For the attached Process Flow Diagram $($PFD$)$ for an amine tank, if there is a failure in the measurement device sending the PV signal to TDIC$-103,$ and the PV signal ERRONEOUSLY READS A LOW VALUE $($as shown in the attached PFD below$),$ how would the INITIAL VALUE of the Process Variable $($PV$)$ of TI$-104($Sweet Gas Outlet Temperature from T$-101)$ change prior to any Control$/$Corrective action by any controller?

options are increase, decrease, or no change?