The Fumasep FAB-PK Series includes high-performance anion exchange membranes (AEMs) reinforced with PK (polyether ketone), designed for advanced applications such as electrodialysis, bipolar electrodialysis, acid recovery, and fuel cells. These membranes offer high proton blocking capability, outstanding chemical resistance (pH 1–14), and mechanical strength.
Available models:
FAB-PK-75 (Thickness: 75 μm)
FAB-PK-130 (Thickness: 130 μm)
These membranes are dry-supplied and require careful handling and conditioning before use.
Download:
fumasep FAB-PK-130 (dry form) Technical Data Sheet.pdf
Property | FAB-PK-75 | FAB-PK-130 |
---|---|---|
Type | Anion Exchange Membrane | Anion Exchange Membrane |
Reinforcement | PK | PK |
Delivery Form | Dry | Dry |
Appearance | Brown | Brown |
Thickness (μm) | 75 | 130 |
Weight per Area (g/m²) | 60 – 90 | 100 – 140 |
Selectivity (%) | > 92 | 93 – 98 |
Area Resistance (Cl- form, Ω·cm²) | < 4 | 5.0 – 9.0 (Cl-), 10–20 (SO4²-) |
Conductivity (mS·cm⁻¹) | - | 1.0 – 2.5 (Cl-), 10–20 (SO4²-) |
Proton Transfer Rate | < 700 nmol/min/cm² | 60 – 400 µmol/min/cm² |
Young’s Modulus (MPa) | > 1000 | 1000 – 1800 |
Tensile Strength (MPa) | > 40 | 40 – 80 |
Elongation at Break (%) | > 15 | 15 – 40 |
Dimensional Swelling in H2O (%) | < 2 | 0 – 1 |
pH Stability Range | 1 – 14 | 0 – 14 |
Operational Temp. (°C) | 15 – 40 | 15 – 40 |
Burst Pressure (bar) | > 3 | > 3 |
Electrodialysis (ED)
Bipolar Electrodialysis (BED)
Acid Concentration / Recovery
Alkaline Fuel Cells
Non-Aqueous Redox Flow Batteries
Electrochemical CO₂ Reduction
Both membranes are delivered in dry Br⁻ form and require proper pretreatment:
Soak in DI water to remove residual solvents.
For electrodialysis or general use, immerse in 0.5 M NaCl at 25 °C for 24–72 hrs.
For alkaline applications (fuel cells, electrolysis):
Convert to OH⁻ form by soaking in 0.5 – 1.0 M NaOH or KOH for ≥ 24 hrs.
Rinse with deionized water before use.
For CO₂ reduction:
Soak in KOH or NaOH, then in carbonate/bicarbonate salt solution for 48–72 hrs.
Do not allow membranes to dry after activation; use in wet/humidified conditions.
Dry form (long-term): Store sealed in clean, dry, dust-free environment.
Wet form (short-term): Store in 0.5–1.5 wt% NaCl or similar solution.
Add biocide (e.g., sodium sulfite or NaN₃) to prevent microbial growth.
Q1: Are these membranes reusable?
A: Yes. With proper handling and storage, the membranes can be reused multiple times.
Q2: Do they have a front or back side?
A: No. Both sides are identical and usable.
Q3: Can the membranes be cut?
A: Yes. Use sharp tools and wear gloves to avoid creasing or contamination.
Q4: What’s the lifespan?
A: Typically 6–24 months depending on the chemical environment and operational conditions.
Q5: Are they suitable for organic solvents?
A: These membranes are not recommended for strong organic solvents like DMF or acetone. However, FAB-PK-130 is more compatible with mild organic solvents used in redox flow batteries.
Q6: Do all anions pass through equally?
A: No. Membrane selectivity allows preferential transport. Conversion into the target anion form (Cl⁻, SO₄²⁻, HCO₃⁻) is required before use.
Q7: Why does water pass through during ion migration?
A: This occurs due to electro-osmosis (hydrated ion movement) and osmotic pressure.
Q8: Why are small amounts of cations seen in anion membranes?
A: Ion-exchange membranes have >90% selectivity, so minor crossover is possible.
