| DATE | HS_CODE | Product Description | Trademark | Country | Net Weight | Statistical Cost | Place | Shipper Name | Consignee Name |
|---|
| 2017-08-04 | 2710129008 | Stable natural gasoline, is used for dissolution and extraction of organic compounds, as raw material for SECONDARY PROCESS OIL REFINING AND PETROCHEMICAL INDUSTRIES, AS A COMPONENT IN THE PROCESS gasoline blending. TU 0272-001-25408280-: 2015, | *** | RUSSIA | 483015 | 164225,1 | *** | ***** | ***** |
| 2017-08-16 | 2710129008 | Stable natural gasoline, is used for dissolution and extraction of organic compounds, as raw material for SECONDARY PROCESS OIL REFINING AND PETROCHEMICAL INDUSTRIES, AS A COMPONENT IN THE PROCESS gasoline blending. TU 0272-001-25408280-: 2015, | *** | RUSSIA | 486735 | 165489,9 | *** | ***** | ***** |
| 2017-08-18 | 2710129008 | Light distillates, OTHER; 90% of the product is distilled at 142.0 TEMPREATURE OS (METHOD ASTM D 86). BOILING TEMPERATURE END 170 OS, the percentage of processed at a temperature of 210 OC is not defined. : Pentane (C5), 36.52% by weight and hexane (C6), 15.60 M. | *** | RUSSIA | 47267 | 20269,04 | *** | ***** | ***** |
| 2017-08-18 | 2710129008 | Light distillates, OTHER; 90% of the product was distilled under 126,0-145,0 TEMPREATURE OS (METHOD ASTM D 86). TEMPERATURE final boiling 170-178 OS PERCENTAGE processed at a temperature of 210 OC is not defined. : Pentane (C5) 23.24% -36.52% and hexane | *** | RUSSIA | 3928101 | 1684448,27 | *** | ***** | ***** |
| 2017-08-23 | 2710129008 | Stable natural gasoline, is used for dissolution and extraction of organic compounds, as raw material for SECONDARY PROCESS OIL REFINING AND PETROCHEMICAL INDUSTRIES, AS A COMPONENT IN THE PROCESS gasoline blending. TU 0272-001-25408280-: 2015, | *** | *** | 475490 | 161666,6 | *** | ***** | ***** |
| 2017-08-24 | 2710129008 | Light distillates, etc; 90% of the product distils at 147.5, 152.0 degrees C; BOILING TEMPERATURE END 174.0; 175.5 degrees C; PERCENTAGE processed at a temperature of 210 OC can not be determined; : Pentane-hexane fraction with pentane (C5) | *** | *** | 556211 | 206337,59 | *** | ***** | ***** |
| 2017-08-28 | 2710129008 | Light distillates, OTHER; 90% of the product was distilled under TEMPREATURE 144.5; 147.5 OC (METHOD ASTM D 86). BOILING TEMPERATURE END 175.5; 178.5 OS, the percentage of processed at a temperature of 210 OC is not defined. : Pentane (C5), 18.158, 19.265% by weight. | *** | *** | 5272361 | 1985992,95 | *** | ***** | ***** |
| 2017-08-28 | 2710129008 | Light distillates, OTHER; 90% of the product is distilled at 152.0 TEMPREATURE OS (METHOD ASTM D 86). BOILING TEMPERATURE END 174.0 OS, the percentage of processed at a temperature of 210 OC is not defined. : Pentane (C5), 17.351% by weight and hexane (C6), 19.6. | *** | *** | 1251842 | 465021,75 | *** | ***** | ***** |
| 2017-08-28 | 2710129008 | Light distillates, OTHER; 90% of the product is distilled at 154.0 TEMPREATURE OS (METHOD ASTM D 86). BOILING TEMPERATURE END 176.5 OS, the percentage of processed at a temperature of 210 OC is not defined. : Pentane (C5), 17.006% by weight and hexane (C6), 20.0. | *** | *** | 10990786 | 4328281,44 | *** | ***** | ***** |
| 2017-08-28 | 2710129008 | Light distillates, OTHER; 90% of the product was distilled under TEMPREATURE 144.5; 152.0 OC (METHOD ASTM D 86). BOILING TEMPERATURE END 174.0; 178.5 OS, the percentage of processed at a temperature of 210 OC is not defined. : Pentane (C5), 17.351, 18.158% by weight. | *** | *** | 8420908 | 3171987,62 | *** | ***** | ***** |