BIS - LIMS (Laboratory Information Management System)

Indian Oil Corporation Ltd(IOCL), Visakha Smart Laboratory

IOCL Visakha Terminal, Malkapuram,, Visakhapatnam, Visakhapatanam, Andhra Pradesh, 530011

8332975583 bsrikanth@indianoil.in

Scope List

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6 Results

S.No.

Indian Standard No.

Product

Grade / Type / Size / Designation etc.

Testing Charges (Excl. Of Taxes)

Validity Date

Remark

IS 1593 (2018)

Fuel oils - Specification (Third Revision)

21110 View breakup
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Clause No.	Exclusion	Testing Charges (Excl. Of Taxes)	Remark
4.2(Pour Point)	-	1900	For the financial year 2025-26
4.3(Asphaltene Content)	-	2270	For the financial year 2025-26
4.4(TOTAL SEDIMENT)	-	1740	For the financial year 2025-26
4.5(Spot Test)	-	410	For the financial year 2025-26
4.6-Table 1-i)(Acidity, inorganic)	-	960	For the financial year 2025-26
4.6-Table 1-ii)(Ash, percent by mass, Max)	-	2070	For the financial year 2025-26
4.6-Table 1-iv)(Gross, calorific value)	-	780	For the financial year 2025-26
4.6-Table 1-v)(Density at 15°C kg/m3or Relative density at 15.6/15.6°C)	-	1130	For the financial year 2025-26
4.6-Table 1-vi)(Flash point (Pensky Martens (closed), °C, Min)	-	1900	For the financial year 2025-26
4.6-Table 1-vii)(Kinematic viscosity in centistokes at 50°C)	-	2270	For the financial year 2025-26
4.6-Table 1-viii)(Sediment, percent by mass, Max)	-	1740	For the financial year 2025-26
4.6-Table 1-ix)(Sulphur, total, percent by mass, Max2))	-	2650	For the financial year 2025-26
4.6-Table 1-x)(Water content, percent by volume, Max)	-	1130	For the financial year 2025-26
4.6-Table 1-iii)(Carbon residue, mass percent, Max)	-	1900	For the financial year 2025-26

14 Nov, 2028

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Excluding: 4.1 (General) 5.1 (Packing) 5.2 (Marking)

IS 15770 (2021)

Heating Oil(LDO) - Specification

18590 View breakup
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Clause No.	Exclusion	Testing Charges (Excl. Of Taxes)	Remark
3.2-Table 1-i)(Acid number, mg KOH/gm, Max)	-	1140	For the financial year 2025-26
3.2-Table 1-ii)(Ash, percent by mass, Max)	-	2070	For the financial year 2025-26
3.2-Table 1-iv)(Pour Point, °C, Max a) Winter [November toFebruary (both months inclusive)], b) Summer (rest of the months in a year))	-	1900	For the financial year 2025-26
3.2-Table 1-vi)(Flash point, Pensky Martens ,°C, Min)	-	1900	For the financial year 2025-26
3.2-Table 1-vii)(Kinematic viscosity at 40 °C, mm2 /sec)	-	2270	For the financial year 2025-26
3.2-Table 1-ix)(Density at 15 °C, Kg/m3)	-	1130	For the financial year 2025-26
3.2-Table 1-x)(Water content, percent by volume, Max)	-	1130	For the financial year 2025-26
3.2-Table 1-xi)(Total sulphur, percent by mass)	-	2650	For the financial year 2025-26
3.2-Table 1-viii)(Sediment, percent by mass, Max)	-	1740	For the financial year 2025-26
3.2-Table 1-iii)(Carbon residue, on whole samples, percent by mass, Max)	-	1530	For the financial year 2025-26
3.2-Table 1-v)(Copper strip corrosion for 3 h at 100 °C)	-	1130	For the financial year 2025-26

14 Nov, 2028

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Excluding: 3.1 (General) 5.1 (Packing) 5.2 (Marking)

IS 16861 (2018)

