Maintaining the cargo tank pressure and temperature by means
of thermal oxidation of cargo vapours, as defined in 1.2.52 and 16.2
shall be permitted only for LNG cargoes. In general:
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.1 thermal oxidation systems shall exhibit no
externally visible flame and shall maintain the uptake exhaust temperature
below 535°C;
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.2 arrangement of spaces where oxidation systems
are located shall comply with 16.3 and supply systems shall comply
with 16.4; and
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.3 if waste gases coming from any other system
are to be burnt, the oxidation system shall be designed to accommodate
all anticipated feed gas compositions.
7.4.2
Thermal oxidation systems
Thermal oxidation systems shall comply with the following:
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.1 each thermal oxidation system shall have a
separate uptake;
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.2 each thermal oxidation system shall have a
dedicated forced draught system; and
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.3 combustion chambers and uptakes of thermal
oxidation systems shall be designed to prevent any accumulation of
gas.
Burners shall be designed to maintain stable combustion
under all design firing conditions.
7.4.4.1 Suitable devices shall be installed and
arranged to ensure that gas flow to the burner is cut off unless satisfactory
ignition has been established and maintained.
7.4.4.2 Each oxidation system shall have provision
to manually isolate its gas fuel supply from a safely accessible position.
7.4.4.3 Provision shall be made for automatic
purging the gas supply piping to the burners by means of an inert
gas, after the extinguishing of these burners.
7.4.4.4 In case of flame failure of all operating
burners for gas or oil or for a combination thereof, the combustion
chambers of the oxidation system shall be automatically purged before
relighting.
7.4.4.5 Arrangements shall be made to enable the
combustion chamber to be manually purged.