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Eximpedia analyzes Llc Novatek Ust Luga export and import records, including data from 4 buyers and 0 suppliers. We provide an intelligence report of Llc Novatek Ust Luga that covers trade statistics, shipment values, quantities, exporters & importers and trade destinations
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Llc Novatek Ust Luga export markets
Explore the RUSSIA export market with monthly export values, major importers, HS Codes, key ports, top suppliers, and competitors
HS CODE | USD VALUE | SHIPMENTS | % |
---|---|---|---|
2710129008 | 2148.79 | 109 | 37.85 |
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 | |||
2710192100 | 631.02 | 35 | 12.15 |
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 | |||
2709001009 | 352.87 | 10 | 3.47 |
2710194290 | 293.20 | 23 | 7.99 |
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 | |||
2710194210 | 114.67 | 10 | 3.47 |
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 | % |
---|---|---|---|
CHINA | 2165.35 | 166 | 57.64 |
TURKEY | 945.17 | 84 | 29.17 |
SINGAPORE | 123.91 | 4 | 1.39 |
LIBYA | 116.09 | 10 | 3.47 |
EGYPT | 77.85 | 9 | 3.12 |
PORTS | USD VALUE | SHIPMENTS | % |
---|---|---|---|
UST-LUGA PORT | 3582.30 | 288 | 100.00 |
COMPANY | USD VALUE | SHIPMENTS |
---|---|---|
OIL TECHNOLOGIES LLC | 426.67 | 315 |
LLC TATNEFT AZS CENTER | 440.02 | 138 |
LLC KNGK INPZ | 587.25 | 177 |
FOXTON FZCO | 873.81 | 71 |
LLC NOVATEK UST LUGA | 4297.58 | 288 |
COMPANY | USD VALUE | SHIPMENTS |
---|---|---|
SILVER EDGE INVESTMENT LIMITED | 417.95 | 63 |
AMUR TRADING FZCO | 419.38 | 275 |
KNGK TRADING DMCC | 554.78 | 94 |
FOXTON FZCO | 1180.28 | 609 |
NOVATEK GAS AND POWER GMBH | 4297.58 | 144 |
If you are looking to establish relationship with Llc Novatek Ust Luga Automation you can save time by getting access to the key decision makers and get a detailed report.
Discover the Llc Novatek Ust Luga with product description, import values, quantities, exporter name, country of origin and key destinations.
HSN Code | Product Description | Imports | Exporter | Origin | Destination | Qty. |
---|---|---|---|---|---|---|
2710194290 | GAS OIL, WITH SULFUR CONTENT NOT MORE THAN 0.05 MASS,%, OTHER, - PERCENTAGE OF DISTILLATION OF PETROLEUM PRODUCTS AT A TEMPERATURE OF 250°C (ACCORDING TO | RUSSIA | LIBYA | 0 | ||
2710196209 | OPERATING SUPPLIES. MARINE FUEL (FUEL OIL), RMD-80 INTENDED FOR BUNKERING OF SHIPS: -START BOILING TEMPERATURE (°C) 227.0; - PERCENTAGE OF DISTILLATION OF PETROLEUM PRODUCTS AT TEMPERATURE 250°C (BY ISO 3405 METHOD, EQUIVALENT ASTM D86 METHOD), (VOL.%) 5.5; - PERCENTAGE OF DISTILLATION OF PETROLEUM PRODUCTS AT TEMPERATURE 350°C (BY ISO 3405 METHOD, EQUIVALENT TO ASTM D86 METHOD), (VOL.%) 48.0; -KINEMATIC VISCOSITY AT TEMPERATURE 50°C (ACCORDING TO EN ISO 3104 METHOD), (MM2/SEC) 8.545; -FLASH POINT IN CLOSED CRUCIBLE (ASTM D93 METHOD), (°C) 109.0; -FLASH TEMPERATURE IN OPEN CRUCCILE (ACCORDING TO ASTM D92 METHOD), (°C) 142; - MASS FRACTION OF TOTAL SULFUR (MASS%) 0.0980; - COLORIMETRICA CHARACTERISTIC (BY ASTM D 6045 METHOD), (UNITS) LESS THAN 1.0; -QUANTITY OF KEROSENE-GAS OIL FRACTIONS DISTILLED TO 350°C ACCORDING TO ASTM D1160 METHOD, (VOL.%) 41; -PROCESSING PROCESS: ATMOSPHERIC DISTILLATION BY RECTIFICATION AND HYDROCRACKING | RUSSIA | CHINA | 0 | ||
