DATE | HS_CODE | Product Description | Trademark | Country | Net Weight | Statistical Cost | Place | Shipper Name | Consignee Name |
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2017-11-01 | 2711129400 | FRACTION propanoic LIQUEFIED PROPANE OVER WITH 90.00% but less than 99.00%, a modifier POLYMERISATION PROCESS IN THE PRODUCTION OF POLYETHYLENE | ABSENT. | FINLAND | 3050000 | 1466623 | Niirala | ***** | ***** |
2017-11-01 | 2711129400 | FRACTION propanoic LIQUEFIED PROPANE OVER WITH 90.00% but less than 99.00%, a modifier POLYMERISATION PROCESS IN THE PRODUCTION OF POLYETHYLENE | ABSENT. | FINLAND | 1650000 | 793419 | Vainikkala | ***** | ***** |
2017-11-02 | 2710121501 | Stable natural gasoline used as raw materials PETROCHEMICAL INDUSTRIES, distilled to 90% v or more ON. LOSS UP TO 210 GRAD. With METHOD ASTM D86, pentane-hexane fraction with pentane (C5) at least 35 wt.% And hexane ( | *** | FINLAND | 9050000 | 4880212,5 | Vainikkala | ***** | ***** |
2017-11-02 | 2710193500 | Heavy distillates, gas oils, For undergoing chemical transformation by a process; LIQUID PARAFFIN OIL, fraction C14-C17, TU 0255-023-05766480-2006; Less than 65% distils at 250 ° C METHOD ISO 3405 (ASTM D 86); 85% or more distilled at | *** | FINLAND | 55000 | 37537,5 | Buslovskaya | ***** | ***** |
2017-11-02 | 2710193500 | Heavy distillates, gas oils, For undergoing chemical transformation by a process; LIQUID PARAFFIN OIL, fraction C14-C17, TU 0255-023-05766480-2006; Less than 65% distils at 250 ° C METHOD ISO 3405 (ASTM D 86); 85% or more distilled at | *** | FINLAND | 55000 | 37537,5 | Buslovskaya | ***** | ***** |
2017-11-02 | 2710193500 | Heavy distillates, gas oils, For undergoing chemical transformation by a process; LIQUID PARAFFIN OIL, fraction C14-C17, TU 0255-023-05766480-2006; Less than 65% distils at 250 ° C METHOD ISO 3405 (ASTM D 86); 85% or more distilled at | *** | FINLAND | 55000 | 37537,5 | Buslovskaya | ***** | ***** |
2017-11-02 | 2710193500 | Heavy distillates, gas oils, For undergoing chemical transformation by a process; LIQUID PARAFFIN OIL, fraction C14-C17, TU 0255-023-05766480-2006; Less than 65% distils at 250 ° C METHOD ISO 3405 (ASTM D 86); 85% or more distilled at | *** | FINLAND | 55000 | 37537,5 | Buslovskaya | ***** | ***** |
2017-11-09 | 2710196601 | PERFORMANCE The stores OIL IET - TYPE II, sulfur content 2.70%, the initial boiling point 221.0 ° C, the percentage was distilled off at 250 ° C 2.5% PERCENT distilled off at 350 ° C 16.5%, amount of kerosene-gas oil fractions distilled to 350 ° C. 14 vol.%, | ABSENT | FINLAND | 1000000 | 247000 | ST PETERSBURG | ***** | ***** |
2017-11-09 | 2711129400 | HYDROCARBON GAS-LIQUID PROPANE (FRACTION propane) MARK "A", TU 0272-023-00151638-99, QUANTITY -. 798,250 TH is used as the solvent during the deasphalting oils and coolants. SODERZH.UGLEVOD.S3 - 97.82; 97.18%, with | ABSENT | FINLAND | 798250 | 318501,75 | STBUSLOVSKAYA AE | ***** | ***** |
2017-11-09 | 2711129400 | HYDROCARBON GAS-LIQUID PROPANE (FRACTION propane) MARK "A", TU 0272-023-00151638-99, QUANTITY -. 192,950 TH is used as the solvent during the deasphalting oils and coolants. SODERZH.UGLEVOD.S3 - 97.04%, INCLUDING | ABSENT | FINLAND | 192950 | 76987,05 | STBUSLOVSKAYA AE | ***** | ***** |