| Literature DB >> 25309959 |
Young-Kyo Seo1, Lakshmi Narayana Suvarapu1, Sung-Ok Baek1.
Abstract
Odorous compounds play an important role in air pollution in industrial areas and the residential areas surrounding them. This study measured the odorous volatile organic compounds (VOC) and carbonyl compounds at Yeosu and Gwangyang, two large industrial areas of South Korea, during four seasons of 2008-2009. Along with these two cities, the same odorous compounds were measured at Suncheon, which was selected as a control site. The concentrations of VOC and carbonyl compounds that were listed as odorous air pollutants by the Ministry of Environment of South Korea are discussed. Benzene and formaldehyde were included in the target analytes because of their carcinogenic nature. Most researchers only examined the concentration of odorous compounds in ambient air but the present study evaluated the odor intensity, which is a new parameter that will help better understand the precise odor perceived by people. This paper describes the seasonal variations and spatial distribution of the above-mentioned odorous compounds at the specified sites. Pearson correlation coefficients between the odorous compounds and other air pollutants, such as ozone, CO, SO2, NO2, and PM10, and meteorological conditions, such as temperature and wind speed, provide the source information of odorous VOC and carbonyl compounds.Entities:
Mesh:
Substances:
Year: 2014 PMID: 25309959 PMCID: PMC4182693 DOI: 10.1155/2014/824301
Source DB: PubMed Journal: ScientificWorldJournal ISSN: 1537-744X
Figure 1Location of the sampling sites at Yeosu, Gwangyang, and Suncheon.
Analytical conditions for VOC with thermodesorption GC/MSD.
|
Thermal desorber |
GC/MSD | ||
|---|---|---|---|
| Oven temp. | 300°C | GC column | Rtx-1 (0.32 mm, 105 m, 1.5 |
| Desorb time | 10 min | Initial temp. | 50°C (10 min) |
| Desorb flow | 50 mL/min | Oven ramp rate | 5°C/min |
| Cold trap holding time | 5 min | Final temp. | 250°C (5 min) |
| Cold trap high temp. | 320°C | Post run | 250°C (5 min) |
| Cold trap low temp. | −10°C | Column flow | 1.13 mL/min |
| Cold trap packing | Tenax TA/carbopack B | Detector type | Quadropole |
| Min. pressure | 12 psi | Q-pole temp. | 150°C |
| Inlet split | No | MS Source temp. | 230°C |
| Outlet split | 10 mL/min | Mass range | 35~300 amu |
| Valve and line temp. | 180°C | Electron energy | 70 eV |
Physicochemical characteristics of odor compounds in this study.
| Compounds | Abb. | CAS No. | Odorous compounds | MW (g/mol) | Bp (°C) | |
|---|---|---|---|---|---|---|
| Korea | Japan | |||||
| Benzene | BZ | 71-43-2 | — | — | 78.11 | 80.1 |
| Ethyl acetate | EA | 141-78-6 | — | ○ | 88.11 | 77.1 |
| Methyl isobutyl ketone | MIBK | 108-10-1 | ○ | ○ | 100.16 | 117.0 |
| Toluene | TOL | 108-88-3 | ○ | ○ | 92.14 | 111.0 |
|
| mpXYLN | 108-38-3 | ○ | ○ | 106.16 | 139.0 |
|
| oXYLN | 95-47-6 | ○ | ○ | 106.17 | 144.4 |
| Styrene | STR | 100-42-5 | ○ | ○ | 104.15 | 145.0 |
| Formaldehyde | FRML | 50-00-0 | — | — | 30.03 | −19.0 |
| Acetaldehyde | ACTL | 75-07-0 | ○ | ○ | 44.05 | 20.2 |
| Propionaldehyde | PPNL | 123-38-6 | ○ | ○ | 58.08 | 46.0 |
| Methyl ethyl ketone | MEK | 78-93-3 | ○ | — | 72.11 | 79.6 |
| Butyraldehyde | BTL | 123-72-8 | ○ | ○ | 72.11 | 74.8 |
|
| iVAL | 590-86-3 | ○ | ○ | 86.13 | 92.0 |
|
| nVAL | 100-62-3 | ○ | ○ | 86.13 | 102.0 |
Operating conditions for the HPLC analysis of carbonyl compounds.
| Operating parameter | Specifications and conditions |
|---|---|
| HPLC system | Shimadzu SCL-6B with Shimadzu SPD-6 AV UV/VIS detector at 360 nm |
| Analytical column | Shim-Pack CL-ODS (M) 4.6 mm × 150 mm with a C18 guard column |
| Mobile phase | A: acetonitrile 100 (V), |
| Gradient elution | 100% for B for 5 min, and then 60 : 40% A : B for 15 min, finally 100% A for 50 min |
| Flow rate and injection volume | 1.0 mL/min and 20 |
Figure 2Concentrations of formaldehyde and acetaldehyde obtained during the analysis at Yeungnam University and Suncheon College (interlab comparison).
