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Abstract
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Hydrogen
(H2) is a secondary fuel derived from natural gas. H2 is a significant
component in refining operations, fertilizer production, and increasingly is used
in the transportation industry as a clean combustion fuel. Recent research
has focused on developing technology that reduces carbon emissions. Consequently,
there has been an increase in technological developments for producing H2
from natural gas. The goal of such technologies is to minimize the cost
increment associated with clean energy production. The natural gas processing
chemical looping technology, developed at The Ohio State University (OSU),
employs an iron-based oxygen carrier and a novel gas–solid counter-current
moving bed reactor for H2 production.
Researchers
examined the theoretical thermodynamic limits for full conversion of natural
gas through iron-based oxygen carrier reactions with methane (CH4), by
utilizing simulations generated with ASPEN modeling software. Their study
initially investigates the reducer and the oxidizer thermodynamic phase
diagrams then derives an optimal auto-thermal operating condition for the
complete loop simulation. This complete loop simulation is initially
normalized for analysis on the basis of one mole of carbon input from natural
gas. The H2 production rate is then scaled to match that of the baseline
study, using a full-scale ASPEN simulation for computing cooling loads, water
requirements and net parasitic energy consumption. The full scale ASPEN
simulation is used to analyze the thermal efficiency of multiple energy
recovery schemes, for further validation of the chemical looping process.
Researchers found the chemical looping technology to produce a cold gas
efficiency improvement of more than 5 percentage points and an effective
thermal efficiency of more than 6 percentage points over the conventional
steam methane reforming process, while producing H2 from natural gas with
greater than 90% carbon capture.
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