| 2881 |
Indian Oil Corporation Ltd. (IOCL), Salem Smart Laboratory, Salem
| 6193914
| IS 2796 (2017) |
Motor gasoline - Specification (Sixth Revision) |
- |
15430 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 |
|
- |
| 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 (ii), b)("Colour:
MG 95") |
- |
200 |
|
- |
| 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) |
- |
530 |
|
TOTAL CHARGE FOR DISTILLATION TEST IS INR 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) |
- |
530 |
|
TOTAL CHARGE FOR DISTILLATION TEST IS INR 2650. |
| 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 |
|
TOTAL CHARGE FOR DISTILLATION TEST IS INR 2650. |
| 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 |
|
TOTAL CHARGE FOR DISTILLATION TEST IS INR 2650. |
| Cl-4.1.4, 4.2.2 & 4.4, Table-1 (iv) (d)(Final boiling point, °C, Max) |
- |
530 |
|
TOTAL CHARGE FOR DISTILLATION TEST IS INR 2650. |
| Cl-4.1.4, 4.2.2 & 4.4, Table-1 (iv) (e)(Residue, percent by volume, Max) |
- |
530 |
|
TOTAL CHARGE FOR DISTILLATION TEST IS INR 2650. |
| 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 (xvi) (a)(Olefin content, percent by volume, Max: MG 91) |
- |
2650 |
|
FIA AROMATICS AND OLEFINS TEST CHARGE IS INR2650. |
| 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 (xvi) (b)(Olefin content, percent by volume, Max :MG 95) |
- |
2650 |
|
FIA AROMATICS AND OLEFINS TEST CHARGE IS INR2650. |
| Cl-4.1.4, 4.2.2 & 4.4, Table-1 (xviii)(Aromatics content, percent by volume, Max) |
- |
2650 |
|
FIA AROMATICS AND OLEFINS TEST CHARGE IS INR2650. |
| 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 (xx)(Ethanol content, percent by volume: a):- E10) |
- |
690 |
|
- |
| Cl-4.1.4, 4.2.2 & 4.4, Table-1 (xx)(Ethanol content, percent by volume: a) Motor gasoline) |
- |
690 |
|
- |
|
16 Dec, 2028 |
- Excluding: 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-4.3 (Other Requirements) 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 (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 (xv) (Engine intake system cleanliness) 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-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 (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 (XXI) (Oxygenates percent by volume, Max) Cl-5.2 (Marketing) |
| 2882 |
INDIAN TEST HOUSE PRIVATE LIMITED, MURADNAGAR
| 8183336
| IS 1328 (2025) |
Veneered Decorative Plywood - Specification ( Fourth Revision ) |
BWP, BWR, MR, TYPE 1, TYPE 2, TYPE 3 |
7500 View breakup
-
| Clause No. |
Exclusion |
Testing Charges (Excl. Of Taxes) |
Effective Date |
Remark |
| Cl 4.1(Grades) |
- |
100 |
|
- |
| Cl 4.2(Type) |
- |
100 |
|
- |
| Cl 4.3(Formaldehyde Class) |
- |
100 |
|
- |
| Cl 5.2(Adhesive) |
- |
100 |
|
- |
| Cl 7.1(Surface Requirements- For Type 1) |
- |
100 |
|
- |
| Cl 7.2(Surface Requirements- For Type 2) |
- |
100 |
|
- |
| Cl 7.3(Surface Requirements- For Type 3) |
- |
100 |
|
- |
| Cl 7.4(Surface Requirements- For Type 4) |
- |
100 |
|
- |
| Cl 8.1(Dimensions (Length and Width)) |
- |
100 |
|
- |
| Cl 8.2(Dimensions (Thickness)) |
- |
100 |
|
- |
| Cl 8.3(Squareness and Edge Straightness as Per Annex B) |
- |
100 |
|
- |
| Cl 8.4- Table 1(Tolerances) |
- |
100 |
|
- |
| Cl 11.3(Moisture Content) |
- |
500 |
|
- |
| Cl 11.4.1(a)(Water Resistance Test( For MR Grade)) |
- |
1300 |
|
- |
| Cl 11.4.1(b)(Water Resistance Test( For BWR Grade)) |
- |
1300 |
|
- |
| Cl 11.4.1(c)(Water Resistance Test( For BWP Grade)) |
- |
1300 |
|
- |
| Cl 11.5(Formaldehyde Content Test) |
- |
3500 |
|
- |
| Cl 12(Marking) |
- |
0 |
|
- |
|
30 Dec, 2027 |
- Included w.e.f 14.10.2025
Exclusion: Cl 11.6 (Steady - State Formaldehyde Emission Test ( Optional Test)) |
| 2883 |
Indian Oil Corporation (IOCL) Mathura Terminal Laboratory
| 9197314
| IS 1459 (2018) |
Kerosene - Specification (Fourth Revision) |
KEROSENE |
13050.00 View breakup
-
| Clause No. |
Exclusion |
Testing Charges (Excl. Of Taxes) |
Effective Date |
Remark |
| 4.2-Table 1-i)(Appearance) |
- |
200.00 |
|
- |
| 4.2-Table 1-iv)(Colour
a)Saybolt (in cas of undyedKerosene)3), Min
b)Visual (in case of dyed Kerosene)) |
- |
200 |
|
- |
| 4.2-Table 1-v)(Copper strip corrosion for 3 h at 50°C) |
- |
1130.00 |
|
- |
| 4.2-Table 1-vi)(Density at 15°C, kg/m3) |
- |
1130.00 |
|
- |
| 4.2-Table 1-vii)(Distillation
a)Percent recovered below200°C, percent (v/v), Min
b)Final boiling point, °C, Max
) |
- |
2650.00 |
|
- |
| 4.2-Table 1-viii)(Flash point ( Abel), °C, Min) |
- |
1900.00 |
|
- |
| 4.2-Table 1-ix)(Smoke Point4), mm, Min) |
- |
1130.00 |
|
- |
| 4.2-Table 1-x)(Total Sulphur Content, percent, m/m, Max) |
- |
4710.00 |
|
- |
|
12 Mar, 2029 |
- - |
| 2884 |
JBS TESTING SOLUTIONS PVT LTD (27), JALANDHAR
| 9164606
| IS 7814 (2005) |
Phosphor bronze sheet, strip and foil - Specification (Second Revision) |
- |
19950 View breakup
-
| Clause No. |
Exclusion |
Testing Charges (Excl. Of Taxes) |
Effective Date |
Remark |
| Clause 4(Supply of material) |
- |
19950 |
|
For complete testing |
| Clause 5("Freedom from
defects") |
- |
19950 |
|
For complete testing |
| Clause 7(chemical composition) |
- |
19950 |
|
For complete testing |
| Clause 8.1(Tensile test) |
- |
19950 |
|
For complete testing |
| Clause 8.2(Bend Test) |
- |
19950 |
|
For complete testing |
| Clause 9.1("Diameter of Strip
and Foil") |
- |
19950 |
|
For complete testing |
| Clause 9.2(Thickness Tolerances) |
- |
19950 |
|
For complete testing |
| Clause 9.3(Width Tolerance) |
- |
19950 |
|
For complete testing |
| Clause 9.4("Length Tolerance
for Sheet") |
- |
19950 |
|
For complete testing |
| Clause 9.5("Permissible Maximum
Value on Camber for Strip") |
- |
19950 |
|
For complete testing |
| Clause 10("Sampling and criteria
for conformity") |
- |
19950 |
|
For complete testing |
| Clause 13(Marking) |
- |
19950 |
|
For complete testing |
|
- |
- Included w.e.f.26.09.2025 |
| 2885 |
Indian Oil Corporation (IOCL) Mathura Terminal Laboratory
| 9197314
| IS 2796 (2017) |
Motor gasoline - Specification (Sixth Revision) |
Motor Gasoline (MS) & It's Variants ( XP MS, Ethanol blends up to E20) |
12980.00 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 |
|
- |
| 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 (ii), b)("Colour:
MG 95") |
- |
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: 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 |
|
- |
| 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 |
|
- |
| 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 |
|
- |
| Cl-4.1.4, 4.2.2 & 4.4, Table-1 (iv) (d)(Final boiling point, °C, Max) |
- |
0 |
|
- |
| Cl-4.1.4, 4.2.2 & 4.4, Table-1 (iv) (e)(Residue, percent by volume, Max) |
- |
0 |
|
- |
| 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 (xx)(Ethanol content, percent by volume: a) Motor gasoline) |
- |
690 |
|
- |
|
12 Mar, 2029 |
- - |
| 2886 |
Perfect International Testing Lab
| 8187826
| IS 302 : Part 2 : Sec 208 (1994) |
Safety of household and similar electrtcal appliances: Part 2 particular requirements: Sec 208 single walled baking ovens |
-- |
30000 View breakup
-
| Clause No. |
Exclusion |
Testing Charges (Excl. Of Taxes) |
Effective Date |
Remark |
| 3(GENERAL REQUIREMENT) |
- |
0 |
|
N/A |
| 4(GENERAL NOTES ON TESTS) |
- |
0 |
|
N/A |
| 5(RATING) |
- |
250 |
|
N/A |
| 6(CLASSIFICATION) |
- |
250 |
|
N/A |
| 7(MARKING) |
- |
500 |
|
N/A |
| 8(PROTECTION AGAINST ELECTRIC SHOCK) |
- |
1000 |
|
N/A |
| 10(INPUT AND CURRENT) |
- |
2000 |
|
N/A |
| 11(TEMPERATURE RISE) |
- |
2000 |
|
N/A |
| 12(OPERATLON UNDER OVERLOAD CONDITIONS OF APPLIANCES
WITH HEATING ELEMENTS) |
- |
0 |
|
N/A |
| 13(ELECTRICAL INSULATION AND LEAKAGE CURRENT
AT OPERATING TEMPERATURE) |
- |
1000 |
|
N/A |
| 14(RADIO AND TELEVISION INTERFERENCE SUPPRESSION) |
- |
2000 |
|
N/A |
| 15(MOISTURE RESESTANCE) |
- |
2000 |
|
N/A |
| 16(INSULATION RESISTANCE AND ELECTRIC SHOCK STRENGTH
( AFTER HUMIDITY TREATMENT )) |
- |
1000 |
|
N/A |
| 17(OVERLOAD PROTECTION) |
- |
1000 |
|
N/A |
| 19(ABNORMAL OPERATION) |
- |
2000 |
|
N/A |
| 20(STABILITY AND MECHANICAL HAZARDS) |
- |
1000 |
|
N/A |
| 21(MECHANICAL STRENGTH) |
- |
1000 |
|
N/A |
| 22(CONSTRUCTION) |
- |
2000 |
|
N/A |
| 23(INTERNAL WIRING) |
- |
1000 |
|
N/A |
| 24(COMPONENTS) |
- |
1000 |
|
N/A |
| 25(SUPPLY CONNECTION AND EXTERNAL FLEXIBLE CABLES AND CORDS) |
- |
1000 |
|
N/A |
| 26(TERMINALS FOR EXTERNAL CONDUCTORS) |
- |
1000 |
|
N/A |
| 27(PROVISION FOR EARTHING) |
- |
1000 |
|
N/A |
| 28(SCREWS AND CONNECTIONS) |
- |
1000 |
|
N/A |
| 29(CREEPAGE DISTANCES, CLEARANCES AND DISTANCES THROUGH INSULATION) |
- |
1000 |
|
N/A |
