Data Hub for Life Cycle Assessment of Climate Change Solutions—Hydrogen Case Study
Abstract
:1. Introduction
2. Materials and Methods
2.1. High-Level Data Hub Architecture
- Build a comprehensive scientific/technical data information architecture to enable efficient data integration from different sources, data analytics, and impact assessments.
- Provide an adaptive architecture to integrate existing databases within and outside the federal labs.
- Provide a dynamic and secure environment for existing and new data to enable faster decision-making for both policymakers and researchers.
2.2. Hierarchy of Data and Data Linkages in Data Hub
2.2.1. Scientific and Technology Data
2.2.2. LCI Data and Framework
2.2.3. Environmental Product Declarations (EPD)
2.2.4. Proxy Data and High-Level Decision-Making Data
3. Results and Discussion
3.1. Case Study—Hydrogen Production Using PEM
3.2. Overview of LCA Methodology
- Goal and scope definition, which state the aims for performing the LCA study and include the scope (product system, system boundary, functional unit, and others as the type of hydrogen production pathway, and geographical scope).
- Life cycle inventory, which comprises a literature review, collection of (primary) data, building a hydrogen LCI database, and data quality evaluation.
- Life cycle impact assessment, which considers the calculation of carbon intensity for a hydrogen production pathway [29].
3.2.1. Goal and Scope
3.2.2. Life Cycle Inventory
- Step 1. Literature review to collect existing LCI datasets, and identify the preliminary process flow diagram, key parameters, and assumptions.
- Step 2. Undertake the process simulation. In this step, a process flow diagram, mass–energy balance, and the initial LCI are obtained.
- Step 3. LCI datasets are finalized, which include LCI data gap, validation, and data quality assessment.
- Step 4. LCI data are transformed into potential environmental impacts using life cycle impact assessment methods.
- Collection of primary LCI data
- Building a hydrogen LCI database
- Data quality evaluation
- The most important parameters (electrolyzer stack efficiency) that affect the electrolyzer electricity consumption were obtained from literature [30]. This technoeconomic assessment study analyzes the H2 production costs of a state-of-the-art PEM electrolyzer. Technical data from four independent electrolyzer companies were obtained through questionnaires, and an engineering system performance model was developed from these inputs to create a generalized electrolyzer system engineering design consistent with the diverse industry input from electrolyzer manufacturers. Hence, these parameters can be considered primary data valid until 2020.
- The anode and cathode pressures are based on literature [31], which is a review paper on high-pressure PEM water electrolyzers. The data are sourced from the average pressure of commercial PEM based on a market survey result of 11 active manufacturers marketing large-scale PEM electrolyzer systems.
- Heat losses and hydrogen diffusion to the anode were based on literature [32], which is a process simulation of alkaline electrolysis operation and experimental validation study using a 10 kW bench scale setup.
- The thermal management and cooling system parameters of the PEM electrolyzer were based on literature [33]. This study models heat generation and its management for a PEM electrolyzer. The models are based on state-of-the-art technology at the time of the study (2019) and hence can be considered secondary data.
- Faradaic efficiency of hydrogen production was obtained from literature [34]. The data are sourced from an experimental lab-scale PEM electrolysis setup of 0.4 kW.
- The majority of data sources used to model the PEM electrolysis plant are from 2019–2022.