High flash high speed diesel fuel - Specification

25910 View breakup
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Clause No.	Exclusion	Testing Charges (Excl. Of Taxes)	Remark
3.3-Table 1-i)(Appearance)	-	200	For the financial year 2025-26
3.3-Table 1-ii)(Acid Number, mg KOH/g, Max)	-	2270	For the financial year 2025-26
3.3-Table 1-iii)(Ash, percent by mass, Max)	-	2070	For the financial year 2025-26
3.3-Table 1-iv)(Carbon residue on the 10 percent Volume Distillation Residue, mass %, Max)	-	1530	For the financial year 2025-26
3.3-Table 1-vi)(Pour Point2), Max a) Winter b) Summer)	-	1900	For the financial year 2025-26
3.3-Table 1-v)(Cetane index1), Min)	-	3770	For the financial year 2025-26
3.3-Table 1-vii)(Copper strip Corrosion for 3 h at 100°C)	-	1130	For the financial year 2025-26
3.3-Table 1-viii)(Distillation, percent (v/v), recovered a) at 350°C, Min b) at 370°C Min)	-	2650	For the financial year 2025-26
3.3-Table 1-ix)(Flash Point Pensky Martens closed cup °C, Min)	-	1900	For the financial year 2025-26
3.3-Table 1-x)(Kinematic viscosity, cSt, at 40°C)	-	2270	For the financial year 2025-26
3.3-Table 1-xi)(Density3) at 15°C, kg/m3 , Max)	-	1130	For the financial year 2025-26
3.3-Table 1-xii)(Total sulphur4), % by mass, Max)	-	4710	For the financial year 2025-26
3.3-Table 1-xiii)(Water content, ppm, max.)	-	4160	For the financial year 2025-26

14 Nov, 2028

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Excluding: 3.1 (General) 3.2 (Composition) 3.3-Table 1-xv) (Oxidation Stability), g/m3 , Max) 3.3-Table 1-xvi) (Lubricity), Corrected WSD at 60°C, microns max) 5.1 (Packing) 5.2 (Marking)

IS 1571 (2018)

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

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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	For the financial year 2025-26
Cl-3.2.2, 3.2.6, Table-1 (B)(Colour)	-	1130	For the financial year 2025-26
Cl-3.2.2, 3.2.6, Table-1, (ii) (a)(Total acidi,t y mg KOHM/ga, x)	-	1530	For the financial year 2025-26
Cl-3.2.2, 3.2.6, Table-1, (ii) (b)("Aromatics, percent by volMumaex, or Total Aromatics, percent by volume, Max")	-	2650	For the financial year 2025-26
Cl-3.2.2, 3.2.6, Table-1, (ii) (c)(Total sulphur percent by mass, Max)	-	2650	For the financial year 2025-26
Cl-3.2.2, 3.2.6, Table-1, (ii) (d)(Sulphur mercaptan, percent m/m. Max)	-	1900	For the financial year 2025-26
Cl-3.2.2, 3.2.6, Table-1, (ii) (e)(Doctor Test)	-	400	For the financial year 2025-26
Cl-3.2.2, 3.2.6, Table-1, (iii) (a), 1)(Distillation:- Initial boiling point, °)	-	0	For the financial year 2025-26
Cl-3.2.2, 3.2.6, Table-1, (iii) (a), 2)(Distillation:- 10 percent recovery °Cv/,v , Max)	-	0	For the financial year 2025-26
Cl-3.2.2, 3.2.6, Table-1, (iii) (a), 3)(Distillation:- 50 percent recovery °C, v/v)	-	0	For the financial year 2025-26
Cl-3.2.2, 3.2.6, Table-1, (iii) (a), 3)(Distillation:- 50 percent recovery °C, v/v)	-	0	For the financial year 2025-26
Cl-3.2.2, 3.2.6, Table-1, (iii) (a), 4)(Distillation:- 90 percent recovery °C, v/v)	-	0	For the financial year 2025-26
Cl-3.2.2, 3.2.6, Table- 1, (iii) (a), 5)(Distillation:- Final boiling point,°C, Max)	-	2650	For the financial year 2025-26
Cl-3.2.2, 3.2.6, Table-1, (iii) (a), 6)(Distillation:- Residue, percent v/v, Max)	-	0	For the financial year 2025-26
Cl-3.2.2, 3.2.6, Table-1, (iii) (a), 7)(Distillation:- Loss, percent v/v, Max)	-	0	For the financial year 2025-26
Cl-3.2.2, 3.2.6, Table-1, (iii) (b)(Flash point ( Abel ), °C, Min)	-	1900	For the financial year 2025-26
Cl-3.2.2, 3.2.6, Table-1, (iii) (c)(Density at 15°C,kg/m3)	-	1130	For the financial year 2025-26
Cl-3.2.2, 3.2.6, Table- 1, (iv) (a)(Fluidity:- Freezing point, °C, Max)	-	2270	For the financial year 2025-26
Cl-3.2.2, 3.2.6, Table-1, (iv) (b)(Fluidity:- Kinematic viscosity at minus 20°C, mm2/s, Max)	-	2270	For the financial year 2025-26
Cl-3.2.2, 3.2.6, Table-1, (v) (a)(Specific energy10) MJ/kg, Min)	-	2480	For the financial year 2025-26
Cl-3.2.2, 3.2.6, Table-1, (v) (b)(Smoke point, mm, Min or)	-	1130	For the financial year 2025-26
Cl-3.2.2, 3.2.6, Table-1, (v) (b) 2)(Naphthalenes, percent v/v, Max)	-	2650	For the financial year 2025-26
Cl-3.2.2, 3.2.6, Table-1, (vi) (a)(Copper strip corrosion for 2 h at 100°C)	-	1130	For the financial year 2025-26
Cl-3.2.2, 3.2.6, Table-1, (vi) (b)("Silver stripcorrosion12) classification, for 4 h at 50°C, Max")	-	1340	For the financial year 2025-26
Cl-3.2.2, 3.2.6, Table-1, (viii)(Contaminants: Existent gum, mg/100 ml, Max)	-	2070	For the financial year 2025-26
Cl-3.2.2, 3.2.6, Table-1, (ix) a)(Water reaction: Interface rating16), Max)	-	780	For the financial year 2025-26
Cl-3.2.2, 3.2.6, Table-1, (x)(Conductivity: Electrical conductivity, pS/m19))	-	780	For the financial year 2025-26