| 30(RESISTANCE TO HEAT, FIRE AND TACKING) |
- |
1000 |
|
N/A |
| 31(RESISTANCE TO RUSTING) |
- |
1000 |
|
N/A |
| 32(RADIATION HAZARDS) |
- |
0 |
|
N/A |
| 101.1(Type Tests) |
- |
0 |
|
N/A |
| 101.2(Acceptance Tests) |
- |
0 |
|
N/A |
| 101.3(Routine Tests) |
- |
0 |
|
N/A |
| Cl-19.11.4.1(Electrostatic discharge) |
- |
1000 |
|
N/A |
| Cl-19.11.4.2(Radiated Fields) |
- |
0 |
|
N/A |
| Cl-19.11.4.3(Fast transient bursts) |
- |
0 |
|
N/A |
| Cl-19.11.4.4(Surge Immunity test) |
- |
1000 |
|
N/A |
| Cl-19.11.4.5(Immunity to conducted discharge) |
- |
0 |
|
N/A |
| Cl-19.11.4.6(Voltage dips and interruptions) |
- |
0 |
|
N/A |
| Cl-19.11.4.7(Harmonics) |
- |
0 |
|
N/A |
| 3(GENERAL REQUIREMENT) |
- |
- |
|
- |
| 4(GENERAL NOTES ON TESTS) |
- |
- |
|
- |
| 5(RATING) |
- |
- |
|
- |
| 6(CLASSIFICATION) |
- |
- |
|
- |
| 7(MARKING) |
- |
- |
|
- |
| 8(PROTECTION AGAINST ELECTRIC SHOCK) |
- |
- |
|
- |
| 10(INPUT AND CURRENT) |
- |
- |
|
- |
| 11(TEMPERATURE RISE) |
- |
- |
|
- |
| 12(OPERATLON UNDER OVERLOAD CONDITIONS OF APPLIANCES
WITH HEATING ELEMENTS) |
- |
- |
|
- |
| 13(ELECTRICAL INSULATION AND LEAKAGE CURRENT
AT OPERATING TEMPERATURE) |
- |
- |
|
- |
| 14(RADIO AND TELEVISION INTERFERENCE SUPPRESSION) |
- |
- |
|
- |
| 15(MOISTURE RESESTANCE) |
- |
- |
|
- |
| 16(INSULATION RESISTANCE AND ELECTRIC SHOCK STRENGTH
( AFTER HUMIDITY TREATMENT )) |
- |
- |
|
- |
| 17(OVERLOAD PROTECTION) |
- |
- |
|
- |
| 19(ABNORMAL OPERATION) |
- |
- |
|
- |
| 20(STABILITY AND MECHANICAL HAZARDS) |
- |
- |
|
- |
| 21(MECHANICAL STRENGTH) |
- |
- |
|
- |
| 22(CONSTRUCTION) |
- |
- |
|
- |
| 23(INTERNAL WIRING) |
- |
- |
|
- |
| 24(COMPONENTS) |
- |
- |
|
- |
| 25(SUPPLY CONNECTION AND EXTERNAL FLEXIBLE CABLES AND CORDS) |
- |
- |
|
- |
| 26(TERMINALS FOR EXTERNAL CONDUCTORS) |
- |
- |
|
- |
| 27(PROVISION FOR EARTHING) |
- |
- |
|
- |
| 28(SCREWS AND CONNECTIONS) |
- |
- |
|
- |
| 29(CREEPAGE DISTANCES, CLEARANCES AND DISTANCES THROUGH INSULATION) |
- |
- |
|
- |
| 30(RESISTANCE TO HEAT, FIRE AND TACKING) |
- |
- |
|
- |
| 31(RESISTANCE TO RUSTING) |
- |
- |
|
- |
| 32(RADIATION HAZARDS) |
- |
- |
|
- |
| 101.1(Type Tests) |
- |
- |
|
- |
| 101.2(Acceptance Tests) |
- |
- |
|
- |
| 101.3(Routine Tests) |
- |
- |
|
- |
| Cl-19.11.4.1(Electrostatic discharge) |
- |
- |
|
- |
| Cl-19.11.4.2(Radiated Fields) |
- |
- |
|
- |
| Cl-19.11.4.3(Fast transient bursts) |
- |
- |
|
- |
| Cl-19.11.4.4(Surge Immunity test) |
- |
- |
|
- |
| Cl-19.11.4.5(Immunity to conducted discharge) |
- |
- |
|
- |
| Cl-19.11.4.6(Voltage dips and interruptions) |
- |
- |
|
- |
| Cl-19.11.4.7(Harmonics) |
- |
- |
|
- |
|
02 Sep, 2028 |
- Included w.e.f 19.12.2025
"32 (RADIATION HAZARDS)
Cl-19.11.4.2 (Radiated Fields)
Cl-19.11.4.3 (Fast transient bursts)
Cl-19.11.4.5 (Immunity to conducted discharge)
Cl-19.11.4.6 (Voltage dips and interruptions)
Cl-19.11.4.7 (Harmonics)
24 (COMPONENTS)" |
| 2887 |
MALKAPUR LABORATORY (IOCL)
| 6196614
| IS 2796 (2017) |
Motor gasoline - Specification (Sixth Revision) |
- |
12610 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 |
|
Exclusive Tax |
| 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 |
|
Exclusive Tax |
| Cl-4.1.4, 4.2.2 & 4.4, Table-1 (iv) (b)(percent evaporated at 100°C (E 100 °C), percent v/v) |
- |
2650 |
|
Exclusive Tax |
| 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) |
- |
2650 |
|
Exclusive Tax |
| Cl-4.1.4, 4.2.2 & 4.4, Table-1 (iv) (d)(Final boiling point, °C, Max) |
- |
2650 |
|
Exclusive Tax |
| Cl-4.1.4, 4.2.2 & 4.4, Table-1 (viii)(Total sulphur, mg/kg, Max) |
- |
4710 |
|
Exclusive Tax |
| Cl-4.1.4, 4.2.2 & 4.4, Table-1 (iv) (e)(Residue, percent by volume, Max) |
- |
2650 |
|
Exclusive Tax |
| Cl-4.1.4, 4.2.2 & 4.4, Table-1 (vii)(Gum content (Solvent washed), g/m3, Max) |
- |
1900 |
|
Exclusive Tax |
| Cl-4.1.4, 4.2.2 & 4.4, Table-1 (xiii)(Copper strip corrosion, for 3 h at 50°C, Max) |
- |
1130 |
|
Exclusive Tax |
| Cl-4.1.4, 4.2.2 & 4.4, Table-1 (xx)(Ethanol content, percent by volume: a) Motor gasoline) |
- |
690 |
|
Exclusive Tax |
| Cl-4.1.4, 4.2.2 & 4.4, Table-1 (ii), a)("Colour:
MG 91") |
- |
200 |
|
Exclusive Tax |
| 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) |
- |
2650 |
|
Exclusive Tax |
| Cl-4.1.4, 4.2.2 & 4.4, Table-1 (i)(Appearance) |
- |
200 |
|
Exclusive Tax |
| Cl-4.1.4, 4.2.2 & 4.4, Table-1 (ii), b)("Colour:
MG 95") |
- |
200 |
|
Exclusive Tax |
| Cl-4.1.4, 4.2.2 & 4.4, Table-1 (xx)(Ethanol content, percent by volume: a):- E10) |
- |
690 |
|
Exclusive Tax |
|
09 Feb, 2029 |
- Excluding: Cl-4.1.4, 4.2.2 & 4.4, Table-1 (vi) (a) (Motor octane number (MON),Min: MG 91) Cl-4.1.3 (Metal Deactivators) Cl-4.1.5 (Motor gasoline multifunctional additives (MFA),) 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 (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 (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 (ixi) (Oxygen content, percent by mass, 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 (XXI) (Oxygenates percent by volume, Max) Cl-4.1 (General- Requirements) Cl-4.2.1 (Organic Oxygenates- Permitted Components) Cl-4.3 (Other Requirements) 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 (xi) (c) (Vapour lock index (VLI),Max :- E10) Cl-5.2 (Marketing) Cl-4.1.2 (Antioxidants) |
| 2888 |
Korba Laboratory (IOCL)
| 5191414
| IS 17021 (2018) |
E 20 fuel - Admixture of anhydrous ethanol and gasoline - As fuel for spark ignited engine powered vehicles - Specification |
- |
12763 View breakup
-
| Clause No. |
Exclusion |
Testing Charges (Excl. Of Taxes) |
Effective Date |
Remark |
| 4.2-Table 1-i)(Appearance) |
- |
200 |
|
- |
| 4.2-Table 1-ii)(Colour) |
- |
200 |
|
- |
| 4.2-Table 1-iii)(Density at 15°C, kg/m3) |
- |
1113 |
|
- |
| 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 |
|
- |
| 4.2-Table 1-vii)(Gum content (Solvent washed), g/m3 , Max) |
- |
2070 |
|
- |
| 4.2-Table 1-viii)(Total Sulphur, mg/kg, Max) |
- |
4710 |
|
- |
| 4.2-Table 1-xiii)(Copper strip corrosion (3 h at 50 °C), Max) |
- |
1130 |
|
- |
| 4.2-Table 1-xx)(Ethanol content6), percent, v/v) |
- |
690 |
|
- |
|
26 Nov, 2028 |
- Exclusion: 4.1 (Description) 4.2-Table 1-v) (Research Octane Number (RON), Min) 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-x) (Reid Vapour pressure at 38°C, kPa, Max) 4.2-Table 1-xi) (Vapour Lock Index (VLI), Max a) Summer) b) Other Months) 4.2-Table 1-xii) (Benzene content, percent by volume, Max) 4.2-Table 1-xiv) (Water tolerance of gasoline-alcohol blends, temperature for phase separation, °C, Max a) other months b) Winter)) 4.2-Table 1-xv) (Engine intake system cleanliness) 4.2-Table 1-xvi) (Olefin content, percent by volume, Max) 4.2-Table 1-xvii) (Oxidation stability, minutes, Min) 4.2-Table 1-xviii) (Aromatic content), percent by volume, Max) 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) 4.4 (Organic Oxygenates) 4.5 (Phosphorous) 6.1 (Packing) 6.2 (Marking)
4.3 (Ethanol Content) 4.2-Table 1-xxiii (Amendment No.3) (Water content) |
| 2889 |
Korba Laboratory (IOCL)
| 5191414
| IS 15607 (2022) |
Biodiesel B-100 - Fatty Acid Methyl Esters FAME Specification Second Revision |
- |
13023 View breakup
-
| Clause No. |
Exclusion |
Testing Charges (Excl. Of Taxes) |
Effective Date |
Remark |
| 5.4(CFPP - ASTM D6371 / EN 16329 / IS 1448 P:110 b) Winter) |
- |
0 |
|
- |
| 4.4(CFPP - ASTM D6371 / EN 16329 / IS 1448 P:110 a) Summer) |
- |
0 |
|
- |
| 4.4(Copper corrosion - IS 1448 P:15 / ISO 2160) |
- |
0 |
|
- |
| 4.4(Sulphur - ISO 20846 / ASTM D5453) |
- |
0 |
|
- |
| 4.4(Flash point (PMCC) - IS 1448 P:21 ) |
- |
0 |
|
- |
| 4.4(Kinematic viscosity at 40°C - IS 1448 P:25/ ISO3104) |
- |
0 |
|
- |
| 4.4(Density at 15 oC - IS 1448 P:16/ ISO 3675/ ISO 12185/ ASTM D4052) |
- |
0 |
|
- |
| 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) |
- |
1113 |
|
- |
| 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-xi)(Copper strip corrosion, 3 h at 50 °C, Max) |
- |
1130 |
|
- |
| 4.4-Table 1-xxvi)(Cold filter plugging point (CFPP), °C Max
a) summer 18 – Part 110
b) winter3)) |
- |
1900 |
|
- |
|
26 Nov, 2028 |
- Exclusion: 4.1 (General) 4.2 (Additives) 4.3 (The materials shall be free from grit) 4.4-Table 1-vii) (Carbon residue (MCR) 2) percent by mass, Max) 4.4-Table 1-viii) (Sulfated ash, percent by mass, Max) 4.4-Table 1-ix) (Water content mg/kg, Max) 4.4-Table 1-x) (Total contamination, mg/kg, Max) 4.4-Table 1-xii) (Cetane No., Min) 4.4-Table 1-xiii) (Acid value, mg KOH/g, Max) 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-xix) (Free Glycerol percent by mass, Max) 4.4-Table 1-xx) (Total 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-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) |
