Продаем JP 54 FOB ROTTERDAM

Delivery Terms: FOB Rotterdam.Origin: Russian Federation. Product: Aviation Kerosene Colonial Grade 54 Jet Fuel.Total Quantity: 26,000,000 BBLS (Twenty six Million BBLS) with possible roll over and extension +/-5%Contract: Spot of 1,000,000 barrels, possible roll over and extension.Price Basis: NWE Platt minus $7.0 Gross per barrel / NWE Platt minus $ 6.0 Net per barrel1. Buyer issue ICPO to seller mandate.2. Seller issues Draft Contract and Commercial Invoice for buyer to countersign upon acceptance of the terms and conditions. 3 Seller issue to buyer the below listed document: a. Certificate of origin of the product.b. Product Passportd. Commitment to supply and product availability in storage reservoir.4. Seller and Buyer endorse the Tank Storage Agreement (TSA) with the hired tank facilitator of the respective port Tank Farm.(Seller and Buyer’s company are to jointly sign the Tank Storage Agreement (TSA) and jointly pay the tank fee to the tank farm to enable seller Pump/Inject the product into the tank to enable buyer conduct dip test.5. Seller issue to buyer the below listed document:a. Dip-Test Authorization.b. SGS or SAYBOLT or INTERTEKc. Pipeline injection report d. Certificate of Conformity of the Producte. NCNDA to all intermediaries.6. Upon successful dip test, buyer makes payment by MT103 T/T wire transfer for the total product available.7. Seller pays commission to intermediaries involved in the transactionJP54 AVIATION KEROSENE COLONIAL GRADE 54 JET FUEL GOST 10227/86№ Indicator Provision of technical regulations (application number 4) standard GOSТ 10227-86 сodе 0251210205 Аctually1 Density at 20 °C, kg/m3, not less than 780 7892 Fractional composition: starting the distillation temperature, ° C, not higher 150 133 10% was distilled off at a temperature, ° C, not higher 205 165 158 50% was distilled off at a temperature, ° C, not higher 195 183 90% was distilled off at a temperature, ° C, not higher 300 230 213 98% was distilled off at a temperature, ° C, not higher 250 237 the remainder of the distillation,%, not more 1,5 1,5 1,0 losses from distillation,%, not more 1,5 1,5 0,53 Kinematic viscosity, mm2 / s (cCt) at temperature 20° C , not less than 1,30(1,30) 1,36 minus 20 ° C, mm2 / s , no more 8 8 34 Net calorific value kJ / kg, not less than 43120 432035 Smoke point, mm ,not less than 25 25 256 Acidity, mg KOH per 100cm3 of fuel, no more 0,7 0,17 Iodine number g iodine per 100 g of fuel, no more 0,2 0,48 Flash point in a closed crucible, °C, not less 28 28 429 Crystallization start temperature, ° C, not higher Minus50 -60 -6010 Thermal stability under static conditions at 150 °C, not more Concentration sludge, mg 100cm3 fuel 18 511 Volume (mass) fraction of aromatic hydrocarbons,%, not more 25 20(22) 16(18)12 Actual resin concentration in mg per 100 cm3 of fuel, not more than 7 3 absence13 The mass fraction of the total sulfur,%, not more 0,25 0,20 0,0414 The mass fraction of mercaptan sulfur,%, not more 0,003 0,003 0,00115 the mass fraction of hydrogen sulfide absence absence16 test on a copper plate at 100 °C for 3:00 stand stand17 Ash,%, not more 0,003 absence18 Сontent of water-soluble acids and alkalis absence absence19 Сontent of solids and water absence absence absence20 Reaction with water, tenths, no more: status of the interface 1 1 the state of the separated phases 1 121 Electrical conductivity S m/m, not more than: without anti-static additive at a temperature of 20 °C 10 10 1 with an antistatic additive (at refueling aircraft) in the range 50-600 50-600 22 thermal stability at the reference temperature 260 °C, no less filter pressure drop, mm Hg, not more than 25 25 0 color scale on the tube, the scores on the color scale (in the absence of atypical deposits), not more 3 3 Less than 1