CourseElectromobility, Batteries & Hydrogen Enrolment open

Course in Storage and Compression at 350/700 bar

Online course of 300 h in storage and compression at 350/700 bar. 6 modules covering ISO 19880-1, ISO 14687 and NIST REFPROP. Assigned tutor and open enrolment.

Duration300 h
ModeOnline
Start datesOctober / March
LocationEurope (Madrid)
AwardSEIUM Institute diploma
Virtual lab · try it before you enrol

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Learning outcomes

What you will be able to do

01

Understand the thermodynamic behaviour of hydrogen at 350 and 700 bar.

02

Select the pressure vessel type suited to each application.

03

Size compression trains and cascade storage banks.

04

Apply SAE J2601 filling protocols at refuelling stations.

05

Identify the risks of leakage, embrittlement and ignition in high-pressure installations.

06

Interpret the approval regulations and pressure equipment standards that apply.

07

Technically and economically evaluate a complete compressed storage system.

Profile

Who it's for

  • Hydrogen systems engineer looking to specialise in Storage and Compression at 350/700 bar.
  • Hydrogen refuelling station technician looking to specialise in Storage and Compression at 350/700 bar.
  • Pressure vessel engineer looking to specialise in Storage and Compression at 350/700 bar.
  • Industrial safety manager looking to specialise in Storage and Compression at 350/700 bar.
  • Hydrogen mobility consultant looking to specialise in Storage and Compression at 350/700 bar.
  • Project manager for refuelling infrastructure looking to specialise in Storage and Compression at 350/700 bar.
  • Graduates in engineering or sciences looking to enter the hydrogen mobility sector.
Standards & tools

What you'll work with

  • ISO 19880-1
  • ISO 14687
  • SAE J2601
  • ISO 17268
  • UN Regulation No. 134 (UN R134)
  • ISO 19881
  • Directive 2014/68/EU of pressure equipment
  • ISO 11114-4
Syllabus

6 modules · 300 h

  1. 1.1Equation of state and compressibility factor Z
  2. 1.2Volumetric and gravimetric density at 350 and 700 bar
  3. 1.3Inverse Joule-Thomson effect of hydrogen
  4. 1.4Adiabatic heating during rapid filling
  5. 1.5Hydrogen embrittlement in steels and alloys
  6. 1.6Permeation through polymer liners
  7. 1.7Flammability limits and minimum ignition energy
  8. 1.8Fuel quality according to ISO 14687
  9. 1.9Comparison with liquid hydrogen and LOHC carriers
  10. 1.10Workshop: calculating stored mass with REFPROP
  1. 2.1Classification of Type I, II, III and IV cylinders
  2. 2.2Carbon fibre and epoxy resins in the overwrap
  3. 2.3High-density polyethylene and aluminium liners
  4. 2.4Filament winding and winding angles
  5. 2.5Burst ratio and design safety factors
  6. 2.6Hydraulic cycling and burst tests
  7. 2.7Localised fire, drop and penetration tests
  8. 2.8OTV valves and TPRD devices
  9. 2.9Service life, periodic inspection and cylinder retirement
  10. 2.10Case study: selecting tanks for an urban bus
  1. 3.1Lubricated and dry reciprocating piston compressors
  2. 3.2Metal diaphragm compressors
  3. 3.3Ionic liquid compressors
  4. 3.4Electrochemical and metal hydride compression
  5. 3.5Stages, compression ratio and intercooling
  6. 3.6Specific energy consumption in kWh/kg
  7. 3.7Sealing, leakage and sealing materials
  8. 3.8Reliability and maintenance of compressors
  9. 3.9Booster compression from tube trailers
  10. 3.10Laboratory: sizing a multistage compression train
  1. 4.1Architecture of a 350 and 700 bar station
  2. 4.2Cascade storage using pressure banks
  3. 4.3Precooling to −40 °C and dispensers
  4. 4.4SAE J2601 filling protocols
  5. 4.5Vehicle-to-dispenser communication according to SAE J2799
  6. 4.6Nozzles and receptacles according to ISO 17268
  7. 4.7Metrology and measurement of dispensed mass
  8. 4.8High-flow refuelling of heavy vehicles
  9. 4.9State of charge, temperature limit and filling rate
  10. 4.10Practice: simulating a 700 bar fill
  1. 5.1HAZOP analysis of a compression station
  2. 5.2ATEX zone classification and safety distances
  3. 5.3Leak detection, venting and emergency shutdown
  4. 5.4Tank approval according to UN R134
  5. 5.5Pressure Equipment Directive 2014/68/EU
  6. 5.6Road transport of compressed gas under ADR
  7. 5.7Levelised cost of compression and storage
  8. 5.8Lessons learned from refuelling station incidents
  9. 5.9Self-protection plan and emergency response
  10. 5.10Case study: risk analysis with HyRAM+
  1. 6.1Definition of the use case and daily demand
  2. 6.2Selection of working pressure and vessel type
  3. 6.3Sizing of compression and cascade banks
  4. 6.4Energy balance of the complete system
  5. 6.5Plant layout and safety distances
  6. 6.6Regulatory compliance matrix
  7. 6.7CAPEX and OPEX estimation
  8. 6.8Commissioning and testing plan
  9. 6.9Report and presentation
  10. 6.10Final review with the tutor
Methodology, software & labs

