| Straight run petrol | |||
|---|---|---|---|
| Description of index | Norm for make | Test method | |
| А | Б | ||
| Octan number for motor method, no less than | 55 | TDS-511 | |
| Fraction composition: | TDS-2177 | ||
| - Initial boiling point.0C . not more than | 35 | 35 | |
| - end of boil, ºС, not higher | 185 | 185 | |
| - balance share in flask, % (for volume), no more than | 2 | 2 | |
| - balance and losses, % (for volume), no more than | 4 | 4 | |
| Saturated steam preassure, kPa | 35-70 | TDS-1756 или TŞ 05766698-34- 2004 ASTM D 323-94 |
|
| Induction period, min, no less than | 600 | ||
| Mass portion of sulfur, %, no less then | 0,1 | TDS-19121 | |
| Actual resin concentration.mg 100sm3 fuel, not more than | 3,0 | TDS-1567 или TŞ 05766698-58- 2004/ ASTM D 381-01 |
|
| Color | From colorless before light yellow | Визуально | |
| Presence of mechanical impurities and water | no | По п. 4.2 | |
| Density 200 C , kg/m3 | Have no standart, Determination is nessesary | TDS-3900 | |
| Slax wax | |||
|---|---|---|---|
| № | Description of Index | Figure | |
| WAX (mix) | WAX (SN-180) | ||
| 1 | Mass portion of oil, %, not more than | 10,0 | TDS-511 |
| 2 | Mass portion of water, %, not more than | 0,1 | TDS-2177 |
| 3 | Density, at 20oC,g/cm3, not more than | Не нормируется, определение обязательно | Не нормируется, определение обязательно |
| 4 | Kinematic viscosity at 100 oC, mm2/s | Не более 4,0 | Не более 4,0 |
| 5 | Flash point, oC, not less than | 200 | 220 |
| 6 | Fluidity temperature, 0С, not less than | 42 | 51 |
| 7 | Mass portion of mechanical impurities,%, not less than | 0,1 | 0,1 |
| 8 | Mass portion of sulfur,%, not more than | 0,5 | 0,5 |
| Base oil | |||||||
|---|---|---|---|---|---|---|---|
| № | Description of Index | Figure | |||||
| SN-80 | SN-180 | SN-350 | SN-600 | SN-1200 | |||
| 1 | Density, at 20oC,g/cm3, not more than | 870 | 880 | 890 | 900 | 905 | |
| 2 | Refraction coefficient at 20oC | не нормируется, определение обязательно | |||||
| 3 | Kinematic viscosity at 100 oC, sSt, within | 2,5-3,5 | 4,5-6,0 | 8,0-9,5 | 11,5-13,5 | 18,0-23,0 | |
| 4 | Pour point, oC, not higher than | -12 | -12 | -12 | -9 | -9 | |
| 5 | Flash point, oC, not less than | 170 | 205 | 220 | 225 | 250 | |
| 6 | Viscosity index, not less than | 95 | 95 | 95 | 95 | 90 | |
| 7 | Color by ЦНТ, max | 0,5 | 0,5 | 1,0 | 2,0 | 3,0 | |
| Color by ASTM, max | - | - | 1,0 | 2,0 | 3,0 | ||
| Color by conditional units of КНС, not more than | 0,5 | 0,5 | - | - | - | ||
| 8 | Mass portion of sulfur,%, not more than | 0,03 | |||||
| 9 | Acidity number, mg KOH by 1g oil, not more than | 0,02 | 0,03 | 0,05 | 0,05 | 0,06 | |
| 10 | Ash,%, not more than | 0,005 | |||||
| 11 | Mass portion of mechanical impurities,%, not less than | 0,005 | |||||
| The calcinated petroleum coke | ||||
|---|---|---|---|---|
| № | Description of index | Figure | ||
| A | B | |||
| 1 | Mass portion of the total moisture, %, not more than | 0,5 | 0,5 | |
| 2 | Ash content, %, not more than | 0,7 | 0,6 | |
| 3 | Mass portion of sulfur, in %, not more than | 1,0 | 0,8 | |
| 4 | Real density, g/ sm3 | 2,01 - 2,06 | 2,06 - 2,08 | |
| 5 | Mass portion of coke with the size of pieces more than 6 mm, %, not less than | 30,0 | 30,0 | |
| 6 | Mass portion of oiled product | - | 0,5 | |
Note:
1. The mass portion of the total moisture is not to rejection indicators at shipment in open semicars and serves for calculation with the consumer.
