| Literature DB >> 35310937 |
Mihrimah Ozkan1,2,3, Saswat Priyadarshi Nayak1, Anthony D Ruiz1, Wenmei Jiang1.
Abstract
Climate change calls for adaptation of negative emission technologies such as direct air capture (DAC) of carbon dioxide (CO2) to lower the global warming impacts of greenhouse gases. Recently, elevated global interests to the DAC technologies prompted implementation of new tax credits and new policies worldwide that motivated the existing DAC companies and prompted the startup boom. There are presently 19 DAC plants operating worldwide, capturing more than 0.01 Mt CO2/year. DAC active plants capturing in average 10,000 tons of CO2 annually are still in their infancy and are expensive. DAC technologies still need to improve in three areas: 1) Contactor, 2) Sorbent, and 3) Regeneration to drive down the costs. Technology-based economic development in all three areas are required to achieve <$100/ton of CO2 which makes DAC economically viable. Current DAC cost is about 2-6 times higher than the desired cost and depends highly on the source of energy used. In this review, we present the current status of commercial DAC technologies and elucidate the five pillars of technology including capture technologies, their energy demand, final costs, environmental impacts, and political support. We explain processing steps for liquid and solid carbon capture technologies and indicate their specific energy requirements. DAC capital and operational cost based on plant power energy sources, land and water needs of DAC are discussed in detail. At 0.01 Mt CO2/year capture capacity, DAC alone faces a challenge to meet the rates of carbon capture described in the goals of the Paris Agreement with 1.5-2°C of global warming. However, DAC may partially help to offset difficult to avoid annual emissions from concrete (∼8%), transportation (∼24%), iron-steel industry (∼11%), and wildfires (∼0.8%).Entities:
Keywords: Chemical engineering; Energy sustainability; Environmental technology; Mechanical engineering
Year: 2022 PMID: 35310937 PMCID: PMC8927912 DOI: 10.1016/j.isci.2022.103990
Source DB: PubMed Journal: iScience ISSN: 2589-0042
Figure 1CO2 captured from air using liquid and solid sorbent DAC plants, storage, and reuse
The ambient air is sucked in through large fans which is then treated with a chemical sorbent (Liquid or Solid) and heated to extract CO2. This CO2 is then either sequestrated or used in other industries as shown.
Figure 2The five pillars of direct air capture
Factors like carbon capture sorbent technology, electrical and thermal energy demand, cost, the environmental impact, and political support from different regimes affects the adoption of the DAC technology. These pillars need to be balanced well for the successful deployment of diverse DAC technologies.
Current DAC plants and future projects
| Company | Plant type/status | Location | CO2 removal capacity (metric tons/yr) | Sorbent type | Thermal energy source | Market application | Date of operation |
|---|---|---|---|---|---|---|---|
| Climeworks | 14 Pilot & Commercial Plants/Operational | Across Europe | Net: 2,000 | Solid | Geothermal,Waste heat etc. | Renewable fuels, food, beverages, and agriculture | 2015–2020 |
| Pilot plant/Operational | Kanton Zurich (Switzerland) | 900 | Solid | Waste Incineration ( | Greenhouse | 2017 | |
| 1 Commercial plant/Operational | Hellisheidi (Iceland) | 4,000 | Solid | Geothermal | CDR services - Microsoft, Shopify, Audi & Storage by mineralization | 2021 ( | |
| Carbon Engineering ( | Pilot plant/Operational | Squamish, British Columbia (Canada) | 350 | Liquid ( | Natural Gas ( | Carbon neutral Fuel | 2015 |
| Innovation center/Under construction | Squamish, British Columbia (Canada) | 1,500 | CO2 capture and storage for shopify and virgin | 2022 ( | |||
| Commercial plant/Under construction | Permian basin, Texas (USA) | 1,000,000 | Enhanced oil recovery and Carbon sequestration | Mid-2020s | |||
| Global Thermostat ( | Pilot plant (DAC + Flue)/Nonoperating | Menlo Park, California (USA) | 10,000 | Direct CO2 capture from air | Residual heat from Industry ( | Not for Commercial use | 2013 |
| Pilot plant/Nonoperating | Huntsville, Alabama (USA) | 4,000 | Not for Commercial use | 2019 | |||
| Pilot plant/planning | Magallanes (Chile) ( | 250 kg/h | Wind power | Synthetic Gasoline | 2022 ( | ||
| 2 Commercial plants /Under construction | Sapulpa, Oklahoma (USA) | 2,000 / Plant | Natural Gas ( | CO2 based fuel, CO2 as industrial gas | 2021 ( | ||
| Mechanical Tree | Prototype /Under construction | Arizona (USA) | 30 tons from a single tree | Moisture driven CO2 sorbents ( | None, Passive DAC | Agriculture, CO2 based fuel, Building materials, Sequestration | 2022-23 ( |
| Commercial Farms/Planning | Global | 4 million/Farm | Second Half of 2020s ( | ||||
| Infinitree | Pilot Plant/Operating | New York (USA) | 100 | Ion exchange sorbent material ( | Humidity Swing mechanism ( | Greenhouse application | 2014–2018 |
The table is adapted from reference (Lebling et al., 2021; The Commercial Case for Direct Air Capture of Carbon Dioxide, 2021).
Figure 3DAC and CCS plants around the globe
Green, Red, and Orange circles denote the operational status of the plants - Operating, Under Construction, or Planning, Nonoperating, respectively.
