BIS - LIMS (Laboratory Information Management System)

INDIAN OIL CORPORATION LIMITED (IOCL), DELHI TERMINAL LABORATORY

INDIAN OIL CORPORATION LTD. (MARKETING DIVISION), DELHI TERMINAL, BIJWASAN, DELHI, South West, Delhi, 110061

9433060668 rrachana@indianoil.in

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S.No.

Indian Standard No.

Product

Grade / Type / Size / Designation etc.

Testing Charges (Excl. Of Taxes)

Validity Date

Remark

IS 15607 (2022)

Biodiesel B-100 - Fatty Acid Methyl Esters FAME Specification Second Revision

137590 View breakup
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Clause No.	Exclusion	Testing Charges (Excl. Of Taxes)	Remark
4.4-Table 1-i)(Appearance, visual)	-	200	-
4.4-Table 1-ii)(Colour, visual)	-	200	-
4.4-Table 1-iii)(Density at 15 °C, kg/m3)	-	1130	-
4.4-Table 1-iv)(Kinematic viscosity at 40 °C, cSt)	-	2270	-
4.4-Table 1-v)(Flash point (PMCC)1) °C, Min)	-	1900	-
4.4-Table 1-vi)(Total Sulphur, mg/kg, Max)	-	4710	-
4.4-Table 1-vii)(Carbon residue (MCR) 2) percent by mass, Max)	-	1900	-
4.4-Table 1-viii)(Sulfated ash, percent by mass, Max)	-	2270	-
4.4-Table 1-ix)(Water content mg/kg, Max)	-	4160	-
4.4-Table 1-xi)(Copper strip corrosion, 3 h at 50 °C, Max)	-	1130	-
4.4-Table 1-xiii)(Acid value, mg KOH/g, Max)	-	1530	-
4.4-Table 1-xiv)(Methanol, percent by mass, Max)	-	21350	-
4.4-Table 1-xv)(Ester content, percent by mass, Min)	-	13340	-
4.4-Table 1-xvi)(Monoglycerides content, percent by mass, Max)	-	22680	Combined rate for mono,di,tri,free & total glycerol.
4.4-Table 1-xvii)(Diglyceride content, percent by mass, Max)	-	22680	Combined rate for mono,di,tri,free & total glycerol.
4.4-Table 1-xviii)(Triglyceride content, percent by mass, Max)	-	22680	Combined rate for mono,di,tri,free & total glycerol.
4.4-Table 1-xix)(Free Glycerol percent by mass, Max)	-	22680	Combined rate for mono,di,tri,free & total glycerol.
4.4-Table 1-xx)(Total Glycerol percent by mass, Max)	-	22680	Combined rate for mono,di,tri,free & total glycerol.
4.4-Table 1-xxi)(Phosphorous mg/kg, Max)	-	2270	-
4.4-Table 1-xxii)(Sodium + Potassium mg/kg, Max)	-	4550	-
4.4-Table 1-xxiii)(Calcium + Magnesium mg/kg, Max)	-	4550	-
4.4-Table 1-xxv)(Oxidation stability, at 110 °C, Min hrs. Accelerated)	-	4280	-
4.4-Table 1-xxvi)(Cold filter plugging point (CFPP), °C Max a) summer 18 – Part 110 b) winter3))	-	1900	-
4.4-Table 1-xxvii)(Linolenic acid methyl ester, percent m/m, Max)	-	13340	-
4.4-Table 1-xxviii)(Polyunsaturated (>_ 4 double bonds) methyl ester percent m/m, Max)	-	17050	-
4.4-Table 1-x)(Total contamination, mg/kg, Max)	-	3440	-
4.4-Table 1-xxiv)(Iodine value, gm iodine/100 gm, Max)	-	3440	-

28 Nov, 2028

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4.1 (General) 4.2 (Additives) 4.3 (The materials shall be free from grit) 4.4-Table 1-xii) (Cetane No., Min) 5.1 (Packing) 5.2 (Marking)

IS 1459 (2018)

Kerosene - Specification (Fourth Revision)