| 2890 |
Korba Laboratory (IOCL)
| 5191414
| IS 15464 (2022) |
ANHYDROUS ETHANOL FOR USE AS BLENDING COMPONENT IN MOTOR GASOLINE SPECIFICATION First Revision |
- |
12513 View breakup
-
| Clause No. |
Exclusion |
Testing Charges (Excl. Of Taxes) |
Effective Date |
Remark |
| 4.4-Table 1-i)(Appearance) |
- |
200 |
|
- |
| 4.4-Table 1-ii)(Relative density at 15.6/15.6 °C, Max) |
- |
1113 |
|
- |
| 4.4-Table 1-iii)(Ethanol, percent, v/v, Min1)). (excluding denaturant)) |
- |
1340 |
|
- |
| 4.4-Table 1-iv)(Ethanol, percent, v/v, Min1). (excluding denaturant)) |
- |
0 |
|
- |
| 4.4-Table 1-vii)(Residue on evaporation, percent by mass, Max.) |
- |
2070 |
|
- |
| 4.4-Table 1-viii)(Acidity (as CH3 COOH), mg/kg, Max.) |
- |
400 |
|
- |
| 4.4-Table 1-ix)(Alkalinity, mg/kg, Max.) |
- |
400 |
|
- |
| 4.4-Table 1-x)(Aldehyde (as CH3 CHO) content, mg/l, Max) |
- |
1900 |
|
- |
| 4.4-Table 1-xv)(Sulfur content, mg/kg, Max.) |
- |
4710 |
|
- |
| 4.4-Table 1-xix)(Miscibility with water) |
- |
380 |
|
- |
|
26 Nov, 2028 |
- Exclusion: 4.1 (Description) 4.2 (Denaturant) 4.3 (Acidity) 4.4-Table 1-v) (Higher saturated alcohols (C3-C5), percent, v/v, Max) 4.4-Table 1-vi) (Boiling point, °C, Min.) 4.4-Table 1-xi) (Electrical conductivity, µS/m, Max) 4.4-Table 1-xii) (Copper, mg/kg, Max.) 4.4-Table 1-xiii) (pHe) 4.4-Table 1-xiv) (Inorganic chloride, mg/kg, Max.) 4.4-Table 1-xvi) (Sulphate content, mg/kg Max.) 4.4-Table 1-xvii) (Water content, percent v/v, Max.) 4.4-Table 1-xviii) (Hydrocarbons, percent v/v) 5.1 (Packing) 5.2 (Marking) 4.4-Table 1-iv) (Ethanol, percent, v/v, Min1). (excluding denaturant)) 4.4-Table 1 iv (Methanol) |
| 2891 |
Korba Laboratory (IOCL)
| 5191414
| IS 1459 (2018) |
Kerosene - Specification (Fourth Revision) |
- |
10973 View breakup
-
| Clause No. |
Exclusion |
Testing Charges (Excl. Of Taxes) |
Effective Date |
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)) |
- |
200 |
|
- |
| 4.2-Table 1-v)(Copper strip corrosion for 3 h at 50°C) |
- |
1130 |
|
- |
| 4.2-Table 1-vi)(Density at 15°C, kg/m3) |
- |
1113 |
|
- |
| 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) |
- |
2650 |
|
- |
|
26 Nov, 2028 |
- Scope restricted to dyed kerosene. Exclusion: 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). |
| 2892 |
Korba Laboratory (IOCL)
| 5191414
| IS 15770 (2021) |
Heating Oil(LDO) - Specification |
- |
10963 View breakup
-
| Clause No. |
Exclusion |
Testing Charges (Excl. Of Taxes) |
Effective Date |
Remark |
| 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 |
|
- |
| 3.2-Table 1-vi)(Flash point, Pensky Martens ,°C, Min) |
- |
1900 |
|
- |
| 3.2-Table 1-vii)(Kinematic viscosity at 40 °C, mm2 /sec) |
- |
2270 |
|
- |
| 3.2-Table 1-ix)(Density at 15 °C, Kg/m3) |
- |
1113 |
|
- |
| 3.2-Table 1-x)(Water content, percent by volume, Max) |
- |
1130 |
|
- |
| 3.2-Table 1-xi)(Total sulphur, percent by mass) |
- |
2650 |
|
- |
|
26 Nov, 2028 |
- Exclusion: 3.1 (General) 3.2-Table 1-i) (Acid number, mg KOH/gm, Max) 3.2-Table 1-ii) (Ash, percent by mass, Max) 3.2-Table 1-iii) (Carbon residue, on whole samples, percent by mass, Max) 3.2-Table 1-v) (Copper strip corrosion for 3 h at 100 °C) 3.2-Table 1-viii) (Sediment, percent by mass, Max) 5.1 (Packing) 5.2 (Marking) |
| 2893 |
Korba Laboratory (IOCL)
| 5191414
| IS 1593 (2018) |
Fuel oils - Specification (Third Revision) |
- |
10803 View breakup
-
| Clause No. |
Exclusion |
Testing Charges (Excl. Of Taxes) |
Effective Date |
Remark |
| 4.6-Table 1-viii)(Sediment, percent by mass, Max) |
- |
1740 |
|
- |
| 4.6-Table 1-v)(Density at 15°C kg/m3or Relative density at 15.6/15.6°C) |
- |
1113 |
|
- |
| 4.6-Table 1-vi)(Flash point (Pensky Martens (closed), °C, Min) |
- |
1900 |
|
- |
| 4.6-Table 1-vii)(Kinematic viscosity in centistokes at 50°C) |
- |
2270 |
|
- |
| 4.6-Table 1-ix)(Sulphur, total, percent by mass, Max2)) |
- |
2650 |
|
- |
| 4.6-Table 1-x)(Water content, percent by volume, Max) |
- |
1130 |
|
- |
|
26 Nov, 2028 |
- Exclusion: Cl 4.1 (General) 4.3 (Asphaltene Content) 4.4 (TOTAL SEDIMENT) 4.5 (Spot Test) 4.6-Table 1-i) (Acidity, inorganic) 4.6-Table 1-ii) (Ash, percent by mass, Max) 4.6-Table 1-iii) (Carbon residue, mass percent, Max) 4.6-Table 1-iv) (Gross, calorific value) 5.1 (Packing) 5.2 (Marking) 4.2 (Pour Point) |
| 2894 |
Alpha Test House Services LLP (160), Sahibzada Ajit Singh Nagar
| 9138706
| IS 4351 (2024) |
Steel Frames for Doors - Specification (Third Revision) |
STEEL FRAMES FOR DOORS |
24900 View breakup
-
| Clause No. |
Exclusion |
Testing Charges (Excl. Of Taxes) |
Effective Date |
Remark |
| Cl-5, Table-1 (i)(Mild steel sheet (cold rolled)) |
- |
24900 |
|
- |
| Cl-5, Table-1 (ii)(Galvanized sheets — Plain grade) |
- |
24900 |
|
- |
| Cl-5, Table-1 (iii)(Stainless steel Grade) |
- |
24900 |
|
- |
| Cl-5, Table-1 (iv)(Pre-painted galvanized steel sheets) |
- |
24900 |
|
- |
| Cl-6.1(Wall Opening Size) |
- |
24900 |
|
- |
| Cl-6.2(Dimensions) |
- |
24900 |
|
- |
| Cl-6.3(Sizes) |
- |
24900 |
|
- |
| Cl-6.4(Tolerance) |
- |
24900 |
|
- |
| Cl-6.5(Shapes/Style of Door Frames) |
- |
24900 |
|
- |
| Cl-7.1(Pressed Steel Frame Profile) |
- |
24900 |
|
- |
| Cl-7.1.2.1(Frame construction) |
- |
24900 |
|
- |
| Cl-7.1.2.2(Hardware reinforcement) |
- |
24900 |
|
- |
| Cl-7.1.2.3(Mortar guards) |
- |
24900 |
|
- |
| Cl-7.1.2.4(Lock strike plate) |
- |
24900 |
|
- |
| Cl-7.1.2.5(Shock absorbers) |
- |
24900 |
|
- |
| Cl-7.1.2.6(Rubber/EPDM seal) |
- |
24900 |
|
- |
| Cl-7.1.2.7(Base ties) |
- |
24900 |
|
- |
| Cl-7.1.3.1(Knockdown frame) |
- |
24900 |
|
- |
| Cl-7.1.3.2(Mitered frame) |
- |
24900 |
|
- |
| Cl-7.1.3.3(Welded frame) |
- |
24900 |
|
- |
| Cl-7.2.1(Tubular Steel Frame Profile) |
- |
24900 |
|
- |
| Cl-7.2.2(Tubular Frame Construction) |
- |
24900 |
|
- |
| Cl-7.2.3(Base Ties) |
- |
24900 |
|
- |
| Cl-7.2.4(Hardware Fixing) |
- |
24900 |
|
- |
| Cl-7.2.5.1(Modular mitered frame) |
- |
24900 |
|
- |
| Cl-7.2.5.2(Mitred frame) |
- |
24900 |
|
- |
| Cl-7.2.5.3(Welded frame) |
- |
24900 |
|
- |
| Cl-8.1(Types of Hinges) |
- |
24900 |
|
- |
| Cl-8.2(Location of Hinges) |
- |
24900 |
|
- |
| Cl-8.3(Fixing of Hinges) |
- |
24900 |
|
- |
| Cl-8.4(Hardware Location) |
- |
24900 |
|
- |
| Cl-9.1.1(Door Frames of Mild Steel (Cold Rolled)) |
- |
24900 |
|
- |
| Cl-9.1.2(Door Frames of Galvanized Plain Steel Sheets) |
- |
24900 |
|
- |
| Cl-9.1.3(Stainless Steel Door Frames) |
- |
24900 |
|
- |
| Cl-9.2(Painting) |
- |
24900 |
|
- |
| Cl-9.3(Powder Coatings) |
- |
24900 |
|
- |
| Cl-9.4(Wood Grain Effect Finish) |
- |
24900 |
|
- |
| Cl-11(Marking) |
- |
24900 |
|
- |
| Cl-7.1.2.8(Aldrop, sliding bolts and tower bolts) |
- |
24900 |
|
- |
|
- |
- Included w.e.f.26.09.2025 |
| 2895 |
ACCURATE TEST SOLUTIONS LLP (F21), NOIDA
| 8141226
| IS 17550 : PART 3 (2021) |
Household Refrigerating Appliance- Characteristics and test methods Part 3 Energy Consumption and volume |
- |
130000 View breakup
-
| Clause No. |
Exclusion |
Testing Charges (Excl. Of Taxes) |
Effective Date |
Remark |
| "Cl. No. 6 "("DETERMINATION OF ENERGY
CONSUMPTION") |
- |
20000 |
|
- |
| "Cl. No.4.8 & Annex H "(Determination Of Volume) |
- |
9500 |
|
- |
| "Cl. No. 6 "("DETERMINATION OF ENERGY
CONSUMPTION") |
- |
20000 |
|
- |
| "Cl. No. 6 "("DETERMINATION OF ENERGY
CONSUMPTION") |
- |
20000 |
|
- |
| "Cl. No.4.8 & Annex H "(Determination Of Volume) |
- |
9500 |
|
- |
| 4.2(Steady State Power Consumption) |
- |
20000 |
|
- |
| 4.3(Defrost and Recovery Energy and temperature change) |
- |
15000 |
|
- |
| 4.4(Defrost Frequency) |
- |
20500 |
|
- |
| 4.5(Number of Test Points and Interpolations) |
- |
10000 |
|
- |
| 4.6(Load Processing Efficiency) |
- |
20000 |
|
- |
| 4.7(Specified Auxiliaries) |
- |
20000 |
|
- |
| 4.8(Volumn Determination) |
- |
9500 |
|
- |
| 6(Determination of Energy Consumption) |
- |
20000 |
|
- |
| Annex B(Determination of Steady state Power & Temperature) |
- |
15000 |
|
- |
| Annex C(Defrost and Recovery Energy and temperature change) |
- |
15000 |
|
- |
| Annex D(Defrost Interval) |
- |
20500 |
|
- |
| Annex E(Interpolation of Results) |
- |
10000 |
|
- |
| Annex F(Energy Consumption of specified auxiliaries) |
- |
20000 |
|
- |
| Annex G(Determination of Load Processing Efficiency) |
- |
20000 |
|
- |
| Annex H(Determination of Volume) |
- |
9500 |
|
- |
|
04 Jul, 2027 |
- Included w.e.f 04.11.2025 |
| 2896 |
Indian Oil Corporation Ltd (IOCL), Jasidih Smart Laboratory
| 5195214
| IS 17021 (2018) |
E 20 fuel - Admixture of anhydrous ethanol and gasoline - As fuel for spark ignited engine powered vehicles - Specification |
