Global Trends and Research and Gaps in Anaerobic Digestion: A Systematic and Bibliometric Review with Implications for Ghana
Abstract
1. Introduction
2. Methods
2.1. Comprehensive Review
2.1.1. Study Design
2.1.2. Review Framework
2.1.3. Data Source and Search Strategy
2.1.4. Inclusion and Exclusion Criteria
2.1.5. Data Extraction and Quality Assessment
2.1.6. Comprehensive Review Results
- Search Results
2.2. Bibliometric Review
2.2.1. Search Strategy
2.2.2. Data Processing and Analysis
2.2.3. Bibliometric Analysis Results
- Bibliometric Coverage
2.3. Data Synthesis
3. Biogas Production in Ghana
3.1. Introduction
3.2. Current State of Biogas Production and Research in Ghana
3.3. Existing Biogas Facilities and Their Operational Capacity
3.4. Benefits of Biogas Production in Ghana
4. Municipal Solid Waste as a Feedstock for Anaerobic Digestion: Ghana vs. The World
4.1. Overview of Municipal Solid Waste Management in Ghana Against the World
4.2. Global Practices in Anaerobic Digestion of Municipal Solid Waste: Ghana vs. Global Trends in Anaerobic Digestion
4.3. Bibliometric Analysis: Municipal Solid Waste as Feedstock for Anaerobic Digestion
5. Feedstocks for Biogas Production (Anaerobic Digestion): Ghana vs. The World
5.1. Feedstock Pretreatment for Biogas Production (Anaerobic Digestion): Ghana vs. The World
5.1.1. Comparative Analysis of Feedstock Pretreatment Methods in Ghana and Global Practices
5.1.2. Challenges and Opportunities in Feedstock Pretreatment for Biogas Production in Ghana
5.1.3. Bibliometric Analysis: Feedstock Pretreatment for Biogas Production
- Co-Authorship of Feedstock Pretreatment for Biogas Production Against Countries
- Citation of Co-Authorship of Feedstock Pretreatment for Biogas Production Against Countries
- Bibliographic Coupling of Co-Authorship of Feedstock Pretreatment for Biogas Production Against Countries
- Documents on Feedstock Pretreatment for Biogas Production by Countries
5.2. Feedstock Characteristics Influencing Methane Yield Performance Across Global and Ghana Studies
6. Biochemical Methane Potential of Feedstock: Ghana vs. The World
6.1. Biochemical Methane Potential and Its Importance
Trends on Biochemical Methane Potential of Feedstocks Around the World vs. Ghana
6.2. Bibliometric Analysis: Biochemical Methane Potential of Feedstock
7. Operating Parameters of Anaerobic Digestion on Biogas Production and Methane Content Around the World vs. Ghana
7.1. One-Time-Factorial and Multifactorial Parameters Analysis in AD for Biogas Production
7.2. Bibliometric Analysis of Optimisation of Operating Parameters of Biogas Production: Ghana vs. The World
8. AD Process Systems Across the World vs. Ghana
8.1. Batch and Continuous AD Process Systems Across the World vs. Ghana
8.2. Types of Biogas Systems: Small, Medium and Large Scale
Current Trends of Small-, Medium- and Large-Scale Biogas Systems in the World vs. Ghana
8.3. Digestate Utilisation and Management Across the World vs. Ghana
9. Summarised Interpretation of Results—Systematic Review
10. Discussion and the Way Forward for Ghana
11. Conclusions
Author Contributions
Funding
Data Availability Statement
Acknowledgments
Conflicts of Interest
References
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| Facilities Name | Scale | Location | Feedstocks | Bioenergy/Biogas Quantity Produced | References |
|---|---|---|---|---|---|
| Safisana Plant | Large pilot | Ashaiman, Greater Accra | Faecal Sludge, Organic Market Waste, abattoir waste and influent waste | 15,925 m3 biogas/day | [21,22] |
