DATE | HS_CODE | Product Description | Trademark | Country | Net Weight | Statistical Cost | Place | Shipper Name | Consignee Name |
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2017-11-01 | 2710196601 | PERFORMANCE The stores liquid fuel, away, fuel for bunkering mass fraction SULFUR more than 2% but not more than 2.8%, is distilled at 250 GRAD.TSELS. LESS THAN 65% METHOD ASTM D 86, was distilled at 350 GRAD.TSELS. LESS THAN 85% METHOD ASTM D | ABSENT | *** | 1300000 | 286000 | Ust Luga | ***** | ***** |
2017-11-02 | 2710196601 | LIQUID FUEL, FUEL OIL FOR OTHER TSELEY.EKSPLUATATSIONNYE supplies (bunkering). With a sulfur content exceeding 2 wt.% But not more than 2.8 mass.%. LESS THAN 65% OF PEREGON.PRI 250C, less than 85 vol.% 350C IN METHOD ASTM D86, initial boiling point of 200C or BOLEEP | WITHOUT A TRADEMARK | *** | 1100000 | 279400 | Ust Luga | ***** | ***** |
2017-11-02 | 2710196601 | .. Heavy distillates, LIQUID FUEL FOR OTHER PURPOSES, fuel oil with a sulfur content over 2.0% by weight but not more than 2.8% by weight distilled: at 250 ° C - less than 65% by volume, at 350 ° C - less than 85 ON.. % (METHOD ASTM D 86). | *** | *** | 8666000 | 2807784 | 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 | 2710196601 | .. Heavy distillates, LIQUID FUEL FOR OTHER PURPOSES, fuel oil with a sulfur content over 2.0% by weight but not more than 2.8% by weight distilled: at 250 ° C - less than 65% by volume, at 350 ° C - less than 85 ON.. % (METHOD ASTM D 86). | *** | *** | 8666000 | 2822949,5 | Ust Luga | ***** | ***** |
2017-11-03 | 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 | *** | 1000000 | 250000 | Ust Luga | ***** | ***** |
2017-11-04 | 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 | *** | 1550000 | 389484 | Ust Luga | ***** | ***** |
2017-11-07 | 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, OF LESS THAN 65% distils at 250 ° C, less than 85% vol -.. At 350 ° C METHOD ASTM D86, fractional composition NOT MORE | *** | *** | 3875000 | 1774750 | Ust Luga | ***** | ***** |
2017-11-08 | 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 | *** | 540000 | 162000 | Ust Luga | ***** | ***** |
2017-11-10 | 2710196601 | LIQUID FUEL FOR OTHER PURPOSES WITH SULFUR CONTENT OVER 2.0 wt.%, But not more than 2.8 mass.%, Oil. . OIL, OF AT LEAST 65% distilled at 250 ° C, less than 85 vol% -. At 350 ° C. METHOD ASTM D86, amount of kerosene-gas oil fraction were distilled to | *** | *** | 12625000 | 4469250 | Ust Luga | ***** | ***** |