Next Article in Journal
Floristic Analysis of Vascular Plants in the Ziwuling Mountains, Shaanxi Province
Next Article in Special Issue
Synergistic Impacts of Phosphorus Deficiency Coupled with Thermal and High-Light Stress on Physiological Profiles of Cultivated Saccharina japonica
Previous Article in Journal
Integrated Nematode Management Strategies: Optimization of Combined Nematicidal and Multi-Functional Inputs
Previous Article in Special Issue
Allelopathic Interactions Between the Green-Tide-Forming Ulva prolifera and the Golden-Tide-Forming Sargassum horneri Under Controlled Laboratory Conditions
 
 
Font Type:
Arial Georgia Verdana
Font Size:
Aa Aa Aa
Line Spacing:
Column Width:
Background:
Article

Renewable Energy from Beach-Cast Seaweed: Calorific Power Heating Studies with Macroalgae

by
Fernando Pinto Coelho
1,2,3,*,
Everardo Valadares de Sá Barreto Sampaio
1,
Márcio Gomes Barboza
4,
Elica Amara Cecília Guedes-Coelho
5,
Manoel Messias da Silva Costa
6,
Emerson Carlos Soares da Silva
7,
Victor Andrei Rodrigues Carneiro
8,
Bruno Moreira Soares
9,
Elvis Joacir de França
10,
Rômulo Simões Cezar Menezes
1 and
Cesar Augusto Moraes de Abreu
1
1
Postgraduate Program in Energy and Nuclear Technologies, Federal University of Pernambuco (UFPE/PROTEN), National Nuclear Energy Commission, Recife 50740-540, Brazil
2
Research Nucleus in Energy Production, National Council for Scientific Research CNPQ, Brasília 70070-010, Brazil
3
Surveying and Cartography Engineering Course, Center of Engineering and Agricultural Sciences, Federal University of Alagoas, Campus—(CECA), Rio Largo 57072-016, Brazil
4
Civil Engineering Technology Centre, Federal University of Alagoas, Campus A. C. Simões, Maceió 57000-000, Brazil
5
Institute of Biological and Health Sciences (ICBS), Federal University of Alagoas, Campus A. C. Simões, Maceió 57000-000, Brazil
6
Federal Institute of Alagoas/IFAL, Brazilian Regional University (UNIRB), Maceió 57035-660, Brazil
7
Aquaculture and Aquatic Ecology, Laboratory of Center of Engineering and Agricultural Science, Federal University of Alagoas, Campus—(CECA), Rio Largo 57072-016, Brazil
8
Institute of Biological Sciences, University of Sao Paulo, São Paulo 05508-220, Brazil
9
Institute of Science, Technology and Innovation—Proalga Brazil—ICTI, São Paulo 01109-060, Brazil
10
Northeast Regional Centre for Nuclear Sciences, Recife 50740-545, Brazil
*
Author to whom correspondence should be addressed.
Plants 2025, 14(7), 1005; https://doi.org/10.3390/plants14071005
Submission received: 21 January 2025 / Revised: 20 February 2025 / Accepted: 25 February 2025 / Published: 23 March 2025
(This article belongs to the Special Issue Marine Macrophytes Responses to Global Change)

Abstract

:
Some stretches of the Brazilian coast are regularly subject to a natural process of macroalgae deposition. In urban beach areas, public institutions responsible for cleaning collect this biomass and dispose of it in landfills. When this biomass is exposed to the sun for a long time in the littoral area, a decomposition process begins and causes greenhouse gas emission into the atmosphere. Macroalgae biomass is a natural resource that could be used for renewable energy, contributing to meeting the growing demand for low environmental impacts of energy, indicating the possibility of participating in sustainable development. The objective of this research was to evaluate the energetic potential of macroalgae biomass deposited on the Maceió coast; specifically, the combustion capacity of aggregate biomass and pellet biofuel produced with macroalgae. The research, which analysed 13 species, proceeded using a calorimetric pump methodology to determine the power heating value and a mass spectrophotometer to determine the available energetic chemical elements. The result of 8.82 MJ/Kg was similar to the main biomass used in Brazil, the sugarcane bagasse, evaluated at 8.91 MJ/Kg. Aggregated macroalgae biomass in condensed pellets with energetic composites obtained a value of 4823 Kcal/Kg, 1.2% more than the average of terrestrial biomass pellets. Therefore, these results show possibilities to produce biofuel using thermal energy from marine macroalgae biomass.

1. Introduction

The macroalgae market is centred on the production, processing, and distribution of macroalgae, which is more commonly referred to as seaweed. This industry exerts a multifaceted influence on various sectors, including food and beverages, pharmaceuticals, cosmetics, and biofuels. The growing recognition of macroalgae as a nutritious food is due to their high content of vitamins, minerals, and antioxidants. This heightened awareness has led to a surge in their incorporation into health foods and dietary supplements, aligning with the preferences of health-conscious consumers [1].
The industrial production systems associated with energy production actively use natural resources and act as consumers of the main raw materials found in nature. These intensified practices claim concerns about environmental defence preservation, life protection and sustainable development [2,3,4,5]. Energy consumption has increased by 65% in the last 30 years and will increase by another 40% by 2030, with investments reaching $600 billion per year [2]. The investment in renewable energy exceeded USD 600 billion per year in 2020 [6,7,8]. Renewable energies offer a viable alternative for the future provision of energy, with a view to the enhancement of biofuel production and the improvement of quality of life for citizens, who will no longer be subject to the constraints imposed by their reliance on fossil fuels. [4]. The algae are thallophyte plants lacking roots, stems, and leaves, with chlorophyll “a” as their primary photosynthetic pigment and they need a sterile covering of cells around the reproduction system [9]. The marine ecosystem is composed of phytobenthic macroalgae [10,11,12], and some species may present an oleaginous concentration composed of fatty acids, with the potential to generate heat in thermoelectric and biofuel industries [13,14,15]. Marine macroalgae biomass is renewable in continental ocean ecosystems and can be an important raw material for new biofuel energy generation. The efficient enhanced growth photosynthesis, which is four times higher than terrestrial plants, became an important factor concerning sustainability [16,17,18,19]. The beach-cast seaweed enables a free daily biomass deposition in various littoral parts of the world; it is the only kind of biomass collected every day and the raw material can be used for energy production, dispensing with irrigation use, pesticides, fertilizers and agricultural inputs. The findings of this study contribute to the existing body of knowledge concerning the utilization of residual biomass for energy generation purposes. In Maceió, the municipal collection service employs a daily removal process that utilizes three specialized buckets with a capacity of six tons of macroalgae aggregated biomass with residual sand. This amount has been invariably discarded in the sanitary landfill and characterized as unusable. The use of macroalgae biomass opens up possibilities for the production of biofuels with new technologies and emphasizes the creation of another sustainable alternative to help overcome the current global energy crisis and reduce its environmental problems. In the research, the combustion capacity of aggregated biomass and pellets was evaluated in relation to the calorific value obtained. It is important to highlight this research in Brazil as the first that produced seaweed pellets with a focus on the energy potential of biomass.

