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Straight Run Naphtha for Exportation


TEST METHOD SPECIFICATION
ASTM - D IP
Specific Gravity    @ 60/60 °F 1298 160 0.690 - 0.730
Colour VISUAL Colourless
R.V.P @ 100 °F     kg/cm2   max 323 69 0.7
Sulphur , Total   %mass   max 2622 107 0.03
Existent Gum     mg / 100 ml 381 131 1
Lead Content   P.P.B mass      max -- 224 10
Octane No. ( motor method )       min 2700 -- 50
Distillation : 86 123 --
Initial Boiling Point    °C -- -- 35-50
10% @   °C    max -- -- 75
50% @   °C    max -- -- 125
90% @   °C    max -- -- 155
Final Boiling Point      °C    max -- -- 185
PONA Analysis : 6730 -- 0.03
Paraffins     % vol -- -- Balance
Olefins   % vol   max & 0.5
Naphthenes    % vol    min -- -- 22.0
Aromatics   % vol -- -- 6 - 12
   * For Guidance Only

Turbine Jet A-1


TEST METHOD SPECIFICATION
ASTM - D IP
Density @15   °C   Kg/L 4052 -- 775 - 840
Appearance VISUAL Clear, Bright and visually free from solid matter and undissolved water at ambient temprature
Colour 156 -- Report
Particulate Contamination    mg/L 5452 -- (Max) 1.0
Total Acidity    mgKOH / g 3242 -- (Max) 0.015
Aromatics    % vol 1319 -- (Max)    25.0
Sulphur Total    % mass 2622 -- (Max)    0.30
Sulhper , Mercaptan    % mass 3227 -- (Max)    0.0030
Distillation : 86 -- --
Initial Boiling Point     °C -- Report
10% Recovered @    °C -- (Max)    205
50% Recovered @    °C -- Report
90% Recovered @    °C -- Report
End Point   °C -- (Max)   300
Residue    % vol -- (Max)    1.5
Loss    % vol -- (Max)    1.5
Flash Point    °C -- 170 (Min) 38
Freezing Point   °C 2386 -- (Max)   minus 47
Viscosity @ minus 20°C    mm2 / S   ( cSt ) 445 -- (Max)    8.0
Smoke Point    mm 1322 -- (Min)    19
Naphthalenes    % vol 1840 -- (Max)    3.0
Specific Energy, net    MJ / kg 4529 -- (Min)    42.8
Corrosion Copper Strip @ 100    °C   Class 130 -- (Max)    1
Thermal Stability ( JFTOT )   @ Control
Temp.  260 °C :
3241 --  
Tube Deposit Rating ( Visual ) -- Less Than 3, No Peacock (P)
Filter Pressure Differential    mm Hg -- (Max)    25
Existent Gum    mg / 100 ml 381 -- (Max)    7
Microseparometer (MSEP) : 3948 --  
Without SDA    Rating -- (Min)    85
With SDA    Rating -- (Min)    70
Electrical Conductivity    pS / M 2624 -- 50 - 600
Lubricity
BOCLE wear scar diameter,    mm
5001
--
-- (Max)   0.85
  •    The fuel is straight run and additives free (zero %) not hydrotreated.
  •    Product meets the requirements of AFQRJOS check list Issue 20 Expert for Electrical Conductivity.
  •    Results Comply with the Requirements of Def-Stan 91 - 91 Issue 6 Publication Date August 2008 for Turbine fuel.
  •    AFQRJOS check list Issue 20 Publication Date 1 October 2008.

Fuel Oil


TEST METHOD SPECIFICATION
ASTM - D IP
Specific Gravity @ 60 / 60 °F*   Max 1298 160 0.995
Kin. Vissosity @ 50°C cSt    Max 445 71 --
Summer ** -- -- (Max) 200
Winter *** -- -- (Max) 250
Viscosity R. 1 @ 100 °F    Sec. -- 70 --
Summer **    Max -- 2200
  Winter ***    Max -- 1700
Flash Point by P.M Closed    °C    Min 93 34 65
Bs & W    % vol    Max 4007 75 1
Calorific value (gross)   Max 4868 --  
MJ / KG -- (Min) 42
  Kcal / Kgm -- 10.000.0
    *  The Test for Guidance Only
   **  Summer : From April to October end.
  ***  Winter : From November to March end.

