| Literature DB >> 27818736 |
Ki-Woong Kim1, Yong Lim Won1, Dong Jin Park1, Young Sun Kim1, Eun Sil Jin2, Sung Kwang Lee2.
Abstract
We determined the toxicity of mixtures of ethyl acetate (EA), isopropyl alcohol (IPA), methyl ethyl ketone (MEK), toluene (TOL) and xylene (XYL) with half-maximal effective concentration (EC50) values obtained using human hepatocytes cells. According to these data, quantitative property-activity relationships (QPAR) models were successfully proposed to predict the toxicity of mixtures by multiple linear regressions (MLR). The leave-one-out cross validation method was used to find the best subsets of descriptors in the learning methods. Significant differences in physico-chemical properties such as boiling point (BP), specific gravity (SG), Reid vapor pressure (rVP) and flash point (FP) were observed between the single substances and the mixtures. The EC50 of the mixture of EA and IPA was significantly lower than that of contained TOL and XYL. The mixture toxicity was related to the mixing ratio of MEK, TOL and XYL (MLR equation EC50 = 3.3081 - 2.5018 × TOL - 3.2595 × XYL - 12.6596 × MEK × XYL), as well as to BP, SG, VP and FP (MLR equation EC50 = 1.3424 + 6.2250 × FP - 7.1198 × SG × FP - 0.03013 × rVP × FP). These results suggest that QPAR-based models could accurately predict the toxicity of polar and nonpolar mixtures used in rotogravure printing industries.Entities:
Keywords: Chemical mixtures; Quantitative property-activity relationship; Rotogravure printing industries; Toxicity
Year: 2016 PMID: 27818736 PMCID: PMC5080860 DOI: 10.5487/TR.2016.32.4.337
Source DB: PubMed Journal: Toxicol Res ISSN: 1976-8257
Classification of experimental groups and mixing ratio of chemicals
| Experimental groups | Mixing ratio (vol/vol) |
|---|---|
| Single | |
| Ethyl acetate (EA) | |
| Isopropyl alcohol (IPA) | |
| Methyl ethyl ketone (MEK) | |
| Toluene (TOL) | |
| Xylene (XYL) | |
|
| |
| Mixtures | |
| MEK + EA (G1) | 9 : 1 |
| MEK + IPA (G2) | 9 : 1 |
| MEK + EA + IPA (G3) | 8 : 1 : 1 |
| EA + IPA + MEK + TOL (G4) | 3 : 1 : 1 : 5 |
| EA + IPA + MEK + XYL (G5) | 3 : 1 : 1 : 5 |
| IPA + MEK + TOL (G6) | 1 : 1 : 5 |
| IPA + MEK + XYL (G7) | 1 : 1 : 5 |
| EA + IPA + MEK + TOL + XYL (G8) | 3 : 1 : 1 : 2.5 : 2.5 |
Letters in parenthesis represents the groups (G1–G8).
Identification and ambient levels of chemicals
| Companies | Mean concentrations of ambient chemicals (ppm) | ||||
|---|---|---|---|---|---|
|
| |||||
| EA | IPA | MEK | Toluene | Xylene | |
| Rotogravure paint manufacturing companies (2 companies) | |||||
| A | 3.4 ± 5.1 | 0.00 | 0.00 | 12.7 ± 16.1 | 12.6 ± 19.1 |
| B | 20.6 ± 19.9 | 3.2 ± 2.6 | 20.6 ± 33.1 | 26.5 ± 32.2 | 21.5 ± 21.8 |
|
| |||||
| Rotogravure printing companies (3 companies) | |||||
| C | 210.4 ± 51.1 | 0.00 | 81.9 ± 24.7 | 77.6 ± 28.7 | 0.00 |
| D | 218.1 ± 291.9 | 20.9 ± 51.1 | 219.4 ± 307.4 | 38.9 ± 55.7 | 0.7 ± 2.1 |
| E | 140.8 ± 52.8 | 4.7 ± 2.2 | 178.7 ± 69.1 | 0.00 | 3.7 ± 2.4 |
|
| |||||
| Total | 132.1 ± 170.5 | 7.2 ± 26.5 | 125.8 ± 179.1 | 26.8 ± 41.5 | 6.6 ± 13.6 |
|
| |||||
| TWA | 400 | 200 | 200 | 50 | 100 |
EA, ethyl acetate; IPA, isopropyl alcohol; MEK, methyl ethyl ketone; TWA, time weighted average.
