| 1 |
IS 16861 (2018) |
High flash high speed diesel fuel - Specification |
- |
31590 View breakup
-
| Clause No. |
Exclusion |
Testing Charges (Excl. Of Taxes) |
Effective Date |
Remark |
| 3.3-Table 1-i)(Appearance) |
- |
200 |
|
Testing charges as per year 2025-26 |
| 3.3-Table 1-ii)(Acid Number, mg KOH/g, Max) |
- |
2270 |
|
Testing charges as per year 2025-26 |
| 3.3-Table 1-iii)(Ash, percent by mass, Max) |
- |
2070 |
|
Testing charges as per year 2025-26 |
| 3.3-Table 1-iv)(Carbon residue on the 10 percent Volume Distillation Residue, mass %, Max) |
- |
1530 |
|
Testing charges as per year 2025-26 |
| 3.3-Table 1-v)(Cetane index1), Min) |
- |
3770 |
|
Testing charges as per year 2025-26 |
| 3.3-Table 1-vi)(Pour Point2), Max
a) Winter
b) Summer) |
- |
1900 |
|
Testing charges as per year 2025-26 |
| 3.3-Table 1-vii)(Copper strip Corrosion for 3 h at 100°C) |
- |
1130 |
|
Testing charges as per year 2025-26 |
| 3.3-Table 1-viii)(Distillation, percent (v/v), recovered
a) at 350°C, Min
b) at 370°C Min) |
- |
2650 |
|
Testing charges as per year 2025-26 |
| 3.3-Table 1-ix)(Flash Point Pensky Martens closed cup °C, Min) |
- |
1900 |
|
Testing charges as per year 2025-26 |
| 3.3-Table 1-x)(Kinematic viscosity, cSt, at 40°C) |
- |
2270 |
|
Testing charges as per year 2025-26 |
| 3.3-Table 1-xi)(Density3) at 15°C, kg/m3 , Max) |
- |
1130 |
|
Testing charges as per year 2025-26 |
| 3.3-Table 1-xii)(Total sulphur4), % by mass, Max) |
- |
4710 |
|
Testing charges as per year 2025-26 |
| 3.3-Table 1-xiii)(Water content, ppm, max.) |
- |
4160 |
|
Testing charges as per year 2025-26 |
| 3.3-Table 1-xiv)(Cold filter plugging point (CFPP), °C) |
- |
1900 |
|
Testing charges as per year 2025-26 |
|
16 Dec, 2028 |
- Excluding: 3.1 (General) 3.2 (Composition) 3.3-Table 1-xv) (Oxidation Stability5), g/m3 , Max) 3.3-Table 1-xvi) (Lubricity6), Corrected WSD at 60°C, microns max) 5.1 (Packing) 5.2 (Marking) |
| 2 |
IS 15464 (2022) |
ANHYDROUS ETHANOL FOR USE AS BLENDING COMPONENT IN MOTOR GASOLINE SPECIFICATION First Revision |
- |
64770 View breakup
-
| Clause No. |
Exclusion |
Testing Charges (Excl. Of Taxes) |
Effective Date |
Remark |
| 4.3(Acidity) |
- |
400 |
|
Testing charges as per year 2025-26 |
| 4.4-Table 1-i)(Appearance) |
- |
200 |
|
Testing charges as per year 2025-26 |
| 4.4-Table 1-ii)(Relative density at 15.6/15.6 °C, Max) |
- |
1130 |
|
Testing charges as per year 2025-26 |
| 4.4-Table 1-iii)(Ethanol, percent, v/v, Min1)). (excluding denaturant)) |
- |
1340 |
|
Testing charges as per year 2025-26 |
| 4.4-Table 1-iv)(Ethanol, percent, v/v, Min1). (excluding denaturant)) |
- |
1340 |
|
Testing charges as per year 2025-26 |
| 4.4-Table 1-v)(Higher saturated alcohols (C3-C5), percent, v/v, Max) |
- |
8090 |
|
Testing charges as per year 2025-26 |
| 4.4-Table 1-vi)(Boiling point, °C, Min.) |
- |
2650 |
|
Testing charges as per year 2025-26 |
| 4.4-Table 1-vii)(Residue on evaporation, percent by mass, Max.) |
- |
1900 |
|
Testing charges as per year 2025-26 |
| 4.4-Table 1-viii)(Acidity (as CH3 COOH), mg/kg, Max.) |
- |
400 |
|
Testing charges as per year 2025-26 |
| 4.4-Table 1-ix)(Alkalinity, mg/kg, Max.) |
- |
400 |
|
Testing charges as per year 2025-26 |
| 4.4-Table 1-x)(Aldehyde (as CH3 CHO) content, mg/l, Max) |
- |
1900 |
|
