Ceypetco Products
|
| |
| SPECIFICATION
FOR UNLEADED PETROL (P-011) - 90 OCTANE |
|
|
Property/Test |
Test |
Method |
Specifications |
| |
IP |
ASTM-D |
|
| Appearance |
|
|
Clear & free from water and impurities |
| Density @15 0 C kg/m 3 |
160 |
1298 |
725- 785 |
| Reid Vapour Pressure @37.8 0 C (100 0
F) |
69 |
323/5193 |
35-70 kpa** (5.0 - 10psi) |
| Marketing Colour |
|
|
Pink |
| Octane Number (RON) |
237 |
2699 |
Min 90 |
| (RON+MON)/2 |
|
2700/2699 |
Min 89 |
| Distilliation |
123 |
86 |
|
| IBP o C |
|
|
To be reported |
| 10% Vol. Evoporated 0 C |
|
|
45-70 |
| 50% Vol. Evoporated 0 C |
|
|
80-125 |
| 70% Vol. Evoporated 0 C |
|
|
Max 188 |
| 90% Vol. Evoporated 0 C |
|
|
Max 215 |
| Res % |
|
|
Mx 2.0 |
| Doctor Test |
30 |
4952 |
Sweet or less than 15ppm RSH |
| Total Sulphur content %wt |
107/243 |
1266 |
Max 0.10 |
| Lead content Pb mg/l |
224 |
3341/3237 |
Max 13 ppm |
| Existent gum mg/100ml |
|
|
Max 5 |
| Oxygenate content Vol % |
|
|
Max 15 |
| Ind period @ 100 0 C |
|
|
Min 480 Minutes |
| Cu Strip corrosion 3 hrs @ 50 0 C |
|
|
Max 188 |
| Benzene % vol |
|
|
Max 8.0 |
|
|
| SPECIFICATION
FOR UNLEADED PETROL (P-018) - 95 OCTANE |
|
|
Property/Test |
Test |
Method
|
Specifications |
| |
IP |
ASTM-D |
|
| Appearance |
|
|
Clear & free from water
and impurities |
| Density @15 0 C kg/m 3 |
160 |
1298 |
725- 785 |
| Reid Vapour Pressure @37.8 0
C (100 0 F) |
69 |
323/5193 |
35-70 kpa** (5.0 - 10psi) |
| Marketing Colour |
|
|
Pink |
| Octane Number (RON) |
237 |
2699 |
Min 95 |
| (RON+MON)/2 |
|
2700/2699 |
Min 89 |
| Distilliation |
123 |
86 |
|
| IBP o C |
|
|
To be reported |
| 10% Vol. Evoporated 0 C |
|
|
45-70 |
| 50% Vol. Evoporated 0 C |
|
|
80-125 |
| 70% Vol. Evoporated 0 C |
|
|
Max 188 |
| 90% Vol. Evoporated 0 C |
|
|
Max 215 |
| Res % |
|
|
Mx 2.0 |
| Doctor Test |
30 |
4952 |
Sweet or less than 15ppm RSH |
| Total Sulphur content %wt |
107/243 |
1266 |
Max 0.10 |
| Lead content Pb mg/l |
224 |
3341/3237 |
Max 13 ppm |
| Existent gum mg/100ml |
|
|
Max 5 |
| Oxygenate content Vol % |
|
|
Max 15 |
| Ind period @ 100 0 C |
|
|
Min 480 Minutes |
| Cu Strip corrosion 3 hrs @ 50
0 C |
|
|
Max 188 |
| Benzene % vol |
|
|
Max 8.0 |
|
|
| SPECIFICATION
FOR AUTO DIESEL (P-013) |
|
|
Property/Test |
Test
|
Method |
Specifications |
| |
IP |
ASTM-D |
|
| Appearance |
|
|
Clear & free from water
and impurities |
| Density @15 0 C kg/m 3 |
160 |
1298 |
Max 870 |
| Colour ASTM |
196 |
1500 |
Report |
| Marketing Colour |
|
|
Amber |
| Distilliation |
123 |
86 |
|
| IBP o C |
|
|
Report (156-194) |
| 10% Evoporated 0 C |
|
|
Report (201 - 266) |
| 50% Evoporated 0 C |
|
|
Report (279 - 294 ) |
| 90% Evoporated 0 C |
