During this study, it was used SimaPro software, for accounting the materials, energy needs, and environmental impacts during the construction and operation of a DAC plant in Ireland. The DAC process used for this study is based on the Climeworks plant: Temperature-Vacuum Swing Adsorption. This analysis is difficult to perform because of the data confidentiality from this emerging technology. Yet, we followed the methodology and guidance from Terlouw to expose our case (Terlouw, Treyer, et al., 2021). The authors made assumptions to approximate the impacts from the construction of the DAC plant: CO2 collectors, process unit, steel tanks and a maintenance hall, for control the process.
Collector boxes are made of plastic, steel, insulation, and fan, which is remarkably similar to the LCI of a passenger vehicle (Van Der Giesen et al., 2017). Thus, we used their approximation, and a 1200 kg compact size petrol/natural gas car was selected as a proxy for the collectors. As stated by Climeworks, 80 collector boxes can capture 4 ktCO2 per year in the plant at Iceland (Climeworks, 2021). The width, height and length of each collector is 2 meters (Climeworks, 2022c). Therefore, the total volume of the collector boxes is 640 m3, with a density of 110 kg/m3.
As well as the collectors, a passenger vehicle is used as an approximation for the process unit. A DAC unit comprises two containers (each container has 9 collector boxes), with a length of 12 meters and a width and height of 2 meters. The total volume of the process unit is estimated to be 50 m3. ORCA’s DAC plant needs 9 process units with a volume of 450 m3 to capture 4 ktCO2 per year (Climeworks, 2021). Moreover, it is necessary one steel tank with a diameter, height, and thickness of 2 meters, 6 meters and 0.02 meters correspondingly per 18 collector boxes.
For the foundations of the plant, it is required to transform the grassland into an industrial area and cover it with concrete (Viebahn et al., 2019). As stated by Climeworks, 90 m2 are needed for the DAC plant at Hinwil (Climeworks, 2022a). Terlouw et al., linearly scale the land use for the ORCA plant and for the future 100 kt plant (Terlouw, Treyer, et al., 2021). They concluded that a concrete layer of 400 m2 and 5000 m2 with a thickness of 1 meter is necessary for the 4 ktco2 and 100 ktco2 plants -Figure 1-. Then, the concrete should be reinforced with 120 kg steel/ m3 (Deutz & Bardow, 2021).
The dimensions of the maintenance hall are unclear (Viebahn et al., 2019). Yet, Terlouw et al. estimated that the building should occupy 75% of the total surface area. All these figures were compared with the data from Climeworks and Terlouw and further scaled for our megaton-capacity plant.
As with many other industrial processes, the operation of a DAC plant will be affected by the energy source. In order to evaluate the climate change impacts, we utilised the EF 3.0 Method, which includes the Global Warming Potential to 100 years (GWP100) as an indicative factor (European Commission, 2013). This study aims to address the kg of CO2 emitted per ton of CO2 removed during the construction, operation, and storage of the process. We proposed different three thresholds to address the efficiency of the process: 25%, 50% and 75%.
Near Ireland, there are potential geological storage locations for CO2 with a quantified capacity to store 93,115 MtCO2, from which 1,505 MtCO2 are practical (Lewis et al., 2009; SEAI, 2008). This study considered the depleted gas field at Kinsale, which was used as gas storage in the past years (Gas networks Ireland, 2020). This is a suitable place for storing the CO2 from DAC in the near term. Moreover, Corrib gas field will soon be exhausted in the coming years, which is a problem for the national energy security but a window of opportunity in the future to boost DAC industry (Casaban & Tsalaporta, 2022; Department of Environment, 2022). The risk for storage of the CO2 have been widely discussed before (Jonathan O’Callaghan, 2018). In 2026, Scotland is going to open the first DAC plant with a megaton capacity (Matt McGrath, 2021). Although the plant is based on an absorption process, it is not unreasonable to think that solid sorbent DAC plants will reach this capacity in the near future. Thus, we set that our plant has a capacity to remove 1 MtCO2 per year. Different locations and distances were studied for a future plant: Kinsale, Tipperary Wexford, Dublin, Castlebar, Donegal.
