| DATE | HS_CODE | Product Description | Trademark | Country | Net Weight | Statistical Cost | Place | Shipper Name | Consignee Name |
|---|
| 2017-08-01 | 2710121101 | LIGHT DISTILLATES AND PRODUCTS. Stable natural gasoline (NAFTA) is used for specific processes (cracking). . 90 vol% or more distilled at 210 C METHOD ASTM D 86, pentane-hexane fraction with pentane content not less than: 35 MAC | *** | RUSSIA | 4715985 | 2182322,06 | *** | ***** | ***** |
| 2017-08-01 | 2710121109 | Light distillates and other products. Stable natural gasoline (NAFTA) is used for specific processes (cracking). . 90 vol% or more distilled at 210 C METHOD ASTM D 86, C pentane UNKNOWN% by weight and hexane: NEIZVES | *** | RUSSIA | 4715985 | 2182322,06 | *** | ***** | ***** |
| 2017-08-01 | 2710121101 | LIGHT DISTILLATES AND PRODUCTS. Stable natural gasoline (NAFTA) is used for specific processes (cracking). . 90 vol% or more distilled at 210 C METHOD ASTM D 86, pentane-hexane fraction with pentane content not less than: 35 MAC | *** | RUSSIA | 282225 | 130599,62 | *** | ***** | ***** |
| 2017-08-01 | 2710121109 | Light distillates and other products. Stable natural gasoline (NAFTA) is used for specific processes (cracking). . 90 vol% or more distilled at 210 C METHOD ASTM D 86, C pentane UNKNOWN% by weight and hexane: NEIZVES | *** | RUSSIA | 282225 | 130599,62 | *** | ***** | ***** |
| 2017-08-01 | 2710121109 | Light distillates and products for specific processes, OTHER: NAFTA coking stations 00151638-006-2015 at a temperature of 210 C is distilled to 100 vol% (by the method ASTM D86), QUANTITY - 1588,150 T:. Pentane (C5): 5.25 MAC .%, hexane | *** | RUSSIA | 1588150 | 457276,03 | *** | ***** | ***** |
| 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 | 2710129008 | OTHER light distillates, 90% or more which was distilled to a temperature of 210 degrees C. METHOD ASTM D 86, stable gas gasoline (obtained from bituminous), the mass fraction of n-pentane,% - not standardized; WEIGHT CONTENT n-hexane,% - NO: normalizing; | *** | RUSSIA | 2500000 | 977576,84 | *** | ***** | ***** |
| 2017-08-02 | 2710121101 | LIGHT DISTILLATES FOR specific processes (reforming, pyrolysis), pentane-hexane fraction with pentane (C5) not less than 35 wt.%, And hexane (C6) at least 55 wt.%, NAFTA coker was distilled to 90% v or more ON . LOSS: up to 2 | *** | RUSSIA | 5000000 | 1510250 | *** | ***** | ***** |
| 2017-08-02 | 2710121109 | DISTILLATES FOR LIGHT specific processes (reforming, pyrolysis) OTHER C pentane (C5) less than 35 wt.%, And hexane (C6) is less than 55 wt.%, NAFTA coker was distilled to 90% v or more ON. Losses to 210 degrees C METHOD: ASTM | *** | RUSSIA | 5000000 | 1510250 | *** | ***** | ***** |
| 2017-08-02 | 2710129008 | OTHER light distillates, gasoline, straight run (NAFTA): 90% OR MORE OF distilled to a temperature of 210 degrees C, the percentage distilled at 210 degrees C is not determined (by the method ASTM D 86), pentane (C5) less than 35 wt. .%, and hexane (C6) M: EH | *** | RUSSIA | 3525017 | 1556295,01 | *** | ***** | ***** |