1. Introduction
The adoption of the “peak carbon and carbon neutral” objective during the 75th session of the United Nations General Assembly and subsequent reaffirmations at the World Summit on Climate Ambition have established a global commitment to reducing carbon emissions [
1]. Projections indicate that by 2030 there will be a minimum 65 percent reduction in global carbon dioxide emissions per unit of GDP compared to 2005 levels, with non-fossil fuels comprising at least 25 percent of primary energy consumption [
2]. This transition will involve wind, solar, and other emerging energy sources contributing to a total installed capacity of 1.2 billion kilowatts worldwide [
3].
As of the end of 2020, China has demonstrated significant momentum in the development of new energy sources, boasting an installed wind power capacity of 280 million kilowatts and solar power capacity of 250 million kilowatts. Experts estimate that within the next decade, China’s combined installed wind and solar power capacity will exceed 670 million kilowatts, accounting for approximately 33 percent of the nation’s total power generation capacity as of 2019 [
4]. However, renewable energy sources, despite their growth, present challenges in meeting electricity demand during certain periods due to their inherent intermittency [
5].
Consequently, the responsibility of ensuring clean energy consumption primarily falls upon thermal power units, which offer large installed capacities, high stability, and mature technology [
6]. Given the substantial integration of renewable energy into the grid, thermal power units face a formidable task in accommodating the additional demand for new energy consumption [
7].
With the widespread integration of renewable energy into the grid, the power system is undergoing significant transformations across various aspects such as stabilization mechanisms, dispatch operations, and planning development [
8]. In recent years, the challenge of domestic power dispatch has gradually surfaced, with the core issue revolving around addressing the spatial and temporal uncertainties stemming from the intermittency of renewable energy sources [
9]. Currently, this challenge is primarily managed by thermal power units, which possess large installed capacities, high stability, and mature technologies [
10]. However, as various types of new energy units and distributed clean energy technologies rapidly develop, the dominance of thermal power units in providing heating services restricts their regulatory capacity, further deepening the integration of energy coupling and information interaction between the power and heating systems [
11].
Power system flexibility, crucial for addressing supply and demand fluctuations and uncertainties in a stable, reliable, and cost-effective manner within specific timeframes, underscores the importance of enhancing the flexible operation capabilities of thermal power units in China’s energy structure transformation and development [
12]. Presently, thermal power units typically operate at as low as 30–40% of their rated load during deep grid peaking, indicating limited flexibility [
13]. Moreover, the presence of numerous cogeneration units within thermal power plants constrains the acceptance of new energy power during heating periods, intensifying the complexity of renewable energy consumption [
14].
To address these challenges, numerous experts and scholars have conducted research on the variable load operations of thermal power units. For instance, Luo Qing et al. [
15] developed a dynamic model of boiler heat exchangers under variable load conditions. Their objective was to investigate the dynamic response characteristics of each heating surface of the boiler when subjected to step changes in various boundary conditions. Zhao Yongliang et al. [
16] utilized GSE software to model the automatic generation control (AGC) variable load process of a thermal power unit. Their study focused on analyzing the variations in key parameters of the thermal power unit during the variable load operations. Additionally, Zlatkovikj et al. [
17] employed Dymola 2022x software to simulate biomass cogeneration boilers, thereby enhancing the control efficacy of the boilers under variable operating conditions
Currently, the primary technical approaches to enhancing the low-load stable combustion capability of thermal power units involve adjustments to the wind
–coal ratio and modifications to the operational control mode of coal mills [
18]. However, implementing these adjustments is often challenging based solely on theoretical understanding and operational experience.
With the advancement and utilization of technologies such as big data analysis, various industries in China are undergoing rapid digitalization and intelligence-driven transformations, unlocking the latent value embedded within data [
19]. In recent years, machine learning, deep learning, and other advanced algorithms have found widespread application in the energy sector, particularly in optimizing control systems and predicting key parameters [
20,
21].
For instance, Si RuiCai et al. [
22] developed a high, medium, and low-load model for a 600 MW thermal power unit using a back propagation (BP) neural network to enhance unit control processes. Additionally, Zhang GuangMing et al. [
23] introduced a data-driven unit modeling approach based on the MLP algorithm, alongside an offline reinforcement learning-based coordinated control method for electricity and heat.
In summary, numerous scholars and experts have dedicated efforts to optimizing control systems to enhance the flexibility of thermal power units [
24,
25]. The primary challenge lies in managing parameter fluctuations during the unit’s variable load operations, particularly in deep peaking scenarios [
26]. This necessitates the development of models for thermal unit operation and control processes, often relying on simulation software or individual intelligent algorithms [
27].
The optimization of load instructions for coal-fired units holds paramount importance. By effectively managing and adjusting load instructions, these units can enhance their flexibility, promptly respond to power system fluctuations, and uphold system equilibrium and stability. Furthermore, optimizing load commands can lead to reduced operational costs, energy conservation, and enhanced economic efficiency. Significantly, it contributes to improved operational efficiency and system performance, mitigates environmental impact, and aligns with sustainable development goals. Hence, optimizing load commands serves not only as a crucial measure to enhance coal-fired units’ operational efficiency but also as a pivotal approach to foster the sustainable development of power systems.
The conventional simulation software’s modeling process can be intricate and lacks specificity for real-world operating units. Models based solely on a single algorithm may display reduced accuracy and necessitate extended recalibration times for diverse unit operating conditions. While the existing literature has primarily examined the variation in key parameters in thermal power units during variable load processes, there has been limited analysis focused on optimizing the actual operational processes.
