Abstract:Prospective energy scenarios usually rely on Carbon Dioxide Removal (CDR) technologies to achieve the climate goals of the Paris Agreement. CDR technologies aim at removing CO2 from the atmosphere in a permanent way. However, the implementation of CDR technologies typically comes along with unintended environmental side-effects such as land transformation or water consumption. These need to be quantified before large-scale implementation of any CDR option by means of Life Cycle Assessment (LCA). Direct Air Car… Show more
“…Lower impacts than conventional diesel production and several biofuels are achieved, if and only if a low-carbon electricity source is used, as illustrated in Figure 9. Under the conditions detailed by Liu et al, 45 capturing ambient air CO 2 using a DAC technology and converting it to 43 Terlouw et al, 49 and Madhu et al, 47 synthetic fuel leads to carbon reduction if an electricity emissions factor lower than 0.37 kgCO 2 -eq per kWh is considered, compared with a case where CO 2 from a natural gas combined cycle power plant is captured and converted to synthetic fuel. Also, if the emissions intensity of the supply exceeds 0.14 kgCO 2 -eq per kWh, the climate change impacts of the DAC-based synthetic fuel will be worse than that of conventional diesel (see Figure 9).…”
Section: Overview Of Lca On Dacmentioning
confidence: 99%
“…Also, the economic costs and environmental impacts of DAC equipment, machinery, operations, and CO 2 disposal, including its use, should be assessed using a full cradle-to-grave approach, as stated by relevant literature. 49 These assessments should also include alternative evaluations of other pathways that achieve at least equivalent CO 2 reductions, such as BECCS and reforestation. There is a large dependency on the energy sources used for CO 2 capture.…”
Section: Recommendationsmentioning
confidence: 99%
“…Independent of the scenario, the investigated process effectively captures and stores CO 2 from the ambient air. The authors point out the large dependency on the energy sources used for the DAC system 49 . (9) Two scenarios were defined where the DAC system is powered by either coal‐fired power plants or a locally installed PV system.…”
Section: Review On Life Cycle Assessments (Lca) On Dacmentioning
confidence: 99%
“…LCA of DACCS system comprises the CO 2 storage stage, that is, the environmental impacts related to the infrastructure (eg, CO 2 compression stations and pipelines), the drilling of injection wells, and CO 2 leakage during the CO 2 transportation. Terlouw et al 49 proposed a comprehensive LCA of DACCS, based on Climeworks technology, including several processes needed for CO 2 storage and appropriate site location discussions. Deutz and Bardow 43 evaluate two commercial low‐temperature DACCS systems, operated by Climeworks, and the associated supply chains focusing mainly on the electricity demand for CO 2 injection.…”
Section: Review On Life Cycle Assessments (Lca) On Dacmentioning
confidence: 99%
“…Global warming potential of captured CO 2 from ambient air when including subsequent CO 2 storage, according to the carbon footprint of the electricity supply. Figure based on data from Deutz and Bardow, 43 Terlouw et al, 49 and Madhu et al, 47 using linear regression (see these references for more details related to the systems involved). BR, Brazil; CA, Canada; CH, Switzerland; CN, China; DE, Germany; ENTSO‐E, European energy mix; FR, France; Global, Global energy mix; IN, India; IS, Iceland; MX, Mexico; NG, natural gas; PL, Poland; PV, photovoltaics; UK, United Kingdom; USA, United States…”
Section: Review On Life Cycle Assessments (Lca) On Dacmentioning
To limit the increase of the global average temperature in the range of 1.5 C to 2 C above pre-industrial levels, it is mandatory to reduce anthropogenic CO 2 emissions. Aggressive mitigation measures are thus needed to tackle these emissions leading to "net negative CO 2 emissions." The present study focuses on direct air capture (DAC) processes among the diverse negative emissions approaches. DAC refers to man-made technologies that selectively extract CO 2 from ambient air and deliver it in a concentrated form for further use or storage. DAC technologies are currently developed at different levels of maturity and performance. They can be classified into three main approaches, the liquid sorbent approach, the solid sorbent approach, and a panel of more innovative technologies combining different approaches. They involve various unit operations and different materials and energy types (electrical and thermal). To better evaluate the status and both the environmental and economic performances, the present paper provides a literature review of the life cycle (LCA) and techno-economic (TEA) assessments in relation to DAC process chains. It was emphasized that DAC could lead to negative emissions if paired with subsequent storage, while the production of synthetic fuels can at best be carbon neutral when using CO 2 from the air. Building large DAC plants has an impact on the amount of energy required to operate them, as well as other environmental impacts with regard to land, water, and material use. Even if the carbon-negative characteristic of DAC was confirmed, these technologies are still expensive. It was highlighted that large DAC costs ranges are currently provided in the literature, from €80/tCO 2 to €1133/tCO 2 for the current DAC processes, while estimations from €34 to €260/tCO 2 are expected in the future.Different levers were identified to improve the environmental and economic performances of DAC processes, such as the availability of waste heat, the heat integration possibilities, and, among others, the improvement of contactors and sorbents properties.
