The objective of this study was to assess the efficiency of electrochemical treatment after pre-treatment coagulation-flocculation (CF) in removing chemical oxygen demand (COD) and turbidity from slaughterhouse wastewater (SWW). During the pre-treatment, FeCl3 showed superior efficacy compared to the other coagulant, effectively eliminating 50% of the COD and 68% of the turbidity. Due to the insufficient removal efficiencies of COD and turbidity, a secondary treatment was required. The coagulated effluent was then treated in a continuous electrooxidation reactor (CEO) using a boron-doped diamond (BDD) electrode. The objective was to examine the impact of current density (5 to 30 mA/cm2), wastewater flow rate (0.9 to 3.6 L/hour), and supporting electrolyte concentration (1 to 3 g/L NaCl). The CEO reactor had higher removal efficiency for COD (97%) and turbidity (~100%) when operated under the optimum treatment conditions (j = 30 mA/cm2, Q = 0.9 L/h, pH = 8.5, SE = 3.0 g/L NaCl, and hydraulic retention time (HRT) = 1 hour). At these optimum conditions, the total operating cost (OC) was 3.5 US $/m3 (1.5 US $/kgCOD). The findings demonstrated that the CF + CEO reactor proved to be a very efficient alternate method for the treatment the SWW.