3.1. The Influence of Ambient Temperature on the Energy and Exergy Performance of the Drying System
In order to fully investigate the influence of ambient temperature on the drying behavior of the drying system, the experimental data in three days with different ambient temperatures and similar relative humidity (17 October: 8.07 °C ≤
T0 ≤ 13.41 °C, 42.51% ≤
RH0 ≤ 56.36%; 30 October: 3.26 °C ≤
T0 ≤ 8.87 °C, 47.26% ≤
RH0 ≤ 65.22%; 19 November: −0.74 °C ≤
T0 ≤ 5.18 °C, 40.35% ≤
RH0 ≤ 63.22%) are adopted for the analysis. The variations of corn moisture content and corn temperature with drying time are shown in
Figure 5.
The loading capacity of the dryer is considered to be 50,000 kg accuracy and the initial moisture content of the corn were also determined to be 32% d.b. for the three experimental days. As shown in
Figure 5,
MC decreases with the increase of
t while
Tc slightly increases with the increase of
t for the three sets of experimental data. The
MC decreases in a stepped way owing to the fact that corn drying is the circulate drying process, and the circulate time for each circle was ascertained to be 90 min. Similar drying process for agricultural product industrial drying were reported by Ma X.Z. et al. in 2017 [
36]. The total drying time for a unit drying operation in 17 October, 30 October, and 19 November, are, respectively, ascertained to be 480, 540, and 600 min, indicating that the
T0 has a great influence on the drying kinetics of the corn industrial drying. The
Tc for the three sets of experimental data are less than 38 °C, as recommended by Skoneczna-Łuczków, J. et al. [
37]. Moreover, it can be obvious found that the
Tc under the same drying time for the three days, in ascending order of values, are as follows:
Tc in 19 November,
Tc in 30 October,
Tc in 17 October, which might be caused by the heat change efficiency of the heat exchanger.
The exergy efficiency of the heat exchanger was calculated followed by Equation (4), and the results are depicted in
Figure 6. As can be seen from the figure, even if the
ηex,h fluctuates a lot with the drying time, which might be caused by the fluctuating inlet flue gas temperature, it can be obviously found that
ηex,h in 17 October is higher than that in 30 October and 19 November. The
ηex,h for the three days, respectively, ranges from 0.391 to 0.648, 0.350 to 0.601, and 0.249 to 0.434. It is interesting that there is a clear upward trend of the
ηex,h for three days after 260 min owing to the fact that
T0 rose up at noon for the three days. Accordingly, it can be concluded that the
T0 has a significant influence on the heat exchange performance of the heat exchanger, as well as the drying performance of the whole drying process. Moreover, for the present industrial-scale drying system, the ambient conditions should not be considered as the dead state, the ambient temperature should be take into consideration when analyzing the energy and exergetic performance of the dryer. Similar findings have been reported by Jörg Schemminger et al. [
38] for ambient air cereal grain drying; they developed a model for predicting the drying behavior based on the climatic data parameters (ambient temperature and relative humidity).
Waste heat recovery is an effective approach to improve the energy efficiency of an energy consumption system. In the present work, eight far-infrared radiators inserted into the drying chamber were adopted to recover the waste heat in outlet flue gas. As can be seen from
Figure 6, the values of
γ in 19 November, 30 October, and 17 October, respectively, vary from 7.61 to 7.90 um, 7.77 to 7.92 um, and 7.81 to 8.15 um, which are all closed to the optimized absorption far-infrared wavelength (9 µm) of cereal grain, as recommend by Zhu W et al. in 2003 [
39]. The
Er under the same drying time for the three days, in ascending order of values, are as follows:
Er in 17 October,
Er in 30 October,
Er in 19 November, owing to the fact that the
Er is directly proportional to the
Tr, as described in Equation (7). The total recovered exergy by the radiators for 17 October, 30 October, and 19 November are, respectively, ascertained to be 571.12, 621.17, and 650.43 MJ, as shown in the
Figure 7b.
3.2. Analysis of Prediction Results of BP Neural Network
Based on the analysis in
Section 2.7, the number of input layers of the IANN and OANN models were, respectively, ascertained to be 9 and 7; the outlet layers of the two models are 3, while the other key parameters, such as numbers of hidden layers, neurons, training epochs, and the momentum coefficient, should be further determined. The variation range of the key parameters of the two models are tabulated in
Table 5.