2710194260 | OPERATING SUPPLIES, LOW-VISCOSITY MARINE FUEL DMA(CMT DMA) DESIGNED | RUSSIA | CHINA | 0 | ||
2710196209 | OPERATING SUPPLIES, MARINE FUEL (MAZUT), RMD-80 DESIGNED FOR D | RUSSIA | TURKEY | 0 | ||
2710196209 | OPERATING SUPPLIES. MARINE FUEL (MAZUT), RMD-80 DESIGNED FOR D | RUSSIA | CHINA | 0 | ||
2710196209 | OPERATING SUPPLIES. MARINE FUEL (MAZUT), RMD-80 INTENDED FOR BUNKERING SHIPS: - BOILING TEMPERATURE (°C) 233.0, - PETROLEUM PRODUCTS DISTILLATION PERCENTAGE AT 250°C (ACCORDING TO ISO 3405 METHOD, EQUIVALENT TO ASTM D86 METHOD), (OB. %) 2 | RUSSIA | CHINA | 0 | ||
2709001009 | GAS CONDENSATE, STABLE | RUSSIA | UNITED ARAB EMIRATES | 0 | ||
2709001009 | GAS CONDENSATE, STABLE | RUSSIA | MALAYSIA | 0 | ||
2710129008 | LIGHT NAPHTHA, -PENTANE CONTENT (C5) 27.49 WT.%; -HEXANE CONTENT (C6) 18.96 WT.%; -N-HEXANE CONTENT 8.27 WT.%; -DISTILLATION PERCENTAGE AT 210°C(AST METHOD | RUSSIA | CHINA | 0 | ||
2710192100 | TURBOJET FUEL, TYPE AVIATION KEROSENE JET A-1, - PERCENTAGE OF DISTILLATION OF PETROLEUM PRODUCTS AT A TEMPERATURE OF 210°C (BY ISO 3405 METHOD, EQUIVALENT ASTM D86 METHOD) LESS THAN 90 VOL.%; -PERCENTAGE OF DISTILLATION OF PETROLEUM PRODUCTS AT TEMPERATURE 250° | RUSSIA | TURKEY | 0 | ||
2710194210 | GAS OIL, DIESEL FUEL (SUMMER) - PERCENTAGE OF DISTILLATION OF PETROLEUM PRODUCTS AT A TEMPERATURE OF 250°C (BY ISO 3405 METHOD, EQUIVALENT ASTM D86 METHOD) LESS THAN 65 VOL.%; - PERCENTAGE OF PETROLEUM PRODUCTS DISTILLATION AT 350°C (METHOD ISO 3405, EQUIVALENT | RUSSIA | TURKEY | 0 | ||
2710196209 | OPERATING SUPPLIES, MARINE FUEL (MAZUT), RMD-80 INTENDED FOR BUNKERING OF SHIPS: -START BOILING TEMPERATURE (°C) 228.0; - PERCENTAGE OF DISTILLATION OF PETROLEUM PRODUCTS AT A TEMPERATURE OF 250°C (BY ISO 3405 METHOD, EQUIVALENT ASTM D86 METHOD), (VOL.%) LESS THAN 2.0; - PERCENTAGE OF DISTILLATION OF PETROLEUM PRODUCTS AT TEMPERATURE 350°C (BY ISO 3405 METHOD, EQUIVALENT TO ASTM D86 METHOD), (VOL.%) 44.0; -KINEMATIC VISCOSITY AT TEMPERATURE 50°C (ACCORDING TO EN ISO 3104 METHOD), (MM2/SEC) 8.614; -FLASH POINT IN CLOSED CRUCIBLE (ASTM D93 METHOD), (°C) 110.0; -FLASH TEMPERATURE IN OPEN CRUCCILE (ACCORDING TO ASTM D92 METHOD), (°C) 148; - MASS FRACTION OF TOTAL SULFUR (MASS%) 0.0907; - COLORIMETRICA CHARACTERISTIC (BY ASTM D 6045 METHOD), (UNITS) LESS THAN 1.0; -QUANTITY OF KEROSENE-GAS OIL FRACTIONS DISTILLED TO 350°C ACCORDING TO ASTM D1160 METHOD, (VOL.%) 39; -PROCESSING PROCESS: ATMOSPHERIC DISTILLATION BY RECTIFICATION AND HYDROCRACKING | RUSSIA | CHINA | 0 | ||
