Installing a power-to-gas system at the wind power plant location opens the possibility for using produced electricity for green hydrogen production. The green hydrogen is then integrated into the gas grid via the injection station as a substitute for natural gas, thereby additionally influencing the acceleration of the energy transition. This method of production is attractive in the case of low electricity prices on the day-ahead market, but also in cases of congestion in the network when the production of the wind power plant should be limited. Therefore, green hydrogen is produced when electricity prices are low and when there is a need for production flexibility services.
The economic profitability model presented in this paper is designed in such a way that with the historical data of the wind power plant and data from the day-ahead market, it calculates how much of the future share of electricity production can be allocated to the power-to-gas system, without affecting the economy of operating the wind power plant. The results of the model provide answers to three key questions:
The model shows the concept of connecting the source of electricity with the gas system, so that mutually integrated systems depending on the electricity price and the optimization of the electrolyzer size, and the marginal price of electricity affect the green hydrogen production and the profitability of the production of the wind power plant.
3.1. Input Data for the Model
This paper presents an hourly price and electricity production breakdown based on which the electrolyzer size and the marginal price of electricity are calculated to align electricity and green hydrogen production. The horizon of the presented model is set to a period of 25 years (corresponding to the lifetime of the energy plant), and several key input variables (market price of electricity, natural gas, and emission units) subject to uncertainty are presented in sensitivity analysis scenarios.
Given that power-to-gas systems consist of several separate parts, the cost estimate and gas grid connection, i.e., the capital (CAPEX) and operating costs (OPEX) of the whole investment, are shown in
Table 1.
The total investment cost at the wind power plant site consists of the capital costs of the power-to-gas system and gas infrastructure construction, annual fixed and variable operating costs, and the annual cost of chemical water treatment. The total capital cost of the power-to-gas system and the construction of the gas infrastructure is calculated at the level of the entire life of the plant, i.e., the period of the model, while the rest of the costs are measured on an annual basis. Fixed plant operating costs represent costs that do not depend on system output, while variable costs include costs that vary depending on the system’s output.
For the individual CAPEX values used in the model according to the literature, they are adjusted for the specific location. Specifically, the CAPEX for the power-to-gas system is 1700.00 EUR/kW. However, in this case, it is additionally increased by the amount of gas grid connection as part of the overall investment. It should be considered that installing a power-to-gas system in a different location has different costs that make up CAPEX. For the investment case presented in this paper, CAPEX consists of parts of the power-to-gas system and the gas grid connection, i.e., the measuring-reduction station, which is also a hydrogen-injection station. OPEX is the market value of the produced electricity that was used for the green hydrogen production.
The model uses a PEM electrolyzer with a perfectly flexible behavior, i.e., in real time, it follows the variable supply of electricity and maintains a constant efficiency of 74%. The efficiency of the electrolyzer is taken from Fu et al. [
29] who applied an efficiency of 74%, which is in line with the achievements and progress of water electrolysis technologies [
29]. It is assumed that large-scale PEM electrolyzer cost reductions should occur soon, so an amount that supports such a prediction is taken for this study. In terms of flexibility, the PEM electrolyzer technology has the most favorable characteristics and is, therefore, the most suitable for solving variable electricity inputs [
12]. The total installed capacity of the electrolyzer must meet the high efficiency of green hydrogen production, that is, it must work at full capacity during the model’s predicted period.
Prices of electricity, natural gas, and CO
2 emissions were estimated on the European Ten-Year Electricity and Gas grid Development Plan (TYNDP 2022), according to the basic scenario of the European Network of Transmission System Operators, ENTSO-E, and the European Network of Transmission System Operators for Gas, ENTSOG [
32].
Table 2 shows estimated prices of electricity, natural gas, and CO
2 emissions, which were used in the model. Certain years were chosen to display prices, although the hourly electricity prices and annual prices of natural gas and CO
2 emissions were used in the model.
The forecast hourly electricity prices reflect the coefficients of the ratio of realized annual and hourly electricity prices on the day-ahead market for the historical five years, from 2018 to 2022, taken from the day-ahead market at CROPEX. The predicted hourly electricity production data were recalculated from the 15 min readings of the Zelengrad wind power plant production for the historical six years, from 2017 to 2022, taken from the report of the Croatian Energy Regulatory Agency [
33].
Additionally, an assessment of the value of the power-to-gas system, together with the gas connection, were performed as the overall investment required for green hydrogen production at the wind power plant location. Since the model includes hourly input variable data for all 25 years, all parts of the model are complex and require a significant amount of data and formulas. In this study, a PEM electrolyzer was chosen for hydrogen production using water electrolysis. To calculate the size of the required electrolyzer, the selected operating hours of the wind power plant were optimized to maximize its utilization. The electrolyzer cannot be of the same size as the wind power plant, given that it does not operate at full capacity throughout the year. Therefore, the capacity of the electrolyzer is optimized to avoid excessive investment that would increase the hydrogen production price.
