| DATE | HS_CODE | Product Description | Trademark | Country | Net Weight | Statistical Cost | Place | Shipper Name | Consignee Name |
|---|
| 2017-08-04 | 2710122501 | LIGHT DISTILLATES AND PRODUCTS 90 vol.% Or more which was distilled to 210 ° C (METHOD ASTM D 86), special gasoline CONTAINING n-hexane not less than 55 MAC.%, But not more than 80 wt.% Initial boiling point not less than 64 ° C and end temperature CI | *** | RUSSIA | 3750000 | 1915312,5 | *** | ***** | ***** |
| 2017-08-21 | 2710122501 | LIGHT DISTILLATES AND PRODUCTS 90 vol.% Or more which was distilled to 210 ° C (METHOD ASTM D 86), special gasoline CONTAINING n-hexane not less than 55 MAC.%, But not more than 80 wt.% Initial boiling point not less than 64 ° C and end temperature CI | *** | *** | 3750000 | 1858125 | *** | ***** | ***** |
| 2017-09-11 | 2710122501 | LIGHT DISTILLATES AND PRODUCTS 90 vol.% Or more which was distilled to 210 ° C (METHOD ASTM D 86), special gasoline CONTAINING n-hexane not less than 55 MAC.%, But not more than 80 wt.% Initial boiling point not less than 64 ° C and end temperature CI | *** | RUSSIA | 3375000 | 1680750 | *** | ***** | ***** |
| 2017-09-11 | 2710122501 | LIGHT DISTILLATES AND PRODUCTS 90 vol.% Or more which was distilled to 210 ° C (METHOD ASTM D 86), special gasoline CONTAINING n-hexane not less than 55 MAC.%, But not more than 80 wt.% Initial boiling point not less than 64 ° C and end temperature CI | *** | RUSSIA | 562500 | 305437,5 | *** | ***** | ***** |
| 2017-09-27 | 2710122501 | LIGHT DISTILLATES AND PRODUCTS 90 vol.% Or more which was distilled to 210 ° C (METHOD ASTM D 86), special gasoline CONTAINING n-hexane not less than 55 MAC.%, But not more than 80 wt.% Initial boiling point not less than 64 ° C and end temperature CI | *** | RUSSIA | 500000 | 261500 | *** | ***** | ***** |
| 2017-09-27 | 2710122501 | LIGHT DISTILLATES AND PRODUCTS 90 vol.% Or more which was distilled to 210 ° C (METHOD ASTM D 86), special gasoline CONTAINING n-hexane not less than 55 MAC.%, But not more than 80 wt.% Initial boiling point not less than 64 ° C and end temperature CI | *** | RUSSIA | 3312500 | 1881500 | *** | ***** | ***** |
| 2017-10-17 | 2710122501 | LIGHT DISTILLATES AND PRODUCTS 90 vol.% Or more which was distilled to 210 ° C (METHOD ASTM D 86), special gasoline CONTAINING n-hexane not less than 55 MAC.%, But not more than 80 wt.% Initial boiling point not less than 64 ° C and end temperature CI | *** | RUSSIA | 3750000 | 2114062,5 | *** | ***** | ***** |
| 2017-10-27 | 2710122501 | LIGHT DISTILLATES AND PRODUCTS 90 vol.% Or more which was distilled to 210 ° C (METHOD ASTM D 86), special gasoline CONTAINING n-hexane not less than 55 MAC.%, But not more than 80 wt.% Initial boiling point not less than 64 ° C and end temperature CI | *** | RUSSIA | 300000 | 125367 | *** | ***** | ***** |
| 2017-11-02 | 2710122501 | LIGHT DISTILLATES AND PRODUCTS 90 vol.% Or more which was distilled to 210 ° C (METHOD ASTM D 86), special gasoline CONTAINING n-hexane not less than 55 MAC.%, But not more than 80 wt.% Initial boiling point not less than 64 ° C and the temperature | *** | SWITZERLAND | 3750000 | 2090625 | *** | ***** | ***** |
| 2017-11-14 | 2710122501 | DISTILLATES AND LIGHT PRODUCTS, 90 OB.% Or more which was distilled to 210 ° C (ASTM D 86 software method) QUALITY products matching SRT 11605031-019-2007 AMENDED AND / OR SRT 11605031-028-2009 AMENDED, SPECIAL GASOLINES CONTAINING H | *** | *** | 2125000 | 1211781,25 | Luga | ***** | ***** |