- |
12780 View breakup
-
| Clause No. |
Exclusion |
Testing Charges (Excl. Of Taxes) |
Effective Date |
Remark |
| 4.2-Table 1-i)(Appearance) |
- |
200 |
|
Applicable for FY 2025-26
Annual increment: 5%
GST applicable: 18% |
| 4.2-Table 1-ii)(Colour) |
- |
200 |
|
Applicable for FY 2025-26
Annual increment: 5%
GST applicable: 18% |
| 4.2-Table 1-iii)(Density at 15°C, kg/m3) |
- |
1130 |
|
Applicable for FY 2025-26
Annual increment: 5%
GST applicable: 18% |
| 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 |
|
Applicable for FY 2025-26
Annual increment: 5%
GST applicable: 18% |
| 4.2-Table 1-vii)(Gum content (Solvent washed), g/m3 , Max) |
- |
2070 |
|
Applicable for FY 2025-26
Annual increment: 5%
GST applicable: 18% |
| 4.2-Table 1-viii)(Total Sulphur, mg/kg, Max) |
- |
4710 |
|
Applicable for FY 2025-26
Annual increment: 5%
GST applicable: 18% |
| 4.2-Table 1-xiii)(Copper strip corrosion (3 h at 50 °C), Max) |
- |
1130 |
|
Applicable for FY 2025-26
Annual increment: 5%
GST applicable: 18% |
| 4.2-Table 1-xx)(Ethanol content6), percent, v/v) |
- |
690 |
|
Applicable for FY 2025-26
Annual increment: 5%
GST applicable: 18% |
|
29 Dec, 2028 |
- Excluding: 4.1 (Description) 4.2-Table 1-v) (Research Octane Number (RON), Min) 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-x) (Reid Vapour pressure at 38°C, kPa, Max) 4.2-Table 1-xi) (Vapour Lock Index (VLI), Max a) Summer2) b) Other Months) 4.2-Table 1-xii) (Benzene content, percent by volume, Max) 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-xv) (Engine intake system cleanliness) 4.2-Table 1-xvi) (Olefin content, percent by volume, Max) 4.2-Table 1-xvii) (Oxidation stability, minutes, Min) 4.2-Table 1-xviii) (Aromatic content5), percent by volume, Max) 4.2-Table 1-xix) (Oxygen content, percent by mass, Max) 4.2-Table 1-xxii) (Motor Gasoline Content, percent, v/v) 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) 4.3 (Ethanol Content) 4.4 (Organic Oxygenates) 4.5 (Phosphorous) 6.1 (Packing) 6.2 (Marking) 4.2-Table 1-xxiii (Amendment No.3) (Water content) |
| 2897 |
Korba Laboratory (IOCL)
| 5191414
| IS 2796 (2017) |
Motor gasoline - Specification (Sixth Revision) |
- |
12073 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 |
|
- |
| Cl-4.1.4, 4.2.2 & 4.4, Table-1 (iii)(Density at 15°C, kg/m³) |
- |
1113 |
|
- |
| 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) |
- |
530 |
|
- |
| 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 |
|
- |
| 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) (e)(Residue, percent by volume, Max) |
- |
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 (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 (ii), a)("Colour:
MG 91") |
- |
200 |
|
- |
| Cl-4.1.4, 4.2.2 & 4.4, Table-1 (ii), b)("Colour:
MG 95") |
- |
0 |
|
- |
|
26 Nov, 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-4.3 (Other Requirements) 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 (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 (ixi) (Oxygen content, percent by mass, 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 (XXI) (Oxygenates percent by volume, Max) Cl-5.2 (Markeing) Cl-4.1.4, 4.2.2 & 4.4, Table-1 (ixi) (Ethanol content, percent by volume: a) Motor gasoline) Cl-4.1.4, 4.2.2 & 4.4, Table-1 (ixi) (Ethanol content, percent by volume: a):- E10) |
| 2898 |
ACCURATE TEST SOLUTIONS LLP (F21), NOIDA
| 8141226
| IS 17550 : Part 2 (2024) |
Household Refrigerating Appliances - Characteristics and Test Methods Part 2 Performance Requirements (First Revision) |
- |
340000 View breakup
-
| Clause No. |
Exclusion |
Testing Charges (Excl. Of Taxes) |
Effective Date |
Remark |
| 6(Storage Test) |
- |
50000 |
|
- |
| 7(Cooling Capacity Test) |
- |
45000 |
|
- |
| 8(Freezing Capacity Test) |
- |
45000 |
|
- |
| 9("Automatic Ice-Making
Capacity Test") |
- |
45000 |
|
- |
| Cl. No.4.6 & Annex A(PULL-DOWN TEST) |
- |
35000 |
|
- |
| Cl. No.4.6(b) & Annex B("Wine Storage
Appliances And
Compartments;
Storage Test") |
- |
35000 |
|
- |
| Cl. No.4.6(C) & AnnexC("Temperature Rise
Test ") |
- |
45000 |
|
- |
| Cl. No.4.6(d) & Annex D("Water Vapour Condensation
Test ") |
- |
40000 |
|
- |
|
04 Jul, 2027 |
- Included w.e.f 17.12.2025 |
| 2899 |
Indian Oil Corporation (IOCL) Mathura Terminal Laboratory
| 9197314
| IS 1460 (2025) |
Automotive Diesel Fuel - Specification (seventh revision) |
Auto Motive Diesel Fuel |
15880.00 View breakup
-
| Clause No. |
Exclusion |
Testing Charges (Excl. Of Taxes) |
Effective Date |
Remark |
| Cl-3.1.4 , 3.2, Table-1 (i)(Appearance) |
- |
200.00 |
|
- |
| Cl-3.1.4 , 3.2, Table-1 (vi)(Cetane index, Min) |
- |
3770.00 |
|
- |
| Cl-3.1.4 , 3.2, Table-1 (vii) (a)(Pour point3, °C, Max: Winter) |
- |
1900.00 |
|
- |
| Cl-3.1.4 , 3.2, Table-1 (vii) (b)(Pour point3, °C, Max: Summer) |
- |
0 |
|
- |
| Cl-3.1.4 , 3.2, Table-1 (viii)(Copper strip corrosion for 3 h at 50 °C, Max) |
- |
1130.00 |
|
- |
| Cl-3.1.4 , 3.2, Table-1 (ix)(Distillation, 95 percent v/v recovery, °C, Max) |
- |
0 |
|
- |
| Cl-3.1.4 , 3.2, Table-1 (x)(Flash point, Abel4, °C, Min) |
- |
1900.00 |
|
- |
| Cl-3.1.4 , 3.2, Table-1 (xi)(Kinematic viscosity, mm2/s, at 40 °C) |
- |
2270.00 |
|
- |
| Cl-3.1.4 , 3.2, Table-1 (xiv)(Total sulphur, mg/kg, Max) |
- |
4710.00 |
|
- |
| Cl-3.1.4 , 3.2, Table-1 (xiii)(Density at 15 °C, kg/m3) |
- |
0 |
|
- |
|
12 Mar, 2029 |
- - |
| 2900 |
Bengaluru Smart Laboratory, Indian Oil Corporation Limited (IOCL)
| 6193214
| IS 1587 (2017) |
Aviation turbine fuel, high flash point type - Specification (Fourth Revision) |
- |
38840 View breakup
-
| Clause No. |
Exclusion |
Testing Charges (Excl. Of Taxes) |
Effective Date |
Remark |
| 3.2-Table 1-i)(Appearance
a) Visual appearance) |
- |
200 |
|
- |
| 3.2-Table 1-ii)(Composition
a) Total acidity, mg KOH /g, Max) |
- |
8730 |
|
- |
| 3.2-Table 1-iii)(Volatility
a) Distillation
1. Initial boiling point, °C) |
- |
5680 |
|
- |
| 3.2-Table 1-iv)(Fluidity
a) Freezing point, °C) |
- |
4540 |
|
- |
| 3.2-Table 1-v)(Combustion
a) Specific energy, MJ/kg,Min) |
- |
3610 |
|
- |
| 3.2-Table 1-vi)(Corrosion
a) Copper strip corrosion for 2 hrs at 100 °C) |
- |
2470 |
|
- |
| 3.2-Table 1-viii)(Contaminants
a) Existent Gum, mg/100 ml, Max) |
- |
2070 |
|
- |
| 3.2-Table 1-i)(Appearance b) Colour) |
- |
200 |
|
- |
| 3.2-Table 1-ii)(Composition
b) Aromatics, % v/v) |
- |
2650 |
|
- |
| 3.2-Table 1-ii)(Composition c) Total Sulphur, %
m/m) |
- |
2650 |
|
- |
| 3.2-Table 1-ii)(Composition d) Sulphur Mercaptan, % m/m) |
- |
1900 |
|
- |
| 3.2-Table 1-iii)(Volatility a) Distillation 2. 10 percent v/ v Recovery at, °C) |
- |
2650 |
|
- |
| 3.2-Table 1-iii)(Volatility a) Distillation 3. 50 percent v/ v Recovery at, °C) |
- |
2650 |
|
- |
| 3.2-Table 1-iii)(Volatility a) Distillation 4. 90 percent v/ v Recovery at, °C) |
- |
2650 |
|
- |
| 3.2-Table 1-iii)(Volatility a) Distillation 5. Final Boiling Point, °C) |
- |
2650 |
|
- |
| 3.2-Table 1-iii)(Volatility a) Distillation 6. Residue, % v / v) |
- |
2650 |
|
- |
| 3.2-Table 1-iii)(Volatility a) Distillation 7. Loss, % v / v) |
- |
2650 |
|
- |
| 3.2-Table 1-iii)(b. Flash point (PMCC), °C) |
- |
1900 |
|
- |
| 3.2-Table 1-iii)(c. Density at 15°C) |
- |
1130 |
|
- |
| 3.2-Table 1-iv(Fluidity b) Kinematic viscosity at – 20 °C) |
- |
2270 |
|
- |
| 3.2-Table 1-vi)(Combustion b) Smoke point) |
- |
1130 |
|
- |
| 3.2-Table 1-v)(Combustion Naphthalenes, % v / v) |
- |
2650 |
|
- |
| 3.2-Table 1-vi)(Corrosion b) Silver strip corrosion) |
- |
1340 |
|
- |
|
10 Dec, 2028 |
- Excluding: 3.2-Table 1-vii) (Thermal Stability JFTOT at control temperature of 260 °C a) Filter pressure differential, mm Hg, Max) 1 (Lubricity Wear scar diameter, mm,Max) 1 (Packing) 1 (Marking) 3.2-Table 1-i) (Appearance c)Particulate contamination at point of manufacture, mg/l) 3.2-Table 1-i) (Appearance d) Particulate at point of manufacture. Cumulative channel particle counts) 3.2-Table 1-ii) (Composition e) Doctor test) 3.2-Table 1-iii) (f) Refining component at point of manufacture 1. Hydro processed component, % vol) 3.2-Table 1-iii) (f) Refining component at point of manufacture 2. Severely hydro processed component, % vol) 3.2-Table 1-vii) (Thermal Stability JFTOT at control temperature of 260 °C b) Tube rating) 3.2-Table 1-viii) (Contaminants b) Microseparometer rating at the point of manufacture and before addition of LIA) 3.2-Table 1-viii) (Lubricity: Wear scar diameter) |
| 2901 |
Bengaluru Smart Laboratory, Indian Oil Corporation Limited (IOCL)
| 6193214
| IS 1604 (2022) |
Aviation gasoline - Specification (fifth revision) |
