Figure 5 compares the effects of TBPO and TBAB on lowering the
pressure requirement for flue gas hydrate formation. With an initial
reagent loading of 5 wt%, at any given temperature under
study, the TBPO SCHs had much lower phase equilibrium pressure
than TBAB SCHs. With an initial reagent loading of 26 wt%, the
TBPO SCHs had slightly lower phase equilibrium pressure than
TBAB SCHs at temperature above 287 K. Below T = 287 K, however,
TBAB appears to be more effective than TBPO in reducing the
hydrate equilibrium pressure of flue gas. Overall, TBPO seems more
effective than TBAB in reducing the phase equilibrium pressure.
Figure 5 compares the effects of TBPO and TBAB on lowering thepressure requirement for flue gas hydrate formation. With an initialreagent loading of 5 wt%, at any given temperature understudy, the TBPO SCHs had much lower phase equilibrium pressurethan TBAB SCHs. With an initial reagent loading of 26 wt%, theTBPO SCHs had slightly lower phase equilibrium pressure thanTBAB SCHs at temperature above 287 K. Below T = 287 K, however,TBAB appears to be more effective than TBPO in reducing thehydrate equilibrium pressure of flue gas. Overall, TBPO seems moreeffective than TBAB in reducing the phase equilibrium pressure.
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