Interlaboratory comparison of the concentration of same carbonyl compounds analyzed at author's laboratory (Yeungnam University, YNU) and another laboratory (Suncheon College, SCC).
| Compounds | Sample number | MDP(1) (%) | MRE I(2) (%) | MRE II(3) (%) |
|
| Paired |
|---|---|---|---|---|---|---|---|
| Formaldehyde | 90 | 27.8 | 23.9 | 37.8 | 0.94∗(5) | 0.2 | 0 |
| Acetaldehyde | 90 | 18.5 | 15.3 | 25.6 | 0.97∗ | 0.46 | 0 |
(1)MDP (mean duplicate precision, %) = (1/n)∑ (|YNU − SCC|/Mean) × 100 (%).
(2)MRE I (mean relative error, %) = (1/n)∑ (|YNU − SCC|/YNU) × 100 (%).
(3)MRE II (mean relative error, %) = (1/n)∑ (|YNU − SCC|/SCC) × 100 (%).
(4) R: correlation coefficient.
(5)∗Correlation coefficients are significant at a level of 0.05.
Statistical summaries of the VOC at different sites in the present study.
| Sites | VOC | Detection frequency | Mean (ppb) | S.D. (ppb) | Median (ppb) | Min (ppb) | Max (ppb) |
|---|---|---|---|---|---|---|---|
| YI | Ethyl acetate | 79% | 0.39 | 1.29 | 0.11 | N.D. | 16.75 |
| Benzene | 100% | 3.65 | 6.86 | 1.75 | 0.14 | 38.31 | |
| Methyl isobutyl ketone | 26% | 0.11 | 0.23 | N.D. | N.D. | 1.46 | |
| Toluene | 100% | 3.25 | 4.40 | 2.01 | 0.06 | 38.61 | |
|
| 100% | 2.50 | 3.57 | 1.17 | 0.06 | 25.61 | |
| Styrene | 48% | 0.25 | 0.44 | N.D. | N.D. | 4.07 | |
|
| 100% | 0.58 | 0.65 | 0.34 | 0.02 | 4.47 | |
|
| |||||||
| YR | Ethyl acetate | 76% | 0.11 | 0.12 | 0.07 | N.D. | 0.49 |
| Benzene | 100% | 1.07 | 1.02 | 0.75 | 0.04 | 5.93 | |
| Methyl isobutyl ketone | 9% | 0.01 | 0.04 | N.D. | N.D. | 0.23 | |
| Toluene | 100% | 1.61 | 2.09 | 0.98 | 0.05 | 17.41 | |
|
| 99% | 0.36 | 0.35 | 0.20 | N.D. | 1.71 | |
| Styrene | 29% | 0.15 | 0.34 | N.D. | N.D. | 1.82 | |
|
| 98% | 0.10 | 0.09 | 0.07 | N.D. | 0.47 | |
|
| |||||||
| GI | Ethyl acetate | 62% | 0.12 | 0.22 | 0.05 | N.D. | 1.64 |
| Benzene | 100% | 1.64 | 3.83 | 0.40 | 0.06 | 27.12 | |
| Methyl isobutyl ketone | 6% | 0.01 | 0.05 | N.D. | N.D. | 0.37 | |
| Toluene | 100% | 0.97 | 0.87 | 0.75 | 0.04 | 8.45 | |
|
| 99% | 1.09 | 5.78 | 0.28 | N.D. | 27.36 | |
| Styrene | 4% | 0.01 | 0.05 | N.D. | N.D. | 0.46 | |
|
| 97% | 0.28 | 1.22 | 0.08 | N.D. | 16.06 | |
|
| |||||||
| GR | Ethyl acetate | 73% | 0.10 | 0.13 | 0.06 | N.D. | 0.83 |
| Benzene | 100% | 0.59 | 0.72 | 0.40 | 0.07 | 6.66 | |
| Methyl isobutyl ketone | 3% | <0.01 | 0.03 | N.D. | N.D. | 0.29 | |
| Toluene | 100% | 0.98 | 0.77 | 0.78 | 0.01 | 4.10 | |
|
| 98% | 0.37 | 0.36 | 0.23 | N.D. | 2.43 | |
| Styrene | 2% | <0.01 | 0.02 | N.D. | N.D. | 0.27 | |
|
| 95% | 0.11 | 0.10 | 0.08 | N.D. | 0.52 | |
|
| |||||||
| SC | Ethyl acetate | 53% | 0.07 | 0.11 | 0.03 | N.D. | 1.11 |
| Benzene | 100% | 0.38 | 0.25 | 0.33 | 0.04 | 2.11 | |
| Methyl isobutyl ketone | 1% | <0.01 | 0.01 | N.D. | N.D. | 0.12 | |
| Toluene | 100% | 0.68 | 0.60 | 0.52 | 0.01 | 5.02 | |
|
| 97% | 0.20 | 0.19 | 0.17 | N.D. | 1.34 | |
| Styrene | 0% | <0.01 | 0.01 | N.D. | N.D. | 0.12 | |
|
| 87% | 0.06 | 0.06 | 0.05 | N.D. | 0.36 | |
N.D.: not detected.