Property / Feature | FAB-PK-75 (Thin Membrane) | FAB-PK-130 (Thick Membrane) |
---|---|---|
Thickness | ~60–90 µm | ~110–140 µm |
Area Resistance (Cl⁻ form) | < 4 Ω·cm² (low resistance) | 5–9 Ω·cm² (slightly higher resistance) |
Selectivity | > 92% | 93–98% |
Proton Blocking Capability | High | Very high (superior for proton-sensitive applications) |
Mechanical Strength | Good but less pressure-resistant | Very high — ideal for pressurized and long-term operation |
Flexibility | More flexible, easier to cut and install | Stiffer, requires careful handling |
Solvent / Crossover Barrier | Moderate | Excellent — minimizes crossover in redox or organic systems |
Ion Transfer Efficiency | Faster response, higher efficiency | Slightly slower, but very stable |
Durability | Moderate (can degrade under harsh mechanical/chemical stress) | Long-lasting, better for aggressive or industrial environments |
Application Area | Recommended Membrane | Notes |
---|---|---|
Electrodialysis (ED), Salt Splitting, Acid Recovery | Both | Use thin membrane for low-energy systems; thick for aggressive media |
Bipolar Membrane Electrodialysis (EDBM) | FAB-PK-130 | Better for alternating pH conditions and harsh electrochemical loads |
Alkaline Fuel Cells / Electrolysis | FAB-PK-130 | Mechanical and chemical stability is crucial |
Non-Aqueous Redox Flow Batteries | FAB-PK-130 | Excellent solvent barrier and long-term mechanical integrity |
Low-concentration Salt Solutions / Extraction | FAB-PK-75 | Ideal for systems needing rapid ion transport and high efficiency |
CO₂ Electrochemical Reduction | FAB-PK-130 | Superior carbonate/bicarbonate exchange, better pH control |
Educational or Lab-Scale Testing | FAB-PK-75 | Cost-effective, responsive, easy to handle |
FAB-PK-75 (Thin)
Best suited for:
Low-pressure lab-scale testing
Fast ion exchange reactions
Energy-efficient electrodialysis systems
FAB-PK-130 (Thick)
Recommended for:
Industrial-scale or long-term systems
Harsh acidic/alkaline environments
Electrolysis, CO₂ reduction, and redox flow batteries
FuMA-Tech Anion exchange membrane series in SCI Materials Hub
FuMA-Tech AEM Series | Thickness (μm) | pH | Temperature (°C) | Counter ion | Reinforcement |
AMI-7001S | 450 | 1-10 | 90°C | -- | None |
Fumasep FAA-3-20 | 20 | 1-12 | 25 - 50°C | Br- | None |
Fumasep FAA-3-PE-30 | 26-34 | -- | -- | Br- | PE |
Fumapem FAA-3-PE-30 | 20-30 | 1-12 | 25 - 50°C | Br- | PE |
Fumasep FAA-3-50 | 50 | 0-14 | 25 - 50°C | Br- | None |
Fumapem FAA-3-50 | 50 | 1-12 | 25 - 50°C | Br- | None |
Fumasep FAA-3-PK-75 | 75 | 0-14 | 25 - 50°C | Br- | PK |
Fumasep FAA-3-PK-130 | 130 | 0-14 | 25 - 50°C | Br- | PK |
Fumasep FAAM-15 | 15 | 6-12 M KOH | 25 - 100°C | None | None |
Fumasep FAAM-20 | 18-22 | 6-12 M KOH | 25 - 100°C | None | None |
Fumasep FAAM-40 | 35-45 | 6-12 M KOH | 25 - 100°C | None | None |
Fumasep FAAM-75-PK | 60-80 | 6-12 M KOH | 25 - 100°C | None | None |
Fumasep FAB-PK-130 | 130 | 0-14 | 25 - 50°C | Br- | PK |
Fumasep FAD-55 | 55 | 1-9 | 25 - 50°C | Br- | None |
Fumasep FAD-PET-75 | 75 | 1-9 | 25 - 50°C | Br- | PET |
Fumasep FAP-450 | 50 | <4 | 25 - 50°C | None | None |
Fumasep FAPQ-330 | 30 | 1-9 | 25 - 50°C | Cl- / MeOSO3- | None |
Fumasep FAS-30 | 30 | 1-12 | 25 - 50°C | Br- | None |
Fumasep FAS-50 | 50 | 1-14 | 25 - 50°C | Br- | None |
Fumasep FAS-PET-75 | 75 | 0-9 | 25 - 50°C | Br- | PET |
Fumasep FAS-PET-130 | 130 | 0-9 | 25 - 50°C | Br- | PET |
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Model | 10×10 cm | 20×20 cm | 20×30 cm |
---|---|---|---|
FAB-PK-75 | $29 | $89 | $119 |
FAB-PK-130 | $29 | $89 | $119 |
📏 Note: All membranes are manually cut; due to moisture sensitivity, final dimensions may vary by ±0.5 cm
⚠️ Notice: These products are for industrial/lab use only and not certified for drinking water applications.
