jssc4520-sup-0001-SuppMat

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Supplementary information
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1. Section 1 – Sampling procedure
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1.1 Preparation of the needle traps
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First, a stainless wire was pressed by two steel guides and fixed into the desired position as a
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spring plug. Then, sorbent particles were aspirated into the needle by a tap-water aspirator and
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held by the spring plug. After packing the desired length of sorbent bed, a small amount of epoxy
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glue was used to immobilize the sorbent in the opening end. During the packing process, the
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aspirator was kept running until the epoxy glue was cured so as to avoid the blockage of the NT
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by the epoxy glue. The sorbent beds packed inside the needles for this work were 1 cm 100/120
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mesh DVB plus 1 cm 60/80 mesh Car. After packing, the NTs were conditioned in a GC injector
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for 3 hours with helium gas continuously flowing through the needle. The conditioning
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temperature was 260 °C. This process was similar to previous works 1–6.
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1.2 Sampling chambers
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The sampling chamber employed for the MFX evaluation consisted of a custom made 1.5 L glass
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bulb with several sampling ports that were plugged with Thermogreen® LB-2 predrilled septa.
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Omega 120 W heating tape was wrapped around the glass bulb to control the temperature inside
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the bulb. An Omega K-type thermocouple was attached to the outside surface of the glass bulb
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in order to control its internal temperature. Heating tape and thermocouple were connected to an
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electronic heat control device constructed by the Electronic Science Shop at the University of
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Waterloo (UW). Air temperatures in the vicinity of the SPME fibres were maintained within
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±1.2% of the adjusted temperature. The standard gas generator consisted of a permeation chamber
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where Teflon tubes filled with the model compounds were placed and maintained at constant
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temperature and nitrogen flow. Standard gas flow rates ranged from 50 to 3000 mL/min, resulting
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in mean air velocities similar to those encountered in indoor air environments. Standard gas
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generators and sampling chambers were validated using a multi-bed needle trap.
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1.3 Indoors time-weighted average sampling
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A diffusive fibre holder (DFH), as well as bare 85 μm FFA CAR/PDMS fibres were used for
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passive sampling. A magnetic plunger was built at the machine shop of the University of
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Waterloo to control the diffusion path of the bare FFA fibre. Rare-earth magnets employed to
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manufacture this plunger were acquired at Lee Valley (Waterloo, Ontario, Canada). Samplings
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were performed over a period of 8 hours, between 9 am and 5 pm, during three different days in
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the same week. For DFH evaluation, as described below, one of the fibres was installed on the
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diffusive fibre holder while another two were used as controls.
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1.4 Indoors air sampling in active mode
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A portable dynamic air sampling device (PDAS) for SPME, described in Section 1 of the
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Supplementary Information (Figure S10), was employed in the quantification of indoor
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contaminants present in the air of a polymer synthesis laboratory at the University of Waterloo 7.
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A magnetic plunger was used to expose the fibre coating; measurements exposing a SPME-FFA
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Car/PDMS fibre for 30 s were performed four times within a day, using independent fibres. The
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concentration of the target analytes was calculated using the diffusion-based SPME quantitative
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model defined by Equation S1 in Section 2 of the Supplementary Information. A complete
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description of the parameters used in these calculations is listed in Table S1.
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1.5 Sampling and desorption of needle traps
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For indoor air sampling and verification of concentrations in the exposure chamber, the NTD was
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connected to the sampling pump while a volume of the gaseous sample was pumped at a flow rate
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of 5 mL min-1. After sampling, the NTD was connected to a 1 mL gas-tight syringe filled with
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helium, and introduced into a GC injector for desorption. Helium was consistently pushed out to
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assist desorption throughout the whole desorption period. For NTDs packed with DVB/Car, the
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needle was injected into the hot GC injector at a temperature of 260 °C for 1 min, assisted by 0.3
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mL of helium 5,6.
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2. Section 2- SPME diffusion based calibration approach
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Significant research with SPME has focused on applications for air sampling and analysis. The
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theory behind equilibrium and non-equilibrium extractions for liquid coatings is well understood
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and described in the literature. Despite the sensitivity of solid coatings for the extraction of VOCs
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being higher when compared to PDMS, competitive adsorption and displacement effects make
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mass calibration and quantification particularly challenging. In order to solve this issue, Koziel et
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al.
