TECHNOLOGY FOCUS - ORGANIC CHEMISTRY - Preferred Composition: The composition further comprises: the step(s) of the reduction in particle size of the raw woody biomass of Pinaceae and Myrtaceae by applying compressive and shearing forces to the raw woody biomass to create a material that is conducive and efficient for solvent flow and extraction through existing processes for chipping and shearing raw woody biomass; the steps of processing the solvent saturated woody biomass through a final wash of only the bridge solvent, the solvent soluble in both the non-polar solvent and in water e.g. acetone or ethanol in order to push out any remaining lipophilic solvent/wood phytolium mixture in the solvent saturated woody biomass for collection of the liquid fraction solution; the steps of subjecting the liquid fraction solution extracted in the process to a clarification and filtration collection tank for removal of sediment and processing of the liquid fraction of the collected solution by means of a centrifugation system comprised of an array of centrifuges to separate and extract the wood Phytolium hydrocarbon oil from the other components; the steps of subjecting the treated and solvent saturated woody biomass particles to processing within an evaporator/boiler heat exchanger chamber where the remaining solvent would be driven off from the solvent saturated woody biomass particles using heat and or negative pressure for re-use and the woody biomass particles removed for reintroduction to existing end use utilization; and the steps of subjecting the liquid solution extracted from the centrifugation system process to a distillation unit system for refinement of the final product composition by the application of pressure and thermal processes to remove any remaining components from the wood phytolium hydrocarbon solution yielding wood phytolium liquid oil including pinene A and pinene B and other oligomerized pentenes. Preferred Process: The processed woody biomass is subjected to a phased multiwash solvent system preferably using hexane or other non-polar solvent solutions together with a bridge solvent soluble in both the non-polar solvent and water e.g. acetone or ethanol for removal of hydrocarbon oil constituents. The phased multi-wash solvent system is refined by a continuous system of washing solvents through the particulated woody biomass using gravity or pressurized solvent flows to achieve the most economical level of gradient of solvent/hydrocarbon oil mixture for extraction. EXAMPLE - No suitable example given.