- Reliability
- Completeness
- Time-related appropriateness
- Geographical appropriateness
- Technological appropriateness
- Process completeness
- Process review
3.2.3. Life Cycle Impact Assessment
3.3. Implementation of H2 Production Datasets in the Collaboration Server
3.4. Life Cycle Sustainablity Assessment
4. Conclusions
Limitations
Author Contributions
Funding
Institutional Review Board Statement
Informed Consent Statement
Data Availability Statement
Conflicts of Interest
References
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Input/Output | Value | Unit |
---|---|---|
Main inputs to the process | ||
Water | 3595.7 | kg/h |
Electricity consumption—Electrolyzer | 20,000 | kW |
Electricity consumption—BoP | 290.61 | kW |
Main outputs from the process | ||
Hydrogen output | kg/h | |
| 396.5 | kg/h |
| 0 | kg/h |
| 0.1 | kg/h |
Purge | kg/h | |
| 1.2 | kg/h |
| 2.4 | kg/h |
| 0 | kg/h |
Oxygen output | kg/h | |
| 0.6 | kg/h |
| 23.5 | kg/h |
| 3161.7 | kg/h |
Residual vapor | kg/h | |
| 0 | kg/h |
| 9.4 | kg/h |
| 0 | kg/h |
Flow Name | Value | Unit | Data Quality (Flows) | Data Quality (Process) |
---|---|---|---|---|
Input flows | (1, 4) | |||
Deionized water required | 9.1 | kg | (3, 5, 1, 3, 2) | |
Electricity required | 55.2 | kWh | (3, 5, 1, 3, 2) | |
Output flows | ||||
Hydrogen produced | 1 | kg | (3, 5, 1, 3, 2) | |
Oxygen produced | 8.0 | kg | (3, 5, 1, 3, 2) |
Environmental Impact Catogory | Result | Unit |
---|---|---|
Mineral resource scarcity | 0.00975 | kg Cu eq |
Human non-carcinogenic toxicity | 1.3809 | kg 1,4-DCB |
Human carcinogenic toxicity | 0.15429 | kg 1,4-DCB |
Freshwater ecotoxicity | 0.26103 | kg 1,4-DCB |
Water consumption | 1.13287 | m3 |
Marine ecotoxicity | 0.32041 | kg 1,4-DCB |
Stratospheric ozone depletion | 3.62 × 10−6 | kg CFC11 eq |
Land use | 0.55658 | m2a crop eq |
Ionizing radiation | 0.60945 | kBq Co-60 eq |
Freshwater eutrophication | 0.00018 | kg P eq |
Terrestrial ecotoxicity | 8.24127 | kg 1,4-DCB |
Marine eutrophication | 2.58 × 10−5 | kg N eq |
Terrestrial acidification | 0.00316 | kg SO2 eq |
Fine particulate matter formation | 0.00123 | kg PM2.5 eq |
Ozone formation, terrestrial ecosystems | 0.00218 | kg NOx eq |
Flow Name | Background System Process |
---|---|
Monoethanolamine | market for monoethanolamine|monoethanolamine {GLO} |
Zinc oxide | market for zinc oxide|zinc oxide {GLO} |
Aluminium oxide | market for aluminium oxide, metallurgical|aluminium oxide, metallurgical {GLO} |
Copper oxide | market for copper oxide|copper oxide {GLO} |
Activated carbon | market for activated carbon, granular|activated carbon, granular {GLO} |
Wastewater | treatment of wastewater, average, capacity 5E9l/year|wastewater, average {CA-QC} |
Steam | steam production, as energy carrier, in chemical industry|heat, from steam, in chemical industry [37] |
Nitrogen | market for Nitrogen, liquid [37] |
KOH | market for potassium hydroxide|potassium hydroxide {GLO} |
Polyacrylic acids | market for Acrylic acid {GLO} |
Sulfuric acid | market for Sulfuric Acid {GLO} |
Caustic soda | market for Caustic Soda {GLO} |
Chlorine | market for Chlorine {GLO} |
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Zargar, S.; Kannangara, M.; Gonzales-Calienes, G.; Yang, J.; Shadbahr, J.; Decès-Petit, C.; Bensebaa, F. Data Hub for Life Cycle Assessment of Climate Change Solutions—Hydrogen Case Study. Data 2024, 9, 129. https://doi.org/10.3390/data9110129
Zargar S, Kannangara M, Gonzales-Calienes G, Yang J, Shadbahr J, Decès-Petit C, Bensebaa F. Data Hub for Life Cycle Assessment of Climate Change Solutions—Hydrogen Case Study. Data. 2024; 9(11):129. https://doi.org/10.3390/data9110129
Chicago/Turabian StyleZargar, Shiva, Miyuru Kannangara, Giovanna Gonzales-Calienes, Jianjun Yang, Jalil Shadbahr, Cyrille Decès-Petit, and Farid Bensebaa. 2024. "Data Hub for Life Cycle Assessment of Climate Change Solutions—Hydrogen Case Study" Data 9, no. 11: 129. https://doi.org/10.3390/data9110129
APA StyleZargar, S., Kannangara, M., Gonzales-Calienes, G., Yang, J., Shadbahr, J., Decès-Petit, C., & Bensebaa, F. (2024). Data Hub for Life Cycle Assessment of Climate Change Solutions—Hydrogen Case Study. Data, 9(11), 129. https://doi.org/10.3390/data9110129