Distribution of Organophosphate Esters between the Gas and Particle

May 4, 2016 - Predictions by the Tool (fpart,T) were compared with those calculated from the Junge-Pankow model (fpart,J-P) and the Harner-Bidleman mo...
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Article

Distribution of organophosphate esters between the gas and particle phase – model predictions vs. measured data Roxana Sühring, Hendrik Wolschke, Miriam L. Diamond, Liisa M. Jantunen, and Martin Scheringer Environ. Sci. Technol., Just Accepted Manuscript • DOI: 10.1021/acs.est.6b00199 • Publication Date (Web): 04 May 2016 Downloaded from http://pubs.acs.org on May 10, 2016

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TOC/Abstract art:

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Distribution of organophosphate esters between the gas and particle phase – model predictions vs. measured data

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Roxana Sühring1,3,6, Hendrik Wolschke1,2, Miriam L. Diamond3, Liisa M. Jantunen4 , Martin Scheringer*1,5,7

3

6 7 8 9 10 11 12 13 14

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Abstract

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Gas-particle partitioning is one of the key factors that affects the environmental fate of semi volatile

17

organic chemicals. Many organophosphate esters (OPEs) have been reported to primarily partition to

18

particles in the atmosphere. However, because of the wide range of their physicochemical properties,

19

it is unlikely that OPEs are mainly in the particle phase “as a class”.

20

We compared gas-particle partitioning predictions for 32 OPEs made by the commonly used OECD

21

POV and LRTP Screening Tool (“the Tool”) with the partitioning models of Junge-Pankow (J-P) and

22

Harner-Bidleman (H-B), as well as recently measured data on OPE gas-particle partitioning.

23

The results indicate that half of the tested OPEs partition into the gas phase. Partitioning into the gas

24

phase seems to be determined by an octanol-air partition coefficient (log KOA) < 10 and a subcooled

25

liquid vapour pressure (log PL) > –5, as well as the total suspended particle concentration (TSP) in the

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sampling area. The uncertainty of the physicochemical property data of the OPEs did not change this

Leuphana University Lüneburg, Institute of Sustainable and Environmental Chemistry, Scharnhorststraße 1, 21335 Lüneburg Helmholtz-Zentrum Geesthacht, Centre for Materials and Coastal Research, Institute of Coastal Research, Department for Environmental Chemistry, Max-Planck-Strasse 1, 21502 Geesthacht, Germany 3 University of Toronto, Department of Earth Sciences, 22 Russell Street, Toronto, Canada M5S 3B1 4 Air Quality Processes Research Section, Environment and Climate Change Canada, Egbert, ON L0L 1N0, Canada 5 Institute for Chemical and Bioengineering, ETH Zürich, 8093 Zürich, Switzerland 6 Centre for Environment, Fisheries and Aquaculture Science (Cefas), Lowestoft, Suffolk NR33 0HT, United Kingdom 7 RECETOX, Masaryk University, 625 00 Brno, Czech Republic 2

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estimate. Furthermore, the predictions by the Tool, J-P- and H-B-models agreed with recently

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measured OPE partitioning.

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1. Introduction

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Organic flame retardants (FRs) have been used in increasing amounts since the 1950s in a variety of

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polymer-based industrial and consumer products to comply with flammability standards. Some FRs,

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such as penta- and octa- polybrominated diphenyl ethers (PBDEs) have been restricted from new

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production and application under the Stockholm Convention due to their hazardous properties,

34

including high persistence and bioaccumulation potential (1) (2). Other brominated FRs (BFRs) such

35

as deca-PBDE are partially restricted or voluntarily phased-out by the industry (3). However, the

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overall demand and production of FRs is still increasing (4). Therefore, the restrictions and phasing-

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out of PBDEs since the early 2000s have led to the introduction of a variety of halogenated and non-

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halogenated alternatives (5) (6).

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One group of substitutes are organophosphate esters (OPEs), which comprise a diverse set of

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compounds varying widely in physicochemical properties. Their production and use have been

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increasing, in part, as a result of restrictions on PBDE use (7). In 2004 the global annual use was

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207,200 tonnes (8), which makes OPEs high-production volume chemicals. OPE uses extend beyond

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that of FRs. Whereas chlorinated OPEs are mainly used as flame retardants, non-chlorinated OPEs are

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also used as plasticizers, antifoaming agents and additives in hydraulic fluids (9).