|
|
Max 370 |
| Recovery @ 315 0 C |
|
|
Min 50 |
| Recovery @ 350 0 C |
|
|
Min 80 |
| Cetane Index or |
|
976 |
Min 45 ** |
| Cetane Number |
|
613 |
Min 48 |
| Cloud Point 0 C ( 0 F) |
|
2500 |
Max 15.5 (Max 60) |
| CFPP 0 C ( 0 F) |
309 |
|
Max 10 (Max 15) |
| Sulphur Content % (w/w) |
61 |
129 or 1552 |
Max 0.3 |
| Flash Point (PMCC) 0 C ( 0 F) |
34 |
93 |
Min 60 (Min 140) |
| Viscocity Kin @37.8 0 C cst |
71 |
445 |
1.5 -5.0 |
| Water Content % (v/v) |
74 |
95 |
Max 0.005 |
| Cu Strip corrosion 3 hrs @ 50
0 C |
154 |
130 |
Max 1 |
| Ash % w/w |
4 |
482 |
Max 0.02 |
| Carbon residue Ramsbottom |
14 |
524 |
Max 0.3 |
| on 10% residue % (w/w) |
53 |
473 |
Max 0.01 |
| Sediment by extraction % (w/w) |
1 |
974 |
Max 0.2 |
| Total Acid No. KOH mg /g |
1 |
947 |
Nil |
| Strong Acid No. KOH mg /g |
12 |
240 |
Min 10500 |
| Caloric value gross K Cal/KG |
|
|
|
| **N/A if any cetane improver
additive is present |
|
|
|
|
|
| SPECIFICATION
FOR SUPER DIESEL (P-016) |
|
|
Property/Test |
Test |
Method |
Specifications |
| |
IP |
ASTM-D |
|
| Appearance |
|
|
Clear & free from water
and impurities |
| Density @15 0 C kg/m 3 |
160 |
1298 |
820 - Max 870 |
| Colour ASTM |
196 |
1500 |
Report |
| Marketing Colour |
|
|
Amber |
| Distilliation |
123 |
86 |
|
| IBP o C |
|
|
Report (196 - 204 ) |
| 10% Evoporated 0 C |
|
|
Report (245 - 245) |
| 50% Evoporated 0 C |
|
|
Report (288 - 294) |
| 90% Evoporated 0 C |
|
|
Max 340 |
| Recovery @ 315 0 C |
|
|
Min 50 |
| Recovery @ 350 0 C |
|
|
Min 80 |
| Cetane Index or |
|
976 |
Min 50 ** |
| Cetane Number |
|
613 |
Min 53 |
| Cloud Point 0 C ( 0 F) |
|
2500 |
Max 15.5 (Max 60) |
| CFPP 0 C ( 0 F) |
309 |
|
Max 10 (Max 15) |
| Sulphur Content % (w/w) |
61 |
129 or 1552 |
Max 0.05 |
| Total Aromatic content |
|
|
25 |
| Poly Aromatic content ( di+tri+)%m/m |
|
|
5 |
| Flash Point (PMCC) 0 C ( 0 F) |
34 |
93 |
Min 60 (Min 140) |
| Viscocity Kin @37.8 0 C cst |
71 |
445 |
1.5 -5.0 |
| Water Content % (v/v) |
74 |
95 |
Max 0.005 |
| Cu Strip corrosion 3 hrs @ 50
0 C |
154 |
130 |
Max 1 |
| Ash % w/w |
4 |
482 |
Max 0.02 |
| Carbon residue Ramsbottom |
|
|
|
| on 10% residue % (w/w) |
14 |
524 |
Max 0.3 |
| Sediment by extraction % (w/w) |
53 |
473 |
Max 0.01 |
| Total Acid No. KOH mg /g |
1 |
974 |
Max 0.08 |
| Strong Acid No. KOH mg /g |
1 |
947 |
Nil |
| Caloric value gross K Cal/KG |
12 |
240 |
Min 10500 |
| **N/A if any cetane improver
additive is present |
|
|
|
|
Note
1: Naptha should be preferably straight run
but, hydrotreated,cracked material may be included up to 10% vol
provided all points of specificationsare met. Alternatively an
agreed Gas liquid Chromotographic method may be used.