Table 1
Characteristics from some of the practical and effective storage basin locations in Ireland
Site name
|
Location
|
Storage type
|
Status
|
Storage capacity (MtCO2)
|
Reservoir type
|
Reservoir depth (m)
|
Kinsale
|
Celtic Sea Basin
|
Gas field
|
Depleted
|
350
|
Triassic sandstone
|
800
|
Spanish Point
|
Porcupine Basin
|
Gas field
|
Depleted
|
120
|
Jurassic Voligian Sandstones
|
-
|
Corrib
|
Northwest Basin
|
Gas field
|
Operational
|
6950
|
Lower Cretaceous sandstone
|
2000
|
Ormskirk Formation
|
Irish Sea Basin
|
Aquifer
|
-
|
630
|
Triassic sandstone
|
900
|
East Irish Sea
|
Irish Sea Basin
|
Oil & Gas field
|
Depleted
|
1050
|
Triassic sandstone
|
900
|
Kish Bank
|
Irish Sea Basin
|
Aquifer
|
-
|
267
|
Sherwood Sandstone
|
1750
|
Lough Neagh
|
Northern Ireland
|
Aquifer
|
-
|
1940
|
Sherwood Sandstone
|
1300
|
According to Climeworks, their plant requires of 500 kWh of electricity and 1500 kWh of heat to operate (Climeworks, 2022a). However, recent studies suggested that in the near future, the improvement of the process will reduce the energy needs to 444 kWh of electricity and 1333 kWh of heat per ton of CO2 captured -Figure 2- (Hanna et al., 2021). In order to meet the heat demands, we assumed that the energy needed for the process can come from the chemical industry or waste incineration plants, as for example, the one at Dublin (Elsam, 2006). In 2020, 3.2 million tonnes of municipal waste were generated and 41% were transformed into energy (EPA, 2023). With reliable access to a source of waste heat, the emissions and the environmental impacts will be markedly reduced (Fasihi et al., 2016). Energy from a natural gas plant and wind energy wind plant have been used as proxies for setting the three different scenarios. These scenarios are based on the future development plans of the island (National Development Plan 2021–2030, 2021).
-
Scenario 1: 55% of the energy comes from fossil origin and 45% from renewable.
-
Scenario 2: 30% of the energy comes from fossil origin and 70% from renewable.
-
Scenario 3: 5% of the energy comes from fossil origin and 95% from renewable.
Climeworks currently have an operation plant at Switzerland with a capacity to capture 4 kt of CO2 per year (Climeworks, 2021). Following the procedure by Terlouw et al., we verified the LCI for a 4 kt plant, and further scale it to our megaton plant. Future installations will not need enormous amounts of materials and land use due to advances in the field: better techniques or new sorbents (Sanz-Pérez et al., 2016).
According to Hendriks et al. (Chris & Wina, 2004), there is a method to estimate the energy needs for the injection step. To transport the CO2, the gas should be compressed from 1 bar to 110 bar in a four-step centrifugal compression (Musardo et al., 2013). If the capacity of the plant is of about 1 MtCO2 per year with a Flh value of 8160, the mass flow of the process is 34 kgCO2/s or 122.4 tCO2/h. All of these parameters are considered in Eq. 1, where Ce is a constant with a value of 87.85 kj/kg.
\(E={C}_{el}*ln\left(\frac{{P}_{outlet}}{{P}_{inlet}}\right)*F\)
|
Equation 1
|
The results showed that 115 kWh of energy are required for the combined compression stages. Furthermore, an additional input of 12 kWh are necessary to inject the CO2 to at least 2000 meters underground. Therefore, the total input of energy from the transport and storage process is around 130 kWh per ton of CO2 removed. This energy will be met depending on the different sources of energy according to the established scenarios.
As well as Terlouw (Terlouw, Treyer, et al., 2021), we considered the fugitive emissions of CO2 during its transport inside of the pipelines (medium baseline). Holloway et al. developed a method to estimate the loss of CO2 during its transmission (Holloway et al., 2006). According to the authors, the CO2 emissions rate is 1.66 times the CH4-emission rate. Thus, this rate should be multiplied by the yearly distribution emission factor of CH4 (Carras Pamela M Franklin et al., 2006). By applying this method, we estimated the losses of CO2 for the different DAC plants on the island (Table 2). The maximum depth of Kinsale gas field is 1000 meters whereas Corrib can reach 3000 meters (Table 1). Storage depth around 2000 meters do not affect to the LCA (Institut & Volkart, 2013). Therefore, the CO2 leakage from the injection wells is insignificant at Kinsale (Kelemen et al., 2019).
Table 2
Leakage emissions from transporting CO2 to Kinsale and Corrib via pipeline.
DAC plant
|
Distance to Kinsale
|
Distance to Corrib
|
Leakage to Kinsale
|
Leakage to Corrib
|
gas field (km)
|
gas field (km)
|
gas field (kgCO2)
|
gas field (kgCO2)
|
Castlebar
|
316
|
128
|
45
|
18.23
|
Donegal
|
393
|
195
|
55.96
|
27.77
|
Dublin
|
260
|
323
|
37.02
|
46
|
Kinsale
|
74
|
336
|
10.54
|
47.85
|
Tipperary
|
150
|
281
|
21.36
|
40.01
|
Wexford
|
171
|
377
|
24.35
|
53.69
|