1. Introduction
According to the State Council of China, it is crucial to focus on the implementation of the key work division outlined in the ‘Government Work Report’. Specifically, there is a need to prioritize the work of carbon peaking and carbon neutralization in many application areas such as industrial and transportation fields [
1,
2] To achieve this, an action plan for carbon emission peaking should be formulated before 2030. Currently, fossil fuels remain the primary source of power globally. However, there is a growing consensus to promote low-carbon electricity and increase the use of renewable clean energy sources to create a more sustainable energy network in Ref. [
3]. Distributed renewable energy sources are geographically dispersed and operate independently, which can result in inefficient resource allocation due to a lack of coordination and unity. However, the virtual power plant also presents an opportunity for innovative solutions to address these challenges in Ref. [
4].
The transition from fossil fuel power generation to cleaner and low-carbon power generation requires a significant amount of time. As a result, the carbon emissions produced by fossil fuel power generation have become the primary obstacle in achieving the ‘dual carbon’ goal. According to ‘China’s Carbon Neutrality Research Report Before 2060’, the development of new energy sources and carbon capture and storage (CCS) technology is the key to achieving carbon neutrality in Ref. [
5]. The utilization of CCS technology in fossil fuel power plants can significantly reduce their carbon emissions and improve their flexibility in operation, thus facilitating the consumption of wind power in Refs. [
6,
7]. However, the storage cost associated with carbon dioxide is high and there is a risk of leakage. To effectively mitigate these issues, reusing the captured CO
2 is the most effective method in Ref. [
8]. P2G technology provides a promising solution for the reuse of CO
2, while also enabling energy conversion and load time-space translation. The stored natural gas can be utilized to consume renewable clean energy and manage peak-shaving and valley-filling of electric load.
Currently, research on carbon emission reduction often focuses on two independent methods: CCS and P2G in Refs. [
9,
10,
11,
12]. Studies on carbon capture units typically examine capital gains, operation decisions, and optimal control in Refs. [
13,
14,
15]. The recent literature has analyzed the advantages of carbon capture power plants participating in peak regulation and suggests that these plants can serve as an ideal supporting power source for wind power in Refs. [
16,
17]. Additionally, wind and photovoltaic power generation can also power the CO
2 capture system, ultimately reducing the cost of generating electricity for carbon capture plants. In the previous literature, carbon capture units were introduced as a means of reducing carbon emissions. A multi-regional VPP optimal scheduling model under the energy market was proposed in Ref. [
18]. Ref. [
19] presented a low-carbon economic dispatch model for electric–gas systems that included carbon capture systems and wind power. This model also factored in the emission cost based on carbon tax into the objective function. Both of these studies confirm that carbon capture units are a more environmentally friendly and flexible alternative to traditional coal-fired power plants.
P2G devices have been extensively researched as coupling elements between power grids and gas networks, as well as controllable energy-consuming response devices. The working principle and performance of P2G, along with its economic evaluation, have been introduced in Refs. [
20,
21]. Additionally, Refs. [
22,
23] have constructed a carbon capture power plant and P2G system framework, which use CO
2 captured by the carbon capture power plant as a raw material for the production of natural gas to reuse CO
2. The fast response of P2G energy conversion and transmission also enhances the flexibility of the system. It has been suggested in Ref. [
24] that P2G can be used to transfer power from peak hours to off-peak hours, thereby easing the pressure on the power supply. These studies confirm that P2G plays a positive role in clean energy consumption, relief of environmental pressure, and economic improvement.
