 |
Light hydrocarbon products and solvents
|
 |
Low-aromatic extraction naphtha III
Use: as a solvent and diluter/thinner in the manufacture of edible fats and oils, chemical industry,
textile industry and the manufacture of paints, glues/adhesives and lacquers
|
Requirements
|
Unit of
measure
|
Value
|
Test method
|
|
Density at 150C,
not highier than
|
kg/m3
|
780
|
PN-EN ISO 12185:2002
|
|
Sulphur content,
not higher than
|
%(m/m)
|
0,003
|
PN-EN ISO 20846:2006
|
|
Benzene content,
not higher than
|
%(m/m)
|
0,05
|
Metoda bad. Nr 092/2009
|
|
Other aromatic hydrocarbon content,
not higher than
|
%(m/m)
|
5
|
Metoda bad. Nr 092/2009
|
|
Distillation beginning point,
not lower than
|
0C
|
70
|
PN-EN ISO 3405:2004
|
|
98% (v/v) destils (evaporates),
not higher than
|
0C
|
120
|
PN-EN ISO 3405:2004
|
|
Total residues and losses,
not higher than
|
%(v/v)
|
2
|
PN-EN ISO 3405:2004
|
|
Non-saturated hydrocarbons content,
not higher than
|
%(m/m)
|
2
|
WT RNJe 14/08 p.3.2
|
|
Non-volatile matter content,
|
-
|
does not
contain
|
WT RNJe 14/08 p.3.3
|
Naphtha 110+
Use: as a solvent or diluter/thinner in the rubber industry, chemical industry and in the manufacture
of paints and lacquers
|
Requirements
|
Unit of
measure
|
Value
|
Test method
|
|
Sulphur content,
max
|
%(m/m)
|
0,003
|
PN-EN ISO 20846:2006
|
|
Benzene content,
max
|
%(m/m)
|
0,05
|
ASTM D 5134
|
|
Aromatic hydrocarbon content, not higher than
|
%(m/m)
|
18
|
ASTM D 5134
|
|
Distillation beginning point,
not lower than
|
0C
|
110
|
PN-EN ISO 3405:2004
|
|
Destillation finishing point
|
0C
|
155
|
PN-EN ISO 3405:2004
|
Wide hexane cut
Use: as a solvent and diluter/thinner in the manufacture of edible fats and oils, chemical industry
and textile industry
|
Requirements
|
Unit of
measure
|
Value
|
Test method
|
|
Density 150C,
max
|
kg/m3
|
725
|
PN-EN ISO 12185:2002
|
|
Sulphur content,
max
|
ppm
|
3
|
PN-EN ISO 20846:2006
|
|
Benzene content
max
|
ppm
|
10
|
Metoda bad. Nr 092/2009
|
|
Other aromatic hydrocarbon content,
max
|
ppm
|
50
|
Metoda bad. Nr 092/2009
|
|
5% (v/v) distile (evaporates),
min
|
0C
|
66
|
PN-EN ISO 3405:2004
|
|
95% (v/v) distils (evaporated),
max
|
0C
|
80
|
PN-EN ISO 3405:2004
|
|
Water content,
max
|
%(m/m)
|
0,01
|
PN-EN ISO 12937:2005
|
Wide hexane cut II
Use: as a solvent and diluter/thinner in the manufacture of edible fats and oils, chemical industry
and textile industry
|
Requirements
|
Unit of
measure
|
Value
|
Test method
|
|
Density 150C,
max
|
kg/m3
|
700
|
PN-EN ISO 12185:2002
|
|
Sulphur content,
max
|
ppm
|
3
|
PN-EN ISO 20846:2006
|
|
Benzene content
max
|
ppm
|
10
|
Metoda bad. Nr 092/2009
|
|
Other aromatic hydrocarbon content,
max
|
ppm
|
50
|
Metoda bad Nr 092/2009
|
|
5% (v/v) distile (evaporates),
min
|
0C
|
45
|
PN-EN ISO 3405:2004
|
|
95% (v/v) distils (evaporated),
max
|
0C
|
80
|
PN-EN ISO 3405:2004
|
|
Water content,
max
|
%(m/m)
|
0,01
|
PN-EN ISO 12937:2005
|
Iso-hexane cut
Use: as a solvent and diluter/thinner in the manufacture of edible fats and oils, chemical industry
and textile industry
|
Requirements
|
Unit of
measure
|
Value
|
Test method
|
|
Density at 150C,
max
|
kg/m3
|
680
|
PN-EN ISO 12185:2002
|
|
Sulphur content,
max
|
ppm
|
3
|
PN-EN ISO 20846:2006
|
|
Benzene content,
max
|
ppm
|
10
|
Metoda bad. Nr 092/2009
|
|
Other aromatic hydrocarbon content,
max
|
ppm
|
50
|
Metoda bad. Nr 092/2009
|
|
Distillation beginning point,
min
|
0C
|
36
|
PN-EN ISO 3405:2004
|
|
98% (v/v) distils (evaporates),
max
|
0C
|
70
|
PN-EN ISO 3405:2004
|
|
Water content,
max
|
%(m/m)
|
0,01
|
PN-EN ISO 12937:2005
|
N-pentane
Use: as a solvent and diluter/thinner in chemical industry and in styropore production
|
Requirements
|
Unit of
measure
|
Value
|
