End Trade Data of Russia Exports under HS Code 27

Get end trade data of Russia exports under HS code 27. Check Russia trade statistics of end exports under HS code 27 with market share and size, price, name of trade partners etc.

 
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552 Shipments Records (Demo)

27  
DateHS CodeProduct DescriptionDestination CountryTrademarkQuantityUnitNet WeightTotal Value [USD] Exporter Name
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30/Nov/20172710129008Light distillates, other; 90% distilled at 132.3 degrees c; boiling temperature end 163.7 degrees c (gost 2177); the content of pentane (c5) 4, 8% contents hexane (c6), 24.5%.REPUBLIC OF BELARUSABSENT******527,759226320,48 ***** 84 More Columns Available along with Company Name and Other Details etc.
29/Nov/20172711190000Hydrocarbon gas, liquid fuel; mark pbt (sum of propane and propylene - 72.33%; butane and butenes - 26.48%) - 17.56tn; party № 6144; used as fuel for road transport; consumers (end-users): ooo "UKRAINEnot mark******17,5608206,94 *****
29/Nov/20172710198200Oil (heavy distillates, the percentage distilled at 250 and 350 degrees c can not be identified by the method astm d86) mineral, packed in 50l. canister on pallets. the oil content of more than 70%. end user: ooo "euroUKRAINE"LUKOIL"******5,520.724922,11 *****
27/Nov/20172710122501Other specific gasolines: petroleum ether-s2-80 / 120 tu 38.401-67-108-92 with a content of n-hexane not less than 55% but not more than 80% by weight, the initial boiling point of at least 64 � c and.. end point boiling not more than 70 � c, without anyUKRAINEABSENT******25,00010087,5 *****
27/Nov/20172707991100Pyrolysis product liquid fraction 35-230 � c and 32-320 � c, mark e-5 tu 2451-075-05766563-2004 c mod. №1-4 fractional composition: initial boiling point 37 � c- 45 � c; boiling temperature end 185 � c-201 � c; weight content aroma. c6-c8 hydrocarbons inKINGDOM OF THE NETHERLANDSABSENT******1,998,000970288,74 *****
24/Nov/20172710121509Light distillates and products for chemical conversions in the process and other. stable natural gasoline, quality corresponds srt 11605031-019-2007, percent distillation at 210 � c is not defined (method astm d 86) tk end of boilingTURKEYABSENT******2,950,5501498289,29 *****
24/Nov/20172710122501Other specific gasolines:. nephras p1-63 / 75 with n-hexane not less than 55% but not more than 80% by weight, the initial boiling point of at least 64 � c and end temperature boiling not more than 70 � c, no. any antiknock additives, qtyREPUBLIC OF BELARUSABSENT******27,00022,950 *****
22/Nov/20172710122509Other specific gasolines: hexane solvent nephras p1-63 / 75, tu 38.1011228-90, fractional composition: initial boiling point of 65.0 � c method en iso 3405, boiling temperature end 77.0 � c method en iso 3405, pentane (c5)THE REPUBLIC OF KAZAKHSTAN*********22,35026388,45 *****
17/Nov/20172710127000Jet fuel ts-1, gost 10227-86 rev. 1-6 at a temperature of 210 c distilled by astm d 86 method (including losses) - measure not determine (boiling temperature end - 207.7 c) number - t 7509, 092UNITED KINGDOMABSENT******7,509,0923896542,93 *****
16/Nov/20172710193500Heavy distillates, gas oils, for undergoing chemical transformation by a process; liquid paraffin oil, fraction c14-c17, mark a; tu 0255-023-05766480-2006; 0% distilled at 250 � c (method astm d 86); initial boiling point 258 � c; end of boiling 284FINLAND*********53,88536711,85 *****
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