Conventional electrochemical precipitation softening often suffers from the low utilization of OH– for hardness precipitation on the cathode surface in traditional undivided electrolytic cell. In this study, an asymmetric cathode was designed to confine the occurrence of H2 evolution reaction at its backside in an undivided electrolytic cell, where the electrodes were placed aslant at an angle of 5° to facilitate the upward motion of H2 bubbles and the water flowing distribution network was used to inhibit the circumfluence of water. This specific cell configuration successfully decoupled the ion convection and electro-migration behaviors, and regulated the convection behaviors of H+ and OH– to counteract their electro-migration behaviors. Specially, theoretical calculations revealed that the OH– convection rate (Vw,b = 0.033 ∼ 0.043 cm s−1) under the combined effects of H2 gas bubbling and water flowing-through cathode at current densities of 1 ∼ 15 mA cm−2 was larger than its electro-migration rate (Ve = 0.0062 ∼ 0.019 cm s−1), which effectively promoted the transport of OH– away from the cathode backside into the bulk solution opposite to the direction toward the anode side. The H+ electro-migration toward the cathode could be also offset by the convection mediated by water flowing-through anode. Thus, the H+–OH– neutralization reaction was effectively inhibited, favoring the hardness precipitation. Under the optimum condition, the developed cell showed a Ca hardness removal efficiency of 80.8 ± 1.18 % and a current efficiency of up to 73 % at an energy consumption of 2.67 ± 0.13 kWh kg−1 CaCO3, which were superior to most electrolytic systems with or without membranes. Generally, this study provides a precisely engineered electrodes configuration for energy-efficient electrochemical water softening in circulating cooling water system.