Operational Data of a 100 kW Proton Exchange Membrane (PEM) Electrolyzer: Collection 2018–2023 (ICPSR doi:10.26165/JUELICH-DATA/FEKKSS)

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Part 2: Study Description
Part 5: Other Study-Related Materials
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Operational Data of a 100 kW Proton Exchange Membrane (PEM) Electrolyzer: Collection 2018–2023

doi:10.26165/JUELICH-DATA/FEKKSS

Jülich DATA

2025-11-10

1

Keller, Roger; Rauls, Edward; Hehemann, Michael; Müller, Martin, 2025, "Operational Data of a 100 kW Proton Exchange Membrane (PEM) Electrolyzer: Collection 2018–2023", https://doi.org/10.26165/JUELICH-DATA/FEKKSS, Jülich DATA, V1

Operational Data of a 100 kW Proton Exchange Membrane (PEM) Electrolyzer: Collection 2018–2023

doi:10.26165/JUELICH-DATA/FEKKSS

Keller, Roger (FZJ / IET-4)

Rauls, Edward (FZJ / IET-4)

Hehemann, Michael (FZJ / IET-4)

Müller, Martin (FZJ / IET-4)

Keller, Roger

Jülich DATA

Keller, Roger

Keller, Roger

2025-01-28

2025-01-28

Engineering

This data set contains detailed measurement and set point data from a 100 kW Proton Exchange Membrane (PEM) electrolyzer test rig developed at IET-4, covering the period 2018–2023 with approximately 200 individual data sets. The system was operated under a wide range of user-defined load profiles, e.g. wind power and photovoltaic (PV). All relevant operational data (~120 measurement values) were continuously recorded, including electrical characteristics (voltage and current), temperature distributions, gas flow rates, and efficiency metrics, as well as auxiliary parameters required for detailed system assessment. The data collection campaign was designed to support systematic investigations on electrochemical performance, thermal behavior, start-up and ramping dynamics, and system efficiency. It further enables research on advanced thermal control strategies [1], transient behavior during start-up phases [2], dynamic system modeling [3], data-driven operational optimization [4], and efficiency evaluation [5]. In addition, the dataset provides a robust foundation for material degradation studies, system design optimization, and the development of advanced control loops and operational strategies. More detailed information on the 100 kW PEM electrolyzer test rig can be found in the referenced publications. Information on the structure and organization of the data and the process flow diagram can be found in the the folder "Documentation".

2018-02-06-2023-11-29

2018-02-06-2023-11-29

experimentel data

The data set is organized in a structured and consistent way. All data files start with “Data_measured”, while the corresponding set point files begin with “Setpoint-Profile”. Set points can either be defined manually or automatically using a predefined set point sequence stored in a file. For each set point file, there exists a corresponding measurement file — but not necessarily the other way around, since some experiments were operated manually without automated set point control. To get an overview of all available measurements, it is recommended to display the data set in "tree structure" view. This provides a quick overview of available measurement days and a short description of what was measured. If a folder contains only one file, the system was operated manually. If a folder contains two files, the experiment was performed automatically using a set point profile.

CC0 Waiver

10.1016/j.conengprac.2021.104992

[1] Roger Keller et al., An adaptive model-based feedforward temperature control of a 100 kW PEM electrolyzer, Control Engineering Practice (2022),

10.1016/j.apenergy.2022.120350

[2] Edward Rauls et al., Favorable Start-Up behavior of polymer electrolyte membrane water electrolyzers, Applied Energy (2023),

10.1016/j.ijhydene.2024.03.302

[3] Edward Rauls et al., System dynamics of polymer electrolyte membrane water electrolyzers and impact of renewable energy sources on systems design, International Journal of Hydrogen Energy (2024),

10.1016/j.apenergy.2025.126014

[4] Roger Keller et al., Experimental Demonstration of Dynamic Demand Response Scheduling for PEM-Electrolyzers, Applied Energy (2025),

10.18154/RWTH-2025-02739

[5] Edward Rauls, Dissertation, Dynamischer Betrieb von Polymer-Elektrolyt-Membran Wasserelektrolyseuren, RWTH Aachen (2025),

Label:

01_Data_Overview.pdf

Text:

This file gives an overview of the data

application/pdf

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01_Process_flow_diagram_100kW-electrolyzer.pdf

Text:

Process flow diagram 100 kW electrolyzer

application/pdf

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01_Structure_Organization_Data.pdf

Text:

This file contains a detailed overview on the structure and organization of the measured data and the used set point profiles.

application/pdf

Label:

2018-02-06_Data_startup-phase_manual-mode.xlsx

Text:

The data corresponds to the startup phase of the 100 kW Proton Exchange Membrane (PEM) electrolyzer, during which the system’s control strategies were tested and initiated. All setpoints were configured manually, without the implementation of automated control sequences.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2018-02-07_Data_startup-phase_manual-mode.xlsx

Text:

The data corresponds to the startup phase of the 100 kW Proton Exchange Membrane (PEM) electrolyzer, during which the system’s control strategies were tested and initiated. All setpoints were configured manually, without the implementation of automated control sequences.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2018-02-07_Data_startup-phase_manual-mode.xlsx

Text:

The data corresponds to the startup phase of the 100 kW Proton Exchange Membrane (PEM) electrolyzer, during which the system’s control strategies were tested and initiated. All setpoints were configured manually, without the implementation of automated control sequences.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2018-02-16_Data_startup-phase_manual-mode.xlsx

Text:

The data corresponds to the startup phase of the 100 kW Proton Exchange Membrane (PEM) electrolyzer, during which the system’s control strategies were tested and initiated. All setpoints were configured manually, without the implementation of automated control sequences.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2018-02-19_Data_startup-phase_manual-mode.xlsx

Text:

The data corresponds to the startup phase of the 100 kW Proton Exchange Membrane (PEM) electrolyzer, during which the system’s control strategies were tested and initiated. All setpoints were configured manually, without the implementation of automated control sequences.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2018-02-20_Data_startup-phase_maunal-mode_high-current.xlsx

Text:

The data corresponds to the startup phase of the 100 kW Proton Exchange Membrane (PEM) electrolyzer, during which the system’s control strategies were tested and initiated. All setpoints were configured manually, without the implementation of automated control sequences. The current density was manually regulated up to 2 A/cm² during the testing period.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2018-02-21_Data_startup-phase_manual-mode_high-current.xlsx

Text:

The data corresponds to the startup phase of the 100 kW Proton Exchange Membrane (PEM) electrolyzer, during which the system’s control strategies were tested and initiated. All setpoints were configured manually, without the implementation of automated control sequences. The current density was manually regulated up to 2 A/cm² during the testing period.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2018-02-22_Data_startup-phase_manual-mode.xlsx

Text:

The data corresponds to the startup phase of the 100 kW Proton Exchange Membrane (PEM) electrolyzer, during which the system’s control strategies were tested and initiated. All setpoints were configured manually, without the implementation of automated control sequences.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2018-02-23_Data_startup-phase_manual-mode_pressure-control-loop.xlsx

Text:

The data corresponds to the startup phase of the 100 kW Proton Exchange Membrane (PEM) electrolyzer, during which the system’s control strategies were tested and initiated. All setpoints were configured manually, without the implementation of automated control sequences. During this phase, the pressure control loop was activated and tested to ensure stable system operation under varying load conditions.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2018-02-26_Data_startup-phase_manual-mode_pressure-control-loop.xlsx

Text:

The data corresponds to the startup phase of the 100 kW Proton Exchange Membrane (PEM) electrolyzer, during which the system’s control strategies were tested and initiated. All setpoints were configured manually, without the implementation of automated control sequences. During this phase, the pressure control loop was activated and tested to ensure stable system operation under varying load conditions.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2018-02-27_Data_startup-phase_manual-mode_pressure-control-loop.xlsx

Text:

The data corresponds to the startup phase of the 100 kW Proton Exchange Membrane (PEM) electrolyzer, during which the system’s control strategies were tested and initiated. All setpoints were configured manually, without the implementation of automated control sequences. During this phase, the pressure control loop was activated and tested to ensure stable system operation under varying load conditions.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2018-02-28_Data_startup-phase_manual-mode_pressure-control-loop.xlsx

Text:

The data corresponds to the startup phase of the 100 kW Proton Exchange Membrane (PEM) electrolyzer, during which the system’s control strategies were tested and initiated. All setpoints were configured manually, without the implementation of automated control sequences. During this phase, the pressure control loop was activated and tested to ensure stable system operation under varying load conditions.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2018-03-06_Data_startup-phase_manual-mode_pressure-control-loop.xlsx

Text:

The data corresponds to the startup phase of the 100 kW Proton Exchange Membrane (PEM) electrolyzer, during which the system’s control strategies were tested and initiated. All setpoints were configured manually, without the implementation of automated control sequences. During this phase, the pressure control loop was activated and tested to ensure stable system operation under varying load conditions.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2018-03-07_Data_startup-phase_manual-mode_heating-up-curve .xlsx

Text:

The data corresponds to the startup phase of the 100 kW Proton Exchange Membrane (PEM) electrolyzer, during which the system’s control strategies were tested and initiated. All setpoints were configured manually, without the implementation of automated control sequences. Additionally, a heating-up temperature curve was recorded to monitor the thermal behavior of the system during initial operation. During this phase, operational parameters for the thermal behavior, e.g. heat capacity and heat transfer, were establish.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2018-03-07_Data_startup-phase_manual-mode_pressure-control-loop.xlsx

Text:

The data corresponds to the startup phase of the 100 kW Proton Exchange Membrane (PEM) electrolyzer, during which the system’s control strategies were tested and initiated. All setpoints were configured manually, without the implementation of automated control sequences. During this phase, the pressure control loop was activated and tested to ensure stable system operation under varying load conditions.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2018-03-08_Data_startup-phase_manual-mode_pressure-control-loop.xlsx

Text:

The data corresponds to the startup phase of the 100 kW Proton Exchange Membrane (PEM) electrolyzer, during which the system’s control strategies were tested and initiated. All setpoints were configured manually, without the implementation of automated control sequences. During this phase, the pressure control loop was activated and tested to ensure stable system operation under varying load conditions.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2018-03-14_Data_startup-phase_manual-mode_pressure-control-loop.xlsx

Text:

The data corresponds to the startup phase of the 100 kW Proton Exchange Membrane (PEM) electrolyzer, during which the system’s control strategies were tested and initiated. All setpoints were configured manually, without the implementation of automated control sequences. During this phase, the pressure control loop was activated and tested to ensure stable system operation under varying load conditions.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2018-03-22_Data_startup-phase_manual-mode_pressure-control-loop.xlsx

Text:

The data corresponds to the startup phase of the 100 kW Proton Exchange Membrane (PEM) electrolyzer, during which the system’s control strategies were tested and initiated. All setpoints were configured manually, without the implementation of automated control sequences. During this phase, the pressure control loop was activated and tested to ensure stable system operation under varying load conditions.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2018-03-28_Data_startup-phase_manual-mode_pressure-control-loop.xlsx

Text:

The data corresponds to the startup phase of the 100 kW Proton Exchange Membrane (PEM) electrolyzer, during which the system’s control strategies were tested and initiated. All setpoints were configured manually, without the implementation of automated control sequences. During this phase, the pressure control loop was activated and tested to ensure stable system operation under varying load conditions.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2018-04-16_Data_startup-phase_manual-mode_pressure-curve-emergency-stop.xlsx

Text:

The data corresponds to the startup phase of the 100 kW Proton Exchange Membrane (PEM) electrolyzer, during which the system’s control strategies were tested and initiated. All setpoints were configured manually, without the implementation of automated control sequences. During this phase, a pressure curve due to emergency stop was recorded.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2018-04-20_Data_startup-phase_manual-mode_heating-up-curve.xlsx

Text:

The data corresponds to the startup phase of the 100 kW Proton Exchange Membrane (PEM) electrolyzer, during which the system’s control strategies were tested and initiated. All setpoints were configured manually, without the implementation of automated control sequences. Additionally, a heating-up temperature curve was recorded to monitor the thermal behavior of the system during initial operation. During this phase, operational parameters for the thermal behavior, e.g. heat capacity and heat transfer, were establish.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2018-05-22_Data_startup-phase_manual-mode_pressure-control-loop.xlsx

