TECHNOLOGY FOCUS - ORGANIC CHEMISTRY - Preferred Process: The process further comprises: manufacturing a fibrous batting mat from the raw biomass of Euphorbia tirucalli by applying compressive and shearing forces to the biomass to create a material that is conducive and efficient for solvent flow and extraction through a 3 step process comprising: (a) the reduction of particle size achieved by application of a hammer mill crushing of the fresh biomass of Euphorbia tirucalli, then, (b) subjecting the crushed raw biomass of Euphorbia tirucalli to shearing forces from a rotating knife blade array to orient the fibrous strands in a parallel arrangement, and then, (c) compressing the strands of the sheared Euphorbia tirucalli by passing the hammered and sheared Euphorbia tirucalli biomass through a series of sets of press rollers to expectorate fluids and prepare the biomass mat for batting; processing the solvent saturated batting mat through an expectoration system of roller presses to prepare the Batting Mat material to be sequentially resubmitted to the phased multi-wash solvent system; completion of the expectoration and extraction of the hydrocarbon oils from the batting mat by subjecting the material to physical and thermal processes to fully extract and drive off the solvents for recovery; subjecting the liquid solution extracted in the process to a centrifugation system comprised of an array of centrifuges to separate and extract the Phytoleum hydrocarbon oil from the other components; and refining the final product by the application of pressure and thermal processes to remove any remaining components from the Phytoleum hydrocarbon oil yielding Phytoleum including Tirucallene A and Tirucallene B and other oligomerized pentenes. The Euphorbia tirucalli processed biomass is amalgamated by the Batt Maker into a Batting Mat comprised of multiple individual layers processed biomass mat layered one atop another to create a fairly uniform biomass layer from the raw biomass. Preferred Components: The batting mat material is subjected to a phased multi-wash solvent system preferably using hexane or other non-polar solvent solutions sequentially selected for removal of hydrocarbon oil constituents. The phased multi-wash system is refined by a continuous system of washing solvents through the Batting Mat using gravity or pressurized solvent flows to achieve the most economical level of gradient of solvent/oil mixture for extraction. The waste biomass bagasse mat would be brought into an evaporator/boiler chamber, where the remaining solvent would be driven off from the batting mat using heat and/or negative pressure. EXAMPLE - None given.