Exploring the Energy Potential of Residual Biomass: A Bibliometric Analysis
Abstract
1. Introduction
2. Waste-to-Energy Conversion Options
3. Bibliometric Analysis of Methodological References
3.1. Methodological Development
3.2. Classification Method
3.3. Results Analysis
3.3.1. Top Publications and Authors
3.3.2. Top Journals
3.3.3. Contributions by Institutions
3.3.4. Contributions per Country
3.3.5. Keywords
3.3.6. Discussion on Selected Publications
4. Conclusions
Author Contributions
Funding
Data Availability Statement
Acknowledgments
Conflicts of Interest
Abbreviations
| CRA | Corporación Autónoma Regional del Atlántico |
| WtE | Waste-to-Energy Technologies |
| AD | Anaerobic Digestion |
| GHGs | Green House Gases |
| MSW | Municipal Solid Waste |
| RDF | Refuse Derived Fuel |
| HTC | Hydrothermal Carbonization |
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| Description | Results |
|---|---|
| Data Overview | |
| Sampling Period | 2017–2021 |
| Sources (Magazines, Books, etc.) | 388 |
| Documents | 1869 |
| Average years since publication | 1.74 |
| Average number of citations per document | 13.7 |
| Average number of citations per year per document | 4.885 |
| Document Types | |
| Papers | 1475 (78.92%) |
| Review Papers | 299 (16.00%) |
| Proceedings Paper | 87 (4.66%) |
| Editorial Material | 6 (0.32%) |
| Letters | 1 (0.05%) |
| Meeting Abstract | 1 (0.05%) |
| Authors | |
| Authors | 5818 |
| Author Participation | 8668 |
| Authors of Single-Author Documents | 41 |
| Authors of Multiple-Author Documents | 5777 |
| Author Collaboration | |
| Single-Author Documents | 46 |
| Documents per Author | 0.321 |
| Authors per Document | 3.11 |
| Co-authors per Document | 4.64 |
| Collaboration Index | 3.17 |
| Sample Size | Assessment Criteria |
|---|---|
| 66 | 25 publications with the highest number of citations |
| 16 publications from Colombia | |
| 25 most recent publications |
| No. | Document Title | Number of Citations | Reference |
|---|---|---|---|
| 1 | A review of the hydrothermal carbonization of biomass waste for hydrochar formation: Process conditions, fundamentals, and physicochemical properties | 349 | [25] |
| 2 | A Technological Overview of Biogas Production from Biowaste | 209 | [26] |
| 3 | Recent advances in the gasification of waste plastics. A critical overview | 205 | [27] |
| 4 | Fates of Chemical Elements in Biomass during Its Pyrolysis | 203 | [28] |
| 5 | A review of technological options of waste-to-energy for effective management of municipal solid waste | 202 | [4] |
| 6 | Co-pyrolysis of biomass and waste plastics as a thermochemical conversion technology for high-grade biofuel production: Recent progress and future directions elsewhere worldwide | 186 | [29] |
| 7 | Anaerobic co-digestion of animal manures and lignocellulosic residues as a potent approach for sustainable biogas production | 181 | [30] |
| 8 | Biomass pyrolysis: A review of the process development and challenges from initial research up to the commercialization stage | 163 | [31] |
| 9 | Hydrogen production from biomass using dark fermentation | 153 | [32] |
| 10 | Biorefineries in circular bioeconomy: A comprehensive review | 145 | [33] |
| No. | Journal | Impact Factor | Number of Publications | Global Percentage | Number of Citations | Global Percentage |
|---|---|---|---|---|---|---|
| 1 | Waste and Biomass Valorization | 3.703 | 112 | 6.0 | 853 | 3.3 |
| 2 | Waste Management | 7.145 | 102 | 5.5 | 2127 | 8.3 |
| 3 | Journal of Cleaner Production | 9.297 | 95 | 5.1 | 1488 | 5.8 |
| 4 | Renewable & Sustainable Energy Reviews | 14.982 | 86 | 4.6 | 3308 | 12.9 |
| 5 | Bioresource Technology | 9.642 | 81 | 4.3 | 2096 | 8.2 |
| WtE Technology | Capital Costs (US$/Ton MSW/Year) | Operation Costs (US$/Ton MSW/Year) |
|---|---|---|
| Incineration | 400–700 | 40–70 |
| Pyrolysis | 400–700 | 50–80 |
| Gasification | 250–850 | 45–85 |
| Anaerobic Digestion | 50–350 | 5–35 |
| Gas Recovery Landfill | 10–30 | 1–3 |
| WtE Technology | Global Warming Potential () |
|---|---|
| Incineration | 424 |
| Pyrolysis and Gasification | 412 |
| Anaerobic Digestion | 222 |
| Gas Recovery Landfill | 746 |
| Technology | Contribution | Author(s) |
|---|---|---|
| Anaerobic Digestion (AD) | The energy potential of animal manure for biogas production is suboptimal due to its high nitrogen content, which lowers its C/N ratio. To address this deficiency, co-digestion with lignocellulosic waste (agricultural, forestry, municipal solids, and agro-industrial waste) compensates for the carbon deficit of the manure and improves the methane yield of the process. | [30] |
To improve the biodegradability of agricultural biomass, pretreatments are used according to the physicochemical characteristics of each raw material. The following treatments can be used:
| [39] | |
| Based on the technological surveillance methodology conducted for the 2009–2019 period in the Scopus and SciELO databases on AD studies of Biological and Food Waste, the main factors that affect the AD process were determined. The most frequently evaluated factor is related to experimental configuration, since it has the largest number of associated variables. Nevertheless, most factors have not yet been widely studied. The organic load rate and the number of stages involved in the process are the most commonly studied variables. Substrate and environmental factors follow, with pretreatment being the main studied variable. Finally, there is the inoculum, which is mainly associated with variables such as the inoculum mixture and the substrate to inoculum ratio (S/I). On the other hand, among the least studied aspects are headspace (2.16%) and retention time (3.03%). In addition, after reviewing the studies and the variables assessed, only 18% simultaneously assessed two or more variables. This analysis is useful to establish whether simultaneous interactions exist among these variables. | [40] | |
