Abstract
Introduction
Volatile organic compounds (VOCs) readily penetrate the respiratory tract and cross the air–liquid interface (ALI), yet their in vitro deposition behavior and dose uniformity remain poorly characterized.
Methods
In this study, we evaluated the delivered concentration in the basolateral compartment and inter-transwell variability of isopropyl alcohol (IPA), acetone, and benzyl alcohol (BA) in a six-transwell ALI exposure system. VOCs were generated by atomization at airflow rates of 0.2−3 L/min and delivered for 1–2 h. Delivered concentrations were quantified using photoionization detection or UV–Vis spectroscopy, and aerosol characteristics were monitored by scanning mobility particle sizing.
Results
Despite rapid evaporation and predominantly vapor-phase transport of IPA and acetone, and semi-volatile aerosol BA, VOC delivery to the ALI was reproducible and spatially uniform. IPA and acetone exposures produced coefficients of variation (CVs) below 10% and 16%, respectively, across transwells, whereas benzyl alcohol exhibited higher variability (CV ≤ 19%) due to its lower vapor pressure and higher viscosity. No statistically significant positional differences were observed under any exposure condition.
Discussion
These findings indicate that volatile organic compounds delivered to the ALI undergo diffusion-driven gas–liquid delivery, resulting in a relatively uniform spatial distribution. This study provides exposure-relevant delivery characterization for VOCs and semi-VOCs in ALI systems, supporting future NAM-based inhalation studies without implying biological dose equivalence.
Keywords: air-liquid interface, delivery, diffusion, in vitro inhalation, organic solvents, VOCs
1. Introduction
VOCs are widely used in industrial, laboratory, and consumer products, and inhalation is a major route of human exposure. Upon entering the respiratory tract, volatile and semi-volatile organic compounds can cross the alveolar–capillary barrier and distribute systemically, leading to both acute and chronic health effects, including central nervous system depression, hepatic dysfunction, and respiratory irritation. The dynamics of solvent uptake in the lung depend on the physicochemical properties of the solvent, particularly vapor pressure, solubility, and diffusivity, which govern partitioning across the air–liquid interface (ALI) (World Health Organization, 2000; Agency for Toxic Substances and Disease Registry, 1997).
Inhalation toxicity testing is costly and resource-intensive, driving the adoption of new approach methodologies (NAMs), including in vitro and in silico test systems, to improve efficiency and ethical standards (Kleinstreuer et al., 2016; EPA, 2021). In vitro ALI exposure systems provide a controlled platform for simulating inhalation exposure while reducing the use of animals in toxicology testing. These systems allow direct contact of airborne materials with cultured lung cells or liquid interfaces, enabling precise quantification of deposited or delivered doses. To ensure relevance to in vivo outcomes, in vitro NAM-based test systems must be supported by dosimetry and dose metrics equivalent to those used in vivo tests (Lee et al., 2025a). Among these, air–liquid interface (ALI) systems expose the apical cell surface to aerosols (the term aerosol includes both the particles and the suspending gas, which is usually air; particle size ranges from about 0.002 to more than 100 ㎛, Hinds, 1999), usually under controlled airflow while maintaining contact with the basal medium. ALI platforms include flow-through systems (e.g., Vitrocell®) and alternatives based on electrostatic precipitation, gravitational settling, or hybrid deposition mechanisms (Lucci et al., 2018; Jeannet et al., 2015; Savi et al., 2008; de Bruijne et al., 2009; Lenz et al., 2009; Aufderheide and Scheffler, 2013). While air–liquid interface (ALI) exposures using transwell systems have become a standard method for simulating inhalation of particulate aerosols and nanomaterials in vitro (Lenz et al., 2009; Aufderheide and Mohr, 2004; de Bruijne et al., 2009; Lenz et al., 2014; Mulhopt et al., 2016), most studies have primarily focused on establishing physiologically relevant exposure conditions and quantifying delivered dose. However, comparatively little attention has been paid to evaluating inter-transwell deposition variability or deposition homogeneity, parameters essential for ensuring the reproducibility and reliability of in vitro inhalation toxicology data. Although recent work has begun to address spatial uniformity and measurement accuracy across exposure wells (Polk et al., 2019; Gkanis et al., 2021), the systematic assessment of deposition reproducibility between wells within a single exposure run remains limited, highlighting a methodological gap in the current ALI testing frameworks.
Several studies have examined organic solvents for VOCs. Organic solvent 1,3-dichloropropene (1,3-DCP) using an in vitro and in silico approach to assess inhalation toxicity. Using human airway epithelial models representing five respiratory regions, researchers measured cytotoxicity and barrier integrity after exposure and applied dosimetry modeling to predict in vivo outcomes. Predicted toxicity thresholds aligned well with animal data, showing a gradient of sensitivity from nasal to alveolar tissues. The results support these integrated methods as viable alternatives to traditional animal testing for inhalation safety assessment (Moreau et al., 2022). Benchmark Dose Modeling Approaches for Volatile Organic Chemicals (VOCs) applied using a novel in vitro air–liquid interface (ALI) exposure system for assessing the toxicity of volatile organic chemicals (VOCs) under physiologically relevant conditions. Using BEAS-2B and primary human bronchial epithelial (pHBEC) cells, researchers evaluated cytotoxicity, cell viability, and gene-expression changes following exposure to several VOCs. Benchmark dose modeling of gene expression identified sensitive molecular responses that aligned closely with known human and animal toxicity data. The findings support this ALI-based approach as a promising method for determining molecular points of departure in airway toxicity testing of volatile chemicals (Speen et al., 2022). Jackson et al. (2025) compared transcriptomic responses to volatile organic chemicals (VOCs) between in vitro human airway models and in vivo mouse inhalation exposures. Using whole-transcriptome and physiologically based toxicokinetic (PBTK) modeling, researchers found largely comparable (<2-fold) points of departure across systems, except for dichloromethane, which differed due to species-specific metabolism. Despite distinct gene expression profiles, Hmox1 was consistently upregulated across models. These findings demonstrate the value of NAM-based test systems when coupled with refined internal dose modeling for improving in vitro–in vivo extrapolation (IVIVE) in inhalation toxicity assessment. The workshop, organized by the American Cleaning Institute (ACI), reviewed the use of in vitro new approach methodologies (NAMs) to assess respiratory irritation, highlighting the importance of exposure characterization and dosimetry to support NAM-derived data in human health risk assessment. Experts discussed exposure systems, cell and tissue models, and integration of NAM data with existing toxicological information. Key outcomes included the need for standardized assay characterization, improved dosimetry and exposure relevance, and guidance to align NAM-derived points of departure (PODs) with current risk assessment practices. The proceedings highlight priorities for advancing and harmonizing in vitro methods in respiratory safety evaluation (Haber et al., 2024).
