Hafsa Mehmoodab,
Haseeb Akbarab,
Pariyapat Nilsalabab and
Shabbir H. Gheewala*ab
aThe Joint Graduate School of Energy and Environment, King Mongkut's University of Technology Thonburi, Bangkok 10140, Thailand. E-mail: shabbir.ghe@kmutt.ac.th; shabbirg@hotmail.com
bCenter of Excellence on Energy Technology and Environment, Ministry of Higher Education, Science, Research and Innovation, Bangkok 10400, Thailand
First published on 17th December 2024
Hydrogen is emerging as an immense source of energy having the potential to at least partly replace fossil fuels. It is an abundant element on earth, but does not mainly exist in free form. Hydrogen can be produced through different technologies and feedstocks, and based on these, it can be categorized into colors with different environmental impacts. This work aimed to review the environmental impacts of the production of gray (from natural gas without carbon capture and storage), brown (from coal gasification), blue (from fossil fuels with carbon capture and storage), green (from renewable energy or biological process), and turquoise (pyrolysis of natural gas) hydrogen and to identify sustainable hydrogen production pathways that minimize environmental impacts. Global warming, acidification, eutrophication, and resource depletion were considered as indicators to assess the environmental impacts. The results showed that brown hydrogen produced via coal gasification had the highest global warming, acidification, and resource depletion impacts among all the options considered. On the other hand, green hydrogen from electrolysis through wind energy had the lowest environmental impacts. However, adopting these hydrogen colors presents different challenges and opportunities. Success depends on effective policy frameworks, international cooperation, and technological readiness to ensure positive contributions to global sustainability goals.
Hydrogen is itself a colorless gas, but is now known by its different colors, which are derived from the technology and source of its production. The emissions generated during the production of hydrogen depend on the resources used for its production. Currently, approximately 95% of all the hydrogen is being produced from fossil fuels with adverse environmental impacts.7 Researchers are trying to find more promising and sustainable ways to produce hydrogen energy. Green hydrogen is increasingly popular because it has the potential to achieve a zero-carbon economy. It is produced from electricity generated by renewable energy sources like solar, wind, and hydro through the electrolysis of water and thus has less GHG emissions. The GHG emissions vary widely from technique to technique for hydrogen production. Thus, most of the studies focused only on GHG emissions linked with hydrogen production.8–10 Focusing solely on GHG emissions can mislead policymakers. For example, blue hydrogen, generated via steam methane reforming (SMR) of natural gas with carbon capture and storage (CCS), has the potential to achieve lower GHG emissions. The integration of CCS technology mitigates a significant portion of the CO2 emissions typically associated with SMR, making blue hydrogen a potentially favorable option in terms of reducing GHG emissions and addressing climate change concerns.11 However, when other environmental impacts such as acidification, eutrophication, and abiotic resource depletion are considered, the overall assessment could lead to a markedly different conclusion.
Most existing reviews have focused primarily on global warming, and some have also considered acidification.12,13 A few mentioned other impact categories, but did not analyze them any further.14 This study conducted a comprehensive review of the existing literature and employed metrics such as global warming, acidification, eutrophication, and resource depletion to analyze the environmental impacts across a comprehensive set of pathways of hydrogen production. In addition, this analysis was used to formulate a ranking of the pathways that were further qualified for short, medium, and long-term application using their technology readiness levels. Ultimately, this research aims to contribute to the global effort of transitioning to cleaner energy, reducing GHGs, and achieving carbon neutrality.
A total of 4266 papers were initially identified in the databases. Papers published before 2014 were excluded (n = 3796), considered only peer-reviewed articles (n = 2215). During the screening process, studies that did not mention LCA or hydrogen production technologies in their abstracts were also excluded (n = 138). The final selection focused on papers discussing hydrogen production technologies with LCA integration, where only those that provided a comprehensive explanation of methodology and framework were included for further analysis (n = 45). The graphical representation of the article selection for the literature review is shown in Fig. 1.
To improve the quality further, highly cited studies were selected for review. The environmental impacts of hydrogen production of different colors by using the LCA methodology were investigated. LCA offers a systematic and analytical approach to assessing the environmental impact of products and services throughout their entire life cycle, from the extraction of raw materials to their disposal or recycling.15 Life cycle assessment provides a holistic approach that enables a thorough assessment of all environmental impacts, including resource depletion, greenhouse gas emissions, energy use, etc. The LCA is widely used in the scientific community. Notable hydrogen-related studies that have applied LCA for environmental assessment include those by Bhandari et al.,16 Osman et al.,14 and Salkuyeh et al.17 The LCA is particularly valuable as it identifies trade-offs between different impact categories and supports informed decision-making by comparing various hydrogen production methods. In contrast to other methodologies, such as the environmental impact assessment method, which focuses on specific projects. Life cycle assessment is superior to other methods, especially for comparative analysis.18 Other methodologies, such as carbon footprint analysis, which mainly assesses greenhouse gas emissions, LCA provides a broader, more detailed evaluation.