The application of Monte Carlo simulation to energy prices enables uncertainty modeling in such a way that the input variables are predicted through continuous probability density functions, which leads to a more realistic representation of the uncertainty of future price movements, based on collected historical data [
34]. In addition to the predicted hourly electricity prices, Monte Carlo simulation was also used for electricity production so that the distribution of historical years was more realistically displayed for the entire model period. When predicting electricity prices, each of the five historical years is allocated to model years in a given ratio, while when predicting electricity production, there is no such limitation. To overlook the price of electricity in the Monte Carlo simulation, a limit of 10% was taken for the year 2020 as a specific pandemic year that is considered less likely to recur, while other historical years had an equal proportion of recurrences. The year 2020, with such a restriction, was repeated twice within the 25-year period of the model.
When calculating the coefficients for forecasting electricity prices, a period of five years of realized electricity prices at the hourly level on the day-ahead market was taken, precisely for the sake of the visibility of electricity price oscillations. In this way, the ratio of higher and lower hourly electricity prices can be seen, that is, the influence of climate conditions or other specificities of the covered historical years. By displaying the hourly production of electricity, it is possible to see in which hours of the year the wind power plant produced at maximum installed capacity, reduced capacity, or did not produce.
The hourly display of the expected market price of electricity and the expected production of electricity for a period of 25 years is important when determining the marginal price of electricity. Within the annual hourly realizations of wind power plant production and hourly realizations of electricity prices, it is necessary to determine the breakeven price of electricity based on which green hydrogen or electricity will be produced. The marginal price of electricity is optimized for each model year. It represents the limit above which the wind power plant delivers the generated electricity to the power grid, and below which green hydrogen is produced from the generated electricity in the electrolyzer. Therefore, the hours of the year when the price of electricity is favorable are determined, at the same time considering the hours in which the production of electricity is high, thus optimizing the marginal price of electricity.
The size of the electrolyzer is determined according to the hourly electricity production of the wind power plant and the market price of electricity during those hours. First, the marginal price of electricity, below which hydrogen is produced and above which the wind power plant delivers the generated electricity to the power grid, was determined. The size of the electrolyzer is based on a certain optimized annual marginal value of production in such a way as to consider the total production of electricity below the level of the marginal price of electricity for 25 years. After that, the hourly production of the wind power plant was analyzed in the hours when the price of electricity was below the marginal price, and according to these hours of production, the optimal size of the electrolyzer was calculated using the Excel solver. With this optimal size of electrolyzer, the lowest production price of hydrogen was obtained. This was performed for each individual year of the model, and based on the results for each of 25 years, the size of the electrolyzer was determined, which was closest to the result for each year. According to the realized hourly production of the wind power plant and the expected hourly prices of electricity on the day-ahead market, the optimal size of the electrolyzer was calculated, which increased the economic value of the production of the wind power plant. Therefore, for choosing the size of the electrolyzer, it is important to predict the prices and production of electricity, i.e., the marginal price of electricity.
Part or all the electricity production when the price of electricity on the day-ahead market is lower than the marginal price of electricity was used for the green hydrogen production. The price of green hydrogen consists of the market value of electricity used for the production of green hydrogen, i.e., the variable part of the cost and fixed costs, taking into account the efficiency of the electrolyzer. Finally, the production price of green hydrogen was calculated as follows:
where
GHPPt: Green hydrogen production price in year t [EUR/MWh];
VHPt: Variable cost of hydrogen production in year t [EUR/MWh];
FHPt: Fixed cost of hydrogen production in year t [EUR/MWh].
Production price of green hydrogen is an annual sum of variable and fixed hydrogen production costs divided by annual hydrogen production for year t.
The component FHP
t is the capital expenditures of hydrogen production and is calculated as follows:
where
FHPt: Fixed cost of hydrogen production in year t [EUR/MWh];
ICt: Investment cost in year t [EUR];
GPCCt: Cost of connection to the gas pipeline in year t [EUR];
HPt: Annual hydrogen production in year t [MWh].
The fixed cost of hydrogen production is a sum of investment cost and the cost of connection to the gas pipeline on an annual basis divided by the hydrogen production in year t.
The component VHP
t is the operating expense of hydrogen production and is calculated as follows:
where
VHPt: Variable cost of hydrogen production in year t [EUR/MWh];
EHPt: Electricity consumed for hydrogen production in year t [MWh];
HEPEMt: Hourly expected price of electricity on the market in year t [EUR/MWh];
MTCt: Maintenance cost in year t [EUR];
WOCt: Cost of water in year t [EUR];
HPt: Annual hydrogen production in year t [MWh].
The variable cost of hydrogen production is a sum of electricity consumed for hydrogen production, hourly expected price of electricity on the market, maintenance cost, and cost of water divided by the hydrogen production in year t.
To be able to calculate the profitability of the production of green hydrogen, it is necessary to calculate the income from the produced amount of green hydrogen, which is calculated according to the price of natural gas. The income from the produced amount of green hydrogen is calculated as follows:
where
IGHPt: Income from produced green hydrogen in year t [EUR];
PNGt: Price of natural gas in year t [EUR/MWh];
PCO2t: Price of CO2 emissions in year t [EUR/t];
HPt: Hydrogen production in year t [MWh].