While ALI exposure has been extensively applied to particulate aerosols and nanomaterials, the in vitro delivery characteristics of volatile organic chemicals with high evaporation rates and rapid diffusion have been seldom studied. Isopropyl alcohol (IPA) and acetone are representative water-miscible solvents with relatively high vapor pressures and rapid evaporation rates, and benzyl alcohol is also a water-soluble solvent with low vapor pressure and high viscosity. Understanding their delivery behavior may provide essential information for interpreting in vitro exposure results and correlating them to real-world inhalation scenarios.
In this study, we conducted a series of in vitro VOC aerosol exposure studies to characterize delivery and inter-transwell delivery to the basolateral compartment, using IPA, acetone, and BA aerosols on 6-transwell ALI plates under different generation flow rates and exposure durations. We quantified delivered VOC concentrations and assessed the homogeneity of delivery (or inter-transwell variation) across transwells. The goal was to determine whether volatile solvent aerosols can achieve consistent, measurable delivery to the ALI, thereby providing foundational data for future studies of solvent inhalation toxicity. Although air–liquid interface exposure systems are frequently discussed within the context of NAM-based inhalation testing, the present study does not introduce a new toxicological test method; rather, it focuses on characterizing delivery and deposition variability to support interpretation of in vitro inhalation studies.”
2. Materials and methods
2.1. Generation of test aerosol
Isopropyl alcohol (IPA, ForPro, item #140258), acetone (ForPro, item #140024), and benzyl alcohol (BA, DMSO Store Inc.) were aerosolized using purified air as the carrier gas. Their chemical properties are shown in Table 1. A mass flow controller (MFC, AERA, FC-7810CD4, V, Tokyo, Japan) was used to generate organic solvent aerosol with air flows of 0.2-3 LPM (L/min). Figure 1 shows the schematic of the solvent aerosol generation and exposure system.
TABLE 1.
Chemical properties at 20 °C.
| VOCs | Water solubility | Vapor pressure | Viscosity | Reference |
|---|---|---|---|---|
| Isopropyl alcohol | Miscible in all proportions with water | ∼44 mmHg (≈5.9 kPa | ∼2.4 mPa·s | www.intersurfchem.com |
| Acetone | Miscible in all proportions with water | ∼181.7 mmHg (≈24.2 kPa) | ∼0.32 mPa·s | https://macro.lsu.edu/HowTo/solvents/acetone.htm?utm_source=chatgpt.com |
| Benzyl alcohol | ∼4.29 g/100 mL | ∼0.167 mmHg (≈0.022 kPa) | ∼5.5–5.8 mPa·s | Registration https://echa.europa.eu/registration-dossier/-/registered-dossier/14748/4/9Dossier - ECHA |
FIGURE 1.
VOC aerosol generation scheme. Arrows indicate air flow direction. (A) fresh air; (B) air cleaner; (C) valve; (D) atomizer; (E) valve; (F) diffuser; (G) PID; (H) SMPS, (I) HIVIS; (J) 6-way collector; (K) impinger; (L) sampling cassette; (M) pump.
The generated VOC aerosols were diluted in a diffuser with five nozzles and delivered to a HIVIS (HCT In Vitro Inhalation System, Figure 2), which delivered them into a 6-transwell. The exhausted air was passed through an impinger to measure the air concentration. The flow rate to the exhausted sampling cassette was 30 mL/min, assuming 5 mL/min per transwell, respectively, using a low flow sampling pump (Gilian LFS-113, Sensidyne, St. Petersburg, FL), which was previously calibrated by a Bios calibrator (Dry Cal DC Lite, Butler, NJ). The HIVIS system accommodated a commercial 6-transwell plate (Falcon cat. 353046) with inserts (0.4 ㎛ transparent Polyethylene terephthalate (PET) membrane, cat. 353090), and each transwell was fitted with an axial-flow inlet funnel and an outlet for exhausted air (Figure 2). A 6-well plate containing cell culture inserts, with 2 mL of water below the inserts, was exposed to VOCs for various durations. We used 100% isopropyl alcohol and acetone to generate VOC aerosols, and 30% benzyl alcohol in ethyl alcohol to reduce viscosity and improve aerosol generation. We used the acellular system to monitor the delivery of VOCs to the ALI. The exposure period was initially 2 h for VOCs. Still, it changed to 1 h for acetone due to rapid consumption of the test material, and benzyl alcohol due to the relatively high viscosity. High-viscosity aerosols tend to form larger, less stable droplets, leading to increased wall losses and reduced delivery efficiency, resulting in lower and more variable delivered doses compared with low-viscosity aerosols (Gou et al., 2025). Therefore, the diffuser condensates benzyl alcohol aerosols, and all tubes from the atomizer to the HIVIS and the collector were cleaned with water and dried after exposure to prepare for the next exposure experiment. All test material generation and monitoring are conducted in a fume hood.
FIGURE 2.
Exposure and exhaust funnel to transwells in HIVIS. Arrows indicate flow direction.
2.2. Droplet evaporation rate estimation
The droplet evaporation rate was calculated based on the formula
where:
d0 = initial diameter
K = evaporation constant (m2/S; depends on vapor pressure, diffusivity, temperature)
d(t) = droplet constant at time t
t = time
2.3. Monitoring of in vitro inhalation and analysis of aerosols
The distribution and maintenance of VOC aerosols in terms of size and number were measured directly using an SMPS (size range: 9–294 nm; ART Plus, Icheon, Korea), which monitored particle diameter and number during the exposure periods. The air samples were collected into 20 mL of water in an impinger at the HIVIS outlet port using a Gilian flow sampler pump at a flow rate of 30 mL/min.
2.4. Determination of delivered concentration to the basolateral compartment
This study was not designed to achieve absolute mass closure relative to the mass initially nebulized. Unavoidable losses due to evaporation, adsorption onto tubing, and interactions with the chamber wall are inherent to exposure systems involving volatile organic compounds. Accordingly, this work focuses on relative delivery efficiency and inter-transwell variability under controlled exposure conditions, rather than on complete mass balance.
An impinger-based analytical method was employed to enable rapid and quantitative determination of volatile organic compounds (VOCs) transferred to the basolateral compartment. This approach was selected because highly volatile compounds cannot be reliably quantified using conventional gravimetric or filter-based methods. The impinger method allows real-time detection of VOCs aerosolized from aqueous media using a photoionization detector (PID), thereby minimizing analytical losses associated with solvent extraction or chromatographic separation.
To generate calibration curves, serial dilutions of each VOC were prepared, and 2 mL of each diluted solution was added to an impinger. Air exiting the impinger was sampled into a PID (Industrial Scientific iBRID MX6; flow rate 0.3 L·min-1), and PID responses were recorded to construct standard curves (Figures 3, 4A). For exposure experiments, transwells containing 2 mL of water in the basolateral compartment were exposed for 1–2 h. Following exposure, the entire 2 mL of basolateral medium was collected and transferred to an impinger. The liquid was aerosolized using a sampling pump (Figure 3), and the resulting VOC-containing aerosol was analyzed in real time by the PID. VOC concentrations in the basolateral compartment were determined using the corresponding calibration curves.
