2. A tank is an enclosed space
which is sealed and may not
have any ventilation.
As a result, there is a
accumulation of gases which
can be dangerous and
harmful to humans.
3. What do we
FEAR MOST
when we speak about
Cargo Tank
atmospheres ?
4. There are Different types
of Tankers.
Such as:
Crude Oil Tankers
Product Tankers
Chemical Tankers
LNG
LPG
Bitumen Tankers
Fruit Juice Tankers (stainless steel tanks)
Wine Tankers (stainless steel tanks)
BUT, we are speaking about our vessels :
Crude Oil & Product Tankers
5. Contributing Factors:
Oxygen
Flammable Vapors
External / Internal Spark
Contributing Factors:
Oxygen Deficiency
Hydro carbon Gas
Toxic Gases
Health Hazard
Hazards associated with tank atmosphere
Fire Hazard
6. Or simply said
A potential source of ignition hazard on oil tankers
Pyrophoric Reaction
What is this ? It is a rapid exothermic oxidation with
Incandescence.
How it is formed ?
• In an inerted atmosphere, the Hydrogen
Sulphide reacts with Iron Oxide (rust) and
forms Iron Sulphide.
• When a tank is exposed to air,the Iron
Sulphide is oxidized back to Iron Oxide This
oxidation is accompanied by generation of
considerable heat so that individual particles
may be incandescent.
Prevention ? All cargo operation is carried in controlled
inerted condition.
8. Fire hazards can be best explained by a
Fire Tetrahedron
It describes the four different factors
required for ignition of a fire.
The Inert Gas is introduced into a
tank to remove the Oxygen side of
the tetrahedron by reducing the
Oxygen content below required
percentage for combustion.
Essentially all four elements must be
present at the same time for a fire to
occur. Removal of any one of these
essential elements will result in the fire
being extinguished :
1. Air (Oxygen)
2. Heat ( Internal / External Spark)
3. Fuel (Cargo vapours)
4. Chain Reaction
9. Introduction of IG in the tank
Safe atmosphere in tank
NO FIRE
In absence of any
one side of the
original Fire
Tetrahedron , the
risk of a fire is non-
existent.
No Fire can take Place even in the presence of Heat or Fuel
because there is not enough oxygen to support it
Chemical
Chain
Reaction
10. G
21
Oxygen-Percentage by volume
Hydrocarbons
Gas-Percentage
by
volume
Flammable
Mixture
5 10 15 20
5
10
15
Flammable
Mixture
The Flammability diagram
Inerted Atmosphere-
Oxygen less than 8%
F
Consider a point representing
typical condition of tank
atmosphere in a inerted
condition
Purged Atmosphere-
Hydrocarbons less than
2% by voulme & oxygen-
less than 8%
Unsafe
atmosphere
Safe Atmosphere
passing well
below the critical
dilution line
What happens when
cargo oil tank
atmosphere is diluted
with air or when air is
introduced for gas
free condition.
11. What is the percentage of
oxygen required to sustain
combustion ?
More than 11 %
What percentage of
oxygen are we required to
maintain in the cargo
tanks ?
By law less than 8 %.
(Some ports require a
vessel to maintain less
than 5 %.)
A Cargo tank is considered “Inerted” when the oxygen content in
the tank is less than 8 % by volume
Controlling Fire Hazard in Cargo Oil Tank
12. Health Hazards
Hazards inside the tank
Oxygen deficiency. (Minimum 20.8% required for man entry)
Contact with Body parts
Inhalation and Ingestion
Risk of slip / trip/ fall due to cargo cling age in the access areas of
tanks.
Hidden risk :The risk of exposure to Health is not only inside a tank but that
same atmosphere may also be present on the open deck areas.
Hazards outside the tank
Release of tank atmosphere content during key cargo operations.
Accidental release by negligence or mechanical faults.
Accumulation due to still air conditions.
Beware!!
13. These includes the Key Cargo Operations such as:
Discharging
Tank Cleaning
Purging
Gas Freeing
Inerting
Loading
When performing these key cargo operations safely
The most important concern is to have a safe & controlled
cargo tank atmosphere.
On a oil tanker the cargo oil tank atmosphere changes as per
various operations the ship is performing.
14. General Policy of Cargo tank atmosphere control
Tankers fitted with an inert gas system should maintain their cargo
tanks in a non-flammable condition at all times.
It follows that:
Tanks are kept inerted when they contain cargo /cargo residue
The atmosphere within the tank should make the transition from
inert condition to gas-free condition without passing through
flammable condition.
In practice before any tank is gas freed, it would be purged with
inert gas until the hydrocarbon content of the tank atmosphere is
below the critical dilution line.
When a ship is in a gas-free condition before arrival at a loading
port, tanks should be re-inerted prior to loading.