14 Nov, 2028

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Excluding: Cl-3.1 (General-Material) Cl-3.2 (Composition) Cl-3.2.1 (Antioxidants) Cl-3.2.2 (Metal Deactivator Additive (MDA)) Cl-3.2.3 (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) 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, (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, (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, (xi) (Lubricity: Wear scar diameter, mm, Max) Cl-3.2.2, 3.2.6, Table-1, (xii) (Identified Incidental Materials :- Fatty Acid Methyl Ester, mg/kg, Max) Cl-5.2 (Marking) Amendment No.5 Table 3 Clause G-2.5 i (Thermal stability) 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 (Tube Rating) 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 ii (Fluidity-Freezing point) Amendment No.5 Table 3 Clause G-2.5 ii (Fluidity-Viscosity at - 40 ℃) Amendment No.5 Table 3 Clause G-2.5 iii (Aromatics) Amendment No.5 Table 3 Clause G-2.5 iv (Volatility- Distillation-T50 to T10, ℃) Amendment No.5 Table 3 Clause G-2.5 iv (Volatility- Distillation-T90 to T10, ℃) 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-3.2.2, 3.2.6, Table- 1, (xi) (Lubricity: Wear scar diameter, mm, Max)

IS 1460 (2025)

Automotive Diesel Fuel - Specification (seventh revision)

29680 View breakup
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Clause No.	Exclusion	Testing Charges (Excl. Of Taxes)	Remark
Cl-3.1.4 , 3.2, Table-1 (vii) (a)(Pour point3, °C, Max: Winter)	-	1900	For the financial year 2025-26
Cl-3.1.4 , 3.2, Table-1 (i)(Appearance)	-	200	For the financial year 2025-26
Cl-3.1.4 , 3.2, Table-1 (vi)(Cetane index, Min)	-	0	For the financial year 2025-26
Cl-3.1.4 , 3.2, Table-1 (vii) (b)(Pour point3, °C, Max: Summer)	-	1900	For the financial year 2025-26
Cl-3.1.4 , 3.2, Table-1 (viii)(Copper strip corrosion for 3 h at 50 °C, Max)	-	1130	For the financial year 2025-26
Cl-3.1.4 , 3.2, Table-1 (ix)(Distillation, 95 percent v/v recovery, °C, Max)	-	2650	For the financial year 2025-26
Cl-3.1.4 , 3.2, Table-1 (x)(Flash point, Abel4, °C, Min)	-	1900	For the financial year 2025-26
Cl-3.1.4 , 3.2, Table-1 (xi)(Kinematic viscosity, mm2/s, at 40 °C)	-	2270	For the financial year 2025-26
Cl-3.1.4 , 3.2, Table-1 (xiii)(Density at 15 °C, kg/m3)	-	1130	For the financial year 2025-26
Cl-3.1.4 , 3.2, Table-1 (xiv)(Total sulphur, mg/kg, Max)	-	4710	For the financial year 2025-26
Cl-3.1.4 , 3.2, Table-1 (xv)(Water content, mg/kg, Max)	-	4160	For the financial year 2025-26
Cl-3.1.4 , 3.2, Table-1 (xvi) (a)(Cold Filter Plugging Point (CFPP)3, °C, Max: Winter)	-	1900	For the financial year 2025-26
Cl-3.1.4 , 3.2, Table-1 (xvi) (b)(Cold Filter Plugging Point (CFPP)3, °C, Max: Summer)	-	1900	For the financial year 2025-26
Cl-3.1.4 , 3.2, Table-1 (ii) C(Total Acid Number (TAN), mg of KOH/g, Max)	-	2270	For the financial year 2025-26
Cl-3.1.4 , 3.2, Table-1 (iii)(Ash, percent by mass, Max)	-	2070	For the financial year 2025-26
Cl-3.1.4 , 3.2, Table-1 (iv)(Carbon residue, on 10 percent residue1, percent by mass, Max)	-	1530	For the financial year 2025-26
Cl-3.1.4 , 3.2, Table-1 (xii)(Total contamination, mg/kg, Max)	-	3440	For the financial year 2025-26
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	For the financial year 2025-26
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)	-	4280	For the financial year 2025-26