| Manure was highlighted as a significant source of ammonia, methane, and nitrogen oxide emissions, which were estimated to be 40%, 22.5%, and 28%, respectively, of total United Kingdom (UK) anthropogenic emissions. AD is a technology that can drastically reduce the potential for manure contamination compared to process absence, thus reducing approximately 90% of methane and 50% of nitrogen oxide emissions. More than 1615 TWh of electricity could be generated, since most of the 90 million tons of manure produced by the UK would be processed through biogas capture. | [41] | |
| Gasification | Three gasification agents were used: air, steam, and oxygen, which produce different gas compositions, calorific values, and yields. Based on this, the authors deduced that steam produces a greater amount of , with a higher calorific value compared to gasification by air and oxygen, thus also reducing tar content from 17% to 24% more than the other agents. Although air is the most common agent for gasification, since it is an abundant natural compound and it is easy to use, it has a major drawback: it contains approximately 79% nitrogen, which largely dilutes the resulting gas and increases its separation cost. Moreover, the re-sulting gas has a low calorific value , being constrained to the on-site generation of heat and power. Oxygen has two drawbacks: the high cost of pure oxygen and the large cost needed to separate oxygen from syngas; hence, it is often combined with steam as a gasification agent. | [42] |
| Plastic waste steam gasification produces a synthesis gas rich in , of interest both for synthesis and energy applications. Furthermore, the absence of increases the calorific value of synthesis gas in values exceeding . Despite obtaining a higher quality syngas through steam gasification of plastics, this process must overcome two main limitations: process endothermicity, and the high tar content of the final product. | [27] | |
| The combined use of biomass/waste results in higher carbon conversion, production of a large amount of gas, and reduced hazardous toxic elements. The authors also deduced that fluidized bed gasifiers are more efficient in conversion, with less tar formation compared to fixed bed gasification techniques, which is one of the main issues of using this technique. | [43] | |
| The production of electricity and heat from biowaste resources in a Fluidyne Micro-Lab Class air-blown gasifier, which operates at atmospheric pressure, was also as-sessed. Poultry litter and digestate (obtained from an AD plant working with a mix-ture of animal manure and green waste) were selected for analysis. All materials were pelletized to increase their energy density. Consequently, the authors found that drying is essential for biowaste with high moisture content (50–60%), such as poultry waste, digestate, and MSW. The PCI of the Synthesis Gas produced oscillated between . In addition, agricultural and forestry waste do not require any pretreatment drying processes and can produce a useful amount of electricity. | [44] | |
| Pyrolysis | A critical review of the fate of the main chemical elements (C, H, O, N, P, Cl, S and metals) and advances in research on the emission, transformation, and distribution of pyrolysis elements was undertaken. First, the authors concluded that future work must be geared toward on-site or online detection and monitoring technologies, such as TG-FTIR-MS and Py-GC/MS, or advanced characterization techniques, such as solid carbon-13 spectroscopy nuclear magnetic resonance and synchrotron-based X-ray absorption spectroscopy, which could provide a feasible strategy to elucidate more deeply and precisely the mechanism and behaviors of lignocellulosic biomass in the pyrolysis process. Second, efficient sustainable catalysts and processes must be de-veloped to convert C, H, and O into desired products (i.e., bio-oil) and to avoid un-wanted products (i.e., tar and persistent organic pollutants). Third, any future works must ultimately predict and prevent the emission of through the development of new reducing agents or catalysts. Fourth, the development of technologies based on the calcium loop within the pyrolysis process could effectively retain N, P, S, and Cl in the biocarbon phase, and thus control their emissions in the bio-oil and gas phases. Likewise, some heavy metals, such as Cu and Ni denote catalytic effects in biomass pyrolysis to improve the final product. Finally, biomass co-pyrolysis with carbon or synthetic polymers (i.e., plastics, and rubbers) contributes to improving both the quality and the quantity of the pyrolysis oil, without having to improve the system process. | [28] |
| The study indicated that co-pyrolysis has been recognized for its ability to significantly improve the quantity and quality of pyrolysis oil, without the addition of catalysts, solvents, or hydrogen pressure to the process. On the other hand, co-pyrolysis has been considered an efficient and economical method for the production of high-grade biofuels from waste co-processing. | [29] | |