Highlights• The paper entitled "Life cycle and techno-economic assessments of direct air capture processes: An integrated review," submitted by Dr Remi Chauvy and Dr Lionel Dubois, fills the current gap in terms of comprehensive
“…Lower impacts than conventional diesel production and several biofuels are achieved, if and only if a low-carbon electricity source is used, as illustrated in Figure 9. Under the conditions detailed by Liu et al, 45 capturing ambient air CO 2 using a DAC technology and converting it to 43 Terlouw et al, 49 and Madhu et al, 47 synthetic fuel leads to carbon reduction if an electricity emissions factor lower than 0.37 kgCO 2 -eq per kWh is considered, compared with a case where CO 2 from a natural gas combined cycle power plant is captured and converted to synthetic fuel. Also, if the emissions intensity of the supply exceeds 0.14 kgCO 2 -eq per kWh, the climate change impacts of the DAC-based synthetic fuel will be worse than that of conventional diesel (see Figure 9).…”
Section: Overview Of Lca On Dacmentioning
confidence: 99%
“…Also, the economic costs and environmental impacts of DAC equipment, machinery, operations, and CO 2 disposal, including its use, should be assessed using a full cradle-to-grave approach, as stated by relevant literature. 49 These assessments should also include alternative evaluations of other pathways that achieve at least equivalent CO 2 reductions, such as BECCS and reforestation. There is a large dependency on the energy sources used for CO 2 capture.…”
Section: Recommendationsmentioning
confidence: 99%
“…Independent of the scenario, the investigated process effectively captures and stores CO 2 from the ambient air. The authors point out the large dependency on the energy sources used for the DAC system 49 . (9) Two scenarios were defined where the DAC system is powered by either coal‐fired power plants or a locally installed PV system.…”
Section: Review On Life Cycle Assessments (Lca) On Dacmentioning
confidence: 99%
“…LCA of DACCS system comprises the CO 2 storage stage, that is, the environmental impacts related to the infrastructure (eg, CO 2 compression stations and pipelines), the drilling of injection wells, and CO 2 leakage during the CO 2 transportation. Terlouw et al 49 proposed a comprehensive LCA of DACCS, based on Climeworks technology, including several processes needed for CO 2 storage and appropriate site location discussions. Deutz and Bardow 43 evaluate two commercial low‐temperature DACCS systems, operated by Climeworks, and the associated supply chains focusing mainly on the electricity demand for CO 2 injection.…”
Section: Review On Life Cycle Assessments (Lca) On Dacmentioning
confidence: 99%
“…Global warming potential of captured CO 2 from ambient air when including subsequent CO 2 storage, according to the carbon footprint of the electricity supply. Figure based on data from Deutz and Bardow, 43 Terlouw et al, 49 and Madhu et al, 47 using linear regression (see these references for more details related to the systems involved). BR, Brazil; CA, Canada; CH, Switzerland; CN, China; DE, Germany; ENTSO‐E, European energy mix; FR, France; Global, Global energy mix; IN, India; IS, Iceland; MX, Mexico; NG, natural gas; PL, Poland; PV, photovoltaics; UK, United Kingdom; USA, United States…”
Section: Review On Life Cycle Assessments (Lca) On Dacmentioning