How you'll learn

100 % online training on the SEIUM campus, with downloadable material, recorded classes and an assigned technical tutor. There are no fixed timetables: students progress at their own pace within the enrolment period, making it possible to combine the course with work.

Each module combines theory, guided reading of the original standard and applied exercises. The working software is NIST REFPROP, Aspen HYSYS, ANSYS Mechanical, HyRAM+, MATLAB/Simulink, in free, academic or trial versions. The exercises are based on real sizing procedures for a 700 bar refuelling station, simulation of a rapid fill with precooling, and leakage risk assessment in a cylinder park. Assessment is continuous, module by module, plus a final integrative project.

Accreditable laboratories(EN ISO/IEC 17025) with rotor bench, EMC/Lightning pre-compliance, HIL/SIL, vibration/acoustics.
Evidence-oriented Master's Thesis:safety case, test plan, compliance dossier and operational limits.
Industry mentoring:lecturers with experience in training, , eVTOL/UAM and flight test.
Flexible format(hybrid/online), international cohorts and support from SEIUM Career Services.
Ethics and safety:safety-by-design approach, cyber-OT, DIH and compliance as pillars.
Capstone project

Build it end to end

Your final project follows the real engineering workflow, step by step, reviewed by your tutor.

Definition of the use case and daily demand

Understand the thermodynamic behaviour of hydrogen at 350 and 700 bar.

Selection of working pressure and vessel type

Select the pressure vessel type suited to each application.

Sizing of compression and cascade banks

Size compression trains and cascade storage banks.

Energy balance of the complete system

Apply SAE J2601 filling protocols at refuelling stations.

Plant layout and safety distances

Identify the risks of leakage, embrittlement and ignition in high-pressure installations.

Career opportunities

Where this takes you

Hydrogen systems engineerHydrogen refuelling station technicianPressure vessel engineerIndustrial safety managerHydrogen mobility consultantProject manager for refuelling infrastructure
Admissions & scholarships

Requirements

  • No prior degree is required.
  • Internet connection and a computer capable of running the programme's software.
  • Spanish-language proficiency sufficient to follow technical standards.

Ready to start?

Send your application today. Our admissions team replies within 72 hours with your study plan and funding options.

FAQ

Frequently asked questions

The programme consists of 300 hours in total, spread over 3 to 5 months. That is between 10 and 15 hours per week on average, compatible with a full-time job.

You work with NIST REFPROP, Aspen HYSYS, ANSYS Mechanical, HyRAM+, MATLAB/Simulink. Free, academic or trial versions are used, and the tutor indicates the free alternative where one exists.

A SEIUM diploma of your own upon passing continuous assessment and the final integrative project. It is in-house training, not an official qualification from the Ministry.

Yes. Modules passed in a Course or Postgraduate Diploma in the same area are recognised towards the higher-level programme. Check the recognition policy when enrolling.

Course in Storage and Compression at 350/700 barEnrol
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