| Ghana Oil Palm Development Company (“GOPDC”) | Large pilot | Kade, Eastern Region | palm oil mill effluent (“POME”) | 18,000 m3 biogas/day | [22,23] |
| Das Biogas–AMA Plant | Large pilot | Accra Metropolitan Area | Organic municipal waste | 52,925 m3 biogas/year | [24,25] |
| Kwamoka Energy Hybrid Plant | Under-development | Oti light Industrial area, Sokoban, Kumasi | Wood and agricultural residues | - | [26] |
| HPW Fresh & Dry plants | Medium pilot | Adeiso, Eastern Region | Fruit processing waste (coconut, papaya, banana, mango and pineapple) | 328,500 m3 biogas/year | [22] |
| Gyankobaa Hybrid PV-Biogas-Pyrolysis Plant | Medium pilot | Gyankobaa, Atwima Nwabiagya South, Ashanti Region | Municipal solid waste | - | [27,28] |
| OxRight Demonstration | Small Pilot | Ghana | Agricultural and organic waste | 1120 m3 biogas/year | [29] |
| Feedstocks | Pretreatment Method | Methane Yield (mL CH4/g VS) | Country | Reference |
|---|---|---|---|---|
| Corn Stover | 2% NaOH, 3 days at ambient temperature | Not specified | China | [81] |
| Corn Stover | Steam explosion | 217.5 | China | [82] |
| Rice Straw | Hydrothermal (100 °C, 10 min) | 280 | China | [83] |
| Reed Biomass | Steam explosion (200 °C, 15 min) | 355 | Spain | [84] |
| Wheat Straw | Mechanical (0.3 mm milling) | 245.6 | Not specified | [85] |
| Cocoa Pod Residues | Hydrothermal (150 °C) | 289.3 | Ghana | [86] |
| Sawdust (Quercus genus) | Biological and alkaline pretreatment | Not specified | Nigeria | [87] |
| Maize Silage | Microbial consortium with high cellulolytic activity | 393.3 | Poland | [88] |
| Sugar Beet | Silage | 350.4–399.4 | Germany | [89] |
| Sunflowers | Silage | 210–286.1 | Germany | [89] |
| Winter Wheat | Silage | 269.2–327.6 | Germany | [89] |
| Barley Straw | Mechanical pretreatment (rotary drum pre-composting) | 339 | China | [90] |
| Miscanthus lutarioriparius | Steam explosion (198 °C, 3 min) | 274.1 | China | [91] |
| Corn Stover | Steam explosion (200 °C, 10 min) | 250 | China | [91] |
| Corn Straw | Oxidative pretreatment (Hydrogen peroxide) | 216.7 | Indonesia | [92] |
| Salvina molesta | Acidic pretreatment (sulfuric acid) | 17.4 | USA | [93] |
| Willow Sawdust | Fungal pretreatment (Leiotrametes menziesii) | 62.4 | Poland | [94] |
| Wheat Straw | Steam explosion (200 °C, 15 min) | Untreated: 180; Pretreated: 280 | China | [95] |
| Wheat Straw | Hydrothermal (160 °C, 45 min) | Untreated: 180; Pretreated: 309.6 | China | [95] |
| Pig manure | Co-Digestion (Mesophilic, Neutral pH) | 201.5–481.0 | - | [96] |
| Cow manure | Mechanical/Co-Digestion (Mesophilic, Neutral pH) | 58.5–201.5 | - | [96] |
| Cattle Manure | Mechanical separation/Co-digestion | 450–600 | Ghana | [97] |
| Cafeteria Waste | Mechanical shredding/Fat removal | 400–520 | Canada | [98] |
| Market Waste | Co-digestion with livestock manure | 300–380 | Canada | [98] |
| Vegetative waste, waste wood, garden waste, citrus waste | Gasification | - | United States | [99] |
| Pretreatment Method | Worldwide Performance | Limitation in Ghana | Feasibility Under Ghanaian Conditions | References |
|---|---|---|---|---|
| Thermal pretreatment (steam explosion, hydrothermal) | High methane yield Expensive | High energy demand, expensive equipment, limited infrastructure | Low-medium | [66,100,101] |
| Chemical pretreatment (Alkali, Acid) | Less expensive, High degradation of complex organic molecules, High efficiency | Chemical costs, corrosion risks, Environmental concerns | Medium | [100,101] |