|
|
| SPECIFICATION
FOR FURNACE OIL 200 SEC (P-031) |
|
|
Property/Test |
Test |
Method |
Specifications |
| |
IP |
ASTM-D |
|
| Density @15 0 C kg/m 3 |
160 |
1298 |
Max 970 |
| Flash Point (PMCC) 0 C ( 0 F) |
34 |
93 |
Min 60 (Min 140) |
| Pour Point 0 C ( 0 F) |
15 |
97 |
Max 21.1(70) |
| Sulphur Content % (w/w) |
61 |
1552 |
Max 3.5 |
| Redwood 1 @100 0 F Sec (Note
1) |
|
|
Max 200 |
| Viscosity Kinematic @ 50 0 C
(112 0 F) |
71 |
445 |
Report |
| Water content %(v/v) |
74 |
95 |
Max 1.0 |
| Ash % wt |
4 |
482 |
Max 0.2 |
| Conradson Carbon % w/w |
|
189 |
Max 12 |
| Sediment by Extraction ppm |
53 |
473 |
Max 0.25 |
| Caloric Value (gross) k.Cal/kg |
12 |
240 |
Min 10200 |
| Strong Acid No. KOH mg /g |
1 |
974 |
Nil |
| Metal Contaminants |
|
|
|
| V |
|
3605 |
Max 200 ppm |
| Na + K |
|
3605 |
Report |
| Ca |
|
3605 |
Report |
| Pb |
|
3605 |
Report |
|
|
| SPECIFICATION
FOR FURNACE OIL 500 SEC (P-025) |
|
|
Property/Test |
Test |
Method |
Specifications |
| |
IP |
ASTM-D |
|
| Density @15 0 C kg/m 3 |
160 |
1298 |
Max 970 |
| Flash Point (PMCC) 0 C ( 0 F) |
34 |
93 |
Min 60 (Min 140) |
| Pour Point 0 C ( 0 F) |
15 |
97 |
Max 21.1(70) |
| Sulphur Content % (w/w) |
61 |
1552 |
Max 3.5 |
| Redwood 1 @100 0 F Sec (Note
1) |
|
|
Max 500 |
| Viscosity Kinematic @ 50 0 C
(112 0 F) |
71 |
445 |
Report |
| Water content %(v/v) |
74 |
95 |
Max 1.0 |
| Ash % wt |
4 |
482 |
Max 0.2 |
| Conradson Carbon % w/w |
|
189 |
Max 12 |
| Sediment by Extraction ppm |
53 |
473 |
Max 0.25 |
| Caloric Value (gross) k.Cal/kg |
12 |
240 |
Min 10200 |
| Strong Acid No. KOH mg /g |
1 |
974 |
Nil |
| Metal Contaminants |
|
|
|
| V |
|
3605 |
Max 200 ppm |
| Na + K |
|
3605 |
Report |
| Ca |
|
3605 |
Report |
| Pb |
|
3605 |
Report |
|
|
| SPECIFICATION
FOR FURNACE OIL 800 SEC (P-026) |
|
|
Property/Test |
Test |
Method |
Specifications |
| |
IP |
ASTM-D |
|
| Density @15 0 C kg/m 3 |
160 |
1298 |
Max 970 |
| Flash Point (PMCC) 0 C ( 0 F) |
34 |
93 |
Min 60 (Min 140) |
| Pour Point 0 C ( 0 F) |
15 |
97 |
Max 21.1(70) |
| Sulphur Content % (w/w) |
61 |
129 or 1552 |
Max 3.5 |
| Redwood 1 @100 0 F Sec (Note
1) |
|
|
Max 800 |
| Viscosity Kinematic @ 50 0 C
(112 0 F) |
71 |
445 |
Report |
| Water content %(v/v) |
74 |
95 |
Max 1.0 |
| Ash % wt |
4 |
482 |
Max 0.2 |
| Conradson Carbon % w/w |
|
189 |
Max 12 |
| Sediment by Extraction ppm |
53 |
473 |
Max 0.25 |
| Caloric Value (gross) k.Cal/kg |
12 |
240 |
Min 10200 |
| Strong Acid No. KOH mg /g |
1 |
974 |
Nil |
| Metal Contaminants |
|
|
|
| V |
|
3605 |
Max 200 ppm |
| Na + K |
|
3605 |
Report |
| Ca |
|
3605 |
Report |
| Pb |
|
3605 |
Report |
|
|
| SPECIFICATION
FOR FURNACE OIL 1000 SEC (P-028) |
|
|
Property/Test |
Test
|
Method |
Specifications |
| |
IP |
ASTM-D |
|
| Density @15 0 C kg/m 3 |
160 |
1298 |
Max 970 |
| Flash Point (PMCC) 0 C ( 0 F) |
34 |
93 |
