1 Introduction
2 Methods
2.1 Goal and scope definition
2.2 System description and lifecycle inventory
-
SS — foreground processes utilising a standard electricity mix, heating provided by a boiler using natural gas and system expansion applied
-
SG — foreground processes utilising a green electricity mix, heating provided by burning biomass and system expansion applied
-
ES — foreground processes utilising a standard electricity mix, heating provided by a boiler using natural gas and environmental impacts allocated to each coproduct on an economic basis
-
EG — foreground processes utilising a green electricity mix, heating provided by burning biomass and environmental impacts allocated to each coproduct on an economic basis
-
MS — foreground processes utilising a standard electricity mix, heating provided by a boiler using natural gas and environmental impacts allocated to each coproduct on a mass basis
-
MG — Foreground processes utilising a green electricity mix, heating provided by burning biomass and environmental impacts allocated to each coproduct on a mass basis
Quantity of input per kg packaging material produced | |||||
---|---|---|---|---|---|
Material/energy inputs | unit | System expansion (SS and SG) | Mass allocation (MS-PM and MG-PM) | Economic allocation (ES-PM and EG-PM) | Ecoinvent 3.6 process |
Seaweed cultivation | |||||
Ammonium nitrate | kg | 1.93E−04 | 1.51E−04 | 9.87E−06 | Market for nitrogen fertiliser, as N | nitrogen fertiliser, as N | cut off, U-GLO |
Sodium phosphate | kg | 7.77E−05 | 6.09E−05 | 3.98E−06 | Market for sodium phosphate | sodium phosphate | cut off, U-RER |
EDTA | kg | 4.25E−05 | 3.33E−05 | 2.17E−06 | Market for EDTA, ethylenediaminetetraacetic acid | EDTA, ethylenediaminetetraacetic acid | cut off, U-GLO |
FeCl3 | kg | 6.43E−06 | 5.03E−06 | 3.29E−07 | Market for iron (III) chloride, without water, in 40% solution state | iron (III) chloride, without water, in 40% solution state | cut off, U-GLO |
Chemical inorganics | kg | 6.38E−06 | 5.00E−06 | 3.27E−07 | Market for chemicals, inorganic | chemical, inorganic | cut off, U-GLO |
Anhydrous boric acid | kg | 3.72E−05 | 2.91E−05 | 1.90E−06 | Market for boric acid, anhydrous, powder | boric acid, anhydrous, powder | cut off, U-GLO |
Water | kg | 1.10E+01 | 8.64E+00 | 5.65E−01 | Tap water production, conventional treatment | tap water | cut off, U-Europe without Switzerland |
Diesel | kg | 6.12E−02 | 4.79E−02 | 3.13E−03 | Market for diesel | diesel | cut off, U-Europe without Switzerland |
Petrol | kg | 5.22E−02 | 4.09E−02 | 2.67E−03 | Market for petrol, unleaded | petrol, unleaded | cut off, U-RER |
Electricity | kWh | 8.19E−01 | 6.42E−01 | 4.20E−02 | a |
Mechanical pre-treatment | |||||
Electricity | kWh | 1.05E−01 | 8.19E−02 | 5.36E−03 | a |
Water extraction | |||||
Water | kg | 1.77E+01 | 1.38E+01 | 9.04E−01 | Tap water production, conventional treatment | tap water | cut off, U-Europe without Switzerland |
Electricity | kWh | 2.46E−01 | 1.93E−01 | 1.26E−02 | a |
Heating | MJ | 6.88E+00 | 5.38E+00 | 3.52E−01 | b |
Acid extraction | |||||
Hydrochloric acid | kg | 1.06E+00 | 8.75E−01 | 7.57E−02 | Market for hydrochloric acid, without water, in 30% solution state | hydrochloric acid, without water, in 30% solution state | cut off, U-RER |
Water | kg | 1.24E+01 | 1.02E+01 | 8.86E−01 | Tap water production, conventional treatment | tap water | cut off, U-Europe without Switzerland |
Electricity | kWh | 2.02E−01 | 1.67E−01 | 1.44E−02 | a |
Heating | MJ | 2.86E+00 | 2.36E+00 | 2.04E−01 | b |
Proteolysis | |||||
Water | kg | 9.24E+00 | 8.11E+00 | 8.12E+00 | Tap water production, conventional treatment | tap water | cut off, U-Europe without Switzerland |
Electricity | kWh | 1.58E−01 | 1.38E−01 | 1.38E−01 | a |
