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Eximpedia analyzes HS Code 2710195109 export and import records, including data from 5 buyers and 0 suppliers. We provide an intelligence report of HS Codes 2710195109 that covers product descriptions, customs tariffs, trade statistics and several subsections that enable shippers to provide detailed product information based solely on numerical data.
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HS Code 2710195109 export markets
Discover HS Code 2710195109 with data on monthly export values, major exporting countries, key ports, leading competitors, and active buyers.
HS CODE | USD VALUE | SHIPMENTS | % |
---|---|---|---|
2710195109 | 56.40 | 31 | 100.00 |
PETROLEUM OILS AND OILS OBTAINED FROM BITUMINOUS MINERALS, OTHER THAN CRUDE; PREPARATIONS NOT ELSEWHERE SPECIFIED OR INCLUDED, CONTAINING BY WEIGHT 70% OR MORE OF PETROLEUM OILS OR OF OILS OBTAINED FROM BITUMINOUS MINERALS, THESE OILS BEING THE BASIC CONS |
COUNTRY | USD VALUE | SHIPMENTS | % |
---|---|---|---|
EGYPT | 55.80 | 5 | 16.13 |
GEORGIA | 0.60 | 2 | 6.45 |
UNITED ARAB EMIRATES | 0.00 | 23 | 74.19 |
UZBEKISTAN | 0.00 | 1 | 3.23 |
PORTS | USD VALUE | SHIPMENTS | % |
---|---|---|---|
NOVOROSSIYSK | 55.80 | 15 | 48.39 |
DIFFERENT | 0.00 | 13 | 41.94 |
ST. SAMUR-EXPORT | 0.60 | 2 | 6.45 |
KIGASH STATION (EXP.) | 0.00 | 1 | 3.23 |
COMPANY | USD VALUE | SHIPMENTS |
---|---|---|
LIMITED LIABILITY COMPANY AFIPSKIY PETROLEUM REFINERY | 0.00 | 80 |
LLC FIRST PLANT | 0.60 | 11 |
OIL TECHNOLOGIES LLC | 55.80 | 315 |
COMPANY | USD VALUE | SHIPMENTS |
---|---|---|
VOLITON DMCC | 0.00 | 114 |
LLC INTERMAX PETROLEUM LLC INTERMAX PETROLEUM | 0.00 | 26 |
FENIX ENERGY DMCC | 0.00 | 109 |
JSC RUSTAVOIL | 0.60 | 66 |
AKRAIA INTERNATIONAL DMCC | 55.80 | 60 |
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Analyze HSN Code 2710195109 with product description, export values, quantities, importer name, country of origin and key import destinations.
HSN Code | Product Description | Imports | Exporter | Origin | Destination | Qty. |
---|---|---|---|---|---|---|
2710195109 | HEAVY DISTILLATES, LIQUID FUELS FOR SPECIFIC PROCESSES | RUSSIA | UNITED ARAB EMIRATES | 0 | ||