Testing charges as per year 2025-26 |
| 4.4-Table 1-xi)(Electrical conductivity, µS/m, Max) |
- |
780 |
|
Testing charges as per year 2025-26 |
| 4.4-Table 1-xii)(Copper, mg/kg, Max.) |
- |
2270 |
|
Testing charges as per year 2025-26 |
| 4.4-Table 1-xiv)(Inorganic chloride, mg/kg, Max.) |
- |
8270 |
|
Testing charges as per year 2025-26 |
| 4.4-Table 1-xv)(Sulfur content, mg/kg, Max.) |
- |
4710 |
|
Testing charges as per year 2025-26 |
| 4.4-Table 1-xvi)(Sulphate content, mg/kg Max.) |
- |
8270 |
|
Testing charges as per year 2025-26 |
| 4.4-Table 1-xvii)(Water content, percent v/v, Max.) |
- |
4160 |
|
Testing charges as per year 2025-26 |
| 4.4-Table 1-xviii)(Hydrocarbons, percent v/v) |
- |
8090 |
|
Testing charges as per year 2025-26 |
| 4.4-Table 1-xix)(Miscibility with water) |
- |
380 |
|
Testing charges as per year 2025-26 |
| 4.4-Table 1 iv(Methanol) |
- |
8090 |
|
Testing charges as per year 2025-26 |
|
16 Dec, 2028 |
- Excluding: 4.1 (Description) 4.2 (Denaturant) 5.1 (Packing) 5.2 (Marking) 4.4-Table 1-xiii) (pHe) 4.4-Table 1-xii) (Copper, mg/kg, Max.) |
| 3 |
IS 15607 (2022) |
Biodiesel B-100 - Fatty Acid Methyl Esters FAME Specification Second Revision |
- |
23840 View breakup
-
| Clause No. |
Exclusion |
Testing Charges (Excl. Of Taxes) |
Effective Date |
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) |
- |
2070 |
|
- |
| 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) |
- |
2270 |
|
- |
| 4.4-Table 1-xxvi)(Cold filter plugging point (CFPP), °C Max
a) summer 18 – Part 110
b) winter3)) |
- |
1900 |
|
- |
|
16 Dec, 2028 |
- Excluding: 4.1 (General) 4.2 (Additives) 4.3 (The materials shall be free from grit) 4.4-Table 1-x) (Total contamination, mg/kg, Max) 4.4-Table 1-xii) (Cetane No., Min) 4.4-Table 1-xiv) (Methanol, percent by mass, Max) 4.4-Table 1-xv) (Ester content, percent by mass, Min) 4.4-Table 1-xvi) (Monoglycerides content, percent by mass, Max) 4.4-Table 1-xvii) (Diglyceride content, percent by mass, Max) 4.4-Table 1-xviii) (Triglyceride content, percent by mass, Max) 4.4-Table 1-xx) (Total Glycerol percent by mass, Max) 4.4-Table 1-xix) (Free Glycerol percent by mass, Max) 4.4-Table 1-xxi) (Phosphorous mg/kg, Max) 4.4-Table 1-xxii) (Sodium + Potassium mg/kg, Max) 4.4-Table 1-xxiii) (Calcium + Magnesium mg/kg, Max) 4.4-Table 1-xxiv) (Iodine value, gm iodine/100 gm, Max) 4.4-Table 1-xxiv) (Iodine value, gm iodine/100 gm, Max) 4.4-Table 1-xxv) (Oxidation stability, at 110 °C, Min hrs. Accelerated) 4.4-Table 1-xxvii) (Linolenic acid methyl ester, percent m/m, Max) 4.4-Table 1-xxviii) (Polyunsaturated (>_ 4 double bonds) methyl ester percent m/m, Max) 5.1 (Packing) 5.2 (Marking) |
| 4 |
IS 17821 (2022) |
ETHANOL AS A FUEL FOR USE IN POSITIVE IGNITION ENGINE POWERED VEHICLES SPECIFICATION |
- |
88910 View breakup
-
| Clause No. |
Exclusion |
Testing Charges (Excl. Of Taxes) |
Effective Date |
Remark |
| 4.3(Acidity) |
- |
400 |
|
- |
| 4.4-Table 1-i)(Appearance) |
- |
200 |
|
- |
| 4.4-Table 1-ii)(Relative density at 15.6/15.6 °C) |
- |
1130 |
|
- |
| 4.4-Table 1-iii)(Ethanol, percent1) v/v) |
- |
8090 |
|
- |
| 4.4-Table 1-iv)(Methanol, percent v/v, Max.) |
- |
8090 |
|
- |
| 4.4-Table 1-v)(Higher saturated alcohols2) (C3-C5), percent v/v, Max.) |
- |
8090 |
|
- |
| 4.4-Table 1-vi)(Distillation, °C, Min.