Based on the configurations of the ANN models, the 327 experimental data sets were used for the training (training epoch number of 1000, learning rate of 0.1). The variation of MSE values with different ANN configurations for the two models are tabulated in
Table 6. As can be seen from the
Table 6, the lowest MSE value of the IANN model is ascertained to be 1.3876 × 10
−4 when the hidden layer number is 2, neuron number is 12, and momentum coefficient is 0.4, while the MSE value of the OANN model is ascertained to be 2.5324 × 10
−4 when the hidden layer number is 2, neuron number is 12 and momentum coefficient is 0.4. In order to further investigate the influence of the training epochs on the MSE of the ANN models, the different training epochs (300–1500) and neuron numbers (5–13) are selected to train the IANN model with the hidden layer number of 2 and momentum coefficient of 0.4, and OANN model, with the hidden layer number of 3, and momentum coefficient of 0.4. The results are shown in
Table 7 and
Table 8. It obviously can be seen from the
Table 7 that the IANN model displays the best prediction performance (MSE = 0.75975 × 10
−4) when the training epochs are 1500 and the hidden layer neuron numbers are 12, while the OANN model displays the best prediction performance (MSE = 1.4542 × 10
−4) when the training epochs are 1500 and the hidden layer neuron numbers are 10. Accordingly, the architecture of the IANN model is ascertained to be 9-2-12-3, while the OANN model is 7-2-10-3.
Based on the obtained architecture of the two models, the data sets were trained by the models and the training results are shown in
Figure 8. As can be seen from the
Figure 8a, the IANN model gets the best prediction performance when the training epochs are 30, where the model gets the lowest MSE value (2.1252 × 10
−4) and the
R-values for the data sets used for training, validating, and testing the model are 0.99852, 0.99623, and 0.99788, respectively. On the other hand, the OANN model gets performs a best prediction performance when the epochs are 31, where the model gets the lowest MSE value (2.1125 × 10
−4) and the
R-values for the data sets used for training, validating, and testing the model are 0.99779, 0.99225, and 0.99231, respectively. Indicating that the established models have sufficient reliability and can be used for predicting the
MC,
ηex,h, and
Er. However, compared with the OANN model, the IANN model has a better prediction performance with the higher values of MSE and
R-values, indicating that the IANN model has a better prediction performance. It can be summarized that the ambient conditions should be taken into consideration when establishing the prediction model. Moreover, in order to achieve the repeatability of the model, the weights of the established IANN model are listed in
Table 9.
3.3. The Application of the IANN Model
To further verify the practicability of the established IANN model, the 117 experimental data sets acquired in 12 November (−3.01 °C ≤
T0 ≤ 5.94 °C, 40.35% ≤
RH0 ≤ 63.23%) were trained by the model. The comparison between experimental values and predicting results of the
MC,
Er, and
ηex,h are depicted in the following
Figure 9. Obviously, it can be seen from the figure that the regression coefficient of determination (
R2) for
MC,
Er, and
ηex,h, respectively, are 0.998, 0.992, and 0.980, mean squared error (
MSE) of 0.067, 0.00296, and 0.0057, mean absolute error (
MAE) of 0.16, 0.04, and 0.0063. The values of the above statistic indexes indicate that the 9-2-12-3 IANN model has an excellent prediction performance and can be used in engineering practice. Moreover, the prediction results of the first cycle (the measured
MC between 28.9% d.b. and 32% d.b.) are slightly deviated from the experimental results, which might be caused by the fact that there is a measurement error for the on-line moisture meter in the high moisture region of cereal grains [
40].
Based on the established 9-2-12-3 IANN model, a control model of the drying process is proposed, as shown in the
Figure 10. During the drying process, the experimental data collected by the corresponding sensor are used to train, and get, the optimal IANN model. As can be seen from
Figure 2 and
Figure 10, the drying process is controlled by the DD and the flue gas valve on the flue gas pipeline. When one of the inputted factors changes, the established IANN model can automatically calculate and analyze the predicted corresponding output indexes at the same time. Accordingly, the intelligent optimized controller optimizes and calculates the grain discharging electric motor (or flue gas valve), and the optimal rotational speed of the electric motor (or optimal openness of the valve) is given to the frequency converter, so as to control the drying process, and realize the optimal control of the
MC,
Er, and
ηex,h. The proposed control model based on the IANN model may strengthen the practical implications.