DATE | HS_CODE | Product Description | Trademark | Country | Net Weight | Statistical Cost | Place | Shipper Name | Consignee Name |
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2017-11-02 | 2710194290 | GAS OIL WITH sulfur content below 0.05 wt%, -PROTSENT DISTILLATION OTHER OIL TEMPERATURE 250 ° C.; (According to ISO 3405 method equivalent to method ASTM D86) of less than 65% vol.; -PROTSENT DISTILLATION OIL TEMPERATURE 350 ° C (ISO 34 METHOD FOR | ABSENT | *** | 13000000 | 6616963,21 | Ust Luga | ***** | ***** |
2017-11-03 | 2710192100 | FUEL FOR turbojet TYPE kerosene JET A-1, -PROTSENT DISTILLATION OIL TEMPERATURE 210 ° C (ISO METHOD 3405, equivalent method ASTM D86) of less than 90 vol.% -PROTSENT DISTILLATION OIL TEMPERATURE 250 ° C | ABSENT | KINGDOM OF DENMARK | 30000000 | 17224476,86 | Ust Luga | ***** | ***** |
2017-11-10 | 2710192100 | FUEL FOR turbojet TYPE kerosene JET A-1, -PROTSENT DISTILLATION OIL TEMPERATURE 210 ° C (ISO METHOD 3405, equivalent method ASTM D86) of less than 90 vol.% -PROTSENT DISTILLATION OIL TEMPERATURE 250 ° C | ABSENT | FINLAND | 22500000 | 13376187,91 | Ust Luga | ***** | ***** |
2017-11-15 | 2710192100 | FUEL FOR turbojet TYPE kerosene JET A-1, -PROTSENT DISTILLATION OIL TEMPERATURE 210 ° C (ISO METHOD 3405, equivalent method ASTM D86) of less than 90 vol.% -PROTSENT DISTILLATION OIL TEMPERATURE 250 ° C | ABSENT | SWEDEN | 13000000 | 7715510,63 | Ust Luga | ***** | ***** |
2017-11-16 | 2710192100 | FUEL FOR turbojet TYPE kerosene JET A-1, -PROTSENT DISTILLATION OIL TEMPERATURE 210 ° C (ISO METHOD 3405, equivalent method ASTM D86) of less than 90 vol.% -PROTSENT DISTILLATION OIL TEMPERATURE 250 ° C | ABSENT | FINLAND | 11500000 | 6638417,59 | Ust Luga | ***** | ***** |
2017-11-20 | 2710194290 | GAS OIL WITH sulfur content below 0.05 wt.%, -PROTSENT DISTILLATION OTHER OIL TEMPERATURE 250 ° C (ISO METHOD 3405, equivalent method ASTM D86) of less than 65 vol.% -PROTSENT DISTILLATION OIL TEMPERATURE 350 ° C ( METHOD ISO 3405 | ABSENT | *** | 16500000 | 8720264,97 | Ust Luga | ***** | ***** |
2017-11-24 | 2710194290 | GAS OIL WITH sulfur content below 0.05 wt.%, -PROTSENT DISTILLATION OTHER OIL TEMPERATURE 250 ° C (ISO METHOD 3405, equivalent method ASTM D86) of less than 65 vol.% -PROTSENT DISTILLATION OIL TEMPERATURE 350 ° C ( METHOD ISO 3405 | ABSENT | *** | 12500000 | 6603107,8 | Ust Luga | ***** | ***** |
2017-11-28 | 2710192100 | FUEL FOR turbojet TYPE kerosene JET A-1, -PROTSENT DISTILLATION OIL TEMPERATURE 210 ° C (ISO METHOD 3405, equivalent method ASTM D86) 74,5 vol.% -PROTSENT DISTILLATION OIL TEMPERATURE 250 ° C (PO | ABSENT | KINGDOM OF DENMARK | 19364600 | 10425477,1 | Ust Luga | ***** | ***** |
2017-11-28 | 2710194290 | GAS OIL OTHER -mass fraction of total sulfur 0.0217 wt% -PROTSENT DISTILLATION OIL TEMPERATURE 250 ° C (ISO METHOD 3405, equivalent method ASTM D86) 16,0 vol.% -PROTSENT DISTILLATION OIL TEMPERATURE 350 ° C (PO METHOD ISO 3405, EC | ABSENT | NORWAY | 21944870 | 11197828,45 | Ust Luga | ***** | ***** |
2017-11-30 | 2710194290 | GAS OIL OTHER -mass fraction of total sulfur 0.0231 wt% -PROTSENT DISTILLATION OIL TEMPERATURE 250 ° C (ISO METHOD 3405, equivalent method ASTM D86) 13,0 vol.% -PROTSENT DISTILLATION OIL TEMPERATURE 350 ° C (PO METHOD ISO 3405, EC | ABSENT | KINGDOM OF DENMARK | 21945137 | 10747538,66 | Ust Luga | ***** | ***** |