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Sequestering carbon dioxide from the atmosphere by enhancing the capacity of the oceans to act as a carbon sink Tim Kruger www.cquestrate.com
CaCO 3     CaO + CO 2 Thermally decompose (calcine) limestone at temperatures greater than 850C Δ H = +163kJ/mol * Assuming no recapture of heat,  energy requirement is 2.669GJ/tonne of CaCO 3 * Reaction enthalpy calculated at 1000C Concept
CaCO 3     CaO + CO 2 CaO + H 2 O    Ca(OH) 2 Ca(OH) 2  + 2CO 2     Ca(HCO 3 ) 2 Concept The calcium oxide generated from the calcination of limestone is added to seawater At seawater pH, the calcium oxide will form a solution of calcium bicarbonate For each mol of CO 2  emitted during the calcination,  almost two mols of CO 2  will be absorbed in the seawater Δ H = -65kJ/mol
CaCO 3     CaO + CO 2 CaO + H 2 O    Ca(OH) 2 Ca(OH) 2  + 2CO 2     Ca(HCO 3 ) 2 CO 2  + H 2 O  H 2 CO 3   H +  + HCO 3 -   2H +  + CO 3 2- Concept On addition of calcium oxide to seawater, the system of equilibria associated with the dissolution of CO 2  in water will be shifted to the right. This  increases the capacity of the  oceans to act as a carbon sink , whilst simultaneously mitigating the effects of ocean acidification caused by heightened levels of CO 2  in the atmosphere
CaCO 3     CaO + CO 2 CaO + H 2 O    Ca(OH) 2 Options Ca(OH) 2  + 2CO 2     Ca(HCO 3 ) 2 CO 2  + H 2 O  H 2 CO 3   H +  + HCO 3 -   2H +  + CO 3 2- Concept There are  five potential ways  in which to deal with the pure CO 2  produced in the calcination process
CaCO 3     CaO + CO 2 CaO + H 2 O    Ca(OH) 2 Options Release Ca(OH) 2  + 2CO 2     Ca(HCO 3 ) 2 CO 2  + H 2 O  H 2 CO 3   H +  + HCO 3 -   2H +  + CO 3 2- Concept Releasing CO 2  into the atmosphere may seem counterproductive – we are after all trying to remove CO 2  – but given that the process is net ‘carbon negative’ even if the CO 2  emitted is released, this may be the most economic route
CaCO 3     CaO + CO 2 CaO + H 2 O    Ca(OH) 2 Options Release Sequester Ca(OH) 2  + 2CO 2     Ca(HCO 3 ) 2 CO 2  + H 2 O  H 2 CO 3   H +  + HCO 3 -   2H +  + CO 3 2- Concept The cost for geologically storing  pure CO 2  has been estimated to be  USD0.5 – 8 per tonne of CO 2 . In comparison sequestering carbon dioxide from the  flue gases  of a conventional fossil fuel power plant, where the CO 2   concentration  is typically in the region of  10% , costs in the region of  USD47 per tonne of CO 2
CaCO 3     CaO + CO 2 CaO + H 2 O    Ca(OH) 2 Options Release Sequester Fuel Production Ca(OH) 2  + 2CO 2     Ca(HCO 3 ) 2 CO 2  + H 2 O  H 2 CO 3   H +  + HCO 3 -   2H +  + CO 3 2- Concept With the addition of  more energy , pure CO 2  can be used as a  feedstock  for the production of hydrocarbons
CaCO 3     CaO + CO 2 CaO + H 2 O    Ca(OH) 2 Options Release Sequester Fuel Production Reduce to Carbon Ca(OH) 2  + 2CO 2     Ca(HCO 3 ) 2 CO 2  + H 2 O  H 2 CO 3   H +  + HCO 3 -   2H +  + CO 3 2- Concept With the addition of more energy, pure CO 2  can be reduced to carbon. If CO 2  emissions are no longer a problem, carbon is an excellent  energy vector , with 6000 times the energy per unit volume of unpressurised hydrogen
Concept CaCO 3     CaO + CO 2 CaO + H 2 O    Ca(OH) 2 Options Release Sequester Fuel Production Reduce to Carbon Growing Biomass in Arid Environments Ca(OH) 2  + 2CO 2     Ca(HCO 3 ) 2 CO 2  + H 2 O  H 2 CO 3   H +  + HCO 3 -   2H +  + CO 3 2-
Growing biomass in arid environments ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object]
Burning methane to calcine limestone leads to a net reduction in carbon dioxide ,[object Object],[object Object],[object Object],[object Object],[object Object]