FIGURE 3.

VOC analysis using an impinger and a PID. (A) PID; (B) Impinger. Air drawn from the impinger containing 2 mL of sample was analyzed by PID. The entire 2 mL of basolateral medium was collected and transferred to an impinger (B). The liquid was aerosolized using a sampling pump (A), and the resulting VOC-containing aerosol was analyzed in real time by the PID. VOC concentrations in the basolateral compartment were determined using the corresponding calibration curves.
FIGURE 4.
Standard curves to determine volatile organic chemical deposition to the transwell. Solid line, measured; dotted, regression. (A) Isopropyl alcohol and acetone. (B) Benzyl alcohol.
Isopropyl alcohol and acetone concentrations were quantified using PID-based standard curves (Figure 4A), constructed by plotting known solution concentrations against PID detector responses (ppm). Benzyl alcohol concentrations were quantified using a UV–Vis spectrophotometer at 265 nm, corresponding to the maximum absorbance of the benzene ring; the calibration curve is shown in Figure 4B.
Percent delivery was calculated as the relative metric (mean VOC concentration in the basolateral compartment divided by the corresponding air concentration at the impinger) × 100. This metric is intended to assess relative delivery efficiency and inter-transwell variability and does not represent a biological dose or absolute deposited mass. Air concentrations were derived from impinger-captured VOC concentrations, accounting for the total sampled air volume and applying appropriate unit conversions. All experiments were conducted under controlled environmental conditions at 20 °C and 40%–60% relative humidity.
2.5. Statistical analysis
The statistical analysis was performed using SPSS version 22.0 (IBM, New York, United States). Data were presented as mean ± standard deviation (SD) and the coefficient of variation (CV).
The statistical analysis was performed using ANOVA for the 6-transwell data from Table 3 to Table 5.
TABLE 3.
Delivered IPA to the basolateral compartment (2 mL) of 6-transwell (MFC 3 LPM; 2-h exposure, 30 mL/min pump flow-rate) (n = 12).
| Trans-well | 1 | 2 | 3 | 4 | 5 | 6 | Mean | SD | CV | Impinger conc. | Total mass in impinger | Total air volume sampled | Air conc | ppm in air | Delivery |
|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|
| Exp | ppm | ppm | ppm | ppm | ppm | ppm | ppm | | % | ppm | mg | m3 | mg/m3 | ppm | % |
| 1 | 10,811 | 11,495 | 11,298 | 9,022 | 9,324 | 9,232 | 10,197 | 1,127 | 10.96 | 3,601 | 72.02 | 0.0036 | 20,006 | 8,139 | 125.3 |
| 2 | 10,956 | 11,628 | 9,785 | 11,228 | 9,927 | 9,114 | 10,440 | 975 | 9.17 | 5,720 | 114.40 | 0.0036 | 31,778 | 12,928 | 80.8 |
| 3 | 7,996 | 10,220 | 11,746 | 10,956 | 12,785 | 11,128 | 10,805 | 1,623 | 15.02 | 3,996 | 79.92 | 0.0036 | 22,200 | 9,031 | 119.6 |
| 4 | 13,641 | 14,825 | 11,667 | 11,259 | 11,759 | 13,483 | 11,272 | 1,415 | 10.75 | 3,996 | 79.92 | 0.0036 | 22,200 | 9,031 | 124.8 |
| 5 | 10,897 | 11,936 | 12,256 | 11,179 | 12,295 | 11,077 | 11,607 | 628 | 5.41 | 3,846 | 76.92 | 0.0036 | 21,367 | 8,692 | 133.5 |
| 6 | 11,205 | 11,090 | 12,333 | 12,615 | 11,667 | 12,064 | 11,829 | 615 | 5.2 | 5,782 | 115.64 | 0.0036 | 32,122 | 13,068 | 90.5 |
| 7 | 14,038 | 10,987 | 11,243 | 12,949 | 14,541 | 14,730 | 13,098 | 1,664 | 13 | 5,833 | 116.66 | 0.0036 | 32,406 | 13,183 | 99.4 |
| 8 | 14,523 | 14,603 | 12,641 | 14,308 | 14,167 | 12,859 | 13,850 | 869 | 6.26 | 6,538 | 130.76 | 0.0036 | 36,322 | 14,777 | 93.7 |
| 9 | 19,122 | 15,570 | 14,581 | 13,500 | 17,000 | 13,108 | 15,513 | 2,281 | 14.7 | 5,270 | 105.40 | 0.0036 | 29,278 | 11,911 | 130.2 |
| 10 | 25,540 | 25,959 | 24,635 | 22,838 | 20,946 | 21,243 | 23,527 | 2,170 | 9.22 | 11,459 | 229.18 | 0.0036 | 63,661 | 25,899 | 90.8 |
| 11 | 11,429 | 14,280 | 12,614 | 13,600 | 14,200 | 14,643 | 13,461 | 1,223 | 9.09 | 9,914 | 198.28 | 0.0036 | 55,078 | 22,407 | 60.1 |
| 12 | 16,457 | 19,486 | 16,600 | 14,540 | 15,142 | 15,557 | 16,290 | 1755 | 10.77 | 4,429 | 88.58 | 0.0036 | 24,606 | 10,010 | 162.7 |
| | 13,385 ±4,721 |
14,339 ±4,505 |
13,450 ±3,923 |
13,166 ±3,448 |
13,646 ±3,172 |
13,185 ±3,267 |
13,491 ±3,712 |
| 9.96 ±3.3 |
5,865 ±2,463 |
117 ±49 |
0.0036 | 32,585.2 ±13,687.8 |
13,256.4 ±5,568.5 |
109.3 ±28.2 |
SD, standard deviation; CV, coefficient of variation; % Delivery = (mean concentration of tanswell (ppm)/(ppm in air) x 100%.
TABLE 5.
Delivered acetone to the basolateral compartment (2 mL) of 6-transwell (MFC 2 LPM; 1-h exposure, 30 mL/min pump flow-rate) (n = 5).