Figure 4Effect of industry growth rate on NET CO2 removal
(A) Net CO2 removal with varying industry growth rate (in % per year). The unmarked black line denotes the nominal growth rate (20% per year) and the varied growth rates are denoted with marked colored lines and labels.
(B) Percent change in net CO2 removal relative to the nominal case. Markers show the mean of all scenarios by year. The funding is from the club of democracies. (The Figure is taken from the reference (Hanna et al., 2021) with author's permission).
Figure 5DAC plant land area requirement
The left column represents Climeworks and the right column represents Carbon Engineering. Both of them require an area of 0.2 km2 per one million of CO2 removal for the given sorbent and thermal energy source combination.
Figure 6DAC technologies
(A) Liquid-Precipitate Cycle.
(B) Liquid Adsorbent.
(C) Solid Adsorbent Cycle. Steam and vacuum values in (C) are included in only one of their respective boxes. Not included in (B) are the energy requirements from recirculation pump and blower work, which gives the overall system an energy requirement of 5.23 GJ/tCO2 (Broehm et al., 2015; Kiani et al., 2020; National Academies of Sciences, 2018; Socolow et al., 2011).
Figure 7DAC cost breakdown and comparison
All systems are presented with data that assumes a plant with removal capacity of one MtCO2/year and a fixed charge factor of 12%.
(A) Liquid Solvent DAC Capital Cost with low and high range.
(B) Liquid Solvent DAC Operating Cost with low and high range.
(C) Solid Sorbent DAC Capital Cost with low, mid, and high range.
(D) Solid Sorbent DAC Operating Cost with low, mid, and high range. Low and high bounds are the result of the type of material used for a specific part, factoring in new technology, and varying costs from vendors (National Academies of Sciences, 2018).
Figure 8Energy requirements for solid and liquid DAC systems
‘Low’ is used for the lower range values, and ‘high’ is used for the higher range values. Values found from reference (Chatterjee and Huang, 2020; Kiani et al., 2020; Krekel et al., 2018; Luis, 2016; National Academies of Sciences, 2018; Realmonte et al., 2019; Rochelle et al., 2011).
Carbon footprint of DAC systems with respect to several energy sources
| Sorbent | Electricity | Heat | Carbon generated from heat (MtCO2/year) | Carbon generated from electricity (MtCO2/year) |
|---|---|---|---|---|
| Liquid | Solar | Natural Gas | 0.47–0.66 | 0.01–0.03 |
| Liquid | Wind | Natural Gas | 0.47–0.66 | 0.004–0.009 |
| Liquid | Nuclear | Natural Gas | 0.47–0.66 | 0.01–0.02 |
| Liquid | Natural Gas | Natural Gas | 0.47–0.66 | 0.11–0.23 |
| Liquid | Coal | Natural Gas | 0.47–0.66 | 0.18–0.38 |
| Solid | Solar | Solar | 0.008–0.01 | 0.0004–0.008 |
| Solid | Nuclear | Nuclear | 0.004–0.005 | 0.002–0.004 |
| Solid | Solar | Natural Gas | 0.22–0.30 | 0.0004–0.008 |
| Solid | Wind | Natural Gas | 0.22–0.30 | 0.002–0.003 |
| Solid | Natural Gas | Natural Gas | 0.22–0.30 | 0.07–0.14 |
| Solid | Coal | Coal | 0.32–0.44 | 0.15–0.3 |
Adapted from reference (National Academies of Sciences, 2018).
Environmental impacts of the construction for the engineered DAC plant and the future DAC plant according to the European Commission's Joint Research Center
| Environmental impacts | Engineered DAC plant | Future DAC plant | Unit |
|---|---|---|---|
| Climate change | 5.68 10−3 | 2.72 10−3 | Kg CO2e |
| Ozone depletion | 1.29 10−10 | 4.97 10−11 | Mole H+ equiv |
| Particulate matter | 2.69 10−10 | 1.06 10−10 | Disease incidences |
| Acidification, terrestrial, and freshwater | 1.93 10−5 | 7.49 10−6 | Kg CFC-11 equiv |
| Eutrophication, freshwater | 4.23 10−7 | 1.56 10−7 | Kg P equiv |
| Eutrophication, marine | 5.09 10−6 | 1.98 10−6 | Kg N equiv |
| Eutrophication, terrestrial | 5.63 10−5 | 2.19 10−5 | Mole N equiv |
| Ionizing radiation | 2.38 10−4 | 8.45 10−5 | kBq 235U equiv |
| Photochemical ozone formation | 1.60 10−5 | 6.22 10−6 | Kg NMVOC equiv |
| Human toxicity, cancer | 1.40 10−10 | 5.47 10−11 | CTUh |
| Human toxicity, noncancer | 6.25 10−10 | 2.44 10−10 | CTUh |
| Ecotoxicity, freshwater | 1.81 10−3 | 7.01 10−4 | CTUe |
| Land use | 2.23 10−2 | 7.99 10−3 | Pt |
| Water scarcity | 1.59 10−3 | 4.98 10−4 | m3 world equiv |
| Resource depletion, energy | 5.19 10−2 | 2.04 10−2 | MJ |
| Resource depletion, mineral, and metals | 2.87 10−8 | 1.00 10−6 | Kg Sb equiv |
Adapted from reference (Deutz and Bardow, 2021).