Partial references citing our materials (from Google Scholar)
Carbon Dioxide Reduction
1. ACS Nano Strain Relaxation in Metal Alloy Catalysts Steers the Product Selectivity of Electrocatalytic CO2 Reduction
The bipolar membrane (Fumasep FBM) in this paper was purchased from SCI Materials Hub, which was used in rechargeable Zn-CO2 battery tests. The authors reported a strain relaxation strategy to determine lattice strains in bimetal MNi alloys (M = Pd, Ag, and Au) and realized an outstanding CO2-to-CO Faradaic efficiency of 96.6% with outstanding activity and durability toward a Zn-CO2 battery.
2. Front. Chem. Boosting Electrochemical Carbon Dioxide Reduction on Atomically Dispersed Nickel Catalyst
In this paper, Vulcan XC-72R was purchased from SCI Materials Hub. Vulcan XC 72R carbon is the most common catalyst support used in the anode and cathode electrodes of Polymer Electrolyte Membrane Fuel Cells (PEMFC), Direct Methanol Fuel Cells (DMFC), Alkaline Fuel Cells (AFC), Microbial Fuel Cells (MFC), Phosphoric Acid Fuel Cells (PAFC), and many more!
3. Adv. Mater. Partially Nitrided Ni Nanoclusters Achieve Energy-Efficient Electrocatalytic CO2 Reduction to CO at Ultralow Overpotential
An AEM membrane (Sustainion X37-50 Grade RT, purchased from SCI Materials Hub) was activated in 1 M KOH for 24 h, washed with ultra-purity water prior to use.
4. Adv. Funct. Mater. Nanoconfined Molecular Catalysts in Integrated Gas Diffusion Electrodes for High-Current-Density CO2 Electroreduction
In this paper (Supporting Information), an anion exchanged membrane (Fumasep FAB-PK-130 obtained from SCI Materials Hub (www.scimaterials.cn)) was used to separate the catholyte and anolyte chambers.
SCI Materials Hub: we also recommend our Fumasep FAB-PK-75 for the use in a flow cell.
5. Appl. Catal. B Efficient utilization of nickel single atoms for CO2 electroreduction by constructing 3D interconnected nitrogen-doped carbon tube network
In this paper, the Nafion 117 membrane was obtained from SCI Materials Hub.
In this paper, Proton exchange membrane (Nafion 117), Nafion D520, and Toray 060 carbon paper were purchased from SCI Materials Hub.
7. National Science Review Confinement of ionomer for electrocatalytic CO2 reduction reaction via efficient mass transfer pathways
An anion exchange membrane (PiperION-A15-HCO3) was obtained from SCI Materials Hub.
8. Catalysis Communications Facilitating CO2 electroreduction to C2H4 through facile regulating {100} & {111} grain boundary of Cu2O
Carbon paper (TGPH060), membrane solution (Nafion D520), and ionic membrane (Nafion N117) were obtained from Wuhu Eryi Material Technology Co., Ltd (a company under SCI Materials Hub).
Batteries
1. J. Mater. Chem. A Blocking polysulfides with a Janus Fe3C/N-CNF@RGO electrode via physiochemical confinement and catalytic conversion for high-performance lithium–sulfur batteries
Graphene oxide (GO) in this paper was obtained from SCI Materials Hub. The authors introduced a Janus Fe3C/N-CNF@RGO electrode consisting of 1D Fe3C decorated N-doped carbon nanofibers (Fe3C/N-CNFs) side and 2D reduced graphene oxide (RGO) side as the free-standing carrier of Li2S6 catholyte to improve the overall electrochemical performance of Li-S batteries.