Results of the physico-chemical properties
| Experimental groups | Physico-chemical properties | |||
|---|---|---|---|---|
|
| ||||
| BP (°C) | SG (g/mL) | rVP (kPa) | FP (°C) | |
| Ethyl acetate (EA) | 77.0 | 0.90 | 22.5 | −4.0 |
| Isopropyl alcohol (IPA) | 83.0 | 0.79 | 12.1 | 11.7 |
| Methyl ethyl ketone (MEK) | 80.0 | 0.80 | 21.6 | −9.0 |
| Toluene (TOL) | 111.0 | 0.86 | 7.0 | 4.0 |
|
| ||||
| Xylene (XYL) | 139.2 | 0.87 | 2.3 | 29.0 |
| MEK + EA (G1) | 78.7 ± 0.1 | 0.8181 ± 0.0008 | 21.23 ± 0.21 | −7.37 ± 0.29 |
| MEK + IPA (G2) | 78.5 ± 0.2 | 0.8015 ± 0.0001 | 21.60 ± 0.36 | −6.85 ± 0.29 |
| MEK + EA + IPA (G3) | 77.6 ± 0.4 | 0.8110 ± 0.0001 | 22.47 ± 0.38 | −6.53 ± 0.29 |
| EA + IPA + MEK + TOL (G4) | 83.9 ± 0.3 | 0.8615 ± 0.0001 | 18.00 ± 0.44 | −2.15 ± 0.50 |
| EA + IPA + MEK + XYL (G5) | 88.1 ± 0.3 | 0.8613 ± 0.0001 | 14.63 ± 0.12 | 0.43 ± 0.01 |
| IPA + MEK+TOL (G6) | 87.9 ± 0.1 | 0.8466 ± 0.0001 | 15.93 ± 0.15 | −0.57 ± 0.50 |
| IPA + MEK + XYL (G7) | 94.4 ± 0.2 | 0.8454 ± 0.0001 | 11.77 ± 0.12 | 6.31 ± 0.44 |
| EA + IPA + MEK + TOL + XYL (G8) | 86.1 ± 0.2 | 0.8610 ± 0.0001 | 16.20 ± 0.20 | −1.01 ± 0.25 |
|
| ||||
| χ2 (Kuskal Wallis test) | 22.375 | 22.683 | 22.426 | 22.406 |
| 0.01 | 0.01 | 0.01 | 0.01 | |
BP, boiling point; SG, specific gravity; rVP, Reid vapor pressure; FP, flash point.
Letters in parenthesis represents the groups (G1–G8).
Fig. 1EC50 (HepG2) values. EA, ethyl acetate; IPA, isopropyl alcohol; MEK, methyl ethyl ketone; G1, MEK + EA; G2, MEK + IPA; G3, MEK + EA + IPA; G4, EA + IPA + MEK + Toluene; G5, EA + IPA + MEK + Xylene; G6, IPA + MEK + Toluene; G7, IPA + MEK + Xylene; G8, EA + IPA + MEK + Toluene + Xylene.
QPAR model according to chemical mixing ratio by linear regression equation
| Solvent groups | Training | LOO CV | Linear regression equation | |
|---|---|---|---|---|
|
| ||||
| R2 | RMSE | Q2 | ||
| MEK, XYL | 0.4487 | 1.1305 | 0.0300 | y = 2.6437 + 0.0293 * MEK − 2.9631 * XYL |
| TOL, XYL | 0.7385 | 0.7786 | 0.6006 | y = 3.2074 − 2.4922 * TOL − 3.6719 * XYL |
| EA, TOL, XYL | 0.7980 | 0.7214 | 0.4725 | y = 2.9383 + 1.2337 * EA − 2.2903 * TOL − 3.4700 * XYL |
| MEK, TOL, XYL | 0.8502 | 0.6211 | 0.6053 | y = 4.0349 − 1.4681 * MEK − 3.4798 * TOL − 4.6595 * XYL |
| TOL, XYL, MEK * XYL | 0.7870 | 0.7408 | 0.7197 | y = 3.3081 − 2.5018 * TOL − 3.2595 * XYL − 12.6596 * MEK * XYL |
| MEK, TOL, XYL, MEK * XYL | 0.9114 | 0.5006 | 0.6678 | y = 4.1971 − 1.5544 * MEK − 3.5487 * TOL − 4.2526 * XYL − 14.2728 * MEK * XYL |
| EA, MEK, TOL, XYL | 0.8560 | 0.6459 | 0.3670 | y = 3.8154 + 0.4561 * EA − 1.2552 * MEK − 3.2620 * TOL − 4.4416 * XYL |
EA, ethyl acetate; IPA, isopropyl alcohol; MEK, methyl ethyl ketone; TOL, toluene; XYL, xylene; LOO CV, leave-one-out cross-validation; R2 and Q2, coefficient; RMSE, root mean square error.
QPAR model according to physico-chemical properties by linear regression equation
| Physico-chemical properties | Training | LOO CV | Linear regression equation | |
|---|---|---|---|---|
|
| ||||
| R2 | RMSE | Q2 | ||
| BP | 0.4811 | 1.0457 | 0.2215 | y = 7.0812 − 0.05513 * BP |
| rVP | 0.4185 | 1.1070 | 0.2654 | y = −0.1222 + 0.1419 * rVP |
| BP, FP | 0.5915 | 0.9731 | 0.4664 | y = 11.0604 − 0.1006 * BP + 0.08954 * FP |
| rVP, FP | 0.5434 | 1.0288 | 0.4570 | y = −2.8460 + 0.3052 * rVP + 0.1116 * FP |
| BP, rVP, FP | 0.6658 | 0.9277 | 0.1462 | y = 5.3946 − 0.06978 * BP + 0.1732 * rVP + 0.1393 * FP |
| BP * SG, BP * FP | 0.5950 | 0.9687 | 0.3622 | y = 10.4646 − 0.1127 * BP * SG = 0.0007994 * BP * FP |
| BP, SG * FP | 0.5910 | 0.9734 | 0.4680 | y = 11.3045 − 0.1034 * BP + 0.1104 * SG * FP |
| FP, SG * FP, rVP * FP | 0.9479 | 0.3664 | 0.5932 | y = 1.3424 + 6.2250 * FP − 7.1198 * SG * FP − 0.03013 * rVP * FP |
| SG, FP, SG * FP, rVP * FP | 0.9623 | 0.3303 | 0.5381 | y = 5.7976 − 5.2754 * SG + 6.1237 * FP − 7.0023 * SG * FP − 0.02938 * rVP * FP |
BP, boiling point; FP, flash point; rVP, Reid vapor pressure; SG, specific gravity; LOO CV, leave-one-out cross-validation; R2 and Q2, coefficient; RMSE, root mean square error.