Statistical summaries of carbonyl compounds at different sites of the present study.
| Sites | Carbonyl compounds | Detection frequency | Mean (ppb) | S.D. (ppb) | Median (ppb) | Min (ppb) | Max (ppb) |
|---|---|---|---|---|---|---|---|
| YI | Formaldehyde | 96% | 7.40 | 5.74 | 4.81 | N.D. | 26.93 |
| Acetaldehyde | 96% | 2.75 | 2.02 | 2.24 | N.D. | 9.89 | |
| Propionaldehyde | 60% | 0.29 | 0.40 | 0.18 | N.D. | 2.67 | |
| Methyl ethyl ketone | 74% | 2.57 | 3.73 | 1.06 | N.D. | 15.92 | |
| Butyraldehyde | 5% | 0.06 | 0.34 | N.D. | N.D. | 2.67 | |
|
| 11% | 0.03 | 0.09 | N.D. | N.D. | 0.50 | |
|
| 31% | 0.11 | 0.22 | N.D. | N.D. | 0.95 | |
|
| |||||||
| YR | Formaldehyde | 99% | 8.06 | 6.27 | 5.88 | N.D. | 31.38 |
| Acetaldehyde | 97% | 3.43 | 3.05 | 2.10 | N.D. | 15.74 | |
| Propionaldehyde | 50% | 0.35 | 0.61 | 0.06 | N.D. | 2.97 | |
| Methyl ethyl ketone | 73% | 2.05 | 2.93 | 0.96 | N.D. | 13.73 | |
| Butyraldehyde | 29% | 0.56 | 1.25 | N.D. | N.D. | 6.08 | |
|
| 12% | 0.03 | 0.10 | N.D. | N.D. | 0.46 | |
|
| 26% | 0.05 | 0.11 | N.D. | N.D. | 0.48 | |
|
| |||||||
| GI | Formaldehyde | 99% | 5.99 | 4.55 | 4.89 | N.D. | 30.52 |
| Acetaldehyde | 99% | 1.97 | 1.12 | 1.85 | N.D. | 5.35 | |
| Propionaldehyde | 44% | 0.14 | 0.18 | N.D. | N.D. | 0.64 | |
| Methyl ethyl ketone | 91% | 2.74 | 3.12 | 2.04 | N.D. | 20.56 | |
| Butyraldehyde | 4% | 0.02 | 0.08 | N.D. | N.D. | 0.51 | |
|
| 8% | 0.02 | 0.06 | N.D. | N.D. | 0.39 | |
|
| 28% | 0.07 | 0.13 | N.D. | N.D. | 0.54 | |
|
| |||||||
| GR | Formaldehyde | 100% | 7.15 | 5.54 | 5.45 | 1.65 | 28.66 |
| Acetaldehyde | 100% | 2.23 | 1.68 | 1.86 | 0.13 | 12.44 | |
| Propionaldehyde | 34% | 0.17 | 0.47 | N.D. | N.D. | 3.92 | |
| Methyl ethyl ketone | 86% | 2.29 | 3.02 | 1.86 | N.D. | 22.34 | |
| Butyraldehyde | 1% | 0.01 | 0.05 | N.D. | N.D. | 0.44 | |
|
| 4% | 0.01 | 0.06 | N.D. | N.D. | 0.40 | |
|
| 11% | 0.03 | 0.08 | N.D. | N.D. | 0.37 | |
|
| |||||||
| SC | Formaldehyde | 98% | 6.52 | 4.84 | 5.30 | N.D. | 25.81 |
| Acetaldehyde | 98% | 2.54 | 2.87 | 1.48 | N.D. | 18.38 | |
| Propionaldehyde | 38% | 0.21 | 0.43 | N.D. | N.D. | 2.91 | |
| Methyl ethyl ketone | 78% | 2.05 | 2.11 | 1.75 | N.D. | 8.59 | |
| Butyraldehyde | 10% | 0.10 | 0.43 | N.D. | N.D. | 2.77 | |
|
| 5% | 0.03 | 0.15 | N.D. | N.D. | 0.84 | |
|
| 18% | 0.05 | 0.12 | N.D. | N.D. | 0.58 | |
N.D.: not detected.
Figure 3Cumulative probability of the distributions of the concentrations of VOC.
Figure 4Cumulative probability of distributions of the concentrations of carbonyl compounds.
Figure 5Seasonal variations of concentrations of VOC.
Figure 6Seasonal variations of the concentrations of carbonyl compounds.
Figure 7(a) Concentration and odor intensity of the odor compounds at YI site. (b) Concentration and odor intensity of the odor compounds at YR site. (c) Concentration and odor intensity of the odor compounds at GI site. (d) Concentration and odor intensity of the odor compounds at GR site. (e) Concentration and odor intensity of the odor compounds at SC site.
