Open Access Article
Fotini Drosoua,
Tryfon Kekes
*a,
Ricardo Uribe-Alvarezb,
Eoin Murphyb,
Mark Fenelonb,
Richard Lynchb and
Magdalini Krokidaa
aLaboratory of Process Analysis and Design, School of Chemical Engineering, National Technical University of Athens, Iroon Polytechneiou 9, 15780 Athens, Greece. E-mail: trykekes@central.ntua.gr; Tel: +(30)-2107723149
bFood Chemistry and Technology Department, Teagasc Food Research Centre, Moorepark, Fermoy, P61 C996, Co. Cork, Ireland
First published on 12th May 2026
The rising demand for healthy and sustainable food options has led to a growing interest in alternative plant-based beverages. The present study aimed to evaluate the environmental and economic impacts of a model nutritional beverage base composed of faba bean protein and maltodextrin, using Life Cycle Assessment (LCA) and Life Cycle Costing (LCC) methodologies. The study adopted a cradle-to-gate system boundary to analyse the entire production process, taking into consideration faba bean cultivation, protein isolate production, and beverage manufacturing. Faba beans are considered a promising sustainable ingredient due to their high protein content, in-field nitrogen-fixing ability and pollinator promotion potential. Across the production process, it was demonstrated that faba beans can provide a protein platform for the sustainable production of a nutritional beverage. Additionally, this study provided a holistic evaluation to guide the development of sustainable plant-based beverages, with findings underscoring the need for innovations such as alternative fractionation methods, energy-efficient processing technologies, and sustainable packaging to further enhance the environmental and economic profile of these beverages. The LCA results highlighted the energy-intensive nature of involved processes, such as decantation and spray-drying, and the utilization of conventional packaging materials as the primary contributor to climate impact, fossil depletion, and fine particulate matter formation, with the corresponding values being 0.229 kg CO2 eq., 0.078 kg oil eq., and 4.81 × 10−5 kg PM2.5 eq. per 330 mL of the model beverage, respectively. Owing to the crop's ability to naturally fix atmospheric nitrogen, fertiliser use during cultivation is minimal. The periodic requirement for phosphorus and possibly potassium led to the value rising up to 2.34 × 10−5 kg P eq. per 330 mL of the model beverage. Economically, protein isolate and beverage production dominated costs, mainly due to the energy and labor demands of involved processes, with cultivation contributing less. The total cost associated with producing 330 mL of the two-component beverage is approximately € 0.46. Collectively, this study provides a holistic evaluation to guide the development of sustainable plant-based beverages, highlighting the environmental and economic advantages of faba beans for the development of functional food products.
Sustainability spotlightAdvancing sustainable nutrition necessitates food systems that minimize environmental burdens while simultaneously supporting economic feasibility and viability. The present work demonstrates that faba beans, due to their nitrogen-fixing capacity, low-input cultivation requirements, and high protein content, offer a promising foundation for climate-conscious beverage production. Through integrated LCA and LCC analyses, energy-intensive steps, like decantation and drying, were identified as key hotspots and highlighted opportunities for improvement through alternative fractionation, energy-efficient processing, and sustainable packaging. By optimising these stages, faba bean-based beverages can achieve lower carbon footprints and reduced resource use while remaining cost-competitive. This research aligns strongly with the UN SDGs on responsible consumption and production (SDG 12), climate action (SDG 13), and industry, innovation, and infrastructure (SDG 9). |
The utilisation of legumes as an alternative source of protein in the human diet is considered an appealing pathway towards the development of sustainable food products with high nutritional value.11,12 Faba beans are a well-known legume species with strong nutritional and agronomic attributes, offering promising potential for developing novel plant-based food products, including beverages.13,14 Faba beans (Vicia faba) can serve as a versatile ingredient to meet rising global nutritional demands due to their high protein content, dietary fibers, and essential micronutrients.15 Furthermore, faba beans are nitrogen-fixing crops, thereby enhancing soil fertility and reducing the use of synthetic fertilisers.16 The aforementioned attributes position faba beans as an ideal candidate for sustainable food innovations, including production of plant-based beverages that can address health and environmental concerns. However, in parallel with the importance of product design and development it is equally important to evaluate the environmental sustainability and economic viability of such products to highlight their potential as novel ingredients in beverage manufacturing.