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Whether or not OPEs are suitable replacements for hazardous FRs, such as PBDEs with known

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carcinogenic or endocrine disrupting properties, is controversial. OPEs are, in general, regarded as

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less persistent in the environment – one of the key criteria for evaluating the potential environmental

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hazard of a chemical. However, our recent study suggested that many OPEs have medium to high

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persistence

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Ethylhexyldiphenyl phosphate, Isodecyl diphenyl phosphate, Tris(2,3-dichloro-1-propyl)phosphate,

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Tris(cresyl) phosphate, Triphenyl phosphate, 1-Propanol, 3-bromo-2,2-bis(bromomethyl)-, 1,1',1''-

(>

1700

h)

and

that

Tetrakis(2-chloroethyl)dichloroisopentyldiphosphate,

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phosphate, and potentially Tris(2-butoxyethyl) phosphate and 1,3-Dichloro-2-propanol phosphate

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(BCMP-BCEP, EHDPP, IDDPP, MC984, TCP, TPhP, TTBNPP, TBEP, TDCPP) have a persistence similar to

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that of PBDEs they are replacing (10). Furthermore, increasing amounts of OPEs have been detected

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in remote areas (11–13) such as the Arctic and Antarctic, which indicates their persistence (POV) and

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long-range transport potential (LRTP).

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To assess potential risks posed by OPEs, it is essential to establish suitable measurement and

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estimation methods that provide information on where and how OPEs are distributed. Most studies

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of OPEs have focused on the particle phase (12, 14, 15), because many OPEs have been reported to

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mostly partition to particles in the atmosphere (14, 15). Sorption to particles has, furthermore, been

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hypothesised as one potential explanation for reduced degradation and thereby increased POV and

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LRTP of OPEs in the environment (16). However, considering the range of physicochemical properties

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of OPEs, notably the vapour pressure (PL) and octanol-air partition coefficient (KOA), from which gas-

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particle partitioning of semi-volatile chemicals can be estimated (17, 18), it seems unlikely that all

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OPEs are particle-sorbed.

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Revisiting the literature that has reported that OPEs are primarily in the particle phase, we found that

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these studies either investigated selected OPEs with similar properties (e.g. only halogenated OPEs),

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screened selected samples for OPEs in the gas phase, or that the detection limits were significantly

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higher for the gas than particle phase (12, 14, 15). Furthermore, studies using the OECD POV and LRTP

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Screening Tool (“the Tool”) for the estimation of the environmental behaviour predicted that about

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half of the tested OPEs should be primarily in the gas phase (10, 19). This could, of course, be an error

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of the model or an error in the physicochemical properties used as input parameters.

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Considering the importance of an accurate and reliable assessment of LRTP and persistence for the

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risk assessment of OPEs, we assessed the hypothesis that OPEs primarily partition to the particle

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phase. Due to the importance of the OECD POV and LRTP Screening Tool as tool for assessment of POV

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and LRTP in chemical risk assessment (20) we decided to use this model, which derives gas-particle

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partitioning from KOA to predict the fraction of OPEs in the particle phase (fpart). Here, fpart is defined as

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the ratio of the concentration of a chemical (x) in the particle phase (cpart(x), ng m–3) to its total

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concentration in particle and gas-phases (∑ cpart(x), cgas(x), ng m–3), with part =

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Our aim was to investigate the hypothesis that all OPEs are in the particle phase. We first assessed

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the impact of uncertainty of various model input parameters on predicted fpart, identified the factors

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determining fpart, and then evaluated and compared these predictions to other gas-particle

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partitioning models (Harner-Bidleman (17)) (Junge-Pankow (18)), as well as measured values of fpart

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from previous studies.

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2. Methods

 

.

      

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2.1 Compounds evaluated

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The 32 compounds evaluated for gas- particle partitioning (Table 1, S1) were taken from those

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assessed by Zhang & Sühring et al. (2016) (10), Liagkouridis et al. (2015) (19), measured in the

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atmosphere by Möller et al. (2011) (15), and measured during a one-year weekly stationary sampling

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at Büsum, Northern Germany (21). We included OPEs with a wide range of physicochemical

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properties: log PL ranged from –5.6 for BCMP-BCEP, Resorcinol bis(diphenyl phosphate) (PBDPP) and

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1-Propanol, 3-bromo-2,2-bis(bromomethyl)-, 1,1',1''-phosphate (TTBNPP) to 1.7 for Trimethyl

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phosphate (TMP) and log KOA ranged from 4.3 for TMP to 22 for Tetrakis(2,6-dimethylphenyl)-m-

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phenylene biphosphate (PBDMPP) (see Supporting Information Tables S2–7 for a detailed description

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of all input data).

