I'd much rather be dealing with industrial quantities of CO2 than Cl2, if that stuff gets into the atmosphere in bulk I doubt it'd end well. The article seems to suggest that the chlorine can be solved commercially so the argument seems to be that it is economical to sequester the chlorine rather than the carbon dioxide.
There are some obvious risks of being left with large amounts of Chlorine to try and find a home for, but the idea is at least plausible on face value.
Big use-case, problem is that in case of fire lots of dioxins are produced.
The costs of CO2 - the real costs, not the subsidized ones - are extraordinarily high, possibly leading to the worst global catastrophe in human history. What is the cost of Cl2?
With the passing of time the answer might not be so clear.
The frogs in the 2 degree warmer pond will be complaining a lot more than the other frogs, so that must be worse.
The pre-industrial levels of CO2 were around 280ppm, while the current CO2 levels are around 440ppm.
For Cl2, in occupational-health situations the permissible exposure is around 1ppm per hour, or 3ppm for 15 minutes. So the 160ppm we'd throw into the atmosphere in this thought experiment (or even the 52ppm at the suggested discount) is going to cause some pretty big problems pretty rapidly.
The problem with H2O wouldn't be the absolute amount, but the changes brought on by the added H2O. For one thing, it would rain pretty much 24/7 in Florida. :) (Yes, I know it's not at all that predictable.)
with carbon and hydrogen from natural gas/coal gasification: CH4 + CO2 -> 2CO + 2H2 Fe2O3 + 3CO -> 2Fe + 3CO2 (exothermic in >50% H2 environment)
with water-sourced hydrogen: 2H2O -> O2 + 2H2 Fe2O3 + 3H2 -> 2Fe + 3H2O (endothermic, requires energy input)
There are two issues with using hydrogen, which can be overcome:
>"The energy balance of the shaft furnace is affected by the absence of the exothermic carbon monoxide reduction. . . Thus, it is necessary to add energy to the shaft furnace to carry heat in the burden."
>"The second issue is the resulting DRI carbon content; the DRI will have 0% carbon with pure hydrogen. The majority of DRI is used in EAFs, and EAF steelmaking practice generally employs carbon addition... Under current melting practices, it will be necessary to add hydrocarbons at some place in the process to achieve the desired carbon level... However, this added carbon will then be converted to CO2 in the EAF... Alternatively, carbon from a renewable source (like biomass) could be used."
https://www.midrex.com/tech-article/ultra-low-co2-ironmaking...