Life Cycle Assessment (LCA) is a valuable framework used for evaluating the environmental impacts of product systems by considering all relevant aspects throughout their life cycle, including inputs, outputs, and potential environmental impacts.17 The primary goal of LCA is to pinpoint significant environmental hotspots at different stages during the production phases and provide insightful recommendations that can improve the environmental sustainability of the product system.18 Similarly, Life Cycle Costing (LCC) is an essential framework that assesses the total economic costs attributed to a product system throughout its entire life cycle by considering all relevant cost flows, including investment, operation and end-of-life expenditures.19 LCC analysis is vital in identifying critical cost hotspots across different stages while proposing strategies/mitigation measures to optimise overall economic performance and guide stakeholders on sustainable decision-making.20
The primary goal of the present work was to evaluate the environmental and economic footprint of a plant-based model beverage, utilising faba bean protein isolate as a base nutritional component, through LCA and LCC analyses. An assessment of the production processes in terms of environmental and economic sustainability aims to determine the feasibility of producing the faba bean-based beverage. Generally, faba beans are not widely used for commercial beverage production; therefore, the studied beverage model can be considered an innovative alternative rather than a direct substitute for soy or other plant-based nutritional drinks. Consequently, it cannot be directly compared, in terms of environmental and economic performance, with other conventional products that already exist in the market. The novelty of this work lies in its holistic approach throughout the different stages of the production chain, combining environmental and economic assessments to guide the development of innovative and sustainable food solutions, and in the evaluation of a novel faba bean-based beverage.
LCC analysis was performed using Microsoft Excel (v15.0) and involved identifying all relevant economic flows. For the present work, only operating expenditures (OPEX) were considered, and capital expenditures (CAPEX) were excluded. CAPEX was not considered, since the production of the model faba-bean protein-based beverage can be completed using equipment and process lines that are considered conventional within the food and beverage sector.
| Process | Flow | In/out | Value | Unit |
|---|---|---|---|---|
| Cultivation | Diesel | In | 78 | L |
| Fungicides | In | 3 | L | |
| Herbicides | In | 9 | L | |
| Insecticides | In | 0.05 | L | |
| Potassium fertilizer | In | 60 | kg | |
| Phosphorus fertilizer | In | 40 | kg | |
| Cultivation area | In | 1 | ha | |
| Faba beans | Out | 5500 | kg |
| Flow | Unit | Value | €/unit | Cost (€) | |
|---|---|---|---|---|---|
| Utilities | Diesel | L | 78 | 1.63 | 127.14 |
| Chemical agents | Fungicides | L | 3 | 13 | 39 |
| Herbicides | L | 9 | 15 | 135 | |
| Insecticides | L | 0.05 | 12 | 0.6 | |
| Fertilisers | P fertiliser | kg | 40 | 1.4 | 56 |
| K fertilizer | kg | 60 | 0.9 | 54 | |
| Labor | Working hours | Hours | 21 | 15.86 | 333.06 |
| Output | Faba beans | kg | 5500 | Total | 741.8 |
| Process | Flow | In/out | Value | Unit |
|---|---|---|---|---|
| a Data from industry expert consultation.b Derived from fundamental theoretical calculation.c Data from pilot scale operation. | ||||