This paper used more than 10 kinds of materials from SCI Materials Hub and the authors gave detailed properity comparsion.
The commercial IEMs of Fumasep FAB-PK-130 and Nafion N117 were obtained from SCI Materials Hub.
Gas diffusion layers of GDL340 (CeTech) and SGL39BC (Sigracet) and Nafion dispersion (Nafion D520) were obtained from SCI Materials Hub.
Zn foil (100 mm thickness) and Zn powder were obtained from the SCI Materials Hub.
Commercial 20% Pt/C, 40% Pt/C and IrO2 catalysts were also obtained from SCI Materials Hub.
3. Journal of Energy Chemistry Vanadium oxide nanospheres encapsulated in N-doped carbon nanofibers with morphology and defect dual-engineering toward advanced aqueous zinc-ion batteries
In this paper, carbon cloth (W0S1011) was obtained from SCI Materials Hub. The flexible carbon cloth matrix guaranteed the stabilization of the electrode and improved the conductivity of the cathode.
4. Energy Storage Materials Defect-abundant commercializable 3D carbon papers for fabricating composite Li anode with high loading and long life
The 3D carbon paper (TGPH060 raw paper) were purchased from SCI Materials Hub.
5. Nanomaterials A Stable Rechargeable Aqueous Zn–Air Battery Enabled by Heterogeneous MoS2 Cathode Catalysts
Nafion D520 (5 wt%), and carbon paper (GDL340) were received from SCI-Materials-Hub.
Carbon cloth (W0S1011) and other electrochemical consumables required for air cathode were provided by SCI Materials Hub.
Oxygen Reduction Reaction
1. J. Chem. Eng. Superior Efficiency Hydrogen Peroxide Production in Acidic Media through Epoxy Group Adjacent to Co-O/C Active Centers on Carbon Black
In this paper, Vulcan XC 72 carbon black, ion membrane (Nafion N115, 127 μL), Nafion solution (D520, 5 wt%), and carbon paper (AvCarb GDS 2230 and Spectracarb 2050A-1050) were purchased from SCI Materials Hub.
2. Journal of Colloid and Interface Science Gaining insight into the impact of electronic property and interface electrostatic field on ORR kinetics in alloy engineering via theoretical prognostication and experimental validation
The 20 wt% Pt3M (M = Cr, Co, Cu, Pd, Sn, and Ir) were purchased from SCI Materials Hub. This work places emphasis on the kinetics of the ORR concerning Pt3M (M = Cr, Co, Cu, Pd, Sn, and Ir) catalysts, and integrates theoretical prognostication and experimental validation to illuminate the fundamental principles of alloy engineering.
Water Electrolysis
1. International Journal of Hydrogen Energy Gold as an efficient hydrogen isotope separation catalyst in proton exchange membrane water electrolysis
The cathodic catalysts of Pt/C (20 wt%, 2–3 nm) and Au/C (20 wt%, 4–5 nm) were purchased from SCI Materials Hub.
2. Small Science Silver Compositing Boosts Water Electrolysis Activity and Durability of RuO2 in a Proton-Exchange-Membrane Water Electrolyzer
Two fiber felts (0.35 mm thickness, SCI Materials Hub) were used as the porous transport layers at both the cathode and the anode.
3. Advanced Functional Materials Hierarchical Crystalline/Amorphous Heterostructure MoNi/NiMoOx for Electrochemical Hydrogen Evolution with Industry-Level Activity and Stability
Anion-exchange membrane (FAA-3-PK-130) was obtained from SCI Materials Hub website.
Fuel Cells
1. Polymer Sub-two-micron ultrathin proton exchange membrane with reinforced mechanical strength
Gas diffusion electrode (60% Pt/C, Carbon paper) was purchased from SCI Materials Hub.
Characterization
1. Chemical Engineering Journal Electrochemical reconstitution of Prussian blue analogue for coupling furfural electro-oxidation with photo-assisted hydrogen evolution reaction
An Au nanoparticle film was deposited on the total reflecting plane of a single reflection ATR crystal (SCI Materials Hub, Wuhu, China) via sputter coater.
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