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1 block diagram of PV and Hydrogen Hybrid power plant

1 block diagram of PV and Hydrogen Hybrid power plant

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The design of a PV-hydrogen gas turbine hybrid power plant is proposed to generate 100 MW electrical load. This electrical power is supplied directly from PV solar panels, and in the case of shortage or lack of solar radiation, it is supplied by a gas turbine power plant working on hydrogen fuel which is produced through using electrolysis of water...

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... Hydrogen GTs can be integrated into various energy systems to generate power. (Ebaid et al., 2015) conducted a study focusing on a novel energy system configuration comprising photovoltaic (PV) cells, an electrolyzer, a storage tank, and a hydrogen GT. The research explored two distinct scenarios: case (a) considered a worst-case scenario with minimal sunshine hours and solar radiation annually, while case (b) represented average sunshine hours and solar radiation throughout the year. ...
Chapter
Hydrogen (H2) is an energy carrier that offers both some of the benefits of fossil fuels and is clean with a low carbon footprint. Production of H2 from the water electrolysis using renewable energy is called green hydrogen and is the preferred pathway for future H2 production. In order to decarbonize the energy sector, green hydrogen must be adapted to existing systems using different technologies. Fuel cells, gas turbines (GTs), and combined heat and power (CHP) systems are the primary applications for hydrogen in power generation. CHP systems are highly efficient and can be employed in buildings, industrial facilities, and district energy systems to provide electrical and thermal energy. Heat pumps integrated with fuel cells are another example of energy-efficient technology. Mixing hydrogen in a specific volumetric ratio improves the resource utilization of the present natural gas heating systems. This chapter focuses on green hydrogen practices in electrical and thermal energy generation applications.
... Applicable methods for hydrogen production[28] Schematic of a PV-hydrogen hybrid system[34] ...
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Due to stricter carbon capture rules, a rise in demand for green energy, and attaining zero carbon emissions to attain the Paris Agreement in 2015 as well as the limited source of natural gas, the share of renewable energy sources like wind and solar is fast rising in our society. But also due to their erratic and fluctuating nature, dependable storage is required, in addition to extremely effective power cycles that can transform stored energy back into usable energy. In a hydrogenfueled power cycle, hydrogen can be created while energy levels are high, stored as a gas or liquid, and then converted back to energy when energy levels are low. Hydrogen is a promising energy carrier. To compete with fossil fuels and achieve a high round-trip efficiency from energy to hydrogen to energy, the power cycle must be extremely efficient. In this study, Aspen HYSYS (an oil and gas process simulator) has been used to simulate and assess a hydrogen-fueled power cycle comparable to a Joule-Brayton cycle (gas cycle) in a LM- 6000 gas turbine with five direct incidences of burning, the volume percentages of hydrogen (H2) in each example are 0%, 20%, 40%, 50%, and 100% in cases where the fuel is a mixture of natural gas and hydrogen fed by high-temperature electrolysis and the heat supply is 50 MW to GT. The project's objectives are to investigate the thermodynamics of the hydrogen cycle's essential parts and assess the cycle's efficiency, emissions, and economics. With NG-H2 mixture and excess air values ranging from 1 to 3, TIT = 1450 °C is reached at excess air values λ of 2.5 for NG-H2 mixture and 2.8 for 100% hydrogen fuel. While using hydrogen fuel instead of natural gas, CO2 emissions were reduced from 10194kg/h to 0 kg/h, and efficiency increased from 39.4% to 40.2. Speaking of efficiency improvement forced us to implement CCGT at TIT = 1450°C to increase the GT efficiency powered by hydrogen to 48.6%, where the temperature inlet the steam turbine is to 530°C. However, an assumption CCGTP to increase the efficiency by using the heat to heat the pumped water instead of going to condenser. Improve the efficiency by adding additional heat exchanger to increase the water pumped temperature, the efficiency become 49.43%. In this model, the separation is carried out under constant volume, pressure, and temperature. The hydrogen produced by high temperature electrolysis is fed by heated water and hydrogen at 750°C and 1 atm. Water to hydrogen ion feed system ratio is 9:1. The process requires 59 MW of heating, but a novel method is being used to reduce the electricity needed by adding a heat exchanger to heat the combination of H2O/H2 by the high temperature ofvi hydrogen produced by HTE before it is sent to the CCGTP. Where the source of electricity is renewable (solar PV and wind turbine) the study showed that adding H2 to natural gas up to 20% could result in a reduction in the amount of oxygen produced per hour, from 21167 to 20102 kg. The highest value of WNET steam cycle in when the mixture is 20% of hydrogen 4.3 MW in case of CCGT and 4.8 MW of CCGTP. An economic analysis demonstrated the OPEX cost (fuel, water, and power supplied) of each scenario, demonstrating that using complete hydrogen as a fuel is significantly less expensive than using natural gas by 58.09 USD/MWh in the case of electricity supplied by wind turbines and by 24.95 USD/MWh solar PV, respectively.
