| Literature DB >> 32180980 |
Lifang Cao1, Bowen Li2,3, Nan Zhao2,3, Huan Li2,3, Yanfeng Wang1, Xing Yu2,3, Xin Huang4,5.
Abstract
Moisture migration is considered to be one of the most important influencer on crop quality during storage, which is easily affected by storage conditions, such as ambient humidity and temperature. The aim of this work was to determine the effect of storage condition on moisture content of Chinese naked oat by simulating 9 equilibrium relative humidity (ERH) and 5 temperatures. The equilibrium moisture content (EMC) of dry sample was achieved by adsorption, while EMC of wet one was achieved by desorption. EMC of oat increased with the increase in ERH and decreased when temperature increased. The sorption isotherm was a typical "S" shape and fitted using current EMC/ERH models. Modified Chung-Pfost (MCPE) model was the most suitable for describing the dynamic sorption process of Chinese naked oat during storage with a ERH range from 10% to 90%. There was an obvious hysteresis between adsorption and desorption isotherms, whose range decreased with the increase of temperature. High temperature accelerated moisture migration by increasing the hydrophilicity of oat surface. Moreover, dynamic moisture migration was imaged by low-field nuclear magnetic resonance (NMR), showing that moisture migrated between ambient environment and oat mainly through endosperm where most moisture accumulated. During sorption, free water migrated firstly, followed by bound water and the change in content of bound water was more stable than that of free water. The results of this study can provide a useful information for future work on quality control of oat during storage.Entities:
Keywords: adsorption; bound water; crop; desorption; free water; moisture content
Year: 2020 PMID: 32180980 PMCID: PMC7063355 DOI: 10.1002/fsn3.1461
Source DB: PubMed Journal: Food Sci Nutr ISSN: 2048-7177 Impact factor: 2.863
ERH produced by some saturated salt solutions
| Saturated salt solution |
ERH (%) Temperature (°C) | ||||
|---|---|---|---|---|---|
| 10 | 15 | 20 | 25 | 30 | |
| Lithium chloride | 11.29 | 11.30 | 11.31 | 11.30 | 11.28 |
| Potassium acetate | 23.38 | 23.40 | 23.11 | 22.51 | 21.61 |
| Magnesium chloride | 33.47 | 33.30 | 33.07 | 32.78 | 32.44 |
| Potassium carbonate | 43.14 | 43.15 | 43.16 | 43.16 | 43.17 |
| Magnesium nitrate | 58.86 | 57.36 | 55.87 | 54.38 | 52.89 |
| Copper chloride | 68.40 | 68.40 | 68.30 | 67.00 | 66.50 |
| Sodium chloride | 75.67 | 75.61 | 75.47 | 75.29 | 75.09 |
| Potassium chloride | 86.77 | 85.92 | 85.11 | 84.34 | 83.62 |
| Potassium nitrate | 95.96 | 95.41 | 94.62 | 93.58 | 92.31 |
Nine common EMC/ERH sorption isotherm models used for fitting the experimental data
| Model | Equation |
|---|---|
| MHE |
|
| MCPE |
|
| MHAE |
|
| MOE |
|
| MGAB |
|
| CCE |
|
| SYE |
|
| BET |
|
| CAE |
|
M is equilibrium moisture content (%); h is environmental equilibrium relative humidity (%); C1, C2, C3, C4, and C5 are equation parameters; T is temperature (°C); and P is saturated vapor pressure (MPa).
EMC of oat obtained from adsorption and desorption at different storage conditions
| Environmental conditions | Equilibrium moisture content (%) | Hysteresis (%) | Environmental conditions | Equilibrium moisture content (%) | Hysteresis (%) | ||||
|---|---|---|---|---|---|---|---|---|---|
| Temperature (°C) | Relative humidity (%) | Adsorption | Desorption | Temperature (°C) | Relative humidity (%) | Adsorption | Desorption | ||
| 10 | 11.29 | 8.45 | 8.97 | 0.52 | 25 | 11.30 | 6.23 | 7.16 | 0.93 |
| 23.38 | 9.80 | 10.13 | 0.33 | 22.51 | 7.96 | 9.06 | 1.10 | ||
