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HXS-30 30 kW AEM electrolyzer stack

Available

Measured 46-cell full-stack data and the design values for this anion exchange membrane (AEM) electrolyzer stack are presented separately.

The HXS-30 is a 30 kW-class AEM water electrolyzer stack. The 46-cell full stack, designed for 6,900 NL/h (15 kg/day), is available to order now. It completed first operation in September 2026 and is currently under long-term evaluation.

30 kW stack
DESIGN TARGET

The figures below are full-stack design values; measured data are identified separately.

Rated production6,900 NL/h · 15 kg/day

46-cell design value

Rated power30 kW
Cell configuration46 cells
Production pressureH₂ side up to 10 barg
Who it is for

A 30 kW full stack for projects that build their own BoP

The 46-cell, 30 kW full stack is available now. Review what the first operation measured separately from the figures that are still design values.

Choose this product when
  • Integrating a 30 kW-class stack into an industrial demonstration or hydrogen production plant
  • System integrators able to design their own BoP, power, control and safety systems
  • Projects evaluating modular scale-up from the 15 kg H₂/day design capacity per unit
EVIDENCE AND TARGET

What was measured on 46 cells, and what is still a design value

Review measured data and design values separately for the available 46-cell full stack when defining operating conditions and integration scope.

MEASURED01

46-cell performance data

i-V curve and all 46 cell voltages

HYDROXPAND02

Full-stack engagement

Supply and technical review against integration conditions

DESIGN TARGET03

Design values

Output, efficiency and consumption are 46-cell design figures

HYDROXPAND

Included supply scope

  • 46-cell HXS-30 full-stack design with power, electrolyte and gas connection specifications
  • Measured 46-cell i-V and cell-to-cell voltage data with recommended operating conditions
  • Exterior/enclosure-only STEP model on request (internal parts and flow fields excluded)
CUSTOMER

Customer preparation

  • A DC power supply sized for the rated operating range (80 V · 360 A design basis; a supply able to deliver up to about 92 V is recommended to cover voltage rise during operation)
  • Electrolyte circulation and temperature control matched to the product connection specification
  • Gas-liquid separation and drying or purification equipment for the required purity
  • Pressure and safety systems designed for up to 10 barg on the H₂ side with the anode at atmospheric pressure
COMPONENTS AND BOPWhat goes around HXS-30Upstream, in-stack and downstream, plus the design review scope
Test results

Measured on the 46-cell full stack at first operation

The label on each chart says whether it is measured, test or design-target data. Test conditions are in each chart caption.

MEASURED01

Cell voltage was measured across current density on the 46-cell full stack.

Measured i-V curve · 46-cell full stack (18 September 2026 · 0.1 M KOH · 50 °C)

Measured i-V curve · 46-cell full stack (18 September 2026 · 0.1 M KOH · 50 °C)
MEASURED02

The voltage distribution across all 46 cells is compared at 362.3 A.

Cell-to-cell voltage · 362.3 A · 0.1 M KOH · 50 °C (1.6602 V per cell = stack voltage ÷ 46; the 1.6562 V line is the mean of the 46 cell-voltage channels; spread 34.3 mV)

Cell-to-cell voltage · 362.3 A · 0.1 M KOH · 50 °C (1.6602 V per cell = stack voltage ÷ 46; the 1.6562 V line is the mean of the 46 cell-voltage channels; spread 34.3 mV)
Specifications

HXS-30 specifications and supply terms

The specification table, support terms and review documents.

Complete product specifications17 items
H₂ production6,900 NL/h (15 kg/day · design)
Outlet pressureUp to 10 barg on the H₂ side
Efficiency (HHV)46-cell, 30 kW full-stack design 84% · approx. 47 kWh/kg-H₂
Recommended operating condition0.1 M KOH · 50 °C (adjustable)
Operating temperatureUp to 80 °C
DC input80 V · 360 A (28.8 kW)
Water consumption6.1 L/h measured (360 A; 18.5 h continuous run, 22–23 September 2026; includes water carried out with the product gas) · electrolysis theory 5.6 L/h
46-cell continuous run360 A constant current · 93.6 h without interruption (as of 26 September 2026, 13:08 KST; latest figures in the 46-cell technical note)
Number of cells46
Electrode area · reference active areaAnode electrode area 600 cm² · cathode active area 512 cm²
Dimensions570 × 400 × 330 mm
Weight120 kg
StructureAnode-side electrolyte circulation
Instrument calibrationFlow and gas analysers calibrated under KOLAS
End plateSUS316L
Bipolar plateNickel-based metallic plate
Material changeYes · we confirm the operating window and validation scope together
Support, lead time and commercial terms3 items
Service & reassembly

Disassembly and reassembly require our dedicated gaskets and a hydraulic press, so conditions are agreed with us in advance. Return service can replace only the MEA and reuse the hardware; the service scope and terms are fixed in the quotation.

Availability & lead time

46-cell, 30 kW full stack available now · under long-term evaluation after first operation

Commercial terms & origin

EXW basis; DAP and other terms by agreement. Country of origin is the Republic of Korea, with certificate of origin provided.

Pricing depends on quantity, configuration and Incoterms, so it is issued as a quotation. The BoP budget (power, circulation, separation, drying and controls) depends on your integration scope; send it with the enquiry and we will review it together.

Enquiry

HXS-30 purchase and integration

Send the required quantity, delivery schedule and your BoP, power and safety design scope so we can review pricing and integration requirements.