96 97 98 99

2.2 Log KOA based fpart predicted using the OECD Tool, fpart,T

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The OECD POV and LRTP Screening Tool (“the Tool”) (Version 2.2 (22)) calculates fpart,T based on the

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octanol-air (KOA) partition coefficient. This approach assumes that absorption into the organic film

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coating of atmospheric particles is the driving factor for the gas-particle partitioning of contaminants

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(23), rather than the adsorption to active sites hypothesised by Junge and Pankow (24, 25). Using

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generalised parameters for the global environment fpart,T is represented in the Tool source code by the

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following equation(22)

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, = φ ∗  ∗ 0.42 ∗ %∗&'* 1 − φ  ∗ %∗&' + φ ∗  ∗ 0.42 ∗ %∗&' (1)

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The volume fraction of aerosol particles in air (φ ) in the Tool is set by default to 2 ∗ 10,$$ -.. The

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default settings in the Tool use coarse particles with an aerosol deposition velocity of 10.8 m h–1,

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usually attributed to a particle diameter of 2.5–10 µm (26). Assuming an average density of aerosol

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particles of 1.5 g cm–3 this value reflects a particle concentration in air of 30 µg m–3, which is the

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target value for PM 2.5 in the Canada-wide Standard for Particulate Matter and Ozone (27). KOA in the

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Tool is calculated as the ratio of the octanol-water partition coefficient (KOW) and the air-water

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partition coefficient (KAW), with  = '/0 . The gas constant (R) is defined as 8.314 ' -67 and the

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temperature (TK) is set to 298.15 K.

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Data for the Tool input parameters were extracted from a total of 50 publications (1979–2015) and

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sorted into three datasets for the evaluation of the Tool (see Supporting Information Tables S2 – S7

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for a detailed list of used data and sources). To test the hypothesis that uncertainty of input data is

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responsible for the discrepancy between modelled and measured partitioning behaviour of OPEs, we

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collected input data with high variability. We explicitly included data published by industry and

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government authorities, as well as data from sources dating back more than 30 years. The aim of this

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approach was to “simulate” datasets that would be used by different stakeholder groups such as

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regulators, industry, the scientific community and NGOs and to test whether the use of different

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datasets and sources would have a significant effect on the predicted fpart.

$

$

$

-.

'

- .45

10

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Input all: Values of KOW, KAW and PL were obtained from modelled and measured data from all 50

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publications (1979–2015) and data provided for registration under the European chemicals regulation

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REACH. The median values of the combined dataset were used as input data for the Tool (a full list of

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the data used and their sources is presented in Tables S1-S4). LogKOA was calculated as

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89: = 89:; − 89:; (2)

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Modelled Data: Values of KOW, KAW and PL estimated by EPI Suite, SPARC and Absolv were taken from

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the studies by Zhang and Sühring et al. (2016) (10) and Liagkouridis et al. (2015) (19). This dataset

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was used to specifically assess the uncertainty of modelled physicochemical properties. LogKOA was

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calculated from log KOW and logKAW (2).

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Outlier Removed: These are the partition coefficients, KOW, KAW, from the input-all dataset with

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outliers removed. Outliers were defined as data points with a value below Q1 – 1.5 IQR or above Q3 +

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1.5 IQR, respectively, with Q1 = the first quartile or 25th percentile, Q3 = the third quartile or 75th

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percentile, and IQR being the interquartile range defined as Q3 – Q1. LogKOA was calculated as noted

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above.

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Predictions by the Tool (fpart,T) were compared with those calculated from the Junge-Pankow model

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(fpart,J-P) and the Harner-Bidleman model (fpart,H-B). Input data to test these models were estimated by

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the three most commonly used models for physicochemical properties, EPISuite, SPARC and Absolv,

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as well as measured data.

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2.3 Data evaluation for the Tool

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To evaluate the impact of uncertain input parameters on the prediction of fpart,T, a sensitivity analysis

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was performed for the Outlier Removed dataset, as well as a Monte Carlo uncertainty analysis for

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compounds of the Outlier Removed dataset with low or intermediate fpart,T (fpart,T< 0.9).

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The sensitivity analysis was performed as described by Morgan and Henrion (1992) (28). The

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sensitivity of fpart,T to a specific input parameter was tested by changing the input parameters one-by6 ACS Paragon Plus Environment

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one and evaluating the impact on fpart,T. A factor of 1.1 was chosen for the change of parameter

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values. The sensitivity (S) of fpart to an individual parameter was quantified as

part,T @ >part ,& ∆@

(3)

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with S defined as sensitivity, Bpart,T defined as change in fpart,T, C as the initial input parameter value

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and ∆C as the change in input parameter value.