As the penetration of renewable energy generation in VPP increases, it also provides a new direction for solving the problem of energy consumption in the operation of carbon capture-P2G systems. However, the variability in wind and photovoltaic power generation can affect the reliability of the VPP power supply and reduce the low-carbon economic benefits of the carbon capture-P2G system in Refs. [
25,
26,
27]. Currently, there are two solutions to this problem. The first approach is to implement a multi-time scale rolling optimization strategy to compensate for forecast errors and increase the consumption of renewable energy generation. The second solution involves using fast adjustment devices like energy storage power plants and carbon capture power plants to manage fluctuations in renewable energy. Since the prediction accuracy of renewable energy generation and load improves with shorter time scales in Ref. [
28], it is relevant to study multi-timescale dispatching strategies in order to correct the deviation of dispatching plans with long time scales from more accurate prediction conditions. In addition, pumped storage (PS) units are becoming increasingly important for peak regulation in power systems due to their rapid output response, flexible adjustment methods, and environmental benefits. Current research focuses on the joint operation mode of wind power and pumped storage in Refs. [
29,
30,
31]; there is a need to consider the coordinated operation of pumped storage units and carbon capture-power-to-gas systems on multiple time scales.
In summary, based on existing research, this paper proposes a framework for collaborative utilization of pumped storage—carbon capture—P2G technologies. It also constructs a multi-time scale low carbon economic dispatch model for VPP to minimize the internal resource operation cost of VPP in each time period. During the intraday scheduling stage, the day-ahead scheduling results as the planned output and the energy flow is then dynamically corrected at a short-term resolution in the framework. This allows for the exploration of the low-carbon potential of each aggregation unit within the virtual power plant. Finally, the validity of the proposed method is verified by example analysis.
2. Pumped Storage—Carbon Capture—P2G VPP Multi-Timescale Low Carbon Operation Framework
2.1. VPP System Architecture
The carbon capture-to-gas synergistic operation framework extends the flexibility of the carbon capture plant by regulating the energy consumption of the carbon capture system and by supplying the captured CO
2 to the P2G plant for methane production. However, the ability of this mechanism to generate greater benefits is limited by the level of load demand at the current moment. It is difficult to support the increasing load peak-to-valley difference from year to year and the regulation demand caused by the anti-peaking characteristic of scaled renewable energy. On this basis, this paper introduces pumped storage units with the characteristics of flexible conversion of operating conditions and fast adjustment of output, with the starting point of improving the flexible adjustment capability of VPP. This paper proposes a pumped storage-carbon capture-electricity-to-gas synergistic utilization framework, as shown in
Figure 1.
In the emission layer, the only source of carbon emissions from the VPP system is the carbon capture plant. A portion of the CO2 is captured by the carbon capture system and another portion of the CO2 is emitted into the atmosphere. The captured CO2 can be used as a feedstock for the production of methane in the P2G plant and the excess can be disposed of by carbon sequestration. Where is the amount of CO2 directly generated by the carbon capture unit for power generation. is the amount of CO2 emitted directly into the atmosphere. is the amount of CO2 captured by the carbon capture system. is the amount of CO2 sequestered. is the amount of CO2 consumed by the P2G unit. is the volume of methane produced by the P2G unit.
At the equipment level, wind power, photovoltaic power generation, and pumped storage units can provide energy consumption for carbon capture systems and P2G equipment. Pumped storage units, as auxiliary regulation resources, can take advantage of the spatial and temporal complementarity of different energy resources in terms of power and energy consumption.
At the dispatch level, the VPP aggregation energy is supplied by wind power, photovoltaic power, pumped storage unit power, and carbon capture plant output. When the pumped storage unit is in pumping mode, the energy consumption is supplied by the VPP aggregation energy. Where and are the feed-in power for wind and PV, respectively; and are the energy consumption provided by wind and PV for P2G, respectively; , , and are the energy consumption provided by wind power, photovoltaic power, and carbon capture plant for the carbon capture system, respectively; , , and are the energy consumption and feed-in power provided by the pumped storage units to the P2G and carbon capture system. is the pumping power of the pumped storage unit as an energy consuming device.
The energy flow based on the framework of synergistic utilization is more flexible to match the change in renewable energy output, the energy consumption of the carbon capture system, and the energy consumption of the P2G equipment, so as to improve the carbon emission reduction and renewable energy consumption level of the VPP.