2. The position № 6 is not rejection. Its share exceeding the established norm is not subject to payment.
| Diesel oil fror little sulfurous crude oil | ||
|---|---|---|
| № | Description of index | Figure |
| 1 | Cetane number, not less than | 45 |
| 2 | Fraction composition: | |
| - 50% 0C, not more than | 290 | |
| - 96% 0C, not more than | 360 | |
| 3 | Kinematic viscosity 200С, mm2/s, (sSt) | 3,0-6,0 |
| 4 | Pour point, 0С, not more than | -10 |
| 5 | Cloud point, 0С, not more than | -5 |
| 6 | Flash point in close cup, 0С, not less than | |
| - for diesel locomotive and ship engines and gas turbines | 62 | |
| - for diesels of the general-purpose | 50 | |
| - for diesels of the general-purpose | 40 | |
| 7 | Mass portion of sulfur, %, not more than | 0,2 |
| 8 | Mass portion of mercaptane sulfur, %, not more than | 0,008 |
| 9 | Mass portion of hydrogen sulfide | Отсутствие |
| 10 | Copper plate testing | Выдерживает |
| 11 | Presence of acids and bases, soluble in water | Отсутствие |
| 12 | Actual resin concentration, mg 100 sm3 fuel, not more than | 40 |
| 13 | Acidity, mg KOH by 100 sm3, not more than | 10 |
| 14 | Iodine number, mg I2 for 100g, not more than | 6 |
| 15 | Ash contents, % weight, not more than | 0,005 |
| 16 | Carbon residue of 10% remainder %, not more than | 0,25 |
| 17 | Filtering factor, not more than | 3,0 |
| 18 | Presence of mechanical impurities | Отсутствие |
| 19 | Presence of water | Отсутствие |
| 20 | Density 200С, kg/m3, not more than | 860 |
Note: <
1. From 1 March before 1 November production and using fuel allowed with pour point not above 0 0C (without determination of the cloud point) and contents of water not more “traces”.
2. Factor on points 1, 7, 8, 9, 15 are defined seasonally, once at 10 days.
| Fuel for reactive engines | ||
|---|---|---|
| № | Description of index | Figure |
| 1 | Density 200 C , kg/m3 | 775 |
| 2 | Fraction composition: | |
| Initial boiling point.0C . not more than | 150 | |
| 10% ,0 C,not more than | 165 | |
| 50%0 ,0 C,not more than | 195 | |
| 90%0 ,C,not more than | 230 | |
| 98 %0 ,C,not more than | 250 | |
| 3 | Kinematic viscosity | |
| 200C mm 2/s ( sST) not less than | 1,25 | |
| 400C mm 2/s ( sST) | 8 | |
| 4 | Lower heat of combustion, not less than k Dž/kg | 42900 |
| 5 | Height of nonsmoke flame, mm | 25 |
| 6 | Acidity, mg KOH by 100sm3 ,not more than | 0,7 |
| 7 | Iodine number,mg KOH by 100g not more than | 3,5 |
| 8 | Flash point in close cup,0 C, not less than | 28 |
| 9 | Теmperature of crystallizations beginning 0C | -50 |
| 10 | Thermo tart stability in steady-state condition under 1500 C (sediment concentration) mg by 100sm3 fuel, not more than | 18 |
| 11 | Mass portion of aromatic hydrocarbons, % , not more than | 22 |
| 12 | Actual resin concentration.mg 100sm3 fuel, not more than | 5,0 |
| 13 | Mass portion of total sulfur. %, not more than | 0,25 |
| 14 | Mass portion of mercaptane sulfur, %. not more than | 0,005 |
| 15 | Mass portion of hydrogen sulfide | no |
| 16 | Copper plate testing (1000 C at 3 hour) | ok |
| 17 | Ash contents. %, not more than | 0,003 |
| 18 | Presence of acids and bases.soluble in water | no |
| 19 | Contents soap of the naften acids | no |
| 20 | Presence of mechanical impurities and water | no |
| 21 | Interaction with water, ball, not more than condition to surfaces of the section condition of the separate phases | 1 |
Note: for fuel TC-1, used for all climatic zones, with the exclusion of zones 1, is allowed temperature of crystallizations beginning not above-50oC
| Home stowed fuel | ||
|---|---|---|
| № | Description of index | Figure |
| 1 | Fraction composition: | |
| -10% 0C not less than | 160 | |
| - 90% 0C not more than | 360 | |
| 2 | Kinematic viscosity 200С, mm3/s, not more than | 8,0 |