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A Monte Carlo uncertainty analysis was performed on all compounds with partitioning behaviour

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contrary to the hypothesis of partitioning into the particle phase, i.e. with fpart,T < 0.9. The Monte

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Carlo calculation assumed that the values of all chemical properties are distributed log-normally

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around their “true value”. Dispersion factors describe the width of the log-normal distribution. In the

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default Monte Carlo analysis implemented in the Tool, this width is estimated by multiplying or

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dividing the median by a factor of 5 for the partition coefficients (22). The Monte Carlo uncertainty

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analysis then generates random values from the distribution of each input parameter, using the

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defined dispersion factors and assuming uncertainties in chemical input parameters were

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uncorrelated. The model was run for a set number N of combinations of the dispersed input

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parameters (22). For this study the Q1 and Q3 determined in the Outlier removed dataset were used

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as dispersion factors, as well as the (higher) default Tool dispersion factors and N was set to 200

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(Tables S9 and S10 for calculated dispersion factors, initial and median fpart from Monte Carlo analysis

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for default and calculated dispersion factors).

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2.4 Junge-Pankow (fpart,J-P) and Harner-Bidleman (fpart,H-B) predictions and evaluation

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Predictions of fpart,T from the Tool were compared to those from the Junge-Pankow (J-P) and Harner-

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Bidleman (H-B) models. The J-P model (18) assumes adsorption to the active sites of an aerosol

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particle according to the subcooled liquid vapour pressure (PL, Pa) of the compound, and the surface

170

area of the adsorbing aerosol particle per volume air (θ, cm2 aerosol cm–3 air) (18). fpart(J-P) is then

171

calculated as

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D5EF,G,4 = 4

172

HI J  HI

(4)

173

where fpart,J-P is the fraction of chemical adsorbed to air particles and c is a constant. The constant (c)

174

depends on the desorption temperature from the particle surface, the volatilisation temperature of

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the compound, and the active sites of the aerosol. We used default values of c = 0.172 Pa cm–1 and

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K = 1.1 ∗ 10,L H-. for urban air (23). PL data were obtained using EPI Suite’s MPBPVP v1.43 (29),

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SPARC (30), as well as measured data (31) and literature data (7, 32) (Tables S6,7).

178

The Harner-Bidleman model (17) estimates fpart, similarly to the Tool, based on KOA and assuming

179

primary absorption into the organic layers of aerosols. fpart,H-B is calculated as

H-M

'P ∗&Q4

D5EF,N,O = '

180

P ∗&Q4$

(5)

log D = log  + log U − 11.91 (6)

181

with

182

where fpart,H-B is the fraction of chemical adsorbed to air particles, KP (m3 µg–1) is the particle-gas

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partition coefficient, TSP is the total suspended particulates concentration (µg m–3), and fOM is the

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fraction of organic matter (OM) on the aerosol particles (gOM gTSP–1). We used default values for urban

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air of TSP of 55 µg m–3 and fOM of 0.40 gOM gTSP–1 (23).

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2.4 Measured fpart,M

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Finally, fpart,T, fpart,H-B and fpart,J-P were compared to measured fpart,M values obtained by Wolschke et al.

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(2016) (21) who measured weekly OPE air concentrations over one year at the sea-side town of

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Büsum in northern Germany. The temperature varied between –7 °C and 20°C over the course of the

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sampling period and TSP varied from 2 µg m–3 to 65 µg m–3 (median 16 µg m–3) (a summary of the

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sampling and analysis techniques is presented in the SI).

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The set of compounds for comparison of fpart,T, fpart,H-B, fpart,J-P and fpart,M included nine compounds:

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TBEP, TCEP, TCP, TCPP, TDCPP, TEHP, TiBP, TnBP and TPhP. This reduced dataset covered a wide range

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of physicochemical properties with log PL between –4.5 for TDCPP and 0.9 for TCEP and log KOA

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between 7 for TIBP and 14 for TEHP.

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3. Results and Discussion

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3.1 fpart predictions by the Tool

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The Tool calculates KOA based on the partition coefficients KAW and KOW. Data for log KAW and log KOW

199

for each compound were on average within two log units but deviated by up to eight and nine log

200

units, respectively, for log KAW (TDBPP) and log KOW (MC984) (Tables S1, S2). Datasets from models

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(EPISuite, SPARC and Absolv) were on average lower for log KAW and higher for log KOW than data from

202

literature sources (Table S5).

203

The approximation of KOA based on other partition coefficients in itself introduces uncertainty.

204

Furthermore, scatter of KAW and KOW data can potentially add additional uncertainty and could,

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therefore, impact the uncertainty of fpart,T.