| Trans-well | 1 | 2 | 3 | 4 | 5 | 6 | Mean | SD | CV | Impinger conc | Total mass in impinger | Total air volume sampled | Air conc | ppm in air | Delivery |
|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|
| Exp | ppm | ppm | ppm | ppm | ppm | ppm | ppm | | % | ppm | mg | m3 | mg/m3 | ppm | % |
| 1 | 2,278 | 1,173 | 1,532 | 2078 | 1978 | 1808 | 1901 | 265 | 13.96 | 2,968 | 59.36 | 0.0018 | 32,978 | 13,883 | 13.7 |
| 2 | 2,403 | 2,328 | 2,178 | 1983 | 2,138 | 2,358 | 2,231 | 160 | 7.17 | 3,018 | 60.36 | 0.0018 | 33,533 | 14,117 | 15.8 |
| 3 | 2,918 | 2,673 | 3,068 | 2,178 | 2,773 | 2,327 | 2,656 | 343 | 12.92 | 4,158 | 83.16 | 0.0018 | 46,200 | 19,449 | 13.7 |
| 4 | 2,940 | 2,416 | 2,353 | 3,184 | 2,228 | 2040 | 2,527 | 441 | 17.44 | 5,134 | 102.68 | 0.0018 | 57,044 | 24,014 | 10.5 |
| 5 | 2,753 | 2,290 | 2,197 | 2,353 | 3,034 | 1853 | 2,413 | 320 | 17.39 | 4,021 | 80.42 | 0.0018 | 44,678 | 18,808 | 12.8 |
| | 2,658 ±302 |
2,176 ±580 |
2,266 ±548 |
2,355 ±483 |
2,430 ±451 |
2077 ±258 |
2,345 ±293 |
| 13.78 ±4,2 |
3,859.8 ±900.3 |
77.2 ±18.0 |
0.0018 | 42,887 ±10,003 |
18,054 ±4,211 |
13.3 ±1.9 |
SD, standard deviation; CV, coefficient of variation; % Delivery = (mean concentration of tanswell (ppm)/(ppm in air) x 100%.
3. Results
3.1. Aerosol number. size distribution and maintenance of concentration during the exposure period
Although particle number and size distributions were monitored, most of the test compounds were present in the vapor phase and were not consistently detected by the SMPS. To estimate the air concentration in the transwell containing HIVIS, an impinger was used to collect VOCs and quantify their concentrations. Figure 5 shows IPA aerosol number and size distribution during a 2-h exposure period. The median diameter, geometric diameter, and geometric standard deviation (GSD) were 65.39 nm, 58.39 nm, and 2.45, respectively. Aerosol number concentration was 2.96 x 106/cc. The median diameter, geometric diameter, and geometric standard deviation of acetone aerosol during 1-h exposure were 128.63 nm, 58.39 nm, and 1.78, respectively. Aerosol number concentration was 5.49 x 106/cc. The VOC concentrations derived from particle number and size measurements by SMPS are shown in Table 2. Based on VOC concentrations calculated from particle number and size distributions, the majority of VOCs are likely in the vapor phase. The duration of the acetone exposure experiment was limited to 1 h due to the solvent’s rapid consumption. Benzyl alcohol aerosol median diameter, geometric mean diameter, and geometric standard deviation during a 2-h exposure period were 109.76 nm, 102.60 nm, and 1.92, respectively. The number concentration was 6.53 x 106/cc.
FIGURE 5.
Maintenance of aerosol concentration during the exposure period and aerosol size distribution. (A) Isopropyl alcohol. (B) Acetone. (C) Benzyl alcohol.
TABLE 2.
Particle size, number, concentration, and evaporation rate of VOCs.
| VOCs | Density at 20 °C (g/mL) | Median (nm) | GM (nm) | GSD | Number (106) | Mass concentration (mg/m3) | ppm | Evaporation time estimate (t) |
|---|---|---|---|---|---|---|---|---|
| Isopropyl alcohol | 0.786 | 65.39 | 58.39 | 2.45 | 2.96 | 12.6 | 5 | 4–8×10–6 s |
| Acetone | 0.79 | 128.63 | 121.64 | 1.78 | 5.49 | 21.6 | 8.95 | 8–16×10–6 s |
| Benzyl alcohol | 1.045 | 109.76 | 102.60 | 1.92 | 6.54 | 32.04 | 7.13 | 0.24–1.2 s |
GM, geometric mean; GSD, geometric standard deviation.
Evaporate rates of isopropyl alcohol and acetone aerosols are so fast that aerosols should be in the vapor phase when they are exposed to the basolateral compartment of the transwell (Table 2). The exposure period was initially 2 h, then changed to 1 h due to the relatively high viscosity of benzyl alcohol. High-viscosity aerosols tend to form larger, less stable droplets, leading to increased wall losses and reduced delivery efficiency, resulting in lower and more variable delivered doses compared with low-viscosity aerosols (Gou et al., 2025). Therefore, all tubes and diffuser were cleaned with water and dried after exposure to prepare for the next exposure experiment.
3.2. Delivery of IPA aerosols to 6-transwell
Table 3 presents the results of IPA delivery onto 6-well plates over a 2-h exposure period. Twelve delivery experiments were conducted at a flow rate of 30 mL/min. The average delivered concentration in each 6-well plate across 10 experiments was 13,491 ± 3712 ppm, with a coefficient of variation (CV) of 9.96% relative to the mean (Table 3). The average delivery rate to the basolateral compartment exceeded 100% of the total delivery rate. A one-way ANOVA showed no significant difference in delivered concentrations among the six trans-well positions, indicating uniform aerosol delivery across the exposure system. The delivered concentration estimate was 109.3 ± 28.2 of the exposed concentration (Table 3). It could be due to the saturation of IPA delivery to the basolateral compartment after 2 h exposure.
3.3. Delivery of acetone aerosols to 6-transwell
Another VOC, acetone, was tested for its delivery on the ALI at a flow rate of 30 mL/min for 1 h. We selected a 1-h exposure because acetone was consumed at a higher rate than IPA. We tested at different MFC flow rates, from 3, 2, 0.5, to 0.2 LPM (Tables 4–7). The results show 7,196 ± 1808, 2,345 ± 293, 1,067 ± 188, and 2,277 ± 319 ppm at 3, 2, 0.5, and 0.2 LPM, respectively (Tables 4–7). Delivery of acetone to the basolateral compartment of transwell was 21.9 ± 6.5, 13.3 ± 1.9, 14.9 ± 3.2, and 7.7 ± 0.7 for 3, 2, 0.5, and 0.2 LPM, respectively, indicating the influence of generation rate. Furthermore, acetone delivery differed from IPA, likely due to differences in exposure duration and evaporation rate. The coefficient of variation (CV) of inter-transwell delivery was 11.73%, 13.78%, 15.8%, and 16.1% at 3, 2, 0.5, and 0.2 LPM, respectively, indicating a decreasing CV with increasing generation rate (Tables 4–7). A one-way ANOVA demonstrated no significant differences in delivered concentrations among the six trans-well positions, indicating uniform aerosol distribution across the exposure system.
TABLE 4.