- |
18180 View breakup
-
| Clause No. |
Exclusion |
Testing Charges (Excl. Of Taxes) |
Effective Date |
Remark |
| 4.1.2-Table 1-i(Appearance) |
- |
200 |
|
- |
| 4.1.2-Table 1-iv(Copper strip corrosion for 2 h at 100°C) |
- |
1130 |
|
- |
| 4.1.2-Table 1-v(Density at 15°C, kg/m3) |
- |
1130 |
|
- |
| 4.1.2-Table 1-vi(Distillation) |
- |
2650 |
|
- |
| 4.1.2-Table 1-viii(Existent gum, mg/100 ml, Max) |
- |
2070 |
|
- |
| 4.1.2-Table 1-ix(Freezing point, °C, Max) |
- |
2270 |
|
- |
| 4.1.2-Table 1-xii(Reid vapour pressure at 38°C, kPa) |
- |
1900 |
|
- |
| 4.1.2-Table 1-xiv(Total sulphur percent m/m, Max) |
- |
4710 |
|
- |
| 4.1.2-Table 1-xvi(Water reaction: Volume change, ml, Max) |
- |
780 |
|
- |
| 4.1.2-Table 1-vii(Electrical conductivity, pS/m) |
- |
1340 |
|
- |
|
10 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) 4.2.2-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-x) (Specific energy MJ/kg, Min or Product of API gravity and aniline point, Min) 4.2.2-Table 1-xii) (Tetraethyl lead, g Pb/l at 15°C, Max) 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) |
| 2902 |
CTL TESTING LABORATORY PRIVATE LIMITED, JAIPUR
| 8180306
| IS 15450 (2022) |
Polyethylene-aluminium-polyethylene composite pressure pipes for hot and cold water supplies Specifications first revision of IS 15450 |
DN 12 TO DN75 |
48000 View breakup
-
| Clause No. |
Exclusion |
Testing Charges (Excl. Of Taxes) |
Effective Date |
Remark |
| 5(MATERIALS) |
- |
5200 |
|
10% DISCOUNT FOR BIS |
| 6(PRESSURE RATING) |
- |
0 |
|
10% DISCOUNT FOR BIS |
| 7(NOMINAL DIAMETERS) |
- |
500 |
|
10% DISCOUNT FOR BIS |
| 8(COLOUR) |
- |
200 |
|
10% DISCOUNT FOR BIS |
| 9(DIMENSIONS OF PIPE) |
- |
500 |
|
10% DISCOUNT FOR BIS |
| 10(VISUAL APPEARANCE) |
- |
200 |
|
10% DISCOUNT FOR BIS |
| 11.1(Density (Method of test as per Table 3)) |
- |
1000 |
|
10% DISCOUNT FOR BIS |
| 11.2(Melt Flow Rate (Method of test as per Table 3)) |
- |
500 |
|
10% DISCOUNT FOR BIS |
| 11.3(Overall Migration) |
- |
2500 |
|
10% DISCOUNT FOR BIS |
| 11.4(Thermal Stability to Oxidation (Method of test as per Table 3)) |
- |
1500 |
|
10% DISCOUNT FOR BIS |
| 11.5(Carbon Black Content and Dispersion (Method of test as per Table 3)) |
- |
500 |
|
10% DISCOUNT FOR BIS |
| 11.6(Pigment Dispersion (For Coloured Pipes) (Method of test as per Table 3)) |
- |
1000 |
|
10% DISCOUNT FOR BIS |
| 11.7(Resistance to Weathering) |
- |
15000 |
|
10% DISCOUNT FOR BIS |
| 11.8(Adhesion Test) |
- |
2500 |
|
10% DISCOUNT FOR BIS |
| 11.9(Apparent Tensile Strength of Pipe) |
- |
1500 |
|
10% DISCOUNT FOR BIS |
| 11.10(Minimum Burst Pressure) |
- |
2500 |
|
10% DISCOUNT FOR BIS |
| 11.11(Hydraulic Characteristics) |
- |
3500 |
|
10% DISCOUNT FOR BIS |
| Table 3(Anti-oxidant (as per IS 2530)) |
- |
1500 |
|
10% DISCOUNT FOR BIS |
| 14(MARKING) |
- |
0 |
|
10% DISCOUNT FOR BIS |
| 5.1(MATERIALS) |
- |
2500 |
|
10% DISCOUNT FOR BIS |
| 5.2.1(MATERIALS) |
- |
3500 |
|
10% DISCOUNT FOR BIS |
| 5.2.1.1(The other constituents) |
- |
1200 |
|
10% DISCOUNT FOR BIS |
| 5.3.1(UV Stabilizer) |
- |
1500 |
|
10% DISCOUNT FOR BIS |
| 5.3.2(UV Stabilizer) |
- |
1500 |
|
10% DISCOUNT FOR BIS |
| 5.4(Aluminium) |
- |
2000 |
|
10% DISCOUNT FOR BIS |
| 5.5(REWORK Material) |
- |
0 |
|
10% DISCOUNT FOR BIS |
| 6(PRESSURE RATING) |
- |
0 |
|
10% DISCOUNT FOR BIS |
| 7(NOMINAL DIAMETERS) |
- |
200 |
|
10% DISCOUNT FOR BIS |
| 8(COLOUR) |
- |
0 |
|
10% DISCOUNT FOR BIS |
| 9.1(DIMENSIONS OF PIPE) |
- |
200 |
|
10% DISCOUNT FOR BIS |
| 9.2.1(Method of Measurements) |
- |
0 |
|
10% DISCOUNT FOR BIS |
| 9.3(Length of Straight Pipe) |
- |
400 |
|
10% DISCOUNT FOR BIS |
| 9.4(Coiling) |
- |
400 |
|
10% DISCOUNT FOR BIS |
| 10(VISUAL APPEARANCE) |
- |
0 |
|
10% DISCOUNT FOR BIS |
| 11.1(Density) |
- |
1000 |
|
10% DISCOUNT FOR BIS |
| 11.3(Melt Flow Rate) |
- |
1000 |
|
10% DISCOUNT FOR BIS |
| 11.3(Overall Migration) |
- |
2500 |
|
10% DISCOUNT FOR BIS |
| 11.4(Thermal Stability to Oxidation) |
- |
1500 |
|
10% DISCOUNT FOR BIS |
| 11.5(Carbon Black Content and Dispersion) |
- |
1500 |
|
10% DISCOUNT FOR BIS |
| 11.6(Pigment Dispersion (For Coloured Pipes)) |
- |
1500 |
|
10% DISCOUNT FOR BIS |
| 11.7(Resistance to Weathering) |
- |
11000 |
|
10% DISCOUNT FOR BIS |
| 11.8(Adhesion Test) |
- |
2500 |
|
10% DISCOUNT FOR BIS |
| 11.9(Apparent Tensile Strength of Pipe) |
- |
2500 |
|
10% DISCOUNT FOR BIS |
| 11.1(Minimum Burst Pressure) |
- |
3500 |
|
10% DISCOUNT FOR BIS |
| 11.11.1(Short Term Hydrostatic Tests) |
- |
3500 |
|
10% DISCOUNT FOR BIS |
| 11.11.12(Long Term Hydrostatic Test) |
- |
3500 |
|
10% DISCOUNT FOR BIS |
| 12.1(Type Test) |
- |
4500 |
|
10% DISCOUNT FOR BIS |
| 5(MATERIALS) |
- |
0 |
|
10% DISCOUNT FOR BIS |
| 6(PRESSURE RATING) |
- |
0 |
|
10% DISCOUNT FOR BIS |
| 7(NOMINAL DIAMETERS) |
- |
0 |
|
10% DISCOUNT FOR BIS |
| 8(COLOUR) |
- |
0 |
|
10% DISCOUNT FOR BIS |
| 9(DIMENSIONS OF PIPE) |
- |
0 |
|
10% DISCOUNT FOR BIS |
| 10(VISUAL APPEARANCE) |
- |
0 |
|
10% DISCOUNT FOR BIS |
| 11.1(Density (Method of test as per Table 3)) |
- |
500 |
|
10% DISCOUNT FOR BIS |
| 11.2(Melt Flow Rate (Method of test as per Table 3)) |
- |
500 |
|
10% DISCOUNT FOR BIS |
| 11.3(Overall Migration) |
- |
1500 |
|
10% DISCOUNT FOR BIS |
| 11.4(Thermal Stability to Oxidation (Method of test as per Table 3)) |
- |
2500 |
|
10% DISCOUNT FOR BIS |
| 11.5(Carbon Black Content and Dispersion (Method of test as per Table 3)) |
- |
1500 |
|
10% DISCOUNT FOR BIS |
| 11.6(Pigment Dispersion (For Coloured Pipes) (Method of test as per Table 3)) |
- |
2500 |
|
10% DISCOUNT FOR BIS |
| 11.7(Resistance to Weathering) |
- |
15000 |
|
10% DISCOUNT FOR BIS |
| 11.8(Adhesion Test) |
- |
0 |
|
10% DISCOUNT FOR BIS |
| 11.9(Apparent Tensile Strength of Pipe) |
- |
0 |
|
10% DISCOUNT FOR BIS |
| 11.10(Minimum Burst Pressure) |
- |
0 |
|
10% DISCOUNT FOR BIS |
| 11.11(Hydraulic Characteristics) |
- |
0 |
|
10% DISCOUNT FOR BIS |
| Table 3(Anti-oxidant (as per IS 2530)) |
- |
0 |
|
10% DISCOUNT FOR BIS |
| 14(MARKING) |
- |
0 |
|
10% DISCOUNT FOR BIS |
| 5.1(MATERIALS) |
- |
0 |
|
10% DISCOUNT FOR BIS |
| 5.2.1(MATERIALS) |
- |
0 |
|
10% DISCOUNT FOR BIS |
| 5.2.1.1(The other constituents) |
- |
0 |
|
10% DISCOUNT FOR BIS |
| 5.3.1(UV Stabilizer) |
- |
0 |
|
10% DISCOUNT FOR BIS |
| 5.3.2(UV Stabilizer) |
- |
0 |
|
10% DISCOUNT FOR BIS |
| 5.4(Aluminium) |
- |
0 |
|
- |
| 5.5(REWORK Material) |
- |
0 |
|
- |
| 6(PRESSURE RATING) |
- |
0 |
|
- |
| 7(NOMINAL DIAMETERS) |
- |
0 |
|
- |
| 8(COLOUR) |
- |
0 |
|
- |
| 9.1(DIMENSIONS OF PIPE) |
- |
0 |
|
- |
| 9.2.1(Method of Measurements) |
- |
0 |
|
- |
| 9.3(Length of Straight Pipe) |
- |
0 |
|
- |
| 9.4(Coiling) |
- |
0 |
|
- |
| 10(VISUAL APPEARANCE) |
- |
0 |
|
- |
| 11.1(Density) |
- |
0 |
|
- |
| 11.3(Melt Flow Rate) |
- |
0 |
|
- |
| 11.3(Overall Migration) |
- |
0 |
|
- |
| 11.4(Thermal Stability to Oxidation) |
- |
0 |
|
- |
| 11.5(Carbon Black Content and Dispersion) |
- |
0 |
|
- |
| 11.6(Pigment Dispersion (For Coloured Pipes)) |
- |
0 |
|
- |
| 11.7(Resistance to Weathering) |
- |
0 |
|
- |
| 11.8(Adhesion Test) |
- |
0 |
|
- |
| 11.9(Apparent Tensile Strength of Pipe) |
- |
0 |
|
- |
| 11.1(Minimum Burst Pressure) |
- |
0 |
|
- |
| 11.11.1(Short Term Hydrostatic Tests) |
- |
0 |
|
- |
| 11.11.12(Long Term Hydrostatic Test) |
- |
0 |
|
- |
| 12.1(Type Test) |
- |
0 |
|
- |
| 5(MATERIALS) |
- |
- |
|
- |
| 6(PRESSURE RATING) |
- |
- |
|
- |
| 7(NOMINAL DIAMETERS) |
- |
- |
|
- |
| 8(COLOUR) |
- |
- |
|
- |
| 9(DIMENSIONS OF PIPE) |
- |
- |
|
- |
| 10(VISUAL APPEARANCE) |
- |
- |
|
- |
| 11.1(Density (Method of test as per Table 3)) |
- |
- |
|
- |
| 11.2(Melt Flow Rate (Method of test as per Table 3)) |
- |
- |
|
- |
| 11.3(Overall Migration) |
- |
- |
|
- |
| 11.4(Thermal Stability to Oxidation (Method of test as per Table 3)) |
- |
- |
|
- |
| 11.5(Carbon Black Content and Dispersion (Method of test as per Table 3)) |
- |
- |
|
- |
| 11.6(Pigment Dispersion (For Coloured Pipes) (Method of test as per Table 3)) |
- |
- |
|
- |
| 11.7(Resistance to Weathering) |
- |
- |
|
- |
| 11.8(Adhesion Test) |
- |
- |
|
- |
| 11.9(Apparent Tensile Strength of Pipe) |
- |
- |
|
- |
| 11.10(Minimum Burst Pressure) |
- |
- |
|
- |
| 11.11(Hydraulic Characteristics) |
- |
- |
|
- |
| Table 3(Anti-oxidant (as per IS 2530)) |
- |
- |
|
- |
| 14(MARKING) |
- |
- |
|
- |
| 5.1(MATERIALS) |
- |
- |
|
- |
| 5.2.1(MATERIALS) |
- |
- |
|
- |
| 5.2.1.1(The other constituents) |
- |
- |
|
- |
| 5.3.1(UV Stabilizer) |
- |
- |
|
- |
| 5.3.2(UV Stabilizer) |
- |
- |
|
- |
| 5.4(Aluminium) |
- |
- |