Min 60 (Min 140) |
| Pour Point 0 C ( 0 F) |
15 |
97 |
Max 21.1(70) |
| Sulphur Content % (w/w) |
61 |
129 or 1552 |
Max 3.5 |
| Redwood 1 @100 0 F Sec (Note
1) |
|
|
Max 1000 |
| Viscosity Kinematic @ 50 0 C
(112 0 F) |
71 |
445 |
Report |
| Water content %(v/v) |
74 |
95 |
Max 1.0 |
| Ash % wt |
4 |
482 |
Max 0.2 |
| Conradson Carbon % w/w |
|
189 |
Max 12 |
| Sediment by Extraction ppm |
53 |
473 |
Max 0.25 |
| Caloric Value (gross) k.Cal/kg |
12 |
240 |
Min 10200 |
| Strong Acid No. KOH mg /g |
1 |
974 |
Nil |
| Metal Contaminants |
|
|
|
| V |
|
3605 |
Max 200 ppm |
| Na + K |
|
3605 |
Report |
| Ca |
|
3605 |
Report |
| Pb |
|
3605 |
Report |
|
|
| SPECIFICATION
FOR FURNACE OIL 1500 SEC (P-029) |
|
|
Property/Test |
Test |
Method |
Specifications |
| |
IP |
ASTM-D |
|
| Density @15 0 C kg/m 3 |
160 |
1298 |
Max 970 |
| Flash Point (PMCC) 0 C ( 0 F) |
34 |
93 |
Min 60 (Min 140) |
| Pour Point 0 C ( 0 F) |
15 |
97 |
Max 21.1(70) |
| Sulphur Content % (w/w) |
61 |
129 or 1552 |
Max 3.5 |
| Redwood 1 @100 0 F Sec (Note
1) |
|
|
Max 1500 |
| Viscosity Kinematic @ 50 0 C
(112 0 F) |
71 |
445 |
Report |
| Water content %(v/v) |
74 |
95 |
Max 1.0 |
| Ash % wt |
4 |
482 |
Max 0.2 |
| Conradson Carbon % w/w |
|
189 |
Max 12 |
| Sediment by Extraction ppm |
53 |
473 |
Max 0.25 |
| Caloric Value (gross) k.Cal/kg |
12 |
240 |
Min 10200 |
| Strong Acid No. KOH mg /g |
1 |
974 |
Nil |
| Metal Contaminants |
|
|
|
| V |
|
3605 |
Max 200 ppm |
| Na + K |
|
3605 |
Report |
| Ca |
|
3605 |
Report |
| Pb |
|
3605 |
Report |
|
|
| SPECIFICATION
FOR LANKA HEAVY DIESEL (P-029) |
|
|
Property/Test |
Test |
Method |
Specifications |
| |
IP |
ASTM-D |
|
| Colour |
196 |
1500 |
|
| Density @15 0 C kg/m 3 |
160 |
1298 |
To be reported |
| Cetane No. |
21 |
|
Min 35 |
| Flash Point (PMCC) 0 C ( 0 F) |
34 |
93 |
Min 65.5 (Min 150) |
| Distilliation |
123 |
86 |
|
| IBP o C |
|
|
Report |
| 10% Evoporated 0 C |
|
|
Report |
| 50% Evoporated 0 C |
|
|
Report |
| 80% Evoporated 0 C |
|
|
Report |
| FBP Evoporated 0 C |
|
|
Report |
| Sulphur Content % (w/w) |
61 |
1552 or 4294 |
Max 1.8 |
| Redwood 1 @100 0 F Sec (Note
1) |
|
|
36-53 |
|
71 |
445 |
Report |
| Water content %(v/v) |
74 |
95 |
Max 1.0 |
| Cu-Strip Corrosion 3Hrs@50 0
C |
154 |
130 |
Max 1 |
| Ash % wt |
4 |
482 |
Max 0.02 |
| Cloud Point 0 C ( 0 F) |
|
2500 |
Max 15.5(60) |
| CFPP 0 C ( 0 F) |
309 |
|
Max10(50) |
| Carbon Residue Ramsbottom |
53 |
473 |
Max 0.25 |
| On 105 residue % (W/W) |
14 |
524 |
Max 0.9 |
| Strong Acid No. KOH mg /g |
1 |
974 |
Nil |
| Metal Contaminants |
|
|
|
| V |
|
3605 |
Report |
| Na |
|
3605 |
Report |
| K |
|
3605 |
Report |
| Ca |
|
3605 |
Report |
| Pb |
|
3605 |
Report |
|
|
| SPECIFICATION
FOR CHEMICAL NAPTHA (P-021) |
|
|
Property/Test |
Test |
Method |
Specifications |
| |
IP |
ASTM-D |
|
| Density @15 0 C kg/m 3 |
160 |
1298 |
