Hydrogen Generator

Gaseous hydrogen generator from chemical reactions for industrial use, operated in environments controlled by qualified personnel. Designed and built in the factory, transported by modules and assembled on site.

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Electrolysis Cell - Technological Core

The electrolysis cell is the central component of our hydrogen generation technology. Its patented electrode design (anode and cathode) represents a technological milestone that optimizes the energy efficiency of the process. Through strategic combination of electrode geometry, surface properties, high-performance materials, flow control and precise thermal management, we maximize hydrogen ion production with the highest market operational efficiency.

Electrolysis Cell

Electrical Specifications

Supply Voltage 24 VDC
Energy Consumption 60 – 5000 W
Current Consumption 10 – 400 A
Operating Temperature -40 °C to 80 °C
Dimensions 0.7 × 0.8 × 0.55 m

Operational Specifications

Output Pressure 30 PSI
H₂ Purity 80% – 90%
Heat Dissipation 40 °C/h
Water Consumption 18 L
Sensors Temperature, Pressure

Fluid Storage System - Integrated Thermal Control

The process isotank is a double-structure container (plastic core with tubular metal reinforcement) designed to ensure maximum durability and performance. It stores and supplies operational fluids in a controlled manner (distilled water or KOH electrolytic solution). Its integrated heat exchanger system maintains optimal thermal conditions throughout operation, ensuring sustained efficiency and extended system lifespan.

Storage System

Tank Characteristics

Capacity 1000 liters (275 gallons)
Dimensions 1.20 × 1.00 × 1.16 m
Weight Empty 53.4 kg
Weight Loaded 1054 kg

Properties and Control

Material Plastic container with tubular metal structure
Fluid Content Water or electrolyte (potassium hydroxide, KOH)
Sensors Temperature and level

Power and Control Rack - Industrial Automation

The power and control rack is the intelligent heart of the system, an industrial automation cabinet that orchestrates every aspect of the hydrogen generator. It integrates advanced PLC control modules, precision power management, real-time monitoring systems, overload protection, and automatic fault diagnosis. It guarantees safe, reliable and efficient operation under any industrial load condition.

Control Rack

General Specifications

Power Supply 220 V — 3 Phase · Neutral · Ground
Dimensions 0.73 × 1.0 × 1.6 m
Weight 90 kg
Center of Mass 0.7 m height

Separation and Cooling System - Hydrogen Purification

The separator tank receives the gas mixture produced in the electrolysis and implements a three-stage gas-liquid separation process: refrigeration condensation, centrifugal spray and gravity decantation. This system guarantees hydrogen purity greater than 99.8%, eliminating residual water vapor and ensuring that only pure hydrogen gas continues to the filtration and storage stage.

Separation System

General Characteristics

Capacity 125 litros / 33 gal
Heat Exchanger Weight 130 kg sin carga · 248 kg con carga
Separation Tank Weight 82 kg sin carga · 123 kg con carga
Dimensions 0.6 × 0.6 × 1.2 m

Safety and Standards

Sensors and Safety Pressure relief valve · Hydrogen safety valve · Control fill solenoid valve
Normative Standard NTC-ISO 22734
Additional Standards ISO 12100 / ASME Section VII–VIII

Hydrogen Storage System - Dual Pressurization

Our storage system integrates two stationary pressure vessels designed under international ISO 9809 standards for maximum safety. Without the need for additional compression, the vessels maintain pure hydrogen at controlled pressure, allowing continuous and reliable supply to industrial application devices. Ideal for applications requiring energy autonomy and reduced dependence on fossil fuels.

Storage System

Storage Specifications

Capacity 125 litros / 33 gal
Weight 82 kg no load
Sensors and Safety Temperature and pressure · Pressure relief valve · Hydrogen safety valve · Check valve · Flame arrestor
Dimensions 0.6 × 0.6 × 1.2 m
Normative Standard NTC-ISO 22734 · ISO 12100 / ASME Section VII–VIII