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Freudenberg H14C9 Wet Proofed Carbon Paper with MPL

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SCI Materials Hub Technical Guide

Freudenberg H14 Series Carbon Paper GDL

Technical Analysis and Application Selection Guide

The Freudenberg H14 series is a family of high-performance gas diffusion layers developed for low-temperature proton exchange membrane fuel cells. The series combines a thin carbon-fiber substrate, a single-sided microporous layer, PTFE hydrophobic treatment and tightly controlled electrical resistance.

LT-PEMFC Single-Sided MPL PTFE Treated Low Through-Plane Resistance Automotive Fuel Cells Stationary CHP Systems
Product Overview

Freudenberg H14 carbon papers are engineered as multifunctional electrode components rather than simple conductive carbon substrates. Their performance is determined by the interaction between gas transport, liquid-water removal, electrical conductivity and mechanical compression.

SCI Materials Hub supplies H14-series GDL materials and organizes their principal properties into a standardized engineering framework. This allows researchers, MEA developers and fuel-cell stack engineers to compare grades according to the parameters most relevant to practical operation.

Engineering Evaluation

Three Core Performance Dimensions

SCI Materials Hub evaluates the H14 series through three connected engineering dimensions.

01

Mass-Transport Capability

Evaluated through Gurley values or equivalent gas-permeability parameters. This dimension affects reactant delivery, water-vapor transport and liquid-water discharge.

02

Electrical Conductivity

Through-plane resistance influences electrode ohmic loss, especially under high current density and high compression.

03

Mechanical Compatibility

Compressed thickness and tensile strength determine sealing compatibility, contact uniformity and resistance to edge damage during MEA assembly.

Standardized Data

H14 Series Technical Comparison

Units have been organized as mm, g/m2, mΩ·cm2, N/cm and Gurley seconds or equivalent gas-permeability values.

GradeThickness
@ 1 MPa
Basis Weight
g/m2
Through-Plane Resistance
mΩ·cm2
Gas Permeability /
Gurley
Tensile Strength
N/cm
PTFE TreatmentMPL
H14C70.017 mm1006.014YesSingle-sided
H14C90.180 mm1007.014YesSingle-sided
H14C100.170 mm975.01.4 μm2 equivalent>14YesSingle-sided
H14C140.145 mm5.50.5 s>14YesSingle-sided
H14C150.145 mm5.515 s>14YesSingle-sided
H14CX4830.180 mm6.01.0 μm2 equivalent>14YesSingle-sided
H14CX6530.185 mm946.01.0 μm2>14YesSingle-sided
Gas-transport values are presented in the form available for each grade. Gurley values and permeability values expressed in μm2 are not directly interchangeable and should be interpreted using the relevant test method.
Grade Classification

Engineering Positioning of the H14 Series

The grades can be grouped into three practical categories according to their primary design objective.

Low Ohmic Loss

Thin, High-Conductivity Grades

H14C7 / H14C10

Designed to reduce through-plane resistance and minimize the electrical contribution of the GDL to total cell resistance.

Recommended for
  • High-current-density PEM fuel cells
  • Automotive dynamic-load systems
  • Low-compression-loss MEA structures
  • Cells operating above approximately 2 A/cm2
Water-Management Balance

Balanced High-Humidity Grades

H14C9 / H14CX653

These grades provide a balanced combination of substrate thickness, gas diffusion and MPL-assisted water control.

Recommended for
  • Stationary combined heat and power systems
  • High-humidity PEMFC operation
  • Long-duration stable power output
  • Applications sensitive to local flooding
Mass Transport

Transport-Optimized Grades

H14C14 / H14C15

Intended for systems where rapid reactant delivery and controlled liquid-water removal are critical to maintaining high-load performance.

Recommended for
  • High-power-density MEAs
  • Rapid dynamic-response systems
  • Automotive fuel-cell electrodes
  • Gas-fed electrochemical research
Performance Mechanisms

How the GDL Structure Influences Cell Performance

M

Microporous Layer

The MPL improves gas distribution at the catalyst-layer interface, supports more uniform current generation and reduces the risk of localized liquid-water accumulation.

  • More uniform reactant distribution
  • Improved catalyst-layer contact
  • Reduced local flooding risk
  • More stable water transport
P

PTFE Hydrophobic Treatment

PTFE modifies the wetting behavior of the carbon-fiber network, helping control water retention and create more stable discharge pathways from the electrode.

  • Controlled liquid-water retention
  • Improved cathode water discharge
  • Reduced pore blockage
  • Improved operational stability
T

Thickness and Compression

Lower thickness can reduce electrical path length, but also decreases mechanical tolerance. Final performance therefore depends on matching the GDL to the gasket and compression design.

  • Lower thickness may reduce ohmic loss
  • Excessive compression can damage the structure
  • Greater thickness may improve water buffering
  • Contact pressure must remain uniform
Application Guide

Recommended Grades by Application

Final selection should also consider operating pressure, humidification, gas stoichiometry, flow-field geometry, catalyst loading and cell compression.

