Introduction to Oil Cargo Loss

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    INTRODUCTION TO OIL CARGO LOSS

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    DESCRIPTION OF CARGO LOSS

    A. PHYSICAL OR ACTUAL LOSS:- is a type of cargo loss that physically or actually

    occurs during the subjected process.- Example : evaporation, leakage, slopping, pilferage,

    contamination, spillage etc.

    B. APPARENT OR SPURIOUS LOSS :- is a type of cargo loss that it is seen on the document,

    but physically does not occur.- Example : inaccurate B/L, Certificate of quality, Ullage

    report etc.

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    RECORD ON CLAIM OF CARGO LOSS

    1. Majority of claim on cargo loss are apparent cargoloss that discrepancy between shore and ship sides ordelivery and outturn figures are more than 0.5%.

    This case cannot be accepted, since there is noevident that is physical loss.

    2. The standard pleading for cargo loss in the past,0.5% could not be applied no longer. Now this limitshould be stipulated in the sale contract or charterparty. This figure is never accepted by USA & othercountries.

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    OIL LOSS

    DIFFERENCES/ CHANGE

    IN

    QUALITY & QUANTITY

    QUALITY DETERIORATION(Degradation, Contamination etc

    QUANTITY DIFFERENCESR 1 ,R 2 , R 3 ,R 4

    PHYSICAL LOSS

    (real loss, actually happen)

    APPARENT LOSS

    (spurious loss/on paper only)

    POTENTIAL FACTORS:1. Evaporation ( MINIMAL)

    2. Leakage or spillage

    3. Slopping

    4. Quality degradation or

    contamination

    5. Crime, etc

    POTENTIAL FACTORS:1. Inaccurate calibration: (expired, deformation, etc)

    - tanks (shore & ship),meter prover

    2. Inaccurate measurement:

    - temperature, gauging, water, sludge, clingage detection

    - rolling & pitching

    2. Inaccurate sampling:

    - method, equipment, position, etc

    2. Inaccurate laboratory analysis/determination:

    - density,

    OIL CARGO LOSSCLASSIFICATION

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    max. 0.5% max. 0.2%

    VEF analysis: Students table for 95% confidence limit Stable & consistent accurate

    max. 0.5%

    SHORETANKS

    Loading Losses: Transportation Losses: Discharging Losses:

    FACTORS OF APPARENT LOSSES:1. Inaccurate calibration:

    Shore tanks Vessel

    2. Inaccurate measurement

    Temperature Ullaging/gauging due to:- Pitching & rolling- Undetectable free water- Sludge or un-pump able

    materials (hard) Free water detection

    3. Sampling & analysis (density, %BS&W)4. Using different tables5. Improper filling of shore lines

    FACTORS OF PHYSICAL LOSSES:

    1. Evaporation2. Spillage or leakage3. Slopping

    4.

    Crime

    FACTORS OF APPARENT LOSSES:1. Inaccurate calibration:

    Vessel Shore tanks Weigh bridges

    2. Inaccurate measurement: Temperature Ullaging / gauging

    3. Using different Density4. Sampling & analysis (density)5. Improper filling of shorelines

    SHORETANK

    B/L(R2 or diff of 2-3)(R1 or diff of 1-2) (R3 or diff of 3-4)

    Supply Losses(R4 or diff of 1-4)max. 0.5%

    Negligible

    Sampling MP

    12 3 4

    VEF analysis VEF analysis

    GENERAL ACCEPTABLE LIMITS OF CARGODISCREPANCIES IN QUANTITY

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    SHORETANK

    Loading Losses: Transportation Losses: Discharging Losses:

    FACTORS AFFECTING APPARENT LOSSES:

    QUANTITY:

    1. Inaccurate calibration tables: Weighbridge Shore tanks Vessels tank

    2. Inaccurate measurement Temperature Sounding/Ullaging due to:- Rolling & Pitching- Overtrimmed or overlisted- Undetectable free water- Sludge or unpumpable materials- Accuracy of sounding/ullaging device

    3. Sampling & Analysis4. Improper filling or displacement of the shore lines

    QUALITY:

    1. Sampling (method, position & temperature)2. Sample compositing3. Analysis

    FACTORS AFFECTING PHYSICAL LOSSES :

    QUANTITY:

    1. Spillage or Leakage2. Slopping3. Pilferage

    QUALITY:

    Contamination due to: Spontaneous hydrolysis by moisture or free water Hydrolysis by water or sea water entrainment Reaction with the residue of the last cargoes Reaction with coating, tank or interior materials. Steam leaking (Heating system)

    SHORETANK

    B/L(R2 or diff of 2-3)

    max. 0.2%

    (R1 or diff of 1-2)

    max. 0.5%

    (R3 or diff of 3-4)

    max. 0.5%

    1 2 3 4

    Supply Losses(R4 or diff of 1-4)

    max. 0.5%

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    RATIO OF CARGO LOSS

    R 1 = loading loss = B/L Qty loaded x 100%B/L

    R 2 = transportation loss = SFAL SFBD x 100%B/L

    R 3 = discharging loss = Qty recd Qty dischd x 100%B/L

    R 4 = supply loss = B/L Qty recd x 100%B/L

    Legends:B/L = Bill of LadingSFAL = ships figure after loading SFBD = ships figure before discharging

