Method for Producing a Highly Porous Fine Powdered Slaked Lime Composition, and Product Obtained Therefrom
US-2019127273-A1 · May 2, 2019 · US
US10940433B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10940433-B2 |
| Application number | US-201916679569-A |
| Country | US |
| Kind code | B2 |
| Filing date | Nov 11, 2019 |
| Priority date | Jan 31, 2019 |
| Publication date | Mar 9, 2021 |
| Grant date | Mar 9, 2021 |
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The subject invention provides systems and methods for capturing carbon dioxide in a cyclic process of mechano-chemical reactions. The subject invention also provides systems and methods for synthesizing siderite, by means of mechano-chemical reactions, using mill rotation. Siderite acts as an efficient reversible sorbent and can be decomposed, generating magnetite, carbon and/or metallic iron as well as pure carbon dioxide. Said systems and methods employing carbon dioxide capture/release reactions in the carbonation-calcination cycles are suitable for using in any iron, steel and non-steel industries to reduce carbon dioxide emissions into the atmosphere.
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We claim: 1. A system for capturing carbon dioxide, comprising a carbonation reactor comprising a mixture of reaction materials, a first port for receiving the reaction materials, a second port for receiving a stream of gaseous carbon dioxide, and a grinding mechanism inside the carbonation reactor, the reaction materials comprising metal oxides and a reducing agent, the reaction materials reacting with carbon dioxide to form carbonates, wherein the first port is located at an upper end of the carbonation reactor and the second port is located at a lower end of the carbonation reactor, and the reducing agent being carbon; and a calcination reactor comprising a first port for receiving carbonates produced in the carbonation reactor, the carbonates being decomposed in the calcination reactor at room temperature conditions to reproduce the reaction materials, and a second port for releasing and recycling the reproduced reaction materials back to the carbonation reactor. 2. The system according to claim 1 , the metal oxides comprising magnetite, hematite, wustite, and/or goethite. 3. The system according to claim 1 , the grinding mechanism comprising grinding balls. 4. The system according to claim 1 , the reaction materials and grinding mechanism having a weight ratio of 2:27. 5. The system according to claim 1 , the reaction materials comprising water ranging from 1 mol to 20 mol. 6. The system according to claim 1 , the carbonation reactor being rotated at a revolution speed ranging from about 100 rpm to 500 rpm. 7. The system according to claim 1 , the carbonation reactor having an internal CO 2 pressure of 10, 20 or 30 bar. 8. The system according to claim 1 , the carbonation reactor having an internal temperature ranging from about 20 to about 600° C. 9. The system according to claim 1 , the metal oxides comprising—magnetite. 10. The system according to claim 1 , which further comprises a sonication unit comprising one or more ultrasound transducers. 11. A system for capturing carbon dioxide, comprising a carbonation reactor comprising 1) a mixture of reaction materials, the reaction materials comprising water, magnetite and carbon; 2) a first port for receiving the reaction materials, wherein the first port is located at an upper end of the carbonation reactor; 3) a second port for receiving a stream of gaseous carbon dioxide, wherein the second port is located at a lower end of the carbonation reactor, and 4) a grinding mechanism inside the carbonation reactor, the reaction materials reacting with carbon dioxide to form siderite; and a calcination reactor comprising a first port for receiving siderite produced in the carbonation reactor, the siderite being decomposed in the calcination reactor at room temperature conditions to reproduce Fe 3 O 4 and C, and a second port for releasing and recycling the Fe 3 O 4 and C back to the carbonation reactor. 12. The system according to claim 11 , the carbonation reactor having an internal CO 2 pressure of 10, 20 or 30 bar. 13. The system according to claim 11 , the carbonation reactor having an internal temperature ranging from about 20 to about 600° C. 14. The system according to claim 11 , the carbonation reactor being rotated at a revolution speed ranging from about 100 rpm to 500 rpm. 15. A system for capturing carbon dioxide, comprising a carbonation reactor comprising a mixture of reaction materials, the reaction materials comprising water, magnetite and carbon; a first port for receiving the reaction materials, the first port being located at an upper end of the carbonation reactor; a second port for receiving a stream of gaseous carbon dioxide, the second port being located at a lower end of the carbonation reactor; a grinding mechanism inside the carbonation reactor, the reaction materials reacting with carbon dioxide to form carbonates; a sonication unit on the wall of the carbonation reactor, the sonication unit comprising one or more ultrasounic transducers; and a third port for obtaining carbonates. 16. A method for capturing carbon dioxide comprising passing a stream of gas comprising carbon dioxide through the system of claim 1 . 17. A method for capturing carbon dioxide comprising passing a stream of gas comprising carbon dioxide through the system of claim 11 . 18. A method for capturing carbon dioxide comprising passing a stream of gas comprising carbon dioxide through the system of claim 15 . 19. The system according to claim 15 , the carbonation reactor being rotated at a revolution speed ranging from about 100 rpm to 500 rpm. 20. The system according to claim 1 , the carbon being selected from graphite, coal, coke, charcoal, and soot.
Removing carbon dioxide · CPC title
comprising oxides or hydroxides of metals not provided for in group B01J20/04 · CPC title
Hydroxides · CPC title
by thermal treatment not covered by groups B01J20/3441 - B01J20/3475, e.g. by heating or cooling · CPC title
Sonic or ultrasonic vibration · CPC title
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