Comparison of the concentrations (ppb) of VOC reported in present method with other cities in the world.
| S. No. | City/country | Sampling period | Site characteristics |
| Analysis | BZ | TOL | XYLN | MIBK | EA | STR | T/B ratio | Reference |
|---|---|---|---|---|---|---|---|---|---|---|---|---|---|
| 1 | Pohang/Korea∗ | Jan, 2006–Feb, 2009 | Steel, Ferro-alloy industries | — | On-line TD/GC-FID | 0.12 | 0.18 | 0.13 | — | — | 0.34 | 1.50 |
[ |
| Residential | 0.78 | 2.50 | 0.66 | — | — | 0.14 | 3.21 | ||||||
|
| |||||||||||||
| 2 | Yokohoma/Japan | June 2007–Nov, 2008 | Petrochemical industries | 69 | GC-FID | 0.70~2.10 | 1.60~5.20 | 0.40~2.10 | — | 0.40~0.60 | — | — |
[ |
| Residential | 0.40~0.90 | 1.90~2.20 | 0.20~0.70 | — | 0.60 | — | — | ||||||
|
| |||||||||||||
| 3 | Tzouying/Taiwan | Oct-Nov, 2004 | Oil refinery | 24 | GC-MS | 1.6~2.5 | 24.5~42.00 | 1.5~2.10 | — | — | — | — | [ |
|
| |||||||||||||
| 4 | Kaohsiung/Taiwan | July and Oct, 2003 | Petrochemical industrial park (Rush hours) | — | GC-MS | 11.29 | 160.88 | 22.07 | — | — | 15.16 | 14.25 |
[ |
| Nonrush hours | 13.49 | 101.99 | 15.15 | — | — | — | 7.56 | ||||||
|
| |||||||||||||
| 5 | Southern Taiwan, Ping-Nan IP | July, 2003–Dec, 2004 | Iron and steel industries | 129 | GC-FID | 1.98 | 4.33 | 3.72 | — | — | — | 2.18 |
[ |
| Rem-Wu IP | Petrochemical and general manufacturing industries | 1.99 | 14.52 | 7.14 | — | — | — | 7.29 | |||||
| Naan-Zi IP | Petroleum and petrochemical industries | 2.17 | 5.41 | 4.95 | — | — | — | 2.49 | |||||
|
| |||||||||||||
| 6 | Shanghai/China | Jan, 2007–Mar, 2010 | Chemical and steel industries | 284 | GC-MS | 1.81 | 4.70 | 1.89 | — | 2.09 | 0.14 | 2.59 | [ |
|
| |||||||||||||
| 7 | Mumbai/India∗ | 2004 | Petrochemical, pharma, and plastic industries | — | TD/GC-MS | 0.62 | 1.47 | 0.02 | — | — | 0.03 | 2.37 | [ |
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| 8 | Mumbai/India∗ | May 2001–Apr, 2002 | Petrochemical industries | 24 | TD/GC-MS | 60.98 | 20.42 | 0.03 | — | — | — | 0.33 |
[ |
| Residential | 13.71 | 7.48 | 0.25 | — | — | — | 0.55 | ||||||
|
| |||||||||||||
| 9 | Dunkerque/France∗ | July–Sep, 2009 | Petrochemical, chemical, and steel industries | — | GC-FID | 0.12 | 0.31 | 0.19 | — | — | 0.03 | 2.58 | [ |
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| 10 | Dunkerque/France∗ | Jan, 2007 | Petrochemical, chemical, and steel industries | — | TD/GC-FID | 0.58 | 2.59 | 0.63 | — | — | — | 4.46 |
[ |
| June, 2007 | 0.47 | 0.54 | 0.18 | — | — | — | 1.14 | ||||||
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| 11 | Seoul/Korea | Feb–Jul, 2009 | Urban residential | 18 | GC-MS | 0.58 | 5.39 | 1.16 | — | — | 0.45 | 9.29 | [ |
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| 12 | Yeosu industrial/Korea | May, Aug, Oct 2008, Jan 2009 | Oil refinery and [petrochemical industries | 234 | TD/GC-MS | 3.65 | 3.25 | 3.08 | 0.11 | 0.39 | 0.25 | 0.89 | this study |
| Yeosu residential/Korea | Residential | 160 | TD/GC-MS | 1.07 | 1.61 | 0.46 | 0.01 | 0.11 | 0.15 | 1.50 | |||
| Gwangyang industrial/Korea | Steel industries | 239 | TD/GC-MS | 1.64 | 0.97 | 1.37 | 0.01 | 0.12 | 0.01 | 0.59 | |||
| Gwangyang residential/Korea | Residential | 199 | TD/GC-MS | 0.59 | 0.98 | 0.48 | <0.01 | 0.10 | <0.01 | 1.66 | |||
| Suncheon comparison/Korea | Residential | 240 | TD/GC-MS | 0.38 | 0.68 | 0.26 | <0.01 | 0.07 | <0.01 | 1.79 | |||
N: no. of data; TD: thermal desorption; BZ: benzene; TOL: toluene; XYLN: m, p, o-xylenes; STR: styrene; EA: ethyl acetate; STR: styrene; IP: industrial park.∗Concentration of VOC is reported by those authors in μg/m3 and in present table they are converted into ppb (at 15°C).