Delivered acetone to the basolateral compartment (2 mL) of 6-transwell (MFC 3 LPM; 1-h exposure, 30 mL/min pump flow-rate) (n = 9).
| Trans-well | 1 | 2 | 3 | 4 | 5 | 6 | Mean | SD | CV | Impinger conc. | Total mass in impinger | Total air volume sampled | Air conc | ppm in air | Delivery |
|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|
| Exp | ppm | ppm | ppm | ppm | ppm | ppm | ppm | | % | ppm | mg | m3 | mg/m3 | ppm | % |
| 1 | 7,279 | 7,136 | 7,940 | 8,550 | 7,836 | 8,121 | 7,818 | 528 | 6.77 | 5,436 | 108.72 | 0.0018 | 60,400 | 25,427 | 30.7 |
| 2 | 7,879 | 7,836 | 7,279 | 7,963 | 7,279 | 7,836 | 7,634 | 282 | 3.69 | 6,135 | 122.70 | 0.0018 | 68,167 | 38,696 | 26.6 |
| 3 | 3,903 | 3,792 | 3,658 | 3,358 | 3,792 | 3,492 | 3,666 | 206 | 5.63 | 3,719 | 74.38 | 0.0018 | 41,322 | 17,395 | 21.1 |
| 4 | 6,548 | 6,548 | 5,781 | 5,992 | 6,103 | 5,003 | 5,996 | 575 | 9.59 | 6,214 | 124.28 | 0.0018 | 69,044 | 29,066 | 20.6 |
| 5 | 8,081 | 9,081 | 8,192 | 10,070 | 10,080 | 7,536 | 8,838 | 1,075 | 12.17 | 6,270 | 125.40 | 0.0018 | 69,667 | 29,328 | 30.1 |
| 6 | 7,421 | 7,564 | 6,150 | 7,135 | 8,135 | 5,864 | 7,045 | 872 | 12.38 | 6,271 | 125.42 | 0.0018 | 69,678 | 29,332 | 24.0 |
| 7 | 6,907 | 6,150 | 6,007 | 3,936 | 4,735 | 7,135 | 5,811 | 1,247 | 21.46 | 7,421 | 148.42 | 0.0018 | 82,456 | 34,711 | 16.7 |
| 8 | 8,835 | 10,107 | 10,678 | 6,435 | 11,378 | 8,864 | 9,566 | 1750 | 18.29 | 17,300 | 346.00 | 0.0018 | 192,222 | 80,920 | 11.8 |
| 9 | 7,007 | 8,979 | 9,964 | 8,835 | 8,978 | 6,579 | 8,390 | 1,308 | 15.60 | 11,378 | 227.56 | 0.0018 | 126,422 | 53,220 | 15.8 |
| | 7,096 ± 1,382 | 7,466 ± 1878 | 7,294 ± 2,187 | 6,919 ± 2,238 | 7,591 ± 2,442 | 6,714 ± 2,442 | 7,196 ± 1808 | | 11.73 ± 6.0 | 7,793.8 ± 4,114.1 | 155.9 ± 82 | 0.0018 | 86,598 ± 45,712 | 37,566 ± 19,027 | 21.9 ± 6.5 |
SD, standard deviation; CV, coefficient of variation; % Delivery = (mean concentration of tanswell (ppm)/(ppm in air) x 100%.
TABLE 7.
Delivered acetone to the basolateral compartment (2 mL) of 6-transwell. (MFC 0.2 LPM, 1-h exposure, 30 mL/min pump flow-rate).
| Trans-well | 1 | 2 | 3 | 4 | 5 | 6 | Mean | SD | CV | Impinger Conc |
Total mass in impinger | Total air volume sampled | Air conc | ppm in air | Deposition |
|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|
| Exp | ppm | ppm | ppm | ppm | ppm | ppm | ppm | | % | ppm | mg | m3 | mg/m3 | ppm | % |
| 1 | 1,450 | 2,570 | 1,450 | 1,550 | 1,550 | 1950 | 1753 | 441 | 25.15 | 4,420 | 88.4 | 0.0018 | 49,111 | 20,674 | 8.5 |
| 2 | 2,440 | 2,440 | 2,840 | 2,740 | 2,740 | 1,550 | 2,508 | 262 | 14.49 | 6,900 | 138 | 0.0018 | 76,667 | 32,274 | 7.8 |
| 3 | 2050 | 2,740 | 3,130 | 2050 | 2,340 | 1850 | 2,360 | 488 | 20.67 | 7,590 | 151.8 | 0.0018 | 84,333 | 35,502 | 6.6 |
| 4 | 1,692 | 2092 | 2,392 | 2092 | 2,192 | 2,882 | 2,224 | 395 | 13.59 | 6,200 | 124 | 0.0018 | 68,889 | 29,000 | 7.7 |
| 5 | 2,592 | 2,682 | 2,392 | 2,392 | 2,392 | 2,782 | 2,539 | 172 | 6.76 | 7,042 | 140.84 | 0.0018 | 78,244 | 32,939 | 7.7 |
| | 2045 ±483 |
2,505± 258 |
2,441 ±636 |
2,165 ±441 |
2,243 ±436 |
2,203 ±594 |
2,277 ±319 |
| 16.1 ±7.1 |
6,430.4 ±1,228 |
129 ±24.6 |
0.0018 | 71,448 ±13,647 |
30,078 ±5,745 |
7.7 ±0.7 |
SD, standard deviation; CV, coefficient of variation; % Delivery = (mean concentration of tanswell (ppm)/(ppm in air) x 100%.
TABLE 6.
Delivered acetone to the basolateral compartment (2 mL) of 6-transwell (MFC 0.5 LPM; 1-h exposure; 30 mL/min pump flow-rate) (n = 5).
| Trans-well | 1 | 2 | 3 | 4 | 5 | 6 | Mean | SD | CV | Impinger conc | Total mass in impinger | Total air volume sampled | Air conc | ppm in air | Delivery |
|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|
| Exp | ppm | ppm | ppm | ppm | ppm | ppm | ppm | | % | ppm | mg | m3 | mg/m3 | ppm | % |
| 1 | 1,009 | 1,567 | 1,231 | 1,094 | 1,517 | 1,046 | 1,244 | 243 | 19.56 | 1,517 | 30.34 | 0.0018 | 16,856 | 7,096 | 17.5 |
| 2 | 1,307 | 1,269 | 1,182 | 787 | 1,144 | 1,022 | 1,119 | 191 | 17.06 | | | 0.0018 | | | - |
| 3 | 1,132 | 1,182 | 1,467 | 1,367 | 1,072 | 1,194 | 1,236 | 150 | 12.16 | 1982 | 39.64 | 0.0018 | 22,022 | 9,271 | 13.3 |
| 4 | 749 | 1,079 | 762 | 912 | 897 | 802 | 864 | 117 | 13.59 | 1812 | 36.24 | 0.0018 | 20,133 | 8,476 | 10.2 |
| 5 | 1,109 | 712 | 884 | 799 | 959 | 774 | 873 | 145 | 16.56 | 1887 | 37.74 | 0.0018 | 20,967 | 8,826 | 9.9 |
| | 1,061 ±205 |
1,162 ±310 |
1,105 ±283 |
992 ±243 |
1,118 ±243 |
968 ±177 |
1,067 ±188 |
| 15.8 ±2.9 |
17,521 ±521 |
36.0 ±4.0 |
0.0018 | 1994 ±2,230 |
8,417 ±939 |
13.9 ±3.2 |
SD, standard deviation; CV, coefficient of variation; % Delivery = (mean concentration of tanswell (ppm)/(ppm in air) × 100%.