| 3 | Pour point, 0С, not more than: | |
| - from 1 September before 1 April | -15 | |
| - from 1 April before 1 September | -5 | |
| 4 | Flash point in close cup, 0С, not less than | 45 |
| 5 | Mass portion of sulfur, %, not more than | 0,5 |
| 6 | Mass portion of hydrogen silfide | no |
| 7 | Copper plate testing | ok |
| 8 | Presence of acids and bases, soluble in water | no |
| 9 | Ash contents, %, not more than | 0,02 |
| 10 | Carbon residue of 10% remainder, %, not more | 0,35 |
| 11 | Presence water | trace |
| 12 | Presence of mechanical impurities | no |
| 13 | Color | From light-drown before black |
| 14 | Density 200С, kg/m3 | No standard, determination necessary |
Note:
1. The factor density is defined for goods-transportation
2. In fuel, delivered population in trade retail, are fixed factors quality: -90 % – not more than 360 0C -kinematic viscosity 20 0C not more than 6 mm2/s (sSt)
3. In consulation with consumer is allowed at March, September, October and November production fuel stove home with pour point not above minus 5, under minimum temperature of the air on place of the using, not below 5
| Hydrotreated Diesel fuel | ||
|---|---|---|
| № | Description of index | Figure |
| 1 | Mass portion of sulfur,ppm,not more than | 0,01(100) |
| 2 | Cetane index, not less than | 50 |
| 3 | Fraction composition: | |
| 95%- ºС, not more than: | 340 | |
| 4 | Presence of water, ppm, not more than | 200 |
| 5 | Pour point, ºС, no more than | -30 |
| 6 | Color, not more than -by ASTM -by SNT | 2.0 |
| 7 | Flash point in close cup, ºС, not less than | 62 |
| 8 | Density 15 ºС, kg/m3 not more than | 840 |
| 9 | Mass portion of poly aromatics, %, not more than | 11 |
| 10 | Mass portion of nitrogen, ppm, not more than | 30 |
| 11 | Copper plate testing | Ok |
| 12 | Filtering factor, not more than | 3.0 |
| 13 | Kinematik viscosity 20 ºС mm2/s (sST) | No |
| 14 | Ash contents, % weight, not more than | 0.25 |
| 15 | Carbon residue of 10 % remainder, %, not more than | 0.005 |
| Kerosine lighting “ko-20” brand | ||
|---|---|---|
| № | Description of index | Figure |
| 1 | Density 200С, kg/m3, not less than | 830 |
| 2 | Fraction composition: | |
| - boiled before 270 0C, %, not less more | 80 | |
| - 98%, 0C, not more than | 310 | |
| 3 | Color, by KHC, not more than | 15 |
| 4 | Height of nonsmoker flame, mm | 20 |
| 5 | Flash point in close cup, 0С, not less than | 40 |
| 6 | Cloud point, 0C, not more than | - 12 |
| 7 | Acidity, mg KOH by 100 sm3, not more than | 1,3 |
| 8 | Ash contents, %, not more than | 0,005 |
| 9 | Mass portion sulfur, %, not more than | 0,1 |
| 10 | Mass portion sulfur, %, not more than | ok |
| 11 | Presence of acids and bases, soluble in water | no |
| 12 | Presence of mechanical impurities and water | no |
| Light gas oil of catalitic crecking | ||
|---|---|---|
| № | Наименование показателей | Норма |
| 1 | Fraction Composition: | |
| - 50% is distilled at temperature, 0С not higher than | 280 | |
| - 96% is distilled at temperature, 0С not higher than | 360 | |
| 2 | Kinematics viscosity, 20°C mm2/s (sSt) | 6,0 |
| 3 | Pour Point, 0 С, not higher than | - 10 |
| 4 | Flash point in close cup, °C, not less than | 62 |
| 5 | Mass portion of sulfur, in %, not more than | 0,35 |
| 6 | Mass portion of mercaptane sulfur, in %, not more than | 0,008 |
| 7 | Hydrogen sulfide content | Отсутствует |
| 8 | Copper plate testing | Выдерживает |
| 9 | Water Soluble Acids and Alkalides | Отсутствует |
| 10 | Ash content, % not more than | 0,005 |
| 11 | Presence of mechanical impurities | Отсутствует |
| 12 | Water Content | Отсутствует |
| 13 | Density 20 0 C, kg/m3, not higher than | 915 |
| 14 | Carbon residue of 10% remainder, %, not more than | 0,25 |
| Petroleum total coke for graphite production | ||
|---|---|---|