Potential sources of energy ,[object Object],[object Object],[object Object],[object Object],[object Object]
Where this could be done ,[object Object],[object Object],[object Object],[object Object],[object Object]

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Cquestrate Presentation

  • 1. Sequestering carbon dioxide from the atmosphere by enhancing the capacity of the oceans to act as a carbon sink Tim Kruger www.cquestrate.com
  • 2. CaCO 3  CaO + CO 2 Thermally decompose (calcine) limestone at temperatures greater than 850C Δ H = +163kJ/mol * Assuming no recapture of heat, energy requirement is 2.669GJ/tonne of CaCO 3 * Reaction enthalpy calculated at 1000C Concept
  • 3. CaCO 3  CaO + CO 2 CaO + H 2 O  Ca(OH) 2 Ca(OH) 2 + 2CO 2  Ca(HCO 3 ) 2 Concept The calcium oxide generated from the calcination of limestone is added to seawater At seawater pH, the calcium oxide will form a solution of calcium bicarbonate For each mol of CO 2 emitted during the calcination, almost two mols of CO 2 will be absorbed in the seawater Δ H = -65kJ/mol
  • 4. CaCO 3  CaO + CO 2 CaO + H 2 O  Ca(OH) 2 Ca(OH) 2 + 2CO 2  Ca(HCO 3 ) 2 CO 2 + H 2 O H 2 CO 3 H + + HCO 3 - 2H + + CO 3 2- Concept On addition of calcium oxide to seawater, the system of equilibria associated with the dissolution of CO 2 in water will be shifted to the right. This increases the capacity of the oceans to act as a carbon sink , whilst simultaneously mitigating the effects of ocean acidification caused by heightened levels of CO 2 in the atmosphere
  • 5. CaCO 3  CaO + CO 2 CaO + H 2 O  Ca(OH) 2 Options Ca(OH) 2 + 2CO 2  Ca(HCO 3 ) 2 CO 2 + H 2 O H 2 CO 3 H + + HCO 3 - 2H + + CO 3 2- Concept There are five potential ways in which to deal with the pure CO 2 produced in the calcination process
  • 6. CaCO 3  CaO + CO 2 CaO + H 2 O  Ca(OH) 2 Options Release Ca(OH) 2 + 2CO 2  Ca(HCO 3 ) 2 CO 2 + H 2 O H 2 CO 3 H + + HCO 3 - 2H + + CO 3 2- Concept Releasing CO 2 into the atmosphere may seem counterproductive – we are after all trying to remove CO 2 – but given that the process is net ‘carbon negative’ even if the CO 2 emitted is released, this may be the most economic route
  • 7. CaCO 3  CaO + CO 2 CaO + H 2 O  Ca(OH) 2 Options Release Sequester Ca(OH) 2 + 2CO 2  Ca(HCO 3 ) 2 CO 2 + H 2 O H 2 CO 3 H + + HCO 3 - 2H + + CO 3 2- Concept The cost for geologically storing pure CO 2 has been estimated to be USD0.5 – 8 per tonne of CO 2 . In comparison sequestering carbon dioxide from the flue gases of a conventional fossil fuel power plant, where the CO 2 concentration is typically in the region of 10% , costs in the region of USD47 per tonne of CO 2
  • 8. CaCO 3  CaO + CO 2 CaO + H 2 O  Ca(OH) 2 Options Release Sequester Fuel Production Ca(OH) 2 + 2CO 2  Ca(HCO 3 ) 2 CO 2 + H 2 O H 2 CO 3 H + + HCO 3 - 2H + + CO 3 2- Concept With the addition of more energy , pure CO 2 can be used as a feedstock for the production of hydrocarbons
  • 9. CaCO 3  CaO + CO 2 CaO + H 2 O  Ca(OH) 2 Options Release Sequester Fuel Production Reduce to Carbon Ca(OH) 2 + 2CO 2  Ca(HCO 3 ) 2 CO 2 + H 2 O H 2 CO 3 H + + HCO 3 - 2H + + CO 3 2- Concept With the addition of more energy, pure CO 2 can be reduced to carbon. If CO 2 emissions are no longer a problem, carbon is an excellent energy vector , with 6000 times the energy per unit volume of unpressurised hydrogen
  • 10. Concept CaCO 3  CaO + CO 2 CaO + H 2 O  Ca(OH) 2 Options Release Sequester Fuel Production Reduce to Carbon Growing Biomass in Arid Environments Ca(OH) 2 + 2CO 2  Ca(HCO 3 ) 2 CO 2 + H 2 O H 2 CO 3 H + + HCO 3 - 2H + + CO 3 2-
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