2.2. VPP Multi-Timescale Coordinated Optimization Strategy
The conventional day-ahead dispatching method can scarcely fulfill the system safety and economic criteria owing to the unpredictability brought by the grid connection of large-scale renewable energy. The multi-timescale rolling optimization theory relies on the principle that the prediction accuracy of renewable energy output and load demand increases as the timescale is shortened and rolling correction of controllable power output in a short timescale to match the fluctuation in renewable energy output, so as to meet the safety and economic requirements of the system. The multi-timescale rolling optimization strategy is shown in
Figure 2.
This paper proposes a multi-timescale rolling optimization strategy for virtual power plants considering a framework for collaborative utilization of pumped storage—carbon capture—P2G technologies based on the multi-timescale optimization theory to modify the energy flow under the framework for collaborative utilization on short timescales to further exploit the fine-grained scheduling advantages of the framework for collaborative utilization.
The prediction and control domains in the day-ahead scheduling are both 24 h with a time resolution of 1 h. The prediction domain in the day-ahead scheduling is the ultra-short-term prediction time scale for uncertain resources, i.e., 4 h with a time resolution of 15 min and the control domain is 15 min. The day-ahead scheduling plan with a time resolution of 1 h is expanded to 96 time periods with a resolution of 15 min. The intraday scheduling time window is rolled back every 15 min, each time rolling to solve the intraday scheduling plan for the 4 h in the prediction domain and execute the 15-min intraday scheduling plan in the control domain. The process is repeated until the intraday scheduling plan is completed.
3. VPP Multi-Time Scale Low Carbon Economic Dispatch Model
Based on the above multi-timescale rolling optimization strategy for virtual power plants considering the pumped storage—carbon capture—P2G synergistic utilization framework, optimal scheduling models are developed for the day-ahead and intraday scheduling phases based on the predicted power of wind power, photovoltaic power, and load at different timescales, respectively.
3.1. Source and Load Uncertainty Treatment
At present, the prediction models for wind power, photovoltaic power generation, and load have been studied in depth, including the historical data method and probabilistic model method and the predicted power of each unit is obtained based on the Monte Carlo simulation method and deep learning algorithm. The focus of this paper is on the optimal scheduling of VPP. So, we assume that the prediction errors of wind and PV power generation and load are inscribed by a normal distribution with zero mean and independent of each other [
32], as shown in the following equation:
where
,
, and
are the forecast variances for wind power, PV power, and load at time
t, respectively.
,
, and
are the variances of the forecast deviations at time
t for wind power, PV power, and load, respectively.
3.2. Day-Ahead Scheduling Model
In the day-ahead dispatching phase, the VPP day-ahead 24 h dispatching plan is formulated based on the short-term predicted power of wind power, PV power, and load with a time resolution of 1 h and one day cycle.
3.2.1. Objective Function
The day-ahead scheduling model takes the total operating cost of VPP in the scheduling cycle as the objective function to minimize.
where
is the fuel cost of the carbon capture plant at time
t.
is the operating cost of the P2G device at time
t. is the cost of switching the operating conditions of the pumped storage unit at moment
t.
is the CO
2-related cost of the VPP at time
t.
is the gain from VPP’s participation in the green certificate transaction at time
t.
and
are the operation and maintenance costs of wind power and photovoltaic power generation at time
t, respectively.
is the penalty costs for wind power abandonment and photovoltaic power abandonment at time
t.
is the cost of electricity purchased from the grid by VPP at time
t.
- (1)
Carbon capture plant fuel costs.
where a, b, and c are the operating cost factors of the carbon capture unit, respectively.
is the equivalent output of the carbon capture unit at time
t.
- (2)
P2G equipment operating costs.
where
is the purchase price of CO
2 for the production of methane for the P2G equipment, CNY/t, (CNY: China Yuan).
is the operating cost factor for P2G equipment, CNY/(MW·h).
is the energy consumption of the P2G equipment at time
t, MW.
is the amount of CO
2 to be purchased at time
t when the P2G equipment consumes more energy and the amount of CO
2 captured is less,
t.
is the fixed price per unit volume of methane in the methane market, CNY/m
3.
is the volume of methane generated by the P2G device at time
t, m
3.