As replacement of fossil energy is the key issue of concern due to its non-renewability and emissions of greenhouse gases, global warming, acidification, eutrophication, and resource depletion were analyzed as the main environmental indicators of interest.19–21 Thus, the LCA methodology was chosen for comparing environmental performance of different colors of hydrogen. Further, these indicators were normalized to rank the hydrogen colors based on environmental impacts. These indicators were normalized by applying the minimum–maximum normalization technique,22 as shown in eqn (1).
(1) |
Steam methane reforming is a primary industrial process for producing hydrogen. It involves a chemical reaction where methane, typically from natural gas, reacts with steam under high temperatures (700 °C to 1000 °C) and pressure in the presence of a nickel-based catalyst.23 The principal reactions in the SMR process are shown in eqn (2) and (3).
CH4 + H2O → CO + 3H2 | (2) |
CO + H2O → CO2 + H2 | (3) |
• Coal gasification
Coal gasification is a process that converts coal into a synthesis gas (syngas) comprising primarily hydrogen, carbon monoxide, and often some carbon dioxide.24 The basic chemical reaction in coal gasification is typically represented as shown in eqn (4).
C + H2O → CO + H2 | (4) |
• Biomass gasification
Biomass gasification is a thermochemical process that transforms organic materials into combustible gases at high temperatures with controlled oxygen or steam. This process starts with pyrolysis, where biomass is decomposed without oxygen to produce char, tar, and gases. The remaining biomass undergoes gasification reactions with steam and carbon dioxide, producing syngas rich in hydrogen, carbon monoxide, and methane. This syngas is cleaned to remove impurities like tar, particulates, and sulfur compounds. The hydrogen content is enhanced through the water–gas shift reaction, where carbon monoxide reacts with steam to produce additional hydrogen and carbon dioxide. Finally, the hydrogen is purified using techniques like pressure swing adsorption or membrane separation, yielding high-purity hydrogen for use in fuel cells, industrial processes, or as a clean energy carrier, providing a sustainable solution to manage biomass waste and decrease dependency on fossil fuels.
• Electrolysis
Hydrogen production via electrolysis involves using electricity to split water into hydrogen and oxygen, as shown in eqn (5). This method is eco-friendly when powered by renewable energy sources, producing “green hydrogen.” Key components include the electrodes (anode and cathode), electrolyte, and power source. Technologies vary in efficiency, including alkaline, PEM (proton exchange membrane), and SOEC (solid oxide electrolysis cells). Electrolysis is crucial for storing renewable energy and supplying clean fuel, particularly useful in heavy industry and transportation.25
H2O + direct current electricity → H2 + 1/2O2 | (5) |
• Dark fermentation
Dark fermentation is a biological process used to produce hydrogen gas from organic materials without the need for light. It involves the anaerobic breakdown of organic substrates by microorganisms, typically bacteria, which results in the production of hydrogen along with other byproducts like carbon dioxide and organic acids.26 The basic chemical reaction in dark fermentation can be summarized by the conversion of glucose, a common substrate, into hydrogen, carbon dioxide, and other organic acids. The generalized chemical equation as shown in eqn (6).
