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Molybdenum Solvent Extraction (Organic Phase) Storage & Tank Compatibility

Storing Molybdenum Solvent Extraction (Organic Phase)? Start Here

Molybdenum solvent extraction (SX) is a hydrometallurgical purification step that recovers and concentrates molybdenum(VI) from acidic leach or process liquors. The working fluid is not a single compound but an engineered organic phase: an amine extractant (commonly a tertiary or secondary trialkylamine) dissolved in an aliphatic kerosene diluent, with a phase modifier such as tributyl phosphate or a long-chain alcohol added to prevent third-phase formation. In the mixer-settlers this organic is repeatedly contacted with the aqueous feed, becoming the "loaded organic" before molybdenum is stripped back into an alkaline solution. Because the bulk of the fluid is a flammable petroleum diluent carrying organic extractants, materials of construction (MOC) are governed by hydrocarbon resistance and flammability — not by aqueous corrosion alone. Choosing the wrong tank material leads to swelling, permeation, and seal failure, so the organic circuit relies on lined steel, FRP, or stainless rather than commodity plastic.

Is Polyethylene (HDPE / XLPE) Safe for the SX Organic Phase?

No — polyethylene is not recommended for the molybdenum SX organic phase. The fluid is dominated by an aliphatic kerosene diluent plus organic modifiers (TBP or alcohols) and dissolved amine extractant. While HDPE shrugs off brief splashes of fuels, continuous contact with kerosene-grade aliphatic hydrocarbons and organic solvents causes polyethylene to absorb the solvent, swell, soften, and lose mechanical strength, and lets vapors permeate the wall. Crosslinked polyethylene (XLPE) is more rigid but is subject to the same permeation and swelling and is likewise not rated for sustained hydrocarbon-solvent storage. For the organic circuit, specify lined carbon steel, FRP (vinyl ester or dual-laminate), or stainless steel with PTFE/FKM (Viton) seals. Polyethylene should only be considered for separate aqueous duties (e.g., dilute aqueous strip make-up) and only after confirming the actual chemistry against a current SDS and the resin maker's resistance chart.

Material compatibility at a glance

This is a non-aqueous hydrocarbon process stream, not a water-based chemical. The kerosene diluent and organic modifiers permeate and swell polyethylene, so HDPE/XLPE tanks are unsuitable for the loaded/stripped organic phase. Standard materials of construction are lined carbon steel, FRP (vinyl ester or dual-laminate), or stainless steel, with PTFE/FKM seals. Polyethylene may still serve adjacent aqueous duties only after independent verification.

MaterialRatingNote
HDPE / XLPEUAliphatic kerosene diluent and organic modifiers permeate and swell polyethylene under continuous contact; not recommended for the SX organic stream.
Carbon steel (lined)SCommon for organic mixer-settlers; internal lining protects against trace acid carryover and entrained aqueous.
Stainless steel (304/316)CUsed where trace chloride/acid is controlled; 316 preferred if any chloride present.
FRP (vinyl ester / dual-laminate)SWidely used for SX vessels and launders; verify resin rating against the specific diluent.
PTFE / FKM (Viton)SPreferred elastomer/gasket choice for hydrocarbon + amine service.
EPDMUSwells severely in aliphatic/aromatic hydrocarbons; avoid for seals in organic service.
PolypropyleneUSimilar hydrocarbon permeation/swelling concerns as polyethylene for continuous contact.

Ratings: S suitable · C conditional / limited · U unsuitable. Verify against the cited resistance charts and your concentration/temperature before specifying.

The safety that actually matters

  • Flammable liquid (H226): the kerosene diluent has a flash point near 38-65°C; keep away from heat, sparks, and open flame, and bond/ground transfer equipment.
  • Aspiration hazard (H304): may be fatal if swallowed and entering the airways — do NOT induce vomiting; this is the most serious acute hazard of hydrocarbon diluents.
  • Vapor and respiratory effects (H336): vapors may cause drowsiness or dizziness; provide local exhaust ventilation in mixer-settler areas.
  • Skin and eye irritation (H315): prolonged contact degreases and irritates skin; wear chemical-resistant nitrile/Viton gloves, goggles, and apron.
  • Acidic aqueous carryover: entrained feed/raffinate can be strongly acidic and chloride-bearing — protect against trace acid corrosion and crud build-up.
  • Static and crud control: manage organic-aqueous interface crud, secondary containment, and vapor accumulation; values above are representative and must be confirmed against the project SDS.