Comparison of the concentrations of carbonyl compounds reported in present method with other cities in the world.
| S. No. | City/country | Sampling period | Site characteristics |
| FRML | ACTL | PPNL | BTL | iVAL | nVAL | MEK |
| Reference |
|---|---|---|---|---|---|---|---|---|---|---|---|---|---|
| 1 | Kolkata/India | Site 1, summer | Mixed (res., traffic, and ind.) | — | 18.60 | 9.09 | 1.50 | 1.46 | — | — | — | 2.0 |
[ |
| Winter | 13.76 | 6.76 | 1.02 | 0.75 | — | — | — | 2.0 | |||||
| Site 2, summer | Mixed (res., traffic, and ind.) | 11.02 | 4.59 | 0.73 | 1.30 | — | — | — | 2.4 | ||||
| Winter | 9.92 | 4.98 | 0.95 | 0.74 | — | — | — | 2.0 | |||||
|
| |||||||||||||
| 2 | Guangzhou/China | July–Sep, 2003 | Residential | 5 | 10.88 | 5.83 | 1.11 | 0.66 | 0.23 | 0.25 | 1.9 |
[ | |
| Industrial | 5 | 11.07 | 3.96 | 0.55 | 0.29 | 0.08 | 0.62 | 2.8 | |||||
|
| |||||||||||||
| 3 | Guangzhou/China | 17–19, Nov–2005 | Residential and traffic site | 12 | 4.74 | 3.95 | 0.35 | 0.78 | 0.12 | 0.16 | 1.2 |
[ | |
| 30 Nov–2, Dec 2005 | Residential and traffic | 12 | 11.49 | 8.91 | 1.16 | 0.81 | 0.18 | 2.74 | 1.3 | ||||
|
| |||||||||||||
| 4 | Ansan, Shi Hung/Republic of Korea | Aug, 2004–Sep, 2005 | Industrial | — | 19.30 | 19.50 | 19.00 | 13.00 | 0.93 | 0.82 | 1.0 | [ | |
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| 5 | Gumi/Republic of Korea | Dec, 2003–Nov, 2004 | Industrial site 1 | 172 | 3.40 | 7.35 | 0.80 | 2.40 | 0.5 |
[ | |||
| 2004 | Industrial site 2 | 78 | 3.87 | 2.52 | 1.01 | 4.81 | 1.5 | ||||||
| 2004 | Industrial, site 3 | 77 | 3.86 | 4.22 | 1.04 | 3.32 | 0.9 | ||||||
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| 6 | Mexico city/Mexico | Mar,1998–Feb, 1999 | Mixed (res., com., and ind.) | 35 | 4.33 | 2.31 | 0.53 | 0.29 | 0.44 | 0.16 | 1.9 | [ | |
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| 7 | Rome/Italy | 2006 | Urban | — | 2.16 | 1.26 | 0.41 | 1.61 | 0.06 | 0.13 | 1.7 | [ | |
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| 8 | Kurkimaki/Finland | — | Residential | — | 0.37 | 0.36 | 0.05 | 0.03 | 1.0 | [ | |||
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| 9 | Roverdo | Nov-Dec, 2005 | Rural | — | — | 0.38 | 0.10 | 0.05 | 0.08 | — |
[ | ||
| Zurich/Switzerland | Nov-Dec, 2005 | Urban res. | — | — | 0.86 | 0.12 | 0.04 | 0.03 | — | ||||
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| 10 | Santiago/Chile | Nov-Dec, 2003 | Downtown | 40 | 3.90 | 3.00 | 0.46 | 3.30 | 0.11 | 1.3 | [ | ||
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| 11 | Yeosu industrial/Korea | May, Aug, Oct 2008, Jan 2009 | Oil refinery, petrochemical industries | 80 | 7.40 | 2.75 | 0.29 | 0.06 | 0.03 | 0.11 | 2.57 | 2.7 | This study |
| Yeosu residential/Korea | Residential | 78 | 8.06 | 3.43 | 0.35 | 0.56 | 0.03 | 0.05 | 2.05 | 2.3 | |||
| Gwangyang industrial/Korea | Steel industries | 79 | 5.99 | 1.97 | 0.14 | 0.02 | 0.02 | 0.07 | 2.74 | 3.0 | |||
| Gwangyang residential/Korea | Residential | 80 | 7.15 | 2.23 | 0.17 | 0.01 | 0.01 | 0.03 | 2.29 | 3.2 | |||