Text:

The data corresponds to the startup phase of the 100 kW Proton Exchange Membrane (PEM) electrolyzer, during which the system’s control strategies were tested and initiated. All setpoints were configured manually, without the implementation of automated control sequences. During this phase, the pressure control loop was activated and tested to ensure stable system operation under differential pressure conditions.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2018-05-23_Data_startup-phase_manual-mode_pressure-control-loop.xlsx

Text:

The data corresponds to the startup phase of the 100 kW Proton Exchange Membrane (PEM) electrolyzer, during which the system’s control strategies were tested and initiated. All setpoints were configured manually, without the implementation of automated control sequences. During this phase, the pressure control loop was activated and tested to ensure stable system operation under differential pressure conditions.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2018-06-04_Data_startup-phase_manual-mode_pressure-control-loop.xlsx

Text:

The data corresponds to the startup phase of the 100 kW Proton Exchange Membrane (PEM) electrolyzer, during which the system’s control strategies were tested and initiated. All setpoints were configured manually, without the implementation of automated control sequences. During this phase, the pressure control loop was activated and tested to ensure stable system operation under varying differential pressure conditions.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2018-06-05_Data_startup-phase_manual-mode_pressure-control-loop.xlsx

Text:

The data corresponds to the startup phase of the 100 kW Proton Exchange Membrane (PEM) electrolyzer, during which the system’s control strategies were tested and initiated. All setpoints were configured manually, without the implementation of automated control sequences. During this phase, the pressure control loop was activated and tested to ensure stable system operation under varying differential pressure conditions.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2018-06-06_Data_startup-phase_manual-mode_pressure-control-loop.xlsx

Text:

The data corresponds to the startup phase of the 100 kW Proton Exchange Membrane (PEM) electrolyzer, during which the system’s control strategies were tested and initiated. All setpoints were configured manually, without the implementation of automated control sequences. During this phase, the pressure control loop was activated and tested to ensure stable system operation under varying differential pressure conditions.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2018-06-11_Data_startup-phase_manual-mode_pressure-control-loop.xlsx

Text:

The data corresponds to the startup phase of the 100 kW Proton Exchange Membrane (PEM) electrolyzer, during which the system’s control strategies were tested and initiated. All setpoints were configured manually, without the implementation of automated control sequences. During this phase, the pressure control loop was activated and tested to ensure stable system operation under varying load conditions.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2018-06-12_Data_startup-phase_manual-mode_pressure-control-loop.xlsx

Text:

The data corresponds to the startup phase of the 100 kW Proton Exchange Membrane (PEM) electrolyzer, during which the system’s control strategies were tested and initiated. All setpoints were configured manually, without the implementation of automated control sequences. During this phase, the pressure control loop was activated and tested to ensure stable system operation under varying load conditions. The set-point of the pressure was 18 bar on the cathode and 17 bar on the anode side.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2018-06-13_Data_startup-phase_manual-mode_pressure-control-loop.xlsx

Text:

The data corresponds to the startup phase of the 100 kW Proton Exchange Membrane (PEM) electrolyzer, during which the system’s control strategies were tested and initiated. All setpoints were configured manually, without the implementation of automated control sequences. During this phase, the pressure control loop was activated and tested to ensure stable system operation under varying load conditions. The set-point of the pressure was 18 bar on the cathode and 17 bar on the anode side.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2018-06-14_Data_startup-phase_manual-mode_pressure-control-loop.xlsx

Text:

The data corresponds to the startup phase of the 100 kW Proton Exchange Membrane (PEM) electrolyzer, during which the system’s control strategies were tested and initiated. All setpoints were configured manually, without the implementation of automated control sequences. During this phase, the pressure control loop was activated and tested to ensure stable system operation under varying differential pressure conditions.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2018-08-02_Data_startup-phase_manual-mode_pressure-control-loop.xlsx

Text:

The data corresponds to the startup phase of the 100 kW Proton Exchange Membrane (PEM) electrolyzer, during which the system’s control strategies were tested and initiated. All setpoints were configured manually, without the implementation of automated control sequences. During this phase, the pressure control loop was activated and tested to ensure stable system operation under varying differential pressure conditions.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2018-08-15_Data_startup-phase_manual-mode_pressure-control-loop.xlsx

Text:

The data corresponds to the startup phase of the 100 kW Proton Exchange Membrane (PEM) electrolyzer, during which the system’s control strategies were tested and initiated. All setpoints were configured manually, without the implementation of automated control sequences. During this phase, the pressure control loop was activated and tested to ensure stable system operation under varying load conditions.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2018-08-28_Data_startup-phase_manual-mode_pressure-control-loop.xlsx

Text:

The data corresponds to the startup phase of the 100 kW Proton Exchange Membrane (PEM) electrolyzer, during which the system’s control strategies were tested and initiated. All setpoints were configured manually, without the implementation of automated control sequences. During this phase, the pressure control loop was activated and tested to ensure stable system operation under varying load conditions and pressure set-points.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2018-08-30_Data_startup-phase_manual-mode_temperature-control-loop.xlsx

Text:

The data corresponds to the startup phase of the 100 kW Proton Exchange Membrane (PEM) electrolyzer, during which the system’s control strategies were tested and initiated. All setpoints were configured manually, without the implementation of automated control sequences. During this phase, the temperature control loop was activated and tested to ensure thermal stable system operation under varying load conditions.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2018-09-24_Data_startup-phase_manual-mode_temperature-control-loop.xlsx

Text:

The data corresponds to the startup phase of the 100 kW Proton Exchange Membrane (PEM) electrolyzer, during which the system’s control strategies were tested and initiated. All setpoints were configured manually, without the implementation of automated control sequences. During this phase, the temperature control loop was activated and tested to ensure thermal stable system operation under varying load conditions.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2018-10-01_Data_startup-phase_manual-mode_temperature-control-loop.xlsx

Text:

The data corresponds to the startup phase of the 100 kW Proton Exchange Membrane (PEM) electrolyzer, during which the system’s control strategies were tested and initiated. All setpoints were configured manually, without the implementation of automated control sequences. During this phase, the temperature control loop was activated and tested to ensure thermal stable system operation under varying load conditions.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2018-10-02_Data_startup-phase_manual-mode_temperature-control-loop.xlsx

Text:

The data corresponds to the startup phase of the 100 kW Proton Exchange Membrane (PEM) electrolyzer, during which the system’s control strategies were tested and initiated. All setpoints were configured manually, without the implementation of automated control sequences. During this phase, the temperature control loop was activated and tested to ensure thermal stable system operation under varying load conditions.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2018-10-08_Data_startup-phase_manual-mode_temperature-control-loop.xlsx

Text:

The data corresponds to the startup phase of the 100 kW Proton Exchange Membrane (PEM) electrolyzer, during which the system’s control strategies were tested and initiated. All setpoints were configured manually, without the implementation of automated control sequences. During this phase, the temperature control loop was activated and tested to ensure thermal stable system operation under varying load conditions.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2018-12-07_Data_startup-phase_manual-mode_temperature-control-loop.xlsx

Text:

The data corresponds to the startup phase of the 100 kW Proton Exchange Membrane (PEM) electrolyzer, during which the system’s control strategies were tested and initiated. All setpoints were configured manually, without the implementation of automated control sequences. During this phase, the temperature control loop was activated and tested to ensure thermal stable system operation under varying load conditions.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2019-02-14_Data_startup-phase_manual-mode_temperature-control-loop.xlsx

Text:

The data corresponds to the startup phase of the 100 kW Proton Exchange Membrane (PEM) electrolyzer, during which the system’s control strategies were tested and initiated. All setpoints were configured manually, without the implementation of automated control sequences. During this phase, the temperature control loop was activated and tested to ensure thermal stable system operation under varying load conditions.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2019-02-18_1st_Data_startup-phase_manual-mode_temperature-control-loop.xlsx

Text:

The data corresponds to the startup phase of the 100 kW Proton Exchange Membrane (PEM) electrolyzer, during which the system’s control strategies were tested and initiated. All setpoints were configured manually, without the implementation of automated control sequences. During this phase, the temperature control loop was activated and tested to ensure thermal stable system operation under varying load conditions and different control parameters.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2019-02-18_2nd_Data_startup-phase_manual-mode_temperature-control-loop.xlsx

Text:

The data corresponds to the startup phase of the 100 kW Proton Exchange Membrane (PEM) electrolyzer, during which the system’s control strategies were tested and initiated. All setpoints were configured manually, without the implementation of automated control sequences. During this phase, the temperature control loop was activated and tested to ensure thermal stable system operation under varying load conditions and different control parameters.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2019-02-19_1st_Data_startup-phase_manual-mode_temperature-control-loop.xlsx

Text:

The data corresponds to the startup phase of the 100 kW Proton Exchange Membrane (PEM) electrolyzer, during which the system’s control strategies were tested and initiated. All setpoints were configured manually, without the implementation of automated control sequences. During this phase, the temperature control loop was activated and tested to ensure thermal stable system operation under varying load conditions and different control parameters.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2019-02-19_2nd_Data_startup-phase_manual-mode_temperature-control-loop.xlsx

Text:

The data corresponds to the startup phase of the 100 kW Proton Exchange Membrane (PEM) electrolyzer, during which the system’s control strategies were tested and initiated. All setpoints were configured manually, without the implementation of automated control sequences. During this phase, the temperature control loop was activated and tested to ensure thermal stable system operation under varying load conditions and different control parameters.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2019-02-20_Data_startup-phase_manual-mode_temperature-control-loop.xlsx

Text:

The data corresponds to the startup phase of the 100 kW Proton Exchange Membrane (PEM) electrolyzer, during which the system’s control strategies were tested and initiated. All setpoints were configured manually, without the implementation of automated control sequences. During this phase, the temperature control loop was activated and tested to ensure thermal stable system operation under varying load conditions and different control parameters.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2019-02-21_Data_startup-phase_manual-mode_temperature-control-loop.xlsx

Text:

The data corresponds to the startup phase of the 100 kW Proton Exchange Membrane (PEM) electrolyzer, during which the system’s control strategies were tested and initiated. All setpoints were configured manually, without the implementation of automated control sequences. During this phase, the temperature control loop was activated and tested to ensure thermal stable system operation under varying load conditions and different control parameters.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2019-02-22_Data_startup-phase_manual-mode_temperature-control-loop.xlsx

Text:

The data corresponds to the startup phase of the 100 kW Proton Exchange Membrane (PEM) electrolyzer, during which the system’s control strategies were tested and initiated. All setpoints were configured manually, without the implementation of automated control sequences. During this phase, the temperature control loop was activated and tested to ensure thermal stable system operation under varying load conditions and different control parameters.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2019-02-25_Data_startup-phase_manual-mode_temperature-control-loop.xlsx

Text:

The data corresponds to the startup phase of the 100 kW Proton Exchange Membrane (PEM) electrolyzer, during which the system’s control strategies were tested and initiated. All setpoints were configured manually, without the implementation of automated control sequences. During this phase, the temperature control loop was activated and tested to ensure thermal stable system operation under varying load conditions and different control parameters

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2019-03-06_Data_startup-phase_manual-mode_temperature-control-loop.xlsx

Text:

The data corresponds to the startup phase of the 100 kW Proton Exchange Membrane (PEM) electrolyzer, during which the system’s control strategies were tested and initiated. All setpoints were configured manually, without the implementation of automated control sequences. During this phase, the temperature control loop was activated and tested to ensure thermal stable system operation under varying load conditions and different control parameters.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2019-03-08_Data_startup-phase_manual-mode_temperature-control-loop.xlsx

Text:

The data corresponds to the startup phase of the 100 kW Proton Exchange Membrane (PEM) electrolyzer, during which the system’s control strategies were tested and initiated. All setpoints were configured manually, without the implementation of automated control sequences. During this phase, the temperature control loop was activated and tested to ensure thermal stable system operation under varying load conditions and different control parameters.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2019-03-11_Data_startup-phase_manual-mode_temperature-control-loop.xlsx