- (3)
Pumped storage unit operating conditions switching costs.
where
is the cost of a single start-up of a pumped storage unit under power generation condition, CNY.
is the cost of a single start-up of a pumped storage unit under power pumping condition, CNY.
and
are the Boolean variables for the state of the pumped storage unit generating and pumping water, respectively.
CO
2-related costs include the cost of carbon sequestration and the cost of VPP participation in carbon trading.
where
is the fixed price for a unit mass of CO
2 sequestered, CNY/t.
is the unit carbon price in the carbon trading market, CNY/t.
is the amount of carbon sequestered at time
t, t.
is the net carbon emission of VPP at time
t, t.
is the carbon emission allowance allocated to VPP in time period
t, t.
is the carbon emission benchmark credit per unit of electricity, t/(MW·h).
- (5)
Green certificate trading revenue.
where
is the unit price of green certificate, CNY/book (green certificate power conversion is 1 green certificate = 1 MW·h).
is the amount of renewable energy generation consumed by VPP in time period
t, MW·h.
is the weight of renewable energy consumption of VPP in time period
t, MW·h.
is the length of the period when VPP is currently involved in green certificate trading.
- (6)
Operation and maintenance costs of wind and photovoltaic power generation.
where
and
are the unit operation and maintenance cost coefficients for wind power and photovoltaic power generation, respectively, CNY/(MW·h).
and
are the energy captured by wind power and photovoltaic power for the carbon capture system, respectively, MW.
and
are the energy consumption provided by wind power and photovoltaic power for power-to-gas equipment, respectively, MW.
and
are the grid-connected power for wind power and photovoltaic power, respectively, MW.
- (7)
Penalty cost for wind and photovoltaic power generation.
where
and
are the penalty cost per unit of wind power abandonment and the penalty cost per unit of photovoltaic power abandonment, respectively, CNY/(MW·h).
and
are the predicted power of wind power and photovoltaic power generation at time
t, respectively, MW.
and
are the grid-connected power of wind power and photovoltaic power respectively, MW.
- (8)
Cost of VPP to purchase electricity from the main network.
When power is in short supply, VPP can purchase power to meet internal power load demand.
where
is the purchased electricity price for time period
t, CNY/(MW·h).
is the amount of electricity purchased from the grid by VPP in time period
t, MW·h.
3.2.2. Constraints
The key of the VPP optimal dispatch model is to optimize the output of each piece of equipment within the permissible range under the premise of ensuring the balance between the VPP aggregation energy and load demand with the goal of economy. The most complicated part of the model is the operating constraints of the equipment.
- (1)
System power balance constraint.
First of all, it is necessary to ensure that the VPP aggregation energy is equal to the load demand, i.e., the power is conserved.
where
is the load demand of VPP at time
t, MW.
- (2)
Carbon capture unit operating constraint.
The operation of a carbon capture plant includes two parts of constraints: the carbon capture unit and the carbon capture system. Among them, the operation constraints of the carbon capture unit are the same as those of the conventional unit, including the output range, the climb limit, and the internal power balance of the carbon capture plant. This is shown in the following equation:
where
and
are the lower and upper limits of carbon capture unit output, respectively, MW.
and
are the energy consumption provided by the carbon capture unit to the carbon capture system at time
t and the net output of the carbon capture unit at time
t, respectively, MW.
The carbon capture unit is converted from a fuel unit so its operating upper and lower limit constraints and climbing constraints are similar to those of the fuel unit. The difference is that a carbon capture system is added to the fuel unit and the energy consumption constraint and operation constraint of the carbon capture system need to be considered.
where
is the equivalent output of the carbon capture unit at time
t − 1, MW.
is the climbing rate constraint of carbon capture unit output, MW.
and
are the fixed and operational energy consumption of the carbon capture system, respectively, MW.
is the total energy consumption of the carbon capture system at time
t, MW.
is the maximum energy consumption of the carbon capture system at time
t, MW.
is the energy required to capture a unit of CO
2 by the carbon capture system, MW/t.
is the unit carbon emission intensity of the carbon capture unit, t/MW.
is the energy consumption provided to the carbon capture system by the pumped storage unit in the power generation condition at time
t, MW.
is the rate of climbing constraint on the energy consumption of the carbon capture system, MW.
is the amount of CO
2 captured by the carbon capture system at time
t, t.