| Suncheon comparison/Korea | Residential | 80 | 6.52 | 2.54 | 0.21 | 0.10 | 0.03 | 0.05 | 2.05 | 2.6 | |||
| Sites | Compounds | Benzene | Ethyl acetate | MIBK | Toluene |
| Styrene |
|---|---|---|---|---|---|---|---|
| YI | Ethyl acetate | 0.053 | |||||
| MIBK | 0.317∗ | 0.059 | |||||
| Toluene | 0.545∗ | 0.070 | 0.581∗ | ||||
|
| 0.532∗ | 0.155∗ | 0.753∗ | 0.692∗ | |||
| Styrene | 0.278∗ | 0.051 | 0.267∗ | 0.408∗ | 0.396∗ | ||
|
| 0.410∗ | 0.084 | 0.773∗ | 0.644∗ | 0.857∗ | 0.430∗ | |
|
| |||||||
| YR | Ethyl acetate | 0.262∗ | |||||
| MIBK | 0.114 | 0.402∗ | |||||
| Toluene | 0.278∗ | 0.178∗ | 0.284∗ | ||||
|
| 0.380∗ | 0.601∗ | 0.475∗ | 0.212∗ | |||
| Styrene | 0.367∗ | 0.256∗ | 0.329∗ | 0.425∗ | 0.302∗ | ||
|
| 0.385∗ | 0.644∗ | 0.445∗ | 0.269∗ | 0.949∗ | 0.349∗ | |
|
| |||||||
| GI | Ethyl acetate | 0.027 | |||||
| MIBK | −0.016 | 0.220∗ | |||||
| Toluene | 0.413∗ | 0.187∗ | 0.391∗ | ||||
|
| 0.032 | −0.031 | 0.300∗ | 0.638∗ | |||
| Styrene | −0.006 | −0.011 | 0.327∗ | 0.450∗ | 0.454∗ | ||
|
| 0.027 | −0.028 | 0.293∗ | 0.646∗ | 0.986∗ | 0.458∗ | |
|
| |||||||
| GR | Ethyl acetate | 0.201∗ | |||||
| MIBK | 0.143∗ | 0.285∗ | |||||
| Toluene | 0.416∗ | 0.490∗ | 0.343∗ | ||||
|
| 0.466∗ | 0.449∗ | 0.329∗ | 0.677∗ | |||
| Styrene | 0.159∗ | 0.011 | −0.019 | 0.219∗ | 0.224∗ | ||
|
| 0.473∗ | 0.466∗ | 0.288∗ | 0.651∗ | 0.953∗ | 0.192∗ | |
|
| |||||||
| SC | Ethyl acetate | 0.271∗ | |||||
| MIBK | 0.159∗ | 0.193∗ | |||||
| Toluene | 0.645∗ | 0.217∗ | 0.230∗ | ||||
|
| 0.500∗ | 0.256∗ | 0.131∗ | 0.735∗ | |||
| Styrene | 0.158∗ | 0.024 | 0.706∗ | 0.241∗ | 0.117 | ||
|
| 0.511∗ | 0.310∗ | 0.190∗ | 0.718∗ | 0.978∗ | 0.151∗ | |
*Correlation coefficients are significant at a level of 0.05.
| Sites | Compounds | SO2 | PM10 | O3 | NO2 | CO | Temp. (°C) | Wind speed (m/s) |
|---|---|---|---|---|---|---|---|---|
| YI | Benzene | −0.074 | 0.130∗ | −0.294∗∗ | 0.253∗ | 0.156∗ | −0.144∗ | −0.214∗ |
| Ethyl acetate | −0.048 | 0.144∗ | 0.052 | 0.081 | −0.057 | 0.079 | −0.109 | |
| MIBK | 0.101 | 0.162∗ | −0.027 | 0.367∗ | −0.064 | 0.063 | −0.266∗ | |
| Toluene | 0.053 | 0.254∗ | −0.077 | 0.463∗ | 0.024 | 0.048 | −0.297∗ | |
|
| 0.030 | 0.235∗ | −0.121 | 0.377∗ | −0.038 | 0.063 | −0.297∗ | |
| Styrene | 0.196∗ | 0.188∗ | −0.239∗∗ | 0.199∗ | −0.022 | 0.223∗ | −0.253∗ | |
|
| 0.048 | 0.140∗ | −0.127 | 0.302∗ | −0.079 | 0.191∗ | −0.330∗ | |
|
| ||||||||
| YR | Benzene | 0.187∗ | 0.317∗ | −0.424∗ | 0.461∗ | 0.592∗ | −0.370∗ | 0.053 |
| Ethyl acetate | 0.412∗ | 0.341∗ | −0.370∗ | 0.462∗ | 0.290∗ | −0.060 | −0.289∗ | |
| MIBK | 0.333∗ | 0.133 | −0.207∗ | 0.280∗ | 0.081 | 0.022 | −0.063 | |
| Toluene | 0.013 | 0.141 | −0.220∗ | 0.217∗ | 0.166∗ | −0.087 | 0.098 | |
|
| 0.589∗ | 0.322∗ | −0.473∗ | 0.552∗ | 0.428∗ | 0.003 | −0.373∗ | |
| Styrene | −0.013 | 0.093 | −0.287∗ | 0.316∗ | 0.351∗ | −0.112 | −0.069 | |
|
| 0.516∗ | 0.323∗ | −0.468∗ | 0.542∗ | 0.373∗ | 0.011 | −0.362∗ | |
|
| ||||||||
| GI | Benzene | 0.586∗ | 0.367∗ | 0.098 | 0.385∗ | 0.070 | 0.213∗ | −0.069 |
| Ethyl acetate | 0.186∗ | 0.151∗ | 0.144∗ | 0.195∗ | 0.155∗ | 0.020 | −0.031 | |
