lessons learned solving pilot valve instability issues on lng storage tanks
TRANSCRIPT
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Lessons learned solving pilot
valve instability issues on LNG
storage tanks
LNG Summit Houston 23/24 Feb 2017
Thorsten Schaper (Speaker)
Braunschweiger Flammenfilter GmbH (PROTEGO)
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Applications for Cryogenic Tanks
LNG Terminal Bulk Storage Tank with a set of P/V valves
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Pilot-operated Valves on LNG-Tanks
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Where are the problems?
• Pilot operated pressure relief valves installed on cryogenic
storage tanks may become unstable as a result of inaccurate
plant design or sudden construction changes on site.
• Pilot operated valves which are forced to become unstable may
not provide sufficient relief capacity resulting in overpressure
and imposing safety risks to the facility.
• It is known that relief valve instability is a dynamic problem
which requires an understanding and coupling of the pressure
source (e.g. LNG storage tank), the inlet line, the pilot operated
pressure relief valve and the discharge line.
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Some reasons for instability and lessons learned
• It is quite obvious that the 3 % rule – known from
pressure safety valves - is not sufficient to guarantee
POV stability.
• POV instability is a dynamics problem which requires
an understanding and coupling of the dynamics of the
following components:
1- Inlet Line
2- Discharge Line
3- Pressure Source or Vessel/Equipment
4- Pilot-Operated Valve - POV
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Since the 80th PROTEGO® delivered a lot of Pilot valves around the world
Lessons learned for 1 and 2
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Since the 80th PROTEGO® delivered a lot of Pilot valves around the world
Lessons learned for 1 and 2
Results:
• Common guidance on
how to design the
piping seems to be
missing or is not
applied in all cases
• Inlet pressure loss
seem to be neglected in
some cases
• Built up pressure in the
discharge line is not
allways considered
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˙
To high inlet pressure loss:
Chattering, hammering, results in flow
reduction and can destroy the valve
To high built up pressure in the vent line:
Pumping, Flow reduction but lower risk of
destroying the valve
Lessons learned for 1 and 2
1- Inlet Line 2- Discharge Line
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Example LNG Plant:
The installed 12“ PROTEGO-devices PM/S 300/350
experienced extrem instabilities.
The valve pallet was hammering on the seat and
destroyed the Aluminum valve pallet.
When opening the discharge line we could see that
the valve pallet did no reach full lift, which can
result in a reduced relief capacity
˙
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Problem-analysis (chattering)
Chattering resulted from to high inlet pressure losses.
For safety relief valve everyone is familiar with the 3%
rule.
When calculating the inlet pressure losses we received
results up 20%-30% of the set pressure
This high inlet pressure loss exceeded the blow down
by far.
In addition the customer used a sensing line directly at
the valve body and not an installation at the tank. In that
case higher flow reduces the static pressure and the
valve acts extremly unstable. The static pressure fell
below the crack pressure of the magnetic valve.
˙
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Solution: Increase blow down of the pilot valve
0
50
100
150
200
250
Magnetplatte Nr 1 pe=+10 … 20 mbar
Magnetplatte Nr 2pe=+21… 120 mbar
Magnetplatte Nr 2pe=+21… 120 mbar
Magnetplatte Nr 3pe=+120… 300 mbar
Magnetplatte Nr 3pe=+120… 300 mbar
pre
ss
ure
in m
ab
rg
Ventileinstelldruck mbar
Schließdruck mbar
Valve set pressure mbarg
Valve reseating pressure mbarg
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Important remarks for sizing
• The tank is insulated but your
discharge pipeline may not be
• In the discharge line the cryogenic
gas warms up due to heat input from
environment
• Consider the density changes along
the line when calculating the pressure
losses and the tank relief loads
• Build up your own or use a
commercial package with a reliable
thermo-fluid dynamic model
• Consider the internal piping within
the tank
Tank
HEAT
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Lessons learned during start up/valve testing (3- Pressure Source or Vessel/Equipment and 4- PRV)
The pressure relief system is designed for (e.g.):
• Liquid LNG input
• Thermal outbreathing
• Liquid Displacement and Flashing by filling
• Roll over
• Recirculation from a submerged pump
This design results in very high relief loads and that
means large valves with very high capacities
But what is your testing procedure before start up?
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Example: Nitrogen evaporation procedure
• The tank is just filled with a small amount of liquid
nitrogen, which then evaporates
• Relative to the design case the evaporation rate is very
small
• This results in chattering of the valve due to massive
oversizing
• If this start up/test procedure is used the valve
potentially runs into instability issues through rapidly
relieving and closing
But how can we solve this during start up and assure
that the valves works even though the valve is operated
within a zone that causes instability?
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Testing to extreme condition
and forcing the valve to
operate instable is a must for
understanding the valve
behavior
Solving the instability challenge during start up
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Instabilty Problem: Valve chattering heavily
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Instabilty Solution: Valve with dampening system
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Lesson learned
Challenge:
• Start up with small vaporizing quantities can result in
valve instability
Solution:
• Dampening systems which prevent valve instabilty
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Cryogenic Test showing chattering effect and the
performance of the damping system
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Cryogenic test
Tests according to ISO 21013-4
„Cryogenic vessels – Pilot operated pressure relief devices –
Part 4: Pressure-relief accessories for cryogenic service“.
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PROTEGO PM/HF with Fiel-Test-Connection and Test-Kit
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Oxygen-Cleanliness-Workshop
Washing machines
Oil-free test bench
UV-light Tent for Visual Inspection
Ultra-sonic bath for small pieces
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Vacuum-Breaker for Cryogenic Application
Propylene Storage Tank
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Vacuum-Breaker for Cryogenic Application
Vacuum Breaker installed on Cryogenic Storage Tanks
need to be very tight against leaking!
• Vacuum breaker are exposed to relativley high
over-pressure due to the operating pressure of the
storage tank which works as a closing force to the
valve pallet
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Competitors soft sealing with FEP-foil
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Competitors valve leaks due to exposure to sun
radiation – Visible through IR-camera
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Vacuum-Breaker for Cryogenic Application
PROTEGO has inproved vacuum breakers with setting
at -2,5 mbar / - 1“ WC, metallic sealing and highest possible capacity
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Thank you for your attention
Excellence in Safety and Environment