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For most chemicals, values of fpart,T obtained from the three data sets were consistent (Table 1, Figure

207

1): All input data sets led to fpart,T > 0.9 for 18 compounds and fpart,T < 0.1 for 13 compounds (Table 1).

208

The results were more diverse for only for seven OPEs; fpart,T estimated from the Modelled Data set

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for isomers of TCP (TmCP, ToCP and TpCP) as well as BEHP, EHDPP, IDDPP and TEHP were considerably

210

lower (0.35, 0.70, 0.24, 0.67 and 0.87) than the results of the Input all and Outlier Removed data sets

211

(1.00, 0.94, 0.97, 0.98 and 1.0) (Table 1).

212

These results do not support the contention that OPEs partition only to the particle phase.

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Specifically, compounds with a log KOA between 10 and 12 were partially in the gas and partially in the

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particle phase: fpart,T for BDCPP was 0.32–0.48, for DCP was 0.14–0.28, for TDCIPP was 0.27, and for

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TDCPP was 0.31–0.38. BEHP, EHDPP, IDDPP and the TCP isomer in the Modelled Data set were also

216

predicted to have appreciable fractions in both phases (as described above) (Figure 1, Table 1).

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Figure 1: fpart,T predicted by the Tool plotted against log KOA obtained from the three input data sets (Input all,

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Modelled Data and Outlier Removed). The dotted lines mark the areas with compounds predominantly in the

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particle phase (fpart,T > 0.9) and compounds predominantly in the gas phase (fpart,T < 0.1). Compounds with more

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than 10% in both phases are labelled individually.

222 223 224 225 226 227 228 229

Table 1: Predictions of fpart,T for 32 OPEs obtained from the OECD Tool Compound

Input all

Outlier removed

Modelled input data

BCMP-BCEP

1.00

1.00

1.00

BDCPP

0.48

0.48

0.32

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BEHP

0.92

0.94

0.74

BPA-BDPP (BADP)

0.97

0.97

1.00

DCP

0.15

0.14 -3

0.28 -3

1.8 x 10

1.8 x 10

EHDPP

0.97

0.97

0.24

IDDPP

0.98

0.98

0.67

MC 984

1.00

1.00

0.99

PBDMPP

1.00

1.00

1.00

PBDPP (RDP)

1.00

1.00

1.00

TBEP

0.98

0.98

0.92

TCEP

4.5 x 10-4

4.5 x 10-4

3.4 x 10-4

TCIPP

5.8 x 10

1.6 x 10

TCP

0.74

0.66

0.54

TDBPP

1.00

1.00

1.00

TDCIPP

0.28

0.28

0.26

TDCPP

0.38

0.38

0.31

TDMPP

1.00

1.00

0.97

TEHP

1.00

-3

-3

1.00 -5 -5

2.8 x 10

-4

DOPO

2.7 x 10

-3

0.87

8.0 x 10

-6

3.3 x 10-6

-5

2.9 x 10

TEP

1.0 x 10

TIBP

9.1 x 10

8.1 x 10

TiPP

2.9 x 10-5

2.0 x 10-5

2.1 x 10-5

TmCP

1.00

1.00

0.35

TMP

-7

1.8 x 10

-3

-4

1.8 x 10

-7

2.1 x 10-7

-4

4.2 x 10

TnBP

1.0 x 10

6.0 x 10

ToCP

1.00

1.00

0.35

TpCP

1.00

1.00

0.35

TPhP

0.059

0.018

0.061

TPPP

1.00

1.00

0.98

TTBNPP

1.00

1.00

1.00

TTBPP

1.00

1.00

1.00

-4

230 231 232 233 234 235

3.2 Evaluation of the impact of uncertainty of input data on the prediction of OPE environmental

236

behaviour with the Tool

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To evaluate the sensitivity of the tested compounds to individual changes of log KOW and log KAW as

238

well as the uncertainty of fpart,T, sensitivity and Monte Carlo uncertainty analyses were performed. For

239

the sensitivity analysis log KOW and log KAW data from the Outlier Removed data set were used. The

240

Monte Carlo uncertainty analysis was performed for all compounds of the Outlier Removed dataset

241

with fpart,T < 0.9.

242

fpart values of 22% of the 32 OPEs (7 compounds) displayed sensitivities from less than 5% (absolute)

243

to as high as 108% to individual changes of log KAW and log KOW by a factor of ±1.1 (±10%). Within this

244

group of 7 compounds, sensitivity was greatest for changes in log KAW. Very high sensitivities were

245

observed for compounds with predicted fpart,T ≤ 10–3, while compounds with predicted fpart close to 1

246

displayed the lowest sensitivities to log KOW and log KAW. However, high absolute sensitivity values for

247

compounds with fpart,T ≤ 10–3 did not change their general partitioning behaviour of fpart,T < 0.1. Effects

248

of changing log KOW and log KAW on the partitioning behaviour were only observed for compounds

249

with fpart,T between 0.1 and 0.9 (Table S8).

