High temperature hydrogen production: Design of a 750KW demonstration plant for a two step thermochemical cycle

• Published in: Solar energy Vol. 135; pp. 232 - 241
• Main Authors: Säck, J.-P., Breuer, S., Cotelli, P., Houaijia, A., Lange, M., Wullenkord, M., Spenke, C., Roeb, M., Sattler, Chr
• Format: Journal Article
• Language: English
• Published: Elsevier Ltd 01.10.2016
• Subjects: Heat losses; Hydrogen; Receiver–reactor; Solar power tower; Thermochemical cycle; Solar power tower; Thermochemical cycle; Hydrogen; Heat losses; Receiver–reactor
• ISSN: 0038-092X; 1471-1257
• DOI: 10.1016/j.solener.2016.05.059

•Development of a plant for hydrogen production with a solar tower.•Thermodynamic model has been developed to check if the thermal power can be supplied.•Opticad model for the needed input power has been developed.•The scheme and the layout of the plant to feed the reactors have been studied.•Definition of Balance of Plant (BoP) components and sub-components has been done. The present work describes the study of a solar reactor for a two-step solar thermo-chemical water splitting cycle concerning the EU-project Hydrosol Plant, which aims to build a plant at the end of 2016 on a solar tower at the Plataforma Solar de Almería with a thermal input power of 750kW to produce 3kg/week of hydrogen. The process applies nickel-ferrite as reactive species, which works optimally at 1100°C for the water splitting step and at 1400°C for the regeneration step. This material is provided in form of monoliths which are used in cars as catalytic converter. On the platform three reactors are placed to reach a volume of about 0.3m3 of active material inside the reactor chambers. During the operations two of these will be regenerated while one will work on water splitting, to reach a quasi-continuous hydrogen production. The design concept of the reactor is taken from the SOLREF reactor, which was originally developed by DLR for methane reforming at 900°C and 10bar. The scheme and the layout of the plant to feed the reactors have been studied, too. A thermodynamic model for the regeneration step has been also developed to check if the thermal power demand of the three reactors can be supplied by the defined thermal input power. The differences to the other HYDROSOL projects are: The Upscaling from 100kW to 750kW, the usage of monoliths completely made of nickel-ferrite and the control strategy with three reactors instead of two.