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critical restrictions: short sampling times and non-equilibrium conditions. Following these rules,
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the effects of competitive adsorption are diminished, and the coating can be calibrated on the initial
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linear extraction region. If the concentration of the analyte is assumed to be constant for a very
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short sampling time, the concentration can be estimated from the following equation:
7,8
proposed an approach that relies on diffusion-controlled extraction. This method has two
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where n is the mass of extracted analyte in nanograms over sampling time t; Dg is the gas-phase
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molecular diffusion coefficient (cm2/s); b is the outside radius of the fibre coating (cm); L is the
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length of the coated rod (cm); δ is the thickness of the boundary layer surrounding the fibre coating
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(cm); t is the sampling time (s), and Cg is the analyte concentration in bulk air (ng/mL). L and b
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are constant for each type of fibre coating, and n can be estimated from the detector response. The
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diffusion coefficients of the analytes can be estimated from physicochemical properties using the
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method proposed by Fuller, Schettler, and Giddings (FSG)9:
𝐢𝑔 =
𝑛 ln((𝑏 + 𝛿)/𝑏)
2πœ‹π·π‘” 𝐿𝑑
Equation S1
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0.001 × π‘‡ 1.75 1/π‘€π‘Žπ‘–π‘Ÿ + 1/𝑀𝑉𝑂𝐢
𝐷𝑔 =
𝑝
π‘‰π‘Žπ‘–π‘Ÿ 1/3 +
𝑉𝑉𝑂𝐢 1/3 2
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Equation S2
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Where Dg is expressed in cm2/s, T is the absolute temperature (K), Mair and MVOC are molecular
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weights for air and the VOC of interest, p is the absolute pressure (atm), and Vair and VVOC are the
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molar volumes of air and the VOC of interest (cm3/mol). Additionally, based on Koziel and
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collaborators, the effective thickness of the boundary layer can be estimated using the following
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equation:
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𝛿 = 9.52 (𝑏/𝑅𝑒 0.62 𝑆𝑐 0.38 )
Equation S3
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Where Re is the Reynolds number, Re = 2ub/v, u is the linear air velocity (cm/s), v is the kinematic
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viscosity for air (cm2/s), Sc is the Schmidt number, and Sc = v/Dg. Particular attention should be
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paid to control convection conditions during extraction in order to maintain a constant boundary
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layer, and hence avoid variations in the extracted amounts of analyte. In addition, by using forced
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air, the sensitivity of the solid coatings is enhanced. In order to facilitate control of convection
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conditions, Augusto et al. designed a Portable Dynamic Air Sampler (PDAS) for SPME. Figure
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S7 presents the schematic of the device built using a hair-dryer. This instrument was modified to
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revert the air flow direction and to disable the internal heating coil. When compared to standard
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methodologies, the authors demonstrated that a 30 s sampling time using PDAS-SPME allowed
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measurement of VOC concentrations that were not detected by the NIOSH standard method, even
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after several hours of extraction using expensive and non-reusable materials. It should be also
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emphasized that short sampling times are important so that the effect of relative humidity on the
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adsorption of VOCs on the solid coatings is minimized. Indeed, to obtain accurate and precise
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concentrations, the sampling time should be properly measured. One interesting advantage of this
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method is that external calibration is not needed since sampling conditions and constants are
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known. Also, since the method depends on the dimensional parameters of the fibres, its dimensions
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and integrity should be checked prior to sampling.
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Supplementary Figures
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Lexan™ case
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Glass bulb
Septa
e
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FFA device
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d
Heating tape
a
Insulation
c
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b
Standard gas
Heat control
Upper view
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Front view
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Figure S1 Glass container for live plants BVOC extraction: 1, silanized glass cylindrical body
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(120 mm x 60 mm); 2, silanized glass lid; 3, sampling holes topped with Thermogreen LB-2 septa;
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4, thermocouple; 5, SPME-FFA 65μm DVB/PDMS; 6, microfan (40 mm x 40 mm x 6 mm); and
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7, Teflon tape seal 10.
