Method and system for sequestering carbon dioxide and producing hydrogen gas
A system and method for the simultaneous sequestration of CO2, production of hydrogen, and production of electricity at any iron and steel industries is described. In one illustrative example, the raw materials particularly used in a blast furnace can also be used for locking CO2 gas in the form of siderite. Siderite, thus formed, can be decomposed to generate pure CO2 gas. Eventually, the generated pure CO2 gas can be sequestered underground, sold or used for oil gas recovery or for other applications.
1. A system for sequestering carbon dioxide, comprising: a carbonation reactor having a port for receiving a hot pressurized gaseous stream of CO 2 and N 2 , wherein the carbonation reactor comprises a reaction mixture comprising (i) magnetite and iron, (ii) wustite, or (iii) hematite and iron, wherein the reaction mixture reacts with the hot pressurized gaseous stream received through the port to produce producing siderite and an unreacted mixture, the unreacted mixture selected from the group consisting of magnetite and iron, wustite, and hematite and iron;
a magnetic separator coupled to the carbonation reactor, the magnetic separator receiving the siderite and the unreacted mixture from the carbonation reactor and separating the siderite and- from the unreacted mixture;
a calciner, the calciner receiving the siderite from the magnetic separator and decomposing the siderite to produce produces magnetite or hematite, and CO2.
2. A system as defined in claim 1 , wherein the hot pressurized gaseous stream is provided by a compressor.
3. A system as defined in claim 1 , wherein the carbonation reactor produces a CO 2 lean pressurized hot gaseous stream.
4. A system as defined in claim 3 , wherein the CO 2 lean pressurized hot gaseous stream is used to generate energy.
5. A system as defined in claim 4 , wherein the energy is produced by a gas or steam turbine.
6. The system of claim 1 , wherein the hot pressurized gaseous stream of CO 2 and N 2 is blast furnace gas.
7. The system of claim 1 , further comprising a water gas shift reactor coupled to the carbonation reactor.
8. A system for sequestering carbon dioxide, comprising:
a carbonation reactor comprising a reaction mixture and a port for receiving a hot pressurized gaseous stream of CO 2 and N 2 , wherein the reaction mixture comprises magnetite and reacts with the gaseous stream to produce siderite and an unreacted mixture comprising magnetite;
a magnetic separator coupled to the carbonation reactor for receiving the siderite and unreacted mixture from the carbonation reactor and separating the siderite from the unreacted mixture;
a calciner adapted to receive the siderite from the magnetic separator and decompose the siderite to produce CO 2 and one or more of magnetite and hematite.
9. The system of claim 8 , wherein the reaction mixture further comprises iron.
10. The system of claim 8 , wherein the hot pressurized gaseous stream of CO 2 and N 2 is blast furnace gas.
11. The system of claim 8 , further comprising a water gas shift reactor coupled to the carbonation reactor.
12. The system of claim 8 , wherein the carbonation reactor produces a CO 2 lean pressurized hot gaseous stream.
13. The system of claim 12 , wherein the CO 2 lean pressurized hot gaseous stream is used to generate energy.
14. A method for sequestering carbon dioxide using the system of claim 1 , comprising: passing a hot and pressurized gaseous stream of CO 2 and N 2 through the carbonation reactor and forming carbonate ions and forming iron based carbonates.