11790 View breakup
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Clause No.	Exclusion	Testing Charges (Excl. Of Taxes)	Remark
4.2-Table 1-i)(Appearance)	-	200	-
4.2-Table 1-iv)(Colour a)Saybolt (in cas of undyedKerosene)3), Min b)Visual (in case of dyed Kerosene))	-	1130	-
4.2-Table 1-vi)(Density at 15°C, kg/m3)	-	1130	-
4.2-Table 1-v)(Copper strip corrosion for 3 h at 50°C)	-	1130	-
4.2-Table 1-vii)(Distillation a)Percent recovered below200°C, percent (v/v), Min b)Final boiling point, °C, Max )	-	2650	-
4.2-Table 1-viii)(Flash point ( Abel), °C, Min)	-	1900	-
4.2-Table 1-ix)(Smoke Point4), mm, Min)	-	1130	-
4.2-Table 1-x)(Total Sulphur Content, percent, m/m, Max)	-	2520	-

28 Nov, 2028

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4.2-Table 1-i) (Appearance) 4.2-Table 1-ii) (Acidity, inorganic) 4.2-Table 1-iii) (Burning quality2) a)Char Value, mg/kg of oil consumed, Max b)Bloom on glass Chimney) 5.1 (Packing) 5.2 (Marking)

IS 1460 (2025)

Automotive Diesel Fuel - Specification (seventh revision)

30000 View breakup
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Clause No.	Exclusion	Testing Charges (Excl. Of Taxes)	Remark
Cl-3.1.4 , 3.2, Table-1 (i)(Appearance)	-	200	-
Cl-3.1.4 , 3.2, Table-1 (xiii)(Density at 15 °C, kg/m3)	-	1130	-
Cl-3.1.4 , 3.2, Table-1 (ix)(Distillation, 95 percent v/v recovery, °C, Max)	-	2650	-
Cl-3.1.4 , 3.2, Table-1 (vi)(Cetane index, Min)	-	3770	-
Cl-3.1.4 , 3.2, Table-1 (vii) (a)(Pour point3, °C, Max: Winter)	-	1900	-
Cl-3.1.4 , 3.2, Table-1 (vii) (b)(Pour point3, °C, Max: Summer)	-	1900	-
Cl-3.1.4 , 3.2, Table-1 (x)(Flash point, Abel4, °C, Min)	-	1900	-
Cl-3.1.4 , 3.2, Table-1 (xi)(Kinematic viscosity, mm2/s, at 40 °C)	-	2270	-
Cl-3.1.4 , 3.2, Table-1 (xiv)(Total sulphur, mg/kg, Max)	-	4710	-
Cl-3.1.4 , 3.2, Table-1 (xviii)(Oxidation stability (for diesel fuel having FAME content of above 2 percent v/v), hours, Min)	-	4280	-
Cl-3.1.4 , 3.2, Table-1 (xvi) (a)(Cold Filter Plugging Point (CFPP)3, °C, Max: Winter)	-	1900	-
Cl-3.1.4 , 3.2, Table-1 (xvi) (b)(Cold Filter Plugging Point (CFPP)3, °C, Max: Summer)	-	1900	-
Cl-3.1.4 , 3.2, Table-1 (viii)(Copper strip corrosion for 3 h at 50 °C, Max)	-	1130	-
Cl-3.1.4 , 3.2, Table-1 (xv)(Water content, mg/kg, Max)	-	4160	-

28 Nov, 2028

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Cl-3.1 (General- Requirements) Cl-3.1.4 , 3.2, Table-1 (ii) C (Total Acid Number (TAN), mg of KOH/g, Max) Cl-3.1.4 , 3.2, Table-1 (iii) (Ash, percent by mass, Max) Cl-3.1.4 , 3.2, Table-1 (iv) (Carbon residue, on 10 percent residue1, percent by mass, Max) Cl-3.1.4 , 3.2, Table-1 (v) (Cetane number, Min) Cl-3.1.4 , 3.2, Table-1 (xii) (Total contamination, mg/kg, Max) Cl-3.1.4 , 3.2, Table-1 (xix) (Polycyclic Aromatic Hydrocarbon (PAH), percent by mass, Max) Cl-3.1.4 , 3.2, Table-1 (xvii) (Oxidation stability6, g/m3, Max) Cl-3.1.4 , 3.2, Table-1 (xvii) (Oxidation stability6, minutes, Min) Cl-3.1.4 , 3.2, Table-1 (xviii) (Oxidation stability (for diesel fuel having FAME content of above 2 percent v/v), minutes, Min) Cl-3.1.4 , 3.2, Table-1 (xx) (Lubricity, wear scar diameter (wsd) at 60 ºC, μm, Max) Cl-3.1.4 , 3.2, Table-1 (xxi) (FAME content7, percent v/v, Max) Cl-3.2 (Composition) Cl-5.2 (Marking)

IS 2796 (2017)

Motor gasoline - Specification (Sixth Revision)