2. Results and Discussion

2.1. The Thermal Capacity of Macroalgae from HCV and LCV

Some species in this research presented higher calorific value (HCV) than others, ranging from 6.3–12.0 MJ/Kg, and lower calorific value (LCV) 5.9–10.8 MJ/Kg—(Table 1), which these values are under than most terrestrial biomasses in according [17,20]. The lower calorific value—8.82 MJ/Kg, (Table 1), was similar to the main biomass used in Brazil, sugarcane bagasse, evaluated at 8.91 MJ/Kg [21]. This result configures an economic possibility to use this marine biomass. Among the factors that could explain the inferior position of HCV of macroalgae in relation to terrestrial biomass, we can mention nearing absence of lignin, high humidity and less concentrations of carbon and hydrogen than terrestrial biomass [22,23]. (Table 2). A selective formulation composed of 25% Sargassum sp., 35% Cryptonemia crenulata, 10% Gracilaria sp., 30% Sargassum vulgare, presented an estimated higher calorific value of 11.29 MJ/Kg, about 11.2% higher than aggregated biomass formulated with all macroalgae species—10.09 MJ/Kg (Table 2), meaning the possibility for selective collection of species with better yield and greater energy potential. According [24], the phylum Chlorophyta and Ochrophyta have higher calorific values, respectively, 8–13 MJ/Kg–9–11 MJ/Kg, indeed, the average found in the present research in both phyla are 8.67MJ/Kg and 10.19 MJ/Kg, which are almost similar range cited in the literature (Table 1). The species of phylum Rhodophyta reached the highest calorific value, 11.4–12.0 MJ/Kg (Table 1). For [25,26], the HCV values of macroalgae are in the range of 11–12 MJ/Kg, lower than those of terrestrial biomasses, which are situated in the range of 17–18 MJ/Kg. Research by [27,28] with macroalgae provided HCV of 17.6 MJ/Kg and 21.7 MJ/Kg, respectively. Along the same high calorific levels, but with other species and from different methods, through performed pyrolysis with macroalgae Laminaria japonica, Fucus serratus and Prophyra tenera at 500 °C, have reached results of 33.57 MJ/Kg; 32.46 MJ/Kg and 29.74 MJ/Kg, respectively [29]. These results are superior to those many terrestrial biomasses. Thus, indications of macroalgae biodiversity configure different chemical compositions in their elements, some aspects of seasonality, environment, regionality and differentiated genetic evolution than terrestrial plants, may, in certain cases, show higher potential energy when compared of terrestrial biomass [29,30,31,32].

2.1.1. Chemical Combustion Elements for Energy Production—Analysis of C, H, N, P, K, O

Research by [33,34], indicated that raw materials with a high content of carbon and hydrogen have a high calorific value, while the presence of oxygen has the opposite effect. The species Ulva lactuca and Hypnea pseudomusciformis contain high levels of carbon mass—50.08% and 61.87% with HCV levels as 11.43 MJ/Kg and 8.73 MJ/Kg respectively, (Table 1 and Table 2), while can be compared with result obtained by [24,35] for the specie Ulva lactuca, of 12.89 MJ/Kg, favouring the use of macroalgae carbon species composition for bioenergy, with possible specific offshore crops marine farms [36].
According [37], the high carbon content of some macroalgae species may be due they have several sulphated polysaccharides (PSs) in their composition, characterizing Hypnea pseudomusciformis specie as Rhodophyta carrageenan, a family of PSs that undergo variations originating from free hydroxyl substitutions. These polymers are formed by the repetition of disaccharide units.

2.1.2. Analysis of Combustion Macroalgae Biomass to Get Bioenergy

Combustion efficiency assessments are based on the results of biomass calorific value. Macroalgae have an average moisture content over 70%, which could be a factor that prevents efficient combustion of their biomass, reducing its calorific value. Although this moisture content varies with the species, extraction processes and technological drying methodologies can make all the difference for efficient combustion [38]. Energy conversion losses are shown to be effective between the lower calorific value and the higher calorific value, this difference from 8.82 MJ/Kg to 10.09 MJ/Kg and 20.19 MJ/Kg for pellets, characterizes the combustion efficiency for raw materials condensed into energy composites, synthesizing greater sustainability for briquettes and pellets produced. The main gases emitted during macroalgae combustion are carbon dioxide (CO2) and water vapor (H2O).
These are the typical products of biomass combustion. CO2 and H2O are formed when the organic compounds present in macroalgae, such as carbohydrates and lipids, react with oxygen during the burning process. It is important to note that although macroalgae emit CO2 during combustion, they also absorb CO2 during their growth through photosynthesis [39,40]. This creates a shorter carbon cycle compared to fossil fuels, potentially reducing the net impact on greenhouse gas emissions [40]. Mitigation process with macroalgae cultivation can act as a carbon sink, absorbing between 0.46–2.55 Pg. of carbon per year [41]. In addition, depending on the specific composition of the macroalgae and combustion conditions, other gases can be emitted in smaller quantities, such as nitrogen oxides—NOx (1–5%) and sulphur compounds (1–2.5%), due to the presence of these elements in the algae biomass [34,40]. Macroalgae produce ash with a high alkaline metal content, which can cause fouling and corrosion in combustion systems.
The co-firing of macroalgae with other fuels has several potential benefits [39,41]: (1) Reduction of emissions: Co-firing can reduce total emissions per unit of energy produced compared to burning fossil fuels alone. (2) Reduction of pollutants: There is potential to reduce emission levels of pollutants such as sulphur oxides, heavy metals, dioxins and furans, due to the composition of macroalgae. (3) Use of waste: The use of macroalgae deposited on beaches, which would otherwise be discarded, minimises waste and reduces transport and disposal costs. (4) Renewable resource: Macroalgae are a source of renewable biomass, contributing to the diversification of the energy matrix. (5) Short-term carbon cycle: Although they emit CO2 during combustion, macroalgae absorb CO2 during their growth, potentially reducing the net impact on greenhouse gas emissions [34]. (6) Energy potential: Some species of macroalgae have a calorific value comparable to that of terrestrial biomass used for energy generation. (7) Mitigation of environmental impacts: Co-firing can reduce soil and water pollution, depending on the chemical composition of the material used [34,39]. It is important to note that, despite these potential benefits, macroalgae co-firing still faces technical and economic challenges that need to be overcome for its large-scale implementation. Direct combustion of macroalgae presents significant challenges due to their unique chemical composition, but their potential as a renewable energy source and carbon sink merits further research and technological development [40].
Biofuels produced with macroalgae have already demonstrated efficiency in the production of ethanol for automotive vehicles, achieve a title of 4.7% volume/volume and a yield of 0.281 weight ethanol/weight dry macroalgae [33], equivalent around 80% of the maximum theoretical yield from the sugar composition in macroalgae [42] and still by pellets, can also be adapted more sustainably for use in bakery ovens, pizzerias and industrial boilers that normally use non-certified wood or biomass with low calorific value.