... Since the project has a time horizon of 22 years, a payback period of 13 years is targeted in the economic analysis. This is a value that is also mentioned in other projects involving hydrogen production and RES [141] [142]. ...
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... Because the project has a time horizon of 22 years, a payback period of 13 years is expected in the economic analysis, a value that is cited in other works involving hydrogen production and RES [30,31]. Regarding the different services/customers that the H 2 PP can provide, the following are detailed. ...
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... In this regard, the thermo-economic analysis of a hybrid power plant, combined photovoltaic (PV) and gas turbines, revealed that taking into account the worst-case scenario and the typical scenario, the average electricity price produced by these two scenarios are respectively 12 and 16 $ = kWh . Besides, the capital return period for these scenarios was 13 and 15 years, respectively (Ebaid, Hammad, and Alghamdi 2015). Sheikh et al. ...
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... turbines with flue gas recirculation [31]. The GTs that use hydrogen-containing fuels can be integrated Figure 5. Schematic of PV-hydrogen hybrid system [53]. ...
... The effect of working parameters on the exergy efficiency can be affected by the configuration of the system Ebaid et al. [53] Hydrogen The performance of a hybrid system, composed of hydrogen GT and solar PV was dependent on the design assumptions Cen et al. [54] Biomass and hydrogen Using hydrogen post-firing in the designed hybrid system leads to carbon dioxide emission reduction compared to natural gas. In another work [50], exergy analysis was performed on a GT using natural gas-hydrogen fuel in different ratios of hydrogen. ...
... Hydrogen GTs can be integrated with other energy systems for power generation [52]. In a study by Ebaid et al. [53], a new configuration composed of PV cell, electrolyzer, storage tank and hydrogen GT was proposed and investigated as shown in Figure 5. Two cases were considered for the design of this system: in case (a), known as a worst-case scenario, it was corresponded to the minimum sunshine hours and solar radiation during the year, while case (b) considers the average sunshine hours and solar radiation during the year. Based on their assumptions, a profit of 25% from the total initial cost and the generated electricity price for cases (a) and (b) were 0.12$/kWh and 0.16$/kWh, respectively. ...
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... They have reported that in a PEM water electrolysis system without separate post-electrolysis compression, the real hydrogen generation will be maximized by controlling the stack hydrogen exit pressure as close to the storage pressure as possible. Ebaid et al. [15] have designed a PV-hydrogen gas turbine hybrid power station to generate 100 MW electrical loads. It is reported that the cost of the electricity produced is 12 cent/kWh for average case scenario and 16 cent/kWh for the worst case scenario. ...
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... In 2014, Yilmaz and Kanoglu [5] investigated hydrogen production by PEM water electrolysis where the required power for PEM was produced by geothermal energy. In 2015, Ebaid et al. [13] thermoeconomically analyzed the coupling of photovoltaic cells with a hydrogen gas turbine hybrid power plant. In 2016, an integrated system with wind turbines and solar photovoltaic arrays was proposed by Khalid et al. [14] for production power and hydrogen. ...
... Therefore, the values of Ẇ grid and ṁ H2 increase (see, Eqs. (12) and (24)) and the values of C w and C H2 decrease (Eqs. (13) and (25)) by increasing of Col r . For example, Ẇ grid increases from 28,822 to 37829 kW (31.2% increasing) and C w decreases from 6.81 cents/kWh to 6.80 cents/kWh (0.15% decreasing) when Col r increases from 320 to 420. ...
