Carbon dioxide sequestration with magnesium hydroxide and regeneration of magnesium hydroxide
Embodiments of the present disclosure are directed to systems and methods of removing carbon dioxide from a gaseous stream using magnesium hydroxide and then regenerating the magnesium hydroxide. In some embodiments, the systems and methods can further comprise using the waste heat from one or more gas streams to provide some or all of the heat needed to drive the reactions. In some embodiments, magnesium chloride is primarily in the form of magnesium chloride dihydrate and is fed to a decomposition reactor to generate magnesium hydroxychloride, which is in turn fed to a second decomposition reactor to generate magnesium hydroxide.
1. A method for producing magnesium hydroxide from magnesium chloride-containing material comprising:
a first stage comprising the steps of introducing said magnesium chloride-containing material into a first reactor, passing a steam mixture into the first reactor with the magnesium chloride-containing material at the approximate temperature of 250 to 400° C., to form magnesium hydroxychloride and HCl, and
a second stage of conveying the magnesium hydroxychloride into a second reactor, introducing therewith steam to form magnesium hydroxide and HCl,
where the magnesium chloride-containing material comprises a water to magnesium chloride ratio of about 2:1.
2. The method of claim 1 , where a portion of a steam mixture exiting the second reactor is the steam mixture introduced into the first reactor.
3. The method of claim 1 , where at least a portion of the HCl formed in the second reactor exits the second reactor with a steam mixture that then passes through the first reactor.
4. The method of claim 1 , where the magnesium chloride-containing material substantially comprises magnesium chloride dihydrate.
5. The method of claim 1 , where a portion of HCl formed in the first reactor exits the first reactor with the steam mixture.
6. The method of claim 1 , where the first reactor is at a temperature of 250-350° C.
7. The method of claim 1 , further comprising transferring heat from a hot gas stream to a first recycling heating fluid and transferring heat from the first recycling heating fluid to the first reactor.
8. The method of claim 1 , where the second reactor is at a temperature of 300-500° C.
9. The method of claim 1 , further comprising transferring heat from a hot gas stream to a second recycling heating fluid and transferring heat from the second recycling heating fluid to the second reactor.
10. The method of claim 1 , where the steam introduced into the second reactor is at a temperature between 350-450° C.
11. The method of claim 1 , where no MgCl 2 is conveyed to the second reactor separate from that in product conveyed from the first reactor.