| MIBK | 0.106 | 0.176∗ | −0.156∗ | 0.228∗ | 0.357∗ | −0.122 | −0.031 | |
| Toluene | 0.316∗ | 0.302∗ | −0.047 | 0.375∗ | 0.122 | 0.154∗ | −0.035 | |
|
| 0.019 | 0.057 | −0.076 | 0.061 | 0.105 | −0.057 | 0.027 | |
| Styrene | 0.063 | 0.123 | −0.078 | 0.154∗ | 0.164∗ | −0.047 | 0.011 | |
|
| 0.021 | 0.060 | −0.082 | 0.074 | 0.120 | −0.074 | 0.042 | |
|
| ||||||||
| GR | Benzene | 0.504∗ | 0.423∗ | −0.112 | 0.558∗ | 0.448∗ | −0.017 | −0.185∗ |
| Ethyl acetate | 0.311∗ | 0.334∗ | −0.105 | 0.384∗ | 0.249∗ | −0.048 | −0.206∗ | |
| MIBK | 0.265∗ | 0.173∗ | −0.141∗ | 0.275∗ | 0.241∗ | −0.056 | −0.060 | |
| Toluene | 0.521∗ | 0.360∗ | −0.137 | 0.566∗ | 0.480∗ | 0.016 | −0.315∗ | |
|
| 0.430∗ | 0.362∗ | −0.483∗ | 0.672∗ | 0.591∗ | −0.199∗ | −0.355∗ | |
| Styrene | 0.107 | 0.053 | −0.053 | 0.150∗ | 0.131 | −0.056 | −0.090 | |
|
| 0.384∗ | 0.402∗ | −0.517∗ | 0.699∗ | 0.584∗ | −0.192∗ | −0.369∗ | |
|
| ||||||||
| SC | Benzene | 0.545∗ | 0.512∗ | −0.086 | 0.430∗ | 0.426∗ | −0.108 | −0.080 |
| Ethyl acetate | 0.218∗ | 0.249∗ | 0.013 | 0.172∗ | 0.175∗ | −0.069 | −0.007 | |
| MIBK | 0.177∗ | 0.063 | −0.034 | 0.068 | 0.106 | −0.075 | −0.011 | |
| Toluene | 0.267∗ | 0.173∗ | −0.188∗ | 0.274∗ | 0.218∗ | −0.006 | −0.158∗ | |
|
| 0.117 | 0.129∗ | −0.262∗ | 0.325∗ | 0.126 | 0.190∗ | −0.367∗ | |
| Styrene | 0.082 | 0.061 | −0.020 | 0.046 | 0.118 | −0.056 | −0.010 | |
|
| 0.127∗ | 0.163∗ | −0.241∗ | 0.332∗ | 0.119 | 0.228∗ | −0.361∗ | |
*Correlation coefficients are significant at a level of 0.05.
| Sites | Compounds | FRML | ACTL | PPNL | MEK | BTL | iVAL |
|---|---|---|---|---|---|---|---|
| YI | ACTL | 0.838∗ | |||||
| PPNL | 0.356∗ | 0.455∗ | |||||
| MEK | 0.507∗ | 0.320∗ | −0.151 | ||||
| BTL | 0.144 | 0.274∗ | 0.164 | −0.061 | |||
| iVAL | 0.099 | 0.074 | 0.155 | 0.077 | −0.053 | ||
| VAL | 0.074 | 0.148 | 0.149 | 0.168 | −0.063 | −0.039 | |
|
| |||||||
| YR | ACTL | 0.821∗ | |||||
| PPNL | 0.638∗ | 0.796∗ | |||||
| MEK | 0.363∗ | 0.209 | 0.061 | ||||
| BTL | 0.287∗ | 0.205 | 0.096 | −0.014 | |||
| iVAL | 0.328∗ | 0.287∗ | 0.385∗ | 0.385∗ | −0.069 | ||
| VAL | 0.397∗ | 0.301∗ | 0.032 | −0.009 | 0.340∗ | 0.189 | |
|
| |||||||
| GI | ACTL | 0.428∗ | |||||
| PPNL | 0.266∗ | 0.485∗ | |||||
| MEK | 0.064 | 0.022 | −0.063 | ||||
| BTL | 0.439∗ | 0.293∗ | 0.041 | −0.081 | |||
| iVAL | 0.011 | 0.050 | 0.001 | 0.356∗ | 0.120 | ||
| VAL | 0.271∗ | 0.141 | 0.303∗ | 0.389∗ | −0.102 | 0.245∗ | |
|
| |||||||
| GR | ACTL | 0.584∗ | |||||
| PPNL | 0.452∗ | 0.697∗ | |||||
| MEK | 0.088 | 0.001 | −0.057 | ||||
| BTL | −0.028 | 0.004 | −0.040 | 0.020 | |||
| iVAL | 0.040 | 0.045 | −0.046 | 0.029 | −0.021 | ||
| VAL | 0.123 | 0.095 | 0.059 | 0.057 | −0.039 | 0.179 | |
|
| |||||||
| SC | ACTL | 0.271∗ | |||||
| PPNL | 0.120 | 0.713∗ | |||||
| MEK | 0.425∗ | 0.251∗ | −0.123 | ||||
| BTL | −0.066 | −0.113 | −0.091 | −0.171 | |||
| iVAL | −0.054 | 0.426∗ | 0.166 | 0.091 | −0.042 | ||
| VAL | 0.122 | −0.118 | 0.004 | −0.229∗ | 0.044 | −0.088 | |
*Correlation coefficients are significant at a level of 0.05.
