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KALIMBASSIERIS MARITIME
KALIMBASSIERIS MARITIME
KALIMBASSIERIS MARITIME
KALIMBASSIERIS MARITIME
KALIMBASSIERIS MARITIME
KALIMBASSIERIS MARITIME
Dimitrios V. Giannakouros, Naval Architect & Marine Engineer
Technical Director, Kalimbassieris Maritime
The Marine Club, Thursday 8 November 2012
Technical Aspects
of Identifying and Managing
Bunker Problems
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1. ISO Standards
• ISO 8217:2005
• ISO 8217:2010
• ISO 8217:2012
2. Sampling operation
• Representative sampling
• IMO sampling guidelines
• In-line continuous drip sample
• Labelling / sealing of samples
• Pitfalls in sampling
3. Shore based testing of fuel
• Why
• Selection of laboratory
• Procedure
4. Off-spec bunkers
• True Value – Repeatability – Reproducibility
• When bunkers are considered off-spec
5. Engine problems due to off-spec bunkers
• Density
• Viscosity
• Sulphur
• Aluminium + Silicon
• Water
• Ash
• Vanadium
• Sodium
• CCAI
6. Suggestions / Conclusions
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Five editions:
• 1987 – first edition
• 1996 – not in use any more
• 2005 - most widely used specification
• 2010 – provides for better fuel quality
• 2012 - adding test method for H2S content
ISO 8217
Petroleum products – Fuels (class F) –
Specifications of marine fuels
Scope:
It specifies the requirements for petroleum fuels for use in marine
diesel engines and boilers, prior to appropriate treatment before
use
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• Max. water content 0.5% from 1%
• Max. sulphur content 4.5% from 5.0%
• Restriction of used lubrication oil (ULO) by setting max. limit for
Zn, Ca & P
• Max. ash level 0.15% from 0.2% (for some highly viscous grades)
• However, some characteristics not yet included or other with too
high limits (e.g. Al + Si, 80 ppm)
• 2005 version remains the most widely used specification although
since that time the Standard has been revised twice
ISO 8217:2005 – Major changes for residual fuels
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ISO 8217:2010 – Significant improvement of fuel quality
What is new in 2010 edition ?
Distillate Fuels Residual Fuels Purpose
Acid number Minimize damage to diesel engine fuel
injection from high acidic compounds
H2S
(from 1st July 2012)
Provide improved margin of safety by
reducing risk of exposure to shipboard
crew
Lubricity (for samples with S<0.05%)
Avoid fuel pump wear due to too low
lubricity
Oxidation stability Minimize addition of bio-diesel (FAME)
to reduce storage risk on board vessel
CCAI Avoid uncharacteristic density viscosity
relationship leading to ignition problem
Sodium Limit any sea water contamination and
restrict high temperature corrosion
• It specifies 4 categories of distillate fuel, one of which is for diesel
engines for emergency purposes, and 6 categories of residual fuel
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What has changed for residual fuels in 2010 edition ?