14 Nov, 2028

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Excluding: Cl-3.1 (General- Requirements) Cl-3.2 (Composition) Cl-3.1.4 , 3.2, Table-1 (v) (Cetane number, Min) Cl-3.1.4 , 3.2, Table-1 (xvii) (Oxidation stability, g/m3, Max) 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 (xix) (Polycyclic Aromatic Hydrocarbon (PAH), percent by mass, Max) 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 content, percent v/v, Max) Cl-5.2 (Marking) Cl-3.1.4 , 3.2, Table-1 (xvii) (Oxidation stability, minutes, Min)

IS 2796 (2017)

Motor gasoline - Specification (Sixth Revision)

14680 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	for the financial year 2025-26
Cl-4.1.4, 4.2.2 & 4.4, Table-1 (ii), a)("Colour: MG 91")	-	200	for the financial year 2025-26
Cl-4.1.4, 4.2.2 & 4.4, Table-1 (ii), b)("Colour: MG 95")	-	200	for the financial year 2025-26
Cl-4.1.4, 4.2.2 & 4.4, Table-1 (iii)(Density at 15°C, kg/m³)	-	1130	for the financial year 2025-26
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)	-	0	for the financial year 2025-26
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)	-	0	for the financial year 2025-26
Cl-4.1.4, 4.2.2 & 4.4, Table-1 (iv) (b)(percent evaporated at 100°C (E 100 °C), percent v/v)	-	0	for the financial year 2025-26
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)	-	0	for the financial year 2025-26
Cl-4.1.4, 4.2.2 & 4.4, Table-1 (iv) (d)(Final boiling point, °C, Max)	-	2650	for the financial year 2025-26
Cl-4.1.4, 4.2.2 & 4.4, Table-1 (iv) (e)(Residue, percent by volume, Max)	-	0	for the financial year 2025-26
Cl-4.1.4, 4.2.2 & 4.4, Table-1 (vii)(Gum content (Solvent washed), g/m3, Max)	-	2070	for the financial year 2025-26
Cl-4.1.4, 4.2.2 & 4.4, Table-1 (viii)(Total sulphur, mg/kg, Max)	-	4710	for the financial year 2025-26
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))	-	1900	for the financial year 2025-26
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)	-	1900	for the financial year 2025-26
Cl-4.1.4, 4.2.2 & 4.4, Table-1 (xiii)(Copper strip corrosion, for 3 h at 50°C, Max)	-	1130	for the financial year 2025-26
Cl-4.1.4, 4.2.2 & 4.4, Table-1 (xx)(Ethanol content, percent by volume: a) Motor gasoline)	-	690	for the financial year 2025-26
Cl-4.1.4, 4.2.2 & 4.4, Table-1 (xx)(Ethanol content, percent by volume: a):- E10)	-	690	for the financial year 2025-26

14 Nov, 2028

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Excluding: Cl-4.1.2 (Antioxidants) Cl-4.1.3 (Metal Deactivators) Cl-4.1.5 (Motor gasoline multifunctional additives (MFA),) Cl-4.2.1 (Organic Oxygenates- Permitted Components) 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 (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 (v) (a) (Research octane number (RON), Min: MG 91) 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 (ix) (Lead content (as Pb ), g/l, 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 (General- Requirements) Cl-4.3 (Other Requirements) Cl-5.2 (Markeing) 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-4.1.4, 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 (xiv) (b) (Water tolerance of motor gasoline-alcohol blends, temperature for phase separation:- Other months, °C, Max)

Bureau of Indian Standards

The National Standards Body of India

Indian Oil Corporation Ltd(IOCL), Visakha Smart Laboratory

IOCL Visakha Terminal, Malkapuram,, Visakhapatnam, Visakhapatanam, Andhra Pradesh, 530011

8332975583 bsrikanth@indianoil.in

Scope List