a) Initial boiling point
b) 95 percent volume recovery
c) Final boiling point
d) Residue, percent by volume, Max) |
- |
2650 |
|
- |
| 4.4-Table 1-vii)(Residue on evaporation, percent by mass, Max.) |
- |
1900 |
|
- |
| 4.4-Table 1-ix)(Alkalinity, mg/l, Max.) |
- |
400 |
|
- |
| 4.4-Table 1-viii)(Acidity (as CH3 COOH), mg/l, Max) |
- |
400 |
|
- |
| 4.4-Table 1-x)(Aldehyde (as CH3 CHO) content, mg/l, Max.) |
- |
1900 |
|
- |
| 4.4-Table 1-xi)(Electrical conductivity, µS/m, Max.) |
- |
780 |
|
- |
| 4.4-Table 1-xv)(Sulphur content, mg/kg, Max.) |
- |
4710 |
|
- |
| 4.4-Table 1-xvii)(Water content3), percent, v/v Max.) |
- |
4160 |
|
- |
| 4.4-Table 1-xviii)(Gasoline4), percent v/v) |
- |
27200 |
|
- |
| 4.4-Table 1-xvi)(Sulphate content, mg/kg Max.) |
- |
8270 |
|
- |
| 4.4-Table 1-xiv)(Inorganic chloride, mg/kg, Max.) |
- |
8270 |
|
- |
| 4.4-Table 1-xii)(Copper, mg/kg, Max.) |
- |
2270 |
|
- |
|
16 Dec, 2028 |
- Excluding: 4.4-Table 1-xviii) (Gasoline), percent v/v) 4.4-Table 1-xii) (Copper, mg/kg, Max.) 4.1 (Description) 4.2 (Denaturant) 4.4-Table 1-xiii) (pHe)) 5.1 (Packing) 5.2 (Marking) 7.1 (Tests shall be conducted) |
| 5 |
IS 1593 (2018) |
Fuel oils - Specification (Third Revision) |
- |
18060 View breakup
-
| Clause No. |
Exclusion |
Testing Charges (Excl. Of Taxes) |
Effective Date |
Remark |
| 4.2(Pour Point) |
- |
1900 |
|
Testing Charges as per year 2025-26 |
| 4.6-Table 1-i)(Acidity, inorganic) |
- |
960 |
|
Testing Charges as per year 2025-26 |
| 4.6-Table 1-ii)(Ash, percent by mass, Max) |
- |
2070 |
|
Testing Charges as per year 2025-26 |
| 4.6-Table 1-iii)(Carbon residue, mass percent, Max) |
- |
1530 |
|
Testing Charges as per year 2025-26 |
| 4.6-Table 1-iv)(Gross, calorific value) |
- |
780 |
|
Testing Charges as per year 2025-26 |
| 4.6-Table 1-v)(Density at 15°C kg/m3or Relative density at 15.6/15.6°C) |
- |
1130 |
|
Testing Charges as per year 2025-26 |
| 4.6-Table 1-vi)(Flash point (Pensky Martens (closed), °C, Min) |
- |
1900 |
|
Testing Charges as per year 2025-26 |
| 4.6-Table 1-vii)(Kinematic viscosity in centistokes at 50°C) |
- |
2270 |
|
Testing Charges as per year 2025-26 |
| 4.6-Table 1-viii)(Sediment, percent by mass, Max) |
- |
1740 |
|
Testing Charges as per year 2025-26 |
| 4.6-Table 1-ix)(Sulphur, total, percent by mass, Max2)) |
- |
2650 |
|
Testing Charges as per year 2025-26 |
| 4.6-Table 1-x)(Water content, percent by volume, Max) |
- |
1130 |
|
Testing Charges as per year 2025-26 |
|
16 Dec, 2028 |
- Excluding: 4.1 (General) 4.3 (Asphaltene Content) 4.4 (TOTAL SEDIMENT) 5.1 (Packing) 5.2 (Marking) 4.5 (Spot Test) |
| 6 |
IS 1604 (2022) |
Aviation gasoline - Specification (fifth revision) |
- |
27790 View breakup
-
| Clause No. |
Exclusion |
Testing Charges (Excl. Of Taxes) |
Effective Date |
Remark |
| 4.1.2-Table 1-i(Appearance) |
- |
200 |
|
Testing Charges as per year 2025-26 |
| 4.1.2-Table 1-iv(Copper strip corrosion for 2 h at 100°C) |
- |
1130 |
|