3.4. Delivery of benzyl alcohol to 6-transwell
When we tested benzyl alcohol delivery to the basolateral compartment of ALI at flow rates of 30 mL/min for 2 h and 1 h, the delivered amounts were 61.1 ± 24.1 and 35.5 ± 21.7 ppm, respectively, which were lower than those of isopropyl alcohol and acetone. The CV for inter-transwell delivery was 18.8% and 15.56%, respectively (Tables 8, 9). The percentages of delivery were 476% ± 529% and 691% ± 1,221% for 2 h and 1 h, respectively. Because of its high viscosity, semi-VOC nature, and strong tendency to adsorb onto walls and tubes, benzyl alcohol air concentrations could not be readily estimated from impinger concentrations.
TABLE 8.
Delivered benzyl alcohol to the basolateral compartment (2 mL) of 6-transwell. SD, standard deviation; CV, coefficient of variation (3 LPM MFC, 2 h exposure, 30 mL/min flow-rate).
| Trans-well no. | 1 | 2 | 3 | 4 | 5 | 6 | Mean | SD | CV | Impinger conc | Total mass in impinger | Total air volume sampled | Air conc | ppm in air | Delivery |
|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|
| Exp | ppm | ppm | ppm | ppm | ppm | ppm | ppm | | % | ppm | mg | m3 | mg/m3 | ppm | % |
| 1 | 81 | 82 | 78 | 88 | 104 | 88 | 86.8 | 9.3 | 10.71 | 58 | 1.16 | 0/0018 | 644/44 | 145.7 | 59.6 |
| 2 | 86 | 83 | 75 | 107 | 87 | 81 | 86.5 | 10.9 | 12.62 | 80 | 1,6 | 0/0018 | 888.89 | 201.0 | 43.0 |
| 3 | 83 | 67 | 73 | 68 | 51 | 68 | 68.3 | 10.39 | 15.18 | 9.1 | 0.18 | 0/0018 | 0.0036 | 22.9 | 298 |
| 4 | 45 | 52 | 58 | 40 | 47 | 54 | 49.3 | 6.56 | 13.30 | 1.5 | 0.03 | 0/0018 | 16.67 | 3.77 | 1,307 |
| 5 | 25 | 24 | 25 | 18 | 20 | 40 | 25.3 | 7.74 | 30.54 | 1,5 | 0.03 | 0/0018 | 16.67 | 3.77 | 670 |
| 6 | 47 | 54 | 51 | 52 | 40 | 38 | 47 | 6.62 | 14.1 | 20.8 | 0.42 | 0/0018 | 231.1 | 52.25 | 90.- |
| Mean± | 61.2 ±25.5 |
57.8 ±23.8 |
58.2 ± 21.6 | 59.7 ±33.9 |
62.7 ±30.1 |
67.2 ±17.7 |
61.1 ±24.1 |
| 16.1 ±7.2 |
33.9 ±33.7 |
0.364 ±0.47 |
0.0018 | 231 ±360 |
71.5 ±82.7 |
476 ±529 |
SD, standard deviation; CV, coefficient of variation; % Delivery = (mean concentration of tanswell (ppm)/(ppm in air) x 100%.
TABLE 9.
Delivered benzyl alcohol to the basolateral compartment (2 mL) of 6-transwell. (3 LPM MFC, 1 h exposure, 30 mL/min flow-rate).
| Trans-well | 1 | 2 | 3 | 4 | 5 | 6 | Mean | SD | CV | Impinger conc | Total mass in impinger | Total air volume sampled | Air conc | ppm in air | Delivery |
|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|
| Exp | ppm | ppm | ppm | ppm | ppm | ppm | ppm | | % | ppm | mg | m3 | mg/m3 | ppm | % |
| 1 | 27 | 22 | 19 | 20 | 19 | 27 | 22.33 | 3.78 | 16.91 | 0.2 | 0.004 | 0/0018 | 2.22 | 0.50 | 4,466 |
| 2 | 17 | 20 | 24 | 18 | 26 | 22 | 21.17 | 3.49 | 16.48 | 1.2 | 0.024 | 0/0018 | 13.33 | 3.01 | 703 |
| 3 | 20 | 24 | 23 | 18 | 19 | 22 | 21.0 | 2.37 | 11.27 | 0 | 0 | 0/0018 | 0 | 0 | - |
| 4 | 9 | 18 | 19 | 20 | 21 | 24 | 18.5 | 5.09 | 27.51 | 4.2 | 0.084 | 0/0018 | 46.67 | 10.55 | 175 |
| 5 | 9 | 18 | 19 | 19 | 20 | 23 | 18.0 | 4.73 | 26.29 | 1.2 | 0.0024 | 0/0018 | 13.33 | 3.01 | 598 |
| 6 | 25 | 19 | 24 | 22 | 29 | 26 | 22.5 | 3.02 | 13.41 | 0 | 0 | 0/0018 | 0 | 0 | - |
| 7 | 21 | 14 | 14 | 17 | 11 | 19 | 16.0 | 3.69 | 23.05 | 0 | 0 | 0/0018 | 0 | 0 | - |
| 8 | 28 | 34 | 26 | 30 | 19 | 35 | 28.67 | 5.85 | 20.42 | 5.2 | 0.014 | 0/0018 | 57.78 | 13.06 | 220 |
| 9 | 27 | 34 | 20 | 29 | 28 | 23 | 26.83 | 4.88 | 18.17 | 2.2 | 0.044 | 0/0018 | 24.44 | 5.53 | 485 |
| 10 | 46 | 47 | 51 | 38 | 45 | 36 | 43.83 | 5.71 | 13.02 | 2.2 | 0.014 | 0/0018 | 24.44 | 5.53 | 793 |
| 11 | 33 | 33 | 38 | 40 | 33 | 34 | 35.17 | 3.06 | 8.70 | 20.2 | 0.404 | 0/0018 | 224.44 | 50.74 | 69.3 |
| 12 | 43 | 34 | 36 | 30 | 32 | 30 | 34.17 | 4.92 | 14.39 | 2.2 | 0.044 | 0/0018 | 24.44 | 5.53 | 618 |
| 13 | 62 | 72 | 68 | 65 | 74 | 70 | 68.50 | 4.46 | 6.51 | 53.2 | 1.064 | 0/0018 | 591.1 | 133.65 | 51.2 |
| 14 | 79 | 80 | 76 | 81 | 77 | 85 | 79.67 | 3.20 | 4.02 | 56.2 | 1.124 | 0/0018 | 624.44 | 141.18 | 56.4 |
| 15 | 69 | 68 | 72 | 89 | 88 | 68 | 75.67 | 10.05 | 13.29 | 53.2 | 1.064 | 0/0018 | 591.11 | 133.74 | 59.6 |
| | 34.3 ±21.3 |
35.8 21.4 |
35.3 ±21.2 |
35.7 ±23.6 |
36.1 ±24.1 |
36.3 ±20.6 |
35.5 ±21.7 |
| 15.56 ±6.8 |
13.4 ±21.7 |
0.26 ±0.44 |
0.0018 | 149 ±241 |
33.7 ±54.5 |
691 ±1,221 |
SD, standard deviation; CV, coefficient of variation; % Delivery = (mean concentration of tanswell (ppm)/(ppm in air) x 100%.