C6H12O6 → 2H2 + 2CO2 + 2CH3COOH | (6) |
• Photo fermentation
Photo fermentation is a process where photosynthetic bacteria use light to convert organic substrates into hydrogen. It primarily involves purple non-sulfur bacteria, which use sunlight to break down organic compounds like glucose into hydrogen and carbon dioxide, as shown in eqn (7) and (8). This method is valued for its use of renewable light energy, its ability to reduce waste by processing organic materials, and minimal carbon emissions. Commonly applied in waste treatment and renewable energy projects, photo fermentation offers a sustainable way to produce clean hydrogen fuel.27,28
6H2O + 6CO2 → C6H12O6 + 6O2 | (7) |
C6H12O6 + 6H2O → 6CO2 + 12H | (8) |
• Thermochemical water splitting
Thermochemical water splitting cycles offer significant benefits, including the absence of catalysis requirements for individual chemical reactions. Water serves as the primary material for hydrogen production, and all other chemicals involved in the cycle are recyclable. Additional advantages of thermochemical water splitting cycles include: (i) no necessity for O2–H2 separation membranes, (ii) a moderate temperature range requirement of 600–1200 K, and (iii) minimal to no electrical energy requirements.29
Fig. 2 Different colors of hydrogen by the technologies and feedstocks.5,30,31 |
Fig. 3 Description of technology readiness level (TRL) of hydrogen production technologies.32 |
Wilkinson et al.34 provided an overview of hydrogen production via different methods and various feedstocks, highlighting technology readiness levels. Electrolytic processes like alkaline electrolysis have the highest readiness at level 9, while newer methods like proton exchange membrane, solid oxide electrolysis, and anion exchange membrane range from levels 2 to 8. thermochemical methods like photovoltaic electrolysis and high-temperature electrolysis are at levels 5–7, while water-splitting cycles are lower at 3–4. Fossil fuel-based methods, particularly steam methane reforming with CCS, are mature at level 9, as are coal gasification and partial oxidation. Emerging technologies like methane cracking and syngas chemical looping are still developing, with readiness levels of 3–5. Biomass-based processes like SMR and gasification are at level 9, while biological methods such as dark fermentation and photo-fermentation are less advanced (levels 1–4). Table 1 covers hydrogen production pathways utilizing a range of energy feedstocks, each with varying technology readiness levels.
Feedstock | Process type | Production technology | Technology readiness level |
---|---|---|---|
Water | Electrolytic | Alkaline electrolysis (AE) | 9 |
Proton exchange membrane electrolysis (PEM) | 6–8 | ||
Solid oxide electrolyser cell electrolysis (SOE) | 5 | ||
Anion exchange membrane electrolysis (AEM) | 2–3 | ||
Nanogap electrochemical cells | 1–3 | ||
Thermochemical | Photovoltaic electrolysis (PVE) | 5–7 | |
High-temperature electrolysis (HTE) | 5–7 | ||
Thermochemical water-splitting cycles (TCC) | 3–4 | ||
Fossil fuel | Photolytic | Photocatalytic water splitting | 1–3 |
Thermochemical | Steam methane reforming (SMR) | 9 (8 with CCS) | |
Partial oxidation – thermal or catalytic | 9 (8 with CCS) | ||
Chemical looping reforming (CLR) | 8 (6 with CCS) | ||
Coal gasification | 9 (7 with CCS) | ||
Autothermal reforming (ATR) – dry or steam | 7 (5 with CCS) | ||
Methane cracking (CRA) | 3–5 | ||
Syngas chemical looping (SCL) | 3–5 | ||
Biomass | Thermochemical | Steam methane reforming (SMR) | 9 (8 with CCS) |
Biomass gasification | 9 (5 with CCS) | ||
Autothermal reforming (ATR) – dry or steam | 7 (5 with CCS) | ||
Biological | Dark fermentation | 2–4 | |
Biological/photolytic | Photo-fermentation | 1–3 | |
Other | Thermochemical | Co-product of industrial process (chlor-alkali) | 1–3 |
Processing of non-organic waste products | 1–3 |
Goren et al.,38 presented energy efficiency of different hydrogen production technologies. The mean value energy efficiencies of different technologies with expected variations is presented in Fig. 4. Fossil fuel steam reforming is highly efficient at 72.5% (±10%), though its effectiveness can vary with feedstock and conditions. Fossil fuel gasification, less efficient at 55% (41–69%), is more inconsistent, making it less reliable for energy production. Biomass steam reforming has similar efficiency (71.5% ± 13%) but with slightly higher uncertainty, while biomass gasification is less efficient (45% ± 12%) and more sensitive to operational conditions. Dark fermentation offers moderate efficiency (60% ± 15%) but is highly variable, impacting its scalability. Photo-fermentation, with the lowest efficiency (16% ± 9%), is an emerging technology that needs further improvement due to significant energy losses. Microbial electrolysis cells (68% ± 9%) are more stable and promising for hydrogen production. Water electrolysis is also efficient (71.5% ± 10%) but depends on electricity sources, especially when using renewable energy.
Fig. 4 Average energy efficiency values of H2 production methods for different resources.38 SR_F is steam reforming using fossil, G_F is gasification using fossil, SR_B is steam reforming using biomass, G_B is gasification using biomass, DF_B is dark fermentation using biomass, PF_B is photo-fermentation, using biomass, MEC_B is microbial electrolysis cell using biomass, and E is electrolysis using water. |
Hydrogen production techniques with wider efficiency ranges, like dark fermentation and biomass gasification, suggest greater sensitivity to operational factors, such as feedstock quality and process conditions.39 This variability may affect their predictability and economic viability, requiring more precise control and technology optimization.40 Hydrogen production techniques like microbial electrolysis cells, with a high efficiency and lower uncertainty, indicate more stable option considering energy efficiency.