To limit the increase of the global average temperature in the range of 1.5 C to 2 C above pre-industrial levels, it is mandatory to reduce anthropogenic CO 2 emissions. Aggressive mitigation measures are thus needed to tackle these emissions leading to "net negative CO 2 emissions." The present study focuses on direct air capture (DAC) processes among the diverse negative emissions approaches. DAC refers to man-made technologies that selectively extract CO 2 from ambient air and deliver it in a concentrated form for further use or storage. DAC technologies are currently developed at different levels of maturity and performance. They can be classified into three main approaches, the liquid sorbent approach, the solid sorbent approach, and a panel of more innovative technologies combining different approaches. They involve various unit operations and different materials and energy types (electrical and thermal). To better evaluate the status and both the environmental and economic performances, the present paper provides a literature review of the life cycle (LCA) and techno-economic (TEA) assessments in relation to DAC process chains. It was emphasized that DAC could lead to negative emissions if paired with subsequent storage, while the production of synthetic fuels can at best be carbon neutral when using CO 2 from the air. Building large DAC plants has an impact on the amount of energy required to operate them, as well as other environmental impacts with regard to land, water, and material use. Even if the carbon-negative characteristic of DAC was confirmed, these technologies are still expensive. It was highlighted that large DAC costs ranges are currently provided in the literature, from €80/tCO 2 to €1133/tCO 2 for the current DAC processes, while estimations from €34 to €260/tCO 2 are expected in the future.Different levers were identified to improve the environmental and economic performances of DAC processes, such as the availability of waste heat, the heat integration possibilities, and, among others, the improvement of contactors and sorbents properties.
Highlights• The paper entitled "Life cycle and techno-economic assessments of direct air capture processes: An integrated review," submitted by Dr Remi Chauvy and Dr Lionel Dubois, fills the current gap in terms of comprehensive
In this work, the density, viscosity, and specific heat capacity of pure 1-dimethylamino-2-propanol (1DMA2P) as well as aqueous unloaded and CO 2 -loaded 1DMA2P solution (with a CO 2 loading of 0.04-0.70 mol CO 2 /mol amine) were measured over the 1DMA2P concentration range of 0.5-3.0 mol/L and temperature range of 293-323 K.The observed experimental results of these thermophysical properties of the 1DMA2P-H 2 O-CO 2 system were correlated using empirical models as well as artificial neural network (ANN) models (namely, back-propagation neural network [BPNN] and radial basis function neural network [RBFNN] models). It was found that the developed BPNN and RBFNN models could predict the experimental results of 1DMA2P-H 2 O-CO 2 better than correlations using empirical models. The results could be treated as one of the accurate and potential methods to predict the physical properties for aqueous amine CO 2 absorption systems.
In the present work, the kinetics of the reactive absorption of CO 2 in 1-dimethylamino-2-propanol (1DMA2P) solution were experimentally measured using a laminar jet absorber over a temperature range of 298-313 K, 1DMA2P concentration range of 0.5-2.0 mol/L, and CO 2 loading range of 0-0.06 mol CO 2 /mol amine. The measured kinetics data were then used to develop a comprehensive numerical kinetics model using a FEM-based COMSOL software. The reaction rate model of the CO 2 absorption into 1DMA2P solution were then validated by comparing model rates with the experimental rates. An excellent agreement of model data with experimental data was achieved with an absolute average deviation (AAD) of 6.5%. In addition, vapor-liquid equilibrium plots of all ions in the 1DMA2P-H 2 O-CO 2 system were also developed. Further, this work has provided an effective criterion for evaluating CO 2 absorption, that can be used for both the conventional amines and alternative amines for the purpose of providing guidelines or information on how to effectively screen solvents.
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