| DATE | HS_CODE | Product Description | Trademark | Country | Net Weight | Statistical Cost | Place | Shipper Name | Consignee Name |
|---|
| 2017-08-01 | 2710122509 | NAFTA LIGHT, -Contents pentane (C5) is not defined -Contents hexane (C6) is less than 55 wt% of n-hexane-content less than 55% by weight -PROTSENT distillation at 210 ° C (METHOD ASTM D86) greater than 90%.. - Initial boiling point (° C) not lower than 27 -TEMPERA: TU | *** | RUSSIA | 36000000 | 15102029,33 | *** | ***** | ***** |
| 2017-08-04 | 2710122509 | NAFTA HEAVY, -Contents pentane (C5) less than 35 wt.% -Contents hexane (C6) is less than 55 wt.% N-hexane-content of less than 55 MAC.% -PROTSENT distillation at 210 ° C (ASTM D86 METHOD FOR) MORE 90% of the initial boiling point is the temperature (° C) not lower than 60 -TEMPE: RA | *** | RUSSIA | 63000000 | 26539116 | *** | ***** | ***** |
| 2017-08-04 | 2710122509 | NAFTA HEAVY, -Contents pentane (C5) less than 35 wt.% -Contents hexane (C6) is less than 55 wt.% N-hexane-content of less than 55 MAC.% -PROTSENT distillation at 210 ° C (ASTM D86 METHOD FOR) MORE 90% of the initial boiling point is the temperature (° C) not lower than 60 -TEMPE: RA | *** | RUSSIA | 31500000 | 13269558 | *** | ***** | ***** |
| 2017-08-04 | 2710122509 | OTHER LIGHT DISTILLATES; Stable natural gasoline BT, 90% or more of which (including loss), distilled to a temperature of 210 degrees C (METHOD ASTM D86), WITHOUT ANY OTHER special gasoline antiknock additives, C pentane (C5) is less than 35 M | *** | RUSSIA | 1100000 | 501325 | *** | ***** | ***** |
| 2017-08-07 | 2710122509 | Petroleum ether (straight run gasoline), a mixture of light aliphatic hydrocarbons (pentane and hexane), was prepared from the associated petroleum gas and light oil, a colorless transparent liquid without precipitation, density at 20 ° C -0.658G / cm3. APPLY PETER | *** | UKRAINE | 3.5 | 30,75 | *** | ***** | ***** |
| 2017-08-08 | 2710122509 | NAFTA LIGHT, -Contents pentane (C5) is not defined -Contents hexane (C6) is less than 55 wt% of n-hexane-content less than 55% by weight -PROTSENT distillation at 210 ° C (METHOD ASTM D86) greater than 90%.. - Initial boiling point (° C) not lower than 27 -TEMPERA: TU | *** | RUSSIA | 38000000 | 16159324,31 | *** | ***** | ***** |
| 2017-08-09 | 2710122509 | NAFTA HEAVY, -Contents pentane (C5) less than 35 wt.% -Contents hexane (C6) is less than 55 wt.% N-hexane-content of less than 55 MAC.% -PROTSENT distillation at 210 ° C (ASTM D86 METHOD FOR) MORE 90% of the initial boiling point is the temperature (° C) not lower than 60 -TEMPE: RA | *** | RUSSIA | 41000000 | 16994322,85 | *** | ***** | ***** |
| 2017-08-16 | 2710122509 | NAFTA LIGHT, -Contents pentane (C5) is not defined -Contents hexane (C6) is less than 55 wt% of n-hexane-content less than 55% by weight -PROTSENT distillation at 210 ° C (METHOD ASTM D86) greater than 90%.. - Initial boiling point (° C) not lower than 27 -TEMPERA: TU | *** | RUSSIA | 36000000 | 14895101,68 | *** | ***** | ***** |
| 2017-08-18 | 2710122509 | NAFTA LIGHT, -Contents pentane (C5) 37.51 MSS.% -Contents hexane (C6), 20.51 MSS.% N-hexane -Contents 8.77 MSS.% -PROTSENT distillation at 210 ° C (ASTM METHOD D86) is not determined -Exit (METHOD ASTM D86) 98,0% by volume is the temperature START:. AL | *** | RUSSIA | 37075491 | 15675680,43 | *** | ***** | ***** |
| 2017-08-18 | 2710122509 | NAFTA LIGHT, -Contents pentane (C5) 36.82 MSS.% -Contents hexane (C6), 20.41 MSS.% N-hexane -Contents 8.76 MSS.% -PROTSENT distillation at 210 ° C (ASTM METHOD D86) is not determined -Exit (METHOD ASTM D86) 98,0% by volume is the temperature START:. AL | *** | RUSSIA | 4092282 | 1827655,22 | *** | ***** | ***** |