250

The Monte Carlo analysis revealed that uncertainties in values of log KOW and log KAW did not alter the

251

general partitioning tendency of the tested compounds using either the 25th-75th percentile or the

252

default dispersion factors (Table S9 and S10). Interestingly, even OPEs with intermediate fpart values

253

(between 0.1 and 0.9) such as BDCPP were not greatly affected by the variation: the predicted value

254

for fpart was 0.46 and the Monte Carlo analysis returned 0.4 and 0.52 for the 25th and 75th percentile.

255

In summary the results of the sensitivity as well as the uncertainty analysis indicated that the Tool’s

256

prediction of OPE partitioning between gas and particle phases did not significantly change with input

257

data uncertainty. Compounds with initial low or non-distinct gas-particle partitioning properties (fpart

258

between 0.1 and 0.9) were found to be more affected by changes in input data than compounds with

259

fpart close to 1. However, this sensitivity did not cause any significant changes in the fpart prediction.

260

3.3 Comparison of Tool (fpart,T), J-P model (fpart,J-P) and H-B model (fpart,H-B) predictions

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Using the Input all or Outlier removed dataset, fpart predictions were statistically indistinguishable for

262

the two KOA-based models, the Tool and the H-B model (Table S11). The J-P model, in general,

263

predicted similar partitioning behaviour to the Tool and H-B model for 27 out of 32 compounds (81

264

%). For the remaining 6 compounds (DCP, TMP, TnBP, ToCP PBDMPP and TDBPP) the Tool/H-B model

265

and J-P model predictions differed considerably (Table S11).

266

An explanation for the considerable differences could be that all of these compounds had either a log

267

KOA between 10 and 12 (Figure 1) or a log PL between –5 and –2 and were therefore predicted to

268

partition between gas and particle phases, which means that fpart is relatively sensitive to differences

269

in input data or estimation method (Figure 1).

270

Unexpectedly, fpart predictions using the J-P model changed significantly when physicochemical input

271

data estimated by SPARC or EPISuite were used (t-test at p < 0.05). Furthermore, J-P results based on

272

EPISuite input data indicated a significantly different partitioning behaviour (t-test at p < 0.05) for 15

273

OPEs (47 %) compared to the Tool and H-B model (Table S11).

274

Interestingly, most (13) of the J-P model fpart,J-P predictions with significant differences compared to

275

the other prediction methods were lower than the Tool and H-B model. Previous studies reported

276

that the J-P model tended to overestimate fpart compared to measurements for several classes of

277

semi-volatile organic compounds (33–36).

278

3.4 Comparison of modelled partitioning with measured partitioning of OPEs (fpart,M)

279

Neither the sensitivity nor the uncertainty analysis provided compelling evidence that the uncertainty

280

of chemical property data was responsible for the observed discrepancy between the fpart values from

281

the Tool and the prevalent hypothesis in the literature that OPEs partition primarily to the particle

282

phase. We therefore re-assessed the initial hypothesis. To this end, we compared the fpart,T, fpart,H-B and

283

fpart,J-P values with measured fpart,M data. We used the dataset of Wolschke et al. (2016) (21), who

284

reported a year of weekly OPE air concentrations for 13 OPEs. The median TSP for the Wolschke et al.

285

(2016) (21) data set was 16 µg m–3. For comparison we calculated all fpart based on this value. 13 ACS Paragon Plus Environment

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Plotting fpart results of calculated vs. measured datasets yielded unexpected results. Calculated values

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of fpart,T, fpart,H-B and fpart,J-P correlated well with fpart,M values (21), which reported a significant fraction

288

of OPEs in the gas-phase (Figure S1, Table 2), whereas they did not agree with the hypothesis that

289

OPEs primarily partition into the particle-phase (Figure S1, S2).

290

Furthermore, fpart,T, fpart,H-B, fpart,J-P and fpart,M all showed strong positive correlations with log KOA and

291

negative correlations with log PL (Table 2, Figures S3 and S4). The weakest correlation resulted from

292

the H-B model for log PL and the J-P model for log KOA with Pearson correlation coefficients, r, of –

293

0.40 for log PL vs. fpart,H-B and r = 0.65 for log KOA vs. fpart,J-P (Table 2). The resulting plots of fpart vs. log

294

KOA show the S-shape that is typical for the relationship between log KOA and particle partitioning with

295

0% partitioning to particles at log KOA < 10 and 100% partitioning into the particle phase at log KOA >

296

12 (Figure 1).