| Cleaninga | Faba beans (wet/dirty) | In | 1181.25 | kg |
| Electricity | In | 3.6 | MJ | |
| Clean faba beans | Out | 1125 | kg | |
| Foreign material | Out | 56.25 | kg | |
| Dryingb | Clean faba beans | In | 1125 | kg |
| Electricity | In | 608 | MJ | |
| Faba beans | Out | 1000 | kg | |
| Water vapor | Out | 125 | kg | |
| Dehullingc | Faba beans | In | 1000 | kg |
| Electricity | In | 18.45 | MJ | |
| Dehulled faba beans | Out | 800 | kg | |
| Faba bean hulls | Out | 200 | kg | |
| Dry millingc | Dehulled faba beans | In | 800 | kg |
| Electricity | In | 46.7 | MJ | |
| Faba flour | Out | 800 | kg | |
| Alkaline solubilizationc | Faba flour | In | 800 | kg |
| Sodium hydroxide (10%) | In | 43.2 | kg | |
| Water | In | 7200 | kg | |
| Protein solution | Out | 8043.2 | kg | |
| Decantation #1a | Protein solution | In | 8043.2 | kg |
| Electricity | In | 198.5 | MJ | |
| Dried cake | Out | 396.27 | kg | |
| Protein solution | Out | 7567.36 | kg | |
| Protein precipitationc | Protein solution | In | 7567.36 | kg |
| Hydrochloric acid (10%) | In | 105.98 | kg | |
| Protein solution | Out | 7673.34 | kg | |
| Decantation #2a | Protein solution | In | 7673.34 | kg |
| Electricity | In | 275.4 | MJ | |
| Acidified water | Out | 6759.71 | kg | |
| Protein cake | Out | 913.63 | kg | |
| Washing & neutralizationc | Protein cake | In | 913.63 | kg |
| Sodium hydroxide (10%) | In | 9.37 | kg | |
| Deionised water | In | 455.25 | kg | |
| Protein solution | Out | 1378.25 | kg | |
| Spray dryinga,b | Protein solution | In | 1378.25 | kg |
| Electricity | In | 167.2 | MJ | |
| Thermal energy from natural gas | In | 4820.57 | MJ | |
| Faba protein isolate | Out | 173.11 | kg | |
| Water vapor | Out | 1205.14 | kg | |
| Flow | Unit | Value | €/unit | Cost (€) | |
|---|---|---|---|---|---|
| Utilities | Electricity | MJ | 1317.85 | 0.1121 | 147.73 |
| Natural gas | MJ | 4820.57 | 0.04 | 192.82 | |
| Water | Process water | kg | 7200 | 0.00185 | 13.32 |
| Deionised water | kg | 455.25 | 1 | 455.25 | |
| Auxiliary materials | Sodium hydroxide | kg | 52.57 | 0.4 | 21.03 |
| Hydrochloric acid | kg | 105.98 | 2.5 | 264.95 | |
| Labor | Working hours | Hours | 16 | 16.46 | 263.36 |
| Wastewater | Acidified water | kg | 6759.71 | 0.00182 | 12.3 |
| Solid wastes | Hulls | kg | 200 | 0.105 | 21 |
| Foreign material | kg | 56.25 | 0.105 | 5.91 | |
| Dried cake | kg | 396.27 | 0.105 | 41.61 | |
| Output | Faba bean protein isolate | kg | 173.11 | Total | 1439.28 |
| Process | Flow | In/out | Value | Unit |
|---|---|---|---|---|
| a Data from pilot scale operations.b Derived from fundamental theoretical calculation.c Data from industrial scale operations. | ||||
| Mixinga | Faba bean protein isolate | In | 60 | kg |
| Maltodextrin | In | 50 | kg | |
| Water | In | 890 | kg | |
| Electricity | In | 9.5 | MJ | |
| Beverage | Out | 1000 | kg | |
| Preheatingb | Beverage | In | 1000 | kg |
| Natural gas | In | 6 | Nm3 | |
| Steam | In | 311.35 | kg | |
| Beverage | Out | 1000 | kg | |
| Final heatingb | Beverage | In | 1000 | kg |
| Natural gas | In | 10.1 | Nm3 | |
| Steam | In | 134.56 | kg | |
| Beverage | Out | 1000 | kg | |
| Homogenisationb | Beverage | In | 1000 | kg |
| Electricity | In | 43.2 | MJ | |
| Beverage | Out | 1000 | kg | |
| Coolingb | Beverage | In | 1000 | kg |
| Electricity | In | 116 | MJ | |
| Beverage | Out | 1000 | kg | |
| Filling & packagingc | Beverage | In | 1000 | kg |
| Electricity | In | 19 | MJ | |
| PET bottles | In | 46.97 | kg | |
| Beverage | Out | 1000 | kg | |
| Flow | Unit | Value | €/unit | Cost (€) | |