- (3)
Power-to-gas equipment operating constraint.
CO2 captured by carbon capture systems can be avoided by carbon sequestration technology but the sequestration technology not only bears the high cost of long-distance transportation but also faces the risk of explosion and environmental hazards due to sequestration leakage. The use of P2G equipment to produce methane requires the consumption of CO2, a low-carbon emission reduction method that not only reduces CO2 emissions but also makes full use of renewable energy to provide energy for P2G equipment.
The relationship between the CO
2 consumed by the P2G equipment to produce methane at time t and its operational energy consumption is as follows:
where
is the amount of CO
2 consumed by the P2G equipment at time
t, t.
is the amount of CO
2 required to generate methane per unit power for the P2G equipment.
is the conversion efficiency of P2G equipment.
is the energy consumption of the P2G equipment at time
t, MW.
The volume of methane generated by the P2G plant at time
t is as follows:
where
is the calorific value of natural gas, taken as 39 MJ/m
3 [
19].
- (4)
Wind and photovoltaic power generation operational constraint.
where
and
are the predicted power of wind power and PV power at time
t, respectively, MW.
and
are the grid-connected power of wind power and photovoltaic power, respectively, MW. The grid-connected power is required to develop an optimal grid-connected plan under the premise of ensuring energy balance. Therefore, the grid-connected power of renewable energy sources at a given moment is less than the predicted power.
- (5)
Operational constraints for pumped storage.
The power limitations of pumped storage units in power generation and pumping conditions and the mutually exclusive relationship between the operating conditions of pumped storage units are expressed as follows:
where
is the equivalent output of the pumped storage unit at time
t, MW.
and
are the power generation and pumping power of pumped storage units at time
t, MW. Due to the abundant storage capacity of the lower water reservoir in pumped storage power plant, this article only restricts the storage capacity of the upper reservoir.
is the capacity of the upper reservoir for pumped storage power plant at time
t, m
3.
and
are the lower and upper limits of the upper reservoir capacity of pumped storage power plant, respectively. The initial storage capacity of the upper reservoir is
.
is the water loss rate.
and
are the average water volume and electricity conversion coefficient of pumped storage units under pumping and power generation conditions, respectively.
and
T are the time interval and total number of time periods within the operation cycle optimized for pumped storage unit, respectively.
3.3. Intraday Scheduling Model
The intraday scheduling model takes the day ahead scheduling plan as a reference. Rolling correction of the output of carbon capture units, energy consumption of carbon capture systems, pumping energy consumption and power generation of wind power, photovoltaic power generation, and pumped storage based on the 15 min–4 h ultra-short term prediction of wind power, photovoltaic power generation, and load, thus forming the intraday scheduling plan.
3.3.1. Objective Function
The daily scheduling model ignores the switching cost of pumped storage units. Each run solves a 4-h scheduling plan, with an execution time resolution of 15 min and a total cycle of 96 time periods. The objective function is as follows:
where
is the fuel cost for carbon capture plants at time
t.
is the operating cost of the P2G device at time
t. is the CO
2-related cost of the VPP at time
t.
is the gain from VPP’s participation in the green certificate transaction at time
t.
and
are the operation and maintenance costs of wind power and photovoltaic power generation at time
t, respectively.
is the penalty costs for wind power abandonment and photovoltaic power abandonment at time
t.
is the cost of electricity purchased from the grid by VPP at time
t.
3.3.2. Constraints
The difference between the constraints of the intraday scheduling model and the day ahead scheduling model is that the optimal time resolution is changed from 1 h to 15 min. The constraints that need to be changed in the intraday scheduling model are as follows:
where
,
, and
, respectively, represent the load demand, predicted power of wind, and photovoltaic power generation during the intraday scheduling phase during time period
t. The physical meaning of other variables is the same as that of the day ahead scheduling phase.