Fig. 5 Specific energy of different fuels (kJ g−1).41 |
Authors | Scope of study | System boundary | Hydrogen production technology | Midpoint impact assessment |
---|---|---|---|---|
Global warming (GW), acidification (AC), eutrophication (EU), resource depletion (RD), land use (LU), water use (WU), ozone depletion (OD), human toxicity (HT), photochemical ozone formation (POF), cumulative energy demand (CED), coal gasification (CG), steam methane reforming (SMR), electrolysis via wind energy (W), biomass gasification (BG), photovoltaic electrolysis (PVE), autothermal reforming (ATR), thermal cracking (TC), high-temperature electrolysis (HTE), coal gasification with carbon capture (CG-CC), thermochemical water splitting (TC-WS), steam methane reforming with carbon capture (SMR-CC), electrolysis (E), photo fermentation (PF), dark fermentation (DF), chemical looping (CL), and pyrolysis (P). | ||||
Acar & Dincer31 | Environment, social, & economic | NA | CG, ATR, DF, PF, BG, TC, & E | GW & AC |
Sadeghi et al.42 | Environment | Gate-to-gate | SMR, CG, & TC | GW, AC, OD, EU, LU, & WU |
Salkuyeh et al.17 | Environment | Cradle-to-gate | E, BG, CG, & SMR | GW, HT, AC, POFP, & EU |
Burkhardt et al.43 | Economic, technical, environment, & thermodynamic | NA | CG, SMR, BG, PV-E, E, CG-CC, SMR-CC, TC, PVE, & PF | GW & AC |
Zhang et al.44 | Environment | Cradle-to-grave | E | GW & CED |
Chelvam et al.45 | Environment & economic | Cradle-to-gate | SMR & ATR | GW |
Ji and Wang46 | Environment | Cradle-to-gate | SMR, BG, BG-CC, ATR, & E | GW, AC, & CED |
Valente et al.47 | Environment & economic | NA | SMR, SMR-CC, CG, CG-CC, ATR, BG, & E, | GW & AC |
Aydin et al.48 | Environment & economic | NA | E, PF, & DF | GW & AC |
Dincer & Acar29 | Environment | Cradle-to-gate | E, PF, & DF | GW & AC |
Martin-Gamboa et al.49 | Environment | Cradle-to-gate | BG | GW, AC, OD, RD, & EU |
Susmozas et al.50 | Environment | Cradle-to-gate | BG | GW, AP, OD, & EU |
Mehmeti et al.51 | Environment | Cradle-to-gate | SMR, CG, BG, E & DF | GW, AC, OD, RD, & EU |
Hamedani et al.52 | Environment | Cradle-to-gate | BG | GW, AC, & EU |
Siddiqui & Dincer53 | Environment | Cradle-to-gate | E, BG & CG | GW |
Valente et al.9 | Environment | Cradle-to-gate | — | GW |
Palmer et al.54 | Environment | Gate-to-gate | PVE | GW |
Parkinson et al.10 | Environment & economic | Cradle-to-gate | PVE | GW |
Patel et al.55 | Environment | Gate-to-gate | SMR & SMR-CCS | GW |
Singh et al.56 | Environment | Gate-to-gate | SMR | GW |
Kerscher et al.57 | Environment | Gate-to-gate | SMR | GW |
Burchart et al.58 | Environment | Gate-to-gate | CG | GW |
Al-Qahtani et al.59 | Environment | Gate-to-gate | CG, CG, SMR, BG, & PVE | GW |
Suleman et al.41 | Environment | Gate-to-gate | CG, SMR, BG, PVE, & W | GW, AC, RD, & EU |
Ozturk & Dincer60 | Environment | Gate-to-gate | SMR | GW, AC, RD, & EU |
Cortés et al.61 | Environment | Gate-to-gate | SMR | GW, AC, RD, & EU |
Reaño62 | Environment | Gate-to-gate | CG, BG, E, & DF | GW, AC, RD, & EU |
Delpierre et al.63 | Environment | Gate-to-gate | E | GW |
Sadeghi and Ghandehariun64 | Environment | Gate-to-gate | PVE | GW, AC, AD, EU, & OD |
Mio et al.65 | Environment | Gate-to-gate | PEV, E, & SMR | GW, AC, AD, EU, FPMF, ME, WU, & OD |
Iyer et al.66 | Environment | Cradle-to-gate | PEV & W | GW |
