| Literature DB >> 35531543 |
Aziz Homayouni Rad1,2, Haniyeh Rasouli Pirouzian1, Nevzat Konar3, Omer Said Toker4, Derya Genc Polat5.
Abstract
Sucrose-free milk chocolates containing different types of bulk (isomalt, xylitol and maltitol) and high intensity (Stevia) sweeteners were produced by using a ball mill. The main quality characteristics of the formulated chocolates were evaluated and compared with those of the conventional sample containing sucrose. The Casson model was the best fitting model for the rheological data. Casson viscosity and Casson yield stress were significantly affected by the type of bulking agent in chocolates formulated with xylitol (p < 0.05). However xylitol notably improved the overall acceptability according to the sensory analysis results. Chocolates containing the sucrose replacers demonstrated lower T onset values and higher enthalpy than the control sample. Sucrose-free chocolates illustrated a higher degree of particle agglomeration. Bulk sweeteners meanwhile seem to have high potential for milk chocolate production with low calorie values by using the ball mill technique. Industrial applications: the production of sucrose-free chocolates with conventional methods requires a lot of time and energy. Recently, using alternative methods for chocolate production has been raising interest in many small industries. This study proposed a ball mill method for the preparation of sucrose-free milk chocolates with physiochemical properties almost ranging in the standard limit defined for chocolate. Although using the ball mill method presents a more cost-effective technique for chocolate production and provides shorter processing times for small chocolate industries, it seems to be less efficient in evaporating moisture than the conventional processing. Challenges are still ahead for upgrading this alternative technique to be efficient in evaporating more moisture during operation ending in a high quality product. This journal is © The Royal Society of Chemistry.Entities:
Year: 2019 PMID: 35531543 PMCID: PMC9071936 DOI: 10.1039/c9ra04486h
Source DB: PubMed Journal: RSC Adv ISSN: 2046-2069 Impact factor: 4.036
Formulations applied for preparation of milk chocolate samplesa (g/100 g)
| Ingredient | Control | T1 | T2 | T3 |
| Fine sucrose | 33 | 0 | 0 | 0 |
| Isomalt | 0 | 33 | 0 | 0 |
| Xylitol | 0 | 0 | 33 | 0 |
| Maltitol | 0 | 0 | 0 | 33 |
| Stevia (ppm) | 0 | 660 | 0 | 330 |
| Cocoa butter | 27.5 | 27.5 | 27.5 | 27.5 |
| Cocoa mass | 13 | 13 | 13 | 13 |
| Whole milk powder | 26 | 26 | 26 | 26 |
| Sunflower lecithin | 0.3 | 0.3 | 0.3 | 0.3 |
| PGPR | 0.2 | 0.2 | 0.2 | 0.2 |
| Ethyl vanillin | 0.01 | 0.01 | 0.01 | 0.01 |
T: treatment.
Water activity, moisture content and PSD values of milk chocolate samples prepared by different bulk sweetenersa
| Sample |
| Moisture content (g/100 g) | PSD values | |||||
|---|---|---|---|---|---|---|---|---|
| SSA (cm3/cm2) |
|
|
|
|
| |||
| Control | 0.269 ± 0.007a | 1.02 ± 0.01d | 5716.3 ± 1.3a | 38.16 ± 0.56c | 5.62 ± 0.07b | 20.00 ± 0.19c | 15.72 ± 0.26b | 17.81 ± 0.43c |
| T1 | 0.238 ± 0.002b | 1.11 ± 0.02c | 5523.7 ± 1.1b | 40.06 ± 0.34b | 5.89 ± 0.01b | 22.00 ± 0.75bc | 16.09 ± 0.34b | 19.06 ± 0.56bc |
| T2 | 0.226 ± 0.003b | 1.37 ± 0.03a | 4968.4 ± 0.9d | 42.52 ± 0.13a | 6.73 ± 0.04a | 28.00 ± 0.63a | 16.86 ± 0.14a | 22.45 ± 0.21a |
| T3 | 0.229 ± 0.003b | 1.24 ± 0.01b | 5216.2 ± 1.5c | 41.23 ± 0.27b | 6.09 ± 0.05a | 25.00 ± 1.14b | 16.15 ± 0.42a | 20.58 ± 0.63b |
Different letters within columns indicate significant differences (P < 0.05). T1: treatments 1 (100% isomalt); T2: treatment 2 (100% xylitol); T3: treatments 3 (100% maltitol). SSA: specific surface area, D4/3 mean, D3/2 median, D10, D50 and D90, respectively, represent 10%, 50% and 90% of all particles finer than these sizes.
