Integrated carbon dioxide conversion system for connecting oxyfuel combustion and catalytic conversion process
A carbon dioxide conversion system is provided. The carbon dioxide conversion system includes: an ion transfer membrane that separates oxygen in the air; an oxy-fuel combustor that combusts using oxygen that is separated at the ion transfer membrane as an oxidizing agent; and a dry-reformer that converts carbon dioxide that is generated through an oxy-fuel combustion reaction of the oxy-fuel combustor and methane gas that is supplied from the outside to carbon monoxide and hydrogen by a dry-reforming reaction.
1. A carbon dioxide conversion system, comprising:
an ion transfer membrane configured to separate oxygen in the air;
an oxy-fuel combustor connected to the ion transfer membrane and configured to combust a natural gas supplied from the outside using the oxygen that is separated at the ion transfer membrane as an oxidizing agent;
a tri-reformer connected to the ion transfer membrane and the oxy-fuel combustor;
a turbine connected to the oxy-fuel combustor and configured to be supplied with exhaust gas discharged from the oxy-fuel combustor, and
a heater connected between the turbine and the tri-reformer, and configured to separate carbon dioxide and steam from the exhaust gas having passed through the turbine, and
wherein the tri-reformer is configured to be supplied with the carbon dioxide and the steam separated from the exhaust gas, and
the tri-reformer is configured to convert the carbon dioxide and the steam that are separated at the heater, methane gas that is supplied from the outside, and the oxygen that is separated at the ion transfer membrane to carbon monoxide and hydrogen by a tri-reforming reaction.
2. The carbon dioxide conversion system of claim 1 , further comprising a co-electrolysis device connected to the oxy-fuel combustor and configured to convert the carbon dioxide and the steam that are generated through an oxy-fuel combustion reaction of the oxy-fuel combustor by applying heat and electrical energy to carbon monoxide, hydrogen, and oxygen.
3. The carbon dioxide conversion system of claim 2 , further comprising a synthesizer installed at the rear end of the tri- reformer and configured to convert the carbon monoxide and the hydrogen that are generated in the tri-reformer or the co-electrolysis device to methanol, ketone, or carbonate.
4. The carbon dioxide conversion system of claim 2 , further comprising:
a mixer connected to the co-electrolysis device and the ion transfer membrane, and configured to mix the oxygen that is generated in the co-electrolysis device and the oxygen that is separated at the ion transfer membrane; and
a 3-way valve connected to the mixer, the oxy-fuel combustor and the tri-reformer, and configured to supply oxygen from the mixer to the oxy-fuel combustor or the tri-reformer.
5. The carbon dioxide conversion system of claim 1 ,
wherein the steam separated from the exhaust gas that is discharged from the oxy-fuel combustor is supplied to the oxy-fuel combustor.
6. The carbon dioxide conversion system of claim 5 , further comprising a 3-way valve connected to the oxy-fuel combustor and the tri-reformer, and configured to adjust a flow rate of steam that is supplied to the tri-reformer and the oxy-fuel combustor.