2710196209 | OPERATING SUPPLIES. MARINE FUEL (FUEL OIL), RMD-80 INTENDED FOR BUNKERING OF SHIPS: -START BOILING TEMPERATURE (°C) 248.0; - PERCENTAGE OF DISTILLATION OF PETROLEUM PRODUCTS AT A TEMPERATURE OF 250°C (BY ISO 3405 METHOD, EQUIVALENT ASTM D86 METHOD), (VOL.%) LESS THAN 0.5; - PERCENTAGE OF DISTILLATION OF PETROLEUM PRODUCTS AT TEMPERATURE 350°C (ACCORDING TO ISO 3405 METHOD, EQUIVALENT TO ASTM D86 METHOD), (VOL.%) 30.0; -KINEMATIC VISCOSITY AT TEMPERATURE 50°C (ACCORDING TO EN ISO 3104 METHOD), (MM2/SEC) 7.682; -FLASH POINT IN CLOSED CRUCIBLE (ASTM D93 METHOD), (°C) 108.0; -FLASH TEMPERATURE IN OPEN CRUCCILE (ACCORDING TO ASTM D92 METHOD), (°C) 154; - MASS FRACTION OF TOTAL SULFUR (MASS%) 0.0244; -COLORIMETRICA CHARACTERISTIC (BY ASTM D 6045 METHOD), (UNITS) 0.5; -QUANTITY OF KEROSENE-GAS OIL FRACTIONS DISTILLED TO 350°C ACCORDING TO ASTM D1160 METHOD, (VOL.%) 42; -PROCESSING PROCESS: ATMOSPHERIC DISTILLATION BY RECTIFICATION AND HYDROCRACKING | RUSSIA | MALAYSIA | 0 | ||
2710129008 | HEAVY NAPHTHA, - PENTANE CONTENT (C5) LESS THAN 35 MASS %; -HEXANE CONTENT (C6) LESS THAN 55 MASS,%; -DISTILLATION PERCENTAGE AT TEMPERATURE 21 | RUSSIA | CHINA | 0 | ||
2710196209 | OPERATING SUPPLIES, MARINE FUEL (MAZUT), RMD-80 INTENDED FOR BUNKERING OF SHIPS: -START BOILING TEMPERATURE IS NOT DETERMINED; -FLASH TEMPERATURE IN CLOSED CRUCIBLE (ACCORDING TO ASTM D 93(B) METHOD), NOT LESS THAN 61(°C); - FLASH POINT IN AN OPEN CRUCCILE (ACCORDING TO ASTM D92 METHOD) NOT LESS THAN 90(°C); -THE PERCENTAGE OF DISTILLATION OF PETROLEUM PRODUCTS AT A TEMPERATURE OF 250°C (ACCORDING TO ISO 3405 METHOD, EQUIVALENT TO ASTM D86 METHOD) LESS THAN 65 VOL.%; - PERCENTAGE OF DISTILLATION OF PETROLEUM PRODUCTS AT A TEMPERATURE OF 350°C (BY ISO 3405 METHOD, EQUIVALENT ASTM D86 METHOD) LESS THAN 85 VOL.%; - THE AMOUNT OF KEROSENE-GAS OIL FRACTIONS DISTILLED TO 350°C ACCORDING TO ASTM D1160 METHOD IS MORE THAN 17 VOL.%; -KINEMATIC VISCOSITY AT TEMPERATURE 50°C (ACCORDING TO EN ISO 3104 METHOD), (MM2/SEC), NO MORE THAN 80; - MASS FRACTION OF TOTAL SULFUR (MASS%) NO MORE THAN 1 VOLUME%; -COLORIMETRIC CHARACTERISTICS NOT DEFINED; -PROCESSING PROCESS: ATMOSPHERIC DISTILLATION BY RECTIFICATION AND HYDROCRACKING | RUSSIA | CHINA | 0 | ||
2709001009 | GAS CONDENSATE STABLE | RUSSIA | TURKEY | 0 | ||
2710192100 | TURBOJET FUEL, TYPE OF AVIATION KEROSENE JET A-1, - PERCENTAGE OF PETROLEUM PRODUCTS DISTILLATION AT 210°C (ACCORDING TO ISO 3405 METHOD, EQUIVALENT | RUSSIA | TURKEY | 0 | ||
2710194260 | OPERATING SUPPLIES. MARINE LOW-VISCOSITY FUEL DMA(CMT DMA) IS INTENDED | RUSSIA | CHINA | 0 | ||
2710192100 | TURBOJET FUEL, TYPE OF AVIATION KEROSENE JET A-1, - PERCENTAGE OF PETROLEUM PRODUCTS DISTILLATION AT 210°C (BY ISO 3405 EQUIVALENT METHOD | RUSSIA | TURKEY | 0 | ||
2710192100 | FUEL FOR TURBOJET ENGINES, TYPE OF AVIATION KEROSENE JET A-1 | RUSSIA | TURKEY | 0 |
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