Gas Oil


TEST METHOD SPECIFICATION
ASTM - D IP
Density @15 °C    g / ml    Min
                                             Max
1298 160 0.820
0.870
  Color ASTM       Max 1500 197 4
Flash Point by P . M .  Closed °C    Min 93 34 55
Kin. Viscosity @ 40 °C    cSt   Min - Max 445 71 1.6 - 7
Redwood (1) Viscosity @    40 °C     Sec    Min - Max -- 70 30 - 43
Pour Point :     °C Max 97 15 --
Months   (Dec - Jan - Feb - Mar) -- 3
Months   (Apr - May - Oct - Nov) -- 9
Months   (Jun - July - Aug - Sep) -- 15
Water and Sediments   % vol   Max 2709 -- 0.1
Ash Content     % mass      Max 482 4 0.01
Sulfur , Total    % mass    Max 2622 -- 0.1
Inorganic Acids and Bases mg  KOH/100 ml    Max -- 177 NIL
Conradson Carbon    % mass     Max
  ( on 10% distillation residue )
189 13 0.1
Recovery @ 350 °C     % Vol    Min 86 123 85
Cetane Index    Min 4737 -- 46
Copper Strip Corrosion  (3hrs. @100°C )    Min 130 154 DIV. 1
Gross Calorific Value    MJ / KG     Min 4868 -- 44.3

Special Gasoil (Marine)


TEST METHOD (ASTM - D) SPECIFICATION
Density    @15 °C   g / cm3   Max 1298 0.85
Engler Viscosity     @ 20 °C 1660 1.35 - 1.68
Engler Viscosity     @ 50 °C 1660 1.15 - 1.29
Kin. Viscosity    @ 20 °C   cSt 445 4.6 - 8.3
Kin. Viscosity    @ 50 °C   cSt 445 2.5 - 4
Cetane   No.  or   Min 613 50
Cetane Index     Min 4737 50
Distillation : 86 --
50% Distilled   @ °C    Max -- 280
95% Distilled   @ °C    Max -- 340
Acidity   mg  KOH / 100ml    Max Ip-182 5
Ash Content    % mass   Max 482 0.02
Sulfur , Total    % mass    Max 2622 0.2
Copper Strip Corrosion (3hrs. @100°C )    Max 130 DIV. 1
Inorganic acids & bases   mg  KOH / 100ml    Max -- Nil
Pour Point °C    Max 97 Zero
Cloud Point    °C    Max 2500 5
Flash Point by P . M . Closed    °C    Min 93 90
Carbon Residue    % mass    Max
  ( on 10% distillation Residue )
189 0.5
    *  The Test for Guidance Only

Kerosene


TEST METHOD SPECIFICATION
ASTM - D IP
Density   @15 °C   g/ml   Max 1298 160 0.820
Flash Point by P. M. C. C    OR °C    Min 93 34 38
Able closed cup -- 170 38
  Smoke Point   mm    Min 1322 57 22
  Sulphur , Total    % mass   Max 2622 107 0.25
Copper strip Corrosion  (3hrs. @100 °C)   Max 130 154 DIV. 1
Distillation : 86 123 --
Recoverd   @ 200 °C   % vol   Min -- 20
F.B.P   °C    Max -- 300
Residue & loss   % vol    Max -- 2
Burning Test : -- 10 --
Consumption of Fuel   g / h    Max -- 24
General Appearance -- Normal
Flame Characteristics ofter 24 hrs
Flame width variation       mm    Max
Flame length vlowering    mm    Max
-- 10
--
--
--
6
5

Hydrotreated Kerosene


TEST METHOD SPECIFICATION
ASTM - D IP
Density     @15 °C   g/ml    Max 1298 160 0.783
Saybolt Colour    Min 156 -- +30
Flash Point by P. M. C. C   °C    Min 93 34 50
Distillation : -- -- --
- I.B.P    % vol    Min -- 186
- F.B.P    % vol    Max -- 214
Sulphur, Total     % wt     Max 1266 -- 0.001
Copper Strip Corrosion   (3Hrs@100°C)     Max 130 154 DIV. 1
Aromatics   % vol    Max UOP 744 1