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35.0
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Amount extracted (ng)
30.0
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25.0
146
20.0
147
15.0
148
10.0
5.0
149
0.0
150
Benzene
Toluene
FB
FF
FL
o-Xylene
FM
FV
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Figure S2 Amount extracted of BTX in nanograms using passive sampling with 5 different
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Car/PDMS fibres (n=5). Samples were taken from a standard gas generator using SPME in passive
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sampling mode (Z=0.2 cm, t = 15 minutes).
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1.0
FL
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FM
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0.5
FB
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Factor 2: 23.62%
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0.0
-0.5
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FF
FV
-1.0
-2
-1
0
1
2
Factor 1: 76.32%
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Figure S3 Principal component analyses of 5 Car/PDMS SPME-FFA fibres. Samples were taken
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from a standard gas generator using SPME in passive sampling mode (Z=0.2 cm, t = 15 minutes).
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Figure S4 Schematic drawing of the Diffusive Sampling Fibre Holder (DFH).
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Concentration of Toluene (ng/mL)
1.8
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1.6
1.4
1.2
1.0
0.8
0.6
0.4
0.2
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0.0
Day 3
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Day 2
AVG-TWA
Day 1
DFH
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Figure S5 Evaluation of the diffusive fibre holder (DFH) versus conventional FFA-SPME devices
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using 85μm Car/PDMS (Z=0.147 cm, t = 8 hours). AVG-TWA is the mean toluene concentration
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value obtained with two fibres without holder. DFH is the value obtained using a single FFA device
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placed on the DFH.
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Percentage of BTX left on the fibre (%)
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110
100
90
80
70
60
50
Benzene
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Toluene
0h
Ethylbenzene
12h
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Figure S6 Evaluation of the storage stability up to 12 hours of the diffusive fibre holder (DFH)
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using 85 μm Car/PDMS (Z=0.147 cm, t = 8 hours, n=5).
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Figure S7 Schematic of the portable dynamic air sampling device for SPME developed by
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Augusto et al. Image was taken with permission from reference 7.
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Supplementary tables
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Table S1 Latin-square design used for the evaluation of 5 different 85 μm CAR/PDMS fibres.
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Positions on the MFX tray and the sampling chamber were both randomized. F#Xx, where # is the
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number of the fibre, X is the position on the chamber, and x is the position on the MFX tray. a,
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position 1; b, position 5; c, position 21; d, position, 25, and e, position 13.
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Replicate
1
2
3
3
5
F1Aa
F2Ab
F3Ac
F4Ad
F5Ae
Fibre Position (F#Xx)
F5Bd
F4Cd
F3De
F1Be
F5Cc
F4Da
F2Ba
F1Cd
F5Db
F3Bd
F2Ce
F1Dc
F4Bc
F3Ca
F2Dd
F2Ec
F3Ed
F4Ee
F5Ea
F1Eb
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Table S2 Experimental parameters used to determine the concentration of toluene in indoor air in
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a polymer synthesis laboratory using SPME diffusion-based calibration.
Parameters/Day time (h)
10:30
11:45
15:30
16:35
Units
Concentration
1.62
0.21
0.14
0.10
ng/mL
37
5
3
2
ng
Temperature
295.6
295.6
295.3
295.2
K
Diffusion coefficient (Dg)
0.0793
0.0793
0.0791
0.0791
cm2/s
Boundary layer thickness
0.0135
0.0135
0.0135
0.0135
cm
Reynolds number
28.339
28.339
28.391
28.407
-
Air kinematic viscosity (v)
0.1535
0.1535
0.1532
0.1531
cm2/s
Schmidt number
1.937
1.937
1.937
1.937
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Amount extracted
Fibre radio (b)
0.0145
cm
Fibre length (L)
1
cm
Sampling time (t)
30
s
Pressure (P)
1
atm
Mass air
28.97
g/mol
Volume air
20.1
cm3/mol
Mr
0.045
mol/g
Mass toluene
92.14
g/mol
Volume toluene
111.14
cm3/mol
150
cm/s
Linear velocity of the air (u)
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References
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