Heating | MJ | 2.29E+00 | 2.01E+00 | 2.01E+00 | b |
Packaging production | |||||
Sodium carbonate | kg | 8.72E−02 | 8.72E−02 | 8.72E−02 | Market for soda ash, dense | soda ash, dense | cut off, U-GLO |
Water | kg | 6.10E−01 | 6.10E−01 | 6.10E−01 | Tap water production, conventional treatment | tap water | cut off, U-Europe without Switzerland |
Electricity | kWh | 4.86E−02 | 4.86E−02 | 4.86E−02 | a |
Heating | MJ | 1.35E+01 | 1.35E+01 | 1.35E+01 | b |
Filtration | |||||
Water | kg | 2.99E+01 | - | - | Tap water production, conventional treatment | tap water | cut off, U-Europe without Switzerland |
Electricity | kWh | 2.95E−01 | - | - | a |
Drying 1 | |||||
Electricity | kWh | 4.42E−02 | - | - | a |
Heating | MJ | 6.29E+00 | - | - | b |
Drying 2 | |||||
Electricity | kWh | 4.42E−02 | - | - | a |
Heating | MJ | 2.28E+00 | - | - | b |
Drying 3 | |||||
Electricity | kWh | 4.42E−02 | - | - | a |
Heating | MJ | 3.40E+01 | - | - | b |
Wastewater treatment | |||||
Wastewater | m3 | 8.44E−02 | 6.61E−02 | 4.32E−03 | Treatment of wastewater from grass refinery, capacity 5e9l/year | wastewater from grass refinery | cut off, U-CH |
Substituted products | |||||
Soybean meal (protein) | kg | 3.02E−01 | N/A | N/A | Soybean meal to generic market for protein feed | protein feed, 100% crude | cut off, U-GLO |
Polylactic acid | kg | 1.00E−01 | N/A | N/A | Market for polylactide, granulate | polylactide, granulate | cut off, U-GLO |
Electricity source | Share (%) | Ecoinvent 3.6 process |
---|---|---|
Imports | ||
Imports: France | 2.6 | Electricity, high voltage, import from FR | electricity, high voltage | cut off, U-GB |
Imports: Netherlands | 1.2 | Electricity, high voltage, import from NL | electricity, high voltage | cut off, U-GB |
Imports: Ireland | 0.05 | Electricity, high voltage, import from IE | electricity, high voltage | cut off, U-GB |
Imports: Belgium | 1.4 | Market for electricity, high voltage | electricity, high voltage | cut off, U-BE |
Non-renewables | ||
Nuclear | 18.1 | Electricity production, nuclear, pressure water reactor | electricity, high voltage | cut off, U-GB |
Petroleum | 0.6 | Electricity production, oil | electricity, high voltage | cut off, U-GB |
Natural Gas | 34.2 | Electricity production, natural gas, combined cycle power plant | electricity, high voltage | cut off, U-GB |
Coal | 2.5 | Electricity production, hard coal | electricity, high voltage | cut off, U-GB |
Renewables | ||
Wind onshore | 6.5 | Electricity production, wind, <1MW turbine, onshore | electricity, high voltage | cut off, U-GB |
Wind offshore | 7.6 | Electricity production, wind, 1–3 MW turbine, offshore | electricity, high voltage | cut off, U-GB |
Solar photovoltaics | 2.5 | Electricity production, photovoltaic, 570kwp open ground installation, multi-Si | electricity, low voltage | cut off, U-GB |
Hydro-electricity | 1.3 | Electricity production, hydro, run-of-river | electricity, high voltage | cut off, U-GB |
Landfill + sewage gas | 3.3 | Heat and power co-generation, biogas, gas engine | electricity, high voltage | cut off, U-GB |
Biomass | 12.8 | Heat and power co-generation, wood chips, 6667 kw | electricity, high voltage | cut off, U-CH |
Municipal waste combustion | 5.5 | Electricity, from municipal waste incineration to generic market for electricity, medium voltage | electricity, medium voltage | cut off, U-GB |
Electricity source | Share (%) | Ecoinvent 3.6 process |
---|---|---|
Wind (onshore) | 14.6 | Electricity production, wind, < 1MW turbine, onshore | electricity, high voltage | cut off, U-GB |
Wind (offshore) | 81.6 | Electricity production, wind, 1–3 MW turbine, offshore | electricity, high voltage | cut off, U-GB |
Solar photovoltaics | 2.4 | Electricity production, photovoltaic, 570 kwp open ground installation, multi-Si | electricity, low voltage | cut off, U-GB |
