Electrochemical technologies for wastewater treatment present several promising characteristics to be used as decentralized water treatment systems to provide a sustainable and cost effective growing water supply complementing centralized water supply systems. However, their application and scaling up has been hindered by the high energy input required, and the mass transfer limitations.To address these limitations, the aim of this thesis is to develop a novel decentralized water treatment system to treat greywater produced at household scale. The system, a three-dimensional (3D) electrochemical reactor, comprises a flow-through electrochemical reactor, in which the contaminated solution will pass through the borondoped diamond (BDD) anode mesh, maximizing the total contact surface of the electrode.In addition, granular activated carbon (GAC) has been added as a bed material in the reactor, which has been recognized that can enhance the performance of the conventional two-dimensional (2D) system due to its adsorption properties and by acting as a third electrode within the system.The main goals of this thesis are: (i) to elucidate how the presence of a bed material can enhance the performance of the electrochemical treatment; (ii) to develop a proof-ofconcepts on the performance of a 3D electrochemical oxidation system for the treatment of greywater; (iii) to determine the effect of current density and volume of greywater loaded, and the bed material on the performance of the 3D system; (iv) to explore the viability of the electrochemical regeneration of the bed material when operating the 3D system for the treatment of greywater.The reactor has worked under three different configurations: (i) adsorption onto activated carbon (GAC system), (ii) electrochemical oxidation on BDD anode (2D system), and (iii) combined adsorption and electrochemical oxidation (3D system) for the treatment of simulated (SGW) and real greywater (RGW). Electrochemical experiments were conducted at a fixed current density of 15 A m ) and two different volume loads (2 L and 6 L) to study the effect of these two parameters in the performance ii of the 3D system (Chapter 6). To minimise the adsorption and catalytic effect of the GAC and determine the electrochemical oxidation capacity of the bed material acting as a third electrode, it has been substituted granular graphite (GG) (Chapter 7). Electrochemical regeneration of the GAC in the 3D system has been studied over the time by loading the reactor with saturated GAC (Chapter 8). Finally, an economic analysis has been conducted for the implementation of a 3D electrochemical system at household scale (Chapter 9).The results showed that the efficiency of a conventional 2D electrochemical system can be enhanced by up to 86% for the removal of chemical oxygen demand (COD) and total organic carbon (TOC) in the 3D system. Obtained positive synergy values suggest that the combination of these two processes may trigger other electrochemical reactions in the 3D system while enabling the el...