A New Geographic Information System (GIS) Tool for Hydrogen Value Chain Planning Optimization: Application to Italian Highways
Abstract
:1. Introduction
2. Materials and Methods
2.1. The SuperP2G-Italy Tool
2.1.1. Overview: The Code and the Structure
2.1.2. Input Data
2.1.3. The Database
2.1.4. Data Elaboration
- Thanks to the high number of renewable plants, clustering techniques are applied to aggregate renewable power plants.
- Territorial meshing is performed to have homogeneous data for distance/costs computation and demand aggregation (only in specific use cases).
- Power and gas/fuel network geometry is manipulated.
- Other preprocessing operations assemble data from different sources (national open databases, administrative/statistical territorial information collections, GIS server for mapping, national infrastructure database).
- The clustering technique (density based, distance based, K-means) used for unsupervised learning.
- The mesh granularity to represent the analysed territory through a set of eligible P2G positions, one among which is selected as the best subset to minimize LCOH.
- The number of selected electrical networks to calculate distances for P2G connections (the presence of different nominal voltage/capacity networks may result in different costs).
- The technique to evaluate the distance from P2G plants to consumers (e.g., geodesic, routing), even if they can be adjusted to simplify calculations.
2.1.5. The Mathematical Optimization Model
2.1.6. The Optimization Solver
2.1.7. SuperP2G-Italy Limitations
- Approximation of continuous variables—the current version of the tool elaborates the data in a mesh in which size can be decided by the users. Therefore, a very fine mesh could be selected to resolve the problem. However, as for other nondeterministic class problems, the computational time increases, rapidly diminishing the size of the mesh.
- Geographical boundary conditions—in the current version, the tool calculated the best position for the plant without taking into account of any potential boundary constraints, such as hydrogeological ones, fire and earthquake risks, and reserve areas or forbidden areas.
- Complex cost models—the estimation of the P2H plants’ capital expenditure (CAPEX) and operational expenditure (OPEX) requires a complex cost function that depends on many parameters and boundary conditions, first of all the size. However, the introduction of too many restrictive constraints or complex cost models could determine an “infeasible” condition using (currently available) deterministic mathematical solvers requiring a simplified estimation.
2.2. Hydrogen Demand on Italian Highways
2.2.1. Italian Highways: Overview
2.2.2. Hydrogen Demand Estimation
- l = 1, 2, 3. Specifically, l = 1 for gasoline, l = 2 for diesel, and l = 3 for LPG.
- n = 1, 2. Specifically, n = 1 for 2030 and n = 2 for 2050.
- αn is the hydrogen penetration in the mobility sector assumed equal to 2% in 2030 and 15% in 2050 in accordance with [50].
- Vl is the annual amount of the lth fuel sold on Italian highways in 2030 and in 2050 [L/year].
- LHV is the low heating value of the fuel, and it is assumed equal to 31.8 MJ/L, 36.1 MJ/L, 25.5 MJ/L, and 120 MJ/kg, respectively, for gasoline, diesel, LPG, and hydrogen.
- k = 1, 2, …,75 is the number of Italian highways’ routes.
- H2,n,p is the estimated hydrogen demand in the kth route.
- Nn,p is the number of refuelling stations in the kth route that will be converted to hydrogen.
2.2.3. Scenario Definitions
- Hydrogen penetration—the parameters will depend on H2 penetration in the mobility market. As shown, in 2030 and 2050, a maximum penetration of 2% and 15%, respectively, is assumed.
- P2H plant nominal size—because there is a lower specific cost from increasing the nominal size, different plant sizes are investigated by the tool. As a preliminary assumption, a maximum P2H plant nominal size of 10 MW is considered for similar applications in 2030, while a high threshold and a low threshold, specifically 20 MW and 30 MW, respectively, are assumed for 2050.
- Baseline and optimized scenarios were investigated following the process from the previous section.
- A maximum daily distance covered by a truck was assumed to be equal to 200 km and 500 km.
#sim | Temporal Frame | P2H Plant Nominal Size [kW] | H2 [%] | Scenario | truck_km | |
---|---|---|---|---|---|---|
1 | Middle Term (2030) | (100, 300, 1000, 3000, 5000, 10,000) | 2 | base | 200 | |
2 | 2 | opt | ||||
3 | 2 | base | 500 | |||
4 | 2 | opt | ||||
5 | Long Term (2050) | (500, 1000, 3000, 5000, 10,000, 20,000, 30,000) | 15 | base | 200 | |
6 | 15 | opt | ||||
7 | 15 | base | 500 | |||
8 | 15 | opt |
3. Results
3.1. Hydrogen Demand on Italian Highways in 2030 and 2050
3.2. Scenario Analysis: 2030
3.3. Scenario Analysis: 2050
- The granularity of the P2G plants’ availability (i.e., the set of available nominal power/capacity values in the scale production).
