Capturing CO2 from ambient air - David Keith
Capturing CO2 from ambient air - David Keith
Capturing CO2 from ambient air - David Keith
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Figure 3.13: Simple diagram of a horizontal flow contactor<br />
data, which was collected for a downward flow system.<br />
Horizontal <strong>air</strong> flow<br />
Another design variation that may reduce contactor cost is a system with horizontal <strong>air</strong> flow. A diagram is<br />
shown in Figure 3.13. Here H would be relatively short, perhaps 20 m, but L may be much longer, perhaps<br />
100 m. A fan would likely be placed at the inlet and a particle trap at the outlet. Spray nozzles would be<br />
spaced along the length, leaving some distance at the end for drops to settle before reaching the outlet.<br />
The energetics are similar to a short tower system but with two advantages. The first advantage is that<br />
the residence time of the spray is longer compared with a vertical system, given simply by τ = H . Longer<br />
vt<br />
τ for a given height reduces pumping energy as described in the previous section. The other advantage is<br />
that a new parameter is introduced, L, which determines the residence time of the <strong>air</strong> independent of the<br />
residence time of the spray. Thus L can be adjusted to keep ˙E f an small. The system shares the drawback<br />
with short towers of high ˙Enozzle, though this is somewhat dampened by the effect of longer residence time.<br />
A low ΔPnozzle would be required.<br />
A horizontal system may offer reduced capital cost compared with a vertical system. Although the<br />
area of wall per unit contactor volume required is larger than for a very large cylindrical cooling tower,<br />
the walls bear a much lighter load and so less material may be required overall. On the other hand, more<br />
land area and a sealed roof would be required. It is not obvious how the capital costs would compare to an<br />
equivalent vertical system.<br />
3.5.3 Water loss<br />
We have measured and calculated a rate of water loss that in volume terms is quite high. We have discussed<br />
how the rate of water loss can be managed with high NaOH concentrations, but it may be desirable for<br />
other reasons to run at lower NaOH concentrations. In that case, water loss is highly dependent on the<br />
meteorology of the site. Paying for water at a rate typical of power plant cooling towers does not raise<br />
overall costs significantly, however in a world where <strong>air</strong> capture is widely deployed, the demand for<br />
water would be large on the scale of developed use, and could upset already overburdened water systems.<br />
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