30990 View breakup
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Clause No.	Exclusion	Testing Charges (Excl. Of Taxes)	Remark
Cl-4.1.4, 4.2.2 & 4.4, Table-1 (i)(Appearance)	-	200	-
Cl-4.1.4, 4.2.2 & 4.4, Table-1 (ii), a)("Colour: MG 91")	-	200	-
Cl-4.1.4, 4.2.2 & 4.4, Table-1 (iii)(Density at 15°C, kg/m³)	-	1130	-
Cl-4.1.4, 4.2.2 & 4.4, Table-1 (iv) (a)(percent evaporated at 70°C (E 70°C), percent v/v: E10)	-	530	-
Cl-4.1.4, 4.2.2 & 4.4, Table-1 (iv) (b)(percent evaporated at 100°C (E 100 °C), percent v/v)	-	530	-
Cl-4.1.4, 4.2.2 & 4.4, Table-1 (iv) (c)(percent evaporated at 150°C (E 150 °C), percent v/v, Min)	-	530	-
Cl-4.1.4, 4.2.2 & 4.4, Table-1 (iv) (d)(Final boiling point, °C, Max)	-	530	-
Cl-4.1.4, 4.2.2 & 4.4, Table-1 (iv) (e)(Residue, percent by volume, Max)	-	530	-
Cl-4.1.4, 4.2.2 & 4.4, Table-1 (vii)(Gum content (Solvent washed), g/m3, Max)	-	2070	-
Cl-4.1.4, 4.2.2 & 4.4, Table-1 (viii)(Total sulphur, mg/kg, Max)	-	4710	-
Cl-4.1.4, 4.2.2 & 4.4, Table-1 (xiii)(Copper strip corrosion, for 3 h at 50°C, Max)	-	1130	-
Cl-4.1.4, 4.2.2 & 4.4, Table-1 (ixi)(Ethanol content, percent by volume: a) Motor gasoline)	-	690	-
Cl-4.1.4, 4.2.2 & 4.4, Table-1 (v) (a)(Research octane number (RON), Min: MG 91)	-	18210	-

28 Nov, 2028

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Cl-4.1 (General- Requirements) Cl-4.1.2 (Antioxidants) Cl-4.1.3 (Metal Deactivators) Cl-4.1.4, 4.2.2 & 4.4, Table-1 (ii), b) ("Colour: MG 95") Cl-4.1.4, 4.2.2 & 4.4, Table-1 (iv) (a) (percent evaporated at 70°C (E 70°C), percent v/v: Motor gasoline) Cl-4.1.4, 4.2.2 & 4.4, Table-1 (ix) (Lead content (as Pb ), g/l, Max) Cl-4.1.4, 4.2.2 & 4.4, Table-1 (ixi) (Ethanol content, percent by volume: a):- E10) Cl-4.1.4, 4.2.2 & 4.4, Table-1 (ixi) (Oxygen content, percent by mass, Max) Cl-4.1.4, 4.2.2 & 4.4, Table-1 (v) (b) (Research octane number (RON), Min: MG 95) Cl-4.1.4, 4.2.2 & 4.4, Table-1 (vi) (a) (Motor octane number (MON),Min: MG 91) Cl-4.1.4, 4.2.2 & 4.4, Table-1 (vi) (b) (Motor octane number (MON),Min: MG 95) Cl-4.1.4, 4.2.2 & 4.4, Table-1 (x) (a) (Reid vapour pressure (RVP) at 38°C, kPa , Max: MG(without ethanol)) Cl-4.1.4, 4.2.2 & 4.4, Table-1 (x) (b) (Reid vapour pressure (RVP) at 38°C, kPa , Max: Ethanol blended MG) Cl-4.1.4, 4.2.2 & 4.4, Table-1 (xi) (a) (Vapour lock index (VLI),Max :- MG (without ethanol)) Cl-4.1.4, 4.2.2 & 4.4, Table-1 (xi) (b) (Vapour lock index (VLI),Max :- MG (with 5 percent v/v ethanol)) Cl-4.1.4, 4.2.2 & 4.4, Table-1 (xi) (c) (Vapour lock index (VLI),Max :- E10) Cl-4.1.4, 4.2.2 & 4.4, Table-1 (xii) (Benzene content, percent by volume, Max) Cl-4.1.4, 4.2.2 & 4.4, Table-1 (xiv) (a) (Water tolerance of motor gasoline-alcohol blends, temperature for phase separation:- Winter, °C, Max) Cl-4.1.4, 4.2.2 & 4.4, Table-1 (xiv) (b) (Water tolerance of motor gasoline-alcohol blends, temperature for phase separation:- Other months, °C, Max) Cl-4.1.4, 4.2.2 & 4.4, Table-1 (xv) (Engine intake system cleanliness) Cl-4.1.4, 4.2.2 & 4.4, Table-1 (xvi) (a) (Olefin content, percent by volume, Max: MG 91) Cl-4.1.4, 4.2.2 & 4.4, Table-1 (xvi) (b) (Olefin content, percent by volume, Max :MG 95) Cl-4.1.4, 4.2.2 & 4.4, Table-1 (xvii) (Oxidation stability, minutes, Min) Cl-4.1.4, 4.2.2 & 4.4, Table-1 (xviii) (Aromatics content, percent by volume, Max) Cl-4.1.4, 4.2.2 & 4.4, Table-1 (XXI) (Oxygenates percent by volume, Max) Cl-4.1.4, 4.2.2 & 4.4, Table-1 (XXI) (Oxygenates percent by volume, Max:- Ethers containing 5 or more ‘C’ atoms per molecules such as MTBE, ETBE or TAME) Cl-4.1.5 (Motor gasoline multifunctional additives (MFA),) Cl-4.2.1 (Organic Oxygenates- Permitted Components) Cl-4.3 (Other Requirements) Cl-5.2 (Markeing)

