| DATE | HS_CODE | Product Description | Trademark | Country | Net Weight | Statistical Cost | Place | Shipper Name | Consignee Name |
|---|
| 2017-11-01 | 2710121109 | Light distillates and other products for recycling specific processes INCLUDING reforming: distillate CONDENSATE GAS LIGHT (NAFTA) QUALITY ACCORDING contract specifications (APPENDIX â„– 1); 90 vol.% Or more (inclusive of | *** | KINGDOM OF THE NETHERLANDS | 19250000 | 7700000 | Ust Luga | ***** | ***** |
| 2017-11-01 | 2710121101 | LIGHT DISTILLATES AND PRODUCTS, recyclable specific processes, INCLUDING reforming; . Pentane-hexane fraction with pentane (C5) not less than 35 wt%, and hexane (C6) at least 55 wt.%: Distillate LIGHT GAS CONDENSATE | *** | KINGDOM OF THE NETHERLANDS | 19250000 | 7700000 | Ust Luga | ***** | ***** |
| 2017-11-02 | 2710196401 | LIQUID FUEL, FUEL OIL FOR OTHER PURPOSES. PERFORMANCE supplies (bunkering) .With contains. SULFUR greater than 1 wt.% But not more than 2 wt.%, Less than 65 vol.% Distilled at 250 ° C, less than 85 vol.% 350C IN METHOD ASTM D86, Tempe. Initial boiling point 200C OR WHICH | ABSENT | *** | 800000 | 228000 | Ust Luga | ***** | ***** |
| 2017-11-02 | 2710196601 | LIQUID FUEL, FUEL OIL FOR OTHER PURPOSES. PERFORMANCE supplies (bunkering). C is found. SULFUR more than 2 wt.% But not more than 2.8 MAC.%, Less than 65 vol.% Distilled at 250 ° C, less than 85 vol.% 350C IN METHOD ASTM D86, Tempe. Initial boiling WHICH 200C | ABSENT | *** | 800000 | 228000 | Ust Luga | ***** | ***** |
| 2017-11-02 | 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 with a content of n-hexane at least 55 | *** | *** | 1090000 | 598410 | Ust Luga | ***** | ***** |
| 2017-11-02 | 2710129002 | OTHER LIGHT DISTILLATES; Stable gas gasoline BT, 90% or more of which (including losses) is distilled to a temperature of 210 oC (METHOD ASTM D86), pentane-hexane fraction with pentane (C5) at least 35% by weight and hexane (C6). AT LEAST | *** | *** | 1090000 | 598410 | Ust Luga | ***** | ***** |
| 2017-11-02 | 2710129008 | OTHER LIGHT DISTILLATES; Stable natural gasoline BT, 90% or more of which (including loss), distilled to a temperature of 210 oC (METHOD ASTM D86), C pentane (C5) less than 35 wt%, and hexane (C6) is less than 55 wt.%. . WEIGHT 1085.000 T. | *** | *** | 1085000 | 595665 | Ust Luga | ***** | ***** |
| 2017-11-02 | 2710122509 | OTHER LIGHT DISTILLATES; Stable natural gasoline, 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, CONTAINING AT LEAST n-hexane 55 wt. | *** | *** | 10000000 | 5490000 | Ust Luga | ***** | ***** |
| 2017-11-02 | 2710129002 | OTHER LIGHT DISTILLATES; Stable natural gasoline, 90% or more of which (including losses) is distilled to a temperature of 210 oC (METHOD ASTM D86), pentane-hexane fraction with pentane (C5) at least 35% by weight and hexane (C6) NOT. less than 55 | *** | *** | 10000000 | 5490000 | Ust Luga | ***** | ***** |
| 2017-11-02 | 2710129008 | OTHER LIGHT DISTILLATES; Stable natural gasoline, 90% or more of which (including loss), distilled to a temperature of 210 oC (METHOD ASTM D86), C pentane (C5) less than 35 wt%, and hexane (C6) is less than 55 wt%... WEIGHT 12000 T. | *** | *** | 12000000 | 6588000 | Ust Luga | ***** | ***** |