| 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 | *** | ***** | ***** |
| 2017-08-01 | 2710122509 | LIGHT DISTILLATES SPECIAL Other gasoline, 90% or more which was distilled to a temperature of 210 degrees C. METHOD ASTM D 86 (equivalent method ISO 3405), antiknock additives WITHOUT AND WITH AT temperature difference that surpass 5% AND 90 ON:. ON. | *** | RUSSIA | 2500000 | 977576,84 | *** | ***** | ***** |
| 2017-08-03 | 2710122509 | OTHER LIGHT DISTILLATES; Stable natural gasoline, 90% or more of which (including losses) is distilled to a temperature of 210 degrees C (METHOD ASTM D86), OTHER SPECIAL-free petrol antiknock additives, CONTAINING hexane (C6) of less than 55: MAC. | *** | RUSSIA | 10000000 | 4592500 | *** | ***** | ***** |
| 2017-08-04 | 2710122509 | LIGHT DISTILLATES AND PRODUCTS OF 90% or more which was distilled to 210 ° C (ASTM D 86 software method), special gasoline, OTHER:. Cat-cracked gasoline (CCL), in an amount 3750T. | *** | RUSSIA | 3750000 | 1915312,5 | *** | ***** | ***** |
| 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 | *** | ***** | ***** |
| 2017-08-08 | 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 | *** | ***** | ***** |
| 2017-08-09 | 2710122509 | Light distillates, OTHER - WHITE SPIRIT T-TU 0251-001-71162433-2011 initial boiling point of 58.0 degrees C, 90% distilled at 73.0 degrees C (METHOD ASTM D86), the density at 15 degrees C 732 CG / M3, the content of n-hexane (C6) is not standardized, SODERZHANIEPENT | *** | RUSSIA | 5824.42 | 4922,3 | *** | ***** | ***** |