Text:

The data corresponds to the startup phase of the 100 kW Proton Exchange Membrane (PEM) electrolyzer, during which the system’s control strategies were tested and initiated. All setpoints were configured manually, without the implementation of automated control sequences. During this phase, the temperature control loop was activated and tested to ensure thermal stable system operation under varying load conditions and different control parameters.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2019-03-12_Data_startup-phase_manual-mode_heating-up-curve.xlsx

Text:

The data corresponds to the startup phase of the 100 kW Proton Exchange Membrane (PEM) electrolyzer, during which the system’s control strategies were tested and initiated. All setpoints were configured manually, without the implementation of automated control sequences. Additionally, a heating-up temperature curve was recorded to monitor the thermal behavior of the system during initial operation.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2019-03-15_Data_startup-phase_manual-mode_heating-up-curve.xlsx

Text:

The data corresponds to the startup phase of the 100 kW Proton Exchange Membrane (PEM) electrolyzer, during which the system’s control strategies were tested and initiated. All setpoints were configured manually, without the implementation of automated control sequences. Additionally, a heating-up temperature curve was recorded to monitor the thermal behavior of the system during initial operation. Varying the load and pressures conditions.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2019-05-08_Data_startup-phase_manual-mode_temperature-control-loop.xlsx

Text:

The data corresponds to the startup phase of the 100 kW Proton Exchange Membrane (PEM) electrolyzer, during which the system’s control strategies were tested and initiated. All setpoints were configured manually, without the implementation of automated control sequences. During this phase, the temperature control loop was activated and tested to ensure thermal stable system operation under varying load conditions and different control parameters.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2019-05-27_Data_startup-phase_manual-mode_temperature-control-loop.xlsx

Text:

The data corresponds to the startup phase of the 100 kW Proton Exchange Membrane (PEM) electrolyzer, during which the system’s control strategies were tested and initiated. All setpoints were configured manually, without the implementation of automated control sequences. During this phase, the temperature control loop was activated and tested to ensure thermal stable system operation under varying load and pressure conditions for different control parameters.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2019-05-29_Data_startup-phase_manual-mode_temperature-control-loop.xlsx

Text:

The data corresponds to the startup phase of the 100 kW Proton Exchange Membrane (PEM) electrolyzer, during which the system’s control strategies were tested and initiated. All setpoints were configured manually, without the implementation of automated control sequences.During this phase, the temperature control loop was activated and tested to ensure thermal stable system operation under varying load and pressure conditions for different control parameters.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2019-06-07_Data_startup-phase_manual-mode_temperature-control-loop.xlsx

Text:

The data corresponds to the startup phase of the 100 kW Proton Exchange Membrane (PEM) electrolyzer, during which the system’s control strategies were tested and initiated. All setpoints were configured manually, without the implementation of automated control sequences. During this phase, the temperature control loop was activated and tested to ensure thermal stable system operation under varying load and pressure conditions for different control parameters

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2019-06-11_1st_Data_startup-phase_manual-mode_temperature-control-loop.xlsx

Text:

The data corresponds to the startup phase of the 100 kW Proton Exchange Membrane (PEM) electrolyzer, during which the system’s control strategies were tested and initiated. All setpoints were configured manually, without the implementation of automated control sequences.During this phase, the temperature control loop was activated and tested to ensure thermal stable system operation under varying load and pressure conditions for different control parameters.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2019-06-11_2nd_Data_startup-phase_manual-mode_temperature-control-loop.xlsx

Text:

The data corresponds to the startup phase of the 100 kW Proton Exchange Membrane (PEM) electrolyzer, during which the system’s control strategies were tested and initiated. All setpoints were configured manually, without the implementation of automated control sequences. During this phase, the temperature control loop was activated and tested to ensure thermal stable system operation under varying load and pressure conditions for different control parameters.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2019-06-12_Data_startup-phase_manual-mode_temperature-control-loop.xlsx

Text:

The data corresponds to the startup phase of the 100 kW Proton Exchange Membrane (PEM) electrolyzer, during which the system’s control strategies were tested and initiated. All setpoints were configured manually, without the implementation of automated control sequences. During this phase, the temperature control loop was activated and tested to ensure thermal stable system operation under varying load and pressure conditions for different control parameters.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2019-06-13_Data_startup-phase_manual-mode_temperature-control-loop.xlsx

Text:

The data corresponds to the startup phase of the 100 kW Proton Exchange Membrane (PEM) electrolyzer, during which the system’s control strategies were tested and initiated. All setpoints were configured manually, without the implementation of automated control sequences. During this phase, the temperature control loop was activated and tested to ensure thermal stable system operation under varying load and pressure conditions for different control parameters and set-points in temperature.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2019-06-19_Data_startup-phase_manual-mode_temperature-control-loop.xlsx

Text:

The data corresponds to the startup phase of the 100 kW Proton Exchange Membrane (PEM) electrolyzer, during which the system’s control strategies were tested and initiated. All setpoints were configured manually, without the implementation of automated control sequences. During this phase, the temperature control loop was activated and tested to ensure thermal stable system operation under varying load and pressure conditions for different control parameters.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2019-07-22_Data_startup-phase_manual-mode_temperature-control-loop.xlsx

Text:

The data corresponds to the startup phase of the 100 kW Proton Exchange Membrane (PEM) electrolyzer, during which the system’s control strategies were tested and initiated. All setpoints were configured manually, without the implementation of automated control sequences. During this phase, the temperature control loop was activated and tested to ensure thermal stable system operation under varying load and pressure conditions for different control parameters.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2019-07-23_Data_startup-phase_manual-mode_temperature-control-loop.xlsx

Text:

The data corresponds to the startup phase of the 100 kW Proton Exchange Membrane (PEM) electrolyzer, during which the system’s control strategies were tested and initiated. All setpoints were configured manually, without the implementation of automated control sequences. During this phase, the temperature control loop was activated and tested to ensure thermal stable system operation under varying load and pressure conditions for different control parameters.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2019-07-24_Data_startup-phase_manual-mode_temperature-control-loop.xlsx

Text:

The data corresponds to the startup phase of the 100 kW Proton Exchange Membrane (PEM) electrolyzer, during which the system’s control strategies were tested and initiated. All setpoints were configured manually, without the implementation of automated control sequences. During this phase, the temperature control loop was activated and tested to ensure thermal stable system operation under varying load and pressure conditions for different control parameters and set-points in temperature.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2019-07-25_1st_Data_startup-phase_manual-mode_temperature-control-loop.xlsx

Text:

The data corresponds to the startup phase of the 100 kW Proton Exchange Membrane (PEM) electrolyzer, during which the system’s control strategies were tested and initiated. All setpoints were configured manually, without the implementation of automated control sequences. During this phase, the temperature control loop was activated and tested to ensure thermal stable system operation under varying load and pressure conditions for different control parameters.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2019-07-25_2nd_Data_startup-phase_manual-mode_temperature-control-loop.xlsx

Text:

The data corresponds to the startup phase of the 100 kW Proton Exchange Membrane (PEM) electrolyzer, during which the system’s control strategies were tested and initiated. All setpoints were configured manually, without the implementation of automated control sequences. During this phase, the temperature control loop was activated and tested to ensure thermal stable system operation under varying load and pressure conditions for different control parameters.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2019-07-26_Data_startup-phase_manual-mode_temperature-control-loop.xlsx

Text:

The data corresponds to the startup phase of the 100 kW Proton Exchange Membrane (PEM) electrolyzer, during which the system’s control strategies were tested and initiated. All setpoints were configured manually, without the implementation of automated control sequences. During this phase, the temperature control loop was activated and tested to ensure thermal stable system operation under varying load and pressure conditions for different control parameters.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2019-07-29_Data_startup-phase_manual-mode_temperature-control-loop.xlsx

Text:

The data corresponds to the startup phase of the 100 kW Proton Exchange Membrane (PEM) electrolyzer, during which the system’s control strategies were tested and initiated. All setpoints were configured manually, without the implementation of automated control sequences. During this phase, the temperature control loop was activated and tested to ensure thermal stable system operation under varying load and pressure conditions for different control parameters and set-points in temperature.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2019-08-02_Data_startup-phase_manual-mode_temperature-control-loop.xlsx

Text:

The data corresponds to the startup phase of the 100 kW Proton Exchange Membrane (PEM) electrolyzer, during which the system’s control strategies were tested and initiated. All setpoints were configured manually, without the implementation of automated control sequences. During this phase, the temperature control loop was activated and tested to ensure thermal stable system operation under varying load and pressure conditions for different control parameters.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2019-08-05_1st_Data_startup-phase_manual-mode_temperature-control-loop.xlsx

Text:

The data corresponds to the startup phase of the 100 kW Proton Exchange Membrane (PEM) electrolyzer, during which the system’s control strategies were tested and initiated. All setpoints were configured manually, without the implementation of automated control sequences. During this phase, the temperature control loop was activated and tested to ensure thermal stable system operation under varying load and pressure conditions for different control parameters and set-points in temperature.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2019-08-05_2nd_Data_startup-phase_manual-mode_temperature-control-loop.xlsx

Text:

The data corresponds to the startup phase of the 100 kW Proton Exchange Membrane (PEM) electrolyzer, during which the system’s control strategies were tested and initiated. All setpoints were configured manually, without the implementation of automated control sequences. During this phase, the temperature control loop was activated and tested to ensure thermal stable system operation under varying load and pressure conditions for different control parameters.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2019-08-30_Data_startup-phase_manual-mode_temperature-control-loop.xlsx

Text:

The data corresponds to the startup phase of the 100 kW Proton Exchange Membrane (PEM) electrolyzer, during which the system’s control strategies were tested and initiated. All setpoints were configured manually, without the implementation of automated control sequences. During this phase, the temperature control loop was activated and tested to ensure thermal stable system operation under varying load and pressure conditions for different control parameters.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2019-09-03_Data_startup-phase_manual-mode_temperature-control-loop.xlsx

Text:

The data corresponds to the startup phase of the 100 kW Proton Exchange Membrane (PEM) electrolyzer, during which the system’s control strategies were tested and initiated. All setpoints were configured manually, without the implementation of automated control sequences. During this phase, the temperature control loop was activated and tested to ensure thermal stable system operation under varying load and pressure conditions for different control parameters.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2019-09-18_1st_Data-measured_Current-pressure-temperature-ramp.xlsx

Text:

The system is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the corresponding measured data recorded during operation of the set-point profile, which defines a temperature ramp.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2019-09-18_1st_Setpoint-profile_Current-pressure-temperature-ramp.xls

Text:

The 100 kW Proton Exchange Membrane (PEM) electrolyzer is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the set-point profile, which defines a temperature ramp executed through a predefined control sequence.

application/vnd.ms-excel

Label:

2019-09-18_2nd_Data-measured_Current-pressure-temperature-ramp.xlsx

Text:

The system is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the corresponding measured data recorded during operation of the set-point profile, which defines a current, pressure and temperature ramp.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2019-09-18_2nd_Setpoint-profil_current-pressure-temperature-ramp.xls

Text:

This file contains the set-point profile, which defines a current, pressure and temperature ramp executed through a predefined control sequence.

application/vnd.ms-excel

Label:

2019-09-27_Data_manual-mode_temperature-control-loop.xlsx

Text:

The data corresponds to the 100 kW Proton Exchange Membrane (PEM) electrolyzer, during which the system’s control strategies were tested and initiated. All set-points were configured manually, without the implementation of automated control sequences. The temperature control loop was activated and tested to ensure thermal stable system operation under varying load conditions and different control parameters.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2019-10-09_Data_manual-mode_heating-up.xlsx

Text:

The data corresponds to the 100 kW Proton Exchange Membrane (PEM) electrolyzer. A heating-up curve was recorded to monitor the thermal behavior of the system during initial operation. During this procedure, the load conditions were systematically varied in order to determine the optimal transition time from standstill to nominal operation.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2019-10-29_Data_manual-mode_heating-up.xlsx