| Mechanical pretreatment (milling, shredding) | Expensive High energy requirements Improve biogas production | Equipment maintenance and high electricity requirements | High | [100,101] |
| Biological pretreatment (fungi, microbes) | High degradation capacity of cellulose/hemicelluloses/lignin. Environmentally friendly, Enhance biogas yield Less energy required | Longer treatment duration, limited technical expertise | High | [101,102] |
| Feedstocks | VS&TS (%) | C/N Ratio | Lignocellulosic Content (%) | MC (%) | Methane Yield Potential | Country/Region | References |
|---|---|---|---|---|---|---|---|
| Food waste | 23.1 VS 23.70 TS | 28.4 Balance | Not given | Not given | High; due to balanced C/N ratio | China | [103,104] |
| Rice straw | 60–70 VS >15 TS | 45.73 High | Cellulose: 38.44 Hemicellulose: 27.21 Lignin: 18.83 | 10.78 Low | Moderate; high VS but high C/N ratio and lignin, reducing methane yield | China | [105] |
| Sugarcane bagasse | 94.2 VS 96.3 TS | 227 High | Not given | Not given | Low-moderate; high VS but very high C/N ratio leading to nitrogen deficiency | Brazil | [106] |
| Cattle manure | 70–85 VS 20–30 TS | 15–25 Moderate | Not given | Not given | Moderate-high; C/N ratio is closed to the optimum range | Europe | [107] |
| MSW | 20–35 TS 80–90 VS | 15–25 Moderate | Not given | Not given | Moderate-high; C/N ratio is favourable | Europe | [107] |
| Cocoa pod husk | 67.82 VS 91.95 TS | 45.49 High | Cellulose: 37.90 Hemicellulose: 54.00 Lignin: 4.10 | Not given | Moderate; high C/N ratio and low nitrogen | Ghana | [108] |
| Food waste | 83.99 VS 25.80 TS | 32.59 Balanced | Not given | 74.35 High | High; due to high VS, high MC and favourable biodegradability | Ghana | [109,110] |
| Human excreta | 82.81 VS 11.34 TS | 8.36 Low | Not given | 88.68 High | Moderate; high VS but low C/N ratio | Ghana | [109,110] |
| Feedstocks | BMP Range Values NmLCH4/gVS | Country/Region | References |
|---|---|---|---|
| Food waste | 467–529 | Europe | [120] |
| 385–627 | China | [123] | |
| Rice straw | 92–196 | China | [122] |
| Corn straw | 205.9 ± 3.4 | China | [129] |
| Sugarcane bagasse | 140–220 | Brazil | [128] |
| Sewage sludge | 300–400 | Europe | [124] |
| Pig slurry | 250–350 | Europe | [124] |
| Poultry manure | 300–500 | Europe | [124] |
| Grass | 300–450 | Europe | [124] |
| Vegetable waste | 200–251 | Europe | [124] |
| Feedstocks | BMP Range Values NmLCH4/gVS | Data Type | References |
|---|---|---|---|
| Cocoa pod husks | 477.94 | Theoretical estimate | [108] |
| OFMSW | 219.35 | Theoretical estimate | [1] |
| Cassava peel | 217.45 | Theoretical estimate | [130] |
| Sewage sludge | Not reported | - | - |
| Faecal sludge | 120–250 | - | [125] |
| Food waste | 175–300 | Experimental estimate | [131] |
| Feedstocks | Methane Yield (L CH4/kg VS) | Country/Region | References |
|---|---|---|---|
| Fruit and vegetable waste | 420 | China | [134] |
| Wheat straw | 297 | China | [135] |
| Cotton stalk | 240 | China | [135] |
| Food waste | 410–573 | Europe | [136,137] |
| Switchgrass | 140–205 | Europe | [138] |
| Energy crops | 250–350 | Europe | [139] |
| Rice straw | 227.3 | China | [140] |
| Pig manure | 450 | Europe | [141] |
| Fruits and Vegetable waste | 342 | Europe | [142] |
| Food waste | 435 | USA | [143] |
| Rice straw | 420 | Ghana | [144] |
| Food waste | 135.27 | Ghana | [110] |
| Human excreta | 253.89 | Ghana | [110] |
| Fruits and vegetables | 198.86 | Ghana | [110] |
| Parameters | World Range | Ghana Range | References |
|---|---|---|---|
| Temperature | Mesophilic: 25–37 °C; Thermophilic: 50–60 °C | Mesophilic: 25–35 °C | [145,156,157,159] |