2.2. Meaning Relation About Fibre Elements Energy in Macroalgae

The lignin rates in this research ranged from 0.31% to 13.74% are low (Table 3). The studies and analysis of [10], demonstrated that macroalgae lignin and cellulose have a reduced calorific value compared to terrestrial biomass, it means that lignin HCV has an average of 0.025 MJ/Kg against 0.015 MJ/Kg for celluloses. It is known that the lignin polymer contains less oxygen than the polysaccharides present in holocellulose [43]. This factor distinguishes in terms of its higher HCV value. The cellulose content between 5.13–23.29%, around 11.28% average (Table 4), it’s not so different by research of [44], when the different chain molecules of cellulose glucose polymer is present in Ochrophyta, Chlorophyta and Rhodophyta with 10%. Reduced cellulose modified in macroalgae, compared to terrestrial plants, would can be caused by the fact that phenolic compounds present in the cell walls of macroalgae are interacting as inhibitors in several development processes; as about cellular level, by lipid metabolism influences, and his biochemical mechanism of respiration, inhibiting glucose transport and cellulose synthesis, it means, contains in quantity the compound responsible for hydrolysis that decomposes the cellulosic polymer [43]. A fibrillar structure is important for the physical reinforcement of cell walls. However, other researches like [44,45], reported that some species, such as Gracilaria verrucosa, reach 60% cellulose, and [46], for a kind of Vallonia specie with more than 70% cellulose. According to [47], cellulose levels in macroalgae depend on different biomass treatment systems, Methane yields, have been improved by 19–68% after the breakdown of biomass structures by mechanical, thermal, enzymatic, and chemical treatments to improve cellular access to polysaccharide-hydrolysing agents [48,49]. Cellular variability in macroalgae membranes can determine the beneficial value of mechanical treatment, where those with more fibrous cell walls would benefit the decrease in its size [50]. Macroalgae exhibit distinct characteristics in the cell wall [51] standing out these differences as brown algae present cellulose in the primary skeletal cell wall, while green and red algae present xylose, mannose and cellulose [52]. This context of low fibre composition can be attributed to the absence of roots, stems and leaves in macroalgae [53]. This factor indicates better possibilities to biogas generation than terrestrial plants, when you have applicate anaerobic digestion and hydrolysis processes, due to the greater ease of permeation inside the plant, being free of lignin barrier in organic matter degradation processes.
According [17,27,29]; The macroalgae ash content is higher than in terrestrial plants. Some species varying 18–55% [54,55]. Therefore, following the analysis of 10 species, the author yielded results ranging from 14–39.7% to 3.3–46% in four species examined [56]. The results in the present research with 11 species analysed found 3.75% for aggregated biomass. It cannot be said that species with the highest ash content, respectively, Padina sp. and Caulerpa microphysa, (Table 3) achieved high calorific value; which means, this element does not translate efficiency calorific energy to use macroalgae.
These different results can be explained because they are not the same species and indeed, this may a present distinct genetic development [1]. Consonant to [29,30], this variation in ash composition is influenced by seasonality in the appearance of species, with more content ashes at certain times of the year.
This regional instable seasonality was observed in the present research in collect process with the appearance of three new species in the summer season; Caulerpa escapiliformes, Bryopsis plumosa and Pictyor mentensii with predominance of Bryopsis plumosa specie from the phylum Chlorophyta. The studies of [57] evaluated that the amino acid content in Saccharina latissima in august was almost double in June and ash mineral contents also increased [58]. It is possible to affirm that three species with the lowest content of lignin, cellulose and ash; Cryptonemia crenulata, Gracilaria sp., Hydropuntia cornea, were that presented the highest indices of calorific value. The last two species with less fibre, had elevated potassium levels, establishing a relationship that less fibre with greater calorific value and more potassium content.

2.3. Sustainability of Macroalgae Biomass Deposition

The sustainability of macroalgae biomass deposited daily along the coast of Alagoas was proven in sampling studies with an average of 5.03 ton/ha [59]. The main reason for this high deposition it is because there is a single harvest per year to terrestrial plants and it is possible to make two collections daily by beach cast seaweed. Environmental problems with marine biomass, such as output greenhouse gases by methane emissions after degradation of organic raw material in high temperature, meaning subjected to long time sun exposure in coastal band area. Therefore, accumulated seaweed biomass transported to landfills every day, would be mitigated with macroalgae biorefinery process. According to the Municipal Secretariat for Sustainable Development of Maceió, two full trucks are stored every day, equivalent to 4 tons of biomass, which is sent to landfills and contributes to high costs for public finances (Figure 1).

2.4. Evaluation of Pellets Produced with Heat Capacity

According to [60], the increase abrasion resistance and reduction wear equipment in the production of biofuel from pellets can be achieved with the addition of natural binders such as corn potato starch, sugarcane molasses, vegetable oil and sulfonated lignin (waste from the pulp and paper industry).
The cylindrical pellets result with granulometry 3 to 5 mm diameter, with a length 8 to 25 mm and a specific mass of 680 Kg/m3, was obtained the value of 20.19 MJ/Kg, being produced 1.28 Kg of pellets with 6 Kg of natural biomass. (Figure 2 and Figure 3). It follows, the corn oil binder participated in the HCV with a contribution of 1.88 MJ/Kg, representing 9.35% of calorific value. In the present work there was a loss of calorific energy by content biomass moisture of 17.61% in the pellets.
According [61] reported that additive uses should be analysed with caution because sulfonated lignin, for example, increases the sulphur content causing undesirable gas emissions when combustion of pellets is evaluated for environmental impact. There is no consensus on the use of binders, in the United States and Italy the use of these additives is limited for some products, to get stamp high quality pellets is not allowed. In Sweden, the use of these binders must be indicated on the product packaging.
Research conducted by [62] in Sweden showed that producers in this country use 0.5 to 2.0% potato starch in wood pellets. A comparison of the higher calorific values of terrestrial biomasses condensed into energetic composites of briquettes versus macroalgae aggregated into pellets (Figure 2) shows 9.83–20.51 MJ/Kg, with an average of 17.61 MJ/Kg, which is 11.46% lower than the higher calorific value of energetically condensed pellets—20.19 MJ/Kg (Figure 3). The higher calorific value of different pellets studied by [63] was also inferior to macroalgae pellets (Table 4). The calorific values of pellets and briquettes are equivalent because they are compacted in the same structure and show no significant differences when analysed for the same biomass, since the compression and moisture suppression processes are similar in the two cylindrical formats.
Another lower calorific value study by [64], with 17 species of pellets, obtained an average LCV of 16.10 MJ/Kg, were also 11.6% lower than macroalgae pellets with LCV of 18.76 MJ/Kg analysed by standard method in this research.
Table 4. Higher calorific value of pellets.
Table 4. Higher calorific value of pellets.
Types of PelletsH.C.V. MJ/KGReferencesAuthors
Wood of Denmark20.08Bruhn et al. (2011)[58]
Wood of Belgium20.31V.K. Verma et al. (2012)[63]
Finland peat21.63V.K. Verma et al. (2012)[63]
Reed canary grass pellets of Finland19.25V.K. Verma et al. (2012)[63]
Poland apple juice from Industrial waste20.68V.K. Verma et al. (2012)[63]
Pectin from citrus shell—Denmark19.24V.K. Verma et al. (2012)[63]
Sunflower husks—Ukraine20.27V.K. Verma et al. (2012)[63]
Belgium wheat straw18.25V.K. Verma et al. (2012)[63]
Macroalgae—Brazil20.19Coelho, F. P. (2024)[59]

3. Material and Methods

3.1. Collection Methodology: Description of Macroalgae Sampling Studies

The research area, estimated to be 408.736 m2, was georeferenced with the geographic coordinates from the first beach (Pajuçara), given as latitude 9°40′53″ S, longitude 35°42′19″ W, to the last beach (Sereia), with latitude 9°35′17″ S, longitude 35°38′49″ W, as in Figure 4. The sizing of the area was performed with the reference collection points made with the My GPS Coordinates application and images from the NOAA, U.S. Navy, NGA, and GEBECO satellites (Google Maps base, Figure 4 and Figure 5). The analyses samples further collections composed by macroalgae species were carried out from 2014 to 2016, on the beaches of Pajuçara, Ponta Verde, Jatiúca, Guaxuma, Garça Torta, Riacho Doce and Sereia, on the north coast of the municipality of Maceió, Alagoas, Northeast of Brazil.
The algae samples were collected manually, weighed in loco with “EEEKIT” Portable Fishing Scale, with measurement of the gross weight, evaluating the losses with sand, water and garbage founded in biomass. Therefore, washing was carried out in tap water in a stainless-steel tank measuring 55 cm × 48 cm, adopting the decanting method which the heaviest solids, such as sea sand, were deposited at tank bottom and lighter garbage was removed manually from the surface level water. The final residue of fine sand was removed by washing algae in running water superimposed on 50/60 cm aluminium screen sieves. The moisture from biomass was removed by manual pressing to extract the largest volume of water. The collected material was transported to Phycology Laboratory of Federal University of Alagoas, where was identified 27 species taxonomically based on the works described by following authors [65,66,67,68,69], being that 13 species were randomly selected for characterization in a mixture constituted as “aggregated biomass”. The scientific identification names of the species were confirmed through database Algae Base [9]. The drying final process was submitting the biomass to sun exposition during three days in the open air.

