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Work Package 2:
Safety
Leader:
Loughborough University
Partners
Leeds
University, CEA, Shell Hydrogen, UK HSE,
National Grid.
Scope and
Objectives
The existing gas
pipeline networks are designed, constructed and
operated based on the premise that natural gas
is the material to be conveyed. However,
hydrogen has different chemical and physical
properties which may adversely affect (increase)
the risk presented to the public. Risk is
a combination of likelihood of an
untoward event (such as failure frequency of
pipelines or ignition probability) and the
consequence (hazard) of the event (such as
the severity of a fire or explosion). Adding
hydrogen to the gas infrastructure may affect
both the likelihood and severity of untoward
events and hence potentially increase the risk
to the public. It is important to quantify this
effect in order to establish if the risk remains
acceptable and to identify the maximum hydrogen
concentration that can be added to the natural
gas without this risk becoming unacceptably
high.
To achieve these objectives, the Safety Work
Package is re-examining the hazards presented by
fire and explosion situations pertinent to the
gas infrastructure, based on a natural
gas/hydrogen mixture being involved.
Additionally, information on the likelihood of
accidental events will be revised so that it is
relevant to the new fuel, for example, pipeline
failure frequencies and ignition probabilities.
To assess the change in consequences small and
large scale experiments are being undertaken to
provide data to aid model development and
validation, specifically:
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Laboratory
experiments to assess the burning velocities
of methane/hydrogen mixtures
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Large scale
experiments of gas build up in a domestic
environment
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Large scale
experiments of gas build up and explosions
in an industrial enclosure/building
-
Field scale and
large scale experiments of explosions in
congested regions (Vapour Cloud Explosions)
-
Large scale
experiments to study jet fires and
underground pipeline failures
Simple and CFD
models are being developed and validated using
this data and then the models used to assess the
impact of different levels of hydrogen on the
severity of the hazards which may arise from a
wide range of accident scenarios.
Data from WP3/4 will aid re-evaluation of the
failure frequencies of pipelines and equipment.
The ignition probability and minimum ignition
energy of gas mixtures is being determined
through laboratory experiments. This data will
be used to revise the ignition probability used
in risk assessments of the gas network.
The above work on likelihood and
consequences is being combined to produce a
risk assessment tool, which can be applied to
gas networks conveying methane/hydrogen
mixtures, enabling the risk to the public to be
calculated for differing levels of hydrogen
introduction and compared with the risk for a
system conveying natural gas. The tool will be
provided as input to the Decision Support Tool
of Work Package 6.
Current Status
To date, all the
large scale experimental work quantifying the
change in consequences (hazard) have been
completed. The gas build up experiments showed
that the nature of methane/hydrogen gas
accumulation appears to be similar to methane
although increased buoyancy of the accumulation
results in increased buoyancy induced
ventilation which is beneficial in limiting gas
concentrations. The confined vented explosions
showed that adding 20% hydrogen had little
effect on explosion severity, but adding 50%
hydrogen resulted in a significant increase. In
unconfined congested regions, studies of Vapour
Cloud Explosions showed that with 50% hydrogen,
the overpressures increase significantly and
there is potential for a transition to
detonation. The data from the jet fire
experiments has shown that the characteristics
of a methane/hydrogen (with 25% hydrogen) flame
are similar to a methane flame but the flame
temperature was slightly higher leading to
higher heat loads to engulfed objects. The data
from the pipeline fire experiments is still
being analysed.
The development of simple and CFD models of gas
build up and explosion hazards are well
advanced. Model predictions have been compared
with the experimental data and the models used
to study the effect of changing parameters.
These models made use of the results obtained
during the laboratory experiments of burning
velocities (laminar and turbulent) for
methane/hydrogen mixtures.
In terms of assessing the likelihood of events,
a series of laboratory based experiments have
been completed to assess the minimum ignition
energy and ignition probability of
methane/hydrogen mixtures containing 0, 25, 50,
75 and 100% hydrogen. The data has been analysed
and a correlation developed will enables the
prediction of the minimum ignition energy for
any methane/hydrogen mixture across the
flammable range.
Failure probabilities for natural gas pipelines
have also been collated from industry databases
and these have been included in the risk
assessment tool being formulated for
transmission pipelines. This risk assessment
package can be run as a stand-alone code or from
within the DST. Currently, the risk assessment
package can be run to predict the risk to the
public from pipelines conveying natural gas.
However, the structure of the package also
allows natural gas/hydrogen mixtures to be
considered, but further work is required in
order to be able to provide suitable failure
probabilities and ignition probabilities for the
mixtures. The results of the fire experiments
may also result in changes to the model of the
hazard presented.
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