JP5


TEST METHOD SPECIFICATION
ASTM - D IP
Density   @15 °C    g / ml    Max
                                                 Min
1298 160 0.788 - 0.845
Flash Point by   P . M .   Closed °C      Min 93 34 60
  Freezing Point   °C     Max 2386 16 Minus 46
  Smoke Point    mm     Min 1322 57 19
Kin. Viscosity     @ -20°    cSt 445 71 8.8
Sulfur, Total    % mass    Max 2622 107 0.4
Sulfur, Mercaptane     % mass      Max 3227 342 0.001
Acidity, Total    mg   KOH/g      Max 3242 354 0.015
Aromatics     %vol    Max 1319? 156 25
Olefins     %vol     Max 1319 156 5
Copper Strip Corrosion  (2 hrs.@100°C)    Max 130 154 1
Silver Strip Corrosion     Max -- 227 1
Existent Gum mg/100ml     Max 381 131 7
Water Separometer Index     Min 3948 -- 85
Water Reaction : 1094 289 --
Inter Face Rating     Max -- 1b
Separation     Max -- 2
Thermal Stability : 3241 323 --
Filter Pressure Differential       mmHg     Max -- 25
Tube Deposit Rating -- Less Than 3, No peacock
Distillation : 86 123 --
I.B.P    °C      Max -- Report
10% Recovered   @    °C      Max -- 205
20% Recovered   @    °C -- Report
50% Recovered   @    °C -- Report
90% Recovered   @    °C -- Report
F.B.P    °C    Max -- 290
Residue    %vol     Max -- 1.5
Loss     %vol     Max -- 1.5

Liquified Commercial Propane - Butane Gas


TEST METHOD SPECIFICATION
Density @15 °C    g/ml ASTM D - 1657 Reported
Vapour pressure @ 50 °C    Kg/cm2
Vapour pressure @ 50 °C    Kg/cm2
Vapour pressure @ 50 °C    Kg/cm2
ASTM D - 1267
ASTM D - 1267
ASTM D - D1267
Max 10    (1)
Max 11.5 (2)
Max 12.8 (3)
Volatility , 95 % vol. evaporated @ °C ASTM D - 1837 Max 2.2
Corrosion Copper strip ASTM D - 1838      (Summer)   (1)
8  (Transition)  (2)
4     (Winter)     (3)
Total Sulphur content    ( % wt ) ASTM D - 2784 0.014
Hydrogen sulphide    ( % wt ) ASTM D - 2420 Nil
Mercaptan Sulpher    ( % wt ) I P . 272 Min    0.003
Max    0.008
Free water Visual Nil
Calorific value    Kcal. / kg calculated Min    11800
  •    (1) Summer months     (May-June-July-August-Septemper).
  •    (2) Transition periods (March-April-October-November).
  •    (3) Winter months        (Desember-January-February).

Liquified Commercial Propane Gas


TEST METHOD SPECIFICATION
Vapour Pressure     @ 50 °C ASTM D - 1267 1667   KPa .    (Max)
17   K.g/cm2.  (Max)
Volatile Residue : -- --
A )   95 % Evaporated     @ °C ASTM D - 1837 - 38   ( Max )
B )   Butane & Heavier     ( % Liq. vol ) ASTM D - 2163 2.5   ( Max )
Residual Matter : -- --
A )   Residue after Evaporation
    100 ml of sample     @ 37.8 °C
-- 0.05 ml   ( Max )
B )   Spot oil test -- Pass
  Corrosion Copper Strip      (Max) ASTM D - 1838 No. 1
Volatile Sulphide   ( Grain / Cubic FT )   ( % wt ) -- 5           ( Max )
0.018   ( Max )
Hydrogen sulphide    ( % wt ) I . P - 103 0.001   ( Max )
MerCaptan Sulphur I . P - 104 0.006   ( Max )
Moisture Content     ( % wt ) -- Pass
Net Calorific Value   ( K.cal / kg ) ASTM D - 3588 11900   ( Min )
Chromatographic Analysis
  Propane      ( % wt )
ASTM D - 2163 93   ( Min )

Automative Gasoline Octane ( 95 )


TEST METHOD SPECIFICATION
ASTM - D IP
Density   @ 15 °C*    g / ml 1298 160 Reported
Color VISUAL Red
V.P ( Reid Method ) @ 100 °F kg / cm2 323 69  
Summer **      Max -- 0.63
Winter ***      Max -- 0.70
Copper strip Corrosion     ( 3hrs.@ 50 °C)       Max 130 154 DIV. 1
Sulfur , Total     % mass     Max 4294 -- 0.05
Existent Gum      mg / 100 ml      Max 381 131 3
Lead   @ 15 °C      gm / L    Max 3237 270 0.013
Octane Number ( Research Method )      Min 2699 237 80
Induction Period     @ 100 °C     minut     Min 525 40 360
Distillation : 86 123  
I . B . P     °C -- Reported
10 % Recoverd     °C      Max -- 70
50 % Recoverd     Max -- 105
90 % Recoverd      °C     Max -- 165
F . B . P     °C     Max -- 190
Residue and Loss      % vol     Max -- 2
Oxgynates content     % wt      Max 6730 -- 2.7
Benzole - Aromatic, olefins      % vol     Max 6729
or
6730
-- Report
    *  The Test for Guidance Only
   **  Summer : From April to October end.
  ***  Winter : From November to March end.