Testing Charges as per year 2025-26 |
| 4.1.2-Table 1-v(Density at 15°C, kg/m3) |
- |
1130 |
|
Testing Charges as per year 2025-26 |
| 4.1.2-Table 1-viii(Existent gum, mg/100 ml, Max) |
- |
2070 |
|
Testing Charges as per year 2025-26 |
| 4.1.2-Table 1-ix(Freezing point, °C, Max) |
- |
2270 |
|
Testing Charges as per year 2025-26 |
| 4.1.2-Table 1-xi(Oxidation stability, 16 h:
a) Potential gum, mg/100 ml, Max
b) Precipitate, mg/100 ml, Max) |
- |
4280 |
|
Testing Charges as per year 2025-26 |
| 4.1.2-Table 1-xii(Reid vapour pressure at 38°C, kPa) |
- |
1900 |
|
Testing Charges as per year 2025-26 |
| 4.1.2-Table 1-xiii(Specific energy MJ/kg, Min) |
- |
2480 |
|
Testing Charges as per year 2025-26 |
| 4.1.2-Table 1-xiv(Total sulphur percent m/m, Max) |
- |
4710 |
|
Testing Charges as per year 2025-26 |
| 4.1.2-Table 1-xv(Tetraethyl lead, g Pb/l at 15°C, Max) |
- |
2650 |
|
Testing Charges as per year 2025-26 |
| 4.1.2-Table 1-xvi(Water reaction: Volume change, ml, Max) |
- |
780 |
|
Testing Charges as per year 2025-26 |
| 4.1.2-Table 1-vii(Electrical conductivity, pS/m) |
- |
1340 |
|
Testing Charges as per year 2025-26 |
| 4.1.2-Table 1-ii(Colour, visual) |
- |
200 |
|
Testing Charges as per year 2025-26 |
| 4.1.2-Table 1-vi(Distillation) |
- |
2650 |
|
Testing Charges as per year 2025-26 |
|
16 Dec, 2028 |
- Excluding: 4.1 (General) 4.2 (Composition) 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) 4.2.4 (Dyes) 4.2.3 (Static Dissipater Additive (SDA)) 4.3 (Materials) 4.4 (Requirements) 6.1 (Packing) 6.2 (Marking) 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) 4.2.5 (Colour by lovibond) |
| 7 |
IS 1571 (2018) |
Aviation turbine fuels, kerosine type, jet - A - 1 - Specification (Tenth Revision) |
- |
32994 View breakup
-
| Clause No. |
Exclusion |
Testing Charges (Excl. Of Taxes) |
Effective Date |
Remark |
| Cl-3.2.2, 3.2.6, Table-1 (a)(Visual appearance) |
- |
200 |
|
Testing Charges as per year 2025-26 |
| Cl-3.2.2, 3.2.6, Table-1, (ii) (a)(Total acidi,t y mg KOHM/ga, x) |
- |
1530 |
|
Testing Charges as per 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 |
|
Testing Charges as per year 2025-26 |
| Cl-3.2.2, 3.2.6, Table-1, (ii) (c)(Total sulphur percent by mass, Max) |
- |
2650 |
|
Testing Charges as per year 2025-26 |
| Cl-3.2.2, 3.2.6, Table-1, (ii) (d)(Sulphur mercaptan, percent m/m. Max) |
- |
1900 |
|
Testing Charges as per year 2025-26 |
| Cl-3.2.2, 3.2.6, Table-1, (iii) (a), 1)(Distillation:- Initial boiling point, °) |
- |
2650 |
|
Testing Charges as per year 2025-26 |
| Cl-3.2.2, 3.2.6, Table-1, (iii) (a), 2)(Distillation:- 10 percent recovery °Cv/,v , Max) |
- |
2650 |
|
Testing Charges as per year 2025-26 |
| Cl-3.2.2, 3.2.6, Table-1, (iii) (a), 3)(Distillation:- 50 percent recovery °C, v/v) |
- |
2650 |
|
Testing Charges as per year 2025-26 |
| Cl-3.2.2, 3.2.6, Table-1, (iii) (a), 3)(Distillation:- 50 percent recovery °C, v/v) |
- |
2650 |
|
Testing Charges as per year 2025-26 |