• RMA 10 grade was added (previous DMC grade)
• RMG and RMK grades were expanded to include additional
viscosity grades
• RMF and RMH grades were removed
• Sulphur limits were excluded from residual fuel limits, as these
are controlled by statutory requirements
• Sulphur limits for distillate fuels were retained
• Ash limit values, for residual fuels, were reduced for many of
the categories (RMG 380 from 0.15% m/m to 0.10% m/m)
• Vanadium limit for RMG 380 was increased from 300 ppm to
350 ppm
• Vanadium limits for other grades were reduced, but for RMB 30
where limit remained unchanged
• Catfine (Al + Si) limits were reduced from 80 ppm to 60 ppm
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Parameter Unit Limit DMX DMA DMZ DMB
Viscosity at 40°C mm²/s Max 5.500 6.000 6.000 11.00
Viscosity at 40°C mm²/s Min 1.400 2.000 3.000 2.000
Micro Carbon Residue
at 10% Residue % m/m Max 0.30 0.30 0.30 -
Density at 15°C kg/m3 Max - 890.0 890.0 900.0
Micro Carbon Residue % m/m Max - - - 0.30
Sulphur a % m/m Max 1.00 1.50 1.50 2.00
Water % V/V Max - - - 0.30 b
Total sediment by hot filtration % m/m Max - - - 0.10 b
Ash % m/m Max 0.010 0.010 0.010 0.010
Flash point 0°C Min 43.0 60.0 60.0 60.0
Pour point, Summer 0°C Max - 0 0 6
Pour point, Winter °C Max - -6 -6 0
Cloud point °C Max -16 - - -
Calculated Cetane Index Min 45 40 40 35
Acid Number mgKOH/g Max 0.5 0.5 0.5 0.5
Oxidation stability g/m3 Max 25 25 25 25 c
Lubricity, corrected wear scar
diameter (wsd 1.4) at 60°C d um Max 520 520 520 520 c
Hydrogen sulphide e mg/kg Max 2.00 2.00 2.00 2.00
Appearance Clear & Bright f b, c
ISO 8217:2010 - MARINE DISTILLATE FUELS
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a
A sulphur limit of 1.00% m/m applies in the Emission Control Areas designated by the International Maritime Organization. As there may be local variations, the purchaser shall define the maximum sulphur content according to the relevant statutory requirements, notwithstanding the limits given in this table.
b If the sample is not clear and bright, total sediment by hot filtration and water test shall be required.
c Oxidation stability and lubricity tests are not applicable if the sample is not clear and bright.
d Applicable if sulphur is less than 0.050% m/m.
e Effective only from 1 July 2012.
f If the sample is dyed and not transparent, water test shall be required. The water content shall not exceed 200 mg/kg (0.02% m/m).
ISO 8217:2010 - MARINE DISTILLATE FUELS
Explanatory notes
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Parameter Unit Limit RMA a RMB RMD RME RMG RMK
10 30 80 180 180 380 500 700 380 500 700
Viscosity at 50°C mm²/s Max 10.00 30.00 80.00 180.0 180.0 380.0 500.0 700.0 380.0 500.0 700.0
Density at 15°C kg/m3 Max 920.0 960.0 975.0 991.0 991.0 1010.0
Micro Carbon Residue % m/m Max 2.50 10.00 14.00 15.00 18.00 20.00
Aluminium + Silicon mg/kg Max 25 40 50 60
Sodium mg/kg Max 50 100 50 100
Ash % m/m Max 0.040 0.070 0.100 0.150
Vanadium mg/kg Max 50 150 350 450
CCAI - Max 850 860 870
Water % V/V Max 0.30 0.50
Pour point (upper) b,
Summer
°C Max 6 30
Pour point (upper) b,
Winter
°C Max 0 30
Flash point °C Min 60.0
Sulphur c % m/m Max Statutory requirements
Total Sediment, aged % m/m Max 0.10
Acid Number e mgKOH/g Max 2.5
Used lubricating oils
(ULO):
Calcium and Zinc; or
Calcium and
Phosphorus
mg/kg - The fuel shall be free from ULO, and shall be considered to contain ULO when either one of the following conditions is
met:
Calcium > 30 and zinc >15; or
Calcium > 30 and phosphorus > 15.
Hydrogen sulphide d mg/kg Max 2.00
ISO 8217:2010 - MARINE RESIDUAL FUELS
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a This residual marine fuel grade is formerly DMC distillate under ISO 8217:2005.
b Purchasers shall ensure that this pour point is suitable for the equipment on board, especially in cold climates.
c The purchaser shall define the maximum sulphur content according to the relevant statutory requirements.
d Effective only from 1 July 2012.
e
Strong acids are not acceptable, even at levels not detectable by the standard test methods for SAN. As acid numbers below the values stated in the table do not guarantee that the fuels are free from problems associated with the presence of acidic compounds, it is the responsibility of the supplier and the purchaser to agree upon an acceptable acid number.
