Abstract
The environmental consequence of meeting the planet’s energy requirements has shown that biological degradation of organic constituent from wastewater does not only produces biogas. It also produces flammable methane that has 21 times more global warming potential or greenhouse effect than carbon dioxide. This becomes a loss of potential renewable energy when it is flared. This study investigates recoverable energy from cassava wastewater and effect of unrecovered onsite (not from treatment plant) wastewater energy. Sludge from both onsite untreated and offsite treated wastewater from a cassava processing station in a sub urban community of Nigeria was analyzed. The result shows that the offsite treatment has a methane potential of 27.428 m3/day compared to the onsite methane emission potential with 17.807 m3/day. The onsite 17.807 m3/day of methane is equivalent to 0.126 kgCH4/year of emitted methane base on industrial procedure standards by the IPCC (2006) guidelines for national greenhouse gas inventories. An additional 54.03% of methane will be recovered if the onsite emissions were to be captured . At an emission efficiency of 0.025 kgCH4/kg COD, the untreated wastewater indicates a potential contribution to the greenhouse effect. A mathematical model analysis was presented for ease in determining the amount of methane emitted from the untreated wastewater. This study support suggested methodologies and previous work comparing anaerobic offsite methane potential and untreated wastewater methane emission potentials along with its greenhouse effects.
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Notes
The inventory year is a 1 year period when information of collected data on a particular type of waste (e.g. waste water) from a particular waste generation source (e.g. cassava processing or households) are noted and accounted for. The units (kg CH4/year, kg COD/year and kgCH4/kg COD) are given for this period.
Abbreviations
- B 0 :
-
Maximum CH4-producing capacity (kg CH4/kg COD)
- BOD:
-
Biological oxygen demand (g/m3)
- CF:
-
Theoretical conversion factor for methane in anaerobic treatments
- ECH4 :
-
Methane emissions in inventory year, (kg CH4/year)
- COD:
-
Chemical oxygen demand (g/m3)
- \( V_{{{\text{CH}}_{4} }} \) :
-
Volume of methane produced at standard condition (m3/day)
- EF i :
-
Emission factor for industry i, (kg CH4/kg COD)
- EF j :
-
Emission factor for each treatment/discharge pathway or system, (kg CH4/kg COD)
- GHG:
-
Greenhouse gas
- GWP:
-
Greenhouse warming potential
- H :
-
Tank height (m)
- HRT:
-
Hydraulic retention time (h)
- i :
-
Industrial sector
- j :
-
Each treatment/discharge pathway or system
- K d :
-
Endogenous coefficient per day
- MCF j :
-
Methane correction factor
- OLR:
-
Organic loading (kg/m3/day)
- P x :
-
Net mass of cell tissue produce per day (kg/day)
- Q :
-
Flow rate (m3/day)
- R :
-
Fraction of COD removed (%)
- R i :
-
Amount of CH4 recovered in inventory year (kg CH4/year)
- S i :
-
Organic component removed as sludge in inventory year (kg COD/year)
- SRT:
-
Solid retention time (d)
- TOW i :
-
Total organically degradable material in wastewater from industry I in inventory year, (kg COD/year)
- TSS:
-
Total solid retention (g/m3)
- Up:
-
The up-flow velocity (m/h)
- V R :
-
Tank volume (m3)
- Y :
-
Yield coefficient, gvss/gbCOD
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Omojaro, P.A. Energy analysis for onsite and offsite suburban wastewater. Environ Dev Sustain 13, 519–533 (2011). https://doi.org/10.1007/s10668-010-9274-4
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DOI: https://doi.org/10.1007/s10668-010-9274-4