| 33.47 | 9.42 | 11.28 | 1.9 | 32.78 | 8.97 | 10.37 | 1.41 | ||
| 43.14 | 11.77 | 13.17 | 1.4 | 43.16 | 10.72 | 11.61 | 0.88 | ||
| 58.86 | 14.12 | 14.56 | 0.44 | 54.38 | 11.42 | 12.50 | 1.08 | ||
| 68.40 | 15.78 | 17.09 | 1.31 | 67.00 | 13.76 | 14.90 | 1.14 | ||
| 75.67 | 15.83 | 17.57 | 1.75 | 75.29 | 15.14 | 15.83 | 0.69 | ||
| 86.77 | 18.84 | 20.65 | 1.81 | 84.34 | 17.61 | 17.88 | 0.27 | ||
| 95.96 | 24.76 | 25.15 | 0.39 | 93.58 | 22.05 | 22.31 | 0.26 | ||
| 15 | 11.30 | 6.04 | 7.84 | 1.80 | 30 | 11.28 | 5.86 | 6.58 | 0.72 |
| 23.40 | 7.84 | 9.62 | 1.77 | 21.61 | 7.63 | 8.57 | 0.94 | ||
| 33.30 | 9.32 | 10.96 | 1.65 | 32.44 | 9.01 | 9.82 | 0.81 | ||
| 43.15 | 10.63 | 12.17 | 1.54 | 43.17 | 10.50 | 11.45 | 0.95 | ||
| 57.36 | 12.27 | 14.04 | 1.77 | 52.89 | 11.25 | 12.22 | 0.97 | ||
| 68.40 | 14.25 | 15.94 | 1.68 | 66.50 | 13.60 | 14.16 | 0.56 | ||
| 75.61 | 16.27 | 17.13 | 0.86 | 75.09 | 15.12 | 15.84 | 0.72 | ||
| 85.92 | 18.80 | 19.61 | 0.81 | 83.62 | 17.35 | 17.57 | 0.22 | ||
| 95.41 | 23.45 | 26.97 | 3.52 | 92.31 | 20.59 | 20.91 | 0.33 | ||
| 20 | 11.31 | 6.38 | 77.19 | 0.82 | |||||
| 23.11 | 8.63 | 9.14 | 0.51 | ||||||
| 33.07 | 9.17 | 10.60 | 1.43 | ||||||
| 43.16 | 11.01 | 12.58 | 1.57 | ||||||
| 55.87 | 12.30 | 13.72 | 1.41 | ||||||
| 68.30 | 14.02 | 15.36 | 1.34 | ||||||
| 75.47 | 15.45 | 16.75 | 1.29 | ||||||
| 85.11 | 18.09 | 18.87 | 0.79 | ||||||
| 94.62 | 23.09 | 23.60 | 0.52 | ||||||
The estimation of parameters of 9 isotherm models for fitting adsorption data
| Model | Pertinent parameters | R2 | Error indicators | ||||||
|---|---|---|---|---|---|---|---|---|---|
| C1 | C2 | C3 | C4 | C5 | RSS | SE | MRE% | ||
| MHE | 0.858 | 90.600 | 2.302 | 0.981 | 0.002 | 0.007 | 4.92 | ||
| MCPE | 1259.000 | 125.700 | 22.070 | 0.996 | 4.901E‐4 | 0.003 | 2.93 | ||
| MHAE | −7.619 | −0.009 | 3.406 | 0.958 | 0.005 | 0.010 | 7.65 | ||
| MOE | 0.122 | −3.630E‐4 | 4.035 | 0.982 | 0.002 | 0.008 | 4.57 | ||
| GAB | 0.078 | 0.694 | 778.300 | 0.985 | 0.002 | 0.006 | 3.78 | ||
| CCE | 1.734 | −0.300 | 0.032 | 1.153 | 0.989 | 0.001 | 0.005 | 3.69 | |
| SYE | 0.165 | 11.810 | 8.218 | 21.270 | 0.995 | 0.017 | 0.019 | 7.77 | |
| BET | 0.066 | −1.903E‐4 | 138.1 | 0.915 | 0.001 | 0.005 | 4.88 | ||
| CAE | 0.351 | 0.286 | 1.381 | 1.122 | 4.691 | 0.957 | 0.147 | 0.058 | 11.46 |
The estimation of parameters of 9 isotherm models for fitting desorption data
| Model | Model parameters | R2 | Error parameters | ||||||
|---|---|---|---|---|---|---|---|---|---|
| C1 | C2 | C3 | C4 | C5 | RSS | SE | MRE% | ||
| MHE | 2.927 | 39.15 | 2.703 | 0.996 | 4.050E‐4 | 0.003 | 3.20 | ||
| MCPE | 648.500 | 30.990 | 23.040 | 0.999 | 1.458E‐4 | 0.002 | 2.04 | ||
| MHAE | −7.253 | −0.024 | 3.530 | 0.969 | 0.004 | 0.009 | 5.88 | ||
| MOE | 0.144 | −0.001 | 4.293 | 0.991 | 0.001 | 0.005 | 3.20 | ||
| GAB | 0.094 | 0.606 | 747.400 | 0.987 | 0.002 | 0.006 | 3.13 | ||
| CCE | 1.039 | −0.438 | 0.019 | 1.247 | 0.988 | 0.001 | 0.006 | 2.76 | |
| SYE | 1.402 | 15.930 | 12.500 | 21.170 | 0.997 | 0.010 | 0.015 | 4.07 | |
| BET | 0.082 | −5.285E‐4 | 192.500 | 0.955 | 3.042E‐4 | 0.004 | 3.13 | ||
| CAE | 0.357 | 0.259 | 2.334 | 1.698 | 0.351 | 0.964 | 0.121 | 0.052 | 9.43 |
Figure 1The predicted sorption isotherm curve of oat by MCPE model at (a) 10, (b) 15, (c) 20, (d) 25, and (e) 30°C
Figure 2Changes in contact angle of water drop deposited on oat surface at temperatures of 10, 15, 20, 25, and 30°C
Figure 3Pseudocolor of 2D proton density images of oat during adsorption and desorption
Figure 4Changes in signal amplitudes of bound water and free water with oat (a) adsorption and (b) desorption times