Common questions

Can I store the molybdenum SX organic phase in an HDPE or XLPE tank?
No. The organic phase is a kerosene-diluent solvent stream that permeates and swells polyethylene under continuous contact. Use lined carbon steel, FRP (vinyl ester or dual-laminate), or stainless steel with PTFE/FKM seals instead.
Why is polyethylene fine for some fuels but not for this?
Polyethylene tolerates brief splashes of fuels, but the SX organic is in sustained contact and also contains organic modifiers and extractants. Long-term aliphatic-hydrocarbon and solvent exposure causes absorption, swelling, softening, and permeation, which commodity poly tanks are not rated to withstand.
What tank material is recommended for the SX circuit?
Industry practice for the organic mixer-settlers and storage is lined carbon steel, FRP, or stainless steel. Match the FRP resin and any elastomer seals (PTFE or FKM/Viton) to your specific diluent and confirm against a current SDS.
Is the contacted aqueous (feed/raffinate) side different?
Yes. The aqueous leach liquor and raffinate are typically acidic and may carry chloride; those streams have their own MOC considerations (lined steel or FRP). Polyethylene for any aqueous duty must be verified independently against the actual chemistry.
Recommended Build

How we build Molybdenum Solvent Extraction (Organic Phase) storage

Molybdenum Solvent Extraction (Organic Phase) is a flammable solvent that permeates polyethylene. It is built in listed steel or stainless, bonded and grounded.

Get an Engineering Quote →or call 866-418-1777MOC verified before fabrication · nationwide freight

Sources & References

All compatibility ratings, hazard classifications, and chemical identifiers on this page are sourced from authoritative third-party publications. Verify against the original references before final specification.

  1. NFPA 704: Standard System for the Identification of the Hazards of Materials for Emergency Response — Defines the health/flammability/reactivity (and special) hazard diamond; values cited here are representative of the kerosene diluent that dominates the organic phase. www.nfpa.org
  2. CAMEO Chemicals (NOAA) — KEROSENE — NFPA 704 ratings Health 2, Flammability 2, Reactivity 0; flash point approx. 95-145°F; used as the basis for the diluent-dominated organic phase. cameochemicals.noaa.gov
  3. UN GHS (Globally Harmonized System of Classification and Labelling of Chemicals), Rev. 10 — Source for pictograms and H-statements (H226, H304, H315, H336); final classification is SDS-dependent for the specific blend. unece.org
  4. Chemical Resistance of High and Low Density Polyethylene (Cipax resistance chart) — Polyethylene resistance reference; aliphatic hydrocarbon solvents cause swelling/permeation of PE under sustained contact, supporting the U rating. cipax.com
  5. Poly Processing — Crosslinked Polyethylene Storage Tanks: Chemical Incompatibilities — Explains hydrocarbon/solvent permeation and swelling limits of XLPE tanks, reinforcing that solvent-borne organic streams are unsuitable for poly. blog.polyprocessing.com
  6. Study of molybdenum extraction by trioctylamine and tributylphosphate and stripping by ammonium solutions (Hydrometallurgy) — Formulation source: trioctylamine extractant with tributyl phosphate modifier in kerosene diluent (e.g. ~4% TOA, 12% TBP, 84% kerosene), stripped with ammonium solution. www.sciencedirect.com
  7. Solvent extraction of molybdenum (VI) by diisododecylamine from sulphuric acid solution (Hydrometallurgy) — Confirms amine extractant in kerosene-type diluent recovering Mo(VI) from acidic (sulphuric) feed; supports acidic aqueous-phase MOC note. www.sciencedirect.com