ISO 8217:2010 - MARINE RESIDUAL FUELS
Explanatory notes
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Why to change to ISO 8217:2010 when ordering fuel?
• Provides for better fuel quality
• Improvement of the safety levels in shipboard operation
• Reduced engine damage and consequential risks
• Positively affects Owners’ image and reputation
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Therefore, when moving from ISO 8217:2005 ....
...go straight to ISO 8217:2012
• Became available on 15th August 2012, in response to concerns
for measuring H2S content
• Introduced test method, IP 570, Procedure A (with Vapour Phase
Processor) as the reference test method
ISO 8217:2012
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• Maybe the most important aspect during bunkering
• Provides evidence for possible quality disputes
• Should be carried out with methodical manner and utmost care
• Main objective: to obtain “representative” sample from the bunkered
fuel
• Very difficult in case of in-line blending
What is representative sample?
a product specimen having its physical
and chemical characteristics identical
to the average characteristics of the
total volume being sampled
IMO Resolution MEPC.182(59)
SAMPLING OPERATION
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IMO Resolution MEPC.182(59)
2009 Guidelines for the sampling of fuel oil for
determination of compliance with the revised MARPOL
Annex VI
• Came in response to Annex VI to MARPOL 73/78
(regulation 18.8.1: BDN shall be accompanied by
a representative sample of the fuel oil delivered)
• Is based on the ISO Technical report No. ISO/TR 13739
• Provides guidelines for sampling method & location, sample
taking, integrity, handling, sealing and storage
• Refers to MARPOL sample, only
• May form the basis for commercial sampling procedures, as
well
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The sample should be:
• Collected throughout the bunkering period
• Obtained by the sampling equipment positioned at the bunker
manifold of the receiving ship
• Obtained by manual valve-setting continuous-drip sampler; or
time / flow proportional automatic sampler
• Of sufficient quantity not less than 400 ml (bottle filled to 90% ±
5% capacity), properly sealed and labelled
• Kept in a safe storage location, not subject to elevated
temperatures, preferably at a cool/ambient temperature, and not
exposed to direct sunlight
• Retained under the ship’s control until the fuel oil is substantially
consumed, but in any case for a period of not less than 12 months
from the time of delivery
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In-line continuous drip sampling
• Manual or automatic
• Manual sampler developed by DNVPS
• Consists of sample probe with holes, screwed into stainless steel
flange, through which sample is collected in cubitainer
• Manual continuous drip sampling is as good as the automatic
one, provided recommended procedure will be followed with
care
Photos by
DNVPS
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• The sampler is connected
directly to the bunker manifold
by pipe fittings
• After start, it will fill one 5 litre
cubitainer and stop automatically
after the preset bunker time in
hours has expired
Automatic continuous bunker sampler
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Remember to:
1. Stir & Shake the cubitainer
before distributing the sample
2. Reduce viscosity of sample, if
cold weather, for assisting
mixing
3. Distribute evenly the
sample into individual
bottles, by filling
each bottle a little at
a time
4. Ensure that the
contents of each
bottle are similar
Photos by DNVPS
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How many sample bottles to prepare?