| Cl-3.2.2, 3.2.6, Table-1, (iii) (a), 4)(Distillation:- 90 percent recovery °C, v/v) |
- |
2650 |
|
Testing Charges as per year 2025-26 |
| Cl-3.2.2, 3.2.6, Table- 1, (iii) (a), 5)(Distillation:- Final boiling point,°C, Max) |
- |
2650 |
|
Testing Charges as per year 2025-26 |
| Cl-3.2.2, 3.2.6, Table-1, (iii) (a), 6)(Distillation:- Residue, percent v/v, Max) |
- |
2650 |
|
Testing Charges as per year 2025-26 |
| Cl-3.2.2, 3.2.6, Table-1, (iii) (a), 7)(Distillation:- Loss, percent v/v, Max) |
- |
2650 |
|
Testing Charges as per year 2025-26 |
| Cl-3.2.2, 3.2.6, Table-1, (iii) (b)(Flash point ( Abel ), °C, Min) |
- |
1900 |
|
Testing Charges as per year 2025-26 |
| Cl-3.2.2, 3.2.6, Table-1, (iii) (c)(Density at 15°C,kg/m3) |
- |
1130 |
|
Testing Charges as per year 2025-26 |
| Cl-3.2.2, 3.2.6, Table- 1, (iv) (a)(Fluidity:- Freezing point, °C, Max) |
- |
2270 |
|
Testing Charges as per 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 |
|
Testing Charges as per year 2025-26 |
| Cl-3.2.2, 3.2.6, Table-1, (v) (a)(Specific energy10) MJ/kg, Min) |
- |
2480 |
|
Testing Charges as per year 2025-26 |
| Cl-3.2.2, 3.2.6, Table-1, (v) (b)(Smoke point, mm, Min or) |
- |
1130 |
|
Testing Charges as per year 2025-26 |
| Cl-3.2.2, 3.2.6, Table-1, (v) (b) 2)(Naphthalenes, percent v/v, Max) |
- |
2650 |
|
Testing Charges as per year 2025-26 |
| Cl-3.2.2, 3.2.6, Table-1, (vi) (a)(Copper strip corrosion for 2 h at 100°C) |
- |
1130 |
|
Testing Charges as per 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 |
|
Testing Charges as per year 2025-26 |
| Cl-3.2.2, 3.2.6, Table-1, (viii)(Contaminants: Existent gum, mg/100 ml, Max) |
- |
2070 |
|
Testing Charges as per year 2025-26 |
| Cl-3.2.2, 3.2.6, Table-1, (ix) a)(Water reaction: Interface rating16), Max) |
- |
780 |
|
Testing Charges as per year 2025-26 |
| Cl-3.2.2, 3.2.6, Table-1, (x)(Conductivity: Electrical conductivity, pS/m19)) |
- |
1340 |
|
Testing Charges as per year 2025-26 |
| Cl-3.2.2, 3.2.6, Table-1, (ii) (b)(Aromatics, percent by vol (Defense requirements)) |
- |
2650 |
|
Testing Charges as per year 2025-26 |
| Cl-3.2.2, 3.2.6, Table-1, (ii) (c)(Total sulphur percent by mass, Max (Defense requirements)) |
- |
2650 |
|
Testing Charges as per year 2025-26 |
| Cl-3.2.2, 3.2.6, Table-1, (ii) (d)(Sulphur mercaptan, percent m/m. (Defense requirements)) |
- |
1900 |
|
Testing Charges as per year 2025-26 |
| Cl-3.2.2, 3.2.6, Table-1, (vi) (b)(Silver stripcorrosion12) classification, for 4 h at 50°C, (Defense requirements)) |
- |
1340 |
|
Testing Charges as per year 2025-26 |
|
16 Dec, 2028 |
