| DATE | HS_CODE | Product Description | Trademark | Country | Net Weight | Statistical Cost | Place | Shipper Name | Consignee Name |
|---|
| 2017-11-01 | 2710196401 | 100 fuel oil (IFO-380), GOST 10585-2013, FLASH POINT OPEN. CRUCIBLE (ASTM D 92) 214 degrees C, with a sulfur content 1.22% IN BOILING TEMP START ASTM D 86 - 280 degrees C, kinematic viscous at 50 gr.S. - 146 CCT (EN ISO 3104), COLOR. HAR. DARKER 8 | not designated | SINGAPORE | 1680000 | 537600 | FIND | ***** | ***** |
| 2017-11-08 | 2707509000 | Liquid pyrolysis products, MARK E-1 (yellow liquid) - the products obtained in an ethylene plant in the pyrolysis of hydrocarbon gases in as a byproduct. It is a complex mixture of an aromatic hydrocarbon ( | Figurative trademark, CB-IN â„–132767 FROM 29/09/95 | SINGAPORE | 124460 | 44126,62 | KAZAN | ***** | ***** |
| 2017-11-08 | 2707509000 | Liquid pyrolysis products, MARK E-1 (yellow liquid) - the products obtained in an ethylene plant in the pyrolysis of hydrocarbon gases in as a byproduct. It is a complex mixture of an aromatic hydrocarbon ( | Figurative trademark, CB-IN â„–132767 FROM 29/09/95 | SINGAPORE | 313850 | 111273,83 | KAZAN | ***** | ***** |
| 2017-11-09 | 2707509000 | Liquid pyrolysis products, MARK E-1 (yellow liquid) - the products obtained in an ethylene plant in the pyrolysis of hydrocarbon gases in as a byproduct. It is a complex mixture of an aromatic hydrocarbon ( | Figurative trademark, CB-IN â„–132767 FROM 29/09/95 | SINGAPORE | 61850 | 19743,65 | KAZAN | ***** | ***** |
| 2017-11-10 | 2710196609 | Bunkering: fuel oil, with a sulfur content of 2.61%, a kinematic viscosity at 268.3 50GR.S CCT (EN ISO3104), FLASH POINT closed cup 91 gr (ASTMD93), Flash Point COC 159 oC ( ASTMD92) initial boiling point of 175 gr. FROM | ABSENT | SINGAPORE | 700000 | 213850 | MURMANSK | ***** | ***** |
| 2017-11-10 | 2707509000 | LIQUID PRODUKTY pyrolysis, Mark E-1 (yellow liquid) - the products obtained in an ethylene plant in the pyrolysis of hydrocarbon gases in as a byproduct. It is a complex mixture of an aromatic hydrocarbon ( | Figurative trademark, CB-IN â„–132767 FROM 29/09/95 | SINGAPORE | 62700 | 22199,65 | KAZAN | ***** | ***** |
| 2017-11-13 | 2707999900 | BALANCE OF HEAVY OIL; ODS-E aroma. HYDROCARBONS 74.6% by weight. (ADJ METHOD Comp-U to the note A №2 HS EAEC.) DENSITY (METHOD EN ISO 12185) 969.0 g / cm3 at 15 ° C; kinematics. Viscosity at 50 ° C: 466.8 mm2 / s (METHOD | ABSENT | SINGAPORE | 2998761 | 733976,74 | Taman | ***** | ***** |
| 2017-11-13 | 2707999900 | BALANCE OF HEAVY OIL; ODS-E aroma. HYDROCARBONS 74.6% by weight. (ADJ METHOD Comp-U to the note A №2 HS EAEC.) DENSITY (METHOD EN ISO 12185) 969.0 g / cm3 at 15 ° C; kinematics. Viscosity at 50 ° C: 466.8 mm2 / s (METHOD | ABSENT | SINGAPORE | 16000000 | 3916160 | Taman | ***** | ***** |
| 2017-11-13 | 2707999900 | BALANCE OF HEAVY OIL; ODS-E aroma. HYDROCARBONS 74.6% by weight. (ADJ METHOD Comp-U to the note A №2 HS EAEC.) DENSITY (METHOD EN ISO 12185) 969.0 g / cm3 at 15 ° C; kinematics. Viscosity at 50 ° C: 466.8 mm2 / s (METHOD | ABSENT | SINGAPORE | 5000000 | 1223800 | Taman | ***** | ***** |
| 2017-11-13 | 2707999900 | BALANCE OF HEAVY OIL; ODS-E aroma. HYDROCARBONS 74.6% by weight. (ADJ METHOD Comp-U to the note A №2 HS EAEC.) DENSITY (METHOD EN ISO 12185) 969.0 g / cm3 at 15 ° C; kinematics. Viscosity at 50 ° C: 466.8 mm2 / s (METHOD | ABSENT | SINGAPORE | 15000000 | 3671400 | Taman | ***** | ***** |