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Fumasep FAA-3-20
Fumasep FAA-3-20

Fumasep FAA-3-20

Fumasep FAA-3-20 Specification

  • Material
  • Polymer Blend (Anion Exchange Membrane)
  • Application
  • Fuel Cells, Electrolyzers, Redox Flow Batteries, Electrodialysis
  • Chemical Composition
  • Fluorinated polymer backbone with quaternary ammonium functional groups
  • Shape
  • Flat Sheet / Membrane
  • Density
  • 0.95 Gram per cubic centimeter(g/cm3)
  • Ion Exchange Capacity (IEC)
  • 1.82.2 mmol/g
  • Color
  • Light Yellow
  • Reinforcement
  • Unreinforced
  • Uptake (Water Uptake at 25C)
  • 3055 wt%
  • Conductivity (Cl- form, 25C)
  • >15 mS/cm
  • Thickness (dry)
  • 20 2 m
  • Dimensional Stability
  • Good (minimal swelling in water)
  • Storage Conditions
  • Store at 530C in sealed packaging
  • Permeability
  • Low crossover for vanadium and bromine species
 

Fumasep FAA-3-20 Trade Information

  • Payment Terms
  • Paypal
  • Delivery Time
  • 15 Days
  • Main Export Market(s)
  • Asia
  • Main Domestic Market
  • All India
 

About Fumasep FAA-3-20

Brand: FuMA-Tech
Product Code: 5041688

 

Fumasep FAA-3-20 is a non-reinforced Anion ExchangeMembrane (AEM) with very low resistance, high selectivity and highstability in pH acidic and basic environment. The polymer backbone forthis AEM is based on a hydrocarbon polymer material.

Fumasep FAA-3-20 membrane comes in a 20cm x 30cm sizesheet. The membrane is delivered in dry form and is the thin brown foil.

Fumatech membranes are highly sensitive to differences inhumidity and moisture content. Therefore the membranes can vary +/- 0.5cm fromthe original cut sizes. Also due to this sensitivity the manufacturer expectswrinkles to form, however soaking the membranes in deionized water will returnthe membranes to the full size planar state according to the manufacturer.

 

Fumasep FAA-3-20 Features:

Applications: Alkaline fuel cells without KOH or at lowKOH concentration. This membrane can also be used for other electrochemicalapplications that require the transfer of anions such as Cl-, Br-, sulfate, andetc.
 Anion Exchange Membrane (AEM)
 Stability Range for pH: 1 - 14
 Thickness: 18 - 22 micrometers (0.709 -0.866 mil)
 Size: 20cm x 30cm

 

Handling:

Keep membrane package closed / sealed when unused. Unpackmembrane only for direct use and process immediately after opening. Store,handle and process the membrane in a clean and dust-free area. Always wearprotective gloves when handling the membrane. Handle with care, be sure not topuncture, crease or scratch the membrane, otherwise leaks will occur. Allsurfaces which may get into contact with the membrane during inspection,storage, pretreatment and mounting must be free of sharp edges or angles.

Storage:

Dry form: Storage for long time scale (> 12 month) maybe done in dry state (sealed container). Wet form: Storage for short and mediumtime scale (hours up to several weeks) may be done in unsealed containers in0.5 1.5 wt% NaCl solution or comparable neutral pH electrolytes. For storageover a longer time period a sealed container is recommended using afore saidelectrolyte with ca. 100 ppm biocide (NaN3) to avoid biological fouling.

 

Pre-Treatmentand Conditioning:

The membrane is delivered in bromide form and dry form.Depending on application and cell design, assembling is possible in dry form(without pretreatment) or wet form. Before assembling in wet form put themembrane sample between stabilizing meshes / spacers (in order to avoidcurling) in NaCl solution - e.g. 0.5 M NaCl solution at T = 25 C for 72 hrsexchanging the solution several times. Do not let the membrane dry out sincemicro-cracks may likely occur during shrinkage.

For standard alkaline fuel cell / electrolysisapplications, the membrane should be converted into OH-form by treating it with0.5 1.0 M NaOH or KOH solution: Put the membrane sample in an aqueoussolution of 0.5 1.0 M NaOH or KOH for at least 24 h at 20C 30C. Afterrinsing with demineralised water (pH ~ 7) the membrane is ready to use. Useclosed container to avoid CO2 contamination (carbonate formation that mayaffect conductivity). The membrane in OH-form must be stored under wet /humidified and CO2-free conditions, avoid drying out of the membrane inOH-form. Long-term storage in dry conditions should be preferably done incarbonate, Cl- or Br-form.

