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Correction

Correction: Gómez-Cruz et al. Valorisation of Exhausted Olive Pomace by an Eco-Friendly Solvent Extraction Process of Natural Antioxidants. Antioxidants 2020, 9, 1010

1
Centre for Advanced Studies in Earth Sciences, Energy and Environment (CEACTEMA), Campus Las Lagunillas, Universidad de Jaén, 23071 Jaén, Spain
2
Department of Chemical, Environmental and Materials Engineering, Campus Las Lagunillas, Universidad de Jaén, 23071 Jaén, Spain
3
Department of Chemical Engineering, Faculty of Science, University of Vigo (Campus Ourense), As Lagoas, 32004 Ourense, Spain
*
Author to whom correspondence should be addressed.
Antioxidants 2021, 10(6), 948; https://doi.org/10.3390/antiox10060948
Submission received: 11 May 2021 / Revised: 25 May 2021 / Accepted: 25 May 2021 / Published: 11 June 2021
The author wishes to make the following correction to this paper [1].
In the original article, there was a mistake in the calculation of the antioxidant activity measured by ABTS assay for runs of the experimental design (Table 3, Table 4 and Table 5 and Figure 2b). All values of ABTS corresponding to the experimental design of the aqueous extraction have been corrected by multiplying by 0.626.
The authors apologise for any inconvenience caused and state that the scientific conclusions are unaffected. The original article has been updated.

Reference

  1. Gómez-Cruz, I.; Cara, C.; Romero, I.; Castro, E.; Gullón, B. Valorisation of Exhausted Olive Pomace by an Eco-Friendly Solvent Extraction Process of Natural Antioxidants. Antioxidants 2020, 9, 1010. [Google Scholar] [CrossRef] [PubMed]
Figure 2. Response surfaces for (a) DPPH (b) ABTS, and (c) ferric reducing power (FRAP) assays as a function of temperature and solid loading (extraction time: 60 min).
Figure 2. Response surfaces for (a) DPPH (b) ABTS, and (c) ferric reducing power (FRAP) assays as a function of temperature and solid loading (extraction time: 60 min).
Antioxidants 10 00948 g001
Table 3. Box–Benhken experimental design in terms of actual and coded factors applied to the aqueous extraction conditions and experimental values of the response variables.
Table 3. Box–Benhken experimental design in terms of actual and coded factors applied to the aqueous extraction conditions and experimental values of the response variables.
RunTtBYield
(%)
Phenolic Concentration
(g/L)
TPC
(mg GAE/g EOP)
TFC
(mg RE/g EOP)
DPPH
(mg TE/g EOP)
ABTS
(mg TE/g EOP)
FRAP
(mg TE/g EOP)
25 (−1)60 (0)25 (1)28.76.728.882.725.861.6328.7
255 (0)60 (0)15 (0)30.64.632.9100.134.566.1934.8
355 (0)30 (−1)25 (1)28.76.025.878.526.358.4029.8
485 (1)90 (1)15 (0)34.55.237.0106.642.189.4043.7
555 (0)60 (0)15 (0)32.14.834.397.735.771.4438.1
685 (1)60 (0)25 (1)33.67.431.794.626.673.8839.4
785 (1)30 (−1)15 (0)32.04.733.4104.539.777.8740.9
855 (0)60 (0)15 (0)32.94.935.2113.439.773.8840.7
925 (−1)60 (0)5 (−1)27.71.438.0148.744.172.4437.6
1055 (0)90 (1)25 (1)31.97.130.686.526.465.6929.1
1125 (−1)30 (−1)15 (0)26.93.625.890.731.458.4425.1
1255 (0)90 (1)5 (−1)35.62.043.6155.646.481.3141.6
1355 (0)30 (−1)5 (−1)30.61.941.2153.446.578.3843.7
1455 (0)60 (0)15 (0)32.14.934.9104.236.974.8135.1
1585 (1)60 (0)5 (−1)33.21.941.2157.649.287.8142.3
1625 (−1)90 (1)15 (0)29.94.229.795.633.667.6930.9
1755 (0)60 (0)15 (0)33.04.935.0102.737.883.0636.5
T: temperature (°C); t: extraction time (min); B: solid loading (%, w/v).
Table 4. Mathematical models and coefficients for the responses using coded values.
Table 4. Mathematical models and coefficients for the responses using coded values.
Dependent VariablesModelsCV (%)R2Adjusted R2F-ValueLack of Fit
(p-Values)
Extraction yield (%)31.9 + 2.52∙T + 1.67∙t − 1.07∙T2 (Equation (1))2.630.9020.87533.710.762
Phenolic concentration
(g GAE/L)
4.50 + 0.41∙T + 0.28∙t + 2.50∙B (Equation (2))7.740.9700.964143.300.020
TPC
(mg GAE/g EOP)
34.83 + 4.03∙T + 1.83∙t − 7.12∙B + 2.35∙T∙B − 3.03∙T2 (Equation (3))2.760.9790.96783.440.486
TFC
(mg RE/g EOP)
100.26 + 5.69∙T − 32.95∙B + 20.61∙B2 (Equation (4))2.040.9940.993644.610.815
DPPH
(mg TE/g EOP)
36.45 + 2.82∙T − 10.13∙B (Equation (5))4.270.9660.960182.270.497
ABTS
(mg TE/g EOP)
73.15 + 8.67∙T + 3.87∙t − 7.49∙B (Equation (6))3.220.8330.79119.900.9413
FRAP
(mg TE/g EOP)
37.08 + 5.40∙T − 5.50∙B (Equation (7))5.690.8610.83837.270.743
Table 5. Real and predicted values by the mathematical model for the responses.
Table 5. Real and predicted values by the mathematical model for the responses.
Predicted ValuesExperimental Values
Extraction yield (%)35.040.9 ± 0.54
Phenolic concentration
(g GAE/L)
3.74.5 ± 0.03
TPC (mg GAE/g EOP)40.544.5 ± 0.25
TFC (mg RE/g EOP)132.4114.9 ± 0.39
DPPH (mg TE/g EOP)45.236.1 ± 0.36
ABTS (mg TE/g EOP)89.595.4 ± 0.72
FRAP (mg TE/g EOP)45.747.6 ± 0.24
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Gómez-Cruz, I.; Cara, C.; Romero, I.; Castro, E.; Gullón, B. Correction: Gómez-Cruz et al. Valorisation of Exhausted Olive Pomace by an Eco-Friendly Solvent Extraction Process of Natural Antioxidants. Antioxidants 2020, 9, 1010. Antioxidants 2021, 10, 948. https://doi.org/10.3390/antiox10060948

AMA Style

Gómez-Cruz I, Cara C, Romero I, Castro E, Gullón B. Correction: Gómez-Cruz et al. Valorisation of Exhausted Olive Pomace by an Eco-Friendly Solvent Extraction Process of Natural Antioxidants. Antioxidants 2020, 9, 1010. Antioxidants. 2021; 10(6):948. https://doi.org/10.3390/antiox10060948

Chicago/Turabian Style

Gómez-Cruz, Irene, Cristóbal Cara, Inmaculada Romero, Eulogio Castro, and Beatriz Gullón. 2021. "Correction: Gómez-Cruz et al. Valorisation of Exhausted Olive Pomace by an Eco-Friendly Solvent Extraction Process of Natural Antioxidants. Antioxidants 2020, 9, 1010" Antioxidants 10, no. 6: 948. https://doi.org/10.3390/antiox10060948

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