650-720 |
| Reid Vapour Pressure @37.8*C (100*F) |
|
322 |
Max 13 PSI (89.7kpa) |
| Colour Saybolt |
|
156 |
Min 2.5 |
| Distillation |
|
86 |
|
| IBP o C |
|
|
|
| 10% Vol. Evoporated 0 C |
|
|
Max 75 |
| 50% Vol. Evoporated 0 C |
|
|
Max 115 |
| 70% Vol. Evoporated 0 C |
|
|
Max 145 |
| 90% Vol. Evoporated 0 C |
|
|
Max 170 |
| End Point o C |
|
|
Max 180 |
| Hydrogen Sulphide ppm |
UOP 163 |
|
Max 3 |
| Sulphur content ppm |
UOP 357 |
|
Max 50 |
| Lead content ppb |
UOP 350 |
|
Max 50 |
| Composition:- |
154 |
|
|
| Parafins % Vol |
|
|
Min 70 |
| Oleines % Vol |
|
|
Max 1.0 |
| Napthenes % Vol |
|
|
To be reported |
| Aromatics % Vol |
156 |
1319 |
Max 15 |
|
|
| SPECIFICATION
FOR LANKA SBP 60 / 145 (P-071) |
|
|
Property/Test |
Test |
Method |
Specifications |
| |
IP |
ASTM-D |
|
| Density @15 0 C kg/m 3 |
160 |
1298 |
Max 713 |
| Colour Saybolt |
|
156 |
-Min 25 |
| Distillation |
123 |
86 |
|
| IBP o C |
|
|
Min 60 |
| 10% Vol. Evoporated 0 C |
|
|
Report |
| 30% Vol. Evoporated 0 C |
|
|
Report |
| 50% Vol. Evoporated 0 C |
|
|
85-105 |
| 70% Vol. Evoporated 0 C |
|
|
Report |
| 90% Vol. Evoporated 0 C |
|
|
105-130 |
| 95% Vol. Evoporated 0 C |
|
|
Max 145 |
| 98.5% Vol. Evoporated 0 C |
|
|
Max 155 |
| Recovery % Vol |
|
|
Min 98 |
| Residue % Vol |
|
|
Max 1 |
| Sulphur content ppm |
243 |
|
Max 50 |
| Aromatic content % Vol |
156 |
1219 |
Max 16 |
| Cu Strip corrosion 3 hrs @ 50*
C |
154 |
130 |
Max 1 |
|
|
| SPECIFICATION
FOR LANKA L P G (P-022) |
|
|
Property/Test |
Test |
Method |
Specifications |
| |
IP |
ASTM-D |
|
| Vapour Pressure @37.8 0 C kPa(PSI) |
|
1267 |
413.8-620.7(60-90) |
| Boil Test |
|
1837 |
|
| 10% Vol. Evoporated 0 C |
|
|
Report |
| 50% Vol. Evoporated 0 C |
|
|
Report |
| 75% Vol. Evoporated 0 C |
|
|
Report |
| 95% Vol. Evoporated 0 C |
|
|
Max 3.3 |
| Residue % voll@ 37.8 0 C |
|
|
Max 1 |
| Composition |
|
GLC |
|
| Propane % vol |
|
|
Report |
| Butane % vol |
|
|
Report |
| C5+%mol |
|
2163 |
Max2 |
| Suophur content ppm - Un-stenched |
|
2784 |
Max 200 |
| RSH ppm |
|
2420 |
Max 50 |
| H2S (Doctor Test) |
|
|
Sweet / 0.75mg m3 max |
| Cu Strip corrosion 2 hrs @ 37.8*
C |
|
1838 |
max1 |
| Dicnes content mol% |
|
GLC |
Max 0.5 |
| Alkynes content mol% |
|
GLC |
Max 0.5 |
|
|
| SPECIFICATION
FOR LANKA INDUSTRIAL KEROSENE (P-012) |
|
|
Property/Test |
Test |
Method |
Specifications |
| |
IP |
ASTM-D |
|
| Vapour Pressure @37.8 0 C kPa(PSI) |
|
1267 |
Clear, bright and visually free
from solid matter & undissolved water at normal ambient
temperature |
| Colour, visual |
|
|
Yellow |
| Density @ 15º C kg/m³ |
160 |
1298 |
775-840 |
| DISTILLATION |
123 |
86 |
|
| IBP º C |
|
|
Report |
| 10% Vol. @ º C |
|
|
Maxc. 205 |
| 20% Vol. @ º C |
|
|
Report |
| 50% Vol. @ º C |
|
|
Report |
| 90% Vol. @ º C |
|
|
Report |
| End Point º C |
|
|
Max. 300 |
Residue % Vol.