| pH | 6.5–7.6 | 6.0–7.7 | [145,157] |
| HRT | 10 to 40 days (Mesophilic) | 20–26 days | [145,156,158] |
| OLR | 1–10 kg VS/m3/day | 1.9–5 kg VS/m3/day | [160,161,162] |
| C/N Ratio | 20:1 to 30:1 | 20:1 to 30:1 | [145,157] |
| TS content | 5–40% TS | 3–30% TS | [160,163] |
| Ammonia | <150 mg/L | Up to 1.5 g/L | [131,147,164] |
| Operating Parameters | Typical Optimum Range | Effect on Biogas Production and Methane Yield | Limitations/Trade-Offs | Feasibility Under Ghanaian Conditions | References |
|---|---|---|---|---|---|
| pH | 6.5–7.5 | Maintains methanogenic activity and process stability; deviations can suppress methane production and lead to volatile fatty acid (VFA) accumulation. | Requires regular monitoring and buffering; chemical addition may increase operating costs. | High—can be monitored and adjusted using relatively simple operational methods or device like a pH controller. | [165,166] |
| Temperature (Mesophilic) | 30–40 °C | Provides stable microbial activity and reliable biogas production with lower energy requirements. | Lower methane yield and longer digestion times compared with thermophilic operation. | High—compatible with Ghana’s tropical climate and lower energy requirements. | [165,167] |
| Temperature (Thermophilic) | 50–60 °C | Increases reaction rates, pathogen destruction and biogas production while reducing retention time. | Additional energy inputs required, increased operational costs and lower process stability. | Low–feasible, mainly for industrial-scale facilities with reliable energy supply. | [146,165] |
| Hydraulic Retention Time (HRT) | 10–40 days at mesophilic range | Longer HRT generally improves substrate degradation and methane recovery. | Excessively long HRT increases digester size and capital cost; very short HRT may cause biomass washout and VFAs acidification. | Medium–High—achievable but may require larger digesters and higher capital investment. | [165,166] |
| Organic Loading Rate (OLR) | 1–8 kg VS m−3 day−1 | Increasing OLR enriched bacteria species, can increase volumetric biogas production | Excessive OLR may result in acidification, VFA accumulation and process failure. | Medium—requires technical expertise and regular monitoring to prevent overloading. | [165,166] |
| C/N Ratio | 20–30 | Supports balanced microbial growth and efficient methane yield. | Low C/N can cause ammonia inhibition, high C/N may result in nutrient deficiency and lower methane yield. | High—can be improved through co-digestion of locally available feedstocks. | [107,165] |
| AD System Types | World | Ghana | Energy Efficiency | Process Stability | References |
|---|---|---|---|---|---|
| Batch systems | single-stage batch digesters, anaerobic sequential batch reactors (ASBR), garage-type digesters, dry batch digesters | single-stage batch digesters; dry batch digesters; laboratory-scale digester | Moderate to high for small-scale applications, but lower overall efficiency due to irregular biogas production | Moderate stability; requires additional digester to maintain stable output | [154,176,194,195] |
| Continuous systems | CSTR, USAB, expanded granular sludge beds (EGSB), plug flow digesters, two-phase anaerobic digesters | fixed-dome, floating drum digesters, CSTR, USAB, Horizontal Plug Flow (HPF) | High energy efficiency and biogas production | High process stability due to continuous feeding and steady-state operation | [185,188,191] |
| Reference | Feedstock/Theme | Pretreatment/Condition | Methane Yield | Main Findings |
