| Literature DB >> 35919573 |
Tabu Mungia Magollah1, Hyo-Rim Kim1, Ji-Yun Ko1, Su-Yeon Park1, Seo-Yeon Kwon1, Yu-Kyeong Kim1, Ji-Hyo Lee1, Yong-Soo Seo2, Ji-Young Yang1, Yang-Bong Lee1.
Abstract
Ethyl carbamate (EC) is a known carcinogen, and therefore its intake is regulated internationally. The objectives of this study were to compare the EC recovery yields under different liquid-liquid extraction (LLE) conditions and to investigate the optimum conditions of the aqueous two-phase system (ATPS) for EC extraction. Our results showed that for the LLE method, addition of 15% NaCl improved the EC yield by 15%, and dichloromethane as the extraction solvent showed a slightly higher yield (about 5%) than chloroform. However, there was little difference in the yield when mixing was performed using an ultrasonic bath compared to a vortex mixer. Using response surface methodology with central composite design to analyze the ATPS results, optimal extraction was found to occur at 21.5°C for 2.8 h in the sample containing 70% alcohol and 15% phosphate, showing a recovery yield of 75.64%. This information can be applied to alcoholic beverages and other fermented food products to analyze EC with better extraction methods, depending on the types of food.Entities:
Keywords: aqueous two-phase system; central composite design; ethyl carbamate; liquid-liquid extraction; response surface methodology
Year: 2022 PMID: 35919573 PMCID: PMC9309073 DOI: 10.3746/pnf.2022.27.2.234
Source DB: PubMed Journal: Prev Nutr Food Sci ISSN: 2287-1098
Matrix and values of independent variables of central composite design used for optimization of ethyl carbamate extraction
| Run no. | X1 | X2 | X3 | X4 | Response |
|---|---|---|---|---|---|
| 1 | 70 (+1) | 15 (+1) | 15 (—1) | 5 (+1) | 80.71 |
| 2 | 55 (0) | 10 (0) | 22.5 (0) | 3.5 (0) | 74.09 |
| 3 | 55 (0) | 10 (0) | 37.5 (+2) | 3.5 (0) | 54.28 |
| 4 | 40 (—1) | 15 (+1) | 15 (—1) | 2 (—1) | 60.36 |
| 5 | 55 (0) | 10 (0) | 22.5 (0) | 3.5 (0) | 60.00 |
| 6 | 40 (—1) | 5 (—1) | 15 (—1) | 5 (+1) | 61.06 |
| 7 | 40 (—1) | 5 (—1) | 30 (+1) | 2 (—1) | 50.94 |
| 8 | 55 (0) | 0 (—2) | 22.5 (0) | 3.5 (0) | 57.93 |
| 9 | 70 (+1) | 5 (—1) | 30 (+1) | 5 (+1) | 61.57 |
| 10 | 70 (+1) | 15 (+1) | 30 (+1) | 2 (—1) | 62.56 |
| 11 | 70 (+1) | 5 (—1) | 15 (—1) | 2 (—1) | 61.13 |
| 12 | 85 (+2) | 10 (0) | 22.5 (0) | 3.5 (0) | 66.94 |
| 13 | 70 (+1) | 15 (+1) | 15 (—1) | 2 (—1) | 67.82 |
| 14 | 40 (—1) | 15 (+1) | 30 (+1) | 5 (+1) | 54.66 |
| 15 | 55 (0) | 10 (0) | 22.5 (0) | 0.5 (—2) | 62.63 |
| 16 | 70 (+1) | 15 (+1) | 30 (+1) | 5 (+1) | 68.16 |
| 17 | 55 (0) | 20 (+2) | 22.5 (0) | 3.5 (0) | 73.74 |
| 18 | 55 (0) | 10 (0) | 7.5 (—2) | 3.5 (0) | 59.28 |
| 19 | 70 (+1) | 5 (—1) | 15 (—1) | 5 (+1) | 81.93 |
| 20 | 70 (+1) | 5 (—1) | 30 (+1) | 2 (—1) | 67.93 |
| 21 | 55 (0) | 10 (0) | 22.5 (0) | 6.5 (+2) | 49.09 |
| 22 | 40 (—1) | 5 (—1) | 30 (+1) | 5 (+1) | 59.75 |
| 23 | 55 (0) | 10 (0) | 22.5 (0) | 3.5 (0) | 75.90 |
| 24 | 40 (—1) | 15 (+1) | 30 (+1) | 2 (—1) | 66.74 |
| 25 | 25 (—2) | 10 (0) | 22.5 (0) | 3.5 (0) | 54.67 |
| 26 | 40 (—1) | 5 (—1) | 15 (—1) | 2 (—1) | 46.07 |
| 27 | 40 (—1) | 15 (+1) | 15 (—1) | 5 (+1) | 46.39 |
X1, alcohol concentration (%); X2, K2HPO4 concentration (%); X3, extraction temperature (°C); X4, extraction time (h); response, recovery yield (%).