Okeke et al.67 | Environment & economic | Cradle to gate | P, P-CCS | GW & AC |
Hren et al.68 | Environment | Gate-to-gate | SMR, BG, ATR, E, DF, & CL | GW, AC, EU |
Lin et al.69 | Environment | Gate-to-gate | P | GW |
Ganeshan et al.70 | Environment & economic | Gate-to-gate | PF, BG, & E | GW |
Batgi & Dincer71 | Environment | Gate-to-gate | SMR | GW, AD, OD, HT, & AC |
Wu et al.72 | Environment & economic | Gate-to-gate | BG | GW, OD, AC, & EU |
Zheng et al.73 | Environment | Gate-to-gate | BG, SMR, & E | GW |
Zang et al.74 | Environment & economic | Gate-to-gate | SMR, SMR-CCS, & ATR | GW |
Gu et al.75 | Environment | Gate-to-gate | PVE | GW |
Weidner et al.76 | Environment & economic | Cradle to gate | PEV, SMR, SMR-CCS, & W | GW |
Ajeeb et al.77 | Environment | Cradle to gate | E | GW, AC, AD, EU, FPMF, ME, WU, & OD |
A detailed comparative analysis of various hydrogen colors based on their environmental impacts was carried out, which includes global warming, acidification, eutrophication, and resource depletion, and their median values for each color of hydrogen are shown in Fig. 6. Moreover, the mean values and the standard error of these are given in Table 3. Coal gasification exhibits the highest environmental impact among the methods analyzed, with a mean global warming impact of 20.80 kg CO2 eq. per kg H2, acidification 29.44 kg SO2 eq. per kg H2, resource depletion 1.4 × 10−5 kg Sb eq. per kg H2, and the eutrophication is 0.04 kg PO43− eq. per kg H2 which is the second highest in the case of coal gasification. These high values indicate that coal gasification contributes significantly to degrade the environment. Steam methane reforming has a moderate environmental impact with a global warming impact of 9.43 kg CO2 eq. per kg H2, acidification 7.49 kg SO2 eq. per kg H2, and resource depletion 0.37 kg Sb eq. per kg H2. The eutrophication impact at 0.0037 kg PO43− eq. per kg H2 is quite low compared to the other colors of hydrogen. Biomass gasification (BG) and photovoltaic electrolysis (PVE) offer a balance between lower global warming and manageable acidification and resource depletion values. These methods provide moderate environmental impacts, making them more sustainable compared to fossil-based methods. High-temperature electrolysis (HTE) stands out with the lowest global warming impact of 1.25 kg CO2 eq. per kg H2; its acidification is also relatively low at of 3.88 kg SO2 eq. per kg H2. Coal gasification with carbon capture (CG-CC) and steam methane reforming with carbon capture (SMR-CC) show reduced global warming almost by half compared to their non-capture counterparts. However, these methods still present significant acidification and resource depletion. Electrolysis (E) has moderate global warming and acidification impacts but stands out with the highest eutrophication of 0.011 kg PO43− eq. per kg H2, indicating a significant impact on nutrient pollution. Photo fermentation (PF) and dark fermentation (DF) show relatively low environmental impacts. Electrolysis via wind energy (W) exhibits a low global warming impact of 1.1 kg CO2 eq. per kg H2 and acidification 2.98 kg SO2 eq. per kg H2, resource depletion 1.7 × 10−4 kg Sb eq. per kg H2, making it one of the most environmentally friendly methods.