Collection Methodology by Moon Tide Table

The collection time was determined by the lowest point of tide moon height, when deposition biomass is intense on coast during 2 h and are determined by moon phases, which magnetism exerted by sun and moon forming a strong linear conjunction with our planet, making tide recede from coastal maritime zone with more intensity in sometimes period of the day, alternating in summer waning and full moons, in winter the new and crescent moons, adopting the methodology collection applied by [70]. The height measures of the tides are adopted by Port Authority of the Brazilian Navy and Directorate of Hydrography and Navigation-DHN (Table 5).

3.2. Macroalgae Characterization for Evaluation Capacity Energy Calorific Power

The total C and N samples contents were carried out by combustion at 925 °C and determined in a CHNS-O elemental analyser (Perkin Elmer PE-2400, Shelton, CT, USA), using the thermo reference standard (1.755% of C; 0.195% of N and 0.039% S). The samples were dried in oven circulation air at 65 °C for 24 h and passed through 100 mesh sieves. Approximately 3 mg of macroalgae sample was used. Phosphorus and potassium were carried out at Northeast Regional Centre for Nuclear Sciences—CRCN, with an energy dispersive x-ray fluorescence spectrophotometer, EDX 720 equipment, using 10 mm polypropylene collimator to control radiation. The samples were placed in container diameter with 31.6 mm, by volumetric capacity of 10 mL, sealed with polypropylene film. The equivalent mass of each sample was 0.5 to 1 g. The reading time when the sample was irradiated with an X-ray fluorescent tube were detected, from 100 to 300 s, and the respective materials were processed from the standard references SRM 1570a, SRM 1547, SRM 1515. Lignin, Cellulose and Ash quantifications were performed in an ANKON (Macedon, NY, USA) fiber determiner according to described method by [71]. The digesting technique consisted of 0.5 g of seaweed sample in bags made of synthetic material, resistant to digestion, previously weighed and dried in an oven at 65 °C for 24 h.

3.3. Analysis of Algae Calorific Value

The high calorific value (HCV) of macroalgae biomass was determined from 13 species with three replicates for each sample, and five replicates for the aggregate biomass sample. The HCV determination was made in an IKA WERKE calorimeter pump (Staufen, Germany), C2000, with 0.6 to 1.0 g raw material placed in a crucible for each sample, into a stainless-steel tank with high pressure (30.0 bar) oxygen atmosphere, which was closed and immersed in a double wall vessel containing 4 L of water.
The water temperature of 23–28 °C was programmed as a function of combustion time relative to biomass amount. For each measurement, with specific heat of the container between 12–28 °C and the water pressure between 1 bar with maximum of 1.5 bar, for energy released during the combustion process was evaluated. The lower calorific value (LCV) of the species and pellets were evaluated using the Standard Method ASTM D-240-64 [72]. The combustion tests based on the HCV results to percentages of hydrogen contained in the biomass by Equation (1):
LCV = HCV − 50.68 × H
It means; LCV is the lower calorific value in calories per gram, HCV is the high calorific value in calories per gram, and H is the percentage of hydrogen in the sample.

3.4. Energetic Pellets Condensates

The macroalgae pellets production was carried out after washing and drying biomass in open air. The dry biomass with 6 Kg without milling was placed in pelletizing machine AF-150, 4 Kw, added with 50 mL of corn oil binder, equivalent to 449.5 kcal (1.88 MJ/Kg). The pellets were compacted through by extrusion process in a pellet machine with pressure exerted around 300 MPa or 3059 Kg f/cm2, approximate temperature of 120 °C, like similar process by [50]. The superior heat calorific value of aggregated biomass from 13 species in form of pellets was evaluated in a calorimetric bomb, referring based on analysis of five replicates to each one pellet, included three sample. The determination of moisture (M) in the aggregate biomass of pellets was calculated by wet weight (Ww) minus dry weight (Dw) divided by the wet weight × 100. Equation (2)
M = Ww − Dw/Ww × 100

4. Conclusions

The aggregated macroalgae biomass can become a new generation of renewable biofuels, reducing the environmental liabilities accumulated in dumps and landfills with elevated costs for public management. Indeed, it’s a free biomass availability with large scale deposition by tropical and continental seas all over the world. Allows efficient use of own energy by achieving a calorific value similar to one of the main biomasses in energy generation, sugar cane. The management of this biomass can reduce costs compared to terrestrial biomasses, without the need for irrigation, fertilizers or other agricultural inputs. The ability to realize two daily collections proves its unique potential for biorefinery. On the positive side, it reinforces its biological characteristics with enhanced photosynthesis four times superior to terrestrial biomass, indeed, a high point to self-sufficient and sustainable biomass production systems with cycle carbon sequestration. Macroalgae pellets have a high calorific value of 20.19 MJ/Kg, with the advantage that they do not interfere with the supply of edible food and do not require large areas of land for cultivation, as is the case with terrestrial biomass. Positive results of marine macroalgae biomass calorific value can range new research and advanced technologies for the production of renewable energy, with reduced costs and environmental balance, promoting a progressive industrial scale in the production of energy with natural resources from the oceans.

Author Contributions

Conceptualization, F.P.C., E.V.d.S.B.S. and C.A.M.d.A.; Methodology, F.P.C., E.V.d.S.B.S., E.A.C.G.-C., E.J.d.F., M.M.d.S.C. and C.A.M.d.A.; Software, E.J.d.F. and M.M.d.S.C.; Validation, R.S.C.M. and C.A.M.d.A.; Formal analysis, E.A.C.G.-C., M.M.d.S.C. and M.G.B.; Investigation, F.P.C., E.V.d.S.B.S., E.A.C.G.-C., B.M.S., V.A.R.C. and C.A.M.d.A.; Resources, E.C.S.d.S., M.G.B. and B.M.S.; Data curation, E.V.d.S.B.S., C.A.M.d.A. and R.S.C.M.; Writing—original draft, F.P.C.; Writing—review & editing, E.C.S.d.S., E.A.C.G.-C., E.V.d.S.B.S. and C.A.M.d.A.; Supervision, F.P.C., E.J.d.F. and R.S.C.M.; Project administration, F.P.C., R.S.C.M. and C.A.M.d.A. All authors have read and agreed to the published version of the manuscript.

Funding

No funding was received to assist in the preparation of this manuscript. No funding or grants or third-party resources were received by any authors. This research did not receive any specific grant from funding agencies in the public, commercial, or not-for-profit sectors.