In addition, due to the change in scheduling resolution from 1 h to 15 min during the intraday phase, the output of the carbon capture plant, the energy consumption climbing constraints of the carbon capture system, and the calculation method of the capacity of the pumped storage upper reservoir also need to be adjusted accordingly.
In the formula, due to the different time resolutions between the day ahead and intraday scheduling stages, the energy consumption ramp response ability of the carbon capture unit and the carbon capture system cannot be significantly adjusted in a short period of time. In addition, the upper reservoir capacity and capacity constraints of pumped storage also need to be calculated at a time resolution of 15 min. Other constraints are the same as those in the day ahead scheduling phase, so they will not be repeated here.
3.4. Solving Process
The solution process of the low-carbon economic dispatch model for virtual power plants based on the collaborative utilization framework of pumped storage–carbon capture–power-to-gas proposed in this article is shown in
Figure 3. The model developed includes a nonlinear objective function, real numbers, and Boolean solution variables, which belong to the mixed-integer nonlinear programming problem that is linearized and optimized by the Cplex solver (Version is 12.8).
To analyze the collaborative utilization framework of the pumped storage–carbon capture–power-to-gas proposal in this article and the impact of multi-time scale scheduling strategies on the scheduling results of virtual power plants, the following four operating schemes are set:
S1: A low-carbon economic scheduling model for a virtual power plant with carbon capture and power-to-gas conversion, as the basic operating scenario;
S2: Introduce pumped storage units on the basis of S1 and establish a low-carbon economic dispatch model for a virtual power plant that includes pumped storage, carbon capture, and power-to-gas conversion, to study the impact of pumped storage on the dispatch results of virtual power plants;
S3: Low carbon economic dispatch of a virtual power plant based on the collaborative operation framework of pumped storage–carbon capture–power-to-gas, to study the linkage effect of various equipment under the collaborative operation strategy;
S4: Multi-time scale low-carbon economic scheduling of virtual power plant based on the collaborative operation framework of pumped storage–carbon capture–power-to-gas and the introduction of 50 MW·h energy storage power plant coordination in the intraday stage to study the impact of multi-time scale rolling optimization strategies on the short-term scheduling results of a virtual power plant.
5. Conclusions
In this paper, the pumped storage–carbon capture–power-to-gas synergistic operation framework is proposed to address the lack of flexible regulation in the joint operation mode of carbon capture plant and P2G equipment. Aiming at the volatility problem of uncertain resources, a multi-timescale low-carbon economic dispatch model for virtual power plants is established based on a multi-timescale rolling optimization strategy. The advantages of the proposed strategy and model are verified through arithmetic simulation and the following conclusions are drawn:
The pumped storage–carbon capture–power-to-gas synergistic operation framework realizes the synergistic complementarity of different aggregation units and the low-carbon economic operation of the VPP. Compared with the carbon capture-electricity-to-gas joint operation mode, the net cost of the virtual power plant is reduced by 126,300 CNY, the amount of renewable energy consumed is increased by 567.46 MW∙h, and the net carbon emission from the system is reduced by 92.7 t. It effectively improves the flexible regulation capability of the virtual power plant and promotes the low-carbon economic operation of the virtual power plant.
The multi-timescale rolling optimization strategy leverages the ability of CCS and P2G equipment energy consumption to track fluctuations in renewable energy. Compared with the day-ahead scheduling plan, the CO2 captured by the carbon capture system increased by 561.5 t and the net carbon emissions from the VPP decreased by 282.1 tons. In addition, the regulation depth of the PS was also tapped. Compared with the previous day’s scheduling plan, the total pumping energy consumption increases by 274.68 MW∙h and the total power generation increases by 190.38 MW∙h. The multi-timescale rolling optimization strategy is capable of correcting the energy flow in the framework of the synergistic operation of pumped storage–carbon capture–power-to-gas with a shorter temporal resolution based on renewable energy sources and the uncertainty of loads. The multi-timescale rolling optimization strategy can further take advantage of the refined scheduling of the pumped storage–carbon capture–power-to-gas synergistic operation framework.