• One (1) To laboratory for testing
• One (1) To be kept onboard as reference
• One (1) To bunker suppliers
• One (1) MARPOL sample to be kept onboard for 12 months
(cannot be used for commercial analysis)
Totally 4 sample bottles (at least)
Photos by
DNVPS
KALIMBASSIERIS MARITIME
Maritime and Port Authority of
Singapore Code of Practice
for Bunkering (CP 60)
1. One sample for the vessel
2. One MARPOL sample for the
vessel’s retention
3. One sample for the bunker tanker
4. One sample for the bunker
surveyor, if engaged (if not,this
fourth sample shall be retained by
the bunker tanker)
5. One sample for the vessel, if the
vessel is on a fuel quality testing
programme (if not,this sample
needs not be collected)
• 5 samples to be collected:
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Sealing & Labelling
• Follow the IMO Guidelines - Resolution MEPC.182(59)
• Installation of security seal with identification no. by the
supplier’s representative in the presence of the ship’s staff
• The label of sample bottles should indicate:
1. location at which, and the method by which, the sample was
drawn;
2. date / place of commencement of delivery;
3. name of bunker tanker/bunker installation;
4. name and IMO number of the receiving ship;
5. signatures and names of the supplier’s representative and the
ship’s representative;
6. details of seal identification; and
7. bunker grade
• Seal number to be also recorded on the BDN
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Sampling can go wrong in case of:
• Taking spot samples from drain cocks
• Using a dirty continuous drip sampler
• Using unclean and wet cubitainer and sample bottles
• Pouring the cubitainer content into sample bottles without
shaking
• Unevenly distributing the bulk sample into the bottles
• Accepting uncontrolled samples given by the bunker suppliers
And always have in mind:
Testing results are as good as the
sample given for analysis
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SHORE BASED TESTING OF BUNKERED FUEL
Is it necessary and why?
1. Assess conformation with
specification or other quality
requirements
2. Decide on the acceptance of the
product prior to its use
Do not ignore that lack of testing or the improper use of off-spec
bunkers can lead to extensive damage to vessel’s machinery,
which is costly both to Owner and the insurer
3. Take the required measures onboard for fuel oil treatment,
aiming at minimizing the problems during or after consumption
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Criteria for laboratory selection
• Being independent
• Having experience with the testing of fuel oils
• Using the appropriate test methods as listed in the ISO 8217
Standard
• Being certified as per ISO or accredited as per National
accreditation scheme
• Providing results promptly
• Providing commercial & technical advice regarding the
results
• Being recognized by all parties in case of quality dispute
• The biggest not always the best
In case of doubt, seek advice from technical consultant
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Which is the procedure?
• Agreeing with the other parties on:
• Ensuring that the correct sample(s) is (are) brought to the lab
• Ensuring that all parties are in attendance
• Checking whether the seal of the bottle(s) is (are) intact
• Taking photos of the bottle/seal before breaking the seal
• Unsealing the bottle in the presence of parties in attendance
• Re-sealing the bottle with new seals, in case analysis is to be
repeated (at same or another lab)
• Signing a relevant unsealing/re-sealing protocol that is normally
prepared on the spot by the lab
– samples to be analysed
– nature and extent of analysis
– standards to be used
– laboratory to be used
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True value
• The limits specified in the ISO 8217 standard refer to the “true
value” of a given property as measured by the specified method
• True value is the average of an infinite number of single results
obtained by an infinite number of laboratories (ISO 4259:2006)
• The true value can never be obtained
Repeatability, r
The variation of results, when a fuel test is run a number of times
at the same laboratory, by the same person, on the same sample,
under the same conditions
Reproducibility, R
The variation of results, when two different laboratories test the
same sample using the same method
When bunkers are off spec ?
