A Position Export Data of Russia

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Find trade data and market research report on a position exports under HS Code 2710195101 and follow up market price of a positions. Know market share of companies exporting a position under HS Code 2710195101

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DATE HS_CODE Product Description TrademarkCountry Net Weight Statistical Cost Place Shipper NameConsignee Name
2017-08-012710195101FUEL OIL EXPORT vacuum distillation of catalytic cracking, hydrocracking, fractional composition METHOD ISO 3405: ​​at T 250 GRAD. With distilled OF LESS THAN 65. % (Including losses) at T 350 GRAD. With distilled OF LESS THAN 85. % (Including losses***RUSSIA3900000998790*************
2017-08-022710195101FUEL OIL VACUUM DISTILLATION EXPORT TO catalytic cracking, hydrocracking fractional composition METHOD ASTM D 86 / ISO 3405: ​​the initial boiling point of 325 ° C, at T 250 ° C distilled 0 vol%, at T 350 ° C distilled 1.5 vol%... QUANTITY***RUSSIA3169142982846,01*************
2017-08-022710195101FUEL OIL VACUUM DISTILLATION EXPORT TO catalytic cracking, hydrocracking fractional composition METHOD ASTM D 86 / ISO 3405: ​​the initial boiling point 335.0 ° C, at T 250 ° C distilled 0 vol%, at T 350 ° C distilled 1.0 vol%... AMOUNTS***RUSSIA728168226008,78*************
2017-08-022710195101FUEL OIL VACUUM DISTILLATION EXPORT TO catalytic cracking, hydrocracking fractional composition METHOD ASTM D 86 / ISO 3405: ​​the initial boiling point 335.0 ° C, at T 250 ° C distilled 0 vol%, at T 350 ° C distilled 1.0 vol%... AMOUNTS***RUSSIA38855391205993,59*************
2017-08-042710195101FUEL OIL EXPORT vacuum distillation of catalytic cracking, hydrocracking, fractional composition according to GOST R EN ISO 3405: ​​initial boiling point of 339-342 ° C; T AT 250 ° C ON distilled.% NOT DEFINED .; T AT 350 ° C distilled 1,0-2,2 vol.%. NUMBER***RUSSIA3836571950821,13*************
2017-08-082710195101FUEL OIL EXPORT TO VACUUM DISTILLATION catalytic cracking, hydrocracking chroma ASTM D 1500 IU 4,5 COMPOSITION FOR FRACTIONAL GOST EN ISO 3405: ​​initial boiling point 339 ° C; T AT 250 ° C ON% distilled NOT DEFINED..; T AT 350 ° C***RUSSIA77215281976556,74*************
2017-08-162710195101FUEL OIL EXPORT vacuum distillation of catalytic cracking, hydrocracking, fractional composition METHOD ISO 3405: ​​at T 250 GRAD. With distilled OF LESS THAN 65. % (Including losses) at T 350 GRAD. With distilled OF LESS THAN 85. % (Including losses***RUSSIA3900000998790*************
2017-08-212710195101FUEL OIL EXPORT TO VACUUM DISTILLATION catalytic cracking, hydrocracking chroma ASTM D 1500 IU 4,5 COMPOSITION FOR FRACTIONAL GOST EN ISO 3405: ​​initial boiling point 342 ° C; T AT 250 ° C ON% distilled NOT DEFINED..; T AT 350 ° C******38212841032625,58*************
2017-08-232710195101FUEL OIL EXPORT vacuum distillation of catalytic cracking, hydrocracking, fractional composition METHOD ISO 3405: ​​at T 250 GRAD. With distilled OF LESS THAN 65. % (Including losses) at T 350 GRAD. With distilled OF LESS THAN 85. % (Including losses******3900000998790*************
2017-08-292710195101FUEL OIL EXPORT vacuum distillation of catalytic cracking, hydrocracking, fractional composition according to GOST R EN ISO 3405: ​​initial boiling point of 336 ° C; T AT 250 ° C ON distilled.% NOT DEFINED .; T AT 350 ° C distilled 0.9 vol.%. QUANTITY******38214711111474,84*************


Our a position export data of Russia and market research report covers market priceof a position and market share of Russian companies. This helps you to do market analysis on the basis of price, company, etc. efficiently and gain knowledge on market size of a position in Russia. Few shipment records with a small number of important columns from Russia export data of a position are given above. Other hidden fields such as Russian Exporter Name with Address, Foreign Exporter Name with Address, Value, Quantity, Origin & Destination Country and more are also covered in Russia customs data of a position. To view more shipment records of a position export data of Russia, you can set a filter by Country Name, HS Code and Place.

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