FIG 2 · INNOVATION ENERGY TECHNOLOGY CORP.PROPOSED — ILLUSTRATIVE

Precursor Line — Iron Phosphate (Cross-Section)

Precursor Line · Iron Phosphate (Single Line)

Hover / tap a block to highlight it · Use ← → keys to step through stages. One scale per figure.

FEED ①REACTOR ②FILTER ③WASH ④DRYER ⑤CALCINER ⑥NH₃ / (NH₄)₂SO₄ ⑦QC ⑧SINGLE-LINE SCALE: one precursor line — counts / sizes illustrative
Feed Reaction Filtration Wash Dry Calcine Recovery
  1. Line scale: one precursor line. Do not read plant-scale totals from this figure.
  2. Solid path: ①→②→③→④→⑤→⑥→ QC. Liquid path: ③ filtrate → ⑦ neutralization → recovery.
  3. Calcination is optional per the user's process file; Fig 2 shows it as an optional station.
  4. All equipment sizes / counts are illustrative.
Proposed — Illustrative. This is a proposed plant, not an existing factory. Layout, equipment counts and building sizes are illustrative and subject to engineering design. Temperatures quoted are literature ranges for LFP processing, not project specifications. No team portraits. Customers shown per user confirmation as confirmed, labeled “Pending legal review” where applicable — no new customer claims added.
Sources: User file ManufacturerMethod.html (ammonia route); MRS Communications LFP manufacturing review (solid-state, roller hearth kilns, 600–800 °C calcination); public patent literature on FePO₄ precipitation / filtration / washing / drying / calcination.