|
- |
| 5.5(REWORK Material) |
- |
- |
|
- |
| 6(PRESSURE RATING) |
- |
- |
|
- |
| 7(NOMINAL DIAMETERS) |
- |
- |
|
- |
| 8(COLOUR) |
- |
- |
|
- |
| 9.1(DIMENSIONS OF PIPE) |
- |
- |
|
- |
| 9.2.1(Method of Measurements) |
- |
- |
|
- |
| 9.3(Length of Straight Pipe) |
- |
- |
|
- |
| 9.4(Coiling) |
- |
- |
|
- |
| 10(VISUAL APPEARANCE) |
- |
- |
|
- |
| 11.1(Density) |
- |
- |
|
- |
| 11.3(Melt Flow Rate) |
- |
- |
|
- |
| 11.3(Overall Migration) |
- |
- |
|
- |
| 11.4(Thermal Stability to Oxidation) |
- |
- |
|
- |
| 11.5(Carbon Black Content and Dispersion) |
- |
- |
|
- |
| 11.6(Pigment Dispersion (For Coloured Pipes)) |
- |
- |
|
- |
| 11.7(Resistance to Weathering) |
- |
- |
|
- |
| 11.8(Adhesion Test) |
- |
- |
|
- |
| 11.9(Apparent Tensile Strength of Pipe) |
- |
- |
|
- |
| 11.1(Minimum Burst Pressure) |
- |
- |
|
- |
| 11.11.1(Short Term Hydrostatic Tests) |
- |
- |
|
- |
| 11.11.12(Long Term Hydrostatic Test) |
- |
- |
|
- |
| 12.1(Type Test) |
- |
- |
|
- |
|
24 Sep, 2027 |
- Included w.e.f. 29.10.2025 |
| 2903 |
Bengaluru Smart Laboratory, Indian Oil Corporation Limited (IOCL)
| 6193214
| IS 17021 (2018) |
E 20 fuel - Admixture of anhydrous ethanol and gasoline - As fuel for spark ignited engine powered vehicles - Specification |
- |
35540 View breakup
-
| Clause No. |
Exclusion |
Testing Charges (Excl. Of Taxes) |
Effective Date |
Remark |
| 4.2-Table 1-i)(Appearance) |
- |
200 |
|
- |
| 4.2-Table 1-ii)(Colour) |
- |
200 |
|
- |
| 4.2-Table 1-iii)(Density at 15°C, kg/m3) |
- |
1130 |
|
- |
| 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 |
|
- |
| 4.2-Table 1-v)(Research Octane Number (RON), Min) |
- |
18210 |
|
- |
| 4.2-Table 1-vii)(Gum content (Solvent washed), g/m3 , Max) |
- |
2070 |
|
- |
| 4.2-Table 1-viii)(Total Sulphur, mg/kg, Max) |
- |
4710 |
|
- |
| 4.2-Table 1-x)(Reid Vapour pressure at 38°C, kPa, Max) |
- |
1900 |
|
- |
| 4.2-Table 1-xiii)(Copper strip corrosion (3 h at 50 °C), Max) |
- |
1130 |
|
- |
| 4.2-Table 1-xviii)(Aromatic content5), percent by volume, Max) |
- |
2650 |
|
- |
| 4.2-Table 1-xx)(Ethanol content6), percent, v/v) |
- |
690 |
|
- |
| 4.3(Ethanol Content) |
- |
690 |
|
- |
|
10 Dec, 2028 |
- Excluding: 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) Summer) b) Other Months) 4.2-Table 1-xii) (Benzene content, percent by volume, Max) 4.2-Table 1-xiv) (Water tolerance of gasoline-alcohol blends, temperature for phase separation, °C, Max a) other months b) Winter)) 4.2-Table 1-xv) (Engine intake system cleanliness) 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) 4.4 (Organic Oxygenates) 4.5 (Phosphorous) 6.1 (Packing) 6.2 (Marking) 4.2-Table 1-xxiii (Amendment No.3) (Water content) |
| 2904 |
Bengaluru Smart Laboratory, Indian Oil Corporation Limited (IOCL)
| 6193214
| IS 15464 (2022) |
ANHYDROUS ETHANOL FOR USE AS BLENDING COMPONENT IN MOTOR GASOLINE SPECIFICATION First Revision |
- |
18030 View breakup
-
| Clause No. |
Exclusion |
Testing Charges (Excl. Of Taxes) |
Effective Date |
Remark |
| 4.4-Table 1-x)(Aldehyde (as CH3 CHO) content, mg/l, Max) |
- |
1900 |
|
- |
| 4.4-Table 1-i)(Appearance) |
- |
200 |
|
- |
| 4.4-Table 1-ii)(Relative density at 15.6/15.6 °C, Max) |
- |
1130 |
|
- |
| 4.4-Table 1-iii)(Ethanol, percent, v/v, Min1)). (excluding denaturant)) |
- |
1340 |
|
- |
| 4.4-Table 1-iv)(Ethanol, percent, v/v, Min1). (excluding denaturant)) |
- |
1340 |
|
- |
| 4.4-Table 1-vii)(Residue on evaporation, percent by mass, Max.) |
- |
2070 |
|
- |
| 4.4-Table 1-ix)(Alkalinity, mg/kg, Max.) |
- |
400 |
|
- |
| 4.4-Table 1-xv)(Sulfur content, mg/kg, Max.) |
- |
4710 |
|
- |
| 4.4-Table 1-xvii)(Water content, percent v/v, Max.) |
- |
4160 |
|
- |
| 4.4-Table 1-xix)(Miscibility with water) |
- |
380 |
|
- |
| 4.4-Table 1-viii)(Acidity (as CH3 COOH), mg/kg, Max.) |
- |
400 |
|
- |
|
10 Dec, 2028 |
- Excluding: 4.1 (Description) 4.2 (Denaturant) 4.3 (Acidity) 4.4-Table 1-v) (Higher saturated alcohols (C3-C5), percent, v/v, Max) 4.4-Table 1-vi) (Boiling point, °C, Min.) 4.4-Table 1-xi) (Electrical conductivity, µS/m, Max) 4.4-Table 1-xii) (Copper, mg/kg, Max.) 4.4-Table 1-xiii) (pHe) 4.4-Table 1-xiv) (Inorganic chloride, mg/kg, Max.) 4.4-Table 1-xvi) (Sulphate content, mg/kg Max.) 4.4-Table 1-xviii) (Hydrocarbons, percent v/v) 5.1 (Packing) 5.2 (Marking) 7.1 (Tests shall be conducted) 4.4-Table 1 iv (Methanol) |
| 2905 |
Bengaluru Smart Laboratory, Indian Oil Corporation Limited (IOCL)
| 6193214
| IS 1459 (2018) |
Kerosene - Specification (Fourth Revision) |
- |
10990 View breakup
-
| Clause No. |
Exclusion |
Testing Charges (Excl. Of Taxes) |
Effective Date |
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)) |
- |
200 |
|
- |
| 4.2-Table 1-v)(Copper strip corrosion for 3 h at 50°C) |
- |
1130 |
|
- |
| 4.2-Table 1-vi)(Density at 15°C, kg/m3) |
- |
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) |
- |
2650 |
|
- |
|
10 Dec, 2028 |
- Scope is restricted to dyed kerosene. Excluding: 4.2-Table 1-ii) (Acidity, inorganic) 4.2-Table 1-iii) (Burning quality) a)Char Value, mg/kg of oil consumed, Max b)Bloom on glass Chimney) 5.1 (Packing) 5.2 (Marking) |
| 2906 |
Bengaluru Smart Laboratory, Indian Oil Corporation Limited (IOCL)
| 6193214
| IS 1460 (2025) |
Automotive Diesel Fuel - Specification (seventh revision) |
- |
33860 View breakup
-
| Clause No. |
Exclusion |
Testing Charges (Excl. Of Taxes) |
Effective Date |
Remark |
| Cl-3.1.4 , 3.2, Table-1 (i)(Appearance) |
- |
200 |
|
- |
| Cl-3.1.4 , 3.2, Table-1 (ii) C(Total Acid Number (TAN), mg of KOH/g, Max) |
- |
2270 |
|
- |
| Cl-3.1.4 , 3.2, Table-1 (iii)(Ash, percent by mass, Max) |
- |
2070 |
|
- |
| 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 (viii)(Copper strip corrosion for 3 h at 50 °C, Max) |
- |
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 (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) |
- |
1130 |
|
- |
| Cl-3.1.4 , 3.2, Table-1 (xiv)(Total sulphur, mg/kg, Max) |
- |
4710 |
|
- |
| Cl-3.1.4 , 3.2, Table-1 (xv)(Water content, mg/kg, Max) |
- |
4160 |
|
- |
| 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 |
|
- |
|
10 Dec, 2028 |
- Excluding: Cl-3.1 (General- Requirements) Cl-3.2 (Composition) Cl-3.1.4 , 3.2, Table-1 (iv) (Carbon residue, on 10 percent residue, percent by mass, Max) Cl-3.1.4 , 3.2, Table-1 (xii) (Total contamination, mg/kg, Max) Cl-3.1.4 , 3.2, Table-1 (xvii) (Oxidation stability, 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), hours, 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 (v) (Cetane number, 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) |
| 2907 |
Bengaluru Smart Laboratory, Indian Oil Corporation Limited (IOCL)
| 6193214
| IS 2796 (2017) |
Motor gasoline - Specification (Sixth Revision) |
- |
69790 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 |
|
- |
| 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: Motor gasoline) |
- |
2650 |
|
- |
| Cl-4.1.4, 4.2.2 & 4.4, Table-1 (iv) (b)(percent evaporated at 100°C (E 100 °C), percent v/v) |
- |
2650 |
|
- |
| 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) |
- |
2650 |
|
- |
| Cl-4.1.4, 4.2.2 & 4.4, Table-1 (iv) (d)(Final boiling point, °C, Max) |
- |
2650 |
|
- |
| Cl-4.1.4, 4.2.2 & 4.4, Table-1 (iv) (e)(Residue, percent by volume, Max) |
- |
2650 |
|
- |
| Cl-4.1.4, 4.2.2 & 4.4, Table-1 (v) (a)(Research octane number (RON), Min: MG 91) |
- |
18210 |
|
- |
| 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 (x) (a)(Reid vapour pressure (RVP) at 38°C, kPa , Max: MG(without ethanol)) |
- |
1900 |
|
- |
| 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 (xx)(Ethanol content, percent by volume: a) Motor gasoline) |
- |
690 |
|
- |
| Cl-4.1.4, 4.2.2 & 4.4, Table-1 (ii), b)("Colour:
MG 95") |
- |
200 |
|
- |
| 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) |
- |
2650 |
|
- |
| Cl-4.1.4, 4.2.2 & 4.4, Table-1 (v) (b)(Research octane number (RON), Min: MG 95) |
- |
18210 |
|
- |
| 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 |
|
- |
| Cl-4.1.4, 4.2.2 & 4.4, Table-1 (xx)(Ethanol content, percent by volume: a):- E10) |
- |
690 |
|
- |
| Cl-4.1.4, 4.2.2 & 4.4, Table-1 (xviii)(Aromatics content, percent by volume, Max) |
- |
2650 |
|
- |
|
10 Dec, 2028 |
- Excluding: 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-4.3 (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 (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 (ixi) (Oxygen content, percent by mass, 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 (XXI) (Oxygenates percent by volume, Max) Cl-5.2 (Marketing) |
| 2908 |
Samridhi Test House Pvt. Ltd.