The income from produced green hydrogen is calculated with the price of natural gas that is multiplied by hydrogen production, after which the CO2 emissions cost’s equivalent is added. The amount of 0.20196 is multiplied by the price of CO2 emissions per ton and by the hydrogen production because green hydrogen can be sold at the natural gas price increased by the price of CO2 emissions and still be competitive to natural gas.
The market value of electricity used to produce green hydrogen is calculated as follows:
where
MEHPt: Market value of electricity used for hydrogen production in year t [EUR];
HEPEMt: Hourly expected price of electricity on the market in year t [EUR/MWh];
EHPt: Electricity consumed for hydrogen production in year t [MWh].
The market value of electricity used for hydrogen production is the product of the hourly expected price of electricity on the market and electricity consumed for hydrogen production. The amount of the required premium subsidy for green hydrogen production is calculated as follows:
where
St: Required premium subsidy in year t [EUR/MWh];
MEHPt: Market value of electricity used for hydrogen production in year t [EUR];
IGHPt: Income from produced green hydrogen in year t [EUR];
HPt: Hydrogen production in year t [MWh].
The required subsidy is calculated as the difference between the market value of electricity used for hydrogen production and the income from the produced green hydrogen divided by the hydrogen production. If the income from the produced green hydrogen is greater than the market value of electricity used for hydrogen production, no premium subsidy is required.
The market value of electricity delivered to the grid is calculated as follows:
where
MVDGt: Market value of electricity delivered to the grid in year t [EUR];
HEPEMt: Hourly expected price of electricity on the market in year t [EUR/MWh];
EPGt: Electricity delivered to the grid in year t [MWh].
The market value of electricity delivered to the grid is the product of the hourly expected price of electricity on the market and electricity delivered to the grid.
The levelized cost of hydrogen (LCOH) is a widely accepted standard for assessing and comparing energy technologies [
35]. LCOH is a sum of total CAPEX and OPEX divided by the amount of produced hydrogen. LCOH was calculated for the basic scenario as well as for all sensitivity scenarios. The formula for levelized cost of hydrogen is as follows:
where
LCOH: The levelized cost of hydrogen [EUR/MWh];
n: Lifetime of power-to-gas system;
FHPt: Fixed cost of hydrogen production in year t [EUR/MWh];
VHPt: Variable cost of hydrogen production in year t [EUR/MWh];
HPt: Annual hydrogen production in year t [MWh];
d: Discount factor [%].
The rate of the discount factor was adopted from the authors Jovan and Dolanc [
36], who used a discount factor of 5%, which we consider applicable in our scenarios as well. The fixed cost of hydrogen production was calculated as the sum of fixed costs, which represent costs that do not depend on system output and include costs of power-to-gas system, gas grid connection costs, and hydrogen injection station costs. The variable cost of hydrogen production was calculated using costs that vary depending on the system’s output, such as the market value of the produced electricity that was used for the green hydrogen production, electrolyzer maintenance costs, and water costs.
3.2. Structure of the Model
The structure of the economic model shown in
Figure 1 illustrates the way in which the proposed model works.
Depending on the production of the wind power plant and the market price of electricity, the marginal price of electricity is determined, which, along with the type and capacity of the newly installed power-to-gas system, is a decision variable in green hydrogen production. With a positive decision, the green hydrogen production technology is implemented in the power-to-gas system via a PEM electrolyzer that separates water molecules into hydrogen and oxygen. Oxygen is released into the atmosphere while green hydrogen is injected into the gas grid. With a negative decision, green hydrogen is not produced, but the produced electricity from the wind power plant is transferred to the power grid.
Based on data on existing wind power plants in the Republic of Croatia, location, year of construction, installed capacity, and production curve, the Zelengrad wind power plant was selected; its data were used as input parameters of the model, and the model results were applied to it. The input parameters of the price and production of electricity are based on historical data, but their predictions of future trends are an uncertain part of this model. The inclusion of this uncertainty through the change of input variables in the scenario sensitivity analysis results in the basis needed for making an investment decision or providing incentives for investing in green hydrogen production technology at the wind power plant location.
The authors are aware of the following limitations of the model:
Predicted price movements of electricity, natural gas, and CO2 emissions;
Predicted trends in electricity production;
Determination of low electricity prices, i.e., marginal price of electricity;
Optimum electrolyzer size to achieve high efficiency;
Accessibility or distance of the gas grid to the renewable energy source.
The output variables of the model are the annual cost of the production price of green hydrogen, the annual consumption of electricity for the green hydrogen production, the capacity of the electrolyzer, the capital and operational cost of the investment, the cost of the chemical preparation of water, and the amount of produced green hydrogen. Based on the amount of produced hydrogen that is injected into the gas grid, the amount of CO2 emissions is also calculated, which is, thereby, reduced.