Method and apparatus for reducing CO2 in a stream by conversion to a Syngas for production of energy
AssigneeGYCO, Inc.
InventorGary C. Young
Life of this patent
Estimating the term…
Abstract
A system and method for producing Syngas from the CO2 in a gaseous stream, such as an exhaust stream, from a power plant or industrial plant, like a cement kiln, is disclosed. A preferred embodiment includes providing the gaseous stream to pyrolysis reactor along with a carbon source such as coke. The CO2 and carbon are heated to about 1330° C. and at about one atmosphere with reactants such as steam such that a reaction takes place that produces Syngas, carbon dioxide (CO2) and hydrogen (H2). The Syngas is then cleaned and provided to a Fischer-Tropsch synthesis reactor to produce Ethanol or Bio-catalytic synthesis reactor.
Claims31
A process for producing syngas that reduces the amount of carbon dioxide in a gaseous stream, the process comprising:
- maintaining a reaction chamber at a temperature of between 400° C. and 5000° C. and at a pressure of about one bar or greater;
- providing a carbonaceous material in said reaction chamber;
- providing H2O to said reaction chamber;
- introducing a gaseous stream containing carbon dioxide (CO2) to said reaction chamber;
- reacting materials in said reaction chamber, wherein said reacting materials consisting essentially of said carbonaceous material, said H2O and said carbon dioxide (CO2) from said gaseous stream to reduce said CO2 and to form syngas comprising carbon monoxide (CO) and hydrogen (H2), said reacting step further resulting in none of the carbonaceous material remaining as un-reacted carbonaceous material in said syngas;
- discharging said formed syngas from said reaction chamber;
- and
- providing said formed syngas comprising carbon monoxide (CO) and hydrogen (H2) to a water-gas shift reactor to adjust the carbon monoxide and hydrogen molar ratio to between 0.2 to 5.0 molecules of carbon monoxide (CO) and 5.0 to 0.2 molecules of hydrogen (H2).
A process for producing syngas that reduces the amount of carbon dioxide in a gaseous stream, the process comprising:
- maintaining a reaction chamber at a temperature of between 400° C. and 5000° C. and at a pressure of about one bar or greater, said reaction chamber is selected to be one of a pyrolysis reactor, a conventional gasifier or a plasma arc gasifier;
- providing a carbonaceous material in said reaction chamber;
- providing H2O to said reaction chamber;
- introducing a gaseous stream containing carbon dioxide (CO2) to said reaction chamber;
- reacting materials provided to said reaction chamber, said reacting materials consisting essentially of said carbonaceous material, said H2O and said carbon dioxide (CO2) in said gaseous stream to form syngas in said reaction chamber comprising carbon monoxide (CO) and hydrogen (H2), wherein the amount of CO2 in said syngas is at least 53% less than the amount of CO2 that was provided in said gaseous stream;
- discharging said formed syngas from said reaction chamber;
- and
- providing said syngas comprising carbon monoxide (CO) and hydrogen (H2) to a water-gas shift reactor to adjust the carbon monoxide and hydrogen molar ratio to between 0.2 to 5.0 molecules of carbon monoxide (CO) and 5.0 to 0.2 molecules of hydrogen (H2).
A process for producing syngas that reduces the amount of carbon dioxide in a gaseous stream, the process comprising:
- maintaining a reaction chamber at a temperature of between 400° C. and 5000° C. and at a pressure of about one bar or greater, said reaction chamber is selected to be one of a pyrolysis reactor, a conventional gasifier or a plasma arc gasifier;
- providing a carbonaceous material in said reaction chamber;
- providing H2O to said reaction chamber;
- introducing a gaseous stream containing carbon dioxide (CO2) to said reaction chamber;
- reacting materials provided to said reaction chamber, the reacting materials consisting essentially of said carbonaceous material, said H2O and said carbon dioxide (CO2) in said gaseous stream to form syngas comprising carbon monoxide (CO) and hydrogen (H2), wherein the amount of CO2 in said syngas is at least 53% less than the amount of CO2 that was provided in said gaseous stream;
- and
- discharging said formed syngas.
A process for producing syngas that reduces the amount of carbon dioxide in a gaseous stream, the process comprising:
- maintaining a reaction chamber at a temperature of between 400° C. and 5000° C. and at a pressure of about one bar or greater;
- providing a carbonaceous material in said reaction chamber;
- providing H2O to said reaction chamber;
- introducing a gaseous stream containing carbon dioxide (CO2) to said reaction chamber;
- reacting materials provided to said reaction chamber, the reacting materials consisting essentially of said carbonaceous material, said H2O and said carbon dioxide (CO2) in said gaseous stream to form a syngas output, said syngas output consisting essentially of carbon dioxide (CO2), nitrogen (N2), carbon monoxide (CO) and hydrogen (H2);
- and
- discharging said formed syngas output.
A process for producing syngas that reduces the amount of carbon dioxide in a gaseous stream, the process comprising:
- maintaining a reaction chamber at a temperature of between 400° C. and 5000° C. and at a pressure of about one bar or greater;
- providing a carbonaceous material in said reaction chamber;
- providing H2O to said reaction chamber;
- introducing a gaseous stream containing carbon dioxide (CO2) to said reaction chamber;
- reacting materials in said reaction chamber, wherein the reacting materials consisting essentially of said carbonaceous material, said H2O and said carbon dioxide (CO2) in said gaseous stream to reduce said CO2 and to form syngas comprising carbon monoxide (CO) and hydrogen (H2), wherein the mole ratio of H2O consumed to carbonaceous material consumed provided to the reactor chamber is about 34.33% and having an amount of CO2 that is less than the amount of CO2 that was provided in said gaseous stream;
- and
- discharging said formed syngas.
A process for producing syngas that reduces the amount of carbon dioxide in a gaseous stream, the process comprising:
- maintaining a reaction chamber at a temperature of between 400° C. and 5000° C. and at a pressure of about one bar or greater;
- providing a carbonaceous material in said reaction chamber;
- providing H2O to said reaction chamber;
- introducing a gaseous stream containing carbon dioxide (CO2) to said reaction chamber;
- reacting materials in said reaction chamber, wherein said reacting materials consisting essentially of said carbonaceous material, said H2O and said carbon dioxide (CO2) from said gaseous stream to reduce said CO2 and to form a syngas output, said syngas output consisting essentially of carbon dioxide (CO2), nitrogen (N2), carbon monoxide (CO) and hydrogen (H2);
- discharging said formed syngas output;
- and
- providing said syngas comprising carbon monoxide (CO) and hydrogen (H2) to a water-gas shift reactor to adjust the carbon monoxide (CO) and hydrogen (H2) molar ratio to between 0.2 to 5.0 molecules of carbon monoxide (CO) and 5.0 to 0.2 molecules of hydrogen (H2).
Dependencies are inferred from the claim text.