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After a single test result:
For the receiver, the fuel fails the specification limit,
with 95% confidence, only if:
• Test result > limit + 0.59 x R (for max. limits) or
• Test result < limit - 0.59 x R (for min. limits)
For the supplier, the fuel meets the specification limit,
with 95% confidence, only if:
• Test result ≤ limit - 0.59 x R (for max. limits) or
• Test result ≥ limit + 0.59 x R (for min. limits)
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Two examples:
Kinematic viscosity - RMG 380 grade
Maximum limit = 380 cSt at 50o C
R = 0.074 x 380
Variation (margin) of result = 0.59 x 0.074 x 380 cSt = 16.59 cSt
Therefore, a residual fuel of RMG 380 grade is considered to fail the
viscosity specification, with 95% confidence, if the single test result
is greater than 396.59 cSt at 50o C
Cat fines (Al + Si) - RMG 180 grade
Maximum limit = 60 ppm
R = 0.3345 x 60
Variation (margin) of result = 0.59 x 0.3345 x 60 ppm = 11.84 ppm
Therefore, a residual fuel of RMG 180 grade is considered to fail the
cat fines specification, with 95% confidence, if the single test result
is greater than 71.84 ppm
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Quality Parameter ISO Limit Reproducibility ‘R’ 0.59R Result ‘out of spec’
if above this value
(limit + 0.59R)
Viscosity at 50o C (max) 180 0.074x180=13.32 7.86 187.86
380 0.074x380=28.12 16.59 396.59
Density at 15o C (max) 991 1.5 0.885 991.885
Al+Si (ICP method) 60
0.3345x60=20.07 11.84 71.84
Flash Point (min) 60o C 6 3.54 56.46
Ash 0.1% 0.024 0.014 0.114
Total Sediment 0.1% 0.294x√0.1=0.055 0.032 0.132
Interpretation of a single test result
ISO 4259:2006
Petroleum products - Determination and application of precision
data in relation to methods of test
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• Contracts signed between fuel sellers and buyers, refer to ISO
4259
• In practice, test results are not interpreted according to ISO 4259
provisions
• It is common for the bunker receivers to raise a claim even when
the single test results are outside the limits prescribed by the ISO
8217 standard, i.e. without taking into account the R margins
• ISO 4529 provides a specific procedure if the receiver and the
supplier have tested the same sample in different laboratories and
find that they cannot agree on the value to be accepted
• Most bunker disputes between receivers and suppliers are solved
on commercial basis
• Owners to have in mind that if a dispute is referred to arbitration,
the suppliers are normally entitled to make use of the ISO 4259
Standard provisions
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SPECIFIED PARAMETERS FOR IFO 180 - RME 180 & TEST RESULTS
Parameters Units Test Results Specification Limits
------------------------------------------------------------------------------------------------------------
Density @ 15°C kg/m3 984.7 (991.0 Max)
Viscocity @50°C cSt 187.1 (180.0 Max)
Upper Pour Point °C 3 (30 Max)
Carbon Residue % (mass) 14.92 (15.00 Max)
Ash % (mass) 0.080 (0.100 Max)
Water % (vol) 0.30 (0.50 Max)
Sulphur % (mass) 2.85 (3.50 Max)
Total Sediment Pot. % (mass) 0.02 (0.10 Max)
Vanadium ppm 121 (200 Max)
Al + Si ppm 235 (80 Max)
Flash Point °C > 70 (60 Min)
Calcium ppm 7 (- Max)
Zinc ppm < 1 (- Max)
Phosphorus ppm 1 (- Max)
ADDITIONAL PARAMETERS
---------------------
Parameters Test Results Units
---------------------------------------------------------------------------------
Viscocity @100°C 22.6 cSt
API Gravity 12.12
Sodium 30 ppm
Aluminium 134 ppm
Silicon 101 ppm
Iron 26 ppm
Lead < 1 ppm
Nickel 28 ppm
Magnesium 2 ppm
Potassium 1 ppm
CALCULATED VALUES
-----------------
Parameters Computed Val Units
----------------------------------------------------------------------------------
Net specific energy 40.21 MJ/kg
Gross specific energy 42.51 MJ/kg
CCAI 853
Temperature at injection (for 13 cSt) 120 °C
Minimum Transfer Temperature 32 °C
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Density
• Max limits: 991 Kg/m3 (RMG Grade) & 1010 Kg/m3 (RMK Grade)
• It is the relation ship between mass and volume at a defined
temperature (15o C)
• Increased density may:
- Affect the centrifuge operation (ineffective in water removal)
- Affect the engine’s performance (increase of CCAI, with
viscosity constant)
- Reduce the specific energy of the fuel
