The acetone+1-butanol+ethanol (ABE) fermentation has a long history but still faces the challenge of enhancing the low ABE concentration to reduce production cost. Nowadays there is an unprecedented resurgence of interest in separation and purification technology to recovery ABE from fermentation broth. Here we describe a simple salting out procedure for extracting ABE fermentation products efficiently from model solutions/fermentation broth by employing tripotassium phosphate (K<SUB>3</SUB>PO<SUB>4</SUB>). Increasing the K<SUB>3</SUB>PO<SUB>4</SUB> content permits the liquid-liquid splits and enables the recovery of ABE. The liquid-liquid equilibria were mainly determined by the K<SUB>3</SUB>PO<SUB>4</SUB> content and slightly affected by temperature and original solvents level. The correlation between the solubility of ABE and the molality of K<SUB>3</SUB>PO<SUB>4</SUB> demonstrated this. More than 90wt% of ABE was recovered from the model solutions/fermentation broth and more than 99.75% of water was removed. This study provides a means to reduce the energy demand of the subsequent distillation process for ABE purification.