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LLC NOVATEK UST LUGA TRADE DATA ANALYSIS

Access comprehensive trade data for Llc Novatek Ust Luga with ease. Explore trade shipments, top suppliers & buyers, and values without the hassle.

Llc Novatek Ust Luga – Overview

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

Llc Novatek Ust Luga Buyers, Suppliers & Shipments

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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

TOP EXPORT HS CODE

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

TOP EXPORT COUNTRY

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

TOP EXPORT PORTS

PORTS USD VALUE SHIPMENTS %
UST-LUGA PORT 3582.30 288 100.00

TOP EXPORT COMPETITORS

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

TOP EXPORT BUYERS

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.

Llc Novatek Ust Luga Export Shipments

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 lock lock 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 lock lock RUSSIA CHINA 0
2710194260 OPERATING SUPPLIES, LOW-VISCOSITY MARINE FUEL DMA(CMT DMA) DESIGNED lock lock RUSSIA CHINA 0
2710196209 OPERATING SUPPLIES, MARINE FUEL (MAZUT), RMD-80 DESIGNED FOR D lock lock RUSSIA TURKEY 0
2710196209 OPERATING SUPPLIES. MARINE FUEL (MAZUT), RMD-80 DESIGNED FOR D lock lock 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 lock lock RUSSIA CHINA 0
2709001009 GAS CONDENSATE, STABLE lock lock RUSSIA UNITED ARAB EMIRATES 0
2709001009 GAS CONDENSATE, STABLE lock lock 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 lock lock 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° lock lock 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 lock lock 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 lock lock 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 lock lock 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 lock lock 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 lock lock RUSSIA CHINA 0
2709001009 GAS CONDENSATE STABLE lock lock 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 lock lock RUSSIA TURKEY 0
2710194260 OPERATING SUPPLIES. MARINE LOW-VISCOSITY FUEL DMA(CMT DMA) IS INTENDED lock lock 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 lock lock RUSSIA TURKEY 0
2710192100 FUEL FOR TURBOJET ENGINES, TYPE OF AVIATION KEROSENE JET A-1 lock lock RUSSIA TURKEY 0

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Llc Novatek Ust Luga frequently asked questions

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