Data Availability Statement

The results of this research can be publicly consulted in: “Digital Repository Data of Pernambuco Federal University” at the link: https://repositorio.ufpe.br/handle/123456789/30792, accessed on 10 December 2024. All statistical and methodological data of research were actualized and confirmed with consent of all authors. The authors declare that they had support of Federal University of Pernambuco, Federal University of Alagoas and Northeast Regional Centre for Nuclear Sciences to carry out laboratory research and chemical analysis of the raw material.

Acknowledgments

My best regards and thanks to Federal University of Alagoas (UFAL), Federal University of Pernambuco (UFPE), Regional Centre for Nuclear Sciences of the Northeast (CRCN), my master’s and doctoral supervisors, all professors who contributed to my training, all my team researcher who helped me in this paper and to my family and friends who always believed in me.

Conflicts of Interest

There are no conflicts to declare.

References

  1. Alakangas, E.; Heikkinen, A.; Lensu, T.; Vestrsrinen, P. Summary Report; Intelligent Energy Europe: Jyväskylä, Finland, 2007; p. 57. ISSN VTT-R-03508-07. [Google Scholar]
  2. Bavisi, A.; Srinivas, B.A.; Shah, M.; Pritam, K.S.; Kumar, A. Sustainable Practices Through Carbon Offset Coins: Incentivizing Green Energy and Efficiency. In Proceedings of the 2024 International Conference on Sustainable Energy: Energy Transition and Net-Zero Climate Future (ICUE), Pattaya City, Thailand, 21–23 October 2024; pp. 1–4. [Google Scholar] [CrossRef]
  3. Balina, K.; Romagnoli, F.; Blumberga, D. Seaweed biorefinery concept for sustainable use of marine resources. Energy Procedia 2017, 128, 504–511. [Google Scholar] [CrossRef]
  4. Liu, H.; Yao, P.; Latif, S.; Aslam, S.; Iqbal, N. Impact of Green financing, FinTech, and financial inclusion on energy efficiency. Environ. Sci. Pollut. Res. 2022, 29, 18955–18966. [Google Scholar] [CrossRef] [PubMed]
  5. Roegen, N.G. The Entropy Law and the Economic Process in Retrospect. East. Econ. J. 1986, 12, 3–25. Available online: https://www.jstor.org/stable/40357380 (accessed on 19 February 2025).
  6. Hickel, J. The contradiction of the Sustainable Development Goals: Growth versus ecology on a finite planet. Sustain. Dev. 2019, 27, 873–884. [Google Scholar] [CrossRef]
  7. French, D.; Kotzé, L.J. Sustainable Development Goals—Law, Theory and Implementation. In European Yearbook of International Economic Law 2019; Bungenberg, M., Krajewski, M., Tams, C.J., Terhechte, J.P., Ziegler, A.R., Eds.; Springer: Cham, Switzerland, 2019; Volume 10. [Google Scholar] [CrossRef]
  8. Moro, M.F.; de Souza Mendonça, A.K.; Barni, G.D.A.C.; Bornia, A.C. Transformação global da energia: A participação das energias renováveis na matriz elétrica das 50 maiores economias. MIX Sustentável 2019, 5, 115–123. [Google Scholar] [CrossRef]
  9. Guiry, M.D.; Guiry, G.M. Macroalgae Base; Worldwide Electronic Publication; National University of Ireland: Galway, Ireland, 2017; Available online: https://www.algaebase.org/ (accessed on 11 February 2025).
  10. Almeida, W.R.; Guimarães, S.M.P.B.; Moura, C.W.D.N. Novas adições à flora marinha bentônica da costa nordeste do Brasil. IHERINGIA Sér. Bot. 2014, 69, 97–105. [Google Scholar]
  11. Taşkin, E.; Güreşen, A.; Bilgiç, F. Implementation of a new Non-destructive Phytobenthic Index (NPI) with the Posidonia Biotic Index (BiPo) to evaluate the ecological status of the Turkish Aegean coasts—Eastern Mediterranean. Turk. J. Bot. 2024, 48, 296–307. [Google Scholar] [CrossRef]
  12. Vijay, K.; Balasundari, S.; Jeyashakila, R.; Velayathum, P.; Masilan, K.; Reshma, R. Proximate and Mineral Composition of Brown Seaweed from Gulf of Mannar. Int. J. Fish. Aquat. Stud. 2017, 5, 106–112. Available online: https://www.fisheriesjournal.com/ (accessed on 19 February 2025).
  13. Ashokkumar, V.; Salim, M.R.; Salam, Z.; Sivakumar, P.; Chong, C.T.; Elumalai, S.; Suresh, V.; Ani, F.N. Production of liquid biofuels (biodiesel and bioethanol) from brown marine macroalgae Padina Tetrastromatica. Energy Convers. Manag. 2017, 135, 351–361. [Google Scholar] [CrossRef]
  14. Jeyakumar, N.; Hoang, A.T.; Nižetić, S.; Balasubramanian, D.; Kamaraj, S.; Pandian, P.L.; Sirohi, R.; Nguyen, P.Q.P.; Nguyen, X.P. Experimental investigation on simultaneous production of bioethanol and biodiesel from macro-algae. Fuel 2022, 329, 125–362. [Google Scholar] [CrossRef]
  15. John, R.P.; Anisha, G.; Nampoothiri, K.M.; Pandey, A. Micro and macroalgal biomass: A renewable source for bioethanol. Bioresour. Technol. 2011, 102, 186–193. [Google Scholar] [CrossRef] [PubMed]
  16. Kim, Y.S.; Chae, S.W.; Park, D.H.; Sunwoo, C. Pretreatment of Gelidium amansii for the production of bioethanol. Bull. Korean Chem. Soc. 2010, 131, 511. [Google Scholar] [CrossRef]
  17. Ross, A.B.; Jones, J.M.; Kubacki, M.L.; Bridgman, T. Classification of macroalgae as fuel and its thermochemical behaviour. Bioresour. Technol. 2008, 99, 6494–6504. [Google Scholar] [CrossRef] [PubMed]
  18. Wi, S.G.; Kim, H.J.; Mahadevan, S.A.; Yang, D.J.; Bae, H.J. The potential value of the seaweed Ceylon moss (Gelidium amansii) as an alternative bioenergy resource. Bioresour. Technol. J. 2009, 100, 6658–6660. [Google Scholar] [CrossRef]
  19. Yoon, J.J.; Kim, S.H.; Ryu, H.J.; Choi, J.Y.; Kim, G.S.; Shin, M.K. Production of polysaccharides and corresponding sugars from red seaweed. Adv. Mater. Res. 2010, 93–94, 463–466. [Google Scholar] [CrossRef]
  20. Roesijadi, G.; Jones, S.B.; Snowden, L.J.S.; Zhu, Y. Macroalgae as a Biomass Feedstock: A Preliminary Analysis; Pacific Northwest National Laboratory: Richland, WA, USA; U.S. Department of Energy: Washington, DC, USA, 2010; pp. 1–50. ISSN PNNL-19944. [Google Scholar] [CrossRef]
  21. Silva Martins, L.O.; e Alex Santos de Andrade, D. Estimativa teórica do potencial de geração de energia elétrica a partir de cana-de-açúcar, capim elefante e coco da Bahia no Brasil. Textura 2021, 14, 38–58. [Google Scholar] [CrossRef]
  22. Brand, M.A. Energia de Biomassa Vegetal; Editora Interciência: Rio de Janeiro, Brazil, 2010; p. 131. ISBN 9788571932449. Available online: https://www.editorainterciencia.com.br/index.asp?pg=prodDetalhado.asp&idprod=79 (accessed on 11 February 2025).
  23. Soares, R.V.; Hakkila, P. Potencial energético dos resíduos de desbastes em plantações de Pinus Taeda no Estado do Paraná, Brasil. Rev. Floresta 1987, 17, 73–94. [Google Scholar] [CrossRef]
  24. Alburo, C.S.; Conje, R.H.; Pino, M.G.; Tan, E.P. Calorific Values and Proximate Analysis of Sargassum spp. and Ulva spp.; USC Chemical Engineering Student Research Annual; Department of Chemical Engineering, University of San Carlos: Cebu, Philippines, 2010; pp. 1–13. [Google Scholar]
  25. Roesijadi, G.; Coleman, A.; Judd, C.; Cleve, B.; Buenau, K.; Thom, R.; Ward, J.; Wigmosta, M. Macroalgae Analysis: A National GIS-Based Analysis of Macroalgae Production Potential; Summary Report and Project Plan; U.S. Department of Energy: Washington, DC, USA; Pacific Northwest National Laboratory Richland: Richland, WA, USA, 2011; pp. 1–69. [Google Scholar] [CrossRef]
  26. Ross, A.B.; Anastasakis, K.; Kubacki, M.; Jones, J.M. Investigation of the pyrolysis behaviour of brown algae before and after pre-treatment using PY-GC/MS and TGA. J. Anal. Appl. Pyrolysis 2009, 85, 3–10. [Google Scholar] [CrossRef]