3.5. Overall evaluation of delivery to 6-transwell
Figure 6 shows the overall inter-transwell VOC delivery in the 6-transwell. The coefficient of variation (CV) quantifies the relative variability of a dataset around its mean. Also, it indicates how consistent or uniform your measurements are, independent of their absolute magnitude. As shown in Table 10, ANOVA revealed no statistically significant differences among the six transwells, indicating consistency across flow rates from 2 LPM to 0.2 LPM, regardless of the test VOCs. It showed statistically uniform delivery. CV values ranged from approximately 7%–19% for most exposure conditions, consistent with reported variability in ALI exposure systems, and did not result in statistically significant positional differences. Our CV ranging 9.96%–18.8% indicates that the transwell system distributes delivery evenly, supporting its use in VOCs like isopropyl alcohol and acetone, and semi-volatile VOCs such as benzyl alcohol exposure studies without concern for positional bias.
FIGURE 6.
Deposition of IPA, Acetone, and Benzyl alcohol to ALI of 6-transwell. (A) IPA (3 LPM, 2 h exposure). (B) Acetone (3 LPM, 1 h exposure). (C) Acetone (2 LPM, 1 h exposure). (D) Acetone (0.5 LPM, 1-h exposure). (E) Aceton (0.2 LPM, 1-h exposure). (F) Benzyl alcohol (3 LPM, 2-h exposure). (G) Benzyl alcohol (3 LPM, 1-h exposure).
TABLE 10.
Summary table for VOC deposition.
| Table | Compound | Flow rate (MFC) LPM | Exposure duration | Pump flow (mL/Min) | Experiment repeat | Overall mean ± SD (ppm) | CV (%) | F-statistic | p-value | Result |
|---|---|---|---|---|---|---|---|---|---|---|
| 3 | IPA | 3 | 2 h | 30 | 12 | 13,491 ± 3,712 | 9.96 | 0.161 | 0.976 | No significant difference |
| 4 | Acetone | 3 | 1 h | 30 | 9 | 7,196 ± 1808 | 11.73 | 0.207 | 0.958 | No significant difference |
| 5 | Acetone | 2 | 1 h | 30 | 5 | 2,345 ± 293 | 13.78 | 1.02 | 0.426 | No significant difference |
| 6 | Acetone | 0.5 | 1 h | 30 | 5 | 1,067 ± 188 | 15.8 | 0.467 | 0.797 | No significant difference |
| 7 | Acetone | 0.2 | 1 h | 30 | 5 | 2,277 ± 319 | 16.1 | 0.629 | 0.679 | No significant difference |
| 8 | Benzyl alcohol | 3 | 2 h | 30 | 6 | 61.1 ± 24.1 | 18.8 | 0.108 | 0.990 | No significant difference |
| 9 | Benzyl alcohol | 3 | 1 h | 30 | 15 | 35.5 ± 21.7 | 15.56 | 0.015 | ≈1.000 | No significant difference |
4. Discussion
4.1. Inter-transwell delivery variation in vitro inhalation studies
A uniform and reproducible delivered concentration is a fundamental requirement for air–liquid interface (ALI) in vitro inhalation models, particularly when such models are used within new approach methodology (NAM)-based inhalation testing frameworks. While ALI platforms have been extensively validated for particulate and nanoparticle aerosols, comparatively little is known about the delivery behavior and spatial uniformity of volatile organic compounds, which exhibit rapid evaporation and diffusion-dominated transport. The present study addresses this gap by systematically quantifying inter-transwell variability in delivery for representative volatile and semi-volatile solvents under controlled exposure conditions.
The results of ten in vivo lung deposition studies conducted with previously silver nanoparticles ranged from 11 to 20 nm, gold nanoparticles 11–105 nm, and multiwalled carbon nanotubes 1,015 nm exposed to 4-6 rats for 6-h in a nose-only inhalation chamber resulted in mean CVs 12.31%, ranging from 6.1% to 21.7% (Lee et al., 2025a). The average percentage of studies evaluating particle-based ALI exposure systems has reported CVs of approximately 10%–25% across transwells under controlled conditions. Lee et al. (2025a) studied an in vitro ALI deposition study using NaCl nanoparticles ranging from 62 to 66 nm, resulted 6.25% and 6.95% CV, with 30 mL/min and 12 mL/min pump flow-rate, respectively. Lee et al. (2025b) also tested ALI deposition of median-size 128 nm protein nanoparticles for inter-transwell deposition. Their study reported CVs of 19.59% and 19.07% of CV at pump flow rates of 12 mL/min and 30 mL/min, respectively. The study by Lenz et al. (2009), which used a flow-through ALI exposure system for nanoparticles, reported well-to-well mass deposition variability of approximately 10%–15%, attributed primarily to small differences in local airflow and particle diffusion. Similarly, Aufderheide and Scheffler (2013) demonstrated that uniform aerosol distribution in multi-insert ALI systems is achievable but requires precise flow control and system calibration, with reported inter-insert variability typically remaining below 20%. Electrostatic precipitation-based ALI systems, such as those incorporating electrostatic enhancement to increase deposition efficiency, have also been evaluated for spatial uniformity. De Bruijne et al. (2009) showed that although electrostatic forces substantially increase the deposited dose, spatial heterogeneity can arise when electric field strength or grounding differs among inserts, leading to increased inter-well variability. Consequently, many studies emphasize the importance of independently validating dose delivery to each insert rather than relying on chamber-averaged concentrations.
Particle size and deposition mechanism strongly influence inter-transwell variability. Diffusion-dominated deposition, characteristic of ultrafine particles and vapors, generally produces more homogeneous distribution across inserts than impaction- or sedimentation-driven deposition of larger particles (Jeannet et al., 2015; Rostami, 2009; Lee et al., 2025b). Computational fluid dynamics (CFD) simulations coupled with experimental validation have demonstrated that even minor flow asymmetries can disproportionately affect the deposition of larger aerosols, whereas gas-phase diffusion tends to smooth spatial gradients (Rostami, 2009). When Lee et al. (2025b) evaluated several deposition mechanisms, diffusion, impaction, gravitational settling, electrostatic deposition, and thermophoretic deposition of 125 nm median size of protein particles to a 6-transwell system, the flow-rates used in that study (12–30 mL/min) exclude impaction and gravitational settling, but mostly diffusion-dominant deposition operated in those settings.
Despite these advances, standardized acceptance criteria for inter-transwell variability are not universally defined. However, several inhalation toxicology reviews and dosimetry workshops suggest that inter-tanswell CV values ≤ 10–20% are generally acceptable for in vitro ALI exposure systems, provided that no statistically significant positional bias is observed (Lenz et al., 2009; Kleinstreuer et al., 2016). Reporting inter-transwell variability alongside deposited dose metrics is increasingly recommended to enhance transparency and reproducibility across studies.
