Fluxara Advanced Renewables Plant Graphics · DPR v17 · September 2026
3 Graphics
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Circular Chemistry — NaOH Recovery Loop

Rice husk combustion provides both the CO₂ and the thermal energy. The NaOH leachant is recovered at 82% efficiency via causticisation — simultaneously producing Nano-PCC as a mandatory co-product. No chemical is purchased twice.

Fluxara Circular Chemistry — NaOH Recovery Loop Diamond-layout process flow showing the four main reactions: Combustion, Leaching, Precipitation, and Causticisation forming a closed NaOH recovery loop RHA 23 MT/day + 199 GJ/day heat Na₂SiO₃ solution Na₂CO₃ (spent NaOH) NaOH Recovered 82% efficiency CO₂ 14.2 MT/day internal flue gas · zero cost COMBUSTION FURNACE Rice Husk → RHA + CO₂ 20 MT/day RH combusted · ≤700°C Bonus RHA 3.6 MT/day · THU 180–220°C 🔥 LEACH REACTORS RHA + 2NaOH → Na₂SiO₃ 10% NaOH · 90°C · 2hr · SS reactors 3 × 15 KL PP-lined · SiO₂ extraction 88% PRECIPITATION & DRYING Na₂SiO₃ + CO₂ → SiO₂↓ + Na₂CO₃ pH 5.5–9 · 50–70°C · MVR + Spray Dryer Output: 20 MT/day PS · BET 140–175 m²/g 💧 CAUSTICISATION Na₂CO₃ + Ca(OH)₂ → NaOH + PCC CaO slaked on-site · draft-tube causticiser Output: 30 MT/day PCC · 0.5–2 µm d50 CLOSED-LOOP RECOVERY 82% NaOH recovered & reused PS 20 MT/day · PCC 30 MT/day CO₂ cost: ₹0 (internal capture) Break-even at 33% utilisation Rice Husk 20 MT/day ₹5,500/MT Purchased RHA 19.4 MT/day · ₹750/MT NaOH Makeup 6.7 MT/day · 18% loss CaO Quicklime 20.5 MT/day · slaked on-site PS PRODUCT ₹42–144/kg export 6,600 MT/yr PCC PRODUCT ₹10–42/kg 9,900 MT/yr Desilicated residue 4.4 MT/day → brick kilns ₹900/MT FLUXARA · CIRCULAR BIOREFINERY CHEMISTRY · DPR v17
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Process Flow Diagram

Six-stage continuous process operating 24×7 across three 8-hour shifts. MVR is mandatory from Day 1 — without it the thermal balance is negative. The NaOH recovery arrow (bottom) reduces NaOH consumption from 37 MT/day gross to 6.7 MT/day fresh makeup.

Fluxara Process Flow Diagram THERMAL LANE MAIN PROCESS LANE NaOH RECOVERY LANE ZLD / WATER RECOVERY FURNACE + THU (Therminol 55) 20 MT/day RH · ≤700°C · 199 GJ/day CO₂ flue gas 25 MT/day generated → 14.2 MT/day to precipitation 199 GJ/day heat via THU oil circuit → MVR + Evaporation 600 kWp Solar PV + 750 kW HT Grid 946,080 kWh/yr · net ₹2.38 Cr/yr electricity RHA STORAGE 23 MT/day total 19.4 purch + 3.6 bonus LEACH REACTORS ×3 15 KL PP-lined SS · 90°C · 2 hr SiO₂ + 2NaOH → Na₂SiO₃ Extraction efficiency 88% FILTER PRESS 1200mm PP Residue → kilns 4.4 MT/day residue → ₹900/MT PRECIPITATION ×3 Na₂SiO₃ + CO₂ → SiO₂↓ + Na₂CO₃ pH 5.5–9 · 50–70°C · HDPE lined CO₂ from furnace flue · zero purchase MVR EVAP 65% energy saving 89.6 GJ/day evap ⚠ MANDATORY DAY 1 FILTER ×2 PS slurry wash → Na₂CO₃ filtrate Na₂CO₃ filtrate → Causticiser SPRAY DRYERS ×3 SS304/316L · Inlet 280°C CTAB HDS treatment 23.1 GJ/day thermal PS PRODUCT NaOH lye 14 MT/day (48%) CaO SLAKER CaO + H₂O → Ca(OH)₂ 20.5 MT/day CaO CaO 20.5 MT/day · ₹6,000/MT DRAFT-TUBE CAUSTICISER Na₂CO₃ + Ca(OH)₂ → 2NaOH + CaCO₃↓ 82% NaOH recovery · PCC nano-crystal nucleation PCC FILTER CaCO₃ slurry wash PCC COAT & DRY Stearic acid / OCC coating 0.5–2 µm d50 · sealant/plastics grade PCC PRODUCT 30 MT/day → 9,900 MT/yr ↺ NaOH RECOVERED — 82% ZLD PLANT UF → RO → MEE → ATFD 80% water recovery · 130 KLD net Process water → ZLD Recycled water 80% FLUXARA · PROCESS FLOW DIAGRAM · 20 MT/DAY PS + 30 MT/DAY PCC · DPR v17
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Isometric Plant Layout — Phase 1 (6 Acres)

Kothakota, Wanaparthy, Telangana. Phase 1 occupies the northern 6 acres of the 12-acre site. Phase 2 land bank (southern 6 acres) reserved for the second furnace from Y2+ accruals. All buildings in RCC frame construction. Process Hall and Furnace in fire-rated RCC — not PEB.

Fluxara Isometric Plant Layout