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Removing Carbon
This piece will dive deeper into direct air capture and the “sponge” like technologies that remove carbon from the atmosphere. And to start, I’d like to take one giant step back.
Ambient air must come in context with the solid sorbent or liquid solvent for the chemistry to occur. This seems obvious, and it is, but it is a critical energetic step in the process. There is a considerable amount of variation within the space.
Climeworks “sucks” the air into the contactor through a fan like the picture below. We can think of this more as an active process.
This model can regulate and modulate the amount of air taken in; however, it does use more electricity than passive air contactors. Depending on the scale, this difference can be in the millions of dollars.
Passive contacting is just as the name suggests, allowing ambient air to flow over the sorbent for contact naturally. This is the approach taken by Carbon Collect, Infinitree, and Heirloom. Yet another approach uses existing infrastructure, like air and liquid flow through cooling towers, to lower the cost of contacting. Noya takes this approach.
So from a process level, you can either pull the air in, let it naturally come in contact, or hook into existing fluid flow systems to minimize the energy and capital costs that come with building fans. However, once the air is in, it will hit the contactor, filled with the solvent or sorbent. The diagrams below provide a high-level look at those processes.
Solvent System Diagram
Solid Sorbent Diagram
Generally speaking, solid sorbents can take the form of metal-organic frameworks (MOFs), sieves, zeolites, and porous natural materials. These structures and chemistries constantly evolve as more research and innovation happens within the space. Once the air comes in contact with the sorbent material, the carbon dioxide bonds to that material while the other molecules present in the air pass through the “sponge” some technologies, like Climeworks, use amine-functionalized filters, these filters increase the number of interactions that carbon dioxide has with the filters. The more interactions a filter may have with the carbon dioxide, the more binding to the solid sorbent.
Liquid solvents rely on the carbon being absorbed into the solvent. This creates a carbon-rich solvent. Packing these solvents is frequent to increase the surface area available for contact1. Skipping over a few highly technical steps here for brevity and sanity. Out of this carbon-rich solvent fluid, calcium carbonate pellets are produced. A high-temperature influx is needed to harvest the carbon dioxide from these pellets. However, high temperature is not a feature unique to the solvent approach.
Both the solid sorbent and liquid solvent DAC approaches require roughly 80% thermal energy and 20% electricity for operation [32]. This is not an arbitrary percentage as both DAC approaches must optimize between a multitude of parameters. In both systems, the thermal energy demand results from the regeneration of the sorbent and the evolution of the previously bound CO2 compounds. For the solid sorbent approach, the electricity requirements result from the contactor fans, which are required to overcome the system pressure drop, and the vacuum pumps, which remove residual air from the contactor during regeneration [2]. The liquid solvent system requires electricity for the contactor fans—also required to overcome the system pressure drop—as well as the pellet reactors, steam slaker and filtration units [17]. Both approaches must optimize between the pressure drop across the contactor and the amount of CO2 removed from the inlet air stream. This optimization determines parameters like the electricity required to power fans to overcome this pressure drop.
The above quote is from “A review of direct air capture (DAC): scaling up commercial technologies and innovating for the future Noah McQueen et al 2021 Prog. Energy 3 032001”. I suggest every reader look over this paper. It presents the state-of-play for direct air capture technology in a technically dense but approachable fashion. I use it frequently.
Driving down the electricity and thermal costs of DAC systems is key to the overall price of capture coming down, alongside the increasing modularity of the systems. Modularity, and its importance, which we will touch on in the coming weeks.
After the carbon is captured within whatever medium, that carbon must be released, and then the sorbent/solvent regenerated to receive the subsequent influx of air. This step, known as regeneration, has three main pathways: temperature swing, pressure swing, and electrochemical swing. We will explore these in the next post.
The below information is taken from last week’s blog as it was germane to this post.
Solid Sorbents
Solid sorbents include a wide variety of physical chemistries to capture the CO2
Benefits of Solid sorbent designs1
Offer the possibility of low energy input
Low operating costs and applicability across a wide range of scales
Challenges of solid sorbent designs2
The need to build a substantial structure at low cost while allowing the entire structure to be periodically sealed from the ambient air during the regeneration step when temperature, pressure, or humidity must be cycled.
The inherently conflicting demands of high sorbent performance, low cost, and prolonged economic life in impure ambient air.
A notable chemical structure in this space are Metal-Organic Frameworks (MOFs)
Benefits include
Challenges
Commercial production of MOFs
Availability of metals for production
Liquid Solvents
Liquid solvents are used less than solid sorbents and come with their host of benefits and challenges.
Benefits of Aqueous sorbents
The contactor can operate continuously
Can be built using cheap cooling-tower hardware
The (liquid) surface is continuously renewed, allowing very long contactor lifetimes despite the dust and atmospheric contaminants.
Once captured, CO2 can be easily pumped to a central regeneration facility allowing economies of scale and avoiding the need to cycle conditions in the inherently large air contactor.
Challenges of Aqueous sorbents
Cost and complexity of the regeneration system
Water loss in dry environments.
Benchmarking
Crawling through various scientific publications, media clips, interviews, and websites, I compiled a non-exhaustive list of DAC companies and the various liquid solvent and solid sorbents they use to achieve removal. I added notes around what differentiates their air intake method when possible.
Given some feedback from several readers. I will continue to benchmark these differentiating qualities between companies and put them into a post as needed. For instance, I’ll be looking at modularity in a couple of weeks and will note which companies employ that strategy.
Liquid Solvent Companies2
Carbon Engineering
Potassium hydroxide solution/calcium carbonation
Fan driven contact
Noya
Undisclosed solvent
Co-opted contact from cooling towers
Mission Zero
Undisclosed non-hydroxide solvent
Contact unclear, but given it’s a liquid solvent, I’m guessing fan driven
1point5
Undisclosed solvent
Fan driven contact
Solid Sorbent Companies3
Climeworks
Amine-functionalized filter
Fan drive contact
Global Thermostat
Amine-modified monolith
Fan driven contact
Infinitree
Ion-exchange sorbent
Passive driven contact
Skytree
Porous plastic beads functionalized with benzylamines
Passive driven contact
Heirloom
Magnesium or calcium oxides in contact with ambient air (which flows through air contactors)
Passive driven contact
Carbon Collect
Solid Sorbent from Silicon Kingdom
Passive contact
Carbon Capture
Active contact
Sustaera
Alki-metal based
Fan driven contact
Verdox
Stacked electrochemical cells
Fan driven contact
Carbon infinity
Metal-organic framework
Fan driven contact
8 Rivers
Calcium oxide as a solid sorbent
Warehouse based contactors - unclear if this is dovetailing on the warehouse system like Noya or something different
Next week: Tech Deep Dive: Direct Air Capture 3 - regeneration mechanisms
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Holmes G and Keith D W 2012 An air-liquid contactor for large-scale capture of CO2 from air Phil. Trans. R. Soc. A 370 4380–403
https://www.nap.edu/read/25259/chapter/7#192
https://www.nap.edu/read/25259/chapter/7#192