Thest method
|
|
Sulphur content,
max
|
ppm
|
3
|
PN-EN ISO 20846:2006
|
|
Destillation beginning point,
min
|
0C
|
30
|
PN-EN ISO 3405:2004
|
|
98% (v/v) distils (evaporates),
max
|
0C
|
42
|
PN-EN ISO 3405:2004
|
|
N-pentane content,
min
|
%(m/m)
|
84
|
ASTM D 5134-98
|
|
Cyclopentane and heavier hydrocarbons contents,
max
|
%(m/m)
|
1,5
|
ASTM D 5134-98
|
Iso-pentane
Use: as a solvent and diluter/thinner in chemical industry and in car/automobile cleaning
|
Requirements
|
Unit of
measure
|
Value
|
Test method
|
|
Sulphur content,
max
|
ppm
|
3
|
PN-EN ISO 20846:2006
|
|
Isopentane content,
min
|
%(m/m)
|
70
|
ASTM D 5134-98
|
|
Butanes content,
max
|
%(m/m)
|
5,0
|
ASTM D 5134-98
|
|
Cyclopentane and heavier hydrocarbons content,
max
|
%(m/m)
|
1,5
|
ASTM D 5134-98
|
Painter's naphtha AP
Use: as a solvent of paints and lacquers
|
Requirements
|
Unit of
measure
|
Value
|
Test method
|
|
Density at 150C,
min
|
g/cm3
|
0,750
|
PN-EN ISO 12185:2002
PN ISO 3675:2004
|
|
Normal distillation, multi-cut composition:
- beginning 0C,
min
- finishing 0C,
max
|
%(v/v)
|
130
250
|
PN-EN ISO 3405:2004
|
|
Sulphur content,
max
|
%(m/m)
|
0,05
|
PN-EN ISO 8754:2007
|
|
Ignition point/temperature,
min
|
0C
|
23
|
PN-EN ISO 2719:2007
|
|
Aromatic hydrocarbons content,
max
|
%(m/m)
|
15
|
PN-78/C-04047
|
Cleaning kerosene
Use: for cleaning metal parts of mechinery, especially rolling bearings, to remove grease,
has anti-corrosive properties
|
Requirements
|
Untol of
measure
|
Value
|
Test method
|
|
Normal distillation, multi-cut composition %(v/v):
- beginning 0C,
not lower than
- finishing 0C,
not higher than
|
0C
|
185
310
|
PN-EN ISO 3405:2004
|
|
Ignition point/temperature,
not lower than
|
0C
|
56
|
PN-EN ISO 2719:2007
|
|
Water content,
|
-
|
does not contain
|
wg pkt. 3.3 TWT 12/96
|
|
Solid foreign matter content,
|
-
|
does not contain
|
PN-58/C-04089
|
|
Water extract reaction,
|
-
|
neutral
|
PN-84/C-04064
|
|
Sulphur content,
not higher than
|
%(m/m)
|
0,15
|
PN-ISO 8754:2007
|
|
Acid number, mg KOH per 100 cm3 of kerosene,
not highier than
|
mg/cm3
|
0,6-3,0
|
PN-85/C-04066
|
|
Corrosive effect testing on a copper plate at 500C, for 96 hours
|
-
|
resists
|
PN-85/C-04093
|
Protective kerosene
Use: for cleaning metal parts of machinery, especially rolling bearings, to remove grease,
has anti-corrosive properties
|
Requirements
|
Unit of
measure
|
Value
|
Test method
|
|
Density at 150C,
|
g/cm3
|
quote in attestation certificates
|
PN-EN ISO 12185:2002
PN-EN ISO 3675:2004
|
|
Normal distillation, multi-cut composition %(v/v):
- beginning,
not lower than
- finishing,
not higher than
|
0C
|
185
310
|
PN-EN ISO 3405:2004
|
|
Ignition point/temperature,
not lower than
|
0C
|
62
|
PN-EN ISO 2719:2003(U)
|
|
Water content,
not higher than
|
%(m/m)
|
0,1
|
PN-EN ISO 12937:2002(U)
|
|
Water extract reaction,
|
-
|
neutral
|
PN-84/C-04064
|
|
Sulphur content,
not higher than
|
%(m/m)
|
0,1
|
PN-ISO 8754:1993
|
|
Acid number, mg KOH per 100 cm3 of kerosene,
not higher than
|
mg/cm3
|
0,6
|
PN-85/C-04066
|
|
Corrosive effect testing on a copper plate at 500C, for 96 hours
|
-
|
1
|
PN-EN ISO 2160:2004
|
Lighting kerosene
Use: for lighting
|
Requirements
|
Unit of
measure
|
Value
|
Test method
|
|
Normal distillation, multi-cut composition %(v/v):
- begining 0C,
not lower than
- finishing 0C,
not higher than
|
0C
|
180
315
|
PN-EN ISO 3405:2004
|
|
Ignition point/temperature,
not lower than
|
0C
|
56
|
PN-EN ISO 2719:2007
|
|
Pour point/temperature,
|
0C
|
-15
|
PN-83/C-04117
|
|
Highest non-smoking flame,
not lower than
|
mm
|
20
|
PN-83/C-04121
|
|
Water extract reaction,
|
-
|
neutral
|
PN-84/C-04064
|
|
Sulphur content,
not higher than
|
%(m/m)
|
0,15
|
PN-ISO 8754:2007
|
|
|