Text:

The data corresponds to the 100 kW Proton Exchange Membrane (PEM) electrolyzer. A heating-up curve was recorded to monitor the thermal behavior of the system during initial operation. During this procedure, the load conditions were systematically varied in order to determine the optimal transition time from standstill to nominal operation.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2020-03-18_1st_Data_manual-mode_heating-up.xlsx

Text:

The data corresponds to the 100 kW Proton Exchange Membrane (PEM) electrolyzer. A heating-up curve was recorded to monitor the thermal behavior of the system during initial operation. During this procedure, the load conditions were systematically varied in order to determine the optimal transition time from standstill to nominal operation.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2020-03-18_2nd_Data_manual-mode_heating-up.xlsx

Text:

The data corresponds to the 100 kW Proton Exchange Membrane (PEM) electrolyzer. A heating-up curve was recorded to monitor the thermal behavior of the system during initial operation. During this procedure, the load conditions were systematically varied in order to determine the optimal transition time from standstill to nominal operation.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2020-03-20_Data_manual-mode_heating-up.xlsx

Text:

The data corresponds to the 100 kW Proton Exchange Membrane (PEM) electrolyzer. A heating-up curve was recorded to monitor the thermal behavior of the system during initial operation. During this procedure, the load conditions were systematically varied in order to determine the optimal transition time from standstill to nominal operation.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2020-04-06_Data_manual-mode_temperature-control-loop.xlsx

Text:

The data corresponds to the 100 kW Proton Exchange Membrane (PEM) electrolyzer, during which the system’s control strategies were tested and initiated. All set-points were configured manually, without the implementation of automated control sequences. During this phase, the temperature control loop was activated and tested to ensure thermal stable system operation under varying load and pressure conditions for different control parameters and set-points in temperature.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2020-04-07_Data_manual-mode_heating-up.xlsx

Text:

The data corresponds to the 100 kW Proton Exchange Membrane (PEM) electrolyzer. A heating-up curve was recorded to monitor the thermal behavior of the system during initial operation. During this procedure, the load conditions were systematically varied in order to determine the optimal transition time from standstill to nominal operation.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2020-04-08_Data_manual-mode_heating-up_temperature_control.xlsx

Text:

The data corresponds to the 100 kW Proton Exchange Membrane (PEM) electrolyzer. A heating-up curve was recorded to monitor the thermal behavior of the system during initial operation. During this procedure, the load conditions were systematically varied in order to determine the optimal transition time from standstill to nominal operation. Moreover, the temperature control loop was tested to ensure thermal stable system operation under varying load and pressure conditions for different control parameters and set-points in temperature.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2020-04-09_Data_manual-mode_heating-up_temperature_control.xlsx

Text:

The data corresponds to the 100 kW Proton Exchange Membrane (PEM) electrolyzer. A heating-up curve was recorded to monitor the thermal behavior of the system during initial operation. During this procedure, the load conditions were systematically varied in order to determine the optimal transition time from standstill to nominal operation. Moreover, the temperature control loop was tested to ensure thermal stable system operation under varying load and pressure conditions for different control parameters and set-points in temperature.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2020-04-20_Data_manual-mode_heating-up_temperature_control.xlsx

Text:

The data corresponds to the 100 kW Proton Exchange Membrane (PEM) electrolyzer. A heating-up curve was recorded to monitor the thermal behavior of the system during initial operation. During this procedure, the load conditions were systematically varied in order to determine the optimal transition time from standstill to nominal operation. Moreover, the temperature control loop was tested to ensure thermal stable system operation under varying load and pressure conditions for different control parameters and set-points in temperature.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2020-04-22_Data_manual-mode_heating-up_temperature_control.xlsx

Text:

The data corresponds to the 100 kW Proton Exchange Membrane (PEM) electrolyzer. A heating-up curve was recorded to monitor the thermal behavior of the system during initial operation. During this procedure, the load conditions were systematically varied in order to determine the optimal transition time from standstill to nominal operation. Moreover, the temperature control loop was tested to ensure thermal stable system operation under varying load and pressure conditions for different control parameters and set-points in temperature.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2020-05-06_Data_manual-mode_heating-up_temperature_control.xlsx

Text:

The data corresponds to the 100 kW Proton Exchange Membrane (PEM) electrolyzer. A heating-up curve was recorded to monitor the thermal behavior of the system during initial operation. During this procedure, the load conditions were systematically varied in order to determine the optimal transition time from standstill to nominal operation. Moreover, the temperature control loop was tested to ensure thermal stable system operation under varying load and pressure conditions for different control parameters and set-points in temperature.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2020-05-11_Data_manual-mode_heating-up.xlsx

Text:

The data corresponds to the 100 kW Proton Exchange Membrane (PEM) electrolyzer. A heating-up curve was recorded to monitor the thermal behavior of the system during initial operation. During this procedure, the load conditions were static in order to determine the optimal transition time from standstill to nominal operation.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2020-05-13_Data_manual-mode_heating-up_temperature_control.xlsx

Text:

The data corresponds to the 100 kW Proton Exchange Membrane (PEM) electrolyzer. A heating-up curve was recorded to monitor the thermal behavior of the system during initial operation. During this procedure, the load conditions were systematically varied in order to determine the optimal transition time from standstill to nominal operation. Moreover, the temperature control loop was tested to ensure thermal stable system operation under varying load and pressure conditions for different control parameters and set-points in temperature.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2020-05-15_Data_manual-mode_heating-up_temperature_control.xlsx

Text:

The data corresponds to the 100 kW Proton Exchange Membrane (PEM) electrolyzer. A heating-up curve was recorded to monitor the thermal behavior of the system during initial operation. During this procedure, the load conditions were systematically varied in order to determine the optimal transition time from standstill to nominal operation. Moreover, the temperature control loop was tested to ensure thermal stable system operation under varying load and pressure conditions for different control parameters and set-points in temperature.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2020-05-20_Data_manual-mode_heating-up_temperature_control.xlsx

Text:

The data corresponds to the 100 kW Proton Exchange Membrane (PEM) electrolyzer. A heating-up curve was recorded to monitor the thermal behavior of the system during initial operation. During this procedure, the load conditions were systematically varied in order to determine the optimal transition time from standstill to nominal operation. Moreover, the temperature control loop was tested to ensure thermal stable system operation under varying load and pressure conditions for different control parameters and set-points in temperature.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2020-05-25_Data_manual-mode_heating-up_temperature_control.xlsx

Text:

The data corresponds to the 100 kW Proton Exchange Membrane (PEM) electrolyzer. A heating-up curve was recorded to monitor the thermal behavior of the system during initial operation. During this procedure, the load conditions were systematically varied in order to determine the optimal transition time from standstill to nominal operation. Moreover, the temperature control loop was tested to ensure thermal stable system operation under varying load and pressure conditions for different control parameters and set-points in temperature.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2020-05-28_Data_manual-mode_heating-up_temperature_control.xlsx

Text:

The data corresponds to the 100 kW Proton Exchange Membrane (PEM) electrolyzer. A heating-up curve was recorded to monitor the thermal behavior of the system during initial operation. During this procedure, the load conditions were systematically varied in order to determine the optimal transition time from standstill to nominal operation. Moreover, the temperature control loop was tested to ensure thermal stable system operation under varying load and pressure conditions for different control parameters and set-points in temperature.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2020-06-02_Data_manual-mode_heating-up_temperature_control.xlsx

Text:

The data corresponds to the 100 kW Proton Exchange Membrane (PEM) electrolyzer. A heating-up curve was recorded to monitor the thermal behavior of the system during initial operation. During this procedure, the load conditions were systematically varied in order to determine the optimal transition time from standstill to nominal operation. Moreover, the temperature control loop was tested to ensure thermal stable system operation under varying load and pressure conditions for different control parameters and set-points in temperature.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2020-06-03_Data_manual-mode_heating-up_temperature_control.xlsx

Text:

The data corresponds to the 100 kW Proton Exchange Membrane (PEM) electrolyzer. A heating-up curve was recorded to monitor the thermal behavior of the system during initial operation. During this procedure, the load conditions were systematically varied in order to determine the optimal transition time from standstill to nominal operation. Moreover, the temperature control loop was tested to ensure thermal stable system operation under varying load and pressure conditions for different control parameters and set-points in temperature.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2020-06-05_Data_manual-mode_heating-up_temperature_control.xlsx

Text:

The data corresponds to the 100 kW Proton Exchange Membrane (PEM) electrolyzer. A heating-up curve was recorded to monitor the thermal behavior of the system during initial operation. During this procedure, the load conditions were systematically varied in order to determine the optimal transition time from standstill to nominal operation. Moreover, the temperature control loop was tested to ensure thermal stable system operation under varying load and pressure conditions for different control parameters and set-points in temperature.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2020-06-05_Data_manual-mode_temperature-control-loop.xlsx

Text:

The data corresponds to the 100 kW Proton Exchange Membrane (PEM) electrolyzer, during which the system’s control strategies were tested and initiated. All set-points were configured manually, without the implementation of automated control sequences. During this phase, the temperature control loop was activated and tested to ensure thermal stable system operation under varying load and pressure conditions for different control parameters and set-points in temperature.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2020-06-08_Data_manual-mode_heating-up.xlsx

Text:

The data corresponds to the 100 kW Proton Exchange Membrane (PEM) electrolyzer. A heating-up curve was recorded to monitor the thermal behavior of the system during initial operation. During this procedure, no load is applied in order to determine the optimal transition time from standstill to nominal operation.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2020-06-09_Data_manual-mode_heating-up.xlsx

Text:

The data corresponds to the 100 kW Proton Exchange Membrane (PEM) electrolyzer. A heating-up curve was recorded to monitor the thermal behavior of the system during initial operation. During this procedure, no load is applied in order to determine the optimal transition time from standstill to nominal operation.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2020-06-10_Data_manual-mode_heating-up.xlsx

Text:

The data corresponds to the 100 kW Proton Exchange Membrane (PEM) electrolyzer. A heating-up curve was recorded to monitor the thermal behavior of the system during initial operation. During this procedure, no load is applied in order to determine the optimal transition time from standstill to nominal operation.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2020-06-19_Data_manual-mode_heating-up_temperature_control.xlsx

Text:

The data corresponds to the 100 kW Proton Exchange Membrane (PEM) electrolyzer. A heating-up curve was recorded to monitor the thermal behavior of the system during initial operation. During this procedure, the load conditions were systematically varied in order to determine the optimal transition time from standstill to nominal operation. Moreover, the temperature control loop was tested to ensure thermal stable system operation under varying load and pressure conditions for different control parameters and set-points in temperature.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2020-06-24_Data_manual-mode_heating-up_temperature_control.xlsx

Text:

The data corresponds to the 100 kW Proton Exchange Membrane (PEM) electrolyzer. A heating-up curve was recorded to monitor the thermal behavior of the system during initial operation. During this procedure, the load conditions were systematically varied in order to determine the optimal transition time from standstill to nominal operation. Moreover, the temperature control loop was tested to ensure thermal stable system operation under varying load and pressure conditions for different control parameters and set-points in temperature.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2020-07-03_Data_manual-mode_heating-up.xlsx

Text:

The data corresponds to the 100 kW Proton Exchange Membrane (PEM) electrolyzer. A heating-up curve was recorded to monitor the thermal behavior of the system during initial operation. During this procedure, no load was applied in order to determine the optimal transition time from standstill to nominal operation.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2020-07-07_1st_Data-measured_Wind-Profile.xlsx

Text:

The system is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the corresponding measured data recorded during operation of the set-point profile, which defines a wind profile.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2020-07-07_1st_Setpoint-profile_Wind-Profile.xls

Text:

The 100 kW Proton Exchange Membrane (PEM) electrolyzer is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the set-point profile, which defines a windprofile executed through a predefined control sequence.

application/vnd.ms-excel

Label:

2020-07-07_2nd_Data-measured_Wind-Profile.xlsx

Text:

The system is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the corresponding measured data recorded during operation of the set-point profile, which defines a wind profile.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2020-07-07_2nd_Setpoint-profile_Wind-Profile.xls

