The invention relates to a process for the production of jet fuel from synthetic crude produced by a Fischer-Tropsch process. increases multiple alkylation of aromatics with ethylene to produce aromatics in the kerosene boiling range, while reducing the ethylene in the product. A process as claimed in any one of the preceding claims, wherein the alkylation process e. avoids co-production of binuclear aromatics.ġ0. A process as claimed in claim 8, wherein the aromatization process d. produces H 2, Benzene, Toluene, Ethylbenzene, Xylene, and kerosene range aromatics.ĩ. A process as claimed in claim 6 or claim 7, wherein the aromatization process d. A process as claimed in claim 6, wherein the aromatization process d converts Naphtha from hydrocracking process a.Ĩ. is selected to produce aromatics and not octane as such.ħ. A process as claimed in any one of the preceding claims, wherein the aromatization process d. removes olefins and additionally removes oxygenates to produce kerosene.Ħ. A process as claimed in any one of the preceding claims, wherein the hydrotreating process c. is selected to oligomerise a C3 to C8 FT syncrude fraction to kerosene range hydrocarbons while maintaining and/or imparting cold flow properties.ĥ. A process as claimed in any one of the preceding claims, wherein the oligomersation process b. A process as claimed in claim 1, wherein processes d. A process as claimed in claim 1, wherein the conversion processes b. alkylating one or more of an FT syncrude fraction including hydrocarbons in the C2 to C6 range, a product from process b., and a product from process d.Ģ. aromatizing one or more of an FT syncrude fraction including hydrocarbons in the range C2 to C8, a product from process a., a product from process b, a product from process c., and a product from an aromatic alkylation process and e. hydrotreating one or more of an FT syncrude fraction, a product from process b., and an alkylated FT syncrude fraction d. oligomerising an FT syncrude fraction including hydrocarbons in the range C2 to C8 c. hydrocracking one or more of a FT kerosene and heavier material fraction and a C9 and heavier FT syncrude fraction b. A Fischer-Tropsch jet fuel refining process which has a jet fuel yield in excess of 60% by mass, said process including at least four of the following five conversion processes: a. SYSTEM AND METHOD FOR OPTIMIZING DILUENT RECOVERY BY A DILUENT RECOVERY UNITīitumen Supply and Grading Method and ApparatusĭESULFURIZATION AND DENITROGENATION WITH IONIC LIQUIDS AND METAL ION SYSTEMSġ.

High viscosity index wide-temperature functional fluid compositions and methods for their making and use Process for desulphurising and dewaxing a hydrocarbon feedstock boiling in the gasoil boiling range METHOD FOR DEWAXING HYDROCARBON OIL AND METHOD FOR PRODUCING LUBRICATING-OIL BASE OIL Integrated Processes For Recovery of Hydrocarbon From Oil Sands METAL SULPHONATE ADDITIVES FOR FOULING MITIGATION IN PETROLEUM REFINERY PROCESSES HYDROPROCESSING FOR DISTILLATE PRODUCTION

Jet a1 density vs temperature table