There is described a method and
system for
carbon dioxide capture using temperature-swing adsorption. First and second, respectively third and fourth temperature-swing adsorber units (TSAD1, TSAD2, TSAC1, TSAC2) are provided that are operable in alternate adsorption and
desorption cycles to capture and remove water and
carbon dioxide, respectively, from the
exhaust gas, each of the temperature-swing adsorber units (TSAD1, TSAD2, TSAC1, TSAC2) including a
sorbent bed (AD) and a
heat exchanger structure (HEX) thermally coupled to the
sorbent bed (AD). Hot
exhaust gas coming from the
internal combustion engine (ICE) is routed through the
heat exchanger structure (HEX) of that one (TSAD1; TSAD2) of the first and second temperature-swing adsorber units (TSAD1, TSAD2) that undergoes a
desorption cycle, to sustain
desorption of water adsorbed by the
sorbent bed (AD) thereof, as well as through the
heat exchanger structure (HEX) of that one (TSAC1; TSAC2) of the third and fourth temperature-swing adsorber units (TSAC1, TSAC2) that undergoes a desorption cycle, to sustain desorption of
carbon dioxide adsorbed by the sorbent bed (AD) thereof. The
exhaust gas is furthermore cooled to produce cold exhaust gas, at least part of which is routed through the sorbent bed (AD) of that one (TSAD2; TSAD1) of the first and second temperature-swing adsorber units (TSAD1, TSAD2) that undergoes an adsorption cycle, to cause adsorption of water by the sorbent bed (AD), and then through the sorbent bed (AD) of that one (TSAC2; TSAC1) of the third and fourth temperature-swing adsorber units (TSAC1, TSAC2) that undergoes an adsorption cycle, to cause adsorption of carbon dioxide by the sorbent bed (AD). Operation of the first to fourth temperature-swing adsorber units (TSAD1, TSAD2, TSAC1, TSAC2) is then switched from the desorption cycle to the adsorption cycle, and vice versa, and the process is cyclically repeated.