Fig. 1

Fig. 2

Fig. 3

Bioreactor conditions to monitor methane generation
| Source of sludge | SEP WWTP |
| Source of inoculum | Digestate from SEP WWTP biogas digester |
| Inoculum: Substrate ratio | 20%:80% |
| Bioreactor pH | pH 7.1–7.3 |
| Bioreactor volume | 400 ml |
| Residence time | 21 days |
| Study temperature | 38°C |
| Mixing conditions | Manually, once every 24 h |
Preliminary economic analysis of incorporating e-beam technology for sludge hygenization solely compared with incorporating e-beam technology for sludge hygenization and biogas cogeneration
| Wastewater treatment plant | |
|---|---|
| I. E-beam technology for sludge hygenization | II. E-beam technology for sludge hygenization and biogas cogeneration |
| Accelerator specification | |
| 100 kW, 2 MeV | 100 kW, 2 MeV + biogas generation |
| Cost savings | |
| Savings from avoiding sludge disposal costs | |
| 1500 tons @ 100 euros = 150 000 euros | 1500 tons @ 100 euros = 150 000 euros |
| Potential revenue from biosolid-based fertilizer sales | |
| 1500 tons @ 94.5 euros = 141 750 euros | 1277.5 tons @ 94.5 euros = 120 723.75 euros |
| Biogas production (1 022 000 m3 annually) | |
| E-beam technology-associated operating costs | |
| Electricity consumption | |
| 130 kW e-beam accelerator | 130 kW e-beam accelerator |
| 70 kW wastewater plant equipment | 70 kW wastewater plant equipment |
| 10 kW heat generation | |
| Total cost | |
| 210 kW × 8000 h × 0.13 euros/kwh = 218 400 euros | 200 kW × 8000 h × 0.13 euros/kwh = 208 000 euros |
| Net income and savings | |
| 73 350 euros annually | 271 668.75 euros annually |
Cumulative SCOD (mg/L) and methane volumes generated (ml/kg TS) as a function of e-beam dose
| Experiment | Dose (kGy) | Volume of biogas produced after 21 days (ml/kg TS) | t-test | SCOD (mgO2/L) before the fermentation | t-test |
|---|---|---|---|---|---|
| H1 | 0 | 118.842 ± 721 | t = −27.0145 | – | |
| 1 | 138.602 ± 1630 | p = 0.0014 | – | ||
| H2 | 0 | 145.822 ± 1003 | t = 0.4654 | 4993 ± 24 | t = −18.0121 |
| 2 | 144.447 ± 6074 | p = 0.6874 | 5754 ± 59 | p = 0.0031 | |
| H3 | 0 | 64.374 ± 910 | t = −7.2157 | 318 ± 0 | t = −664.0 |
| 3 | 76.844 ± 3647 | p = 0.0187 | 1425 ± 3 | p = 0.000002 |