| № | Description of Index | Figure |
| 1 | Mass portion of the total moisture,%,not more than | 3,0 |
| 2 | Ash content,%, not more than | 0,6 |
| 3 | Mass portion of sulfur,in%, not more than | 0,6 |
| 4 | Mass portion of flying substances,%,not more than | 11,0 |
| 5 | Real density after warming up at 1300oC in a current of 5 hours,g/sm3, not less than | 2,08 |
| 6 | Mass portion of coke with the size of pieces not less than 8 mm,%, not more than | 60 |
Note: The position №1 is not rejection and defined for calculation with consumer
| Technical kerosine KТ-2 | ||
|---|---|---|
| № | Description of index | Figure |
| 1 | Fraction composition: | |
| - 10%, 0C | 110-180 | |
| - 50%, 0C, not less than | 190 | |
| - 90%, 0C | 240-275 | |
| - 98%, 0C, not more than | 300 | |
| 2 | Acidity, mg KOH by 100 sm3, not more than | 4,5 |
| 3 | Ash contents, %, not more than | 0,005 |
| 4 | Actual resin concentration, mg 100 sm3 kerosine, not more than | 40 |
| 5 | Mass portion sulfur, %, not more than | 1,0 |
| 6 | Copper plate testing | Выдерживает |
| 7 | Presence of acids and bases, soluble in water | Отсутствие |
| 8 | Presence of mechanical impurities | Отсутствие |
| 9 | Presence of water | Отсутствие |
| 10 | Flash point in close cup, 0С, not less than | 28 |
| 11 | Density 200С, kg/m3, not less than | 825 |
| Viscous petroleum bitumen | |||
|---|---|---|---|
| № | Description of index | Figures for grades | |
| BND 60/90 | BND 40/60 | ||
| 1 | The depth of needle penetration 0,1mm, not less than | ||
| at 25 oC | 61-90 | 40-60 | |
| at 0 oC | 20 | 13 | |
| 2 | Melting point by ring in sphere, 0C; not less than | 47 | 51 |
| 3 | Extensibility, sm, not less than | ||
| at 25 oC | 55 | 45 | |
| at 0 oC | 3,5 | - | |
| 4 | Fragility temperature, oC, not higher than | -15 | -12 |
| 5 | Changes of the softening temperature after heating up, oC, not more than | 5 | 5 |
| 6 | Flash point, oC, not less than | 230 | 230 |
| 7 | Mass portion of water-soluble compounds, %, not more | 0,30 | 0,30 |
| 8 | Penetration index | -1,0 до +1,0 | -1,0 до +1,0 |
| Unleaded car benzene | ||||
|---|---|---|---|---|
| № | Description of index | Figure for mark | ||
| А-80 | А-92 | А-95 | ||
| 1 | Octane number. not less than | |||
| - By motor method | 76,0 | 82,5 | 85,0 | |
| - By researcher method | 80,0 | 92,0 | 95,0 | |
| 2 | Actual resin concentration.mg 100sm3benzine not more than | 5,0 | 5,0 | 5,0 |
| 3 | Induction period.min. not less than: | 360 | 360 | 360 |
| 4 | Mass portion of sulfur, % not more than | 0,1 | 0,05 | 0,05 |
| 5 | Copper plate testing | Выдерживает | ||
| 6 | Color | От бесцветного до желтого | ||
| 7 | Density 200C. kg|m3 | Не нормируется, определение обязательно |
||
| 8 | Saturated vapor pressure, kPa | 35-70 | ||
| 9 | Fraction composition : | |||
| - initial boiling point, 0C, not less than: | 35 | 35 | 35 | |
| Пределы перегонки, 0С, не выше: | ||||
| - 10%-summer time | 80 | 80 | 80 | |
| - 10%-winter time | 75 | 75 | 75 | |
| - 50% | 120 | 120 | 120 | |
| - 90% | 190 | 190 | 190 | |
| - Final boiling point, oC, not more than: | 215 | 215 | 215 | |
| - Mass portion of residue in flask, %, (vol), not more than | 2 | 2 | 2 | |
| - Losses, %,(vol.), not more than | 4 | 4 | 4 | |
| 10 | Vapor stopper index, not more than | |||
| - summer time | 950 | 950 | 950 | |
| - winter time | 1250 | 1250 | 1250 | |
| 11 | Acidity , mg KOH by 100 sm3, not more than | 3,0 | 3,0 | 3,0 |
| 12 | Mass portion of merkaptan sulfur, % not more than | 0,001 | 0,001 | |
| 13 | Presence of acids and bases, soluble in water | Отсутствие | ||
| 14 | Presence of acids and bases, soluble in water | Отсутствие | ||
Note:
1. Car benzene intended for long keeping (5 years) in Gosrezerve and Ministry of defense, must have a period to inductions not less 1200 min.
