Cryogenic carbon capture (CCC) is an innovative technology to desublimate
$\text {CO}_2$
out of industrial flue gases. A comprehensive understanding of
$\text {CO}_2$
desublimation and sublimation is essential for widespread application of CCC, which is highly challenging due to the complex physics behind. In this work, a lattice Boltzmann (LB) model is proposed to study
$\text {CO}_2$
desublimation and sublimation for different operating conditions, including the bed temperature (subcooling degree
$\Delta T_s$
), gas feed rate (Péclet number
$Pe $
) and bed porosity (
$\psi$
). The
$\text {CO}_2$
desublimation and sublimation properties are reproduced. Interactions between convective
$\text {CO}_2$
supply and desublimation/sublimation intensity are analysed. In the single-grain case,
$Pe $
is suggested to exceed a critical value
$Pe _c$
at each
$\Delta T_s$
to avoid the convection-limited regime. Beyond
$Pe _c$
, the
$\text {CO}_2$
capture rate (
$v_c$
) grows monotonically with
$\Delta T_s$
, indicating a desublimation-limited regime. In the packed bed case, multiple grains render the convective
$\text {CO}_2$
supply insufficient and make CCC operate under the convection-limited mechanism. Besides, in small-
$\Delta T_s$
and high-
$Pe $
tests,
$\text {CO}_2$
desublimation becomes insufficient compared with convective
$\text {CO}_2$
supply, thus introducing the desublimation-limited regime with severe
$\text {CO}_2$
capture capacity loss (
$\eta _d$
). Moreover, large
$\psi$
enhances gas mobility while decreasing cold grain volume. A moderate porosity
$\psi _c$
is recommended for improving the
$\text {CO}_2$
capture performance. By analysing
$v_c$
and
$\eta _d$
, regime diagrams are proposed in
$\Delta T_s$
–
$Pe $
space to show distributions of convection-limited and desublimation-limited regimes, thus suggesting optimal conditions for efficient
$\text {CO}_2$
capture. This work develops a viable LB model to examine CCC under extensive operating conditions, contributing to facilitating its application.