Text:

The 100 kW Proton Exchange Membrane (PEM) electrolyzer is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the set-point profile, which defines a wind profile executed through a predefined control sequence.

application/vnd.ms-excel

Label:

2020-07-09_Data_manual-mode_heating-up.xlsx

Text:

The data corresponds to the 100 kW Proton Exchange Membrane (PEM) electrolyzer. A heating-up curve was recorded to monitor the thermal behavior of the system during initial operation. During this procedure, the load conditions were systematically varied in order to determine the optimal transition time from standstill to nominal operation.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2020-07-13_Data_manual-mode_heating-up.xlsx

Text:

The data corresponds to the 100 kW Proton Exchange Membrane (PEM) electrolyzer. A heating-up curve was recorded to monitor the thermal behavior of the system during initial operation. During this procedure, the load conditions were systematically varied in order to determine the optimal transition time from standstill to nominal operation.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2020-07-14_Data_manual-mode_heating-up.xlsx

Text:

The data corresponds to the 100 kW Proton Exchange Membrane (PEM) electrolyzer. A heating-up curve was recorded to monitor the thermal behavior of the system during initial operation. During this procedure, the load conditions were systematically varied in order to determine the optimal transition time from standstill to nominal operation.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2020-07-23_Data_manual-mode_heating-up_temperature_control.xlsx

Text:

The data corresponds to the 100 kW Proton Exchange Membrane (PEM) electrolyzer. A heating-up curve was recorded to monitor the thermal behavior of the system during initial operation. During this procedure, the load conditions were systematically varied in order to determine the optimal transition time from standstill to nominal operation. Moreover, the temperature control loop was tested to ensure thermal stable system operation under varying load and pressure conditions for different control parameters and set-points in temperature.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2020-07-27_Data_manual-mode_heating-up_temperature_control.xlsx

Text:

The data corresponds to the 100 kW Proton Exchange Membrane (PEM) electrolyzer. A heating-up curve was recorded to monitor the thermal behavior of the system during initial operation. During this procedure, the load conditions were systematically varied in order to determine the optimal transition time from standstill to nominal operation. Moreover, the temperature control loop was tested to ensure thermal stable system operation under varying load and pressure conditions for different control parameters and set-points in temperature.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2020-08-18_Data_manual-mode_heating-up_temperature_control.xlsx

Text:

The data corresponds to the 100 kW Proton Exchange Membrane (PEM) electrolyzer. A heating-up curve was recorded to monitor the thermal behavior of the system during initial operation. During this procedure, the load conditions were systematically varied in order to determine the optimal transition time from standstill to nominal operation. Moreover, the temperature control loop was tested to ensure thermal stable system operation under varying load and pressure conditions for different control parameters and set-points in temperature.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2020-08-19_Data_manual-mode_heating-up.xlsx

Text:

The data corresponds to the 100 kW Proton Exchange Membrane (PEM) electrolyzer. A heating-up curve was recorded to monitor the thermal behavior of the system during initial operation. During this procedure, the load conditions were systematically varied in order to determine the optimal transition time from standstill to nominal operation.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2020-08-20_Data_manual-mode_heating-up_temperature_control.xlsx

Text:

The data corresponds to the 100 kW Proton Exchange Membrane (PEM) electrolyzer. A heating-up curve was recorded to monitor the thermal behavior of the system during initial operation. During this procedure, the load conditions were systematically varied in order to determine the optimal transition time from standstill to nominal operation. Moreover, the temperature control loop was tested to ensure thermal stable system operation under varying load and pressure conditions for different control parameters and set-points in temperature.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2020-08-24_Data_manual-mode_heating-up_temperature_control.xlsx

Text:

The data corresponds to the 100 kW Proton Exchange Membrane (PEM) electrolyzer. A heating-up curve was recorded to monitor the thermal behavior of the system during initial operation. During this procedure, the load conditions were systematically varied in order to determine the optimal transition time from standstill to nominal operation. Moreover, the temperature control loop was tested to ensure thermal stable system operation under varying load and pressure conditions for different control parameters and set-points in temperature.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2020-08-25_Data-measured_heating-up_temperature-ramp.xlsx

Text:

The system is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the corresponding measured data recorded during operation of the set-point profile, which defines a temperature ramp.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2020-08-25_Setpoint-profile_heating-up_temperature-ramp.xls

Text:

The 100 kW Proton Exchange Membrane (PEM) electrolyzer is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the set-point profile, which defines a temperature ramp executed through a predefined control sequence.

application/vnd.ms-excel

Label:

2020-08-26_Data-measured_Kombi-Step-Response.xlsx

Text:

The system is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the corresponding measured data recorded during operation of the set-point profile, which defines a trajectory of a Kombi-Step-Response in current density .

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2020-08-26_Setpoint-profile_Kombi-Step-Response.xls

Text:

The 100 kW Proton Exchange Membrane (PEM) electrolyzer is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the set-point profile, which defines a trajectory of a Kombi-Step-Response in current density executed through a predefined control sequence.

application/vnd.ms-excel

Label:

2020-08-27_Data-measured_Kombi-Current-Step-Response-20min.xlsx

Text:

The system is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the corresponding measured data recorded during operation of the set-point profile, which defines a trajectory of a Kombi Current-Step Response 20min executed through a predefined control sequence.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2020-08-27_Setpoint-profile_Kombi-Current-Step Response_20min.xls

Text:

The 100 kW Proton Exchange Membrane (PEM) electrolyzer is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the set-point profile, which defines a trajectory of a Kombi Current-Step Response 20min executed through a predefined control sequence.

application/vnd.ms-excel

Label:

2020-08-28_Data-measured_Kombi-Voltage-Step-Response_20min.xlsx

Text:

The system is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the corresponding measured data recorded during operation of the set-point profile, which defines a trajectory of Kombi Voltage Step Response 20min.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2020-08-28_Setpoint-profile_Kombi-Voltage-Step-Response_20min.xls

Text:

The 100 kW Proton Exchange Membrane (PEM) electrolyzer is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the set-point profile, which defines a trajectory of a Kombi Voltage Step Response 20min executed through a predefined control sequence.

application/vnd.ms-excel

Label:

2020-08-31_Data-measured_Kombi-Current-Wind Power_20min.xlsx

Text:

The system is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the corresponding measured data recorded during operation of the set-point profile, which defines a trajectory of a wind turbine 20min.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2020-08-31_Setpoint-profile_Kombi-Current-Wind Power_20min.xls

Text:

The 100 kW Proton Exchange Membrane (PEM) electrolyzer is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the set-point profile, which defines a trajectory of a wind turbine 20min executed through a predefined control sequence.

application/vnd.ms-excel

Label:

2020-10-14_1st_Data-measured_Heat-up_1.8V_75C_15lpm_Low_Current_Densities.xlsx

Text:

The system is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the corresponding measured data recorded during operation of the set-point profile, which defines a trajectory of heating up the system with constant cell voltage of 1.8 V.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2020-10-14_1st_Setpoint-Profile_Heat-up_1.8V_75C_15lpm_Low_Current_Densities.xls

Text:

The 100 kW Proton Exchange Membrane (PEM) electrolyzer is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the set-point profile, which defines a trajectory heating up the system with constant cell voltage of 1.8 V.

application/vnd.ms-excel

Label:

2020-10-14_2nd_Data_measured_Heat-up_1.8V_75C_15lpm_Low_Current_Densities_abort.xlsx

Text:

The system is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the corresponding measured data recorded during operation of the set-point profile, which defines a trajectory of heating up the system with constant cell voltage of 1.8 V.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2020-10-14_2nd_Setpoint-Profile_Heat-up_1.8V_75C_15lpm_Low_Current_Densities_abort.xls

Text:

The 100 kW Proton Exchange Membrane (PEM) electrolyzer is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the set-point profile, which defines a trajectory heating up the system with constant cell voltage of 1.8 V.

application/vnd.ms-excel

Label:

2020-10-15_1st_Data_measured_Kombi-Current-Step Response_10min_abort.xlsx

Text:

The system is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the corresponding measured data recorded during operation of the set-point profile, which defines a trajectory of Kombi Current Step Response 10min.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2020-10-15_1st_Setpoint-Profile_Kombi-Current-Step Response_10min_abort.xls

Text:

The 100 kW Proton Exchange Membrane (PEM) electrolyzer is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the set-point profile, which defines a trajectory of a Kombi Current Step Response 10min executed through a predefined control sequence.

application/vnd.ms-excel

Label:

2020-10-15_2nd_Data_measured_Kombi-Current-Step Response_10min.xlsx

Text:

The system is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the corresponding measured data recorded during operation of the set-point profile, which defines a trajectory of Kombi Current Step Response 10min.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2020-10-15_2nd_Setpoint-Profile_Kombi-Current-Step Response_10min.xls

Text:

The 100 kW Proton Exchange Membrane (PEM) electrolyzer is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the set-point profile, which defines a trajectory of a Kombi Current Step Response 10min executed through a predefined control sequence.

application/vnd.ms-excel

Label:

2020-10-16_Data_measured_Kombi-Current-Step Response_10min.xlsx

Text:

The system is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the corresponding measured data recorded during operation of the set-point profile, which defines a trajectory of Kombi Current Step Response 10min.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2020-10-16_Setpoint-Profile_Kombi-Current-Step Response_10min.xls

Text:

The 100 kW Proton Exchange Membrane (PEM) electrolyzer is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the set-point profile, which defines a trajectory of a Kombi Current Step Response 10min executed through a predefined control sequence.

application/vnd.ms-excel

Label:

2020-10-20_Thermoneutral_Operation.xlsx

Text:

The data corresponds to the 100 kW Proton Exchange Membrane (PEM) electrolyzer. During this procedure, the load conditions were constant in order to determine the thermoneutral operation point

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2020-10-21_Thermoneutral_Operation.xlsx

Text:

The data corresponds to the 100 kW Proton Exchange Membrane (PEM) electrolyzer. During this procedure, the load conditions were constant in order to determine the thermoneutral operation point

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2020-11-03_Data_measured_Kombi-PV-Profile_PHOEBUS-1.xlsx

Text:

The system is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the corresponding measured data recorded during operation of the set-point profile, which defines a trajectory of a Kombi-PV-Profile from the Project PHOEBUS.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2020-11-03_Setpoint-Profile_Kombi-PV-Profile_PHOEBUS-1.xls

Text:

The 100 kW Proton Exchange Membrane (PEM) electrolyzer is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the set-point profile, which defines a trajectory of a Kombi-PV-Profile from the Project PHOEBUS executed through a predefined control sequence.

application/vnd.ms-excel

Label:

2020-11-04_Data_measured_Kombi-Current-Step Response_60C_10min.xlsx

Text:

The system is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the corresponding measured data recorded during operation of the set-point profile, which defines a trajectory of Kombi Current Step Response for 10min at 60 °C.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2020-11-04_Setpoint-Profile_Kombi-Current-Step Response_60C_10min.xls

Text:

The 100 kW Proton Exchange Membrane (PEM) electrolyzer is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the set-point profile, which defines a trajectory of a Kombi Current Step Response for 10min at 60 °C executed through a predefined control sequence.

application/vnd.ms-excel

Label:

2020-11-05_Data_measured_Kombi-PV-Profile_PHOEBUS-2.xlsx

Text:

The system is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the corresponding measured data recorded during operation of the set-point profile, which defines a trajectory of a Kombi-PV-Profile from the Project PHOEBUS.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2020-11-05_Setpoint-Profile_Kombi-PV-Profile_PHOEBUS-2.xls

Text:

The 100 kW Proton Exchange Membrane (PEM) electrolyzer is operating under normal conditions, with all set-points defined by a PV-Profile originating from the PHOEBUS project and executed through a control sequence. This file contains the PV-Profile, which specifies the dynamic trajectory of operating points applied to the electrolyzer via the predefined control sequence.

application/vnd.ms-excel

Label:

2020-11-06_Data_measured_Kombi-Current-Step Response_60min_1.xlsx

Text:

