Hi setra;
Activated carbon absorbs many, many things so the use of this material to remove CO2 is not too surprising. There experts who do much more work in this field than I have ever done and thus have better idea of what to expect, but I'm sure they would agree that only bench scale testing can verify the applicability for specific cases.
I would anticipate the activated carbon would absorb at least some CO2 but it should be saturated with respect to CO2 fairly quickly. The adsorbed CO2 will interfere with absorption of other contaminants to some extent but relative strength of absorption for the different species (or selectivity) is the important factor concerning the amount of absorption of the other species and the residual concentrations.
Operationally the initial CO2 absorption probably releases heat (any change of state has a heat of transition, the absorbed species go from a purely gas mixture state to the gas-solid state; such state changes are most commonly exothermic). A new carbon bed should be brought on line slowly (introduce process gas slowly) to avoid a high temperature; important for systems larger than bench scale. The absorption heat for CO2 (or the other major gas components, i.e. N2) may not large enough to be a problem but has to be checked (there may be existing data). I have heard of carbon bed fires where traces of nitrogen trichloride (a highly explosive contaminant) was being removed from chlorine gas due to rapid switching on-line and the heat of absorption of chlorine on activated carbon is "high".
If there is sufficient adsorption of contaminants to warrant this approach (also depending upon the scale of operation), other safety considerations have to taken into account. Especially vessel entry or handling during disposal (CO2 and other gases will be released for a long time and in enclosed spaces the atmosphere will not support animal/human life).
A carbon bed will become saturated with different species according to selectivities and inlet concentrations. The carbon bed may be regenerated by pulling a vacuum and/or passing a higher temperature inert gas through the bed. However, some species such as aromatics may not be easily removed and the carbon may simply have to be replaced. I'm still thinking of a relatively small scale application where the use of a simple carbon bed system without getting into regeneration, etc. would be convenient, and relatively inexpensive to install and operate.
Using a water spray to cool the gas will absorb some CO2. The amount of absorption will not be a significant portion of the gas stream. If you are going for commercial CO2 production, it would an recovery inefficiency. Again I'm still thinking a small localized system to enrich the atmosphere of a local greenhouse with the "conditioned" gas. If the exit water stream is a large amount, it should be diluted and downstream enclosed spaces avoided due to CO2 release.
On the other hand, perhaps the water stream might be used for mist in the greenhouse providing CO2 as well as moisture. I don't think the water should be used for irrigation since the water will be acidic due to presence of carbonic acid, the plant people would have to comment. A greater concentration of CO2 in the water would be effected by doing the gas-liquid contact in a pressurized vessel and more CO2 will be released during the misting. However, other contaminants absorbed into the water may be an issue (e.g. SO2, VOC's, etc.) although they may be removed by passing the water through absorption beds such as carbon or other absorbent materials that have greater specific selectivities. Low selectivity for CO2 in this case is more important.
Further thoughts; two or more stages in a water spray system might work where a first stage water spray removes the contaminants easily absorbed into water; the water stream then disposed. For a second stage water spray, the gas is now more easily compressed, if pressurization is desirable, and hopefully the concentrations of other contaminants is small enough to be tolerated so the final stage exit water can be used for mist in the greenhouse. A second stage spray under pressure may remove more contaminants. For small scale systems, a water ring compressor would act as a second stage contactor while compressing the gas for the next stage. More CO2 is absorbed at lower temperatures as well.
"Are there different coals available according to the molecular structure of the materials?" I take it, you are referring to activated carbon. There are certainly many forms of activated carbon depending upon the source material used in the manufacture of activated carbon; bone charcoal and coconut charcoal are examples of "natural" activated carbon but there is a huge variety of material sources plus differences in the products due to purification treatments, etc. and then there is doping with things for different effects including special catalytic results for reactions. So much I would have to learn to give a proper discourse. It is entirely possible to find an activated carbon product that is much better for removing the particular contaminants than other products. Norit,
is a large supplier of activated and other forms of carbon for different purposes but there are many other suppliers.
Having an absorbent specific to molecular structure and/or size gets more into synthetic absorbents that can be "tailored" with such properties. These are commonly referred to as "molecular sieves", air drying absorbents are examples. There may be something worth considering in these products but they are usually expensive. It will be interesting to see if carbon nanotube chemistry will develop any such materials (of practical, economically viable use).
Regards