01

Automotive PEM Fuel Cells

Recommended: H14C10 / H14C14 / H14C15
Selection rationale Low through-plane resistance, rapid dynamic response and suitability for high-current-density MEA operation.
02

Stationary CHP Systems

Recommended: H14C9 / H14CX653
Selection rationale Balanced water management, stable operation under humid conditions and suitability for long-duration power generation.
03

High-Power Experimental MEAs

Recommended: H14C7 / H14C10
Selection rationale Low ohmic contribution and compatibility with cells designed for operation above approximately 2–3 A/cm2.
04

CO?RR and Water-Electrolysis Research

Recommended: H14C14 / H14C15
Selection rationale The MPL can support a more stable gas–liquid interface and more uniform reaction distribution, subject to wetting optimization.
Processing Guide

Recommended Electrode Preparation Workflow

Step 01

Catalyst-Layer Spraying

  • Prepare Pt/C and Nafion or AEM-ionomer catalyst ink.
  • Ultrasonically disperse the ink for 30–60 minutes.
  • Spray the catalyst ink onto the MPL side.
  • Use multiple thin passes to improve coating uniformity.
Standard PEMFC loading 0.1–0.4 mg Pt/cm2
High-power loading 0.3–0.6 mg Pt/cm2
Step 02

CCM Preparation

  • Prepare or transfer the catalyst layer onto the membrane.
  • Confirm membrane and electrode alignment.
  • Apply controlled temperature and pressure.
  • Avoid local overpressure and membrane deformation.
Hot-press temperature 120–140°C
Pressure 1–2 MPa
Time 2–5 min
Step 03

MEA Assembly

  • Place the MPL side toward the catalyst layer.
  • Keep the GDL, catalyst layer and membrane centered.
  • Match gasket thickness to the target compression.
  • Avoid excessive pressure near the electrode edge.
Recommended compression 20–30%
High-risk compression >35%

MPL Orientation Is Critical

During standard PEMFC MEA assembly, the smooth MPL-coated surface should face the catalyst layer, while the fibrous carbon-paper surface should face the flow field or bipolar plate.

Technical FAQ

Frequently Asked Questions

What is the main difference between H14C7 and H14C10?

H14C7 is positioned as a more extremely thin, low-resistance option. H14C10 provides a more balanced combination of low resistance and gas-transport stability.

Why is the lowest electrical resistance not always the best choice?

GDL selection is a multiparameter decision. A very thin, low-resistance structure may provide less mechanical tolerance or less water-storage capacity. Under highly humidified conditions, the overall pore structure and liquid-water transport can be more important than resistance alone.

Is an MPL necessary for PEM fuel cells?

An MPL is strongly recommended for most PEMFC electrodes because it improves the interface between the macroporous substrate and the catalyst layer. It may not be required for basic gas permeability testing. In CO? electrolysis, an MPL is often beneficial, but its hydrophobicity and wetting behavior must be optimized for the specific electrolyte and operating mode.

Why can carbon paper crack during electrode fabrication?

Common causes include:

  • Compression substantially above the design range
  • Uneven pressure or incorrect gasket thickness
  • Incompatible coating solvents
  • Excessive bending or handling of a thin GDL
  • Mechanical damage to the MPL during cutting or assembly
Which grades are suitable for CO? electroreduction?

H14C14 and H14C15 may be considered where a stable gas–liquid interface and MPL-supported reaction uniformity are required. However, electrolyte breakthrough, salt precipitation, hydrophobicity and pressure balance should be validated for the actual electrolyzer configuration.

Can the carbon paper be treated by prolonged ultrasonication?

Prolonged direct ultrasonication is not recommended. It can damage the carbon-fiber network, detach the MPL or alter the treated surface. Catalyst ink should normally be dispersed separately before coating.

SCI Materials Hub Selection Framework

A multifunctional GDL system for controlling transport, conductivity, water management and compression.

Thin and Low Resistance: C7 / C10 + Balanced Water Management: C9 / CX653 + Enhanced Mass Transport: C14 / C15
MEA Material Selection
Electrode Coating Guidance
Stack Compression Matching
GDL–Catalyst Layer Optimization
Technical notice: The information above is intended for preliminary material comparison and application selection. Values and processing recommendations should be confirmed against the current manufacturer datasheet and validated under the actual cell structure and operating conditions.
Pricing and Purchasing

Freudenberg® H14 Series GDL Price List

Research-size carbon paper GDL supplied by SCI Materials Hub.

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Freudenberg® H14 Series GDL Product Sizes and Prices

Reference retail prices for standard research-size, single-sheet cutting.

Grade5 × 5 cm10 × 10 cm20 × 20 cm
H14C7US$99.80
H14C9US$99.80
H14C10US$99.80
H14C14US$20.00US$70.00US$240.00
H14C15US$20.00US$70.00US$240.00
H14Cx483US$39.80US$119.80US$359.80
H14Cx653US$39.80US$119.80US$359.80

Price and Supply Notes

  • The prices above are SCI Materials Hub reference prices for standard research-size materials.
  • Standard orders are supplied as individually cut sheets suitable for fuel-cell, water-electrolysis, electrochemical and CO₂ electroreduction research.
  • Larger sheets, full-size materials and bulk quantities are available upon request.
  • Custom cutting, laser cutting, MEA-compatible materials and batch supply services are available.
  • International shipping, taxes and platform service fees are not included unless otherwise stated.
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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.


6. Vacuum Modulable Cu(0)/Cu(I)/Cu(II) sites of Cu/C catalysts derived from MOF for highly selective CO2 electroreduction to hydrocarbons

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.


2. Joule A high-voltage and stable zinc-air battery enabled by dual-hydrophobic-induced proton shuttle shielding

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.


6. SSRN An Axially Directed Cobalt-Phthalocyanine Covalent Organic Polymer as High-Efficient Bifunctional Catalyst for Zn-Air Battery

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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