This paper presents an investigation of a storage option of green hydrogen (H 2 ) in the form of ammonia (NH 3 ) based on system simulations considering detailed technical properties. Experimental data from a 1 MW PEM electrolyzer is used to develop an electrolyzer model and downstream a kinetic reactor for NH 3 synthesis. Exemplarily, the electricity is supposed to be supplied by a hydropower plant in Norway. An economical evaluation of the plant is performed for optimized process parameters. The costs of H 2 and NH 3 are calculated based on electrolyzer investment costs published for deployment between 2020 and 2030 and several electricity cost scenarios. From the results, a broad economic optimum of the operating range of the electrolyzer in the entire plant is obtained. This work provides a basis for the future evaluation of complex plants with electrolyzers for the production of green ammonia as well as strategies for the reduction of costs of green NH 3 in the future.