|---|---|---|---|---|
| [81] | Corn stover | 2% NaOH, 3 days ambient | Not specified | The experimental results showed alkaline pretreatment improved degradation efficiency in China. |
| [82] | Corn stover | Steam explosion | 217.5 mL CH4/g VS | This paper investigates steam explosion and confirms enhanced methane yield compared to untreated stover. |
| [83] | Rice straw | Hydrothermal (100 °C, 10 min) | 280 mL CH4/g VS | The experimental results showed hydrothermal pretreatment improved biogas recovery. |
| [84] | Reed biomass | Steam explosion (200 °C, 15 min) | 355 mL CH4/g VS | This result confirms steam explosion significantly enhanced methane yield in Spain. |
| [85] | Wheat straw | Mechanical milling (0.3 mm) | 245.6 mL CH4/g VS | This paper investigates mechanical pretreatment and confirms improved biodegradability despite high energy demand. |
| [86] | Cocoa pod residues | Hydrothermal (150 °C) | 289.3 mL CH4/g VS | The experimental results showed hydrothermal pretreatment increased methane yield in Ghana. |
| [87] | Sawdust (Quercus genus) | Biological + alkaline | Not specified | This paper investigates combined pretreatment and confirms enhanced biomethanation in Nigeria. |
| [88] | Maize silage | Microbial consortium | 393.3 mL CH4/g VS | The experimental results showed microbial pretreatment improved cellulose breakdown in Poland. |
| [89] | Sugar beet, sunflower, wheat | Silage | 210–399 mL CH4/g VS | This paper investigates silage crops and confirms variable methane yields depending on species in Germany. |
| [90] | Barley straw | Mechanical (rotary drum pre-composting) | 339 mL CH4/kg VS | The experimental results showed mechanical pretreatment improved methane yield in China. |
| [91] | Miscanthus lutarioriparius | Steam explosion (198 °C, 3 min) | 274.1 mL CH4/g VS | This paper investigates steam explosion and confirms improved methane yield in China. |
| [92] | Corn straw | Oxidative (H2O2) | 216.7 mL CH4/g VS | The experimental results showed oxidative pretreatment enhanced methane yield in Indonesia. |
| [93] | Salvina molesta | Acidic (sulfuric acid) | 17.4 mL CH4/g VS | This paper investigates acid pretreatment and confirms low methane yield in USA conditions. |
| [94] | Willow sawdust | Fungal pretreatment | 62.4 mL CH4/g VS | The experimental results showed fungal pretreatment improved biodegradability in Poland. |
| [66,100,101] | Pretreatment comparison | Thermal, chemical, mechanical, biological | Variable | These papers investigates pretreatment methods worldwide and confirms thermal yields are highest but least feasible in Ghana. |
| [101,102] | Biological pretreatment | Fungi, microbes | High degradation | The results confirm biological pretreatment is environmentally friendly and feasible in Ghana. |
| [103,104] | Food waste | Balanced C/N ratio | High methane potential | The experimental results showed food waste has high biodegradability and methane yield in China. |
| [105] | Rice straw | High lignin, high C/N | Moderate methane | This paper investigates rice straw and confirms lignin content reduces methane yield. |
| [106] | Sugarcane bagasse | High C/N ratio | Low–moderate methane | The experimental results showed nitrogen deficiency limits yield in Brazil. |
| [107] | Cattle manure, MSW | Moderate C/N | Moderate–high methane | This paper investigates manure/MSW and confirms favourable C/N ratios improve yield in Europe. |
| [108] | Cocoa pod husk | High C/N ratio | 477.9 NmL CH4/g VS (theoretical) | This paper investigates cocoa pods and confirms moderate methane potential in Ghana. |