The system is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the corresponding measured data recorded during operation of the set-point profile, which defines a trajectory of Kombi Current Step Response for 1 h at 60 °C.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2020-11-06_Setpoint-Profile_Kombi-Current-Step Response_60min_1.xls

Text:

The 100 kW Proton Exchange Membrane (PEM) electrolyzer is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the set-point profile, which defines a trajectory of a Kombi Current Step Response for 1 h at 60 °C executed through a predefined control sequence.

application/vnd.ms-excel

Label:

2020-11-09_Data_measured_Kombi-Current-Step Response_60min_2.xlsx

Text:

The system is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the corresponding measured data recorded during operation of the set-point profile, which defines a trajectory of Kombi Current Step Response for 1 h at 75 °C.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2020-11-09_Setpoint-Profile_Kombi-Current-Step Response_60min_2.xls

Text:

The 100 kW Proton Exchange Membrane (PEM) electrolyzer is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the set-point profile, which defines a trajectory of a Kombi Current Step Response for 1 h at 75 °C executed through a predefined control sequence.

application/vnd.ms-excel

Label:

2020-11-10_Data_measured_Kombi-Current-Step Response_60min_3.xlsx

Text:

The system is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the corresponding measured data recorded during operation of the set-point profile, which defines a trajectory of Kombi Current Step Response for 1 h at 75 °C.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2020-11-10_Setpoint-Profile_Kombi-Current-Step Response_60min_3.xls

Text:

The 100 kW Proton Exchange Membrane (PEM) electrolyzer is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the set-point profile, which defines a trajectory of a Kombi Current Step Response for 1 h at 75 °C executed through a predefined control sequence.

application/vnd.ms-excel

Label:

2020-11-11_Data_measured_Kombi-Current-Step Response_60min_4.xlsx

Text:

The system is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the corresponding measured data recorded during operation of the set-point profile, which defines a trajectory of Kombi Current Step Response for 1 h at 75 °C

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2020-11-11_Setpoint-Profile_Kombi-Current-Step Response_60min_4.xls

Text:

The 100 kW Proton Exchange Membrane (PEM) electrolyzer is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the set-point profile, which defines a trajectory of a Kombi Current Step Response for 1 h at 75 °C executed through a predefined control sequence.

application/vnd.ms-excel

Label:

2020-11-12_Data_measured_Kombi-Current-Step Response_60min_5.xlsx

Text:

The system is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the corresponding measured data recorded during operation of the set-point profile, which defines a trajectory of Kombi Current Step Response for 1 h at 75 °C.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2020-11-12_Setpoint-Profile_Kombi-Current-Step Response_60min_5.xls

Text:

The 100 kW Proton Exchange Membrane (PEM) electrolyzer is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the set-point profile, which defines a trajectory of a Kombi Current Step Response for 1 h at 75 °C executed through a predefined control sequence.

application/vnd.ms-excel

Label:

2020-11-13_Data_measured_Kombi-Current.Pump-Step Response_10min_2_1bar.xlsx

Text:

The system is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the corresponding measured data recorded during operation of the set-point profile, which defines a trajectory of Kombi Current Step Response for 10min at 75 °C.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2020-11-13_Setpoint-Profile_Kombi-Current+Pump-Step Response_10min_2_1bar.xls

Text:

The 100 kW Proton Exchange Membrane (PEM) electrolyzer is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the set-point profile, which defines a trajectory of a Kombi Current Step Response for 10min at 75 °C executed through a predefined control sequence.

application/vnd.ms-excel

Label:

2020-11-16_Data_measured_Kombi-Current-Step Response_65.C_60min_1.xlsx

Text:

The system is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the corresponding measured data recorded during operation of the set-point profile, which defines a trajectory of Kombi Current Step Response for 1 h at 65 °C.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2020-11-16_Setpoint-Profile_Kombi-Current-Step Response_65°C_60min_1.xls

Text:

The 100 kW Proton Exchange Membrane (PEM) electrolyzer is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the set-point profile, which defines a trajectory of a Kombi Current Step Response for 1 h at 65 °C executed through a predefined control sequence.

application/vnd.ms-excel

Label:

2020-11-18_Data_measured_Kombi-Current-Step Response_65.C_60min_2.xlsx

Text:

The system is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the corresponding measured data recorded during operation of the set-point profile, which defines a trajectory of Kombi Current Step Response for 1 h at 65 °C.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2020-11-18_Setpoint-Profile_Kombi-Current-Step Response_65°C_60min_2.xls

Text:

The 100 kW Proton Exchange Membrane (PEM) electrolyzer is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the set-point profile, which defines a trajectory of a Kombi Current Step Response for 1 h at 65 °C executed through a predefined control sequence.

application/vnd.ms-excel

Label:

2020-11-19_Data_measured_Kombi-Current-Step Response_65.C_60min_3.xlsx

Text:

The system is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the corresponding measured data recorded during operation of the set-point profile, which defines a trajectory of Kombi Current Step Response for 1 h at 65 °C.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2020-11-19_Setpoint-Profile_Kombi-Current-Step Response_65°C_60min_3.xls

Text:

The 100 kW Proton Exchange Membrane (PEM) electrolyzer is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the set-point profile, which defines a trajectory of a Kombi Current Step Response for 1 h at 65 °C executed through a predefined control sequence.

application/vnd.ms-excel

Label:

2020-11-23_Data_measured_Kombi-Current-Step Response_65.C_60min_4.xlsx

Text:

The system is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the corresponding measured data recorded during operation of the set-point profile, which defines a trajectory of Kombi Current Step Response for 1 h at 65 °C.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2020-11-23_Setpoint-Profile_Kombi-Current-Step Response_65°C_60min_4.xls

Text:

The 100 kW Proton Exchange Membrane (PEM) electrolyzer is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the set-point profile, which defines a trajectory of a Kombi Current Step Response for 1 h at 65 °C executed through a predefined control sequence.

application/vnd.ms-excel

Label:

2020-12-08_Thermoneutral Operation_5-4bar_0.8 Acm-2.xlsx

Text:

The data corresponds to the 100 kW Proton Exchange Membrane (PEM) electrolyzer. During this procedure, the load conditions were constant in order to determine the thermoneutral operation point

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2020-12-09_Data_measured_Kombi-Current-Step Response_55.C_60min_1.xlsx

Text:

The system is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the corresponding measured data recorded during operation of the set-point profile, which defines a trajectory of Kombi Current Step Response for 1 h at 55 °C.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2020-12-09_Setpoint-Profile_Kombi-Current-Step Response_55°C_60min_1.xls

Text:

The 100 kW Proton Exchange Membrane (PEM) electrolyzer is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the set-point profile, which defines a trajectory of a Kombi Current Step Response for 1 h at 55 °C executed through a predefined control sequence.

application/vnd.ms-excel

Label:

2020-12-10_Data_measured_Kombi-Current-Step Response_45.C_60min_1.xlsx

Text:

The system is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the corresponding measured data recorded during operation of the set-point profile, which defines a trajectory of Kombi Current Step Response for 1 h at 45 °C.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2020-12-10_Setpoint-Profile_Kombi-Current-Step Response_45°C_60min_1.xls

Text:

The 100 kW Proton Exchange Membrane (PEM) electrolyzer is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the set-point profile, which defines a trajectory of a Kombi Current Step Response for 1 h at 45 °C executed through a predefined control sequence.

application/vnd.ms-excel

Label:

2020-12-11_Data_measured_Kombi-Current-Step Response_45.C_60min_1-2.xlsx

Text:

The system is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the corresponding measured data recorded during operation of the set-point profile, which defines a trajectory of Kombi Current Step Response for 1 h at 45 °C.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2020-12-11_Setpoint-Profile_Kombi-Current-Step Response_45°C_60min_1-2.xls

Text:

The 100 kW Proton Exchange Membrane (PEM) electrolyzer is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the set-point profile, which defines a trajectory of a Kombi Current Step Response for 1 h at 45 °C executed through a predefined control sequence.

application/vnd.ms-excel

Label:

2020-12-14_Data_measured_Kombi-Current-Step Response_35.C_60min_1.xlsx

Text:

The system is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the corresponding measured data recorded during operation of the set-point profile, which defines a trajectory of Kombi Current Step Response for 1 h at 35 °C.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2020-12-14_Setpoint-Profile_Kombi-Current-Step Response_35°C_60min_1.xls

Text:

The 100 kW Proton Exchange Membrane (PEM) electrolyzer is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the set-point profile, which defines a trajectory of a Kombi Current Step Response for 1 h at 35 °C executed through a predefined control sequence.

application/vnd.ms-excel

Label:

2020-12-15_Data_measured_Kombi-Current-Step Response_HighlyDynamic.xlsx

Text:

The system is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the corresponding measured data recorded during operation of the set-point profile, which defines a trajectory of a high dynamic Current Step Response at 75 °C.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2020-12-15_Setpoint-Profile_Kombi-Current-Step Response_HighlyDynamic.xls

Text:

The 100 kW Proton Exchange Membrane (PEM) electrolyzer is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the set-point profile, which defines a trajectory of a high dynamic Current Step Response at 75 °C executed through a predefined control sequence.

application/vnd.ms-excel

Label:

2021-01-11_Data_measured_Kombi-Current-Step Response_55.C_60min_2.xlsx

Text:

The system is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the corresponding measured data recorded during operation of the set-point profile, which defines a trajectory of Kombi Current Step Response for 1 h at 55 °C.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2021-01-11_Setpoint-Profile_Kombi-Current-Step Response_55°C_60min_2.xls

Text:

The 100 kW Proton Exchange Membrane (PEM) electrolyzer is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the set-point profile, which defines a trajectory of a Kombi Current Step Response for 1 h at 55 °C executed through a predefined control sequence.

application/vnd.ms-excel

Label:

2021-01-12_Data_measured_Kombi-Current-Step Response_45.C_60min_3.xlsx

Text:

The system is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the corresponding measured data recorded during operation of the set-point profile, which defines a trajectory of Kombi Current Step Response for 1 h at 45 °C.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2021-01-12_Setpoint-Profile_Kombi-Current-Step Response_45°C_60min_3.xls

Text:

The 100 kW Proton Exchange Membrane (PEM) electrolyzer is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the set-point profile, which defines a trajectory of a Kombi Current Step Response for 1 h at 45 °C executed through a predefined control sequence.

application/vnd.ms-excel

Label:

2021-01-13_Data_measured_Kombi-Current-Step Response_45.C_60min_4.xlsx

Text:

The system is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the corresponding measured data recorded during operation of the set-point profile, which defines a trajectory of Kombi Current Step Response for 1 h at 45 °C.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2021-01-13_Setpoint-Profile_Kombi-Current-Step Response_45°C_60min_4.xls

Text:

The 100 kW Proton Exchange Membrane (PEM) electrolyzer is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the set-point profile, which defines a trajectory of a Kombi Current Step Response for 1 h at 45 °C executed through a predefined control sequence.

application/vnd.ms-excel

Label:

2021-01-14_Data_measured_Kombi-Current-Step Response_55.C_60min_3.xlsx

Text:

The system is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the corresponding measured data recorded during operation of the set-point profile, which defines a trajectory of Kombi Current Step Response for 1 h at 55 °C.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2021-01-14_Setpoint-Profile_Kombi-Current-Step Response_55°C_60min_3.xls

Text:

The 100 kW Proton Exchange Membrane (PEM) electrolyzer is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the set-point profile, which defines a trajectory of a Kombi Current Step Response for 1 h at 55 °C executed through a predefined control sequence.

application/vnd.ms-excel

Label:

2021-01-15_Data_measured_Kombi-Current-Step Response_35.C_60min_2.xlsx

Text:

The system is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the corresponding measured data recorded during operation of the set-point profile, which defines a trajectory of Kombi Current Step Response for 1 h at 35 °C.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2021-01-15_Setpoint-Profile_Kombi-Current-Step Response_35°C_60min_2.xls

Text:

The 100 kW Proton Exchange Membrane (PEM) electrolyzer is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the set-point profile, which defines a trajectory of a Kombi Current Step Response for 1 h at 35 °C executed through a predefined control sequence.