• Reduced density than that declared by suppliers, results in
economical loss for the buyers; bunkers are sold by weight, but
delivered by volume
Example: Bunkered quantity delivered onboard: 2000 m3
Density, as declared by the suppliers: 991 Kg/m3
Density, as determined by the laboratory: 985 Kg/m3
Short delivery, 2000 m3 x (991–985) Kg/m3=12 tons
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Viscosity
• Viscosity is a measure of how fuel will flow and it varies with
temperature; as heavy oil is heated, it will flow more easily
• Viscosity is measured at 40o C for distillate and 50o C for residual
fuels
• For residual oils, the common viscosity is 180 cSt and 380 cSt, but
it reaches up to 700 cSt
• Viscosity greater than specified, may affect pumpability,
preheating, settling / separation, spray formation, atomization and
combustion
• The maximum viscosity of the fuel that can be used in an engine
depends on the heating facilities available
• However, too hot fuel, part of it may turn to gas at the injection
pumps, which is preventing the generation of proper injection
pressure
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Fuel Viscosity
cSt
Injection Temperature Fuel Viscosity
cSt
Injection Temperature
For 10 cSt For 15 cSt For 10 cSt For 15 cSt
100 117 101 320 142 125
120 121 105 340 143 126
140 124 108 360 145 127
160 127 111 380 146 128
180 130 113 400 147 129
200 132 116 420 148 130
220 134 118 440 149 131
240 136 119 460 149 132
260 138 121 480 150 133
280 139 122 500 151 134
300 141 124
• Increased viscosity is not a problem for the engine, provided that
it is reduced to levels recommended by the engine manufacturers
(10-15 cSt at engine inlet)
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Receipt Data Unit
------------ ----
Source Of Data Ch.Eng
Density @ 15oC kg/m3 968.2
Viscosity @ 50oC mm2/s 160.0
Sulfur % m/m 2.47
Test Parameter Unit Result RME180
-------------- ---- ------ ------
Density @ 15oC kg/m3 987.8 991.0
Viscosity @ 50oC mm2/s 306.7 180.0
Water % V/V 0.3 0.5
Micro Carbon Residue % m/m 14 15
Sulfur % m/m 2.52 4.50
Total Sediment Potential % m/m 0.01 0.10
Ash % m/m 0.08 0.10
Vanadium mg/kg 164 200
Sodium mg/kg 43
Aluminium mg/kg 13
Silicon mg/kg 14
Iron mg/kg 51
Nickel mg/kg 52
Calcium mg/kg 37
Magnesium mg/kg 3
Lead mg/kg LT 1
Zinc mg/kg 4
Phosphorus mg/kg 3
Potassium mg/kg LT 1
Pour Point oC LT 24 30
Flash Point oC GT 70 60
Calculated Values
-----------------
Aluminium + Silicon mg/kg 27 80
Net Specific Energy MJ/kg 40.28
CCAI (Ignition Quality) - 851
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Sulphur
• Sulphur content is dependant on the geographical source of crude
oil and the degree of blending with low-sulphur components
• Sulphur will burn to form sulphur oxides (SOx) which may convert
to corrosive acids under certain conditions (low temperatures) and
cause corrosion to low temperature zones (“cold corrosion”)
• Acidity is neutralized by the alkalinity of the cylinder lubricating
oil (BN)
• Selection of cylinder oil depending on the sulphur content of the
fuel oil
• Low-sulphur fuels (below 1%), if used with high BN cylinder
lubricating oil, will result in overdose with alkaline additives,
leading to alkaline deposits on the piston top land
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Accumulation of alkaline deposits on piston crown’s topland
• Alkaline deposits will scrape-off cylinder oil film, resulting in dry
friction between the cylinder wall and piston rings and the
development of cylinder liner scuffing
Recommended action:
• Carefully select the cylinder lubricating oil to be compatible
with fuel oil sulphur content
• Carry 2 grades of cylinder oil; one for use with high sulphur
fuel and the other for operation on low sulphur fuel
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Aluminium + Silicon
• Limit as per ISO 8217:2010, RMG & RMK grades – 60 ppm (previous
80 ppm)
• Hard and abrasive particles used as catalyst in petroleum refining
process
• Engine manufacturers limit the amount of catalytic fines in the
fuel injected into the engines to 15 mg/kg
• Not always evenly distributed in the fuel. Sometimes accumulated
in the sediment
• Very difficult to be removed, as they are attracted to water
droplets
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Exceeding the level of Al+Si of 15 mg/kg at the engine’s inlet ....