2710195109 | HEAVY DISTILLATES. LIQUID FUELS FOR SPECIFIC PROCESSING PROCESSES. OTHER. COMMERCIAL NAME - VACUUM GAS OIL (STO 52821717-055-2018) AND/OR VACUUM DISTILLED OIL FUEL (STO 52821717-065-2020). WEIGHT 33,000,000 T. DESIGNED FOR SPECIFIC PROCESSES OF CATALYTIC CRACKING AND HYDROCRACKING. LESS THAN 65 RPM % OF WHICH (INCLUDING LOSSES) IS DISTILLED AT TEMP. 250°C BY ASTM D 86 METHOD, OR % DISTILLATION OF WHICH AT TEMP. 250°C CANNOT BE DETERMINED BY THIS METHOD. LESS THAN 85 RPM % OF WHICH (INCLUDING LOSSES) IS DISTILLED AT TEMP. 350°C ACCORDING TO ISO 3405 METHOD (EQUIVALENT TO ASTM D 86 METHOD). PACE. BOILING START OF 200°C OR MORE ACCORDING TO ASTM D 86 METHOD, THE QUANTITY OF KEROSENE-GAS OIL FRACTIONS DISTILLIBLE TO 350°C ACCORDING TO ASTM D 1160 METHOD IS MORE THAN 17 VOL. %, TEMP. FLASHES IN OPEN CRUCULA AT NOT BELOW 90°C ACCORDING TO ASTMD METHOD 92 | RUSSIA | UNITED ARAB EMIRATES | 0 | ||
2710195109 | HEAVY DISTILLATES, LIQUID FUELS FOR SPECIFIC PROCESSING PROCESSES. OTHER. COMMERCIAL NAME - VACUUM GAS OIL (STO 52821717-055-2018). WEIGHT 33,000,000 T, DESIGNED FOR SPECIFIC PROCESSES OF CATALYTIC CRACKING AND HYDROCRACKING. LESS THAN 65 RPM % OF WHICH (INCLUDING LOSSES) IS DISTILLED AT TEMP. 250°C BY ASTM D 86 METHOD, OR % DISTILLATION OF WHICH AT TEMP. 250°C CANNOT BE DETERMINED BY THIS METHOD. LESS THAN 85 RPM % OF WHICH (INCLUDING LOSSES) IS DISTILLED AT TEMP. 350°C ACCORDING TO ISO 3405 METHOD (EQUIVALENT TO ASTM D 86 METHOD). PACE. BOILING START OF 200°C OR MORE ACCORDING TO ASTM D 86 METHOD, THE QUANTITY OF KEROSENE-GAS OIL FRACTIONS DISTILLIBLE TO 350°C ACCORDING TO ASTM D 1160 METHOD IS MORE THAN 17 VOL. %,PACE. FLASHES IN OPEN CRUCULA AT NOT BELOW 90°C ACCORDING TO ASTMD METHOD 92 | RUSSIA | UNITED ARAB EMIRATES | 0 | ||
2710195109 | HEAVY DISTILLATES, LIQUID FUELS FOR SPECIFIC PROCESSING PROCESSES. OTHER COMMERCIAL NAME - VACUUM GAS OIL (STO 52821717-055-2018) AND/OR VACUUM DISTILLED OIL FUEL (STO 52821717-065-2020). WEIGHT 34500,000 T. DESIGNED FOR SPECIFIC PROCESSES OF CATALYTIC CRACKING AND HYDROCRACKING. LESS THAN 65 RPM % OF WHICH (INCLUDING LOSSES) IS DISTILLED AT TEMP. 250°C BY ASTM D 86 METHOD, OR % DISTILLATION OF WHICH AT TEMP. 250°C CANNOT BE DETERMINED BY THIS METHOD. LESS THAN 85 RPM % OF WHICH (INCLUDING LOSSES) IS DISTILLED AT TEMP. 350°C ACCORDING TO ISO 3405 METHOD (EQUIVALENT TO ASTM D 86 METHOD). PACE. BOILING START OF 200°C OR MORE ACCORDING TO ASTM D 86 METHOD, THE QUANTITY OF KEROSENE-GAS OIL FRACTIONS DISTILLIBLE TO 350°C ACCORDING TO ASTM D 1160 METHOD IS MORE THAN 17 VOL. %, TEMP. FLASHES IN OPEN CRUCULA AT NOT BELOW 90°C ACCORDING TO ASTMD METHOD 92 | RUSSIA | UNITED ARAB EMIRATES | 0 | ||
2710195109 | HEAVY DISTILLATES, LIQUID FUELS FOR SPECIFIC PROCESSES | RUSSIA | UNITED ARAB EMIRATES | 0 | ||