4. Discussion
5. Conclusions
- An LCOH in the range from 5 to 8 €/kg, i.e., 0.042 to 0.067 €/MJ, was calculated for the eight scenarios. Therefore, according to the present purchase costs without incentives or other supporting strategies, hydrogen mobility would be less convenient than a traditional one, resulting in a barrier to market uptake.
- Several plants must cover the entire hydrogen demand in all the investigated scenarios. While the plants’ design would be not so critical, authorization procedures have to be lightened, reducing the complexity and the time required to complete a project. Additionally, efforts should be taken to improve the public’s understanding of hydrogen, increasing social acceptance and avoiding phenomena such as NIMBYism that could stop projects and increase the expected costs.
- To increase the competitiveness of hydrogen mobility, efforts should be performed in R&D to reduce the cost of plants and improve efficiency. In the first case, standardized modules with a predefined size should be designed, and the plant configuration should be optimized to minimize investment costs. To date, this market is more characterized by customization that increases the total cost. In the second case, research should address increases in efficiency or the use of low-grade energy. New designs of traditional electrolysers, the use of different materials, or the direct exploitation of solar irradiation are some of the potential actions that can be taken.
- The possibility to use continuous values of P2H plants’ nominal capacity rather than a discrete set of values.
- While in the existing version, the geodesic distance is used to approximate the length of the path between two locations, the exact road distance will be implemented, increasing the accuracy of the results.
- The possibility for users to design their plant configuration, deriving expected CAPEX and OPEX.
Author Contributions
Funding
Institutional Review Board Statement
Informed Consent Statement
Data Availability Statement
Conflicts of Interest
Appendix A
Appendix A.1. Hydrogen Transport Cost
- cij is the transport cost between the jth consumer and the ith P2G plant.
- Di,j is the distance between the jth consumer and the ith P2G plant, in km.
Source of cost | Value |
---|---|
CAPEX (truck + trailer) | 0.835 M€ (= 0.185 + 0.65) |
O and M | 12% CAPEX truck + 2% CAPEX trailer |
H2 conveyed by a truck | 300 kg |
Fuel consumption | 34.5 km/L |
Diesel cost | 1.4 €/L |
Personnel cost | 3185 €/month |
Daily operation | 8 h/day |
WACC | 8% |
Appendix A.2. P2G Plant’s Electrical Connection Costs
- Pi is the P2G electrical power, kW.
- Dik is the geodetic distance between the P2G plant and the nearest medium/low-voltage electric cabinet.
- D’’ik is the geodetic distance between the P2G plant and the nearest high voltage transformation cabinet.
Appendix A.3. P2G Plant’s CAPEX and OPEX
- Water electrolysis section—hydrogen is produced in this section by electrolysers. For the calculation, the PEM technology was assumed to be based on its greater flexibility with respect to the alkaline technology, even its higher CAPEX.
- Compression section—hydrogen is compressed up to 250 barg from a suction pressure of up to 30 barg. Two compressors are considered in the simplified configuration to maximize the availability of the plant.
- Storage section—hydrogen is assumed to be stored in AISI 316L Type I storage vessels.
- Refilling—hydrogen is filled in the truck in this section.
- CAPEXEL is the CAPEX of the electrolysis section [€].
- CAPEXCOMP is the CAPEX of the compression section [€].
- CAPEXSTORAGE is the CAPEX of the storage section [€].
- CAPEXFILLING is the CAPEX of the filling section [€].
- OTHER includes nonequipment and civil work costs that are required for the realization of the plant [€]. Particularly, nonequipment costs include (i) engineering costs, (ii) distributed control system (DCS) and energy management unit (EMU) installation costs, and (iii) interconnection, commissioning, and start-up costs.
- OPEXEL includes the following source of costs: electricity, O and M, water, and stack replacement.
- OPEXCOMP includes electricity and O and M.
- OPEXSTORAGE includes O and M costs.
- OPEXFILLING includes electricity and O and M.
- OTHER includes the P2G plant’s general O and M costs.