... may cause excessive wear of the components in the combustion
chamber (piston grooves, piston rings, cylinder liners) and of the fuel
injection equipment (fuel pump plunger and barrel, fuel injection
valves)
Photos by DNVPS
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Precautions to take:
• Maintain the separators according
to manufacturers’ instructions,
using approved spare parts
• Ensure efficient centrifuging
through FO separators, which will
reduce Al+Si content to
acceptable levels (reduced
throughput and temperature
around 98°C)
• Thorough separation required even if bunkered fuel within
specification (catfines settle in the tank and may be supplied
to the FO system during rough weather)
KALIMBASSIERIS MARITIME
Precautions to take: (continued)
• Consider reducing consumption/speed to ensure reduced flow
through separator
• Check fuel system efficiency by taking samples before and after
separator, to gauge the fuel oil quality, at intervals of 4 to 6
months
• Also take samples before engine inlet, to assess whether
makers’ requirements are met
• Clean storage, settling and service tanks at regular intervals
• Train personnel for the operation and maintenance of
separators
Embedded catfines (red arrows) and
abrasive wear traces
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• If accelerated cylinder liner wear (>0.1mm/1000 hrs), take replica
imprints for microscopic examination, to assess whether catfines
are embedded
Embedded catfines (red arrows) and
abrasive wear traces
Micrograph of normal surface
(20x magnification)
Micrograph of normal surface
(20x magnification)
Embedded catfines (red arrows) and
abrasive wear traces
Micrograph of normal surface
(20x magnification)
Micrograph of normal surface
(20x magnification)
Embedded catfines (red arrows) and
abrasive wear traces
Micrograph of normal surface
(20x magnification)
Embedded catfines (red arrows) and
abrasive wear traces
Micrograph of normal surface
(20x magnification)
Embedded catfines (red arrows) and
abrasive wear traces
Micrograph of normal surface
(20x magnification)
Embedded catfines (red arrows) and
abrasive wear traces
Micrograph of normal surface
(20x magnification)
Embedded catfines (red arrows) and
abrasive wear traces
KALIMBASSIERIS MARITIME
Water
• Allowed up to 0.5% v/v for residual fuels and 0.3% v/v for distillate
fuels (DMB)
• Water reduces specific energy
• Water may lead to a wide range of engine problems depending on
the source of the water; fresh or seawater
• Fresh water contamination from condensation, leaking steam
heating coils, badly set up centrifuges and rain water ingress
through tank lids or sounding pipes
• It may lead to corrosion damages to fuel pumps and injectors
• Removal of fresh water by centrifuging only if free in the fuel
(emulsification renders the separation difficult, if at all possible)
KALIMBASSIERIS MARITIME
• Seawater contamination, usually from bunkering barges, is more
serious because of the sodium content (1.0% seawater in the fuel
oil corresponds to 100ppm sodium)
• Ash deposits on exhaust valves and turbochargers
• High-temperature corrosion, as a result of chemical reaction
between the sodium and vanadium in the fuel, when
sodium/vanadium ratio = 1:3
• Recommended centrifuging
separation, sufficient settling time,
sufficient heating in the settling
tanks and by the use of proper
draining arrangements on the
settling and service tanks
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Ash
• Allowed up to 0.15% m/m, for residual and 0.01% m/m, for
distillate fuels
• During combustion, metal content is converted into solid ash
particles, which - at certain temperatures - become partly fluid,
adhering and causing corrosion damage to piston crowns, exhaust
valves, turbocharger blade surfaces and boiler tubes
• Stiction temperature is lowest for ashes that are rich in vanadium
and/or sodium
• A sodium/vanadium ratio of 1:3 is generally facilitating the
phenomenon of high temperature corrosion to occur, as ash
melting temperature is even below 400o C
• Ash removal recommended by frequent cleaning
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Vanadium
• Allowed up to 450 ppm for RMK and 350 ppm for RMG grades
• Vanadium in fuel oil occurs naturally and content varies depending
on the origin (Mexican & Venezuelan fuels with highest V content)
• Vanadium is not a major problem in itself, but it becomes an issue
when accompanied by high levels of sodium.