| 8184706
| IS 2619 (2018) |
Glass beakers - Specification (Third Revision) |
All Grade / Type / Size / Designation |
12800 View breakup
-
| Clause No. |
Exclusion |
Testing Charges (Excl. Of Taxes) |
Effective Date |
Remark |
| Cl.8.5 Thermal shock resistance(Beakers shall have a thermal shock resistance of 160 °C when tested in accordance with ISO 718.) |
- |
2800 |
|
- |
| Cl.5 Capacity
(b) Distance between the levels corresponding to the nominal and overflow capacities shall be at least
10 mm.) |
- |
1500 |
|
- |
| Cl.6 Material(Beakers shall be made of borosilicate glass 3.3 in accordance with ISO 3585. The glass shall be
reasonably free from residual strain and from visible glass defects which might impair the safety and
performance of the beaker.) |
- |
0 |
|
- |
| Cl.7.1 Dimensions(Low-form and tall-form beakers shall observe the dimensions specified in Table 1 and thick-walled
beakers the dimensions specifed in Table 2. The tolerances on the external diameter shall be ±5 % of
the value given in the tables.) |
- |
1000 |
|
- |
| Cl.7.2 Radius at base(Beakers having a nominal capacity of 250 ml or greater shall have an external radius at the junction
between the base and the side of 10 % to 20 % of the external diameter.) |
- |
1000 |
|
- |
| Cl.7.2 Radius at base(Beakers having a nominal capacity less than 250 ml shall have a minimum radius at the junction
between the base and the side of 5 % of the external diameter.) |
- |
1000 |
|
- |
| Cl.7.3 Wall thickness(Substantial local irregularities from the minimum values for wall thickness given in the tables shall
be avoided. That means, the minimum wall thickness shall fall at no place below the values given in
Table 1 and Table 2 and the beakers shall comply with the requirement for thermal shock endurance
specified in 8.5.) |
- |
1000 |
|
- |
| Cl.8.1 Base(The design of the base shall enable the beaker to stand vertically on a plane horizontal surface without
spinning or rocking) |
- |
1000 |
|
- |
| 8.2 Upper edge(The side of the beaker shall be slightly flared near the brim in a smooth and regular curve. The diameter
of the brim shall be of the order of 5 % to 15 % greater than the diameter of the body. The edge of the
brim shall be finished in a plane parallel with that of the horizontal base.) |
- |
500 |
|
- |
| Cl. 8.3 Spout(The spout shall be shaped so that, when the beaker is filled with water, the water may be poured in a
regular stream clear of the side of the beaker. When the beaker is placed on a horizontal surface and
filling is continued beyond its overflow capacity, the water shall first overflow from the spout and not
from any other part of the brim.) |
- |
500 |
|
- |
| Cl.8.4 Scale(Beakers may be provided with a scale, which should approximately indicate the volume contained
in the beaker.) |
- |
1000 |
|
- |
| Cl.8.5 Thermal shock resistance(Beakers shall have a thermal shock resistance of 160 °C when tested in accordance with ISO 718.) |
- |
2800 |
|
- |
| Cl.5 Capacity
(a)overflow of capacity of a beaker shall exceed the nominal capacity by at least 5 %;) |
- |
0 |
|
- |
| Cl.5 Capacity
(b) Distance between the levels corresponding to the nominal and overflow capacities shall be at least
10 mm.) |
- |
0 |
|
- |
| Cl.6 Material(Beakers shall be made of borosilicate glass 3.3 in accordance with ISO 3585. The glass shall be
reasonably free from residual strain and from visible glass defects which might impair the safety and
performance of the beaker.) |
- |
0 |
|
- |
| Cl.7.1 Dimensions(Low-form and tall-form beakers shall observe the dimensions specified in Table 1 and thick-walled
beakers the dimensions specifed in Table 2. The tolerances on the external diameter shall be ±5 % of
the value given in the tables.) |
- |
0 |
|
- |
| Cl.7.2 Radius at base(Beakers having a nominal capacity of 250 ml or greater shall have an external radius at the junction
between the base and the side of 10 % to 20 % of the external diameter.) |
- |
0 |
|
- |
| Cl.7.2 Radius at base(Beakers having a nominal capacity less than 250 ml shall have a minimum radius at the junction
between the base and the side of 5 % of the external diameter.) |
- |
0 |
|
- |
| Cl.7.3 Wall thickness(Substantial local irregularities from the minimum values for wall thickness given in the tables shall
be avoided. That means, the minimum wall thickness shall fall at no place below the values given in
Table 1 and Table 2 and the beakers shall comply with the requirement for thermal shock endurance
specified in 8.5.) |
- |
0 |
|
- |
| Cl.8.1 Base(The design of the base shall enable the beaker to stand vertically on a plane horizontal surface without
spinning or rocking) |
- |
0 |
|
- |
| 8.2 Upper edge(The side of the beaker shall be slightly flared near the brim in a smooth and regular curve. The diameter
of the brim shall be of the order of 5 % to 15 % greater than the diameter of the body. The edge of the
brim shall be finished in a plane parallel with that of the horizontal base.) |
- |
0 |
|
- |
| Cl. 8.3 Spout(The spout shall be shaped so that, when the beaker is filled with water, the water may be poured in a
regular stream clear of the side of the beaker. When the beaker is placed on a horizontal surface and
filling is continued beyond its overflow capacity, the water shall first overflow from the spout and not
from any other part of the brim.) |
- |
0 |
|
- |
| Cl.8.4 Scale(Beakers may be provided with a scale, which should approximately indicate the volume contained
in the beaker.) |
- |
0 |
|
- |
| Cl.8.5 Thermal shock resistance(Beakers shall have a thermal shock resistance of 160 °C when tested in accordance with ISO 718.) |
- |
0 |
|
- |
| Cl.5 Capacity
(a)overflow of capacity of a beaker shall exceed the nominal capacity by at least 5 %;) |
- |
0 |
|
- |
| Cl.5 Capacity
(b) Distance between the levels corresponding to the nominal and overflow capacities shall be at least
10 mm.) |
- |
0 |
|
- |
| Cl.6 Material(Beakers shall be made of borosilicate glass 3.3 in accordance with ISO 3585. The glass shall be
reasonably free from residual strain and from visible glass defects which might impair the safety and
performance of the beaker.) |
- |
0 |
|
- |
| Cl.7.1 Dimensions(Low-form and tall-form beakers shall observe the dimensions specified in Table 1 and thick-walled
beakers the dimensions specifed in Table 2. The tolerances on the external diameter shall be ±5 % of
the value given in the tables.) |
- |
0 |
|
- |
| Cl.7.2 Radius at base(Beakers having a nominal capacity of 250 ml or greater shall have an external radius at the junction
between the base and the side of 10 % to 20 % of the external diameter.) |
- |
0 |
|
- |
| Cl.7.2 Radius at base(Beakers having a nominal capacity less than 250 ml shall have a minimum radius at the junction
between the base and the side of 5 % of the external diameter.) |
- |
0 |
|
- |
| Cl.7.3 Wall thickness(Substantial local irregularities from the minimum values for wall thickness given in the tables shall
be avoided. That means, the minimum wall thickness shall fall at no place below the values given in
Table 1 and Table 2 and the beakers shall comply with the requirement for thermal shock endurance
specified in 8.5.) |
- |
0 |
|
- |
| Cl.8.1 Base(The design of the base shall enable the beaker to stand vertically on a plane horizontal surface without
spinning or rocking) |
- |
0 |
|
- |
| 8.2 Upper edge(The side of the beaker shall be slightly flared near the brim in a smooth and regular curve. The diameter
of the brim shall be of the order of 5 % to 15 % greater than the diameter of the body. The edge of the
brim shall be finished in a plane parallel with that of the horizontal base.) |
- |
0 |
|
- |
| Cl. 8.3 Spout(The spout shall be shaped so that, when the beaker is filled with water, the water may be poured in a
regular stream clear of the side of the beaker. When the beaker is placed on a horizontal surface and
filling is continued beyond its overflow capacity, the water shall first overflow from the spout and not
from any other part of the brim.) |
- |
0 |
|
- |
| Cl.8.4 Scale(Beakers may be provided with a scale, which should approximately indicate the volume contained
in the beaker.) |
- |
0 |
|
- |
| Cl.5 Capacity
(a)overflow of capacity of a beaker shall exceed the nominal capacity by at least 5 %;) |
- |
0 |
|
- |
| Cl.8.5 Thermal shock resistance(Beakers shall have a thermal shock resistance of 160 °C when tested in accordance with ISO 718.) |
- |
0 |
|
- |
| Cl.5 Capacity
(b) Distance between the levels corresponding to the nominal and overflow capacities shall be at least
10 mm.) |
- |
0 |
|
- |
| Cl.6 Material(Beakers shall be made of borosilicate glass 3.3 in accordance with ISO 3585. The glass shall be
reasonably free from residual strain and from visible glass defects which might impair the safety and
performance of the beaker.) |
- |
0 |
|
- |
| Cl.7.1 Dimensions(Low-form and tall-form beakers shall observe the dimensions specified in Table 1 and thick-walled
beakers the dimensions specifed in Table 2. The tolerances on the external diameter shall be ±5 % of
the value given in the tables.) |
- |
0 |
|
- |
| Cl.7.2 Radius at base(Beakers having a nominal capacity of 250 ml or greater shall have an external radius at the junction
between the base and the side of 10 % to 20 % of the external diameter.) |
- |
0 |
|
- |
| Cl.7.2 Radius at base(Beakers having a nominal capacity less than 250 ml shall have a minimum radius at the junction
between the base and the side of 5 % of the external diameter.) |
- |
0 |
|
- |
| Cl.7.3 Wall thickness(Substantial local irregularities from the minimum values for wall thickness given in the tables shall
be avoided. That means, the minimum wall thickness shall fall at no place below the values given in
Table 1 and Table 2 and the beakers shall comply with the requirement for thermal shock endurance
specified in 8.5.) |
- |
0 |
|
- |
| Cl.8.1 Base(The design of the base shall enable the beaker to stand vertically on a plane horizontal surface without
spinning or rocking) |
- |
0 |
|
- |
| 8.2 Upper edge(The side of the beaker shall be slightly flared near the brim in a smooth and regular curve. The diameter
of the brim shall be of the order of 5 % to 15 % greater than the diameter of the body. The edge of the
brim shall be finished in a plane parallel with that of the horizontal base.) |
- |
0 |
|
- |
| Cl. 8.3 Spout(The spout shall be shaped so that, when the beaker is filled with water, the water may be poured in a
regular stream clear of the side of the beaker. When the beaker is placed on a horizontal surface and
filling is continued beyond its overflow capacity, the water shall first overflow from the spout and not
from any other part of the brim.) |
- |
0 |
|
- |
| Cl.8.4 Scale(Beakers may be provided with a scale, which should approximately indicate the volume contained
in the beaker.) |
- |
0 |
|
- |
| Cl.8.5 Thermal shock resistance(Beakers shall have a thermal shock resistance of 160 °C when tested in accordance with ISO 718.) |
- |
0 |
|
- |
| Cl.5 Capacity
(a)overflow of capacity of a beaker shall exceed the nominal capacity by at least 5 %;) |
- |
0 |
|
- |
| Cl.5 Capacity
(b) Distance between the levels corresponding to the nominal and overflow capacities shall be at least
10 mm.) |
- |
0 |
|
- |
| Cl.6 Material(Beakers shall be made of borosilicate glass 3.3 in accordance with ISO 3585. The glass shall be
reasonably free from residual strain and from visible glass defects which might impair the safety and
performance of the beaker.) |
- |
0 |
|
- |
| Cl.7.1 Dimensions(Low-form and tall-form beakers shall observe the dimensions specified in Table 1 and thick-walled
beakers the dimensions specifed in Table 2. The tolerances on the external diameter shall be ±5 % of
the value given in the tables.) |
- |
0 |
|
- |
| Cl.7.2 Radius at base(Beakers having a nominal capacity of 250 ml or greater shall have an external radius at the junction
between the base and the side of 10 % to 20 % of the external diameter.) |
- |
0 |
|
- |
| Cl.7.2 Radius at base(Beakers having a nominal capacity less than 250 ml shall have a minimum radius at the junction
between the base and the side of 5 % of the external diameter.) |
- |
0 |
|
- |
| Cl.7.3 Wall thickness(Substantial local irregularities from the minimum values for wall thickness given in the tables shall
be avoided. That means, the minimum wall thickness shall fall at no place below the values given in
Table 1 and Table 2 and the beakers shall comply with the requirement for thermal shock endurance
specified in 8.5.) |
- |
0 |
|
- |
| Cl.8.1 Base(The design of the base shall enable the beaker to stand vertically on a plane horizontal surface without
spinning or rocking) |
- |
0 |
|
- |
| 8.2 Upper edge(The side of the beaker shall be slightly flared near the brim in a smooth and regular curve. The diameter
of the brim shall be of the order of 5 % to 15 % greater than the diameter of the body. The edge of the
brim shall be finished in a plane parallel with that of the horizontal base.) |
- |
0 |
|
- |
| Cl. 8.3 Spout(The spout shall be shaped so that, when the beaker is filled with water, the water may be poured in a
regular stream clear of the side of the beaker. When the beaker is placed on a horizontal surface and
filling is continued beyond its overflow capacity, the water shall first overflow from the spout and not
from any other part of the brim.) |
- |
0 |
|
- |
| Cl.8.4 Scale(Beakers may be provided with a scale, which should approximately indicate the volume contained
in the beaker.) |
- |
0 |
|
- |
| Cl.8.5 Thermal shock resistance(Beakers shall have a thermal shock resistance of 160 °C when tested in accordance with ISO 718.) |
- |
0 |
|
- |
| Cl.5 Capacity
(a)overflow of capacity of a beaker shall exceed the nominal capacity by at least 5 %;) |
- |
0 |
|
- |
| Cl.5 Capacity
(b) Distance between the levels corresponding to the nominal and overflow capacities shall be at least
10 mm.) |
- |
0 |
|
- |
| Cl.6 Material(Beakers shall be made of borosilicate glass 3.3 in accordance with ISO 3585. The glass shall be
reasonably free from residual strain and from visible glass defects which might impair the safety and
performance of the beaker.) |
- |
0 |
|
- |
| Cl.7.1 Dimensions(Low-form and tall-form beakers shall observe the dimensions specified in Table 1 and thick-walled
beakers the dimensions specifed in Table 2. The tolerances on the external diameter shall be ±5 % of
the value given in the tables.) |
- |
0 |
|
- |
| Cl.7.2 Radius at base(Beakers having a nominal capacity of 250 ml or greater shall have an external radius at the junction
between the base and the side of 10 % to 20 % of the external diameter.) |
- |
0 |
|
- |
| Cl.7.2 Radius at base(Beakers having a nominal capacity less than 250 ml shall have a minimum radius at the junction
between the base and the side of 5 % of the external diameter.) |
- |
0 |
|
- |
| Cl.7.3 Wall thickness(Substantial local irregularities from the minimum values for wall thickness given in the tables shall
be avoided. That means, the minimum wall thickness shall fall at no place below the values given in
Table 1 and Table 2 and the beakers shall comply with the requirement for thermal shock endurance
specified in 8.5.) |
- |
0 |
|
- |
| Cl.8.1 Base(The design of the base shall enable the beaker to stand vertically on a plane horizontal surface without
spinning or rocking) |
- |
0 |
|
- |
| 8.2 Upper edge(The side of the beaker shall be slightly flared near the brim in a smooth and regular curve. The diameter
of the brim shall be of the order of 5 % to 15 % greater than the diameter of the body. The edge of the
brim shall be finished in a plane parallel with that of the horizontal base.) |
- |
0 |
|
- |
| Cl. 8.3 Spout(The spout shall be shaped so that, when the beaker is filled with water, the water may be poured in a
regular stream clear of the side of the beaker. When the beaker is placed on a horizontal surface and
filling is continued beyond its overflow capacity, the water shall first overflow from the spout and not
from any other part of the brim.) |
- |
0 |
|
- |
| Cl.8.4 Scale(Beakers may be provided with a scale, which should approximately indicate the volume contained
in the beaker.) |
- |
0 |
|
- |
| Cl.5 Capacity
(a)overflow of capacity of a beaker shall exceed the nominal capacity by at least 5 %;) |
- |
0 |
|
- |
|
- |
- Included w.e.f 26.11.2025
Cl.6 Material (Beakers shall be made of borosilicate glass 3.3 in accordance with ISO 3585. The glass shall be reasonably free from residual strain and from visible glass defects which might impair the safety and performance of the beaker.) |
| 2909 |
CTL TESTING LABORATORY PRIVATE LIMITED, JAIPUR
| 8180306
| IS 12818 (2010) |
Unplasticized polyvinyl chloride (Pvc - U) screen and casing pipes for bore/tubewells - Specification (Second Revision) |
RMS 35 TO 400, RDS DN100 TO 400, PMS DN200 TO DN400, PDS DN200 TO DN400, CS DN150 TO DN400, CM DN35 TO DN400 AND CD DN100 TO DN400 |
15000 View breakup
-
| Clause No. |
Exclusion |
Testing Charges (Excl. Of Taxes) |
Effective Date |
Remark |
| 9.6(Vicat Softening Temperature
IS 12235 (Part 2).) |
- |
1000 |
|
10% DISCOUNT FOR BIS |
| 9.5(Tensile Strength
IS 12235(Part 13)) |
- |
500 |
|
10% DISCOUNT FOR BIS |
| 9.4 and Table 14(Resistance to External Blows at 0 ?C
IS 12235 (Part 9)) |
- |
1200 |
|
10% DISCOUNT FOR BIS |
| 9.3(Density
IS 12235 (Part 14)) |
- |
500 |
|
10% DISCOUNT FOR BIS |
| 9.2(Internal Diameter) |
- |
200 |
|
10% DISCOUNT FOR BIS |
| 9.1( Visual Appearance) |
- |
0 |
|
10% DISCOUNT FOR BIS |
| 9.1(Visual Appearance) |
- |
0 |
|
10% DISCOUNT FOR BIS |
| 8.4.1 and Table 13
Fig 3B & 4B(Dimensions of sealing elements) |
- |
1000 |
|
10% DISCOUNT FOR BIS |
| 8.4.1 and Table 13
Fig 3B & 4B(Dimensions of sealing elements) |
- |
1500 |
|
10% DISCOUNT FOR BIS |
| 8.4.1 and Table 13
Fig 3B & 4B(Dimensions of sealing elements) |
- |
1000 |
|
10% DISCOUNT FOR BIS |
| 8.4.1 and Table 13
Fig 3B & 4B(Dimensions of sealing elements) |
- |
1000 |
|
10% DISCOUNT FOR BIS |
| 8.4.1 and Table 13
Fig 3B & 4B(Dimensions of sealing elements) |
- |
1000 |
|
10% DISCOUNT FOR BIS |
| 8.4.1 and Table 13
Fig 3B & 4B(Dimensions of sealing elements) |
- |
1000 |
|
10% DISCOUNT FOR BIS |
| 8.4.1 and Table 13
Fig 3B & 4B(Dimensions of sealing elements) |
- |
200 |
|
10% DISCOUNT FOR BIS |
| 8.4(Sealing rings - Hardness) |
- |
500 |
|
10% DISCOUNT FOR BIS |
| 8.1 to 8.3 and Table 11 &12
Fig 3A & 4A(THREADING OF SCREEN ANDCASING PIPES.