IS 1604 (2022)

Aviation gasoline - Specification (fifth revision)

12540 View breakup
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Clause No.	Exclusion	Testing Charges (Excl. Of Taxes)	Remark
4.2.2-Table 1-i)(Appearance)	-	200	-
4.2.2-Table 1-ii)(Copper strip corrosion for 2 h at 100°C)	-	1130	-
4.2.2-Table 1-iii)(Density at 15°C, kg/m3)	-	1130	-
4.2.2-Table 1-iv)(Distillation:)	-	2650	-
4.2.2-Table 1-v)(Existent gum, mg/100 ml, Max)	-	2070	-
4.2.2-Table 1-ix)(Reid vapour pressure at 38°C, kPa)	-	1900	-
4.2.2-Table 1-x)(Specific energy MJ/kg, Min or Product of API gravity and aniline point, Min)	-	2480	-
4.2.2-Table 1-xiii)(Water reaction: a) Interface rating, Max b) Volume change, ml, Max)	-	780	-
4.2.5(Colour)	-	200	-

28 Nov, 2028

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4.1 (General) 4.2 (Composition) 4.2.2-Table 1-vi) (Freezing point, °C, Max) 4.2.2-Table 1-vii) (Knock rating: a) Lean mixture,motor method,octane number, Min b) Rich mixture, octane number, Min c) Rich mixture, performance number, Min) 4.2.2-Table 1-viii) (Oxidation stability, 16 h: a) Potential gum, mg/100 ml, Max b) Potential gum, mg/100 ml, Max) 4.2.2-Table 1-xi) (Total sulphur percent m/m, Max) 4.2.2-Table 1-xii) (Tetraethyl lead, g Pb/l at 15°C, Max) 4.2.2-Table 1-xiv) (Electrical conductivity, pS/m) 4.2.3 (Static Dissipater Additive (SDA)) 4.2.4 (Dyes) 4.2.5 (Colour) 4.3 (Materials) 4.4 (Requirements) 6.1 (Packing) 6.2 (Marking)

IS 1571 (2018)

Aviation turbine fuels, kerosine type, jet - A - 1 - Specification (Tenth Revision)