  27. Ghadiryanfar, M.; Rosentrater, K.A.; Keyhani, A.; Omid, M. A review of macroalgae production, with potential applications in biofuels and bioenergy. Renew. Sustain. Energy Rev. 2016, 54, 473–481. [Google Scholar] [CrossRef]
  28. Lane, C.E.; Mayes, C.; Druehl, L.D.; Saunders, G.W. A multi-gene molecular investigation of the kelps (Laminariales, Ochrophyta) supports substantial taxonomic re-organization. J. Phycol. 2006, 42, 493–512. [Google Scholar] [CrossRef]
  29. Chen, H.; Zhou, D.; Luo, G.; Zhang, S.; Chen, J. Macroalgae for biofuels production: Progress and perspectives. Renew. Sustain. Energy Rev. 2015, 47, 427–437. [Google Scholar] [CrossRef]
  30. Marinho Soriano, E.; Fonseca, P.C.; Carneiro, M.A.A.; Moreira, W.S.C. Seasonal variation in the chemical composition of two tropical seaweeds. Bioresour. Technol. 2006, 18, 2402–2406. [Google Scholar] [CrossRef]
  31. Migliore, G.; Alisi, C.; Sprocati, A.R.; Massi, E.; Ciccoli, R.; Lenzi, M.; Wang, A.; Cremisini, C. Anaerobic digestion of macroalgal biomass and sediments sourced from the Orbetello lagoon, Italy. Biomass Bioenergy 2012, 42, 69–77. [Google Scholar] [CrossRef]
  32. Moreira, A.; Cruz, S.; Marques, R.; Cartaxana, P. The underexplored potential of green macroalgae in aquaculture. Rev. Aquac. 2021, 14, 526. [Google Scholar] [CrossRef]
  33. Wargacki, A.J.; Leonard, E.; Win, M.N.; Regitsky, D.D.; Santos, C.N.S.; Kim, P.B.; Cooper, S.R.; Raisner, R.M.; Herman, A.; Sivitz, A.B.; et al. An engineered microbial platform for direct biofuel production from brown macroalgae. Science 2012, 335, 308–313. [Google Scholar] [CrossRef]
  34. Lane, D.J.; Ashman, P.J.; Zevenhoven, M.; Hupa, M.; van Eyk, P.J.; de Nys, R.; Karlström, O.; Lewis, D.M. Combustion Behavior of Algal Biomass: Carbon Release, Nitrogen Release, and Char Reactivity. Energy Fuels 2014, 28, 41–51. [Google Scholar] [CrossRef]
  35. Wang, J.; Wang, G.; Zhang, M.; Chen, M.; Li, D.; Min, F.; Zang, S.; Ren, Z.; Yan, Y. A comparative study of termolysis characteristics and kinetics of seaweeds and fir wood. Process Biochem. 2006, 41, 1883–1886. [Google Scholar] [CrossRef]
  36. Kumar, G.; Sahoo, D. Effect of seaweed liquid extract on growth and yield of Triticum aestivum var. Pusa Gold. J. Appl. Phycol. 2011, 23, 251–255. [Google Scholar] [CrossRef]
  37. Reis, R.P.; Leal, M.C.R.; Yoneshigue-Valentin, Y.; Belluco, F. Efeito de fatores bióticos no crescimento de Hypnea musciformis (RhodophytaGigartinales). Acta Bot. Bras. 2003, 17, 279–286. [Google Scholar] [CrossRef]
  38. Lee, M.S.; Lee, J.H. Ethanol production from Laminaria japonica: Effect of metal ion adsorption. J. Ind. Eng. Chem. 2012, 18, 1662–1665. [Google Scholar] [CrossRef]
  39. Milledge, J.J.; Smith, B.; Dyer, P.W.; Harvey, P. Macroalgae-Derived Biofuel: A Review of Methods of Energy Extraction from Seaweed Biomass. Energies 2014, 7, 7194–7222. [Google Scholar] [CrossRef]
  40. Krause-Jensen, D.; Duarte, C. Substantial role of macroalgae in marine carbon sequestration. Nat. Geosci. 2016, 9, 737–742. [Google Scholar] [CrossRef]
  41. Gonzalez Pelayo, A. Prospectus for Future Research: Temperature Effects on Green Macroalgae. Bachelor’s Thesis, Portland State University, Portland, OR, USA, 2016; p. 316. [Google Scholar] [CrossRef]
  42. Habeebullah, S.F.K.; Alagarsamy, S.; Sattari, Z.; Al-Haddad, S.; Fakhraldeen, S.; Al-Ghunaim, A.; Al-Yamani, F. Enzyme-assisted extraction of bioactive compounds from brown seaweeds and characterization. J. Appl. Phycol. 2020, 32, 615–629. [Google Scholar] [CrossRef]
  43. Dhargalkar, V.K.; Deshmukhe, G.V. Subtidal Marine Algae of the Dwaraka Coast (Gujarat). Indian J. Mar. Sci. 1996, 25, 297–301. Available online: http://drs.nio.org/drs/handle/2264/2157 (accessed on 11 February 2024).
  44. Wegeberg, S.; Felby, C. Algae biomass for bioenergy in Denmark. In Biological/Technical Challenges and Opportunities; Technical Report; Department of Biology, Science, University of Copenhagen: København, Danmark, 2010; p. 60. Available online: https://www.osti.gov/etdeweb/biblio/992674 (accessed on 11 February 2024).
  45. Barbot, Y.N.; Benz, R.; Thomsen, L. Thermo-Acidic Pre-treatment of Beach Macroalgae from Rügen to Optimize Biomethane Production—Double Benefit with Simultaneous Bioenergy Production and Improvement of Local Beach and Waste Management. Mar. Drugs 2015, 13, 5681–5705. [Google Scholar] [CrossRef]
  46. Chemodanov, A.; Jinjikhashvily, G.; Habiby, O.; Liberzon, A.; Israel, A.; Yakhini, Z.; Golberg, A. Net primary productivity, biofuel production and CO2 emissions reduction potential of Ulva sp. (Chlorophyta) biomass in a coastal area of the Eastern Mediterranean. Energy Convers. Manag. 2017, 148, 1497–1507. [Google Scholar] [CrossRef]
  47. Maneein, S.; Milledge, J.J.; Nielsen, B.V.; Harvey, P.J. A Review of Seaweed Pre-Treatment Methods for Enhanced Biofuel Production by Anaerobic Digestion or Fermentation. Fermentation 2018, 4, 100. [Google Scholar] [CrossRef]
  48. Wei, N.; Quarterman, J.; Jin, Y.S. Marine macroalgae: An untapped resource for producing fuels and chemicals. Trends Biotechnol. 2013, 31, 71. [Google Scholar] [CrossRef]
  49. Sharma, S.; Hansen, L.D.; Hansen, J.Ø.; Mydland, L.T.; Horn, S.J.; Øverland, M.; Eijsink, V.G.H.; Vuoristo, K.S. Microbial Protein Produced from Brown Seaweed and Spruce Wood as a Feed Ingredient. J. Agric. Food Chem. 2018, 66, 8328–8335. [Google Scholar] [CrossRef]
  50. Nielsen, N.P.K.; Gardner, D.G.; Felby, C. Effect of extractives and storage on the pelletizing of sawdust. Fuel 2009, 89, 94–98. [Google Scholar] [CrossRef]
  51. Deniaud-Bouët, E.; Hardouin, K.; Potin, P.; Kloareg, B.; Hervé, C. A review about brown algal cell walls and fucose-containing sulphated polysaccharides: Cell wall context, biomedical properties and key research challenges. Carbohydr. Polym. 2017, 175, 395–408. [Google Scholar] [CrossRef]
  52. Coelho, F.P.; Menezes, R.S.C.; Sampaio, E.V.d.S.B.; Barboza, M.G.; Soares, E.C.; Guedes-Coelho, E.A.C.; de França, E.J.; dos Santos, A.J.; de Lima, M.F.; Costa, M.M.d.S.; et al. Biorefinery of Beach Cast Seaweed in Brazil: Renewable Energy and Sustainability. Phycology 2024, 4, 394–413. [Google Scholar] [CrossRef]
  53. Ladeira, A.M.; Zaidan, L.B.P.; Figueiredo, R.C.L. Ageratum conyzoides L. Compositae: Germinação, floração e ocorrência de derivados fenólicos em diferentes estágios de desenvolvimento. Hoehnea 1987, 15, 53–62. [Google Scholar]
  54. Tabassum, M.R.; Xia, A.; Murphy, J.D. Comparison of pre-treatments to reduce salinity and enhance biomethane yields of Laminaria digitata harvested in different seasons. Energy 2017, 140, 546–551. [Google Scholar] [CrossRef]
  55. Guedes, E.A.C.; Moura, A.D.N. Estudo da Biomassa e composição mineral de “algas arribadas” em Praias do Litoral Norte de Alagoas. Bol. Estud. Ciênc. Mar. 1996, 9, 19–30. [Google Scholar]
  56. Allen, E.; Wall, D.M.; Herrmann, C.; Murphy, J.D. Investigation of the optimal percentage of green seaweed that may be co-digested with dairy slurry to produce gaseous biofuel. Bioresour. Technol. 2014, 170, 436–444. [Google Scholar] [CrossRef]
  57. Brown, L.M.; Zeiler, K.G. Aquatic biomass and carbon dioxide trapping. Energy Convers. Manag. 1993, 34, 1005–1013. [Google Scholar] [CrossRef]
