| DATE | HS_CODE | Product Description | Trademark | Country | Net Weight | Statistical Cost | Place | Shipper Name | Consignee Name |
|---|
| 2017-11-02 | 2710122509 | OTHER LIGHT DISTILLATES; Stable natural gasoline BT, 90% or more of which (including loss), distilled to a temperature of 210 degrees C (METHOD ASTM D86), WITHOUT ANY OTHER special gasoline antiknock additives with a content of n-hexane at least 55 | *** | *** | 1090000 | 598410 | Ust Luga | ***** | ***** |
| 2017-11-02 | 2710122509 | OTHER LIGHT DISTILLATES; Stable natural gasoline, 90% or more of which (including loss), distilled to a temperature of 210 degrees C (METHOD ASTM D86), WITHOUT ANY OTHER special gasoline antiknock additives, CONTAINING AT LEAST n-hexane 55 wt. | *** | *** | 10000000 | 5490000 | Ust Luga | ***** | ***** |
| 2017-11-08 | 2710122509 | NAFTA LIGHT, -Contents pentane (C5) is not defined; -Contents hexane (C6) is less than 55 wt.%; N-hexane-content of less than 55 wt.%; -PROTSENT distillation at 210 ° C (METHOD ASTM D86) greater than 90%; Initial boiling point is the temperature (° C) not lower than 27; -THOSE | ABSENT | *** | 36000000 | 19503091,4 | Ust Luga | ***** | ***** |
| 2017-11-10 | 2710122509 | NAFTA HEAVY, -Contents pentane (C5) less than 35 wt.%; -Contents hexane (C6) is less than 55 wt.%; N-hexane-content of less than 55 wt.%; -PROTSENT distillation at 210 ° C (METHOD ASTM D86) greater than 90%; Initial boiling point is the temperature (° C) not lower than 60; - | ABSENT | *** | 94500000 | 50817603,23 | Ust Luga | ***** | ***** |
| 2017-11-13 | 2710122509 | NAFTA LIGHT, -Contents pentane (C5) is not defined; -Contents hexane (C6) is less than 55 wt.%; N-hexane-content of less than 55 wt.%; -PROTSENT distillation at 210 ° C (METHOD ASTM D86) greater than 90%; Initial boiling point is the temperature (° C) not lower than 27; -THOSE | ABSENT | *** | 37000000 | 19970750 | Ust Luga | ***** | ***** |
| 2017-11-13 | 2710122509 | OTHER LIGHT DISTILLATES; Stable natural gasoline, 90% or more of which (including loss), distilled to a temperature of 210 degrees C (METHOD ASTM D86), WITHOUT ANY OTHER special gasoline antiknock additives, CONTAINING hexane (C6) is less than 55 | *** | *** | 8000000 | 4594000 | Ust Luga | ***** | ***** |
| 2017-11-17 | 2710122509 | NAFTA LIGHT, -Contents pentane (C5) is not defined; -Contents hexane (C6) is less than 55 wt.%; N-hexane-content of less than 55 wt.%; -PROTSENT distillation at 210 ° C (METHOD ASTM D86) greater than 90%; Initial boiling point is the temperature (° C) not lower than 27; -THOSE | ABSENT | *** | 37000000 | 19397250 | Ust Luga | ***** | ***** |
| 2017-11-21 | 2710122509 | NAFTA HEAVY, -Contents pentane (C5) 2.93 wt.%; -Contents hexane (C6) 6.92 wt.%; N-hexane-content 3.48 wt.%; -PROTSENT distillation at a temperature of 210 ° C (METHOD ASTMD86) is not determined; -Exit (METHOD ASTM D86) 98,0% vol.; -TEMPERATURE | ABSENT | CHINA | 30833819 | 16070895,15 | Ust Luga | ***** | ***** |
| 2017-11-23 | 2710122509 | OTHER LIGHT DISTILLATES; Stable natural gasoline, 90% or more of which (including loss), distilled to a temperature of 210 degrees C (METHOD ASTM D86), WITHOUT ANY OTHER special gasoline antiknock additives, CONTAINING hexane (C6) is less than 55 | *** | SWITZERLAND | 10000000 | 5605000 | Ust Luga | ***** | ***** |
| 2017-11-24 | 2710122509 | NAFTA LIGHT, -Contents pentane (C5), 36.74 wt.%; -Contents hexane (C6), 20.40 wt.%; N-hexane-content 8.78 wt.%; -PROTSENT distillation at a temperature of 210 ° C (METHOD ASTM D86) is not determined; -Exit (METHOD ASTM D86) 98,0% vol.; -temperature | ABSENT | USA | 35479294 | 18148253,75 | Ust Luga | ***** | ***** |