Process for onboard carbon capture using CO
Described is a system for capturing and recovering carbon dioxide (CO 2 ) from multiple distinct waste heat sources. The system includes an absorber for extracting CO 2 from exhaust gas into a solvent stream selective for absorbing CO 2 and creating a rich solvent stream. A solvent regenerator converts a first fraction of the rich solvent stream into a lean solvent stream and a crude CO 2 vapor. A cross exchanger exchanges heat between lean and rich solvent streams. Several heat exchangers are associated with the solvent regenerator to transfer heat from multiple distinct waste heat sources into a second fraction of the rich solvent stream as well as recover waste heat from the multiple distinct waste heat sources. A compressor converts the crude CO 2 vapor into a concentrated pressurized CO 2 product, and a CO 2 storage tank receives and stores the CO 2 product.
1 . A system for capturing and recovering carbon dioxide (CO2) from two or more distinct waste heat sources, the system comprising:
an absorber configured to extract at least a portion of CO2 from an exhaust gas into a lean solvent stream comprising a solvent selective for absorbing CO2 and to produce a rich solvent stream comprising solvent and absorbed CO2;
a solvent regenerator configured to convert a first fraction of the rich solvent stream into the lean solvent stream and a crude CO2 vapor, wherein the solvent regenerator is coupled to the absorber such that the solvent regenerator is downstream of the absorber for receiving the first fraction of the rich solvent stream and upstream of the absorber for providing the lean solvent stream;
a cross exchanger configured to exchange heat between the lean solvent stream being fed from the solvent regenerator to the absorber and the rich solvent stream being fed from the absorber to the solvent regenerator;
two or more heat exchangers associated with the solvent regenerator and configured to transfer heat from the two or more distinct waste heat sources into a second fraction of the rich solvent stream and to recover waste heat from the two or more distinct waste heat sources;
a compressor configured to convert the crude CO2 vapor into a concentrated pressurized CO2 product, wherein the compressor is downstream of the solvent regenerator; and
a CO2 storage tank configured to both receive and store the concentrated pressurized CO2 product, wherein the CO2 storage tank is downstream of the compressor.
2 . The system of claim 1 , wherein the system is mounted on a mobile vehicle or vessel.
3 . The system of claim 1 , wherein the two or more distinct waste heat sources comprise at least two of an engine exhaust going to a tailpipe of an internal combustion engine; an engine exhaust being recirculated to the internal combustion engine; a boiler exhaust; and an engine coolant.
4 . The system of claim 3 , wherein a first of the two or more heat exchangers is configured to exchange heat between the solvent and the engine exhaust going to the tailpipe and a second of the two or more heat exchangers is configured to exchange heat between the solvent and the engine exhaust being recirculated.
5 . The system of claim 3 , wherein a first of the two or more heat exchangers is configured to exchange heat between the solvent and the engine exhaust going to the tailpipe and a second of the two or more heat exchangers is configured to exchange heat between the solvent and the engine coolant.
6 . The system of claim 3 , wherein a first of the two or more heat exchangers is configured to exchange heat between the solvent and the engine exhaust being recirculated and a second of the two or more heat exchangers is configured to exchange heat between the solvent and the engine coolant.
7 . The system of claim 3 , wherein a first of the two or more heat exchangers is configured to exchange heat between the solvent and the boiler exhaust and a second of the two or more heat exchangers is configured to exchange heat between the solvent and the engine exhaust going to the tailpipe.
8 . The system of claim 3 , wherein a first of the two or more heat exchangers is configured to exchange heat between the solvent and the boiler exhaust and a second of the two or more heat exchangers is configured to exchange heat between the solvent and the engine exhaust being recirculated.
9 . The system of claim 1 , further comprising a pump configured to pressurize the lean solvent stream being fed from the solvent regenerator to the absorber.
10 . The system of claim 9 , further comprising a trim cooler configured to reduce a temperature of the lean solvent stream being fed from the pump before the lean solvent stream returns to the absorber, wherein the trim cooler is downstream of the pump and upstream of the absorber.
11 . The system of claim 1 , further comprising a control system configured to maintain a temperature of the solvent below a set point temperature and a short residence time sufficient to limit solvent degradation.
12 . The system of claim 1 , further comprising a control system configured for one or more of: controlling a flow rate of the first fraction of the rich solvent stream, controlling a flow rate of the second fraction of the rich solvent stream, controlling a temperature or a pressure of the solvent regenerator; or, controlling a temperature or a pressure of the rich solvent stream or the lean solvent stream.
13 . The system of claim 1 , wherein the solvent regenerator comprises a stripper column containing packing material configured to facilitate mass transfer between gas and liquid phases, and wherein the stripper column is configured to receive the first fraction of the rich solvent stream in an upper portion of the stripper column and to receive solvent from the two or more heat exchangers in a lower portion of the stripper column.
14 . A process for capturing and recovering carbon dioxide (CO 2 ) from two or more distinct waste heat sources using a system for capturing and recovering CO 2 mounted on a mobile vehicle or vessel, the process comprising:
introducing a lean solvent stream comprising a solvent selective for absorbing CO 2 into the system;
operating the system such that CO 2 is absorbed into the lean solvent stream using an absorber, forming a rich solvent stream;
operating the system such that heat is transferred from the lean solvent stream into the rich solvent stream using a cross exchanger;
operating the system such that a first fraction of the rich solvent stream is converted into the lean solvent stream and a crude CO 2 vapor using a solvent regenerator;
operating the system such that heat is transferred from the two or more distinct waste heat sources into a second fraction of the rich solvent stream using two or more heat exchangers associated with the solvent regenerator;
operating the system such that the crude CO 2 vapor is converted into a concentrated pressurized CO 2 product using a compressor; and
operating the system such that the concentrated pressurized CO 2 product is received and stored in a CO 2 storage tank.
15 . The process of claim 14 , further comprising passing the concentrated pressurized CO 2 product from the mobile vehicle or vessel.
16 . The process of claim 14 , further comprising operating the system such that a temperature, a flow rate, or a pressure of the rich solvent stream or the lean solvent stream is controlled by a control system.