Hydro-electricity | 1.4 | Electricity production, hydro, run-of-river | electricity, high voltage | cut off, U-GB |
2.2.1 Seaweed cultivation phase
2.2.2 Solid-stream bioprocessing phases
2.2.3 Liquid-stream bioprocessing phases
2.3 Description of coproduct management procedures
2.4 Lifecycle impact assessment
2.5 Key assumptions and limitations
-
This LCA study was commissioned at the early stages of product and product-system development — a juncture where the properties of the proposed seaweed biopolymer were little understood. In the absence of material characterisation data, a 1:1 equivalence was drawn between the proposed seaweed biopolymer and PLA which it is assumed to substitute out in the system expansion scenarios (SS & SG).
-
A decision was made to exclude inputs relating to the construction/maintenance/decommissioning of infrastructure (or ‘capital goods’) from the lifecycle inventory of the modelled foreground unit processes. Within the context of this study, examples of infrastructural inputs would be buildings containing the plantlet hatchery and biorefinery; machinery and tools used in the cultivation, maintenance and harvest of macroalgal biomass, as well as that in the biorefinery, and materials used to form the offshore cultivation apparatus. The focus was solely placed on the consumable product system inputs (i.e. chemicals/materials and energy), as environmental optimisations based on such inputs have been deemed more impactful and plausible than strategies involving improvements to infrastructural inputs, which typically have high investment requirements (Silva et al. 2018).
-
In the protein extraction phase, enzymes (proteases) are required to catalyse the hydrolysis of the algal peptide chains into activated peptide fragments (giving rise to their bioactive functionality). However, details regarding the type, quantity and life-span/recyclability of proteases used during this process were not specified. Moreover, enzymes are not immediately consumed in the chemical reaction and are largely recyclable, hence have been categorised as ‘infrastructure’ in this study, and omitted from the inventory data.
-
The final stage of the packaging material pathway comprises a belt-drying step resulting in the formation of alginate/cellulose (2:1) polymeric material. Details regarding ‘forming and moulding’ processes that typically follow polymeric resin production (i.e. thermoforming, calendaring, extrusion, injection moulding) were not specified, nor was there mention of the addition of plasticiser (an additive used to improve polymer flexibility). As such, the ‘gate’ portion of the system boundary was positioned after the production of cellulose: alginate resin.
-
As with all real-world manufacturing processes, mass losses throughout the seaweed biorefining process (e.g. via the adherence of product to machining equipment) would be inevitable. However, the mass balance on which this LCA model was based does not account for mass losses — due to the studied process largely being theoretical in nature. The final product yields were assumed equivalent to the content of fucoidan, laminarin, protein and carbohydrates (alginate and cellulose) in the feedstock biomass — unrealistically implying (1) a 100% coproduct yield and (2) 100% coproduct purity. It is likely that the real-life execution of the proposed scheme would result in actual coproduct yields, significantly different from the theoretical yield, ultimately influencing the allocation of environmental impacts between the coproducts.
-
This LCA model does not factor in biogenic exchanges associated with seaweed cultivation or the environmental impacts associated with land-use change.