Comparison of extraction methods for analyzing ethyl carbamate in alcoholic beverage
| Variable | SPE | LLE | ATPS | SPME |
|---|---|---|---|---|
| Sample/solvent quantity | 10 g/80 mL | 5 mL/5 mL | 15 mL | 20 μL/300 μL acetone, 60 μL TFA |
| Absorbent | Chem Elut | − | − | Fiber |
| Mixer | − | Vortex mixer | Vortex mixer | − |
| Concentration method | Water bath, rotary evaporator | − | − | − |
| Centrifugation setting | − | 4°C, 10,000 rpm, 10 min | 3,600 rpm, 5 min | − |
| Extraction time | 33.3 min | 15.6 min | 57 min | 18 min |
| Reference |
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SPE, solid phase extraction; LLE, liquid-liquid extraction; ATPS, aqueous two-phase system; SPME, solid phase micro-extraction; TFA, trifluoroacetic acid.
Comparison of recovery yields in several extraction methods for isolating ethyl carbamate
| Method | I | II | III | IV | V | VI | VII | VIII | IX (ATPS) |
|---|---|---|---|---|---|---|---|---|---|
| Treatment | EC+BC | EC+BC | EC+BC | EC+BC | EC+BC+NaCl | EC+BC+NaCl | EC+BC+NaCl | EC+BC+NaCl | EC+BC+K2HPO4 |
| Solvent | DCM | DCM | CF | CF | DCM | DCM | CF | CF | ‒ |
| Mixing | Vortex | Ultrasonic | Vortex | Ultrasonic | Vortex | Ultrasonic | Vortex | Ultrasonic | Vortex |
| Yield | 43±5 | 42±3 | 47±4 | 43±3 | 53±8 | 57±2 | 62±11 | 58±6 | 90±4 |
Values are presented as mean±standard deviation for triplicate.
Both concentrations of NaCl and K2HPO4 are 15%. A vortex is used for 10 s and ultrasonic is operated for 30 min in a bath.
ATPS, aqueous two-phase system; EC, ethyl carbamate; BC, butyl carbamate; DCM, dichloromethane; CF, chloroform.
Fig. 1The main effect of factors on extraction yield using Minitab.
Results of statistical analysis a regression model of central composite design on extraction yield from the model system for Maesil wine
| Source | Yield |
|---|---|
| Linear | 0.005 |
| X1 | <0.001 |
| X2 | <0.001 |
| X3 | 0.193 |
| X4 | 0.672 |
| Quadratic | 0.002 |
| X1X2 | 0.596 |
| X1X3 | 0.143 |
| X1X4 | 0.568 |
| X2X3 | 0.690 |
| X2X4 | 0.003 |
| X3X4 | 0.013 |
| X12 | 0.005 |
| X22 | 0.035 |
| X32 | <0.001 |
| X42 | 0.001 |
| Residual | |
| Lack of fit | 0.577 |
| Fitness of model (R2) | 0.920 |
Statistically significant at *P<0.05.
Fig. 2Response surface plot showing the effects of alcohol concentration (X1), K2HPO4 concentration (X2), extraction temperature (X3), and time (X4) on extraction yield (Y).
Optimum conditions and comparison of predicted and observed values for verification
| Response | Optimum extraction condition | ||||||
|---|---|---|---|---|---|---|---|
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| Alcohol concentration (%) | K2HPO4 concentration (%) | Extraction temperature (°C) | Extraction time (h) | Predicted | Observed | Error (%) | |
| Recovery yield (%) | 69 | 15 | 21.5 | 2.8 | 75.6 | 78.2±0.2 | 3.4 |
Values are presented as number only or mean±standard deviation.