Accurate solubility data is essential to make critical decisions from the earliest stage of drug discovery, through the entire process development, formulation, and up to process design. The present research work aims to evaluate the solid–liquid equilibrium data of para-tert-butylbenzoic acid (PTBBA) in binary systems such as acetonitrile + water, isopropyl alcohol + water, and isopropyl alcohol + acetonitrile at 288.15 to 328.15 K and a ternary solvent mixture of isopropyl alcohol + acetonitrile + water system in the temperature range of 298.15 to 323.15 K with varying mass fraction of the binary mixture (isopropyl alcohol + acetonitrile) for a constant mass fraction of water (0.1 and 0.3) using gravimetric and titrimetric methods. It is observed that the solubility of PTBBA increases with an increase in temperature for all the selected solvent systems. Moreover, the solubility of PTBBA in the binary and ternary system is affected by an increase in the mass fraction of water at a given temperature, which acts as an antisolvent. The measured data is correlated with various thermodynamic models such as Van’t Hoff equation, Modified Apelblat equation, Buchowski equation, and Wilson models. It is observed that there is a good agreement between measured and calculated values with an average relative deviation of 0.95 for isopropyl alcohol + acetonitrile system in the case of the modified Apelblat equation.