Antisolvent crystallization is a crystallization technique, which is normally operated isothermally. However, non-isothermal operation is on occasions performed for solutes that have temperature dependent solubility. This paper shows that it is beneficial to operate antisolvent crystallizers non-isothermally even for solutes whose solubility is weakly dependent on temperature. In this context, it demonstrates the joint control of particle mean size and size distribution coefficient of variation. A non-isothermal crystallization model-based framework is developed for the sodium chloride-ethanol-water system and validated for both isothermal and non-isothermal operations. This framework was used to systematically determine both the optimal antisolvent feed rate and temperature profiles that minimize the coefficient of variation while producing a specified mean crystal size.