Technologies | Global warming (kg CO2 eq. per kg H2) | Acidification (kg SO2 eq. per kg H2) | Eutrophication (kg PO43− eq. per kg H2) | Resource depletion (kg Sb eq. per kg H2) |
---|---|---|---|---|
Coal gasification (CG), steam methane reforming (SMR), biomass gasification (BG), photovoltaic electrolysis (PVE), high-temperature electrolysis (HTE), coal gasification with carbon capture (CG-CC), thermochemical water splitting (TC-WS), steam methane reforming with carbon capture (SMR-CC), electrolysis (E), photo fermentation (PF), dark fermentation (DF), and pyrolysis (P), and electrolysis via wind energy (W). | ||||
CG | 2.1 × 101 ± 1.9 × 100 | 2.9 × 101 ± 1.4 × 101 | 4.0 × 10−2 ± 1.6 × 10−2 | 1.4 × 10−5 ± 1.5 × 10−6 |
SMR | 9.4 × 100 ± 7.5 × 10−1 | 7.5 × 100 ± 2.1 × 100 | 3.7 × 10−3 ± 2.1 × 10−3 | 3.7 × 10−1 ± 3.1 × 10−1 |
BG | 3.9 × 100 ± 6.4 × 10−1 | 1.5 × 101 ± 5.1 × 100 | 3.8 × 10−3 ± 2.3 × 10−3 | 3.8 × 10−3 ± 0.0 × 100 |
PVE | 2.6 × 100 ± 3.2 × 10−1 | 6.1 × 100 ± 2.9 × 100 | 3.3 × 10−3 ± 2.0 × 10−3 | 1.8 × 10−3 ± 7.9 × 10−4 |
HTE | 1.3 × 100 ± 3.4 × 10−1 | 3.9 × 100 ± 4.1 × 10−1 | — | — |
CG-CC | 5.6 × 100 ± 2.3 × 100 | 1.3 × 101 ± 0.0 × 100 | — | — |
TC-WS | 4.0 × 100 ± 2.1 × 100 | 1.3 × 100 ± 6.7 × 10−1 | 2.0 × 10−2 ± 0.0 × 100 | — |
SMR-CC | 5.6 × 100 ± 7.5 × 10−1 | 1.2 × 10−2 ± 3.1 × 10−3 | 4.5 × 10−4 ± 1.4 × 10−4 | — |
E | 1.3 × 101 ± 3.4 × 100 | 1.9 × 101 ± 1.1 × 101 | 1.1 × 10−2 ± 3.6 × 10−3 | 3.2 × 10−3 ± 1.4 × 10−3 |
PF | 3.1 × 100 ± 9.2 × 10−1 | 2.1 × 100 ± 9.0 × 10−1 | — | — |
DF | 5.7 × 100 ± 1.9 × 100 | 5.8 × 10−1 ± 3.3 × 10−1 | 7.7 × 10−2 ± 7.1 × 10−2 | — |
W | 1.1 × 100 ± 1.5 × 10−1 | 3.0 × 100 ± 1.0 × 100 | 7.5 × 10−4 ± 6.5 × 10−4 | 1.7 × 10−4 ± 3.3 × 10−5 |
P | 5.1 × 100 ± 1.1 × 100 | 1.1 × 10−2 ± 1.6 × 10−3 | 1.2 × 10−5 ± 0.0 × 100 | — |
Environmental impacts are moderate to high particularly due to the highest freshwater eutrophication compared to the other technologies. Dark fermentation typically utilizes organic waste, agricultural residues, or biomass as substrates, which often contain elevated levels of phosphorus (such as phosphates). If not properly controlled, the resulting wastewater or byproducts can release these nutrients into freshwater systems, contributing to eutrophication. Additionally, dark fermentation generates volatile fatty acids (VFAs) as byproducts. Inadequate handling of effluents containing VFAs can further drive nutrient cycling in aquatic environments, intensifying the eutrophication process.
Electrolysis through the grid (Orange) and coal gasification with carbon capture (Blue) show moderate environmental impacts, with normalized scores around 0.35, suggesting that carbon capture can somewhat mitigate the burden associated with coal-based processes. Biomass gasification (Green) and thermochemical water splitting (Turquoise) are among the lower-impact methods, with scores of 0.18 and 0.15, respectively, reflecting their potential for more sustainable hydrogen production.
At the lower end of the impact spectrum are several advanced and renewable-based technologies. Methods such as photo-fermentation (Green), photovoltaic electrolysis (Green), steam methane reforming with carbon capture (Blue), high-temperature electrolysis (Turquoise), and pyrolysis (Turquoise) all exhibit normalized scores below 0.1, indicating relatively minimal environmental impact. Among these, wind power-based electrolysis (Green) emerges as the most environmentally friendly option, with the lowest burden of 0.03.
This ranking highlights a clear progression from high-impact, fossil fuel-based methods to more sustainable, low-impact renewable, and advanced thermal processes. The spectrum of environmental impacts reveals how methods like wind-powered electrolysis and biomass gasification can significantly reduce environmental harm in areas such as global warming, acidification, freshwater eutrophication, and resource depletion potential, paving the way for greener hydrogen production technologies.
Based on the normalized scores, different colors of hydrogen and techniques were ranked from high to low environmental impacts, as shown in Fig. 7. Brown hydrogen, produced via coal gasification, exhibits the highest environmental impacts among the hydrogen production methods under consideration. This process is characterized by significant contributions to global warming, acidification, and resource depletion. These high values indicate that coal gasification significantly exacerbates climate change, contributes to the formation of acid rain, and depletes non-renewable resources at a substantial rate, making it the least sustainable option for hydrogen production.
