4.2.1
Best Practices/Design
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.1 Manual pressure relief procedures (tank pressure
control);
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.2 P/V valve condition and maintenance;
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.3 Condition of gaskets for hatches and piping;
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.4 Inert gas topping up procedures;
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.5 Partially filled tanks;
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.6 Loading sequence and rate; and
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.7 COW procedures (closed cyclefootnote).
4.2.2
VOCON procedure
By reference to Figure 4.2 below, this procedure requires the
monitoring and the recording of the pressure drop during a release
of gas from the cargo tank vapour system. This can be undertaken with
the use of the Inert Gas pressure gauge in the cargo control room
or, as available, located on the Inert Gas pipeline on deck. Figure
4.2 shows a pressure drop profile using the mast riser and the inflection
in the pressure drop where the mast riser valve should be shut.
Figure 4.2 A mast riser release
The VOCON operational procedure
(1) Before opening the mast riser, note
the pressure in the Inert Gas pipeline system.
(2) Open the pressure release valve
and record/monitor the pressure within the Inert Gas pipeline at regular
short intervals (every 30 seconds for a mast riser release).
(3) Plot the pressure drop profile.
This can be achieved either manually or by use of the Inert Gas Oxygen
and Pressure Recorder in the Cargo Control Room but an increase in
the Recorder paper feed rate will be required to achieve definition
of the plot.
(4) When the rate of pressure drop becomes
constant (after the initial rapid pressure drop) then the gas release
should be stopped and the valve closed.
(5) Monitor the Tank Gas Pressure after
completion of the controlled release in order to check the final pressure
obtained within the Vapour/Inert Gas system.
(A) A review of Figure 4.2 shows a clear
change in the rate of pressure drop during the release period. If
the gas release continues after this point then the pressure in the
Inert Gas system will be quickly restored to the pressure associated
with the point where the rate of pressure drop changes.
(B) If there is a straight line drop
of pressure observed and no inflection observed by 800 mmWG, then
close the release valve anyway.
(C) By reference to the ISGOTT Publication,
all safety measures should be taken to minimize the hazards associated
with vented gases from the vessel’s cargo tank system.
4.2.3
Recovery of excess VOC and tank absorption
(Venturi system)
The Venturi system involves a process where evolved VOC is reabsorbed
back into the cargo. The system typically consists of a pressure controlled
pump, feeding oil to a unit with Venturi(s). The Venturi draws VOC,
H2S and inert gases (IG) from the common cargo tank venting/inert
gas main line. The Venturi unit is designed to generate a bubble size
optimal for their collapse in the crude oil cargo and rapid absorption.
Released near the tank bottom, the soluble compounds are kept dissolved
by the pressure head there. Inert gas will eventually surface.
For ships that have been provided with a Venturi type system,
the VOC emissions will be controlled when the system is in operation.
The VOC control system efficiency as well as any operational
limitations related to, e.g., applicability for different cargo handling
modes (loading, transit, COW), maximum allowable loading rates or
crude vapour pressures, are to be specified in the VOC management
plan.