| Several biomass pretreatments have been developed, such as physical, thermal, chemical, and biological methods to improve the performance and quality of bio-oil; however, the structural configuration of raw materials and how they relate to bio-oil composition and properties must be studied further. Likewise, many researchers have developed different reactor configurations to maximize the yield of bio-oil or to improve the properties or certain specific properties thereof. Despite this, a large number of reactors still cannot fully meet the requirements of commercial pyrolysis reactors on an industrial scale, since a pyrolizer must have the ability to process versatile raw materials and accommodate low raw and reactor material requirements, as well as high heat transfer efficiency, among other aspects to reduce the operation costs and meet commercial use requirements. In this context, zeolite-based catalysts have emerged as promising agents for converting biomass into a low-oxygen fuel. Even so, they still suffer from coke fuel formation and its consequent rapid deactivation. Moreover, low bio-oil yields and carbon deficiency are the other parameters that must be considered when working with these catalysts. | [31] | |
| A pyrolysis study of different refuse derived fuel (RDF) samples was conducted in a semi-batch rotary kiln. These RDF samples were obtained from two different waste treatment plants operated by Bharuch Enviro Infrastructure Limited in the city of Ahmedabad, India, at an average feed particle size of 50 mm with different shapes. The thermal behavior of the RDF samples was studied using a thermal gravimetric analysis by heating in the presence of pure nitrogen (100 mL/min) at 20 °C/min up to 900 °C. Pure nitrogen was used to remove gaseous condensable products and air from the pyrolysis zone. The results showed that the quality of the pyrolysis product varied according to the feed composition and the operating temperature, wherein the highest oil yield (43%) was obtained with the RDF sample containing 77% of plastics at 500 °C. | [45] | |
| Other Technologies | A review of the critical Hydrothermal Carbonization (HTC) parameters was conducted, including temperature, residence time, heating speed, reagent concentration, and water quality. This review provided new perspectives that can be used to enhance the potential of this technology. The authors concluded that future work efforts must address the influence of a wide variety of organic substances contained in the biomass and identify their conversion mechanisms during the HTC process. Temperature was identified as the critical parameter governing hydrocarbon characteristics; however, more variables must be considered, such as heating rate, particle size, substrate concentration, packing ratio, catalyst addition, and liquid quality. | [25] |
| HTC from organic MSW fractions could reduce the problem of landfills and provide a sustainable source of solid fuel. The research indicated that upon increasing carbonization severity (higher temperatures and longer residence times), the solid yield and volatile hydrocarbon matter content generally decreased, while elemental carbon content increased, leading to higher heating values. However, at carbonization temperatures exceeding 260 °C, the amount of extractable “secondary” carbon decreased, after an initial increase to 220–240 °C. | [46] | |
| In Ecuador, a study assessed the energy potential of from MSW considering thermochemical (gasification combined with steam reform-ing) and electrochemical (gasification combined with electrolysis) paths for their conversion. This study also proved the feasibility of satisfying the energy demand of urban public transportation in 91% of the country with derived from MSW. Here, the authors offered very promising benefits, including a solution to the problem of final MSW disposal, with an improvement in urban transport infrastructure and its corresponding environmental indicators. | [47] |
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Ceballos-Sandoval, J.; Pulido-Rojano, A.D.; Rincón-Laurens, H.; Villalobos-Toro, B.; Ospino-Toro, O.; Rincón-Laurens, R.; Restrepo-Vieco, J. Exploring the Energy Potential of Residual Biomass: A Bibliometric Analysis. Energies 2025, 18, 6009. https://doi.org/10.3390/en18226009
Ceballos-Sandoval J, Pulido-Rojano AD, Rincón-Laurens H, Villalobos-Toro B, Ospino-Toro O, Rincón-Laurens R, Restrepo-Vieco J. Exploring the Energy Potential of Residual Biomass: A Bibliometric Analysis. Energies. 2025; 18(22):6009. https://doi.org/10.3390/en18226009
Chicago/Turabian StyleCeballos-Sandoval, Jairo, Alexander D. Pulido-Rojano, Hegel Rincón-Laurens, Bertha Villalobos-Toro, Oscar Ospino-Toro, Ray Rincón-Laurens, and Javier Restrepo-Vieco. 2025. "Exploring the Energy Potential of Residual Biomass: A Bibliometric Analysis" Energies 18, no. 22: 6009. https://doi.org/10.3390/en18226009
APA StyleCeballos-Sandoval, J., Pulido-Rojano, A. D., Rincón-Laurens, H., Villalobos-Toro, B., Ospino-Toro, O., Rincón-Laurens, R., & Restrepo-Vieco, J. (2025). Exploring the Energy Potential of Residual Biomass: A Bibliometric Analysis. Energies, 18(22), 6009. https://doi.org/10.3390/en18226009