15. Venting system for a cargo oil tank
Secondary Venting System
High Velocity Pressure
Vacuum valve
Primary Venting System
Mast Riser
Pressure side
Vaccum side
Gas Free Cover
Gas outlet
16. Cargo oil Pump
Suction bell
mouth
Suction line
Cargo
in the
tank
Ullage
space
Discharge line
Deck Discharge
line
Pump room
Cargo Oil Tank
Manifold
Shore Hose / Arm
Pressure
Vacuum
valve
From Inert Gas System
Drop of level &
increase of ullage
space.
This increase in ullage space is filled
with Inert gas, so that there is no
vacuum and no ingress of air in tank
Discharging Operation
Tank atmosphere is
controlled with use
of IG
Empty cargo tank
17. Cargo oil Pump
Main Suction
bell mouth
Suction line
Discharge line
Deck Discharge
line
Pump
room
Cargo
Oil Tank
Manifold
Pressure
Vacuum
valve
From Inert Gas System
Tank Cleaning Operation
Stripping Suction bell
mouth
Stripping line to Stripping
pump or Eductor
Generation
of static
electricity
due water
droplets
Wash water in
slop tank
Unsafe
Atmosphere
IG introduced to
maintain safe
atmosphere
18. After tank cleaning there are 3 operations which involve replacement of gas
in cargo tanks.
And there are 2 principal means of Gas Replacement for above
operations, these are :
Dilution , which is a mixing process
Displacement, which is layering process
Namely:
Purging (For reducing the hydrocarbon /H2S content )
Gas-freeing (For man-entry).
Inerting (For preparation before arrival load Port)
19. Dilution method
Dilution theory assumes Incoming
inert gas / air, mixes with the
original gas mixture in tank to
form a homogenous mixture
throughout the tank,
In result concentration of original
gas decreases gradually.
For complete replacement the entry velocity of incoming
gas should be high enough for the jet to reach the bottom
of tank.
Important!!!
Inert gas or
fresh air
Completion of gas
replacement
PV valve gas free
cover kept open
for venting.
20. Displacement method
For ideal replacement a stable
horizontal interface should be
formed between the lighter gas
entering at the top of tank and
heavier gas being displayed from
the bottom of tank through some
suitable pipping arrangment.
In result the tank atmosphere is
changed gradually.
For complete replacement a relativley low entry velocity of
gas is required. In practice more than one volume change
is necessary
Important!!!
Inert gas or
fresh air
Purge Pipe
kept open
for venting.
Completion of gas
replacement
21. Several arrangements are put in use on board tanker,
when using dilution or displacement method.
One feature which is common to all is that the inlet
and outlet points should be so located that efficient
gas replacement can take place through out the tank.
There are three principal arrangement:
Inlet Point Outlet point Principle
1. Top Top Dilution
2. Bottom Top Dilution
3. Top Bottom Displacement
or dilution
22. Displacement /Dilution method-using
bottom cargo lines from one tank to
other tank
Inert gas or
fresh air from
top PV valve gas free
cover kept open
for venting from
top
PV Valve on auto
mode.
Completion of gas
replacement by
displacement
Cargo Bottom line
Completion of gas
replacement by
dilution
23. Dilution method-using bottom cargo
lines from IG line to tank
Inert gas or
fresh air
Gas free cover on
PV Valve for
venting from top
Completion of gas
replacement
Inlet of gas
into tank
from bottom
24. Gas Freeing blowers
Used for
Gas freeing purposes
Continuous ventilation
during the duration of
man entry in cargo oil
tank
Butterworth holes for
cargo oil tank
Main deck
Ventilation ducts
25. Loading Operation
Bell mouth
Suction line
Cargo
in the
tank
Ullage
space
Drop line
Deck Cargo line
Cargo
Oil Tank
Manifold
Shore Hose / Arm
Pressure
Vacuum
valve
From pump room
IG line
Mast
Riser
Increase of level,
& reduction in
ullage space.
Increase of tank
pressure,as
loading is done in
closed ullaging
system to control
the safe
atmosphere in
tank
Venting done through the
Mast Riser connected to IG
line
26. For a safe and effective control of tank atmosphere, it is
important to know and understand the tank content at all stages
of operations.
There a various equipments available on board for the detecting
the contents in a cargo oil tank.
Some of these are:
Portable Oxygen Meter (To check oxygen content)
Explosimeter or Combustible Gas Indicator (To measure
hydrocarbon content in a gas free condition)
Tankscope (To measure hydrocarbon content in a inerted
condition)
Multi-Gas meters (Basically used to check oxygen,
hdrocarbon and any one toxic gas for a gas free tank).
Gas detector tubes (To measure other toxic gases such
as; ammonia, benzene, carbon monoxifr,mercaptans.)
Portable Gas Detectors on board
27. Oxygen meter Hydro carbon detector
Portable Gas Detectors on board
Multi
gas
Monitor Gas Detector Tubes