| DATE | HS_CODE | Product Description | Trademark | Country | Net Weight | Statistical Cost | Place | Shipper Name | Consignee Name |
|---|
| 2017-11-09 | 2710196201 | LIQUID FUEL FOR OTHER PURPOSES With a sulfur content of 1.0 wt.% Oil. HEAVY FUEL OIL EXPORT less 65OB% distilled at 250 ° C LESS 85OB% -.. At 350 ° C. METHOD ASTM D86, amount of kerosene-gas oil fraction were distilled | *** | *** | 5875000 | 2189377,5 | Vanina | ***** | ***** |
| 2017-11-09 | 2710196401 | LIQUID FUEL FOR OTHER PURPOSES WITH SULFUR CONTENT OVER 1.0 wt.%, But not more than 2.0 wt.% Oil. HEAVY FUEL OIL EXPORT less 65OB% distilled at 250 ° C LESS 85OB% -.. At 350 ° C. METHOD ASTM D86, amount of kerosene-gas oil | *** | *** | 5875000 | 2189377,5 | Vanina | ***** | ***** |
| 2017-11-09 | 2710196601 | LIQUID FUEL FOR OTHER PURPOSES WITH SULFUR CONTENT OVER 2.0 wt.%, But not more than 2.8 mass.%, Oil. HEAVY FUEL OIL EXPORT less 65OB% distilled at 250 ° C LESS 85OB% -.. At 350 ° C. METHOD ASTM D86, amount of kerosene-gas oil | *** | *** | 5875000 | 2189377,5 | Vanina | ***** | ***** |
| 2017-11-09 | 2710196801 | LIQUID FUEL FOR OTHER PURPOSES WITH SULFUR CONTENT OVER 2.8 MSS.% Oil. HEAVY FUEL OIL EXPORT less 65OB% distilled at 250 ° C LESS 85OB% -.. At 350 ° C. METHOD ASTM D86, amount of kerosene-gas oil fraction were distilled to | *** | *** | 5875000 | 2189377,5 | Vanina | ***** | ***** |
| 2017-11-22 | 2710196201 | LIQUID FUEL FOR OTHER PURPOSES With a sulfur content of 1.0 wt.% Oil. HEAVY FUEL OIL EXPORT less 65OB% distilled at 250 ° C LESS 85OB% -.. At 350 ° C. METHOD ASTM D86, amount of kerosene-gas oil fraction were distilled | *** | *** | 2500000 | 913425 | Vanina | ***** | ***** |
| 2017-11-22 | 2710196401 | LIQUID FUEL FOR OTHER PURPOSES WITH SULFUR CONTENT OVER 1.0 wt.%, But not more than 2.0 wt.% Oil. HEAVY FUEL OIL EXPORT less 65OB% distilled at 250 ° C LESS 85OB% -.. At 350 ° C. METHOD ASTM D86, amount of kerosene-gas oil | *** | *** | 2500000 | 913425 | Vanina | ***** | ***** |
| 2017-11-22 | 2710196601 | LIQUID FUEL FOR OTHER PURPOSES WITH SULFUR CONTENT OVER 2.0 wt.%, But not more than 2.8 mass.%, Oil. HEAVY FUEL OIL EXPORT less 65OB% distilled at 250 ° C LESS 85OB% -.. At 350 ° C. METHOD ASTM D86, amount of kerosene-gas oil | *** | *** | 2500000 | 913425 | Vanina | ***** | ***** |
| 2017-11-22 | 2710196801 | LIQUID FUEL FOR OTHER PURPOSES WITH SULFUR CONTENT OVER 2.8 MSS.% Oil. HEAVY FUEL OIL EXPORT less 65OB% distilled at 250 ° C LESS 85OB% -.. At 350 ° C. METHOD ASTM D86, amount of kerosene-gas oil fraction were distilled to | *** | *** | 2500000 | 913425 | Vanina | ***** | ***** |
| 2017-11-28 | 2710196201 | LIQUID FUEL FOR OTHER PURPOSES With a sulfur content of 1.0 wt.% Oil. HEAVY FUEL OIL EXPORT less 65OB% distilled at 250 ° C LESS 85OB% -.. At 350 ° C. METHOD ASTM D86, amount of kerosene-gas oil fraction were distilled | *** | *** | 4125000 | 1522743,75 | Vanina | ***** | ***** |
| 2017-11-28 | 2710196401 | LIQUID FUEL FOR OTHER PURPOSES WITH SULFUR CONTENT OVER 1.0 wt.%, But not more than 2.0 wt.% Oil. HEAVY FUEL OIL EXPORT less 65OB% distilled at 250 ° C LESS 85OB% -.. At 350 ° C. METHOD ASTM D86, amount of kerosene-gas oil | *** | *** | 4125000 | 1522743,75 | Vanina | ***** | ***** |