Hence, this paper employs an enhanced PSO-LSTM algorithm to develop a data model and scrutinize AGC dynamic traits following rigorous validations. Consequently, diverse load commands are assessed to identify the optimal command that yields the most favorable dynamic traits for coal-fired units. This study aims to offer insights into setting load commands effectively for coal-fired power plants.
4. Results and Discussion
4.1. AGC Variable Load Process Study
To investigate the dynamic characteristics of the optimized numerical model’s AGC variable load process, simulations were conducted for load rising and load reduction processes from 75% THA to 100% THA using various load change rates. These simulations started from 0 s, and all load command changes followed primary function changes. The results of these simulations are presented in
Figure 8 and summarized in
Table 9.
From the analysis of
Figure 8 and
Table 9, it is evident that the power generation response time during load raising process is slightly faster compared to load reduction. Moreover, as the load change rate in the model increases, there is a corresponding increase in the overshoot of actual generation power, and the intensity of fluctuations becomes more pronounced.
4.2. AGC Variable Operating Condition Evaluation Index
Due to the implementation of the “two regulations” in each regional grid of the power system, the demands on thermal power units have become increasingly stringent. Consequently, a more detailed and comprehensive evaluation index for AGC variable operating conditions in thermal power units has been developed [
39]. A specific evaluation index for the “two regulations” is proposed [
40], and its calculation method is outlined in Equations (18)–(20).
where
K1 is the regulation rate index and
K2 is the regulation accuracy index;
λ1 and
λ2 are the weighting coefficients, the sum of which is 1;
Km is the measured AGC regulation rate of the unit, and
Kb is the basic response rate of the unit;
β is the precision deflation coefficient, which is used to unify the order of magnitude of the two indexes;
P1(t) is the actual output of the unit under the process of variable load of the AGC, and
P2(t) is the target output of the unit after the action of the AGC; and
T is the time of input of the AGC.
4.3. Load Command Optimization
The load command input into the simulated AGC variable load process above is currently set using a basic primary function. To establish the optimal load command settings and refine the AGC variable load control process, the numerical model developed in this study can be applied to simulate the AGC variable load process. Initially, the load command settings are determined based on the relationship, as depicted in Equations (21) and (22), enabling the generation of various load command sets.
where
U is the load command,
T is the time, and
γ is the power index, which is set to change the load command by setting different values;
a and
b are constants, which are determined by Equation (22) and the variable load process;
c is the initial value of the load; and
T1 is the time for the load command to reach the target load. The power function is chosen as a function to determine the relationship between load command and time, and the derivative of the load command is 0 when the target load is reached by Equation (22) in order to reduce the loss of economy and safety of the unit caused by the amount of overshoot of the AGC variable load.
As an example, considering a 50–75% THA variable load with a load change rate of 10 MW/min and
T1 = 900 s, the load instruction changes are illustrated in
Figure 8. Various load command sets are input into the deep learning model to derive
P1(t), which is then used in conjunction with Equation (20) to compute the comprehensive evaluation index for variable load. In this calculation, the accuracy deflation factor
b is set to 0.01, and
λ1 =
λ2 = 0.5. The variable load evaluation indexes under different load command settings are detailed in
Table 10 and
Table 11.
The analysis presented in
Table 10 and
Table 11 reveals an inverse relationship between γ and stabilization time during both load rising and load reduction processes. This phenomenon arises due to the nature of
γ: a larger value indicates a more abrupt initial change in the load command, followed by a smoother transition towards the final change. Consequently, while the load experiences greater variation at the onset, the system gradually adapts during subsequent periods, reducing the system’s instability during the response transition and hastening the time needed to attain a stable state.
However, it is essential to note that while within the experimental range a decrease in stabilization time is observed with increasing γ, such conclusions have limits. When γ becomes sufficiently large, the load command undergoes very sharp changes initially, potentially causing significant oscillations or overshoots in the system. This can lead to a longer recovery time and a delay in reaching the stable state, ultimately resulting in an increased stabilization time. Thus, the impact of γ on stabilization time exhibits a nuanced relationship that depends on the specific system dynamics and the extent of load command changes.
The regulation rate indicator K1 exhibits a decreasing trend with increasing γ, observed during both load rising and load reduction processes. This behavior can be attributed to the relationship between γ and the initial load command change. Specifically, as γ increases, the load command undergoes a more abrupt change at the beginning. Consequently, the output power also begins to change drastically earlier, leading to an earlier attainment of the target command. This early convergence towards the target load results in a decrease in the regulation rate indicator K1 as γ increases.
The regulation accuracy index K2 exhibits a non-linear trend with respect to γ in both the load rising and load reduction processes. Initially, K2 decreases as γ increases, indicating that when the load command changes steeply followed by a smooth transition, the control system may experience over-regulation or oscillations, leading to reduced regulation accuracy. Conversely, when the load command changes smoothly and then steeply, the system can adjust the load more gently, albeit potentially resulting in a slower regulation response and reduced timeliness in regulation accuracy. Therefore, an optimal value of γ is crucial to achieve the best regulation accuracy, striking a balance between rapid response to load changes and maintaining stability to ensure effective regulation.
In summary, the comprehensive evaluation indicator Ik demonstrates a non-linear trend with increasing γ. Specifically, within the experimental range, γ = 1.8 yields optimal comprehensive evaluation indicators for the regulation accuracy and regulation rate. However, it is important to note that this study offers a generalized approach and guidance for load command optimization in coal-fired power plants. The applicability of these conclusions may vary for other coal-fired power plants due to differences in load command strategies, control systems, and system configurations. Nonetheless, this methodology provides a framework for evaluation that can be adapted and applied across various coal-fired power plant contexts.