33200.00 View breakup
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Clause No.	Exclusion	Testing Charges (Excl. Of Taxes)	Remark
Cl-3.2.2, 3.2.6, Table-1 (a)(Visual appearance)	-	200	-
Cl-3.2.2, 3.2.6, Table-1 (B)(Colour)	-	1130	-
Cl-3.2.2, 3.2.6, Table-1, (ii) (a)(Total acidi,t y mg KOHM/ga, x)	-	1530	-
Cl-3.2.2, 3.2.6, Table-1, (ii) (b)("Aromatics, percent by volMumaex, or Total Aromatics, percent by volume, Max")	-	2650	-
Cl-3.2.2, 3.2.6, Table-1, (ii) (c)(Total sulphur percent by mass, Max)	-	2650	-
Cl-3.2.2, 3.2.6, Table-1, (ii) (d)(Sulphur mercaptan, percent m/m. Max)	-	1900	-
Cl-3.2.2, 3.2.6, Table-1, (iii) (a), 1)(Distillation:- Initial boiling point, °)	-	378.57	-
Cl-3.2.2, 3.2.6, Table-1, (iii) (a), 2)(Distillation:- 10 percent recovery °Cv/,v , Max)	-	378.57	-
Cl-3.2.2, 3.2.6, Table-1, (iii) (a), 3)(Distillation:- 50 percent recovery °C, v/v)	-	378.57	-
Cl-3.2.2, 3.2.6, Table-1, (iii) (a), 4)(Distillation:- 90 percent recovery °C, v/v)	-	378.57	-
Cl-3.2.2, 3.2.6, Table- 1, (iii) (a), 5)(Distillation:- Final boiling point,°C, Max)	-	378.57	-
Cl-3.2.2, 3.2.6, Table-1, (iii) (a), 6)(Distillation:- Residue, percent v/v, Max)	-	378.57	-
Cl-3.2.2, 3.2.6, Table-1, (iii) (a), 7)(Distillation:- Loss, percent v/v, Max)	-	378.57	-
Cl-3.2.2, 3.2.6, Table-1, (iii) (b)(Flash point ( Abel ), °C, Min)	-	378.57	-
Cl-3.2.2, 3.2.6, Table-1, (iii) (c)(Density at 15°C,kg/m3)	-	1130	-
Cl-3.2.2, 3.2.6, Table- 1, (iv) (a)(Fluidity:- Freezing point, °C, Max)	-	2270	-
Cl-3.2.2, 3.2.6, Table-1, (iv) (b)(Fluidity:- Kinematic viscosity at minus 20°C, mm2/s, Max)	-	2270	-
Cl-3.2.2, 3.2.6, Table-1, (v) (a)(Specific energy10) MJ/kg, Min)	-	2480	-
Cl-3.2.2, 3.2.6, Table-1, (v) (b)(Smoke point, mm, Min or)	-	1130	-
Cl-3.2.2, 3.2.6, Table-1, (v) (b) 2)(Naphthalenes, percent v/v, Max)	-	2650	-
Cl-3.2.2, 3.2.6, Table-1, (vi) (a)(Copper strip corrosion for 2 h at 100°C)	-	1130	NA
Cl-3.2.2, 3.2.6, Table-1, (vi) (b)("Silver stripcorrosion12) classification, for 4 h at 50°C, Max")	-	1340	NA
Cl-3.2.2, 3.2.6, Table-1, (viii)(Contaminants: Existent gum, mg/100 ml, Max)	-	2070	-
Cl-3.2.2, 3.2.6, Table-1, (ix) a)(Water reaction: Interface rating16), Max)	-	780	-
Cl-3.2.2, 3.2.6, Table-1, (x)(Conductivity: Electrical conductivity, pS/m19))	-	1340	-
Cl-3.2.2, 3.2.6, Table-1, (ii) (e)(Doctor Test)	-	400	-
Cl-3.2.2, 3.2.6, Table-1, (ii) (b)(Aromatics, percent by vol (Defense requirements))	-	2650	-
Cl-3.2.2, 3.2.6, Table-1, (ii) (c)(Total sulphur percent by mass, Max (Defense requirements))	-	2650	-
Cl-3.2.2, 3.2.6, Table-1, (ii) (d)(Sulphur mercaptan, percent m/m. (Defense requirements))	-	1900	-
Cl-3.2.2, 3.2.6, Table-1, (vi) (b)(Silver stripcorrosion12) classification, for 4 h at 50°C, (Defense requirements))	-	1340	-
Amendment No.5 Table 3 Clause G-2.5 ii(Fluidity-Freezing point)	-	2270	-
Amendment No.5 Table 3 Clause G-2.5 iii(Aromatics)	-	2650	-
Amendment No.5 Table 3 Clause G-2.5 iv(Volatility- Distillation-T50 to T10, ℃)	-	2650	-
Amendment No.5 Table 3 Clause G-2.5 iv(Volatility- Distillation-T90 to T10, ℃)	-	2650	-

