Carbon dioxide capture from a cement manufacturing process
View Patent ↗A process of manufacturing cement clinker is provided in which a clean supply of CO 2 gas may be captured. The process also involves using an open loop conversion of CaO/MgO from a calciner to capture CO 2 from combustion flue gases thereby forming CaCO 3 /CaMg(CO 3 ) 2 . The CaCO 3 /CaMg(CO 3 ) 2 is then returned to the calciner where CO 2 gas is evolved. The evolved CO 2 gas, along with other evolved CO 2 gases from the calciner are removed from the calciner. The reactants (CaO/MgO) are feed to a high temperature calciner for control of the clinker production composition.
1. A process for the production of cement clinker which comprises the steps of:
heating the limestone/dolomite components of the a clinker feed in a first calciner at a temperature of between about 650° C. to about 1050° C., said calciner containing no combustion gases;
removing a portion of a CaO/MgO reaction product from said calciner;
using said removed CaO/MgO to capture CO 2 from fuel combustion flue gas associated with said cement production process, thereby generating a supply of CaCO 3 /CaMg(CO 3 ) 2 ;
introducing said supply of CaCO 3 /CaMg(CO 3 ) 2 from said flue gas environment into said first calciner, said CaCO 3 /CaMg(CO 3 ) 2 thereby releasing CO 2 ;
removing released CO 2 from said calciner; and,
removing additional reaction products from said calciner and subsequently exposing said reaction products in a second calciner to a temperature of between about 1300° C. to about 1450° C. until clinker is formed.
2. The process according to claim 1 wherein prior to said step of heating said limestone/dolomite components of a clinker feed, said limestone/dolomite components are separated from other constituents of said clinker feed.
3. The process according to claim 1 wherein said heating in said first calciner of the limestone/dolomite components of a clinker feed is performed in an environment free of combustion gases.
4. The process according to claim 1 wherein carbonate oxides are added to said second calciner, a temperature and a residence time of said carbonate oxides within said second calciner affecting a yield and a ratio of belite to alite within the clinker feed.