alarping risk reduction measures - ichememay 28, 2019 · cdoif and ca guidance on era and alarp 7...
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ALARPing Risk Reduction Measures: Better quantification for better results
Presented by
Jack Davy and David Craig of Wood
Stuart Turner of EDF Energy
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Introduction
EDF Energy is part of EDF Group
and is one of the largest energy
companies in the UK, supplying
around 5 million residential and
business accounts with electricity
or gas.
We produce around one-fifth
(20%) of the nation’s electricity
and that makes us the largest
supplier by volume - something
we’re really proud of.
EDF Energy employs over
13,500 people across the UK.
• 7 Advanced Gas-cooled
Reactor (AGR) power stations
• 1 Pressurised Water Reactor
(PWR) power station
• Combined generation
capacity of 8,918 MWe
• All located on estuarine or
open coasts
• All lower tier COMAH
establishments
EDF Energy UK nuclear power plant
(NPP) fleet
Fuel Oil
• Providing an
essential back
up electrical
supply.
• Also used for
the generation
of auxiliary
steam,
vaporisation of
CO2 and some
other heating
and ventilation
Ammonia
• Primarily for
boiler feed
water
treatment to
avoid acidic
conditions
thereby
minimising
corrosion.
Sodium
Hypochlorite
• Dosed into the
incoming
cooling water
to mitigate
efficiency
reductions in
condenser and
circulating
water system
plant due to
biofouling.
Hydrazine
• Used as an
oxygen
scavenger to
control
concentrations
of dissolved
oxygen
thereby
minimising
corrosion.
Typical NPP COMAH substances
The process
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CDOIF and CA Guidance on ERA and
ALARP
28/05/20197
EDF Energy approach to ERA
► In 2014, the COMAH Competent Authority (CA) requested EDF Energy
undertake Environmental Risk Tolerability Assessments based on previously
submitted PHR scenarios using the CDOIF ERA methodology.
► In 2015, the first Phase 1 report was submitted which assessed MATTE potential
for all receptor types demonstrating that the risk was bounded by potential
effects on surface water due to the characteristics of these NPP sites.
► In 2016, the CA agreed streamlining of method to a bounding S-P-R linkage of:
Liquid Dangerous Substances
↓Surface Drainage
↓Surface Water Type Receptors
EDF Energy approach to ERA
Phase 1
Part 1
• EDF Energy assessment with support from an Independent Marine Biology
specialist contracted to provide conservative high-level consequence assessment
reports for Surface Water type receptors avoiding the need for detailed
monitoring beyond the screening intent of this stage.
Phase 1
Part 2
• Risk assessment specialists from Wood contracted to support failure frequency
and risk assessment stage of work adding external challenge and experience.
• Positive feedback received from Competent Authority concerning approach to
assessments including format of output.
Phase 2
• Compliance against HSE Technical Measures
• ALARP Assessment of the key scenarios for each station
• Calculation of benefits based on reduction in aggregated risk against agreed
event ‘costs’ (£1-100M)
When writing this paper, we asked
ourselves?
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Delivering on
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►Does use of this approach give a meaningful output?
►Does it provide decision-making output when the answer is
not obvious?
► Is it effective in considering combinations of measures which
may be interdependent?
►Can it generate options to reduce risk which
►Are logical and make “engineering sense”?
►Allow the best options to be prioritised?
Case studies
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Station 1 – simple example
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►Workshop identified 46 potential improvement options and
screened in 12 for further assessment (4 reducing FO risk and 8
on the hypo system).
►Sodium hypochlorite system
► All releases are MATTE B but a release outside the bund goes direct
to marine receptor.
► 8 options assessed – 7 of these were not grossly disproportionate –
option with the greatest absolute risk reduction selected due to
HSE guidance.
“The option, or combination of options which achieves the lowest level of residual risk should be implemented, provided grossly disproportionate costs are not incurred”
Station 1 – simple example
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►Two Independent systems with dominant risks.
Off loading area
Station 2 – Targeted effective measures
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►Workshop identified 56 potential improvement options and
screened in 10 for further assessment (2 reducing FO risk and 8
on the hydrazine system).
►Hydrazine system
► Lots of options – obvious from MJS that multiple measures needed.
► 8 options assessed – some options were mutually exclusive and others
options became disproportionate when initial measures implemented.
► Option 48 preferred for higher benefit for lower CAPEX. If implemented,
makes Option 38 grossly disproportionate.
Description
CAPEX
Before other
measure
After other
measureRisk
ReductionMJS
Risk
ReductionMJS
38 Double walled pipework £25k 2.88E-5 £389k 3.17E-7 £4.3k
48 Secondary containment
around pipework £10k 3.17E-5 £428k 2.88E-7 £3.8k
Station 2 – Targeted effective measures
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►The approach to ALARP gives increased clarity in choosing
between options
►Hydrazine system
► Assumption that options 7 (FO) and 48 already to be implemented
► Following implementation of initial measures, the MJS and DF
factors should be recalculated.
► Option 42 was not initially GD (and preferable to Option 41 in
isolation) but becomes GD when others implemented
Option. Description CAPEXInitial
MJS
Revised
MJS
Grossly
Disproportionate
41Replace plastic IBCs with
steel£10 k £34 k £23 k No
42Use of dedicated delivery
vehicle£50 k £61 k £41 k Yes
Station 2 – Targeted effective measures
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►Two different systems focus of ALARP study
►Hydrazine – dominant risks – multiple release cases
► Pipe between bund and processing
► IBC type
Station 3 – Global measures
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►Site only held fuel oil in MATTE quantities
►No scenarios dominate the risk
Station 3 – Global measures
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►Fuel oil systems
► Workshop identified 32 potential improvement options and
screened in 4 for further assessment.
► Site wide fuel oil MJS ~£180k
► Options are not independent – implementation of any option
reduces the benefit of all remaining options
►Result of assessment: Option 8 is the most-favoured by CBA but
Option 7 was implemented given operational constraints
(nuclear safety case)
Option
No.
Description CAPEX Benefit Remaining MJS
2 Alarm on bulk tanks £50k £109k £70k
3 Sump level alarm £40k £141k £38k
7 Oil on Water alarm £50k £170k £10k
8 Oil on Water trip £70k £173k £7k
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Lessons learned
Inputs, communication and efficiency
► Initial supporting guidance was limited for the whole process
► Pragmatic & engaged regulators were essential
► Centralised Project Management with consistent lead roles
aided consistency
► Risk Assessment processes developed in a ‘proportionate’ way
without which the project would have been driven to an
unsustainable level of detail thus delaying the implementation
of any outcome enhancements.
The challenge that continues is to embed consideration of
environmental risk tolerability within the modification process
Lessons about the ALARP Process
Lessons learned from ALARP assessment
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►ALARP process can work well using CA fundamental approach
but the differences of environmental risk must be considered.
► Must use appropriate inputs (generic event costs) and
proportionate level of detail – expert judgement & sensitivity
analysis
► Must consider all significant Major Accidents (MAH and MATTE)
and all significant receptors
► Must consider the aggregated effects of risk reduction
► Important to consider the interaction and inter-dependency of
measures
►Use of different metrics can be used to prioritise measures and
combinations of measures
ALARP process can effectively be transferred in environmental risk
and produce clear prioritized risk reduction measures.
Thanks for listening
Any questions?
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