  58. Bruhn, A.; Dahl, J.; Bangs, H.N.; Nikolaisen, L.; Rasmussen, M.B.; Markager, S.; Olesen, B.; Arias, C.; Jensen, P.D. Bioenergy potential of Ulva Lactuca: Biomass yield, methane production and combustion. Bioresour. Technol. 2011, 102, 2595–2604. [Google Scholar] [CrossRef]
  59. Coelho, F.P.; Barboza, M.G.; Guedes-Coelho, É.A.C.; Costa, M.M.d.S.; dos Santos, A.J.; de Lima, M.F.; da Silva, E.C.S.; Carneiro, V.A.R.; Soares, B.M.; de França, E.J.; et al. Sustainability of beach cast seaweed biomass for biorefinery process: Sampling studies in the littoral of Alagoas/Brazil. Contemp. J. 2024, 4, e5306. [Google Scholar] [CrossRef]
  60. Kuokkanen, M.; Vilpo, T.; Kuokkanen, T.; Stoor, T.; Ninimaki, J. Additives in wood pellet production—A pilot scale study of binding agent usage. Bioresources 2011, 6, 4331–4355. [Google Scholar] [CrossRef]
  61. Lethikangas, P. Quality properties of pelletised sawdust, logging residues and bark. Biomass Bioenergy 2001, 19, 351–360. [Google Scholar] [CrossRef]
  62. Arromdee, P.; Ninduangdee, P. Combustion characteristics of pelletized-biomass fuels: A thermogravimetric analysis and combustion study in a fluidized bed combustor. Energy Ecol. Environ. 2023, 8, 69–88. [Google Scholar] [CrossRef]
  63. Verma, V.K.; Bram, S.; Delattin, F.; Laha, P.; Vandendael, I.; Hubin, A.; De Ruyck, J. Agro-pellets for domestic heating boilers: Standard laboratory and real-life performance. Appl. Energy 2012, 90, 17–23. [Google Scholar] [CrossRef]
  64. Telmo, C.; Lousada, J. Heating values of wood pellets from different species. Biomass Bioenergy 2011, 35, 2634–2639. [Google Scholar] [CrossRef]
  65. Guimarães, S.M.P.B.; Pereira, A.P.V. Rodofíceas marinhas bentônicas do estado do Espírito Santo, Brasil: Gênero Calliblepharis (Cystocloniaceae, Gigartinales). Hoehnea 1993, 20, 35–46. [Google Scholar]
  66. Lopes, A.S. Estudos Taxonômicos da Ordem Dictyotales (Ochrophyta) da Praia de Serrambi (Município de Ipojuca—Estado de Pernambuco—Brasil). Master’s Thesis, Universidade Federal Rural de Pernambuco, Recife, Brazil, 1993; p. 110. [Google Scholar]
  67. Nunes, J.M.C.; Santos, A.C.C.; Minervino, A.; Brito, K.S. Algas marinhas bentônicas do município de Ilhéus, Bahia, Brasil. Acta Bot. Malacit. 1999, 24, 5–12. [Google Scholar]
  68. Nunes, J.M.C.; Paula, E.J. O gênero Dictyota Lamour. (Dictyotaceae-Ochrophyta) no Litoral do estado da Bahia. Acta Bot. Malacit. 2001, 26, 5–18. Available online: https://hdl.handle.net/10630/3999 (accessed on 19 February 2025).
  69. Nunes, J.M.C.; Barros-Barreto, M.B.; Guimarães, S.M.P.B. A família Ceramiaceae (Ceramiales, Rhodphyta) no estado da Bahia, Brasil. Monogr. Ficológicas 2008, 3, 75–159. [Google Scholar]
  70. Bast, F. Ancestors of land plants with rich diversity. Resonance 2014, 1, 1032–1043. [Google Scholar] [CrossRef]
  71. Van Soest, P.J. Use of detergent in analysis of fibrous feeds; Study of effects of heating and drying on yield of fiber and lignin in forages. J. Assoc. Off. Agric. Chem. 2020, 48, 785–790. [Google Scholar] [CrossRef]
  72. ASTM D-240-64; Standard Test Method for Heat of Combustion of Liquid Hydrocarbon Fuels by Bomb Calorimeter. Annual Book of ASTM Standards. ASTM: West Conshohocken, PA, USA, 2013.
Figure 1. Tractors remove seaweed biomass from Maceió coast beaches (2025).
Figure 1. Tractors remove seaweed biomass from Maceió coast beaches (2025).
Plants 14 01005 g001
Figure 2. Macroalgae pellets biomass.
Figure 2. Macroalgae pellets biomass.
Plants 14 01005 g002
Figure 3. Calorific value comparison of energetic condensates composite from terrestrial biomass against seaweed pellets.
Figure 3. Calorific value comparison of energetic condensates composite from terrestrial biomass against seaweed pellets.
Plants 14 01005 g003
Figure 4. Detailing of macroalgae biomass collection area.
Figure 4. Detailing of macroalgae biomass collection area.
Plants 14 01005 g004
Figure 5. Collection points of macroalgae biomass—Ponta Verde beach in Maceió, Alagoas.
Figure 5. Collection points of macroalgae biomass—Ponta Verde beach in Maceió, Alagoas.
Plants 14 01005 g005
Table 1. Macroalgae species—Higher calorific value (HCV) and lower calorific value (LCV).
Table 1. Macroalgae species—Higher calorific value (HCV) and lower calorific value (LCV).
SpeciesPhylumHCV/MJ/KgLCV/MJ/Kg
Cryptonemia luxuriansRhodophyta11.4310.04
Sargassum sp.Ochrophyta10.689.67
Ulva fasciataChlorophyta8.216.76
Cryptonemia crenulataRhodophyta12.0210.87
Lobophora variegataOchrophyta10.589.58
Gracilaria sp.Rhodophyta11.149.91
Cryptonemia seminervisRhodophyta9.678.99
Ulva lactucaChlorophyta11.439.38
Hydropuntia corneaRhodophyta11.429.86
Padina sp.Ochrophyta8.327.31
Caulerpa microphysaChlorophyta6.375.97
Hypnea pseudomusciformisRhodophyta8.736.51
Sargassum vulgareOchrophyta11.199.79
Average-10.098.82
Table 2. Nutrient concentrations macroalgae species founding in the beaches of Maceió, Alagoas, Brazil.
Table 2. Nutrient concentrations macroalgae species founding in the beaches of Maceió, Alagoas, Brazil.
Species/BiomassWeight/gCarbon %Hydrogen %Nitrogen %Phosphorus g/KgPotassium g/Kg
Cryptonemia sp.3.137.946.543.740.7303.113
Sargassum sp.3.128.994.781.300.04819.869
Ulva fasciata3.129.516.861.620.2365.691
Cryptonemia crenulata2.830.425.443.030.5828.022
Lobophora variegata3.130.624.721.190.4707.606
Gracilaria sp.2.933.625.82.550.22534.872
Cryptonemia seminervis320.603.222.351.2556.197
Ulva lactuca2.950.089.644.180.3014.819
Hydropuntia cornea3.141.977.330.95ND34.014
Padina sp.3.128.214.791.590.2849.181
Caulerpa microphysa316.581.880.981.1861.466
Hypnea pseudomusciformis361.8710.444.790.65850.068
Sargassum vulgare2.938.606.63.330.5959.412
Aggregate biomass2.943.976.734.530.5938.795
ND—Not detected.
Table 3. Fibre components of 11 seaweeds species and aggregate biomass.
Table 3. Fibre components of 11 seaweeds species and aggregate biomass.
Seaweed SpeciesPhylumLignin (%)Cellulose (%)Ashes (%)
Sargassum sp.Ochrophyta9.4111.768.06
Cryptonemia crenulataRhodophyta2.449.272.46
Lobophora variegataOchrophyta5.2723.294.04
Gracilaria sp.Rhodophyta1.987.173.16
Cryptonemia seminervisRhodophyta4.118.333.86
Ulva lactucaChlorophyta9.139.574.15
Hydropuntia corneaRhodophyta0.315.131.86
Padina sp.Ochrophyta12.7210.4210.56
Caulerpa microphysaChlorophyta13.7413.929.79
Hypnea pseudomusciformisRhodophyta8.588.237.32
Sargassum vulgareOchrophyta7.1317.724.33
Aggregate biomass-7.2912.013.75
Overall average 6.8111.285.30
Table 5. Tide table on the days of macroalgae collections.
Table 5. Tide table on the days of macroalgae collections.
DateHoursTide Height/mMoon Phases
12 March 201513.47 m0.6full moonPlants 14 01005 i001
4 April 20159.47 m0.2full moonPlants 14 01005 i001
5 April 201510.15 m0.2full moonPlants 14 01005 i001
5 March 20167.11 m0.6waning moonPlants 14 01005 i002
12 March 201612.09 m0.1new moonPlants 14 01005 i003
17 September 201610.00 m0.0full moonPlants 14 01005 i001
15 October 20168.56 m0.0waxing moonPlants 14 01005 i004
16 October 20169.38 m0.0full moonPlants 14 01005 i001
Disclaimer/Publisher’s Note: The statements, opinions and data contained in all publications are solely those of the individual author(s) and contributor(s) and not of MDPI and/or the editor(s). MDPI and/or the editor(s) disclaim responsibility for any injury to people or property resulting from any ideas, methods, instructions or products referred to in the content.