IS 554.) |
- |
500 |
|
10% DISCOUNT FOR BIS |
| 8.1 to 8.3 and Table 11 &12
Fig 3A & 4A(THREADING OF SCREEN ANDCASING PIPES.
IS 554.) |
- |
1000 |
|
10% DISCOUNT FOR BIS |
| 7.5 and Table 10
Fig 2A & 2B(Approximate Free Passage Area, in Percent (Mean Value) for Width of Slot (w)) |
- |
500 |
|
10% DISCOUNT FOR BIS |
| 7.5 and Table 10
Fig 2A & 2B(Minimum number of slots on the circumference of the cross-section.) |
- |
500 |
|
10% DISCOUNT FOR BIS |
| 7.5 and Table 10
Fig 2A & 2B(Summation of slot lengths over internal circumference of the cross- section.) |
- |
500 |
|
10% DISCOUNT FOR BIS |
| 7.4 Table 8 & 9 Fig 1(Segmental length for Spigot (average of 4.0)) |
- |
500 |
|
10% DISCOUNT FOR BIS |
| 7.4 Table 8 & 9 Fig 1(Segmental length,mm for socket (average of 4.0)) |
- |
500 |
|
10% DISCOUNT FOR BIS |
| 7.4 Table 8 & 9
Fig 1(Segmental length, l3) |
- |
500 |
|
10% DISCOUNT FOR BIS |
| 7.4 Table 8 & 9
Fig 1(Effective length, l2) |
- |
500 |
|
10% DISCOUNT FOR BIS |
| 7.3.2(Rib height) |
- |
500 |
|
10% DISCOUNT FOR BIS |
| 7.3.1(No.of Ribs) |
- |
500 |
|
10% DISCOUNT FOR BIS |
| 7.2 and Table 5, 6 & 7
Fig 1B(Wall thickness, Max) |
- |
500 |
|
10% DISCOUNT FOR BIS |
| 7.2 and Table 5, 6 & 7
Fig 1B(Wall thickness, Min) |
- |
500 |
|
10% DISCOUNT FOR BIS |
| 7.1, 7.2 and Table 5, 6 & 7 Fig 1B(Mean outside dia over connection,mm (Take 4 reading and maximum valu reported)) |
- |
500 |
|
10% DISCOUNT FOR BIS |
| 7.1, 7.2 and Table 5, 6 & 7 Fig 1B(Outer Diameter at any point, Max) |
- |
500 |
|
10% DISCOUNT FOR BIS |
| 7.1, 7.2 and Table 5, 6 & 7 Fig 1B(Outer Diameter at any point , Min) |
- |
500 |
|
10% DISCOUNT FOR BIS |
| 7.2 and Table 5, 6 & 7
Fig 1B(Mean Outer Diameter of Pipe , Max) |
- |
500 |
|
10% DISCOUNT FOR BIS |
| 7.2 and Table 5, 6 & 7
Fig 1B(Mean Outer Diameter of Pipe, Min) |
- |
500 |
|
10% DISCOUNT FOR BIS |
| 7.2 and Table 5, 6 & 7
Fig 1B(Nominal Diameter) |
- |
500 |
|
10% DISCOUNT FOR BIS |
| 7.2 and Table 5, 6 & 7
Fig 1B(DIMENSIONS - Casing Pipes) |
- |
500 |
|
10% DISCOUNT FOR BIS |
| 7.1 and Table 1, 2, 3, & 4
Fig 1A & 1B(Wall thickness) |
- |
500 |
|
10% DISCOUNT FOR BIS |
| 7.1 and Table 1, 2, 3, & 4
Fig 1A & 1B(Mean Outer Diameter over Connection) |
- |
500 |
|
10% DISCOUNT FOR BIS |
| 7.1 and Table 1, 2, 3, & 4
Fig 1A & 1B(Outer Diameter at any point ) |
- |
500 |
|
10% DISCOUNT FOR BIS |
| 7.1 and Table 1, 2, 3, & 4
Fig 1A & 1B(Mean Outer Diameter of Pipe) |
- |
500 |
|
10% DISCOUNT FOR BIS |
| 7.1 and Table 1, 2, 3, & 4
Fig 1A & 1B(Nominal Diameter) |
- |
500 |
|
10% DISCOUNT FOR BIS |
| 4.1.2 (Ref. Cl 11 of IS 4669)(Composition -Sulphated ash content ) |
- |
500 |
|
10% DISCOUNT FOR BIS |
| 4.1.2 (Ref. Cl 5.1. of IS 4669)(Composition - Loss on heating ) |
- |
500 |
|
10% DISCOUNT FOR BIS |
| 4.1.1 (Ref. 3.4.1. of IS 10151)(Composition - The monomer content (VCM content) in the
resin - Annex A ofIS 10151) |
- |
500 |
|
10% DISCOUNT FOR BIS |
| 5(COLOUR) |
- |
200 |
|
10% DISCOUNT FOR BIS |
| 8.4(Sealing elements
a. Elastomeric material
b. Shore A hardness of sealing Elements
) |
- |
500 |
|
10% DISCOUNT FOR BIS |
| 8.4(Width b) |
- |
200 |
|
10% DISCOUNT FOR BIS |
| 8.3.1
&
8.3.2
(Threading of casing pipe (from 100 to 200 DN Table – 11 & Fig. 3A) & (from 250 to 400 DN Table – 12 & Fig. 4A)
Outside diameter
d1(+0, -0.3)
d2
d3
D1 (+0.3, -0)
D2
D4
D5 (+0.3, -0)
Z
h3 (+0, -0.1)
H4 (+0, -0.1)
) |
- |
200 |
|
10% DISCOUNT FOR BIS |
| 8.2(Threading of casing pipe As per IS 554 (from 40 to 80mm DN)
Number of threads in 25.4mm
Pitch (P)
Height of thread (h)
Major (Gauge Diameter) d
Pitch(d2)
Minor (d1)
External Thread gauge length
Nominal
No. of turns of thread
max
min
) |
- |
200 |
|
10% DISCOUNT FOR BIS |
| 7.5.1
7.5.2
(Slot Dimension (Table 10) Fig 2A & 2B
a. Minimum number of slot on the circumference
b. Σa±5%
c. Mean value of approximate free passage area (%) for width of slot (w)
d. Tolerance on width of slot (w)
e. Width of material between slot (b)) |
- |
200 |
|
10% DISCOUNT FOR BIS |
| 5.0(Colour of Pipes) |
- |
500 |
|
10% DISCOUNT FOR BIS |
| 9.7(Effect on Water
a) Lead (first extraction)
b) Lead (Third extraction)
c) Dialkyl Tin C4 & higher homologues measured as Tin (Third extraction)
d) Cadmium (All three extracts)
e) Mercury (All three extracts)
f) Other Toxic Substances
) |
- |
2500 |
|
10% DISCOUNT FOR BIS |
| 4.1.2(K-Value as per IS-4669) |
- |
1500 |
|
10% DISCOUNT FOR BIS |
| 4.1.1
(VCM Content as per IS 10151 (Annex A)) |
- |
5000 |
|
10% DISCOUNT FOR BIS |
| 7.1(Screen Pipes) |
- |
0 |
|
10% DISCOUNT FOR BIS |
| 11(Marking) |
- |
0 |
|
10% DISCOUNT FOR BIS |
| 5.1(Materials) |
- |
3500 |
|
10% DISCOUNT FOR BIS |
| 8(Packing) |
- |
0 |
|
10% DISCOUNT FOR BIS |
| 4.1.3(Cross Chain Length) |
- |
0 |
|
10% DISCOUNT FOR BIS |
| 7.2(Link Twisted (Cross chain)) |
- |
0 |
|
10% DISCOUNT FOR BIS |
| 7.3(The Basic chains) |
- |
0 |
|
10% DISCOUNT FOR BIS |
| 7.9(Case Depth) |
- |
0 |
|
10% DISCOUNT FOR BIS |
| 8(Marking) |
- |
0 |
|
10% DISCOUNT FOR BIS |
| Cl 9.7(Effect on Water Lead (first extraction)) |
- |
3500 |
|
10% DISCOUNT FOR BIS |
| Cl 9.7(Effect on Water Lead (third extraction)) |
- |
3500 |
|
10% DISCOUNT FOR BIS |
| Cl 9.7(Effect on Water Dialkyl tin C4 and higher homologues(measuredas tin )(third extraction )) |
- |
3500 |
|
10% DISCOUNT FOR BIS |
| Cl 9.7(Effect on Water Cadmium (mean of first extraction, second extraction and third extraction)) |
- |
3500 |
|
10% DISCOUNT FOR BIS |
| Cl 9.7(Effect on Water Mercury (mean of first extraction, second extraction and third extraction)) |
- |
3500 |
|
10% DISCOUNT FOR BIS |
|
24 Sep, 2027 |
- Included w.e.f.08.10.2025 |
| 2910 |
Eastern Regional Laboratory (IOCL), Howrah Terminal
| 5192414
| IS 1460 (2025) |
Automotive Diesel Fuel - Specification (seventh revision) |
- |
19660 View breakup
-
| Clause No. |
Exclusion |
Testing Charges (Excl. Of Taxes) |
Effective Date |
Remark |
| 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) |
- |
0 |
|
- |
| Cl-3.1.4 , 3.2, Table-1 (vii) (b)(Pour point3, °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 (ix)(Distillation, 95 percent v/v recovery, °C, Max) |
- |
2650 |
|
- |
| 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) |
- |
1130 |
|
- |
| Cl-3.1.4 , 3.2, Table-1 (xiv)(Total sulphur, mg/kg, Max) |
- |
4710 |
|
- |
| Cl-3.1.4 , 3.2, Table-1 (xv)(Water content, mg/kg, Max) |
- |
4160 |
|
- |
|
04 Dec, 2028 |
- 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 (xvi) (a) (Cold Filter Plugging Point (CFPP)3, °C, Max: Winter)
Cl-3.1.4 , 3.2, Table-1 (xvi) (b) (Cold Filter Plugging Point (CFPP)3, °C, Max: Summer)
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, 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), hours, 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) |