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Created with Pixso. Advanced Battery Material Packaging FIBC 500kg Type D Static Dissipative Moisture Barrier for Lithium-Ion NMC

Advanced Battery Material Packaging FIBC 500kg Type D Static Dissipative Moisture Barrier for Lithium-Ion NMC

Brand Name: Sinopack
Model Number: BMP-FIBC-500-NMC
MOQ: 100 Pieces
Price: USD 18.00-48.00 / Piece
Delivery Time: 15-25 working days after order confirmation
Payment Terms: T/T, L/C at sight
Detail Information
Place of Origin:
Shandong, China
Certification:
UN 13H3/Y Available, IEC 61340-5-1, ISO 9001:2015
Static Protection:
Type D Static Dissipative — No External Grounding Required
Surface Resistivity:
10⁸-10¹⁰ Ω (Inner Surface), Corona Discharge Network
Moisture Barrier (WVTR):
<0.5 G/m²/24h (38°C, 90% RH)
Cathode Material Compatibility:
NMC (111, 532, 622, 811), LFP, LCO, NCA, LMO
Safe Working Load:
250-500 Kg (Conservative Rating For High-Value Material)
Liner Construction:
Anti-Static PE 100μm / Aluminum Metallized PET 12μm / PE 60μm
Metal Contamination Control:
Non-Magnetic Stainless Steel Production Tools, <1ppm Fe Contamination Limit
Traceability:
Lot-Level Traceability, CoA With Surface Resistivity And WVTR Test Data
Packaging Details:
Anti-static PE outer wrap, vacuum-sealed on conductive pallet, moisture indicator and ESD certificate included
Supply Ability:
80000 Pieces per Month
Highlight:

Battery Material Packaging FIBC

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NMC Cathode Powder Bag

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Lithium-Ion Material Logistics

Product Description

1. Problem: Metal Contamination — The Single Most Expensive Quality Failure in Battery Materials

Lithium-ion battery cathode materials — NMC (LiNiₓMnᵧCo₁₋ₓ₋ᵧO₂), LFP (LiFePO₄), and NCA (LiNi₀.₈Co₀.₁₅Al₀.₀₅O₂) — have a market value of $15-50/kg depending on composition and performance grade. A 500kg FIBC of NMC811 cathode powder is worth $15,000-25,000. The single most catastrophic quality failure is magnetic metal contamination: a single stainless steel particle (≥50μm) originating from manufacturing equipment can create an internal short circuit in a finished battery cell, leading to thermal runaway, fire, and product recall.

The battery industry's metal contamination specification is the most stringent in chemical manufacturing: <50 ppb (parts per billion) total magnetic metal, with individual particles limited to <25μm (approximately the thickness of a typical battery separator). For context, this is 100-1000* stricter than typical pharmaceutical metal limits (USP <232> limits for oral drug products: elemental iron <10,000 ppb). A single non-compliant batch of cathode powder can trigger rejection of the entire shipment, costing $75,000-125,000 per 5-tonne container in product loss plus potential liability claims if contaminated material reaches cell production undetected.

2. Cause: Multiple Metal Contamination Entry Points in the Packaging Chain

Metal contamination enters cathode powder through multiple pathways: (1) Steel production equipment — extruder screws, cutting blades, sewing needles (all typically made of hardened steel, composition Fe-Cr-Mo-V alloys) generate wear particles during normal operation. A single industrial sewing machine operating at 4,000 stitches/minute produces approximately 0.1-1.0 mg of steel wear particles per 8-hour shift from needle-fabric friction alone. (2) Environmental fallout — airborne metal particles (from nearby machining, welding, or vehicle traffic) settle on exposed fabric surfaces during manufacturing. (3) Handling tools — metal hooks, forklift tines, and conveyor components can abrade against bag surfaces, generating metal particles. (4) Cross-contamination — shared production equipment used for both battery-grade and non-battery-grade FIBCs can transfer metal particles between product runs.

The detection challenge: a 50μm stainless steel particle weighs approximately 0.5 μg. To detect this at the 50 ppb level in a 500kg batch (maximum allowable 25mg total magnetic metal), magnetic separation and microscopic counting are required — standard metal detectors (sensitivity typically 1.5mm Fe) are 30* too insensitive for battery-grade requirements.

3. Solution: Battery-Grade Clean Manufacturing Protocol

Our BMP-FIBC-500-NMC is manufactured under a battery-grade contamination control protocol. All production equipment contacting the bag interior is non-magnetic stainless steel (316L grade, <0.05% ferrite content by Ferritescope measurement) or ceramic (Al₂O₃, ZrO₂). Sewing needles are 316L stainless with a needle-use log (each needle replaced after 8 machine-hours, well before the onset of measurable wear). All cutting blades are ceramic (zirconia-toughened alumina, hardness 1300 HV) that produce zero metallic wear particles.

