-air condition has little effect in terms of desiccation on the viability of fungal spores during brief exposure times; oxidation, on the other hand, has a dominant effect on the viability of fungal spores.
Fungi produce many agents that can be toxic with sufficient exposure. In general, there are two classes of these agents: secondary products of metabolism (e.g., mycotoxins, antibiotics, and volatile organic compounds) and structural components [e.g., (1
3)-β-D-glucan]. In this study, we showed that an increase in the surrounding temperature produced a significant decline in the A. versicolor (1
3)-β-D-glucan concentration. The standard depyrogenation treatment in the pharmaceutical industry for heat-stable materials has been to expose them to temperature conditions greater than 270°C for more than 30 min in a closed system (30). However, in our study, we obtained a (1
3)-β-D-glucan removal ratio of more than 30% by maintaining a temperature of 700°C for only about 0.2 s. Although we could not compare this result to that of previous studies because few studies have been published on the removal of (1
3)-β-D-glucan by an HTST process in a continuous-flow system, this result shows the possibility of rapid removal of (1
3)-β-D-glucan, which is a thermally stable component. In addition, the condition of either a high temperature of more than 700°C or a long exposure time of more than 0.2 s is needed for a (1
3)-β-D-glucan removal ratio of more than 30% in this system. In the data shown in Fig. 8, the correlation between the total (1
3)-β-D-glucan removal ratio and the combined GMD reduction ratio of the fungal bioaerosols shows that the particle GMD reduction ratio can be a sensitive indicator for determining the (1
3)-β-D-glucan removal ratio in the thermal inactivation process.
The presented thermal HTST process was found to be very effective for controlling fungal bioaerosols in continuous airflow. Parameters and mechanisms for the inactivation of airborne microorganisms are useful to meet the increasing need for developing extensive control methods for fungal bioaerosols.
Published ahead of print on 6 February 2009. ![]()
|
|
|---|
3)-beta-D-glucan causes airway eosinophilia. Mediators Inflamm. 10:13-19.[Medline]
3)-β-D-glucancan. Environ. Health Perspect. 107(Suppl. 3):501-503.[Medline]
3)-β-D-glucancan in healthy humans. Mediators Inflamm. 10:173-178.[Medline]
3)-β-D-glucan immunobiology. Mediators Inflamm. 6:247-250.[CrossRef][Medline]
| |||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||
Copyright © 2009 by the American Society for Microbiology. For an alternate route to Journals.ASM.org, visit: http://intl-journals.asm.org | More Info»