2. Summer time- from 1 April before 1 October Winter time- from 1 October before 1 April
| Liquetied hydrocarbon gases fuel for household consumption | ||||
|---|---|---|---|---|
| № | Description of Index | Figure | ||
| ТР | ТВРМ | ТВ | ||
| 1 | Mass portion of components, %: | |||
| - Methane, ethane and ethylene sum | No standard | |||
| - Propane, and propylene sum, not less than | 75 | No standard | ||
| - Butane and butylene sum not more than | No standard | - | 60 | |
| - Butane and butylene sum not less than | No standard | 60 | - | |
| 2 | Volume portion of the liquid rest at 200C, %, not more than | 0,7 | 1,6 | 1,8 |
| 3 | Excess pressure of saturated vapors, MPa at | 360 | ||
| +450C, not more than | 1,6 | 1,6 | 1,6 | |
| -200C, not less than | 0,16 | - | - | |
| 4 | Mass portion of hydrogen sulfide and mercaptan sulfur, %, not more than | 0,013 | 0,013 | 0,013 |
| Including hydrogen sulfide, not more than | 0,003 | 0,003 | 0,003 | |
| 5 | The content of free water and alkali | No | ||
| Turkmenplen (polypropylen) | ||||
|---|---|---|---|---|
| № | Description of Index | Figure | ||
| TPP D30 S | TPP F 79 FB | TPP D 382 BF | ||
| 1 | Volume speed of fluidity, g/10 min | 2,7-3,7 | 10-15 | 2,7-3,7 |
| 2 | Index of polymeric granules turning yellow, not more than | 2 | 2 | 2 |
| 3 | Dimension of granules, ps/g | 40-60 | 40-60 | 40-60 |
| 4 | Uniformity of granules,%, not more than | 50 | 50 | 50 |
| 5 | The elasticity module at a bend, N/mm2, not less than | 1300 | 1450 | 1300 |
| 6 | Strength at a stretching in a fluidity limit, N/mm2, not less than | 30 | 31 | 30 |
| 7 | Relative lengthening at a stretching in a fluidity limit, %, not less than | 11 | 12 | 11 |
| 8 | Shock durabilityby Изоду (with a cut at 23°C), kDj/m2 | 4,5 | 2,5 | 4,5 |
| 9 | Softening temperature by Vick (10N),°C, not less than | 145 | 150 | - |
| 10 | Temperature of admissible deformation at 0,46 MPa, °C, not less than | 110 | 130 | - |
| 11 | Thermooxidizing stability at 150°C (in the environment of air), hour, not less than | 360 | 120 | 360 |
| 12 | Definition of number and the sizes of gels in polyolefines, not more than | |||
| - Defects >0,2 mm | - | - | 500 | |
| - Defects 0,7-1,5 mm | - | - | 50 | |
| - Defects 1,5-2,5 mm | - | - | 10 | |
| - Defects > 2,5 mm | - | - | 0 | |
| 13 | Turbidity polyolefine plates and films | - | - | Не нормируется, определение обязательно |
Note: Thermooxidizing stability at 150°C (in the environment of air) defines once at 10 days.
| Technical sulfur | ||||||
|---|---|---|---|---|---|---|
| № | Description of index | Figure | ||||
| 9998 | 9995 | 9990 | 9950 | 9920 | ||
| 1 | Mass portion of sulfur,% not less than | 99,98 | 99,95 | 99,90 | 99,50 | 99,20 |
| 2 | Mass portion of ash,% not less than | 0,02 | 0,03 | 0,05 | 0,2 | 0,4 |
| 3 | Mass portion of organic compounds,%, not more than | 0,01 | 0,03 | 0,06 | 0,25 | 0,5 |
| 4 | Mass portion of acids converted to sulfuric acid, %, max | 0,0015 | 0,003 | 0,004 | 0,01 | 0,02 |
| 5 | Mass portion of water,%, not more than | 0,2 | 0,2 | 0,2 | 0,2 | 1,0 |
| 6 | Presence of mechanical impurities(paper, wood pieces, sand) | No | ||||
Note: Standard values for items 1-4 are converty to the dry basis substance