In this context, the variability in inter-transwell delivery to the basolateral compartment observed in the present study (CV approximately 7%–19%, depending on compound and exposure conditions) is comparable to or lower than values reported for many particle-based ALI systems. The absence of statistically significant differences across transwell positions indicates a stable airflow distribution and reproducible dose delivery. These findings support the suitability of diffusion-dominated ALI exposure approaches for volatile and semi-volatile organic compounds and align with current expectations for acellular in vitro inhalation exposure systems used to support NAM-based assessments.
4.2. Diffusion-driven delivery of volatile solvents at the ALI
This study demonstrates that volatile organic solvents with high vapor pressures, such as isopropyl alcohol (IPA) and acetone, can be reproducibly delivered onto an air–liquid interface (ALI) under controlled in vitro exposure conditions. Although these solvents rapidly evaporate following atomization, their delivery onto the aqueous ALI is governed primarily by gas-phase diffusion rather than by inertial impaction or gravitational settling. Highly water-miscible aerosols and vapors readily dissolve in the liquid phase at the ALI, consistent with classical gas–liquid mass-transfer theory and pulmonary-uptake models (Fiserova-Bergerova, 1983; Rostami, 2009).
The relatively low coefficients of variation (CV < 10% for IPA and <16% for acetone) indicate that diffusion-driven transport produces spatially uniform solvent delivery across the six transwells. This behavior contrasts with particulate aerosols, for which deposition is often dominated by aerodynamic size, electrostatic effects, and flow maldistribution, frequently resulting in higher inter-well variability (Lenz et al., 2009; Aufderheide and Scheffler, 2013).
4.3. Influence of physicochemical properties on delivery efficiency
Differences in the delivered concentrations of IPA, acetone, and benzyl alcohol are consistent with their vapor pressures, evaporation rates, and viscosities. Acetone, with a vapor pressure approximately four times higher than that of IPA, exhibited lower delivery efficiency and modestly increased variability, reflecting greater evaporative loss during aerosol generation and transport. Similar observations have been reported in inhalation studies of highly volatile solvents, in which rapid vapor-phase dilution reduces the effective dose at the epithelial surface (Fiserova-Bergerova and Hughes, 1969; Morris et al., 1996).
Benzyl alcohol, a semi-volatile organic compound with low vapor pressure and high viscosity, displayed lower delivery but maintained CV values below 20%. Elevated viscosity affects aerosol formation by promoting larger, less stable droplets and increasing wall losses in tubing and exposure chambers. High-viscosity organic aerosols also exhibit slower internal diffusion and altered gas–particle partitioning, which can limit evaporation and condensation dynamics (Shiraiwa et al., 2013). These mechanisms likely contributed to the lower and more variable benzyl alcohol delivery observed here, particularly at longer exposure durations.
4.4. Effect of generation flow rate on delivery uniformity
The nonlinear relationship between acetone delivery and generation flow rate suggests a balance between aerosol residence time, dilution, and evaporation. At higher generation flows, increased aerosol concentration improves delivered concentration, whereas at very low flows, prolonged residence time may enhance diffusive transport despite lower source strength. Similar tradeoffs have been described in ALI exposure systems for volatile and semi-volatile compounds, where both airflow and exposure duration critically determine delivered dose (de Bruijne et al., 2009; Jeannet et al., 2015). Importantly, across all tested flow rates (0.2–3 L/min), no statistically significant inter-transwell differences were observed, demonstrating that the HIVIS system provides stable, well-distributed airflow. This robustness is essential for ensuring reproducible dose delivery in vitro inhalation studies intended to support NAM-based inhalation testing.”
4.5. Implications for in vitro inhalation testing and NAM-supportive dosimetry
Uniform deposition or delivery across exposure wells is a key requirement for in vitro inhalation test systems used within new approach methodologies (NAMs), as spatial dose variability can confound concentration–response relationships and biological interpretation. The CV values observed in this study (approximately 7%–19%) are comparable to, or better than, those reported for many particle-based ALI systems and fall within acceptable experimental variability for in vitro inhalation testing (Lenz et al., 2009; Lucci et al., 2018).
By demonstrating consistent delivery of volatile and semi-volatile solvents without electrostatic enhancement or complex aerosol conditioning, this study supports the applicability of diffusion-dominated ALI exposure for organic vapors. Coupled with real-time PID monitoring and post-exposure chemical quantification, this approach enables quantitative dosimetry, a critical component supporting the regulatory acceptance of NAM-based in vitro inhalation test systems (Kleinstreuer et al., 2016; Lee et al., 2025a).
4.6. Limitations and future directions
This study employed an acellular ALI model to isolate physicochemical delivery behavior. The presence of cells, mucus layers, or surfactant may alter solvent uptake kinetics and retention. Additionally, temperature and relative humidity were not actively controlled, though both parameters strongly influence evaporation and gas–liquid partitioning of VOCs (Rostami, 2009). Also, our concentration levels were very high, not the human-exposed concentrations. The diffusion-driven VOC delivery should operate at both low and high concentration levels. Future work integrating controlled environmental conditions and computational fluid–dynamic modeling would further refine dose prediction and enhance in vitro–in vivo extrapolation. Accordingly, the present findings should be interpreted as providing exposure and dosimetry context rather than toxicological hazard characterization.
Funding Statement
The author(s) declared that financial support was not received for this work and/or its publication.
Footnotes
Edited by: Stina Oredsson, Lund University, Sweden
Reviewed by: Maurizio Gualtieri, University of Milano-Bicocca, Italy
Tanja Hansen, Fraunhofer Institute for Toxicology and Experimental Medicine (FHG), Germany
Data availability statement
The original contributions presented in the study are included in the article/supplementary material, further inquiries can be directed to the corresponding author.
Author contributions
JL: Data curation, Formal Analysis, Investigation, Methodology, Writing – original draft, Writing – review and editing. HL: Methodology, Supervision, Writing – review and editing. KA: Investigation, Methodology, Supervision, Writing – review and editing. MJ: Writing – review and editing. JK: Data curation, Formal Analysis, Writing – review and editing. YH: Data curation, Methodology, Writing – review and editing. YK: Project administration, Resources, Supervision, Writing – review and editing. EF: Investigation, Supervision, Writing – review and editing. IY: Writing – original draft, Writing – review and editing.
Conflict of interest
Authors JL, and IY, were employed by HCT Seattle. Authors HL, and MJ, were employed by HCTm. Authors JK, and YK, were employed by H&H Bio.
The remaining author(s) declared that this work was conducted in the absence of any commercial or financial relationships that could be construed as a potential conflict of interest.
The author IY declared that they were an editorial board member of Frontiers at the time of submission. This had no impact on the peer review process and the final decision.
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Associated Data
This section collects any data citations, data availability statements, or supplementary materials included in this article.
Data Availability Statement
The original contributions presented in the study are included in the article/supplementary material, further inquiries can be directed to the corresponding author.





