the maximum sorbent loading at low temperatures drops to 0.1 and the temperature region allowing for near full H2 conversion is extended to higher temperatures. In comparison to the conventional case, the equilibrium H2 conversion is > 90 % at 400 °C. These results indicate that the region of near full conversion can be pushed to higher temperatures by adding more sorbent to the system, which also becomes apparent from Figure (d) at a sorbent ratio of 1000. Here, however, the sorbent loading approaches 0 emphasizing the trade-off between high sorbent usability and high H2 conversion. This can be explained by the absorption driving force, which is lower at high sorbent loadings, but on the other hand crucial for achieving an impact on the synthesis equilibrium.