In contrast, hydrogen production through electrolysis using wind energy, often referred to as green hydrogen, has the lowest environmental impacts among the methods analyzed. This process involves splitting water into hydrogen and oxygen using electricity generated from wind turbines, a renewable energy source.
Bolz et al.78 identified five key barriers to adopting new technologies: regulation, technology, costs, availability, and acceptance. Jeje et al.79 discussed four key challenges in hydrogen production: technology, economy, regulation, and infrastructure. Technological hurdles include efficiency and scalability, while high costs limit economic feasibility. Inconsistent policies and underdeveloped infrastructure further hinder widespread adoption. Addressing these is vital for advancing hydrogen as an energy source.
In this prospect, hydrogen production technologies face challenges related to TRL, feedstock, and methods. Low TRL technologies like photocatalytic water splitting struggle with feasibility, efficiency, and high R&D costs. Addressing these issues requires more R&D funding, innovation, collaboration, and pilot projects. Medium TRL technologies like biolysis and PEM face barriers such as the need for technical optimization, high production costs, and lack of clear policies. Overcoming these challenges requires research to improve efficiency and reduce costs, along with supportive policies and public–private partnerships to foster adoption and innovation. High TRL technologies like alkaline electrolysis and gasification face challenges in infrastructure and scale. Despite being commercially viable, they require extensive infrastructure, such as pipelines and storage, and high capital costs, especially for renewable-powered electrolysis. Additionally, technologies like coal and natural gas gasification raise environmental concerns unless combined with carbon capture and storage (CCS). Addressing these issues requires major investments in infrastructure, renewable energy integration, and CCS to meet decarburization goals.
In summary, different feedstocks and production methods face unique challenges. For example, water-based technologies like alkaline electrolysis are efficient but have high energy demands.80 Biomass technologies, such as gasification, are viable but raise environmental concerns (land use change), competition with other commodities that use biomass as raw material, and a lack of biomass availability.81 Natural gas and hydrocarbon methods, like steam methane reforming, are efficient and cost-effective but rely on fossil fuels, leading to carbon emission issues.12
Several possible solutions can be implemented to address the challenges of hydrogen production methods. For water-based technologies like alkaline electrolysis, integrating renewable energy sources and improving system efficiency can reduce high energy demands. Biomass technologies, such as gasification, can benefit from sustainable sourcing practices, enhanced biomass availability, and carbon capture to mitigate environmental concerns. For natural gas and hydrocarbon methods like steam methane reforming, adopting low-carbon technologies, incorporating carbon capture and storage, and exploring green hydrogen alternatives can help reduce carbon emissions and reliance on fossil fuels.
Technology-specific impacts further illustrate these variations. For example, steam methane reforming (SMR) and biomass gasification (BG) both exhibit significant environmental effects, but in different ways. SMR is typically associated with higher GWP due to its dependence on fossil fuels, leading to greater greenhouse gas emissions. In contrast, BG's environmental impact fluctuates based on the type of biomass used and the processing methods applied, suggesting that BG can either mitigate or exacerbate environmental harm depending on these factors.
Studies with broader scopes, such as Acar & Dincer,31 provide a more comprehensive overview of hydrogen production pathways but may lack in-depth analysis of specific technologies. Conversely, more focused studies, such as Cetinkaya et al.,83 deliver detailed insights into particular technologies, offering a granular perspective on their environmental impacts, though they might overlook broader, system-level implications. Additionally, Nikolaidis & Poullikkas84 examine greenhouse gas emissions and the economic efficiency of hydrogen production technologies, further highlighting how both environmental and economic factors shape the sustainability of different hydrogen pathways. Overall, the wide variation in study findings emphasizes the need for standardized methods and transparent assumptions when comparing the environmental impacts of hydrogen production technologies.
Bhandari et al.16 conducted a life cycle assessment of hydrogen production via electrolysis. Their study found that the GWP for hydrogen production through biomass gasification is higher than that of steam methane reforming, contrary to the findings of most other studies, which typically indicate that GWP is greater for SMR than biomass gasification. Ji and Wang46 compared various hydrogen production methods and found that the acidification potential is higher for biomass gasification compared to coal gasification. Conversely, Valente et al.47 reported that coal gasification has a higher acidification potential than biomass gasification for hydrogen production. These differing findings highlight the variability in environmental impacts depending on the study and the specific conditions or assumptions used in each assessment.
Overall, these insights suggest that while current studies provide valuable information, there is no one-size-fits-all answer to the environmental impacts of hydrogen production methods. A nuanced approach that considers specific conditions, technologies, and contexts is essential for a comprehensive understanding.