|---|---|---|---|---|---|
| Utilities | Electricity | MJ | 187.7 | 0.1121 | 21.04 |
| Natural gas | Nm3 | 16.1 | 1.725 | 27.77 | |
| Steam | kg | 445.91 | 0.42 | 187.28 | |
| Water | Process water | kg | 890 | 0.00185 | 1.65 |
| Auxiliary materials | Maltodextrin | kg | 50 | 4.25 | 212.5 |
| PET bottle | kg | 46.97 | 1.19 | 55.89 | |
| Labor | Working hours | Hours | 16 | 16.46 | 263.36 |
| Output | Beverage | kg | 1000 | Total | 769.49 |
According to the LCA results, the use of energy-intensive processes during faba bean protein isolate manufacture and beverage production is the primary contributor to the environmental impact. Among the production stages, the filling and packaging, decantation and spray-drying processes are identified as the most impactful, contributing to climate change, fossil depletion, and fine particulate matter formation (0.229 kg CO2 eq., 0.077 kg oil eq., and 4.81 × 10−5 kg PM2.5 eq. per 330 mL of the beverage, respectively). This is attributed to the energy use and packaging materials of the filling and packaging, along with the energy use of spray-drying and decantation processes and the use of sodium hydroxide during alkaline solubilization.26–28 However, freshwater consumption (8.45 × 10−4 m3 per 330 mL of the beverage) is relatively unaffected by cultivation since faba beans are not irrigated. However, the use of fertilisers during cultivation has the potential to contribute to eutrophication risk (2.34 × 10−5 kg P eq. per 330 mL of the beverage), in circumstances where crop management does not mitigate nutrient runoff potential.29 Finally, dehulling and the first decantation process contribute to metal depletion (2.12 × 10−4 kg oil eq. per 330 mL of the beverage) due to the electricity consumption and the generation of solid wastes, respectively.26,30 The difference in the performance of the two decantation processes in some environmental metrics, such as freshwater consumption and climate change, is attributed to the different output streams subsequently processed in the process line. Specifically, during the first decantation the dried cake is considered as a side-stream that is disposed, while the protein solution is undergoing further treatment. However, in the second decantation process the acidified water is treated in a municipal wastewater treatment plant, thus it is treated and can return to the aquatic environment,31 while the protein cake is further treated to obtain the protein isolate.
Faba bean-based beverages are not well-established in the marketplace, so the results of the present work cannot be directly compared with other studies. However, it is insightful to compare them with other plant-based drinks. According to published articles, the carbon footprint of almond, soy and oat beverages is 0.154, 0.175, and 0.099 kg CO2 eq. per 330 mL of the product, respectively.32–34, compared to the faba bean result of 0.229 kg CO2 eq. However, it is worth noting that, in the aforementioned studies, the drink was produced using slightly processed crops (i.e. dehulled or washed crops), and not a protein isolate, therefore, the environmental footprint is lower compared to the present study. However, the utilisation of protein isolate can increase protein concentration, improve solubility, reduce off-flavors, and minimise anti-nutritional factors, providing a smoother and more appealing final product.35,36
A detailed breakdown of each beverage production component contribution in the studied midpoints is depicted in Fig. 3.
