T-GARC Node: Datasets for Technology Database for Carbon Neutrality
Data stock: Default root data stock [ Download ]

Process data set overview page

Data set: Hydrogen; from Small-scale hydrogen reforming (00.00.001)

Full name
Hydrogen; from Small-scale hydrogen reforming; at plant; Single site; H2 (99.999%,30bar)
Location
KR
Reference year
2024
Valid until
2028
Reference flow(s)
Type
LCI result
Parameterized?
no
LCIA results included?
yes
Category
Materials production / Other materials
Synonyms
Use advice for data set
Data set use approval
General comment
This process represents a set of unit processes for a small-scale modular Steam Methane Reforming (SMR) system that produces high-purity hydrogen using city gas (natural gas, NG), water, and electricity as inputs. The final hydrogen product has a purity of 99.999%, and the product hydrogen outlet pressure is set at 30 bar. The city gas is first subjected to a desulfurization process to remove sulfur compounds and is then supplied to the steam methane reformer. Water is treated and converted into steam through the water treatment and steam generation processes before being fed together with the natural gas. In the steam methane reformer, methane, the main component of the city gas, reacts with steam at a high temperature of approximately 700–900°C to produce reformate gas consisting mainly of carbon monoxide and hydrogen. The heat required for the reforming reaction is supplied by combusting city gas and off-gas recovered from downstream processes in the reformer burner. The reformate gas is then supplied to the shift reactor, where carbon monoxide reacts with steam through the water-gas shift reaction to form carbon dioxide and additional hydrogen. After the shift reaction, the reformate gas is cooled in a cold box, where the moisture contained in the gas is condensed and separated into gaseous and liquid phases. The cooled and gas-liquid separated reformate gas is subsequently supplied to a Pressure Swing Adsorption (PSA) unit, where impurities such as carbon dioxide, unreacted methane, and residual carbon monoxide are removed by adsorption. As a result, a high-purity hydrogen product with a purity of 99.999% and an outlet pressure of 30 bar is produced. The off-gas separated in the PSA process is recycled to the steam methane reformer burner as an auxiliary fuel and utilized as a process heat source. Gaseous emissions, including carbon dioxide generated from fuel combustion and the reforming process, are released to the atmosphere, while the water condensed and separated in the cold box is discharged as an aqueous emission (H₂O).
LCI Method Principle
Attributional
LCI Method Approaches
  • Allocation - net calorific value
Completeness of product model
All relevant flows quantified
Reviews
  • Accredited third party review by
    No records found.
License and access conditions
Copyright
yes
License type
Free of charge for all users and uses
Owner of data set
KENTECH
Technical purpose
Input Products
No records found.
Co-Products
No records found.
Data set version
00.00.001
Time stamp (last saved)
2026-10-14T01:40:50.000
Data set format
Compliance systems
No records found.
Tag
Registered in
Registry nameBase URLStatus
GLADhttps://www.globallcadataaccess.org
Data Set deregistration
Are you sure you want to deregister selected dataset?
Please enter the reason of deregistration and confirm.