A significant gap in the current understanding of hydrogen production's environmental impacts is the reliance on outdated or regionally specific data. This lack of transparency in energy mix assumptions, emission factors, and technological efficiencies often undermines the credibility of many studies. Future research should focus on creating open-source databases that provide transparent and up-to-date life cycle inventory (LCI) data. Such databases would improve the accuracy of environmental assessments, particularly if they incorporate region-specific variables, such as local energy mixes, regulatory frameworks, and resource availability. This would facilitate more precise global assessments of hydrogen production technologies.
Established technologies like steam methane reforming have been extensively studied, but emerging technologies, including electrolysis methods like anion exchange membrane, proton exchange membrane, and solid oxide electrolyzer, as well as advanced biomass gasification, lack comprehensive impact assessments. These technologies, particularly those still in development, need detailed assessments to understand their scalability and potential environmental impacts. Future research should focus on conducting targeted LCAs for emerging hydrogen technologies like microbial electrolysis cells, photo-fermentation, and thermochemical water-splitting cycles. Comparative studies are also essential to evaluate how these new technologies fare against traditional fossil fuel-based hydrogen pathways in terms of environmental sustainability.
While LCA studies on hydrogen production focus solely on environmental impacts, the social and economic aspects are often neglected. Job creation, resource availability, and geopolitical factors play a crucial role in the overall sustainability of hydrogen technologies. Future research should integrate social life cycle assessment and techno-economic analyses to evaluate trade-offs between environmental performance and socio-economic benefits. Case studies exploring the socio-economic impacts of hydrogen production in different regions, particularly in developing countries, would provide valuable insights into local impacts and opportunities.
Many studies do not consider how region-specific policies, regulatory incentives, and resource availability impact hydrogen production's environmental outcomes. These factors can greatly influence the overall viability of hydrogen technologies. Future research should focus on comparative studies that assess how regional policies, such as carbon taxes or renewable energy subsidies, affect both the environmental and economic performance of hydrogen production pathways. Moreover, it is crucial to explore hydrogen production in resource-constrained regions, such as water-scarce areas, and to assess the environmental trade-offs, including water usage and land degradation.
From a policy standpoint, implementing these environmentally friendly technologies requires robust support through government incentives, subsidies, or regulations that encourage investment in renewable technologies. For developing nations, international cooperation and funding might be necessary to build the infrastructure needed to adopt these advanced technologies. Green hydrogen produced from biomass presents a viable alternative for nations rich in biomass due to the renewable nature of the feedstock. It achieves nearly 50% efficiency, and its technology readiness level of 9 indicates that it is well-developed. This aligns with SDG 12 (responsible consumption and production) by promoting the efficient use of natural resources. Moreover, it could help to mitigate energy poverty as outlined in SDG 7, particularly in rural areas of developing countries.
Additionally, countries could consider blue hydrogen (with carbon capture and storage) and gray hydrogen (SMR) as alternatives. These methods, which utilize natural gas as a feedstock, offer a pragmatic step towards transitioning from fossil fuels to more sustainable energy sources. This approach could serve as an interim solution that supports SDG 9 (Industry, Innovation, and Infrastructure) by developing new technologies and infrastructure for hydrogen production. While these methods are neither significantly environmentally friendly nor particularly harmful, they do offer high-efficiency percentages and are technologically advanced, as given in Table 1. Policy-wise, blue and gray hydrogen production might require regulations that ensure the carbon capture and storage component effectively reduces CO2 emissions, thus contributing positively to SDG 13 (climate action). Additionally, creating a regulatory framework that supports fair and sustainable natural gas extraction practices could help achieve SDG 15 (life on land).
In summary, while the adoption of these hydrogen technologies poses certain challenges, they offer considerable opportunities to advance multiple SDGs. Effective policy frameworks, international cooperation, and technological readiness are crucial for their successful implementation and to ensure they contribute positively to global sustainability goals.
• Enhancing and expanding the use of carbon capture technologies for coal gasification and steam methane reforming can mitigate some of their environmental drawbacks, although a gradual phase-out of coal gasification is advised due to its high environmental impact.
• Supporting research and development in innovative hydrogen production methods, such as high-temperature electrolysis and thermochemical water splitting, is crucial for further reducing environmental impacts.
• Policymakers should implement subsidies, tax incentives, and financial support for green hydrogen projects, along with developing regulations and standards to limit environmental impacts.
• Increasing public awareness and engaging stakeholders are essential for garnering support and collaboratively transitioning to greener hydrogen production methods.
• It is also recommended to consider all significant impact categories while conducting life cycle assessments, as focusing solely on global warming can overlook other critical environmental impacts.
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