Share and Cite

MDPI and ACS Style

Coelho, F.P.; Sampaio, E.V.d.S.B.; Barboza, M.G.; Guedes-Coelho, E.A.C.; Costa, M.M.d.S.; Silva, E.C.S.d.; Carneiro, V.A.R.; Soares, B.M.; França, E.J.d.; Menezes, R.S.C.; et al. Renewable Energy from Beach-Cast Seaweed: Calorific Power Heating Studies with Macroalgae. Plants 2025, 14, 1005. https://doi.org/10.3390/plants14071005

AMA Style

Coelho FP, Sampaio EVdSB, Barboza MG, Guedes-Coelho EAC, Costa MMdS, Silva ECSd, Carneiro VAR, Soares BM, França EJd, Menezes RSC, et al. Renewable Energy from Beach-Cast Seaweed: Calorific Power Heating Studies with Macroalgae. Plants. 2025; 14(7):1005. https://doi.org/10.3390/plants14071005

Chicago/Turabian Style

Coelho, Fernando Pinto, Everardo Valadares de Sá Barreto Sampaio, Márcio Gomes Barboza, Elica Amara Cecília Guedes-Coelho, Manoel Messias da Silva Costa, Emerson Carlos Soares da Silva, Victor Andrei Rodrigues Carneiro, Bruno Moreira Soares, Elvis Joacir de França, Rômulo Simões Cezar Menezes, and et al. 2025. "Renewable Energy from Beach-Cast Seaweed: Calorific Power Heating Studies with Macroalgae" Plants 14, no. 7: 1005. https://doi.org/10.3390/plants14071005

APA Style

Coelho, F. P., Sampaio, E. V. d. S. B., Barboza, M. G., Guedes-Coelho, E. A. C., Costa, M. M. d. S., Silva, E. C. S. d., Carneiro, V. A. R., Soares, B. M., França, E. J. d., Menezes, R. S. C., & Abreu, C. A. M. d. (2025). Renewable Energy from Beach-Cast Seaweed: Calorific Power Heating Studies with Macroalgae. Plants, 14(7), 1005. https://doi.org/10.3390/plants14071005

Note that from the first issue of 2016, this journal uses article numbers instead of page numbers. See further details here.

Article Metrics

Back to TopTop