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    SHIPBOARD QUANTITY DETERMINATIONENVIRONTMENTCONDITION

    CHARACT. OFCARGO

    TEMP. DRAFT / TRIM GAUGING LIST FWDETECTION

    TRIMCORRT

    LISTCORRT

    MEASUREMENT& READING

    SAMPLING

    LAB. ANALYSIS

    ASTM, API, IPTABLES

    OLD & NEW

    DENSITY 15(API GRAVITY,

    REL. DENS)

    WCF

    VCF

    CORRECTEDGAUGE

    TOV

    GOV

    NSV

    GSV

    NET WEIGHT

    % S&W

    VOLFW

    SHIPS

    TANK CALIBRTABLES

    ENVIRONTMENTCONDITION

    Note :

    Trim & List Corrections shallbe deleted for shore quantity

    determination

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    TYPICAL DIFFERENCE OF VCF BETWEEN OLD & NEW ASTMTABLES

    ( FOR API = 33.0 )

    No. TEMP. F OLD TABLE NEW TABLE DIFFERENCE ,%

    1. 50 1.0044 1.0046 + 0.022. 60 1.0000 1.0000 0.003. 70 0.9956 0.9954 - 0.024. 80 0.9913 0.9907 - 0.065. 90 0.9869 0.9861 - 0.086. 100 0.9826 0.9814 - 0.127. 110 0.9782 0.9768 - 0.148. 120 0.9739 0.9721 - 0.18

    9. 130 0.9695 0.9674 - 0.21

    CATATAN : TEMP. MAKIN JAUH DARI 60 F, BEDA VCF MAKIN BESAR .

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    CARGO RECONCILIATION

    1. IF THE DISCREPANCY BETWEEN SHORE AND SHIP FIGURESEXCEEDS THE ACCEPTABLE/ ALLOWABLE LIMIT , CHECK

    SHORE & SHIP FIGURES CALCULATION .

    2. ENSURE THE LINE IS FULL.

    3. REGAUGE SHORE & SHIP SIDES , INCL. TEMPERATURE, FW,SUITABILITY OF THE MEASURING DEVICES USED, REF.HEIGHT ETC.

    4. ENSURING THAT THERE IS NO MISFLOW/ MISLOADED/MISDISCHARGED:- CHECK COFFERDAM, DEEP TANK, BALLAST TANK, FORE

    PEAK, BUNKER AND OTHER HIDEN SPACES.

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    Continued

    - CHECK DATA OF INITIAL & FINAL QUANTITY OF BUNKER ANDFUEL CONSUMPTION OF THE VESSEL.

    - CHECK OBQ OR ROB AND RESIDUAL CARGO REMAINING ONBOARD OR AT THE SHORE/ STORAGE TANK(S) WHETHER

    ANY CLINGANGE, SEDIMENT, SLUDGE OR OTHERUNPUMPABLE MATERIALS ?

    5. ANALYSE DIFFERENCE OF FIGURES PER SEGMENT ANDQUANTITY COMPONENT .- CHECK THE CORRESPONDING COMPONENT PER SEGMENT.- CHECK PETROLEUM TABLE APPLIED, DENSITY, % S & W,

    TEMPERATURE, SEA CONDITION, VEF ETC.

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    APPARENT LOSS IN QUANTITY

    A. CAUSES :

    - INACCURATE GAUGING & TEMP. MEASUREMENT ( method,equipment, condition, skill etc )

    - INACCURATE CALIBRATION OF SHIP, SHORE TANKS ANDFLOWMETER.

    - DISTURBED CONDITIONS ( cargo properties, surroundings,vessel position & stability etc )

    - INACCURATE SAMPLING & ANLYSIS

    - DIFFERENT OR INACCURATE TABLE USED & INACCURATECALCULATION.

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    Continued

    B. PROTECTIVE & PREVENTIVE ACTIONS:

    - ACCURATE GAUGING & TEMP. MEASUREMENT.

    - ACCURATE SAMPLING & ANALYSIS

    - SAME TABLE & METHOD OF CALCULATION.

    - MINIMIZE CONDITION DISTURBANCE.

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    APPARENT LOSS IN QUALITY

    A. CAUSES:

    - INACCURATE SAMPLING ( method, equipment, samplingpoint, sample preparation etc ).

    - INACCURATE ANALYSIS ( method, equipment, preparation,calculation etc ).

    B. PROTECTIVE & PREVENTIVE ACTIONS:

    - ACCURATE SAMPLING & SAMPLE PREPARATION.- ACCURATE ANALYSIS

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    PHYSICAL LOSS IN QUALITY

    A. CAUSE:

    - CONTAMINATION, QUALITY DETERIORATION, ON FIRE/EXPLOSION ETC.

    B. PROTECTIVE & PREVENTIVE ACTION :

    - CLEAN & DRY COMPARTMENT WITH SUITABLE MATERIAL,- TANK CLEANING, GASING UP, INERTING, N2 BLANKETING

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    CARGO LOSS CONTROL

    1. CRUDE OIL WASHING ( COW ):

    - improvement discharge operation by spraying the tank wall withher own cargo.

    2. GASING UP:- removing residual gas in a confined space by blowing with fresh

    air ( gas freeing ), inert gas, nitrogen or loading vapor ( purging ).

    3 . HEATING:- increasing temperature for preventing solidification of the cargo.

    4. RELIEF VALVE:- a device for retaining gas in a tank/ vessel up to certain

    pressure.

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    CLOSING SPEECH

    THANK YOU FOR YOUR KIND ATTENTIONGOOD LUCK