NOVELTY - Producing distillate transportation fuels from municipal solid waste and triglycerides, comprises: feeding solid waste stream to treatment zone; obtaining syngas by gasifying refuse derived fuel; obtaining cleaned syngas and passing hydrogen depleted syngas to Fischer-Tropsch synthesis (600) zone; separating vapor stream and liquid streams; combining light liquid stream with triglyceride stream and passing hydrotreated stream to hydroisomerization zone; passing heavy Fischer-Tropsch liquid stream to hydrocracking zone; and co-feeding product streams into fractionating zone (1100).    USE - The process is useful for producing distillate transportation fuels from municipal solid waste and triglycerides.    ADVANTAGE - The process: exhibits improved efficiency, which allows a gasifier to operate at conditions that enhance operability with respect to handling a variety of biomass materials; increases the overall yield of the conversion of triglycerides to transportation fuel; and is unique, integrated and synergistic which allows for fuel specifications, thus minimizing yield loss due to degradation to lower value by-products.    DETAILED DESCRIPTION - Producing distillate transportation fuels from municipal solid waste and triglycerides, comprises: (a) feeding a municipal solid waste stream comprising inorganic material, organic material, and water to a treatment zone, where it is converted to a refuse derived fuel by removing at least a portion of the inorganic material; (b) conducting at least a portion of the refuse derived fuel to a drying zone (200), where the level of water is adjusted to a level that will produce a syngas having a hydrogen to carbon monoxide ratio of 2-2.6 when the refuse derived fuel is gasified, and at least one contaminant; (c) gasifying the refuse derived fuel to produce a syngas containing particulates; (d) treating the syngas to remove at least a portion of any particulates and at least one contaminant comprising hydrogen sulfide, carbonyl sulfide, hydrochloric acid, ammonia, hydrogen cyanide or mercury, resulting in a cleaned syngas; (e) passing the cleaned syngas to a hydrogen recovery (500) zone where hydrogen in excess of the amount needed for downstream Fischer-Tropsch synthesis (600) is removed, resulting in a hydrogen depleted syngas stream; (f) passing at least a portion of the hydrogen depleted syngas stream to a Fischer-Tropsch synthesis zone where it is reacted under Fischer-Tropsch reaction conditions and in the presence of a Fischer-Tropsch catalyst to produce a vapor phase stream, a light liquid stream comprised predominantly of hydrocarbons, where the carbon range is 5-20C, and a heavy liquid stream comprised predominantly of hydrocarbons in the carbon range of 8-20C or more; (g) separating the vapor stream from the liquid streams; (h) combining the light liquid stream with a triglyceride stream and passing the combined stream to a hydrotreating zone (700) where it is subjected to hydrotreating conditions in the presence of a hydrotreating catalyst to produce a hydrotreated liquid hydrocarbon stream substantially free of oxygenates and unsaturated bonds; (i) passing the hydrotreated stream to a hydroisomerization zone where it is subjected to hydroisomerization conditions in the presence of an hydroisomerization catalyst resulting in an isomerized hydrotreated stream containing substantially more branched compounds than the hydrotreated stream before hydroisomerization; (j) passing the heavy Fischer-Tropsch liquid stream from the synthesis zone to a hydrocracking zone where it is subjected to hydrocracking conditions in the presence of a hydrocracking catalyst, to produce a lower boiling product stream boiling primarily in the distillate boiling range; and (k) co-feeding the product streams from the hydrocracking zone and the hydroisomerization zone into a common fractionating zone (1100), to produce at least two predetermined fractions one of which is a distillate boiling range transportation fuel stream.    DESCRIPTION OF DRAWING(S) - The figure shows a block diagram view of a process for producing distillate transportation fuels from municipal solid waste and triglycerides.    Drying zone (200)    Hydrogen recovery (500)    Fischer-Tropsch synthesis (600)    Hydrotreating zone (700)    Fractionating zone (1100)