Method and device for converting carbon dioxide in flue gas into natural gas
A method for converting carbon dioxide in flue gas into natural gas using dump energy. The method includes: 1) transforming and rectifying a voltage of dump energy generated from a renewable energy plant, introducing the voltage-transformed and rectified dump energy into an electrolyte solution to electrolyze water therein to yield H 2 and O 2 ; 2) purifying industrial flue gas to separate CO 2 therein and purifying CO 2 ; 3) transporting H 2 generated and CO 2 to a synthesis equipment, allowing a methanation reaction between H 2 and CO 2 to happen to yield a high-temperature mixed gas with main ingredients of CH 4 and water vapor; 4) employing the high-temperature mixed gas to conduct indirect heat exchange with process water to yield superheated water vapor; 5) delivering the superheated water vapor to a turbine to generate electric energy, and returning the electric energy to step 1); and 6) condensing and drying the mixed gas.
1. A method for converting carbon dioxide in flue gas into natural gas using dump energy, the method comprising:
1) transforming and rectifying a voltage of dump energy generated from a renewable energy plant, introducing the voltage-transformed and rectified dump energy into an electrolyte solution to electrolyze water therein to yield H 2 and O 2 , and drying H 2 ;
2) purifying industrial flue gas to separate CO 2 therein and purifying CO 2 ;
3) transporting H 2 generated from step 1) and CO 2 from step 2) to a synthesis equipment comprising at least two fixed bed reactors, allowing a methanation reaction between H 2 and CO 2 to happen to yield a high-temperature mixed gas with main ingredients of CH 4 and water vapor;
4) employing the high-temperature mixed gas generated from step 3) to conduct indirect heat exchange with process water to yield superheated water vapor;
5) delivering the superheated water vapor generated from step 4) to a turbine to generate electric energy, and returning the electric energy to step 1) for water electrolysis; and
6) condensing and drying the mixed gas in step 4) cooled through the indirect heat exchange, until natural gas with CH 4 content up to the standard is obtained.
2. The method of claim 1 , wherein the renewable energy is selected from solar energy, hydroenergy, wind energy, or a combination thereof.
3. The method of claim 1 , wherein the electrolyte solution is a potassium hydroxide solution with a density of 1.2-1.4 kg/m 3 , and a reaction temperature of the electrolyte solution is controlled at 90±2° C.
4. The method of claim 3 , wherein in step 3), the fixed bed reactors have an inlet temperature of 250-300° C., a reaction pressure of 3-4 MPa, and an outlet temperature of 350-700° C.
5. The method of claim 3 , wherein in step 3), part of the high-temperature mixed gas from a primary fixed bed reactor is bypassed for cooling, water removal, pressurization and heating, and is then mixed with fresh H 2 and CO 2 , so that the mixed gas is transported back to the primary fixed bed reactor after a volume content of CO 2 therein is 6-8%.
6. The method of claim 3 , wherein in step 4), the process water is first heated to produce superheated water, which is then converted to yield water vapor, and finally the water vapor is converted to yield the superheated water vapor.
7. The method of claim 3 , wherein in step 5), steam exhaust generated by a turbine after being driven for power generation is condensed to water, and then sent back to a process water line for recycling.
8. The method of claim 3 , wherein in step 6), condensed water from the mixed gas is transported back to a process water line for recycling.