The LCA results highlight the distinct contributions of cultivation, ingredient production, and beverage production across the various environmental categories studied. The third component of the production chain, namely the beverage production emerges as the dominant contributor to most impact categories, including fine particulate matter formation (46%), fossil depletion (68%), and freshwater consumption (79%) due to the energy consumption of heating and filling & packaging processes, along with the inclusion of packaging materials and the use of water as the basis for the beverage production. In contrast, cultivation as with standard cropping systems presents a risk of freshwater eutrophication in the absence of crop mitigation measures due to fertiliser use but has minimal influence on freshwater consumption (4%), as faba beans in the studied product system are not irrigated. However, in other pedoclimatic regions with limited rainfall, faba beans may need irrigation, and thus, freshwater consumption will differ. However, ingredient production is the primary contributor to climate change (54%) and metal depletion (74%) due to the inclusion of energy-intensive processes such as decantation and spray-drying. In particular, for the fine particulate matter formation, faba cultivation exhibits a significant role, which is attributed to the utilization of diesel in agricultural machinery, required for cultivation practices.37 It is worth noting that, regarding freshwater consumption in which beverage production predominantly contributes, it is attributed to the use of water that is necessary for the production of the beverage, while the vast majority of water utilized during the ingredient production is treated in wastewater plants and returned to the aquatic environment. This breakdown highlights the importance of targeted improvements in energy efficiency during protein isolate and beverage production, as well as the utilisation of soils with high P and K indices, resulting from optimal pH and effective system management.
The endpoint analysis of the LCA offers a comprehensive perspective on the environmental impacts of beverage production, focusing on three key areas: human health, ecosystems, and resource availability.38 Fig. 4 illustrates the aggregated effects of the different production components across these categories, highlighting their broader environmental implications.
The results of the ReCiPe endpoints indicate that the ingredient production exhibits the highest contribution regarding the impact on ecosystems and resource availability, while beverage production is the highest contributor to the impact on human health. Specifically, beverage production accounts for the largest share in the impact on human health (5.91 × 10−7 DALY), while ingredient production plays a secondary role. In contrast, faba protein isolate production exhibits the highest impact on ecosystems, compared to the cultivation and beverage production phases, with the total value rising up to 1.91 × 10−8 species per year. This can be attributed to the substantial quantities of resources used to produce the protein isolate. Finally, regarding resource availability, ingredient production is driven by its reliance on energy-intensive inputs, with a total value of 2.433 × 10−2 $. Cultivation has a minimal impact in all categories, reflecting its comparatively low resource demands.
The beverage cost analysis provides a comprehensive breakdown of the financial contributions from various production stages, offering valuable insight into where resources are allocated. According to the obtained results, 0.46 € are required to produce 330 mL of the beverage, considering all operating expenditures across the three different compounds of the production chain. Beverage production is the dominant contributor to the total production cost, with 0.24 €. This is largely due to the energy demands associated with heating and the utilization of conventional packaging materials in the packaging & filling of the final product, which constitutes a key factor especially as consumer demand for premium packaging and efficient delivery systems increases. Protein isolate production ranks as the second largest contributor, a production component that encompasses various activities requiring significant quantities of energy, labour, and materials. While less costly than beverage production, ingredient production (0.16 €) remains a key factor. Maintenance and other costs represent the third largest contributor to the overall production cost (0.021 € each). These include expenses associated with equipment upkeep, repairs, operational overheads and any other relevant cost flow. Finally, cultivation contributes the least to the total cost with the total costs for producing the necessary quantities of faba bean for 1 beverage rising to 0.018 €. This indicates efficient agricultural practices or the use of low-cost, non-irrigated crops that require minimal input, such as fertilisers or water. While cultivation costs are minimal, they remain an important foundation for the supply chain, as the quality of raw ingredients directly affects the attributes of the final product. A detailed breakdown of the ingredient and beverage component cost flows is depicted in Fig. 6. The corresponding results for the cultivation component are not presented, since the costs associated with this phase are lower compared to those of the other components and do not influence the economic footprint of the final product.
![]() | ||
| Fig. 6 Cost flow breakdown for (a) faba bean protein isolate production and (b) beverage production. | ||
The cost breakdown analysis highlights the varying contributions of ingredient production and beverage production to the overall cost structure. Ingredient production shows a predominance of water associated costs, representing 32% of the total cost, with deionizing water playing a major role. Utility costs account for 24%, while auxiliary materials and labor contribute 20% and 18%, respectively, with minimal costs being allocated to wastewater and solid wastes. Finally, regarding beverage production cost breakdown, auxiliary materials, labor and utilities contribute significantly to the cost structure, with 35%, 34%, and 31% contributions, respectively. In contrast, costs associated with water can be characterized as negligible.
