Devices, systems, facilities and processes for carbon capture optimization in industrial facilities
Devices, systems, and methods for carbon capture optimization in industrial facilities are disclosed herein. An example carbon capture process involves cooling a flue gas stream using at least one gas-to-air heat exchanger disposed upstream of a carbon dioxide (CO2) absorber. Another example carbon capture process involves heating a heat medium for solvent regeneration and CO2 stripping using a fired heater and/or using at least one waste heat recovery unit.
1. A method for processing a flue gas stream, the method comprising:
receiving, at a solvent regenerator, a rich solvent flowing from a carbon dioxide absorber, wherein the flue gas stream flows through the carbon dioxide absorber, and the rich solvent comprises carbon dioxide captured from the flue gas stream in the carbon dioxide absorber;
heating a heat medium using at least a fired heater;
transporting the heated heat medium from the fired heater to the solvent regenerator;
generating, by the fired heater, a fired heater flue gas; and
transporting the fired heater flue gas into the flue gas stream at a position upstream of the carbon dioxide absorber;
producing a generator flue gas by a power generator in fluid communication with a generator flue gas waste heat recovery unit, wherein the power generator generates electricity; and
transporting the generator flue from the power generator to the waste heat recovery unit,
wherein heating the heat medium using the generator flue gas waste heat recovery unit is based on heat recovered by the waste heat recovery unit from the generator flue gas.
2. A method for processing a flue gas stream, the method comprising:
receiving, at a solvent regenerator, a rich solvent flowing from a carbon dioxide absorber, wherein the flue gas stream flows through the carbon dioxide absorber, and the rich solvent comprises carbon dioxide captured from the flue gas stream in the carbon dioxide absorber;
heating a heat medium using at least a fired heater;
transporting the heated heat medium from the fired heater to the solvent regenerator;
generating, by the fired heater, a fired heater flue gas;
transporting the fired heater flue gas into the flue gas stream at a position upstream of the carbon dioxide absorber;
driving a carbon dioxide compressor using a driver, the driver producing a driver flue gas; and
transporting the driver flue gas from the driver to a waste heat recovery unit,
wherein heating the heat medium using the waste heat recovery unit is based on heat recovered by the waste heat recovery unit from the driver flue gas.
3. The method of claim 2 , further comprising:
transporting, from the waste heat recovery unit, the generator flue gas into the flue gas stream upstream of the carbon dioxide absorber.
4. The method of claim 2 , further comprising:
transporting, from the compressor driver waste heat recovery unit, the driver flue gas into the flue gas stream upstream of the carbon dioxide absorber.
5. The method of claim 2 , wherein the driver is an internal combustion engine.