Anaerobic wastewater treatment utilizes complex consortia of anaerobic micro-organisms to stabilize organic matter in the complete absence of molecular oxygen. Unlike aerobic processes that require intensive energy for mechanical aeration, anaerobic digestion converts complex organic pollutants primarily into biogas, consisting mainly of methane ($\text{CH}_4$, 60%–70%) and carbon dioxide ($\text{CO}_2$, 30%–40%), while producing significantly lower excess biological sludge.
The biological conversion occurs via four sequential biochemical stages: Hydrolysis, Acidogenesis, Acetogenesis, and Methanogenesis. Methanogenesis is the rate-limiting step governed by strict anaerobes (methanogens). Stoichiometrically, the theoretical ultimate methane yield per unit of COD destroyed under standard conditions ($0^\circ\text{C}$ and $1\text{ atm}$) is derived as:
$$V_{\text{CH}_4} = 0.35 \cdot \left(\text{COD}_{\text{removed}} - 1.42 \cdot P_x\right)$$
Where $V_{\text{CH}_4}$ is the daily volume of methane gas produced ($\text{m}^3/\text{day}$), $\text{COD}_{\text{removed}}$ is the total COD mass degraded per day ($\text{kg/day}$), and $P_x$ is the net biomass synthesized per day ($\text{kg VSS/day}$). Accounting for operating operational temperatures ($T$ in Kelvin):
$$V_{\text{CH}_4(T)} = 0.35 \cdot \left(\frac{T}{273}\right) \cdot \left(\text{COD}_{\text{removed}} - 1.42 \cdot P_x\right)$$
The Upflow Anaerobic Sludge Blanket (UASB) reactor represents a high-rate anaerobic technology where influent wastewater enters from the bottom and flows vertically upward through a dense bed of self-immobilized anaerobic granular sludge. The upflow velocity ($v_u$) must be carefully balanced to maintain fluidization without washing out the sludge bed:
$$v_u = \frac{Q}{A_s} \le 1.0\text{ m/hr}$$
Where $Q$ is the influent flow rate and $A_s$ is the cross-sectional reactor area. A three-phase Gas-Liquid-Solid (GLS) separator located at the top of the reactor diverts methane gas bubbles into collection hoods while allowing clarified effluent to overflow and dense sludge granules to settle back into the digestion zone.
UASB technology gained widespread adoption across India during early river action plans (such as the Ganga Action Plan) due to low operating costs and high organic load handling capacity. However, early generation UASBs faced performance limitations during severe winter temperatures, along with incomplete nitrogen and phosphorus removal, uncaptured dissolved methane emissions, and hydrogen sulfide ($\text{H}_2\text{S}$) odor challenges.
Modern municipal wastewater projects across India are advancing traditional UASB systems into high-efficiency **Expanded Granular Sludge Bed (EGSB) Reactors** and **Internal Circulation (IC) Reactors**. These advanced setups utilize higher upflow velocities ($v_u \ge 5\text{ m/hr}$) and taller geometry to enhance liquid-granule contact and improve low-temperature treatment efficiency. Additionally, under circular economy initiatives, modern Indian STPs are integrating combined heat and power (CHP) co-generation engines to convert captured biogas into renewable electricity, self-powering plant operations while polishing UASB effluent with downstream aerobic MBBR or SBR systems to meet modern regulatory discharge limits.
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