For electrochemical CO2 reduction applications, theanion exchange membrane should be converted to the carbonate or bicarbonate formby treating the membrane initially with 0.1 to 0.5 M KOH or NaOH solution andthen with 0.1 to 0.5 M water soluble carbonate or bicarbonate salt solutions(such as potassium carbonate or potassium bicarbonate that is dissolved inde-ionized water or distilled water).  Fully submerging the anion exchangemembrane into KOH or NaOH solution for 6 to 12 hours and then to the desiredcarbonate or bicarbonate salt solution for a period of 48-72 hours would besufficient to fully convert the membrane into either carbonate or bicarbonateform.  After rinsing the membrane (which is in the carbonate form) withdeionized water or distilled water, it can be assembled inside theelectrochemical setup for electrochemical CO2 reduction experiments. Whilethe submersion of the membrane into the KOH or NaOH can be skipped, for suchsituations, a longer submersion time may be required in order to fully convertthe membrane to carbonate or bicarbonate form.  Initial conversion to OH- formsignificantly improves the carbonate ion exchange process due to expanded poresizes.

For otherelectrochemical (electrodialysis, desalination, electro-electrodialysis,reverse electrodialysis, acid recovery, salt splitting, etc.) andnon-electrochemical applications, the membrane should be converted into theanionic form that is relevant for the intended application.  For example,if the application is requiring the Cl- anions to be transferred through themembrane, then this anion exchange membrane needs to be converted into the Cl-form.  In order to convert this membrane into Cl- form, it needs to besubmerged into a 1-2 M salt solution of NaCl or KCl (dissolved in deionizedwater) for a period of 24-72 hours and then rinsed with deionized water toremove the excess salt from the membrane surface.  Or if the intendedapplication is requiring to transfer sulfate anions, then this anion exchangemembrane needs to be converted into the sulfate form prior to its assembly intothe cell.  A neutral salt solution of Na2SO4 or K2SO4 wouldusually be sufficient to achieve the full conversion of membrane into thesulfate form after fully submerging the membrane into the salt solution for24-72 hours at room temperature.

 



Superior Conductivity and Stability

Fumasep FAA-3-20 offers exceptional ionic conductivity, exceeding 15 mS/cm in chloride form at 25C. Its robust polymer blend, combined with quaternary ammonium functional groups, helps maintain excellent dimensional stability in aqueous environments. The membrane resists swelling and ensures steady performance, making it well-suited for demanding devices such as fuel cells and electrolyzers.


Versatile Application Range

Designed for fuel cells, electrolyzers, redox flow batteries, and electrodialysis, Fumasep FAA-3-20 provides reliable anion exchange properties that fit a broad spectrum of energy and separation technologies. Its flat sheet shape and flexibility, along with its good water uptake characteristics, make it easy to incorporate into various system architectures.


Material Benefits and Handling

The fluorinated polymer backbone in Fumasep FAA-3-20 offers chemical resilience and thermal stability. With a density of 0.95 g/cm3 and minimal swelling in water, the membrane is easy to handle during installation. It should be stored in sealed packaging between 5 and 30C to retain its functional integrity and maximize shelf life.

FAQ's of Fumasep FAA-3-20:


Q: How should Fumasep FAA-3-20 membranes be stored for optimal preservation?

A: Fumasep FAA-3-20 should be stored in sealed packaging at temperatures between 5C and 30C. This prevents moisture loss or contamination and ensures the membrane maintains its chemical and physical properties until use.

Q: What unique benefits does Fumasep FAA-3-20 offer in fuel cell and battery applications?

A: The membrane has low crossover for vanadium and bromine ions, excellent conductivity, and good dimensional stability, which together enhance efficiency, prevent unwanted species migration, and contribute to longer system lifespans.

Q: When is Fumasep FAA-3-20 recommended for use in electrochemical processes?

A: This membrane is ideal for continuous or cyclic operation in fuel cells, electrolyzers, redox flow batteries, and electrodialysis systems when high ionic conductivity and minimal swelling are critical for system performance.

Q: Where can Fumasep FAA-3-20 be sourced within the United States?

A: The membrane is available through a range of channels including distributors, manufacturers, retailers, suppliers, and traders throughout the United States. It is commonly distributed in flat sheet format suitable for industrial and laboratory applications.

Q: What is the process for integrating Fumasep FAA-3-20 into an energy system?

A: Fumasep FAA-3-20 is cut to size and installed as a flat sheet within membrane electrode assemblies. Its flexibility and stable structure help simplify handling and integration into fuel cells, batteries, and electrodialysis stacks.

Q: How does the fluorinated polymer backbone benefit the membrane's performance?

A: The fluorinated polymer backbone enhances chemical resistance and thermal stability, ensuring durability in harsh chemical environments and under thermal stress, which is essential for long-term operation.

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