- 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-5.2 (Marking) Cl-3.2.4 (Lubricity Improver Additive (LIA)) 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) 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-5.2 (Marking) 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), 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, percent/ 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) (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 (B) (Colour) Cl-3.2.2, 3.2.6, Table-1, (ii) (e) (Doctor Test) 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, (xi) (Lubricity: Wear scar diameter, mm (defense requirements)) Cl-3.2.7 (Leak Detection Additive) Cl-3.2.2, 3.2.6, Table- 1, (xi) (Lubricity: Wear scar diameter, mm, Max) |
| 8 |
IS 2796 (2017) |
Motor gasoline - Specification (Sixth Revision) |
- |
42930 View breakup
-
| Clause No. |
Exclusion |
Testing Charges (Excl. Of Taxes) |
Effective Date |
Remark |
| Cl-4.1.4, 4.2.2 & 4.4, Table-1 (i)(Appearance) |
- |
200 |
|
TESTING CHARGES AS PER YEAR 2025-26 |
| Cl-4.1.4, 4.2.2 & 4.4, Table-1 (ii), a)("Colour:
MG 91") |
- |
200 |
|
TESTING CHARGES AS PER YEAR 2025-26 |
| Cl-4.1.4, 4.2.2 & 4.4, Table-1 (ii), b)("Colour:
MG 95") |
- |
200 |
|
TESTING CHARGES AS PER YEAR 2025-26 |
| Cl-4.1.4, 4.2.2 & 4.4, Table-1 (iii)(Density at 15°C, kg/m³) |
- |
1130 |
|
TESTING CHARGES AS PER 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) |
- |
2650 |
|
TESTING CHARGES AS PER 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 |
|
TESTING CHARGES AS PER 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 |
|
TESTING CHARGES AS PER 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 |
|
TESTING CHARGES AS PER YEAR 2025-26 |
| Cl-4.1.4, 4.2.2 & 4.4, Table-1 (iv) (d)(Final boiling point, °C, Max) |
- |
0 |
|
TESTING CHARGES AS PER YEAR 2025-26 |
| Cl-4.1.4, 4.2.2 & 4.4, Table-1 (iv) (e)(Residue, percent by volume, Max) |
- |
0 |
|
TESTING CHARGES AS PER YEAR 2025-26 |
| Cl-4.1.4, 4.2.2 & 4.4, Table-1 (v) (a)(Research octane number (RON), Min: MG 91) |
- |
18230 |
|
TESTING CHARGES AS PER YEAR 2025-26 |
| Cl-4.1.4, 4.2.2 & 4.4, Table-1 (v) (b)(Research octane number (RON), Min: MG 95) |
- |
18230 |
|
TESTING CHARGES AS PER YEAR 2025-26 |
| Cl-4.1.4, 4.2.2 & 4.4, Table-1 (vii)(Gum content (Solvent washed), g/m3, Max) |
- |
2070 |
|
TESTING CHARGES AS PER YEAR 2025-26 |
| Cl-4.1.4, 4.2.2 & 4.4, Table-1 (viii)(Total sulphur, mg/kg, Max) |
- |
4710 |
|
TESTING CHARGES AS PER 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 |
|
TESTING CHARGES AS PER 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 |
|
TESTING CHARGES AS PER YEAR 2025-26 |
| Cl-4.1.4, 4.2.2 & 4.4, Table-1 (xvi) (a)(Olefin content, percent by volume, Max: MG 91) |
- |
2650 |
|
TESTING CHARGES AS PER YEAR 2025-26 |
| Cl-4.1.4, 4.2.2 & 4.4, Table-1 (xvi) (b)(Olefin content, percent by volume, Max :MG 95) |
- |
2650 |
|
TESTING CHARGES AS PER YEAR 2025-26 |
| Cl-4.1.4, 4.2.2 & 4.4, Table-1 (xviii)(Aromatics content, percent by volume, Max) |
- |
2650 |
|
TESTING CHARGES AS PER YEAR 2025-26 |
| Cl-4.1.4, 4.2.2 & 4.4, Table-1 (xx)(Ethanol content, percent by volume: a) Motor gasoline) |
- |
690 |
|
TESTING CHARGES AS PER YEAR 2025-26 |
| Cl-4.1.4, 4.2.2 & 4.4, Table-1 (xx)(Ethanol content, percent by volume: a):- E10) |
- |