297

Table 2: Pearson correlation coefficient, r, for fpart results of measured and modelled datasets as well as with the

298

partition coefficients log KOW and log KOA and subcooled liquid vapour pressure log PL.

OECD POV and LRT Screening Tool fpart,M

fpart Modelled Data

fpart fpart fpart Input all Outlier Removed H-B model

fpart J-P model

log PL log KOA

–0.90 0.89

–0.70 0.84

–0.76 0.85

–0.75 0.86

–0.40 0.83

–0.91 0.65

fpart,M

1

0.95

0.83

0.80

0.87

0.90

299 300

The strong correlations between predicted and measured fpart for the nine compared OPEs (presented

301

in Figure S1) are primarily related to the agreement of predictions and measurements of fpart for OPEs

302

with distinct predicted partitioning (fpart below 0.1 or above 0.9). OPEs with predicted fpart between

303

0.1 and 0.9 displayed high variability in measured as well as modelled fpart. To identify the driving

304

factors for the variation in observed fpart for these compounds, namely TDCPP, TPhP and TCP, we

305

assessed the impact of various factors on the partitioning behaviour of OPEs.

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EPISuite, SPARC and Absolv are commonly used to estimate physicochemical properties. In our recent

308

paper (Zhang and Suhring et al. 2016) we found that predictions for physicochemical properties could

309

vary significantly between EPISuite and SPARC, whereas Absolv and EPISuite produced similar

310

datasets. We therefore, assessed the correlations of fpart estimates from the Tool, the H-B model and

311

the J-P model with measured fpart,M data using only measured physicochemical properties and those

312

estimated by EPISuite and SPARC as model inputs.

313

For all three models input data estimated with SPARC led to highest correlations with fpart,M (Figure 2).

314

The Tool had the overall best agreement with fpart,M followed by the H-B model predictions (Figure 2).

315

Unexpectedly, fpart,J-P correlated poorly with the measured results (fpart,M) when either EPISuite or

316

SPARC input data were used (Figure 2). This was unexpected because, with median values from

317

SPARC, EPISuite and literature, fpart,J-P was in good agreement with fpart,M (Table 2). Furthermore, using

318

measured PL as input also gave good agreement of fpart,J-P and fpart,M (Table 2, Figure 2).

319

Contrary to the Tool predictions, the J-P model predictions seemed to be strongly affected by the

320

variability in input data – specifically PL. These strong differences in J-P model predictions based on

321

different input data sets emphasize the need for reliable and evaluated physicochemical property

322

data in order to obtain consistent and reproducible results that can be used in chemical risk

323

assessment.

324 325

Figure 2: fpart,M vs. fpart,H-B and fpart,J-P (measured PL) (left) and fpart,M vs. fpart,J-P (right) using physicochemical

326

properties estimated by EPISuite and SPARC as well as measured PL.

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327 328

3.5 Driving factors for partitioning behaviour of OPEs

329

All tests assessing potential errors and sources of uncertainty in the Tool and H-B model – the

330

evaluation of the impact of input data uncertainty, the comparison of model results with measured

331

fpart,M and correlation with physicochemical properties – led to the same conclusion: OPEs with a log

332

KOA < 10 partition into the gas-phase. This is in contrast to previous reports on OPE behaviour in the

333

environment (12, 13, 14, 15, 37).

334

To some extent, this discrepancy may be explained by the choice of analytes in the literature, e.g.

335

primarily halogenated OPEs with high log KOA. However, that does not explain the frequent reports of

336

e.g. TCEP in the particle phase of atmospheric samples around the world (12, 13, 15, 37, 38), because

337

according to the Tool, H-B and J-P model TCEP would primarily partition into the gas phase.

338

Our results indicate that uncertainty (Monte Carlo analysis) of physicochemical properties such as log

339

KAW, log KOW and log PL was not responsible for significant differences in the predicted partitioning

340

behaviour between gas- and particle phases in the Tool and H-B model. Therefore, our next step was

341

to identify and evaluate potential external drivers. External factors could be meteorological factors

342

such as temperature.