2710195109 | HEAVY DISTILLATES, LIQUID FUELS FOR SPECIFIC PROCESSES | RUSSIA | UNITED ARAB EMIRATES | 0 | ||
2710195109 | HEAVY DISTILLATES, LIQUID FUELS FOR SPECIFIC PROCESSING PROCESSES. OTHER COMMERCIAL NAME - VACUUM GAS OIL (STO 52821717-055-2018) AND/OR VACUUM DISTILLED OIL FUEL (STO 52821717-065-2020). WEIGHT 33,000,000 T. DESIGNED FOR SPECIFIC PROCESSING PROCESSES BY CATALYTIC CRACKING AND HYDROCRACKING. LESS THAN 65 RPM % OF WHICH (INCLUDING LOSSES) IS DISTILLED AT TEMP. 250°C BY ASTM D 86 METHOD, OR % DISTILLATION OF WHICH AT TEMP. 250°C CANNOT BE DETERMINED BY THIS METHOD. LESS THAN 85 RPM % OF WHICH (INCLUDING LOSSES) IS DISTILLED AT TEMP. 350°C ACCORDING TO ISO 3405 METHOD (EQUIVALENT TO ASTM D 86 METHOD). PACE. BOILING START OF 200°C OR MORE ACCORDING TO ASTM D 86 METHOD, THE QUANTITY OF KEROSENE-GAS OIL FRACTIONS DISTILLIBLE TO 350°C ACCORDING TO ASTM D 1160 METHOD IS MORE THAN 17 VOL. %, TEMP. FLASHES IN OPEN CRUCULA AT NOT BELOW 90°C ACCORDING TO ASTMD METHOD 92 | RUSSIA | UNITED ARAB EMIRATES | 0 | ||
2710195109 | HEAVY DISTILLATES, LIQUID FUELS FOR SPECIFIC PROCESSING PROCESSES. OTHER. COMMERCIAL NAME - VACUUM GAS OIL (STO 52821717-055-2018) AND/OR VACUUM DISTILLED OIL FUEL (STO 52821717-065-2020). WEIGHT 30 100.000 T. DESIGNED FOR SPECIFIC PROCESSES OF CATALYTIC CRACKING AND HYDROCRACKING. LESS THAN 65 RPM % OF WHICH (INCLUDING LOSSES) IS DISTILLED AT TEMP. 250°C BY ASTM D 86 METHOD, OR % DISTILLATION OF WHICH AT TEMP. 250°C CANNOT BE DETERMINED BY THIS METHOD. LESS THAN 85 RPM % OF WHICH (INCLUDING LOSSES) IS DISTILLED AT TEMP. 350°C ACCORDING TO ISO 3405 METHOD (EQUIVALENT TO ASTM D 86 METHOD). PACE. BOILING START OF 200°C OR MORE ACCORDING TO ASTM D 86 METHOD, THE QUANTITY OF KEROSENE-GAS OIL FRACTIONS DISTILLIBLE TO 350°C ACCORDING TO ASTM D 1160 METHOD IS MORE THAN 17 VOL. %, TEMP. FLASH RESULTS IN OPEN CRUCULA AT NOT BELOW 90°C ACCORDING TO ASTMD METHOD 92 | RUSSIA | UNITED ARAB EMIRATES | 0 | ||
2710195109 | HEAVY DISTILLATES, LIQUID FUELS FOR SPECIFIC PROCESSING PROCESSES. OTHER. COMMERCIAL NAME - VACUUM GAS OIL (STO 52821717-055-2018). WEIGHT 33,000,000 T. DESIGNED FOR SPECIFIC CATALYTIC PROCESSES | RUSSIA | UNITED ARAB EMIRATES | 0 | ||
2710195109 | HEAVY DISTILLATES, LIQUID FUELS FOR SPECIFIC PROCESSING PROCESSES. OTHER. COMMERCIAL NAME - VACUUM GAS OIL (STO 52821717-055-2018). WEIGHT 34500,000 T. DESIGNED FOR SPECIFIC CATALYTIC PROCESSES | RUSSIA | UNITED ARAB EMIRATES | 0 |
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