Highly efficient and durable membrane electrode assemblies have been developed by integrating novel electrocatalysts with low CRM materials and will impact the next generation of components for PEM electrolysers. The tested CRM-free electrodes showed promising performances but unfortunately far away from the CRM-based catalysts. Thus, in the second period, PROMET-H2 has decided focus on the CRM drastic reduction route. Two promising candidates were selected for the OER: Iridium deposited on antimony tin oxide (ATO) (CENMAT) and the Ir mixed oxide (CSIC). DLR developed an MEA with 0.2 mgIr cm-2 using Ir mixed oxides (Sr2CaIrO6 perovskite). With a cell voltage of 1.81 V at nominal current density of 2 A cm-2, the performance full fill PROMET-H2 targets with a successful 1000 h long-term test at constant 2 A cm-2 demonstrated the Ir content in the MEA can be drastically reduced without compromising performance or durability. In parallel FZJ measured similar performances with 0.2 mgIr cm-2 using Ir ATO (CENMAT). The activation at MEA level and scalability potential were the arguments for PROMET-H2 to selected the Ir ATO to produce the MEAs for the NEL and PROPULS short stacks. The MEAs produced by FZJ have been already sent to Propuls and NEL. Chemours continued with the development of novel membranes (80 µm thickness) that showed remarkably lowered H2 cross-over (ca. 0.2% H2 in O2) and was able to fulfill PROMET-H2 target of < 2% H2 in O2 at 0.5 A cm-2. But some stability studies and internal Chemours decision excluded the membrane for assembly in the PROMET-H2 stacks. MONOLITHOS develops a low cost and simple recycling process that allows the reuse of the catalysts, which is necessary for environmental and economic reasons. The hydrometallurgical leaching process for PGMs recovery developed by MONOLITHOS is proposed for CRMs recovery from End-of-Life PEMWE MEAs with efficiency higher than 99% for Pt content and 60% for Ir. Stainless steel (SS) based bipolar plates (BPP) were coated and tested with dense coatings (Nb/Ti) by vacuum plasma spray. Electrochemical accelerated stress tests in acid environment verified the stability of the coatings protecting the stainless steel from corrosion. These BPPs have lower cost than the state-of-the-art Ti-based ones. In order to study the restricted performances at stack level using low Ir loadings (0.2mgIrcm-2) PROMET-H2 will compare 3 different PTLs coatings: two with PGM low content and one without PGM. The 3 different configurations of PTLs were sent to NEL. The short stack with PROMET-H2 MEAs was assembled at NEL and has been purchased to FZJ and it will be tested in the last period of the project. From results obtained in the second period, PROMET-H2 will try use SS-BPP without any coating in the PROMET-H2 stack. The baseline stack is ready to be tested in the last period of the project. DLR has develop a segmented cell for the Propuls novel Hydraulic stack. The segmented cell has been designed with 44 segments (approx. 4.8 cm2 segment area) and 16 temperature sensors giving the chance to measure independently the current in 44 areas and 16 temperatures. The board was calibrated and tested. The complete set-up is ready to be assembled and will be tested in the third period. The interfaces and boundaries between stack, system and site were clarified and a new system concept for the integration of a 25-kW electrolysis stack based on hydraulic compression was developed. The delivery of the system to Air Liquide is scheduled for end of June 2023. A report about techno-economic analysis (TEA) and life cycle assessment (LCA) were developed. The development in the PROMET-H2 project will reach industrial levels.