343

The temperature in the Tool is set to 298.15 K by default. However, the partitioning behaviour, as

344

calculated by the Tool, does not depend on changes in temperature (Table S12). This lack of

345

temperature dependence in the Tool could be a source of error for fpart predictions. Both log KOA as

346

well as PL are highly temperature dependent (39). The derived partition coefficient log KOA in the Tool

347

should represent this temperature dependence. Otherwise, fpart could be systematically under

348

predicted in regions with temperatures consistantly below 20°C (298.15 K) such as the Arctic. A

349

correlation of the fpart values reported by Wolschke et al. (2016) (21) with temperatures at the time of

350

sampling yielded, however, a correlation coefficient, r, (Pearson) below 0.30, perhaps because of the

351

narrow temperature range between 3 and 17oC (Table S13). The parameter with the highest 16 ACS Paragon Plus Environment

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correlation with fpart,M was the particle concentration in air, with r up to 0.45 for compounds with

353

measured (and predicted) fpart > 0.8 (Table S13)..

354

Thus, we next assessed the impact of particle concentration (coarse, ø 2.5–10 μm) in the atmosphere

355

(TSPcoarse) on fpart,T. TSPcoarse varies by several orders of magnitude between different countries or

356

regions; with annual mean values between 2 μg m-3 in Powell River, Canada, to 153 μg m-3 in Delhi,

357

India (40). Daily concentrations have even been reported to reach up to 1000 μg m-3 in Beijing, China

358

(41). Locally, TSPcoarse concentrations can be increased at low temperatures or decreased by rain/snow

359

events (26).

360

In the Tool TSPcoarse is expressed as a volume fraction. The default value is 2 * 10–11, which represents

361

an average background particle concentration, equal to 30 pg m–3. However, OPEs are usually

362

produced and emitted and urban or industrial areas, with TSPcoarse in the 10–10 range or higher,

363

whereas deposition in the Arctic would suggest TSPcoarse volume fractions of 10–12. The default TSPcoarse

364

used in the Tool is therefore likely not representative for the conditions in these environments.

365

To assess the impact of varying particle concentrations in the atmosphere on fpart,T we used TSPcoarse

366

volume fractions between 10–12 and 10–9 on the Outlier Removed data set as well as the Modelled

367

Data set. This caused major changes in the partitioning behaviour of OPEs with log KOA between 6 and

368

12, whereas the partitioning of compounds with log KOA below 7 or higher than 12 was not affected

369

(Figure 3). Interestingly, differences in the general predicted partitioning behaviour between the

370

Outlier Removed data set and Modelled Data set (Table 1) disappeared at TSPcoarse above 10–11 (Tables

371

S14, S15). For TSPcoarse of 10-12 in the Outlier removed and modelled dataset, the fraction of OPEs

372

partitioning into the gas phase was 44% and 66%, respectively. At TSPcoarse of 10–11, this fraction was

373

reduced to 41% and 53%. At TSPcoarse of 10-10 and 10-9 the datasets produced the same predictions for

374

the number of OPEs in the gas phase with 28% and 25%, respectively (see Supporting Information

375

Tables S14 and S15 for detailed information).

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376 377

Figure 3: Log KOA vs. fpart,T for the Outlier Removed dataset for different values of TSPcoarse; the dotted lines mark

378

the areas of distinct partitioning behaviour for all scenarios (above fpart,T = 0.9/ below fpart,T = 0.1). Compounds

379

with major fpart,T changes depending on TSPcoarse are labelled individually.

380

Our results indicate that roughly half of the OPEs into the gas phase regardless of whether

381

predictions are made with the Tool, the H-B model, or J-P model, and are consistent with

382

measurements of fpart by Wolschke et al. (2016) (21). However, the lack of temperature dependence

383

of fpart,T estimated by the Tool is a potential source of error and could lead to a systematic

384

underestimation of fpart in cold regions.

385

Of the commonly used models for estimating physicochemical properties and partition coefficients,

386

SPARC led to fpart estimates closer to the measured data than EPISuite. The unexpected discrepancy

387

between fpart,J-P estimates using modelled PL and measured fpart,M should be further investigated,

388

especially considering that J-P predictions using measured PL showed strong correlations with fpart,M.

389

Changes in fpart,T based on differences in TSP emphasize the importance of sampling location in

390

addition to time (e.g. before or after rain events) on fpart. In conclusion, our results show that OPEs 18 ACS Paragon Plus Environment

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391

with log KOA values below 10 or a log PL above –5, such as BDCPP, DCP, DOPO, TCEP, TCIPP, TDCIPP,

392

TDCPP, TEP, TIBP, TIPP, TMP, TnBP and TPhP, should not be limited to the particle phase.

393

Acknowledgements

394 395

We would like to thank Xianming Zhang from the University of Toronto and Zhiyong Xie from the Helmholtz-Zentrum Geesthacht for their help in data analysis and evaluation.

396 397 398 399 400 401 402 403 404 405 406 407 408 409 410 411 412 413 414 415 416 417 418 419 420 421 422 423 424 425 426 427 428 429 430 431

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