Fig. 1Effects of sugar replacers on shear stress and apparent viscosity-shear rate rheograms of functional milk chocolates.
Hardness and rheological parameters of milk chocolate samplesa
| Sample | Hardness (kgF) | Rheological parameters | ||
|---|---|---|---|---|
| Apparent viscosity (Pa s) | Casson viscosity (Pa s) | Casson yield (Pa) | ||
| Control | 4.46 ± 0.29c | 1.96 ± 0.009b | 1.60 ± 0.093b | 0.67 ± 0.306b |
| T1 | 4.78 ± 0.56b | 3.7 ± 1.05b | 2.78 ± 0.091b | 2.71 ± 0.457b |
| T2 | 4.54 ± 0.12c | 8.19 ± 0.86a | 6.11 ± 0.63a | 6.94 ± 1.017a |
| T3 | 5.14 ± 0.34a | 6.07 ± 0.89a | 4.91 ± 0.16a | 2.61 ± 0.583b |
Different letters within columns indicate significant differences (P < 0.05). T1: treatments 1 (100% isomalt); T2: treatment 2 (100% xylitol); T3: treatments 3 (100% maltitol). *Apparent viscosities are stated at a constant shear rate (40 s−1) for comparison aims.
Color and melting properties of milk chocolate samplesa
| Sample | Color parameters | Melting properties | ||||||
|---|---|---|---|---|---|---|---|---|
|
|
|
|
|
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| Width (°C) | Δ | |
| Control | 56.26 ± 0.28a | 18.18 ± 0.12a | 52.26 ± 0.64a | 20.4 ± 0.51a | 31.7 ± 0.37a | 38.3 ± 0.85a | 4.01 ± 0.3b | 29.9 ± 0.13c |
| T1 | 51.47 ± 0.33c | 15.60 ± 0.36b | 47.10 ± 0.76d | 17.4 ± 0.18c | 29.7 ± 0.23c | 37.1 ± 0.01a | 4.87 ± 0.4a | 34.6 ± 0.45 ab |
| T2 | 56.03 ± 0.47a | 17.51 ± 0.08a | 49.84 ± 0.32b | 18.7 ± 0.09b | 30.8 ± 0.05b | 37.3 ± 0.19a | 4.79 ± 0.2a | 33.5 ± 0.23b |
| T3 | 54.80 ± 0.16b | 17.15 ± 0.51a | 48.92 ± 0.15c | 19.0 ± 0.16b | 30.8 ± 0.01b | 37.7 ± 0.16a | 4.93 ± 0.4a | 35.4 ± 0.15a |
Different letters within columns indicate significant differences (P < 0.05). T1: treatments 1 (100% isomalt); T2: treatment 2 (100% xylitol); T3: treatments 3 (100% maltitol).
Fig. 2Particle agglomeration of chocolates sweetened with sucrose and polyols obtained with scanning electron microscopy: (a, c and e) control chocolates; (b, d and f) sucrose-free chocolates.
Fig. 3Spider chart representing (a) melting rate and texture, (b) aroma and taste and (c) appearance and total acceptance of chocolate samples.
Effects of sugar replacers on fitting of experimental data with rheological models in terms of R2 and RMSE parametersa
| Samples | Power law | Bingham | Herschel–Bulkley | Casson | ||||
|---|---|---|---|---|---|---|---|---|
|
| RMSE |
| RMSE |
| RMSE |
| RMSE | |
| Control | 0.998 | 1.021 | 0.999 | 0.153 | 0.998 | 0.119 | 0.999 | 0.085 |
| T1 | 0.999 | 1.690 | 0.999 | 1.368 | 0.999 | 0.380 | 0.999 | 0.063 |
| T2 | 0.997 | 5.253 | 0.988 | 12.25 | 0.995 | 4.841 | 0.998 | 0.295 |
| T3 | 0.999 | 1.751 | 0.998 | 2.965 | 0.999 | 1.221 | 0.999 | 0.081 |
R 2 = determination coefficient, RMSE: Root Mean Square Error. T1: treatment 1 (100% isomalt); T2: treatment 2 (100% xylitol); T3: treatment 3 (100% maltitol).