TABLE 4.
Pretreatments and effects on carcasses and swine manure biomass.
| Pretreatment | Biomass | Positive aspects | Negative aspects | Conditions | Biogas and/or hydrogen yield | References |
| Alkaline | Manure | Easy retrieval (high volatility), not corrosive, low energy. | Implementation at a large scale, and chemical application. | Aqueous ammonia 32% w/w 20°C, 96 h. | 244% increase in CH4 yield in 17 days of digestion. | Lymperatou et al., 2017 |
| Carcasses | No uncontrolled emission of gas, nutrients or pathogens into the environment. It is effective in eliminating pathogens. | Effluent production with toxic characteristics, high chemical and biological oxygen demand. Neutralization of digestate is necessary, i.e., mixing with other substrate. | Potassium hydroxide 2–8 M 20°C 20 days | 600 mL CH4 g–1 VS in 42 days of digestion with KOH 2M. | Arias et al., 2018 | |
| Thermal | Manure | Promote the solubilization of cellulose and hemicellulose, increase in the total concentration of volatile fatty acids, and the hydrolysis of protein | High energy consumption | Continuously stirred tank reactors 70 ± 1°C, 1–4 days | 281.6 mL CH4 g–1 VS in 22 days of digestion, with 3 days of pretreatment | Wu J. et al., 2017 |
| Carcasses | Effective pathogen inactivation. Decomposes organic matter in the solid phase. | Proteins are difficult to decompose, risking ammonium inhibition. | 250 g carcasses 170°C, 30 min | 236 mL CH4 g–1 VS in 25 days | Xu et al., 2018 | |
| Enzymatic | Manure | High conversion of carbohydrate and protein. Facilitates the acidogenesis step. | High mineral content and salinity (13 g L–1) | Stainless steel reactor 30–90°C Enzymes used: Delvolase; Delvozyme L; Filtrase NL; Bakezyme | 36% increase in CH4 yield | Wang et al., 2015 |
| Carcass | Accelerate biomethane fermentation reaction | Accumulation of organic acids results in excessive acidification and slows the methane production rate | pH 6.5–9.0 Enzyme concentration (Porcine Trypsin) 0.5–2.5% 40°C, 24 h | 104.59 mL CH4 L–1 of substrate in 23 days | He et al., 2019 | |
| Electrolysis cell | Manure | Electrolysis cell design is simple and can achieve high biofuel rates. | A large percentage of electrons are not successfully transferred to the current. Promising for the production of biohydrogen, but is not viable for biogas | Electrolysis cells: platinum cathode and graphite fiber anode, enriched with exoelogenic bacteria. 16–184 h 30°C. Current: 0.5 V. | 14% increase in CH4 and 64% increase in H2 | Wagner et al., 2009 |
| Flocculation and Sieving | Manure | Remove the organic load and nutrients and simple to operate. Increases manure biodegradability. | Use of pretreatment chemical compounds that may affect the later stage of anaerobic digestion | Flocculation with commercial polymer (Chemifloc CV/300), and subsequent sieving (0.25 mm). | 75.4% increase in CH4 | González-Fernández et al., 2008; Wang D. et al., 2019; Wang L. et al., 2019 |
| Grinding | Carcass | The digester needs to be emptied less frequently. Reduces the collection frequency and improves final product biosafety. | Not effective for pathogen control and features high power consumption. | 13 mm and 4 mm double grinding | 53.7% increase in CH4 | Kirby et al., 2018 |
| Ultrasound | Manure | Increases solubilization of organic matter, nitrogen and ammonia. It promotes particle disintegration, reduces bound protein and increases soluble protein. | High energy, reduces the efficiency of CH4 production, due to the formation of inhibitors | Ultrasonic probe (500 W, 20 kHz) Sonication pulses: 2 on 2 s 30°C | 28% increase in CH4 | Elbeshbishy et al., 2011 |
| Carcasses and manure (co-digestion) | Increases hydrolysis rate, methane production and inoculum methanogenic activity. Removal of volatile solids. | Release of flocculating agents and lignin compounds that decrease hydrolysis rate | Ultrasonic processor (30 kHz) 22 ± 5°C using specific energy inputs of 1000 kJ/kgTS 109 days | 340 m3 CH4 t–1 VS | Luste et al., 2012 | |