Source of Cost | Value |
---|---|
CAPEXEL | Pel < 700 kW: Pel ≥ 700 kW and Pel < 2000 kW: Pel ≥700 kW: where C0: 4000 €/kW; C0,1: 1000 €/kW; Pel,0: 100 kW; Pel,1: 700 kW; n = −0.37; a: 0.7 |
CAPEXCOMP CAPEXFILLING-GASEOUS | A: 100 [€], B: 300 [€], a: 0.66; b: 0.66; c: 0.25; d: 0.25—COMP A: 500 [€], B: 300 [€], a: 0.66; b: 0.66; c: 0.25; d: 0.25—COMP Q is the nominal flowrate [kg/h]; Qref is the reference flowrate equal to 50 kg/h; pdisc is the discharge pressure [bar], pin is the inlet pressure [bar], and pref is the reference pressure equal to 50 barg and 200 barg; and inflation and depreciation from 2017 are taken into account. |
CAPEXSTORAGE | 300 |
Cother | |
Electricity price | 75 €/MWh |
OPEX | Electrolyser: 2%, 3%, or 4% of the CAPEX for, respectively, Pel < 1000 kW, 1000 ≤Pel < 5000, and Pel> 5000 kW Compressors, storage; filling stations: 2% of CAPEX |
Electricity cost | 75 €/MWh |
Appendix A.4. Assumed Constraints
- Energy and mass conservation balances
- ○
- For each user/customer, the sum of the xij fractions must be 1;
- ○
- For each generator, the sum of x’ik must be lower than 1;
- ○
- The sum of hydrogen flows leaving each P2G plant must be lower than the plant capacity;
- ○
- The sum of the electrical power supply for each P2G plant must be lower than the plant capacity;
- ○
- The sum of hydrogen flows cannot be higher than the energy supplied (net of conversion efficiency coefficient).
- Market orientation/exploitation
- ○
- The P2G capacity nominal value belongs to a discrete set (to simulate a standardization of the plants for mass adoption/scaling economy).
- Distance and positioning limitations
- ○
- Each grid mesh centroid out of the considered territory was discarded as an eligible P2G position;
- ○
- As an option of the tool, the eligible P2G plant positions too far away from adequate (in terms of nominal voltage) electrical lines were neglected, owing to the hypothesis of relevant electrical connection costs;
- ○
- The case of hydrogen delivery by trucks was (for the sake of the completeness of the analysis) customized with the (optional) possibility to limit the trucks’ autonomy (i.e., routing distance).
Appendix A.5. Other Assumptions
- Meshing resolution—40 km2 mesh was adopted for the case study;
- P2G plant capacity sets—to estimate the importance of developing high-capacity electrolysers in the future (i.e., reduction of highest values of the set);
- Variable percentage of the aggregated fuel demand replaced with hydrogen equivalent;
- Maximum truck autonomy to reach users from P2G plants.
- Renewable energy generation—the overall PV production at NUTS-3 granularity (provincia in Italian). This is to exploit the current scenarios predicting continuous increments of RES plant penetration that can supply (along and beside the participation to the energy market) the conversion systems with a surplus (e.g., net of the possible consumption by priority loads) in production;
- On the demand side—the georeferenced information (position, fuel demand, association to specific motorways) of the refuelling devices on the Italian motorway network.
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Case | P2H Nominal Power [MW] | Number of Plants [-] | LCOH [€/kg] |
---|---|---|---|
1 | 293.6 | 105 | 7.46 |
2 | 208.0 | 83 | 7.98 |
3 | 295.7 | 81 | 7.02 |
4 | 205.0 | 52 | 6.93 |
Case | P2H Nominal Power [MW] | Number of Plants [-] | LCOH [€/kg] |
---|---|---|---|
5 | 2277.0 | 111 | 5.62 |
6 | 991.0 | 101 | 5.69 |
7 | 2231.5 | 100 | 5.63 |
8 | 1084.0 | 101 | 6.12 |
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Guzzini, A.; Brunaccini, G.; Aloisio, D.; Pellegrini, M.; Saccani, C.; Sergi, F. A New Geographic Information System (GIS) Tool for Hydrogen Value Chain Planning Optimization: Application to Italian Highways. Sustainability 2023, 15, 2080. https://doi.org/10.3390/su15032080
Guzzini A, Brunaccini G, Aloisio D, Pellegrini M, Saccani C, Sergi F. A New Geographic Information System (GIS) Tool for Hydrogen Value Chain Planning Optimization: Application to Italian Highways. Sustainability. 2023; 15(3):2080. https://doi.org/10.3390/su15032080
Chicago/Turabian StyleGuzzini, Alessandro, Giovanni Brunaccini, Davide Aloisio, Marco Pellegrini, Cesare Saccani, and Francesco Sergi. 2023. "A New Geographic Information System (GIS) Tool for Hydrogen Value Chain Planning Optimization: Application to Italian Highways" Sustainability 15, no. 3: 2080. https://doi.org/10.3390/su15032080
APA StyleGuzzini, A., Brunaccini, G., Aloisio, D., Pellegrini, M., Saccani, C., & Sergi, F. (2023). A New Geographic Information System (GIS) Tool for Hydrogen Value Chain Planning Optimization: Application to Italian Highways. Sustainability, 15(3), 2080. https://doi.org/10.3390/su15032080