application/vnd.ms-excel

Label:

2021-01-18_Data_measured_Kombi-Current-Step Response_25.C_60min_1.xlsx

Text:

The system is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the corresponding measured data recorded during operation of the set-point profile, which defines a trajectory of Kombi Current Step Response for 1 h at 25 °C.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2021-01-18_Setpoint-Profile_Kombi-Current-Step Response_25°C_60min_1.xls

Text:

The 100 kW Proton Exchange Membrane (PEM) electrolyzer is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the set-point profile, which defines a trajectory of a Kombi Current Step Response for 1 h at 25 °C executed through a predefined control sequence.

application/vnd.ms-excel

Label:

2021-01-19_Data_measured_Kombi-Current-Step Response_35-55.C_60min_1.xlsx

Text:

The system is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the corresponding measured data recorded during operation of the set-point profile, which defines a trajectory of Kombi Current Step Response for 1 h at 35 - 55 °C.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2021-01-19_Setpoint-Profile_Kombi-Current-Step Response_35-55°C_60min_1.xls

Text:

The 100 kW Proton Exchange Membrane (PEM) electrolyzer is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the set-point profile, which defines a trajectory of a Kombi Current Step Response for 1 h at 35 -55 °C executed through a predefined control sequence.

application/vnd.ms-excel

Label:

2021-01-20_Data_measured_Kombi-Current-Wind Power_300min_2.xlsx

Text:

The system is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the corresponding measured data recorded during operation of the set-point profile, which defines a trajectory of a wind turbine 300 min.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2021-01-20_Setpoint-Profile_Kombi-Current-Wind Power_300min_2.xls

Text:

The 100 kW Proton Exchange Membrane (PEM) electrolyzer is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the set-point profile, which defines a trajectory of a wind turbine 300 min executed through a predefined control sequence.

application/vnd.ms-excel

Label:

2021-01-21_Data_measured_Kombi-PV-Profile_PHOEBUS-3.xlsx

Text:

The system is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the corresponding measured data recorded during operation of the set-point profile, which defines a trajectory of a Kombi-PV-Profile from the Project PHOEBUS.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2021-01-21_Setpoint-Profile_Kombi-PV-Profile_PHOEBUS-3.xls

Text:

The 100 kW Proton Exchange Membrane (PEM) electrolyzer is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the set-point profile, which defines a trajectory of a Kombi-PV-Profile from the Project PHOEBUS executed through a predefined control sequence

application/vnd.ms-excel

Label:

2021-01-22_Data_measured_Kombi-PV-Profile_PHOEBUS-4.xlsx

Text:

The system is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the corresponding measured data recorded during operation of the set-point profile, which defines a trajectory of a Kombi-PV-Profile from the Project PHOEBUS.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2021-01-22_Setpoint-Profile_Kombi-PV-Profile_PHOEBUS-4.xls

Text:

The 100 kW Proton Exchange Membrane (PEM) electrolyzer is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the set-point profile, which defines a trajectory of a Kombi-PV-Profile from the Project PHOEBUS executed through a predefined control sequence

application/vnd.ms-excel

Label:

2021-01-26_Data_measured_Kombi-Current-Step Response_10min_2-3bar.xlsx

Text:

The system is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the corresponding measured data recorded during operation of the set-point profile, which defines a trajectory of Kombi Current Step Response for 1min at 75 °C.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2021-01-26_Setpoint-Profile_Kombi-Current-Step Response_10min_2-3bar.xls

Text:

The 100 kW Proton Exchange Membrane (PEM) electrolyzer is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the set-point profile, which defines a trajectory of a Kombi Current Step Response for 10 min at 75 °C executed through a predefined control sequence.

application/vnd.ms-excel

Label:

2021-01-27_1st_Data_measured_Kombi-Current-Step Response_75.C_5min.xlsx

Text:

The system is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the corresponding measured data recorded during operation of the set-point profile, which defines a trajectory of Kombi Current Step Response for 5 min at 75 °C.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2021-01-27_1st_Setpoint-Profile_Kombi-Current-Step Response_75.C_5min.xls

Text:

The 100 kW Proton Exchange Membrane (PEM) electrolyzer is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the set-point profile, which defines a trajectory of a Kombi Current Step Response for 5 min at 75 °C executed through a predefined control sequence.

application/vnd.ms-excel

Label:

2021-01-27_2nd_Data_measured_Kombi-Current-Step Response_75.C_5min.xlsx

Text:

The system is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the corresponding measured data recorded during operation of the set-point profile, which defines a trajectory of Kombi Current Step Response for 5 min at 75 °C.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2021-01-27_2nd_Setpoint-Profile_Kombi-Current-Step Response_75°C_5min.xls

Text:

The 100 kW Proton Exchange Membrane (PEM) electrolyzer is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the set-point profile, which defines a trajectory of a Kombi Current Step Response for 5 min at 75 °C executed through a predefined control sequence.

application/vnd.ms-excel

Label:

2021-01-28_Data_measured_Kombi-Current-Step Response_10min_Single-Stack.xlsx

Text:

The system is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the corresponding measured data recorded during operation of the set-point profile, which defines a trajectory of Kombi Current Step Response for 10 min at 75 °C on a single stack.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2021-01-28_Setpoint-Profile_Kombi-Current-Step Response_10min_Single-Stack.xls

Text:

The 100 kW Proton Exchange Membrane (PEM) electrolyzer is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the set-point profile, which defines a trajectory of a Kombi Current Step Response for 10 min at 65 °C executed through a predefined control sequence on a single stack.

application/vnd.ms-excel

Label:

2021-02-10_1st_Data_measured_Kombi-Current-Step Response_10min_varPump.xlsx

Text:

The system is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the corresponding measured data recorded during operation of the set-point profile, which defines a trajectory of Kombi Current Step Response for 10 min at 75 °C.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2021-02-10_1st_Setpoint-Profile_Kombi-Current-Step Response_10min_varPump.xls

Text:

The 100 kW Proton Exchange Membrane (PEM) electrolyzer is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the set-point profile, which defines a trajectory of a Kombi Current Step Response for 10 min at 75 °C executed through a predefined control sequence.

application/vnd.ms-excel

Label:

2021-02-10_2nd_Data_measured_Kombi-Current-Step Response_10min_varPump.xlsx

Text:

The system is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the corresponding measured data recorded during operation of the set-point profile, which defines a trajectory of Kombi Current Step Response for 10 min at 75 °C.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2021-02-10_2nd_Setpoint-Profile_Kombi-Current-Step Response_10min_varPump.xls

Text:

The 100 kW Proton Exchange Membrane (PEM) electrolyzer is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the set-point profile, which defines a trajectory of a Kombi Current Step Response for 10 min at 75 °C executed through a predefined control sequence.

application/vnd.ms-excel

Label:

2021-05-06_Data_measured_Heating-Up-Phase_no current.xlsx

Text:

The data corresponds to the 100 kW Proton Exchange Membrane (PEM) electrolyzer, during which the system’s control strategies were tested and initiated. All set-points were configured manually, without the implementation of automated control sequences. During this phase, the system is heated up without an additional current.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2021-12-21_Data_measured_Heating-Up-Phase_no_current.xlsx

Text:

The data corresponds to the 100 kW Proton Exchange Membrane (PEM) electrolyzer, during which the system’s control strategies were tested and initiated. All set-points were configured manually, without the implementation of automated control sequences. During this phase, the system is heated up without an additional current.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2022-01-17_Data_measured_Heating-Up-Phase_no_current.xlsx

Text:

The data corresponds to the 100 kW Proton Exchange Membrane (PEM) electrolyzer, during which the system’s control strategies were tested and initiated. All set-points were configured manually, without the implementation of automated control sequences. During this phase, the system is heated up without an additional current.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2022-01-26_Data_measured_Heating-Up-Phase_no_current.xlsx

Text:

The data corresponds to the 100 kW Proton Exchange Membrane (PEM) electrolyzer, during which the system’s control strategies were tested and initiated. All set-points were configured manually, without the implementation of automated control sequences. During this phase, the system is heated up without an additional current.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2023-10-11_Data_measured_Test_Dynamic_Ramping_constraints.xlsx

Text:

The system is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the corresponding measured data recorded during operation of the set-point profile, which defines a trajectory of dynamic ramping constraints.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2023-10-11_Setpoint-Profile_Test_Dynamic_Ramping_constraints.xls

Text:

The 100 kW Proton Exchange Membrane (PEM) electrolyzer is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the set-point profile, which defines a trajectory of dynamic ramping constraints executed through a predefined control sequence.

application/vnd.ms-excel

Label:

2023-10-26_Data-measured_Dynamic-Feedforward_Dynamic-Ramping_no-turn-off_abort-1.xlsx

Text:

The system is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the corresponding measured data recorded during operation of the set-point profile, which defines a trajectory of dynamic ramping constraints. The stack temperature is controlled by a dynamic feedforward control loop. Throughout the procedure, the load remains active and is not switched off.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2023-10-26_Data-measured_Dynamic-Feedforward_Dynamic-Ramping_no-turn-off_abort-2.xlsx

Text:

The system is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the corresponding measured data recorded during operation of the set-point profile, which defines a trajectory of dynamic ramping constraints. The stack temperature is controlled by a dynamic feedforward control loop. Throughout the procedure, the load remains active and is not switched off.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2023-10-26_Data-measured_Dynamic-Feedforward_Dynamic-Ramping_no-turn-off_abort-3.xlsx

Text:

The system is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the corresponding measured data recorded during operation of the set-point profile, which defines a trajectory of dynamic ramping constraints.The stack temperature is controlled by a dynamic feedforward control loop. Throughout the procedure, the load remains active and is not switched off.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2023-10-26_Setpoint-Profile_Dynamic-Feedforward_Dynamic-Ramping_no-turn-off_abort-1.xls

Text:

The 100 kW Proton Exchange Membrane (PEM) electrolyzer is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file defines the set-point profile, specifying the trajectory of dynamic ramping constraints applied through a predefined control sequence. The stack temperature is controlled by a dynamic feedforward control loop. Throughout the procedure, the load remains active and is not switched off.

application/vnd.ms-excel

Label:

2023-10-26_Setpoint-Profile_Dynamic-Feedforward_Dynamic-Ramping_no-turn-off_abort-2.xls

Text:

The 100 kW Proton Exchange Membrane (PEM) electrolyzer is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file defines the set-point profile, specifying the trajectory of dynamic ramping constraints applied through a predefined control sequence. The stack temperature is controlled by a dynamic feedforward control loop. Throughout the procedure, the load remains active and is not switched off.

application/vnd.ms-excel

Label:

2023-10-26_Setpoint-Profile_Dynamic-Feedforward_Dynamic-Ramping_no-turn-off_abort-3.xls

Text:

The 100 kW Proton Exchange Membrane (PEM) electrolyzer is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file defines the set-point profile, specifying the trajectory of dynamic ramping constraints applied through a predefined control sequence. The stack temperature is controlled by a dynamic feedforward control loop. Throughout the procedure, the load remains active and is not switched off.

application/vnd.ms-excel

Label:

2023-11-02_Data-measured_Dynamic-Feedforward_Dynamic-Ramping_no-turn-off_meas-1.xlsx

Text:

The system is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the corresponding measured data recorded during operation of the set-point profile, which defines a trajectory of dynamic ramping constraints. The stack temperature is controlled by a dynamic feedforward control loop. Throughout the procedure, the load remains active and is not switched off.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2023-11-02_Setpoint-Profile_Dynamic-Feedforward_Dynamic-Ramping_no-turn-off_meas-1.xls

Text:

The 100 kW Proton Exchange Membrane (PEM) electrolyzer is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file defines the set-point profile, specifying the trajectory of dynamic ramping constraints applied through a predefined control sequence. The stack temperature is controlled by a dynamic feedforward control loop. Throughout the procedure, the load remains active and is not switched off.

application/vnd.ms-excel

Label:

2023-11-03_Data-measured_Dynamic-Feedforward_Dynamic-Ramping_no-turn-off_abort-4.xlsx