Max |
|
|
1.5 |
| Loss % Vol. Max. |
|
|
1.5 |
| COMBUSTION |
|
|
|
| Smoke point mm |
|
1322 |
19 |
| Flash point °C |
170 |
56 |
Min 38 |
| COMPOSITION |
|
|
|
Acidity, total mg
KOH/g |
354 |
3242 |
0.05 |
| Aromatic % Vol. Max. |
156 |
1319 |
25 |
| Olefin, % Vol. Max. |
156 |
1319 |
5 |
Sulpher, total % mass
Max. |
|
4294 |
0.3 |
Sulpher, Mercaptantotal % mass
Max. |
342 |
3227 |
0.003 |
| Or Doctor Test |
30 |
4952 |
Negative |
Cu Corrosion 2 hrs. @
100 º C |
154 |
130 |
1 |
|
|
| SPECIFICATION
FOR BITUMEN (80/100) |
|
|
Property/Test |
Test |
Method |
Specifications |
| |
IP |
ASTM-D |
|
| SPECIFIC GRAVITY @ 25/25 DEG.C |
|
|
1.01 - 1.06 |
| PENETRATION @ 25 DEG.C 100 G 5
SECS. 1/10 MM |
19 |
5 |
80 - 100 |
| SOFTENING POINT DEG. C |
58 |
36 |
45 - 55 |
| LOSS ON HEATING FOR 5 HRS. AT 163
DEG.C |
|
|
|
| |
LOSS BY WEIGHT PERCENT |
45 |
6 |
0.5 MAX. |
| |
PENETRATION AFTER LOSS ON HEATING TEST, PERCENTAGE
OF ITS ORIGINAL VALUE |
49 |
5 |
80 MIN |
SOLUBILITY IN CS 2 OR CCL 4 OR
TRICHLOROETHYLENE WEIGHT PERCENT
|
|
4 |
99.0 MIN. |
| FLASH POINT COC DEG.C |
|
92 |
232 MIN. |
| DUCTILITY @ 25 DEG. C (MM) |
|
113 |
1000 MIN. |
|
|
| SPECIFICATION
FOR BITUMEN (60/70) |
|
|
Property/Test |
Test |
Method |
Specifications |
| |
IP |
ASTM-D |
|
| SPECIFIC GRAVITY @ 25/25 DEG.C |
|
|
1.01 - 1.06 |
| PENETRATION @ 25 DEG.C 100 G 5
SECS. 1/10 MM |
19 |
5 |
60 - 70 |
| SOFTENING POINT DEG. C |
58 |
36 |
48 - 56 |
| LOSS ON HEATING FOR 5 HRS. AT 163
DEG.C |
|
|
|
| |
LOSS BY WEIGHT PERCENT |
45 |
6 |
0.2 MAX. |
| |
PENETRATION AFTER LOSS ON HEATING TEST, PERCENTAGE
OF ITS ORIGINAL VALUE |
|
|
|
| SOLUBILITY IN CS 2 OR CCL 4 OR
TRICHLOROETHYLENE WEIGHT PERCENT |
|
4 |
99.0 MIN. |
| FLASH POINT COC DEG.C |
|
92 |
250 MIN. |
| DUCTILITY @ 25 DEG. C (MM) |
|
113 |
1000 MIN. |
|
|
Agro Products & Prices
The price payable for Agro Chemical
products shall be the price effective on the date of delivery.
These prices are subject to change without prior notice. Since
the application of these products are beyond our control, we cannot
assume responsibility either for the application, storage, transport,
or handling of the chemical or any damage to crops or human beings/livestock
other than for the quality of the product at the time of despatch
from our Godown. This price list cancels and supersedes all previous
price notifications relating to the sale of Agro Chemical Products.
We look forward to receiving
your esteemed orders for the above products which will receive
our prompt attention.
|