| 1 |
IS 1571 (2018) |
Aviation turbine fuels, kerosine type, jet - A - 1 - Specification (Tenth Revision) |
- |
33200 View breakup
-
| Clause No. |
Exclusion |
Testing Charges (Excl. Of Taxes) |
Effective Date |
Remark |
| Cl-3.2.2, 3.2.6, Table-1, (ii) (c)(Total sulphur percent by mass, Max) |
- |
2650 |
|
NA |
| Cl-3.2.2, 3.2.6, Table-1, (iii) (a), 1)(Distillation:- Initial boiling point, °) |
- |
2650 |
|
NA |
| Cl-3.2.2, 3.2.6, Table-1, (iii) (a), 2)(Distillation:- 10 percent recovery °Cv/,v , Max) |
- |
2650 |
|
NA |
| Cl-3.2.2, 3.2.6, Table-1, (iii) (a), 3)(Distillation:- 50 percent recovery °C, v/v) |
- |
2650 |
|
NA |
| Cl-3.2.2, 3.2.6, Table-1, (iii) (a), 4)(Distillation:- 90 percent recovery °C, v/v) |
- |
2650 |
|
NA |
| Cl-3.2.2, 3.2.6, Table- 1, (iii) (a), 5)(Distillation:- Final boiling point,°C, Max) |
- |
2650 |
|
NA |
| Cl-3.2.2, 3.2.6, Table-1, (iii) (a), 6)(Distillation:- Residue, percent v/v, Max) |
- |
2650 |
|
NA |
| Cl-3.2.2, 3.2.6, Table-1, (iii) (a), 7)(Distillation:- Loss, percent v/v, Max) |
- |
2650 |
|
NA |
| Cl-3.2.2, 3.2.6, Table-1, (iii) (b)(Flash point ( Abel ), °C, Min) |
- |
1900 |
|
NA |
| Cl-3.2.2, 3.2.6, Table-1, (iii) (c)(Density at 15°C,kg/m3) |
- |
1130 |
|
NA |
| Cl-3.2.2, 3.2.6, Table-1, (iv) (b)(Fluidity:- Kinematic viscosity at minus 20°C, mm2/s, Max) |
- |
2270 |
|
NA |
| Cl-3.2.2, 3.2.6, Table- 1, (iv) (a)(Fluidity:- Freezing point, °C, Max) |
- |
2270 |
|
NA |
| Cl-3.2.2, 3.2.6, Table-1, (ii) (a)(Total acidi,t y mg KOHM/ga, x) |
- |
1806 |
|
NA |
| Cl-3.2.2, 3.2.6, Table-1, (v) (b) 2)(Naphthalenes, percent v/v, Max) |
- |
3127 |
|
NA |
| 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") |
- |
1582 |
|
NA |
| Cl-3.2.2, 3.2.6, Table-1, (ii) (b)(Aromatics, percent by vol (Defense requirements)) |
- |
3127 |
|
NA |
| Cl-3.2.2, 3.2.6, Table-1, (viii)(Contaminants: Existent gum, mg/100 ml, Max) |
- |
2443 |
|
NA |
| Cl-3.2.2, 3.2.6, Table-1 (a)(Visual appearance) |
- |
236 |
|
NA |
| Cl-3.2.2, 3.2.6, Table-1 (B)(Colour) |
- |
1334 |
|
NA |
| Cl-3.2.2, 3.2.6, Table-1, (x)(Conductivity: Electrical conductivity, pS/m19)) |
- |
920 |
|
NA |
|
17 Feb, 2029 |
- - |
| 2 |
IS 1460 (2025) |
Automotive Diesel Fuel - Specification (seventh revision) |
- |
15880 View breakup
-
| Clause No. |
Exclusion |
Testing Charges (Excl. Of Taxes) |
Effective Date |
Remark |
| Cl-3.1.4 , 3.2, Table-1 (ix)(Distillation, 95 percent v/v recovery, °C, Max) |
- |
0 |
|
TESTING CHARGE INCLUDED IN Cl-3.1.4 , 3.2, Table-1 (vi) (Cetane index, Min) |
| 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 (xiii)(Density at 15 °C, kg/m3) |
- |
0 |
|
TESTING CHARGE INCLUDED IN Cl-3.1.4 , 3.2, Table-1 (vi) (Cetane index, Min) |
| Cl-3.1.4 , 3.2, Table-1 (xiv)(Total sulphur, mg/kg, Max) |
- |
4710 |
|
- |
| Cl-3.1.4 , 3.2, Table-1 (i)(Appearance) |
- |
200 |
|
- |
| 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) |
- |
0 |
|
TESTING CHARGE INCLUDED IN Cl-3.1.4 , 3.2, Table-1 (vii) (a) (Pour point3, °C, Max: Winter) |
| Cl-3.1.4 , 3.2, Table-1 (viii)(Copper strip corrosion for 3 h at 50 °C, Max) |
- |
1130 |
|
- |
|
17 Feb, 2029 |
- - |
| 3 |
IS 2796 (2017) |
Motor gasoline - Specification (Sixth Revision) |
- |
12090 View breakup
-
| Clause No. |
Exclusion |
Testing Charges (Excl. Of Taxes) |
Effective Date |
Remark |
| 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: Motor gasoline) |
- |
2650 |
|
- |
| 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 Charge included in Cl-4.1.4, 4.2.2 & 4.4, Table-1 (iv) (a) (percent evaporated at 70°C ( |
| 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 Charge included in Cl-4.1.4, 4.2.2 & 4.4, Table-1 (iv) (a) (percent evaporated at 70°C ( |
| 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 Charge included in Cl-4.1.4, 4.2.2 & 4.4, Table-1 (iv) (a) (percent evaporated at 70°C ( |
| Cl-4.1.4, 4.2.2 & 4.4, Table-1 (iv) (d)(Final boiling point, °C, Max) |
- |
0 |
|
Testing Charge included in Cl-4.1.4, 4.2.2 & 4.4, Table-1 (iv) (a) (percent evaporated at 70°C ( |
| Cl-4.1.4, 4.2.2 & 4.4, Table-1 (iv) (e)(Residue, percent by volume, Max) |
- |
0 |
|
Testing Charge included in Cl-4.1.4, 4.2.2 & 4.4, Table-1 (iv) (a) (percent evaporated at 70°C ( |
| 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 (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 (vii)(Gum content (Solvent washed), g/m3, Max) |
- |
2070 |
|
- |
| Cl-4.1.4, 4.2.2 & 4.4, Table-1 (xiii)(Copper strip corrosion, for 3 h at 50°C, Max) |
- |
1130 |
|
- |
|
17 Feb, 2029 |
- - |