Text:

The system is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the corresponding measured data recorded during operation of the set-point profile, which defines a trajectory of dynamic ramping constraints.The stack temperature is controlled by a dynamic feedforward control loop. Throughout the procedure, the load remains active and is not switched off.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2023-11-03_Data-measured_Dynamic-Feedforward_Dynamic-Ramping_no-turn-off_abort-5.xlsx

Text:

The system is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the corresponding measured data recorded during operation of the set-point profile, which defines a trajectory of dynamic ramping constraints. The stack temperature is controlled by a dynamic feedforward control loop. Throughout the procedure, the load remains active and is not switched off.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2023-11-03_Data-measured_Dynamic-Feedforward_Dynamic-Ramping_no-turn-off_abort-6.xlsx

Text:

The system is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the corresponding measured data recorded during operation of the set-point profile, which defines a trajectory of dynamic ramping constraints. The stack temperature is controlled by a dynamic feedforward control loop. Throughout the procedure, the load remains active and is not switched off.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2023-11-03_Data-measured_Dynamic-Feedforward_Dynamic-Ramping_no-turn-off_abort-7.xlsx

Text:

The system is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the corresponding measured data recorded during operation of the set-point profile, which defines a trajectory of dynamic ramping constraints. The stack temperature is controlled by a dynamic feedforward control loop. Throughout the procedure, the load remains active and is not switched off.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2023-11-03_Setpoint-Profile_Dynamic-Feedforward_Dynamic-Ramping_no-turn-off_abort-4.xls

Text:

The 100 kW Proton Exchange Membrane (PEM) electrolyzer is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file defines the set-point profile, specifying the trajectory of dynamic ramping constraints applied through a predefined control sequence. The stack temperature is controlled by a dynamic feedforward control loop. Throughout the procedure, the load remains active and is not switched off.

application/vnd.ms-excel

Label:

2023-11-03_Setpoint-Profile_Dynamic-Feedforward_Dynamic-Ramping_no-turn-off_abort-5.xls

Text:

The 100 kW Proton Exchange Membrane (PEM) electrolyzer is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file defines the set-point profile, specifying the trajectory of dynamic ramping constraints applied through a predefined control sequence. The stack temperature is controlled by a dynamic feedforward control loop. Throughout the procedure, the load remains active and is not switched off.

application/vnd.ms-excel

Label:

2023-11-03_Setpoint-Profile_Dynamic-Feedforward_Dynamic-Ramping_no-turn-off_abort-6.xls

Text:

The 100 kW Proton Exchange Membrane (PEM) electrolyzer is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file defines the set-point profile, specifying the trajectory of dynamic ramping constraints applied through a predefined control sequence. The stack temperature is controlled by a dynamic feedforward control loop. Throughout the procedure, the load remains active and is not switched off.

application/vnd.ms-excel

Label:

2023-11-03_Setpoint-Profile_Dynamic-Feedforward_Dynamic-Ramping_no-turn-off_abort-7.xls

Text:

The 100 kW Proton Exchange Membrane (PEM) electrolyzer is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file defines the set-point profile, specifying the trajectory of dynamic ramping constraints applied through a predefined control sequence. The stack temperature is controlled by a dynamic feedforward control loop. Throughout the procedure, the load remains active and is not switched off.

application/vnd.ms-excel

Label:

2023-11-09_Data-measured_Dynamic-Feedforward_Dynamic-Ramping_turn-off_abort-8.xlsx

Text:

The system is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the corresponding measured data recorded during operation of the set-point profile, which defines a trajectory of dynamic ramping constraints. The stack temperature is controlled by a dynamic feedforward control loop. During the procedure, the load was partially switched off.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2023-11-09_Data-measured_Dynamic-Feedforward_Dynamic-Ramping_turn-off_abort-9.xlsx

Text:

The system is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the corresponding measured data recorded during operation of the set-point profile, which defines a trajectory of dynamic ramping constraints. The stack temperature is controlled by a dynamic feedforward control loop. During the procedure, the load was partially switched off.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2023-11-09_Setpoint-Profile_Dynamic-Feedforward_Dynamic-Ramping_turn-off_abort-8.xls

Text:

The 100 kW Proton Exchange Membrane (PEM) electrolyzer is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file defines the set-point profile, specifying the trajectory of dynamic ramping constraints applied through a predefined control sequence. The stack temperature is controlled by a dynamic feedforward control loop. During the procedure, the load was partially switched off.

application/vnd.ms-excel

Label:

2023-11-09_Setpoint-Profile_Dynamic-Feedforward_Dynamic-Ramping_turn-off_abort-9.xls

Text:

The 100 kW Proton Exchange Membrane (PEM) electrolyzer is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file defines the set-point profile, specifying the trajectory of dynamic ramping constraints applied through a predefined control sequence. The stack temperature is controlled by a dynamic feedforward control loop. During the procedure, the load was partially switched off.

application/vnd.ms-excel

Label:

2023-11-13_Data-measured_Dynamic-Feedforward_Dynamic-Ramping_turn-off_abort-10.xlsx

Text:

The system is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the corresponding measured data recorded during operation of the set-point profile, which defines a trajectory of dynamic ramping constraints. The stack temperature is controlled by a dynamic feedforward control loop. During the procedure, the load was partially switched off.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2023-11-13_Setpoint-Profile_Dynamic-Feedforward_Dynamic-Ramping_turn-off_abort-10.xls

Text:

The 100 kW Proton Exchange Membrane (PEM) electrolyzer is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file defines the set-point profile, specifying the trajectory of dynamic ramping constraints applied through a predefined control sequence. The stack temperature is controlled by a dynamic feedforward control loop. During the procedure, the load was partially switched off.

application/vnd.ms-excel

Label:

2023-11-14_Data-measured_Dynamic-Feedforward_Dynamic-Ramping_turn-off-1_meas-2.xlsx

Text:

The system is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the corresponding measured data recorded during operation of the set-point profile, which defines a trajectory of dynamic ramping constraints. The stack temperature is controlled by a dynamic feedforward control loop. During the procedure, the load was partially switched off.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2023-11-14_Setpoint-Profile_Dynamic-Feedforward_Dynamic-Ramping_turn-off-1_meas-2.xls

Text:

The 100 kW Proton Exchange Membrane (PEM) electrolyzer is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file defines the set-point profile, specifying the trajectory of dynamic ramping constraints applied through a predefined control sequence. The stack temperature is controlled by a dynamic feedforward control loop. During the procedure, the load was partially switched off.

application/vnd.ms-excel

Label:

2023-11-15_Data-measured_Dynamic-Feedforward_Dynamic-Ramping_turn-off-2_meas-3.xlsx

Text:

The system is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the corresponding measured data recorded during operation of the set-point profile, which defines a trajectory of dynamic ramping constraints. The stack temperature is controlled by a dynamic feedforward control loop. During the procedure, the load was partially switched off.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

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2023-11-15_Setpoint-Profile_Dynamic-Feedforward_Dynamic-Ramping_turn-off-2_meas-3.xls

Text:

The 100 kW Proton Exchange Membrane (PEM) electrolyzer is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file defines the set-point profile, specifying the trajectory of dynamic ramping constraints applied through a predefined control sequence. The stack temperature is controlled by a dynamic feedforward control loop. During the procedure, the load was partially switched off.

application/vnd.ms-excel

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2023-11-20_Data-measured_PID_Dynamic-Ramping_turn-off_meas-4.xlsx

Text:

The system is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the corresponding measured data recorded during operation of the set-point profile, which defines a trajectory of dynamic ramping constraints. The stack temperature is controlled by a PID control loop. During the procedure, the load was partially switched off.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2023-11-20_Setpoint-Profile_PID_Dynamic-Ramping_turn-off_meas-4.xls

Text:

The 100 kW Proton Exchange Membrane (PEM) electrolyzer is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file defines the set-point profile, specifying the trajectory of dynamic ramping constraints applied through a predefined control sequence. The stack temperature is controlled by a PID control loop. During the procedure, the load was partially switched off.

application/vnd.ms-excel

Label:

2023-11-22_Data-measured_PID_Dynamic-Ramping_no-turn-off_meas-5.xlsx

Text:

The system is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the corresponding measured data recorded during operation of the set-point profile, which defines a trajectory of dynamic ramping constraints. The stack temperature is controlled by a PID control loop. Throughout the procedure, the load remains active and is not switched off.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2023-11-22_Setpoint-Profile_PID_Dynamic-Ramping_no-turn-off_meas-5.xls

Text:

The 100 kW Proton Exchange Membrane (PEM) electrolyzer is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file defines the set-point profile, specifying the trajectory of dynamic ramping constraints applied through a predefined control sequence. The stack temperature is controlled by a PID control loop. Throughout the procedure, the load remains active and is not switched off.

application/vnd.ms-excel

Label:

2023-11-23_Data-measured_Dynamic-Feedforward_Benchmark_no-turn-off_meas-6.xlsx

Text:

The system is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the corresponding measured data recorded during operation of the set-point profile, which defines a trajectory of dynamic ramping constraints. The stack temperature is controlled by a dynamic feedforward control loop. Throughout the procedure, the load remains active and is not switched off.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2023-11-23_Setpoint-Profile_Dynamic-Feedforward_Benchmark_no-turn-off_meas-6.xls

Text:

The 100 kW Proton Exchange Membrane (PEM) electrolyzer is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file defines the set-point profile, specifying the trajectory of dynamic ramping constraints applied through a predefined control sequence. The stack temperature is controlled by a dynamic feedforward control loop. Throughout the procedure, the load remains active and is not switched off.

application/vnd.ms-excel

Label:

2023-11-27_Data-measured_PID_Benchmark_no-turn-off_meas-7.xlsx

Text:

The system is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the corresponding measured data recorded during operation of the set-point profile, which defines a trajectory of dynamic ramping constraints. The stack temperature is controlled by a PID control loop. Throughout the procedure, the load remains active and is not switched off.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2023-11-27_Setpoint-Profile_PID_Benchmark_no-turn-off_meas-7.xls

Text:

The 100 kW Proton Exchange Membrane (PEM) electrolyzer is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file defines the set-point profile, specifying the trajectory of dynamic ramping constraints applied through a predefined control sequence. The stack temperature is controlled by a PID control loop. Throughout the procedure, the load remains active and is not switched off.

application/vnd.ms-excel

Label:

2023-11-28_Data-measured_Static-Feedforward_Dynamic-Ramping_no-turn-off_meas-8.xlsx

Text:

The system is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the corresponding measured data recorded during operation of the set-point profile, which defines a trajectory of dynamic ramping constraints. The stack temperature is controlled by a static feedforward control loop. Throughout the procedure, the load remains active and is not switched off.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2023-11-28_Setpoint-Profile_Static-Feedforward_Dynamic-Ramping_no-turn-off_meas-8.xls

Text:

The 100 kW Proton Exchange Membrane (PEM) electrolyzer is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file defines the set-point profile, specifying the trajectory of dynamic ramping constraints applied through a predefined control sequence. The stack temperature is controlled by a static feedforward control loop. Throughout the procedure, the load remains active and is not switched off.

application/vnd.ms-excel

Label:

2023-11-29_Data-measured_Static-Feedforward_Dynamic-Ramping_turn-off_meas-9.xlsx

Text:

The system is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file contains the corresponding measured data recorded during operation of the set-point profile, which defines a trajectory of dynamic ramping constraints. The stack temperature is controlled by a static feedforward control loop. During the procedure, the load was partially switched off.

application/vnd.openxmlformats-officedocument.spreadsheetml.sheet

Label:

2023-11-29_Setpoint-Profile_Static-Feedforward_Dynamic-Ramping_turn-off_meas-9.xls

Text:

The 100 kW Proton Exchange Membrane (PEM) electrolyzer is operating under normal conditions, with all set-points defined by a predefined set-point profile executed through a control sequence. This file defines the set-point profile, specifying the trajectory of dynamic ramping constraints applied through a predefined control sequence. The stack temperature is controlled by a static feedforward control loop. During the procedure, the load was partially switched off.

application/vnd.ms-excel