One of the main challenges in producing protein isolates utilising the conventional wet fractionation process is the environmental and economic footprint associated with consecutive decantation steps and spray drying. Decantation is widely used to separate solid and liquid phases following extraction or solubilization, but the process often requires continuous rotational forces and high shear operation to achieve sufficient clarity and yield. These demands result in elevated energy consumption, increased equipment wear, and greater operational costs, particularly when large volumes of dilute suspensions must be processed.39 Meanwhile, spray drying is an energy-intensive process contributing significantly to production costs and environmental impact.34 Evaporation is widely used for many feedstocks prior to spray drying to reduce the volume of the material subjected to subsequent drying, thereby saving energy.40,41 The viscosity of the feed material determines the extent to which a liquid feed can be concentrated. Therefore, the type, quantity, and functionality of protein directly affect process efficiency by determining how much water can be removed before spray drying. Additionally, dry fractionation methods could replace, in the case of protein concentrates, wet processes entirely, eliminating the need for consecutive decantation steps and spray drying; however, it must be noted that these methods cannot be used to obtain protein isolates.42,43 This approach can potentially reduce energy consumption and align with sustainability goals by lowering greenhouse gas emissions and the overall environmental footprint.44
Optimising energy use during thermal treatment presents an important opportunity in beverage production. Innovations such as microwave or ohmic heating offer potential for more energy-efficient processing at small scales. However, their use in large-scale production can be constrained by low throughput. Packaging also presents a significant opportunity for improvement. The transition from conventional polymer-based packaging materials to biodegradable or lightweight materials could reduce the environmental impact and lower costs, ensuring both sustainability and economic viability.45
Additionally, excluding labor-associated costs, utilities, particularly energy, remain a significant cost contributor throughout the beverage production chain. Reducing energy consumption would therefore directly reduce production costs. This can be achieved through energy recovery systems and improved process efficiencies. Furthermore, investing in a renewable energy infrastructure, such as solar panels or biomass energy systems, could offset reliance on conventional electricity sources. Although such investments involve high capital expenditures (CAPEX), they promise long-term economic and environmental benefits.46,47
Generally, adopting novel technologies is vital to reduce the overall environmental footprint. However, these technologies must be carefully evaluated through a life-cycle cost (LCC) analysis to account for initial CAPEX alongside potential operational savings and sustainability benefits. For instance, advanced filtration systems or renewable energy equipment may initially require substantial investment but could significantly reduce utility costs and greenhouse gas emissions in the long term. By balancing economic considerations with environmental priorities, the production process can be optimised to meet market and sustainability demands.
Life cycle costing revealed that beverage production constitutes the highest cost component, driven primarily by labour and utilities associated with heating and packaging. Protein isolate production is the second most costly stage, reflecting the resource-intensive nature of wet fractionation, multiple decantation steps, and spray drying. Although cultivation costs are comparatively low, they remain essential to overall supply-chain performance. The cost structure indicates that reducing energy use and enhancing process efficiencies could significantly improve economic feasibility.
Based on the LCA and LCC results, faba beans can be characterised as a sustainable ingredient that can be used for producing novel plant-based beverages; however, the environmental and economic performance of these products can be significantly improved. Future innovations and process optimisation present promising pathways for enhancing sustainability and reducing costs. Transitioning to renewable energy sources, adopting energy-efficient technologies, and exploring alternatives to spray drying, such as substituting wet with dry fractionation, could address the current challenges. Moreover, integrating biodegradable or lightweight packaging options can further reduce environmental impacts. While these changes require initial capital investment, which can increase to significant monetary values in some circumstances, the long-term benefits align with sustainability goals and market demands for eco-friendly health-conscious products. Overall, this comprehensive approach positions faba bean-based beverages as a viable solution for a sustainable food system.
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