28 Nov, 2028

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Amendment No.5 Table 3 Clause G-2.5 i (Annex B VTR) Amendment No.5 Table 3 Clause G-2.5 i (Annex C ITR or Annex D ETR, average over an area of 2.5 mm2) Amendment No.5 Table 3 Clause G-2.5 i (Pressure differential) Amendment No.5 Table 3 Clause G-2.5 i (Test temperature for 2.5 h) Amendment No.5 Table 3 Clause G-2.5 i (Thermal stability) Amendment No.5 Table 3 Clause G-2.5 i (Tube Rating) Amendment No.5 Table 3 Clause G-2.5 ii (Fluidity-Viscosity at - 40 ℃) Amendment No.5 Table 3 Clause G-2.5 v (Lubricity) Amendment No.5 Table 3 Clause G-2.5 vi (Unconverted fatty acid esters and fatty acids) Cl-3.1 (General-Material) Cl-3.2 (Composition) Cl-3.2.1 (Antioxidants) Cl-3.2.2 (Metal Deactivator Additive (MDA)) Cl-3.2.2, 3.2.6, Table- 1, (xi) (Lubricity: Wear scar diameter, mm (defense requirements)) Cl-3.2.2, 3.2.6, Table- 1, (xi) (Lubricity: Wear scar diameter, mm, Max) Cl-3.2.2, 3.2.6, Table-1 (c) (Particulate contamination, at point of 1.02) manufacture, mg/l, Max) Cl-3.2.2, 3.2.6, Table-1 (d) 1) (Particulate, at point of manufacture, cumulative channel particle counts:- ≥ 4 μm©) Cl-3.2.2, 3.2.6, Table-1 (d) 2) (Particulate, at point of manufacture, cumulative channel particle counts:- ≥6 μm(c) Cl-3.2.2, 3.2.6, Table-1 (d) 3) (Particulate, at point of manufacture, cumulative channel particle counts:- ≥14 μm©) Cl-3.2.2, 3.2.6, Table-1 (d) 4) (Particulate, at point of manufacture, cumulative channel particle counts:- ≥21 μm©) Cl-3.2.2, 3.2.6, Table-1 (d) 5) (Particulate, at point of manufacture, cumulative channel particle counts:-≥25 μm©) Cl-3.2.2, 3.2.6, Table-1 (d) 6) (Particulate, at point of manufacture, cumulative channel particle counts:- ≥30 μm©) Cl-3.2.2, 3.2.6, Table-1, (ii) (f), 1) ("Refining components, at the point of manufacture8) :- Non Hydro processed Components, percent v/v") Cl-3.2.2, 3.2.6, Table-1, (ii) (f), 2) ("Refining components, at the point of manufacture8) :- Mildly Hydro processed Components, percent v/v") Cl-3.2.2, 3.2.6, Table-1, (ii) (f), 3) ("Refining components, at the point of manufacture8) :- Severely Hydro processed Components, percent v/v") Cl-3.2.2, 3.2.6, Table-1, (ii) (f), 4) ("Refining components, at the point of manufacture8) :- Synthetic Components, percenvt/ v") Cl-3.2.2, 3.2.6, Table-1, (iii) (a), 3) (Distillation:- 50 percent recovery °C, v/v) Cl-3.2.2, 3.2.6, Table-1, (ix) b), 1) ("Micro-separometer rating18) at the point of manufacture: - MSEP without SDA, Min") Cl-3.2.2, 3.2.6, Table-1, (ix) b), 2) ("Micro-separometer rating18) at the point of manufacture: MSEP with SDA, Min") Cl-3.2.2, 3.2.6, Table-1, (vii) (a) (Filter pressure differential, mm Hg, Max) Cl-3.2.2, 3.2.6, Table-1, (vii) (b) 1) (Tube rating, visual (VTR)) Cl-3.2.2, 3.2.6, Table-1, (vii) (b) 2) (ITR or ETR, average over area of 2.5 mm2 in nm) Cl-3.2.2, 3.2.6, Table-1, (xii) (Identified Incidental Materials :- Fatty Acid Methyl Ester, mg/kg, Max) Cl-3.2.2, 3.2.6, Table-1, (xii) (Identified Incidental Materials :- Fatty Acid Methyl Ester, mg/kg, Max) Cl-3.2.3 (Static Dissipater Additive (SDA)) Cl-3.2.4 (Lubricity Improver Additive (LIA)) Cl-3.2.5 (Fuel System Icing Inhibitor (FSII)) Cl-3.2.7 (Leak Detection Additive) Cl-5.2 (Marking)

Bureau of Indian Standards

The National Standards Body of India

INDIAN OIL CORPORATION LIMITED (IOCL), DELHI TERMINAL LABORATORY

INDIAN OIL CORPORATION LTD. (MARKETING DIVISION), DELHI TERMINAL, BIJWASAN, DELHI, South West, Delhi, 110061

9433060668 rrachana@indianoil.in

Scope List