• No practical methods for removing vanadium onboard a ship. The
only way is to restrict V in the fuel oil is by lowering allowed limit
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Sodium
• Allowed up to 100 ppm for RMK & RMG grades
• Sodium is found originally in fuel oil and very occasionally the
sodium hydroxide used in the refining process
• Fuels normally have a sodium content between about 10 ppm and
50 ppm
• Sodium in contaminating seawater greatly increases the problems,
i.e. high temperature corrosion (1% by mass seawater 100 ppm
of sodium content)
• Unlike vanadium, sodium can be removed by water removal
(centrifugal treatment and settling)
• Also, high temperature corrosion problems are limited by:
- Efficient cooling of valve seats and faces
- Use of valve rotators to even out the thermal load on the valves
- Use of corrosion-resistant materials (stellite and nimonic steels)
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Calculated Carbon Aromaticity Index (CCAI)
• Introduced in ISO 8217:2010
standard. Max. limit 870 for
RMG & RMK grades
• CCAI is not determined by a
specific testing method, but
calculated with a specific
formula on the basis of
density and viscosity
• CCAI value can be read from
nomogram (aside)
• CCAI does not provide
information related to the
combustion characteristics,
but an indication of ignition
delay (knocking)
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• CCAI between 850 and 860 would
render better fuels. Residual fuels
with a CCAI higher than 870 are
often problematic
• FIA (Fuel Ignition Analysis) is a
reliable means to assess the
ignition quality of fuels based on
an actually measured ignition
delay
• Ignition quality of a fuel is
expressed as FIA CN (Cetane
Number), ranging for heavy fuels
from less than 18.7 to above 40
• The combustion properties of a
fuel are evaluated by means of the
ROHR (Rate of Heat Release)
curve. Fuel Ignition Analyser FIA 100/3
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Conclusions / Tips
• Order fuel to desired ISO grade and describe it in the charterparty,
as well as in the requisition to supplier
• Insist in the fuel meeting the specifications set out in
ISO8217:2010
• Take representative samples at the time of delivery. Ensure that
the samples taken are properly labelled
• If the supplier takes other samples at the time of the delivery, try
to establish how and when they were obtained. Protest if not
invited to witness the taking of these samples
• Make use of reliable fuel testing services such as DNV Petroleum
Services (DNVPS) or Lloyds Register (FOBAS)
• Segregate new fuel from that held on board (not always possible
though)
• Avoid using new fuel until the analysis results have been examined
and it has been established that it is suitable
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Conclusions / Tips (continued)
• Maintain records of previous bunkering operations, including BDN
and/or sampling reports
• Maintain careful reliable daily records of the contents and
consumption from each fuel tank
• Ensure good maintenance and calibration records are kept for all
machinery
• Ensure engine log books properly record all temperatures,
pressures and remarks of engine performance on a daily basis
• Consider de-bunkering of off-spec bunkers, if unsuitable for use
• If inferior quality bunkers have to be used, the charterers (if
purchased the fuel) and bunker supplier should be informed and
put on notice for possible damages. Insurers are also to be
informed
• Contact the engine manufacturer for advice, depending on which
parameter is off-specification and/or what the particular problem
is (the degree of quality deviation from the specification must be
considered)