| 1/14/2022 | 2710196209 | FUEL LIQUID: MARINE DISTILLATE FUEL TYPE III (MGO), STO 85778267-002-2014, MASS FRACTION OF SULFUR 0.492%, FLASH POINT IN OPEN CRUCIBLE (ASTM D 92) 118 G.C, BOILING START TEMP (ASTM D 86) - 197 GR.S, FRACTIONAL COMPOSITION ACCORDING TO ASTM D86: VOLUME OF REDISTANT | 30000 | 20702.6 | China | VLADIVISTOK RUSSIA | ALFATREYD LLC |
| 1/24/2022 | 2710196209 | FUEL LIQUID: MARINE DISTILLATE FUEL TYPE III (MGO), STO 85778267-002-2014, MASS FRACTION OF SULFUR 0.492%, FLASH POINT IN OPEN CRUCIBLE (ASTM D 92) 118 G.C, BOILING START TEMP (ASTM D 86) - 197 GR.S, FRACTIONAL COMPOSITION ACCORDING TO ASTM D86: VOLUME OF REDISTANT | 10000 | 6902.6 | China | FIND | ALFATREYD LLC |
| 1/25/2022 | 2710121501 | LIGHT DISTILLATES AND PRODUCTS FOR CHEMICAL TRANSFORMATION IN PROCESSES, OTHER; STABLE GAS GASOLINE AT TEMPERATURE 210░? DISTILLS, % VOL. END BOILING TEMPERATURE (ACCORDING TO GOST 2177-99, METHOD A), ░ ?: 138.0-166.0; REMAINING B | 2826200 | 1903192.7 | Finland | VAYNIKKALA EXP | PJSC TATNEFT IM V D SHASHINA BUGULMIN MANAGEMENT BASE OF TATNEFTESNAB |
| 1/25/2022 | 2710121501 | LIGHT DISTILLATES AND PRODUCTS FOR CHEMICAL TRANSFORMATION IN PROCESSES, OTHER; STABLE GAS GASOLINE AT TEMPERATURE 210░? DISTILLS, % VOL. END BOILING TEMPERATURE (according to GOST 2177-99, METHOD A), ░ ?: 145.0-170.0; REMAINING B | 7173700 | 5137352.7 | Finland | VAYNIKKALA EXP | PJSC TATNEFT IM V D SHASHINA BUGULMIN MANAGEMENT BASE OF TATNEFTESNAB |
| 1/1/2022 | 2710196809 | HEAVY DISTILLATES, FUELS, LIQUID, FOR OTHER PURPOSE, WITH A SULFUR CONTENT OF MORE THAN 2.8 WT.%, OTHER, BOILING POINT ACCORDING TO METHOD ASTM D 86, NUMBER OF kerosene-gas oil fractions distilled up to 350 GR.TS. ACCORDING TO ISO 3405 FLASH TEMPERATURE | 3252500 | 2.3 | United Arab Emirates | SEA PORT CAUCASUS | SMANN SA FROM RESOURCES OF TRADE AND INDUSTRIAL COMPANY LLC |
| 1/1/2022 | 2710196609 | HEAVY DISTILLATES, FUELS, LIQUID, FOR OTHER PURPOSE, WITH A SULFUR CONTENT OF MORE THAN 2 % WT BUT NOT MORE THAN 2.8 WT %, OTHER, BOILING POINT ASTM D 86, NUMBER OF kerosene-gas oil fractions distilling50 .Ts. BY ISO METHOD 3 | 3252500 | 2.3 | United Arab Emirates | SEA PORT CAUCASUS | SMANN SA FROM RESOURCES OF TRADE AND INDUSTRIAL COMPANY LLC |
| 1/1/2022 | 2710196601 | HEAVY DISTILLATES, FUELS, LIQUID, FOR OTHER PURPOSE, WITH A SULFUR CONTENT OF MORE THAN 2 WT.%, BUT NOT MORE THAN 2.8 WT.%, FUEL OILS, THE BOILING POINT OF WHICH IS 200 G.C. FRACTIONS DISTILLING TO | 3252500 | 2.3 | United Arab Emirates | SEA PORT CAUCASUS | SMANN SA FROM RESOURCES OF TRADE AND INDUSTRIAL COMPANY LLC |
| 1/1/2022 | 2710196801 | HEAVY DISTILLATES, FUELS, LIQUID, FOR OTHER PURPOSE, WITH A SULFUR CONTENT OF MORE THAN 2.8 WT.%, FUEL OILS, THE BOILING POINT OF WHICH IS 200 GR.TS OR MORE ACCORDING TO THE ISO 3405 METHOD, BY METHOD A | 3252500 | 2.3 | United Arab Emirates | SEA PORT CAUCASUS | SMANN SA FROM RESOURCES OF TRADE AND INDUSTRIAL COMPANY LLC |
| 1/24/2022 | 2710196601 | HEAVY DISTILLATES, FUELS, LIQUID, FOR OTHER PURPOSE, WITH A SULFUR CONTENT OF MORE THAN 2 WT.%, BUT NOT MORE THAN 2.8 WT.%, FUEL OILS, THE BOILING POINT OF WHICH IS 200 G.C. FRACTIONS DISTILLING TO | 1050000 | 2.6 | United Arab Emirates | SEA PORT CAUCASUS | SMANN SA FROM RESOURCES OF TRADE AND INDUSTRIAL COMPANY LLC |
| 1/24/2022 | 2710196609 | HEAVY DISTILLATES, FUELS, LIQUID, FOR OTHER PURPOSE, WITH A SULFUR CONTENT OF MORE THAN 2 % WT BUT NOT MORE THAN 2.8 WT %, OTHER, BOILING POINT ASTM D 86, NUMBER OF kerosene-gas oil fractions distilling50 .Ts. BY ISO METHOD 3 | 1652500 | 2.6 | United Arab Emirates | SEA PORT CAUCASUS | SMANN SA FROM RESOURCES OF TRADE AND INDUSTRIAL COMPANY LLC |