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One of the most important methods for hydrogen production is proton exchange membrane electrolysis because of its low environmental impact and easy maintenance. In the present work, a proton exchange membrane electrolyzer system for hydrogen production is established where the required power is generated by a steam Rankine cycle. Solar energy is used for producing steam using parabolic trough solar collectors. The effect of active parameters such as inlet temperature and pressure of steam turbine, efficiencies of turbine and pump, the mass flow rate and outlet temperature of parabolic trough solar collectors, the number of solar collectors in rows, the electric current density, and proton exchange membrane temperature are investigated on the amount of hydrogen production, the net produced power, the cost of produced electricity, the produced hydrogen cost and net profit of the products. The results discovered that the average cost of electricity and the levelized cost of hydrogen per kg H2 decrease by increasing the steam turbine's inlet pressure and temperature. The cost of hydrogen is almost 6 $/kg at 8 MPa inlet pressure of a steam turbine. The profit increases with increasing the values of mass flow rate while the average cost of electricity and the levelized cost of hydrogen per kilogram of H2 decrease when mass flow rate increases. The value of profit increases 43.1% when the outlet temperature of oil in the receiver increases from 313 °C to 333°C .
... However, both studies only considered a natural gas-based operation of gas turbines. In contrast, Ebaid et al. conducted a model-based analysis of the operation of a 100MW el photovoltaic and hydrogen-fired gas turbine power plant [26]. Similarly, Colbertaldo et al. analyzed the potential of employing hydrogen-fired combined cycle power plants to balance electricity grids with a high share of RPG [27]. ...
... The optimized operational management based on DP aims to produce the same amount of CO 2 -neutral hydrogen as the RB operational management. 26 Consequently, the final state constraint of the considered optimal control problem corresponds to the maximum allowable pressure of the storage vessels. To comply with this final state constraint, the optimized operational management foresees the displayed operation of the electrolyzer between 2 p.m. and 5 p.m. and between 8 p.m. and 12 a. ...
... However, Fig. 8 also highlights that the utilized potential for optimization mainly derives from the fact that the operating time of the electrolyzer is limited by the available hydrogen storage capacity. As 6. RB unit commitment during exemplary period B. 26 As mentioned in Sec. 5.1, the exemplary period A corresponds to a weekend day. ...
Article
Hydrogen-based energy storage has the potential to compensate for the volatility of renewable power generation in energy systems with a high renewable penetration. The operation of these storage facilities can be optimized using automated energy management systems. This work presents a Reinforcement Learning-based energy management approach in the context of CO2-neutral hydrogen production and storage for an industrial combined heat and power application. The economic performance of the presented approach is compared to a rule-based energy management strategy as a lower benchmark and a Dynamic Programming-based unit commitment as an upper benchmark. The comparative analysis highlights both the potential benefits and drawbacks of the implemented Reinforcement Learning approach. The simulation results indicate a promising potential of Reinforcement Learning-based algorithms for hydrogen production planning, outperforming the lower benchmark. Furthermore, a novel approach in the scientific literature demonstrates that including energy and price forecasts in the Reinforcement Learning observation space significantly improves optimization results and allows the algorithm to take variable prices into account. An unresolved challenge, however, is balancing multiple conflicting objectives in a setting with few degrees of freedom. As a result, no parameterization of the reward function could be found that fully satisfied all predefined targets, highlighting one of the major challenges for Reinforcement Learning -based energy management algorithms to overcome.
... Hydrogen is the most abundant element and an environmentally benign energy carrier and is considered a promising material for energy storage [6]. The specific energy of hydrogen is 143 MJ, which is higher than any common fuel by weight and around three times larger than liquid hydrocarbon fuels [7]. ...
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Power generation and its storage using solar energy and hydrogen energy systems is a promising approach to overcome serious challenges associated with fossil fuel-based power plants. In this study, an exergoeconomic model is developed to analyze a direct steam solar tower-hydrogen gas turbine power plant under different operating conditions. An on-grid solar power plant integrated with a hydrogen storage system composed of an electrolyser, hydrogen gas turbine and fuel cell is considered. When solar energy is not available, electrical power is generated by the gas turbine and the fuel cell utilizing the hydrogen produced by the electrolyser. The effects of different working parameters on the cycle performance during charging and discharging processes are investigated using thermodynamic analysis. The results indicate that increasing the solar irradiation by 36%, leads to 13% increase in the exergy efficiency of the cycle. Moreover, the mass flow rate of the heat transfer fluid in solar system has a considerable effect on the exergy cost of output power. Solar tower has the highest exergy destruction and capital investment cost. The highest exergoeconomic factor for the integrated cycle is 60.94%. The steam turbine and PEM electrolyser have the highest share of exergoeconomic factor i.e., 80.4% and 50%, respectively.