FIG 1 · INNOVATION ENERGY TECHNOLOGY CORP.PROPOSED — ILLUSTRATIVE

Plant Overview — Proposed 50,000 t/yr LFP Cathode Plant

Plant Overview · Cross-Section · Proposed 50,000 t/yr LFP Cathode Plant

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

How to read this figure: the isometric drawing above shows the site layout (where each hall sits); the Section A–A′ strip below shows the process profile in cross-section — material flows left → right above ground, while the utilities spine runs below grade and serves both halls. Side streams (filtrate, wash water) leave the main line to the recovery / MVR block and return as recovered water and ammonium sulfate.

RAW MAT. ①PRECURSOR HALL ②CATHODE HALL ③UTILITIES ④WASTEWATER / MVR ⑤WAREHOUSE ⑥OFFICE ⑦ filtrate → IN → RAW ① → PRECURSOR ② → CATHODE ③ → WAREHOUSE ⑥ → OUT (illustrative flow)

SECTION A–A′ · PROCESS PROFILE (Cross-Section: Process Flow and Layers)

① RAW RECEIVINGFeSO₄ + MAP + Li / Csilos · QC sampling ② PRECURSOR HALLreact → filter → wash→ dry → calcine (opt.) ③ CATHODE HALLmix → sinter → mill→ coat → pack ⑥ WAREHOUSELFP powder · FePO₄(NH₄)₂SO₄ by-product GROUNDABOVE GROUND · PROCESS ④ UTILITIES SPINE — water / ammonia / nitrogen / steam / power BELOW GRADE · UTILITIES ⑤ WASTEWATER / MVR — filtrate → neutralization → (NH₄)₂SO₄ recovery · wash water → reuse Target: 50,000 t/yr LFP cathode (proposed). Building sizes, line counts and equipment counts are illustrative.
Raw Precursor Cathode Recovery Utilities Main flow Side stream: filtrate → recovery
  1. Site scale: whole plant — do not read line-scale details from this figure; see Figs 2–4.
  2. Flow runs left → right: raw → precursor → cathode → warehouse. The section strip shows the same flow in cross-section.
  3. Utilities spine (④–⑤) serves both halls; the circular ammonia / water loop is detailed in Fig 4.
  4. Consistent target across all figures: 50,000 t/yr LFP cathode (proposed). Line counts / building sizes 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.