| [109,110] | Food waste, human excreta | Balanced vs. low C/N | 135–300 NmL CH4/g VS | The experimental results showed food waste has high yield, while human excreta is limited by low C/N in Ghana. |
| [120,123] | Food waste | BMP assays | 385–627 NmL CH4/g VS | Papers investigates BMP values and confirms food waste has high methane potential in Europe and China. |
| [122] | Rice straw | BMP assays | 92–196 NmL CH4/g VS | The experimental results showed rice straw has low BMP due to lignin content. |
| [128] | Sugarcane bagasse | BMP assays | 140–220 NmL CH4/g VS | This paper investigates bagasse and confirms moderate methane potential in Brazil. |
| [124] | Sewage sludge, pig slurry, poultry manure | BMP assays | 250–500 NmL CH4/g VS | The experimental results showed animal manures have high methane potential in Europe. |
| [130] | Cassava peel | BMP assays | 217.45 NmL CH4/g VS | This paper investigates cassava peel and confirms moderate methane potential in Ghana. |
| [131] | Food waste (Ghana) | BMP assays | 175–300 NmL CH4/g VS | The experimental results showed food waste has high methane potential under Ghanaian conditions. |
| [134,135,136,137,138,139,140,141,142,143] | Global feedstocks | Various | 198–573 L CH4/kg VS | These papers investigates global feedstocks and confirms food waste and pig manure have highest yields. |
| [144] | Rice straw (Ghana) | Experimental | 420 L CH4/kg VS | The experimental results showed rice straw has high methane yield in Ghana. |
| [145,146,147,148,149,150,151,152,153,154,155,156,157,158,159,160,161,162,163,164,165,166] | Operating parameters | pH, temperature, HRT, OLR | Variable | The paper here investigates operating ranges and confirms mesophilic conditions are most feasible in Ghana. |
| [154,176,194,195] | AD system types | Batch systems | Moderate efficiency | Investigates batch digesters and confirms moderate stability but irregular gas output. |
| [185,188,191] | AD system types | Continuous systems | High efficiency | The experimental results showed continuous systems provide stable operation and higher yields. |
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Darmey, J.; Narra, S.; Achaw, O.-W.; Stinner, W.; Frimpong, I.K.; Amoatey, N.K.; Agyekum, T.O.; Amaniampong, D. Global Trends and Research and Gaps in Anaerobic Digestion: A Systematic and Bibliometric Review with Implications for Ghana. Environments 2026, 13, 408. https://doi.org/10.3390/environments13070408
Darmey J, Narra S, Achaw O-W, Stinner W, Frimpong IK, Amoatey NK, Agyekum TO, Amaniampong D. Global Trends and Research and Gaps in Anaerobic Digestion: A Systematic and Bibliometric Review with Implications for Ghana. Environments. 2026; 13(7):408. https://doi.org/10.3390/environments13070408
Chicago/Turabian StyleDarmey, James, Satyanarayana Narra, Osei-Wusu Achaw, Walter Stinner, Isaac Kwasi Frimpong, Nene Kwabla Amoatey, Theophilus Ofori Agyekum, and Daniel Amaniampong. 2026. "Global Trends and Research and Gaps in Anaerobic Digestion: A Systematic and Bibliometric Review with Implications for Ghana" Environments 13, no. 7: 408. https://doi.org/10.3390/environments13070408
APA StyleDarmey, J., Narra, S., Achaw, O.-W., Stinner, W., Frimpong, I. K., Amoatey, N. K., Agyekum, T. O., & Amaniampong, D. (2026). Global Trends and Research and Gaps in Anaerobic Digestion: A Systematic and Bibliometric Review with Implications for Ghana. Environments, 13(7), 408. https://doi.org/10.3390/environments13070408