690 |
|
TESTING CHARGES AS PER YEAR 2025-26 |
| 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) |
- |
5470 |
|
TESTING CHARGES AS PER YEAR 2025-26 |
| Cl-4.1.4, 4.2.2 & 4.4, Table-1 (XXI)(Oxygenates percent by volume, Max) |
- |
5470 |
|
TESTING CHARGES AS PER 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 |
|
TESTING CHARGES AS PER YEAR 2025-26 |
|
16 Dec, 2028 |
- Exclusion: Cl-4.1 (General- Requirements) 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-4.2.1 (Organic Oxygenates- Permitted Components) Cl-4.3 (Other Requirements) 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 (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 (xv) (Engine intake system cleanliness) 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 (xvii) (Oxidation stability, minutes, Min) Cl-5.2 (Markeing) Cl-4.1.4, 4.2.2 & 4.4, Table-1 (ixi) (Oxygen content, percent by mass, Max) |
| 9 |
IS 17021 (2018) |
E 20 fuel - Admixture of anhydrous ethanol and gasoline - As fuel for spark ignited engine powered vehicles - Specification |
- |
39330 View breakup
-
| Clause No. |
Exclusion |
Testing Charges (Excl. Of Taxes) |
Effective Date |
Remark |
| 4.2-Table 1-i)(Appearance) |
- |
200 |
|
Charges as per year 2025-26 |
| 4.2-Table 1-iii)(Density at 15°C, kg/m3) |
- |
1130 |
|
Charges as per year 2025-26 |
| 4.2-Table 1-iv)(Distillation
a) percent evaporated at 70 °C
(E70 °C), percent v/v
b) percent evaporated at 100 °C
(E100 °C), percent v/v
c) percent evaporated at 150 °C
(E150 °C ), percent v/v, Min
d) Final Boiling Point, °C, Max
e) Residue, percent by volume, Max) |
- |
2650 |
|
Charges as per year 2025-26 |
| 4.2-Table 1-v)(Research Octane Number (RON), Min) |
- |
18210.0 |
|
Charges as per year 2025-26 |
| 4.2-Table 1-viii)(Total Sulphur, mg/kg, Max) |
- |
4710 |
|
Charges as per year 2025-26 |
| 4.2-Table 1-xiii)(Copper strip corrosion (3 h at 50 °C), Max) |
- |
2270 |
|
Charges as per year 2025-26 |
| 4.2-Table 1-xx)(Ethanol content6), percent, v/v) |
- |
8090 |
|
Charges as per year 2025-26 |
| 4.3(Ethanol Content) |
- |
8090 |
|
Charges as per year 2025-26 |
| 4.2-Table 1-vii)(Gum content (Solvent washed), g/m3 , Max) |
- |
2070 |
|
- |
| 4.2-Table 1-xxiii (Amendment No.3)(Water content) |
- |
2400 |
|
- |
|
16 Dec, 2028 |
- Excluding: 4.2-Table 1-xviii) (Aromatic content), percent by volume, Max) 4.1 (Description) 4.2-Table 1-vi) (Motor Octane Number (MON), Min) 4.2-Table 1-ix) (Lead Content (as Pb), g/l, Max) 4.2-Table 1-xi) (Vapour Lock Index (VLI), Max a) Summer2) b) Other Months) 4.2-Table 1-xv) (Engine intake system cleanliness) 4.2-Table 1-xiv) (Water tolerance of gasoline-alcohol blends, temperature for phase separation, °C, Max a) other months b) Winter3)) 4.2-Table 1-xii) (Benzene content, percent by volume, Max) 4.2-Table 1-xvi) (Olefin content, percent by volume, Max) 4.2-Table 1-xvii) (Oxidation stability, minutes, Min) 4.2-Table 1-xix) (Oxygen content, percent by mass, Max) 4.2-Table 1-xxi) (Oxygenates percent by volume, Max a) Ethers containing 5 or more “C” atoms per molecules such as MTBE, ETBE or TAME b) Any other oxygenates) 4.2-Table 1-xxii) (Motor Gasoline Content, percent, v/v) 4.2-Table 1-ii) (Colour) 4.2-Table 1-x) (Reid Vapour pressure at 38°C, kPa, Max) 4.4 (Organic Oxygenates) 4.5 (Phosphorous) 6.1 (Packing) 6.2 (Marking) |
