Submitted:
12 June 2025
Posted:
12 June 2025
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Abstract
Keywords:
1. Introduction
2. Methodology
3. Wind Power Potential
3.1. Comparing Characteristics Between Onshore Wind and Offshore Wind
3.2. Levelized Cost of Electricity of Onshore Wind and Offshore Wind
3.3. Additional Benefits and Technological Advancements in Offshore Wind
4. Why Hydrogen Is Useful
4.1. Hydrogen Production
4.2. Implementation of Green Hydrogen
5. Economics of Hydrogen
6. The New Zealand Context
6.1. Opportunities
6.1.1. Export
6.1.2. Storage
- Ammonia (material-based storage), as the costs of storing and transporting this chemical are much cheaper than storing H2 itself. However, there are significant efficiency losses associated with this process as electrolyzer generated hydrogen would be converted into ammonia, then back to hydrogen when it is needed for power generation [43]. Whilst electrolyzer energy losses could be as low as 25%, the conversion and reversion will increase energy losses to 59% [43]. Therefore, storage and transportation of hydrogen as ammonia may present higher costs relative to using a natural gas reservoir such as Ahuroa. Currently, NZ only has one ammonia-urea manufacturing plant located in Taranaki, converting atmospheric nitrogen and hydrogen into ammonia, then subsequently to urea, both of which still have carbon emissions due to natural gas usage in the process [33]. There is an established export market for ammonia, and it could be essential as a near-term means of storage and transportation as established processes make it easier for a transition into a hydrogen economy.
- Compressed H2, by using specific compressors and stored in tanks. The volume of hydrogen is almost four times as large as natural gas, therefore, H2 needs to be compressed for practical purposes [50]. Also, FCEV uses highly compressed hydrogen and therefore if this was the main end-user application, then it will be beneficial to have the gas compressed and stored in this form after production [50].
- Liquified H2, if further compression of the gas is required. The current Japan-Australia hydrogen supply chain tests are using liquified hydrogen as the carrier method for overseas shipment but the process of liquifying and storing it is very complex and costly. As mentioned above, hydrogen liquifies at -253°C and needs to be stored in insulated tanks for minimal temperature and evaporation losses [50]. Economies of scale may make liquefaction more feasible in the future.
6.2. Employment
6.3. Costs
- Service stations: For uses in fuel cell electric vehicles (FCEV), where high compression is needed, leading to double compression losses compared to bulk storage. This also includes service station overhead costs, similar to building a petrol station.
- Off-grid: Similar to the bulk storage case but avoids network costs as hydrogen is produced with an off-grid energy supply. A caveat to this, however, is that it will incur large storage costs and lower electrolyzer utilization factors. Lower utilization factors are due to the intermittent nature of renewable electricity supplied compared to using grid electricity, leading to larger capital recovery costs per kg of produced H2. In Figure 10, an assumed utilization factor for this scenario is based off solar generation which is much lower than that of offshore or onshore wind. Also, this scenario may lead to higher wholesale electricity costs if local renewable generation is not able to achieve the same economies of scale and grid generation. Currently, if we were to apply the cost of generating more MWs from offshore wind as the electricity cost variable, it would be uneconomical as offshore wind is very expensive. However, in the future if projections for lower offshore wind costs are to be realized, this method may become more cost effective, given the higher electrolyzer utilization factors associated with this type of renewable generation. Concept’s assessment, however, is that the cost effectiveness of off-grid method is only realized when the electricity network costs from connecting to the grid are higher than what is shown in Figure 11 [43].
- Grid-gen & gas-grid overlap: Similar scenario to Gas Tx injection, however, in this case the grid connected renewable energy generators are located close to a gas transmission line. Additionally, with an electrolyzer placed behind the renewable generation plant, incremental electricity network costs can be avoided. This scenario is cost effective and is evident as in Figure 10 this gives the lowest hydrogen production costs compared to the other scenarios. Possibilities for this method in NZ would be in, for example, Taranaki, where established gas transmission lines and potential for large renewable generation is in the same proximity.
- One study investigated the potential of green hydrogen production from wind-generated electricity in Pakistan using 660kW wind turbines and results concluded that production costs of green hydrogen were US$4.304/kg H2 (NZ$6.48), with supply costs withing a range of US$5.30-5.80kg/H2 (NZ$7.98-8.73) [55]. These estimates included costs such as CAPEX, storage, configuration, OPEX, water supply, and even considered the selling price of oxygen to offset some of the costs. They reported that at the four sites the examined in Pakistan, 10.5 tonnes/day of hydrogen can be produced, with potential for optimization in summer when country wide electricity demand is lower [55].
- A study conducted in Ireland looked specifically at offshore wind in their country with their case study comprising of a hypothetical 101.3 MW total capacity on Ireland’s East coast. Their model considers a specific type of electrolyzer (PEM), varying wind speeds in the area, electrolysis plant size, wind power out, and includes cost-effective underground means of storage. They concluded that the farm would be profitable at €5/kg H2 (NZ$8.48 [US$6.76]) (with all estimated variables using 2030 costs from various literatures), with underground storage potential ranging from 2 to 45 days with the latter becoming less economical due to the larger capital costs associated with underground storage [56].
7. Conclusions
Acknowledgments
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| Site | Generation Type [Capacity] | Geostorage Type | Potential use case |
|---|---|---|---|
| Manapouri | Hydro [850 MW] | Hard rock cavern | Dry-year storage |
| Ohai-Eastern Bush | Hydro [850 MW] | Sedimentary porous-media storage | Dry-year storage Domestic markets Export markets |
| Tiwai Point | Hydro [850 MW] | Hard rock cavern | Export markets Domestic markets |
| Waipipi | Wind [133 MW] | Sedimentary porous-media storage | Dry-year storage Domestic markets |
| Mokai | Geothermal [112 MW] | Volcanic porous-media storage | Domestic markets |
| Marsden Point | Solar [26.7] MW | Volcanic porous-media storage | Domestic markets Export markets |
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