FRML: formaldehyde; ACTL: acetaldehyde; PPNL: propionaldehyde; MEK: methyl ethyl ketone; BTL: butyraldehyde.
iVAL: i-valeraldehyde; VAL: n-valeraldehyde.
| Sites | Compounds | SO2 | PM10 | O3 | NO2 | CO | Temp (°C) | Wind speed (m/s) |
|---|---|---|---|---|---|---|---|---|
| YI | FRML | 0.225∗ | 0.298∗ | 0.532∗ | 0.016 | −0.175 | 0.276∗ | −0.160 |
| ACTL | 0.448∗ | 0.365∗ | 0.279∗ | 0.230∗ | 0.093 | 0.021 | −0.072 | |
| PPNL | 0.345∗ | 0.076 | 0.053 | 0.168 | 0.126 | 0.051 | −0.074 | |
| MEK | −0.089 | 0.139 | 0.237∗ | −0.023 | −0.176 | 0.134 | −0.267∗ | |
| BTL | 0.575∗ | 0.167 | 0.130 | −0.019 | −0.007 | 0.014 | 0.236∗ | |
| iVAL | −0.016 | 0.014 | 0.275∗ | −0.125 | −0.019 | 0.090 | 0.046 | |
| VAL | −0.012 | 0.099 | −0.049 | 0.072 | 0.110 | −0.239∗ | 0.049 | |
|
| ||||||||
| YR | FRML | 0.096 | 0.509∗ | 0.115 | 0.498∗ | 0.185 | 0.151 | −0.246∗ |
| ACTL | 0.143 | 0.581∗ | −0.112 | 0.714∗ | 0.402∗ | −0.102 | −0.247∗ | |
| PPNL | 0.084 | 0.337∗ | −0.099 | 0.497∗ | 0.275∗ | −0.079 | −0.251∗ | |
| MEK | 0.162 | 0.169 | −0.221 | 0.086 | 0.100 | 0.004 | −0.097 | |
| BTL | −0.105 | 0.227∗ | 0.144 | 0.100 | −0.038 | 0.101 | 0.220 | |
| iVAL | 0.033 | 0.062 | −0.157 | 0.090 | 0.084 | 0.055 | −0.173 | |
| VAL | 0.035 | 0.297∗ | 0.107 | 0.209 | 0.049 | 0.251∗ | −0.172 | |
|
| ||||||||
| GI | FRML | 0.033 | 0.118 | 0.279∗ | 0.126 | −0.049 | 0.362∗ | −0.127 |
| ACTL | 0.261∗ | 0.410∗ | 0.058 | 0.525∗ | 0.332∗ | 0.249∗ | −0.303∗ | |
| PPNL | 0.139 | 0.091 | 0.194 | 0.169 | 0.026 | 0.528∗∗ | 0.000 | |
| MEK | −0.247∗ | −0.062 | −0.195 | −0.195 | −0.073 | 0.132 | −0.030 | |
| BTL | 0.039 | 0.051 | 0.155 | 0.176 | −0.049 | 0.116 | −0.041 | |
| iVAL | −0.063 | 0.119 | −0.028 | 0.038 | −0.004 | 0.066 | −0.087 | |
| VAL | −0.163 | 0.039 | −0.015 | −0.128 | −0.150 | 0.312∗ | 0.021 | |
|
| ||||||||
| GR | FRML | −0.004 | 0.161 | 0.180 | 0.100 | 0.027 | 0.248∗ | −0.197 |
| ACTL | 0.258∗ | 0.505∗ | 0.044 | 0.478∗ | 0.360∗ | 0.114 | −0.392∗ | |
| PPNL | 0.004 | 0.072 | 0.141 | 0.069 | 0.007 | 0.200 | −0.174 | |
| MEK | 0.042 | 0.067 | −0.218 | 0.072 | 0.084 | 0.056 | −0.079 | |
| BTL | −0.081 | −0.021 | −0.048 | −0.096 | −0.072 | −0.024 | −0.064 | |
| iVAL | 0.052 | 0.205 | 0.089 | 0.095 | −0.004 | 0.129 | −0.072 | |
| VAL | 0.075 | 0.035 | 0.110 | −0.037 | 0.057 | 0.329∗ | −0.072 | |
|
| ||||||||
| SC | FRML | 0.347∗ | 0.414∗ | 0.015 | 0.460∗ | 0.377∗ | 0.138 | −0.378∗ |
| ACTL | 0.295∗ | 0.327∗ | −0.109 | 0.466∗ | 0.348∗ | −0.057 | −0.405∗ | |
| PPNL | 0.292∗ | 0.223∗ | −0.133 | 0.263∗ | 0.155 | −0.127 | −0.244∗ | |
| MEK | 0.267∗ | 0.465∗ | −0.063 | 0.488∗ | 0.590∗ | −0.231∗ | −0.277∗ | |
| BTL | −0.135 | −0.061 | 0.075 | −0.138 | −0.155 | 0.116 | 0.097 | |
| iVAL | 0.058 | 0.025 | −0.283∗ | 0.252∗ | 0.300∗ | −0.175 | −0.237∗ | |
| VAL | −0.162 | −0.120 | 0.189 | −0.196 | −0.198 | 0.396∗ | 0.026 | |
*Correlation coefficients are significant at a level of 0.05.
FRML: formaldehyde; ACTL: acetaldehyde; PPNL: propionaldehyde; MEK: methyl ethyl ketone; BTL: butyraldehyde.
iVAL: i-valeraldehyde; VAL: n-valeraldehyde.