| 10 |
IS 1460 (2025) |
Automotive Diesel Fuel - Specification (seventh revision) |
- |
37060 View breakup
-
| Clause No. |
Exclusion |
Testing Charges (Excl. Of Taxes) |
Effective Date |
Remark |
| Cl-3.1.4 , 3.2, Table-1 (ii) C(Total Acid Number (TAN), mg of KOH/g, Max) |
- |
2270 |
|
Charges for the year 2025-26 |
| Cl-3.1.4 , 3.2, Table-1 (xiv)(Total sulphur, mg/kg, Max) |
- |
4710 |
|
Charges for the year 2025-26 |
| Cl-3.1.4 , 3.2, Table-1 (xv)(Water content, mg/kg, Max) |
- |
4160 |
|
Charges for the year 2025-26 |
| Cl-3.1.4 , 3.2, Table-1 (xiii)(Density at 15 °C, kg/m3) |
- |
1130 |
|
Charges for the year 2025-26 |
| Cl-3.1.4 , 3.2, Table-1 (iii)(Ash, percent by mass, Max) |
- |
2070 |
|
Charges for the year 2025-26 |
| Cl-3.1.4 , 3.2, Table-1 (iv)(Carbon residue, on 10 percent residue1, percent by mass, Max) |
- |
1530 |
|
Charges for the year 2025-26 |
| Cl-3.1.4 , 3.2, Table-1 (xi)(Kinematic viscosity, mm2/s, at 40 °C) |
- |
2270 |
|
Charges for the year 2025-26 |
| Cl-3.1.4 , 3.2, Table-1 (xvi) (a)(Cold Filter Plugging Point (CFPP)3, °C, Max: Winter) |
- |
1900 |
|
Charges for the year 2025-26 |
| Cl-3.1.4 , 3.2, Table-1 (vi)(Cetane index, Min) |
- |
3770 |
|
Charges for the year 2025-26 |
| Cl-3.1.4 , 3.2, Table-1 (x)(Flash point, Abel4, °C, Min) |
- |
1900 |
|
Charges for the year 2025-26 |
| Cl-3.1.4 , 3.2, Table-1 (ix)(Distillation, 95 percent v/v recovery, °C, Max) |
- |
2650 |
|
Charges for the year 2025-26 |
| Cl-3.1.4 , 3.2, Table-1 (viii)(Copper strip corrosion for 3 h at 50 °C, Max) |
- |
1130 |
|
Charges for the year 2025-26 |
| Cl-3.1.4 , 3.2, Table-1 (xxi)(FAME content7, percent v/v, Max) |
- |
5470 |
|
Charges for the year 2025-26 |
| Cl-3.1.4 , 3.2, Table-1 (vii) (b)(Pour point3, °C, Max: Summer) |
- |
1900 |
|
Charges for the year 2025-26 |
| Cl-3.1.4 , 3.2, Table-1 (xvi) (b)(Cold Filter Plugging Point (CFPP)3, °C, Max: Summer) |
- |
1900 |
|
Charges for the year 2025-26 |
| Cl-3.1.4 , 3.2, Table-1 (i)(Appearance) |
- |
200 |
|
Charges for the year 2025-26 |
| Cl-3.1.4 , 3.2, Table-1 (vii) (a)(Pour point3, °C, Max: Winter) |
- |
1900 |
|
Charges for the year 2025-26 |
|
16 Dec, 2028 |
- Excluding: Cl-3.1.4 , 3.2, Table-1 (xii) (Total contamination, mg/kg, Max) Cl-3.1.4 , 3.2, Table-1 (v) (Cetane number, 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-5.2 (Marking) Cl-3.1 (General- Requirements) Cl-3.2 (Composition) 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) Cl-3.1.4 , 3.2, Table-1 (xvii) (Oxidation stability, minutes, Min) Cl-3.1.4 , 3.2, Cl-3.1.4 , 3.2, Table-1 (xvii) (Oxidation stability, g/m3, Max) |