The production area is maintained under positive pressure with HEPA filtration (H13 grade, 99.95% at 0.3μm) to exclude airborne metal particles. Magnetic separation audit: after each production shift, the production line is vacuumed with a magnetic filter vacuum cleaner, and the collected magnetic material is weighed. Production continues only if magnetic material collected is <2 mg/shift (equivalent to <2 ppm contamination risk for the 1000kg of material processed per shift).

Each finished bag undergoes a final magnetic particle audit: a rare-earth magnetic wand (NdFeB, 12,000 Gauss surface field) is passed over the entire bag interior for 5 minutes. Any magnetic particles collected are photographed, measured, and documented. Bag acceptance requires zero magnetic particles >25μm detected. Bags failing this audit are rejected and recycled through a dedicated non-battery-grade recycling stream.

4. Application: Battery Material Supply Chains

4.1 NMC Cathode Powder from China to Gigafactories

Chinese cathode manufacturers (Ronbay, Easpring, XTC) shipping NMC powder to Tesla, CATL, LG Energy Solution, and Panasonic gigafactories in the US and Europe require packaging that meets the stringent metal contamination specifications of automotive OEM battery qualification (typically <50 ppb Fe, <25 ppb Cu, <25 ppb Zn). Our bags provide validated contamination control with lot-level audit data.

4.2 Lithium Iron Phosphate (LFP) for Energy Storage Systems

LFP cathode material for stationary energy storage has slightly less stringent contamination specifications (<100 ppb total magnetic metal) but requires the same packaging quality management approach. The increasing adoption of LFP in entry-level EVs is driving demand for battery-grade packaging.

5. How to Choose: Battery Material Packaging by Contamination Sensitivity

Material TypeMetal Contamination LimitPackaging Requirement
Anode graphite (natural/synthetic)<500 ppb FeStandard FIBC with metal detection
LFP cathode (energy storage grade)<100 ppb magnetic metalClean manufacturing, metal audit
NMC cathode (EV grade)<50 ppb magnetic metalBattery-grade clean protocol, full audit trail
Solid electrolyte (Li₇La₃Zr₂O₁₂, sulfide)<10 ppb all metalsCleanroom manufacturing + inert atmosphere

6. FAQ

Q1: How do you verify the metal contamination level of each bag?

We use a 3-stage verification: (1) Production magnetic audit — magnetic filter vacuum of the production line after each shift (acceptance <2 mg/shift), (2) Per-bag magnetic wand test — 5-minute rare-earth magnet sweep of the bag interior (acceptance: zero particles >25μm), and (3) Lot-level ICP-MS analysis — 3 bags per 500-bag lot are rinsed with 1% HNO₃, the rinse solution is analyzed by ICP-MS for Fe, Cr, Ni, Cu, Zn, and Co (reporting limit 1 ppb in solution, equivalent to approximately 5 ppb in the bag). The lot certificate reports all 6 elements. For customers requiring independent verification, we provide retained samples (sealed clean bags from each lot) that can be sent to a third-party laboratory for ICP-MS testing.

Q2: Why is Type D static dissipative used instead of Type C conductive for battery materials?

Type D is preferred for battery cathode materials for three reasons: (1) No grounding dependency — battery cathode manufacturing facilities often lack verified grounding at every packaging station, especially at pilot and scale-up production lines. Type D bags self-limit surface potential without requiring operator compliance with grounding procedures. (2) Carbon contamination risk with Type C — Type C bags use carbon-black-loaded fabric to achieve conductivity. Under mechanical stress (vibration during transport), microscopic carbon black particles can shed from the fabric and contaminate the cathode powder. Carbon is an electrochemically active contaminant in lithium-ion cells (it can participate in parasitic side reactions at the cathode-electrolyte interface). Type D bags use quasi-conductive yarns with lower carbon black loading and lower shedding risk. (3) The MIE of cathode powders is typically >10 mJ (NMC powder MIE approximately 30-50 mJ per ASTM E2019), well within Type D's safe operating range.

Q3: What is the moisture specification for battery cathode powder packaging?

NMC and NCA cathode powders are hygroscopic and react with atmospheric moisture to form LiOH and Li₂CO₃ surface species (the "residual lithium" that must be controlled <1000 ppm for high-nickel NMC). Moisture uptake also degrades the cathode's electrochemical performance during cell manufacturing (moisture reacts with LiPF₆ electrolyte to form HF, which dissolves transition metals from the cathode structure). Our moisture barrier liner (WVTR <0.5 g/m²/24h) is combined with nitrogen purging before closure and an integrated desiccant pack (500g molecular sieve, <10 ppm H₂O equilibrium at 25°C) to maintain internal humidity <100 ppm H₂O. Cathode powder filled under dry room conditions (<1% RH) into our moisture-protected bags will maintain moisture below the <500 ppm specification limit for 90+ days in sealed storage.