TECHNOLOGY FOCUS - BIOLOGY - Preferred Components: The biomass is fungi, bacteria, yeast, mold, microalgae, macroalgae or related high moisture agricultural products. The microalgae is e.g. Achnanthes orientalis, Agmenellum spp., Amphiprora hyaline, Amphora coffeaeformis, Linea, Punctata, Taylori, Tenuis, Amphora delicatissima, Amphora delicatissima var, Capitata, Amphora spp., Anabaena, Ankistrodesmus, Ankistrodesmus falcatus, Boekelovia hooglandii, Cyclotella spp., Botryococcus braunii, Botryococcus sudeticus, Bracteococcus minor, Bracteococcus medionucleatus, Carteria, Chaetoceros gracilis, Chaetoceros muelleri, Chaetoceros muelleri var, Chaetoceros spp., Chlamydomonas perigranulata, Chlorella anitrata, Chlorella Antarctica, Chlorella aureoviridis, Chlorella, Candida, Dunaliella spp., Chlorella desiccate, Chlorella ellipsoidea, Chlorella emersonii, Chlorella fusca, Chlorella fusca var, Chlorella zofingiensis, Chlorella trebouxioides, Chlorella vulgaris, Chlorococcum infusionum, Chlorococcum spp., Chlorogonium, Chroomonas spp., Cyclotella meneghiniana, Crocosphaera spp., Crypthecodinium cohnii, Cryptomonas spp., Cyclotella cryptica.    TECHNOLOGY FOCUS - INORGANIC CHEMISTRY - Preferred Components: The acid is acetic acid, hydrochloric acid, nitric acid, phosphoric acid, sulfuric acid, boric acid, hydrofluoric acid, hydrobromic acid, lactic acid, formic acid and/or propionic acid. The base is sodium hydroxide, potassium hydroxide, calcium hydroxide, and other metal hydroxides from the alkali metals and alkaline earth metals, ammonium hydroxide, ammonia, sodium carbonate, potassium carbonate, boron hydroxide, aluminum hydroxide, borax, amino alcohols such as ethanol amine, diethanolamine, triethanol amine, isopropanolamine, diisopropylamine, triisopropylamine, propylamine, 2-propylamine, methylamine, dimethylamine, trimethylamine, dimethylethanol amine, monoethylethanolamine, 2-(2-aminoethoxy)ethanol, diglycolamines, diethylamine and/or other similar polyamines. The polar biomass solution of primary and secondary macronutrients and micronutrients comprise phosphorus, nitrogen, potassium, calcium, sulfur, magnesium, boron, chlorine, manganese, iron, zinc, copper, molybdenum or selenium.    TECHNOLOGY FOCUS - ORGANIC CHEMISTRY - Preferred Process: The step (a) further includes fractionating polar and water soluble components from the biomass; heating the biomass at 25-200 degrees C, 45-150 degrees C, 55-140 degrees C or 60-130 degrees C; a disordering treatment comprising enzymatic treatment, mechanical treatment, electrical treatment, osmotic shock, infection with a lytic virus, exposure to elevated pressure, rapid pressure oscillation conditions and/or vacuum and pressure oscillation; subjecting the biomass to low voltage pulse electric fields with voltage 1-150 volts; and subjecting the biomass to high voltage pulse electric fields with voltage of 150-9000 volts. The step (a) is further defined as adding an acid to the biomass, where the pH is adjusted to 1-6.5; and adding a base to the biomass, where the pH is adjusted to 7.5-14. The step (b) further includes the step of fractionating polar and non-polar components including lipids from the biomass, where the non-polar solvent is carbon tetrachloride, chloroform, cyclohexane, 1,2-dichloroethane, dichloromethane, diethyl ether, dimethyl formamide, ethyl acetate, butane isomers, heptane isomers, hexane isomers, octane isomers, nonane isomers, decane isomers, methyl-tert-butyl ether, pentane isomers, toluene, hexane, heptene, octane, nonene, decene, mineral spirits or 2,2,4-trimethylpentane; and the non-polar solvent further includes relatively the polar solvent in addition to water. The step (b) is further defined as forming a multi-phase suspension including a non-polar solvent solution including hydrophobic lipid compounds, a polar biomass solution including soluble polar compounds, and residual biomass by subjecting the pH adjusted solution and solvent to a mechanical disruption process. The subjecting step is performed by a mechanical disruption process comprising homogenization, sonicating, vortexing, cavitation, shearing, grinding, milling, shaking, mixing, blending and/or hammering. The step (b) further includes the step of applying pulsing electric field to increase intimate contact between biomass and the non-polar solvent. The step (b) is performed at 60-120 degrees C. The partitioning step is further defined as: separating the non-polar solvent solution from the polar biomass solution and residual biomass; and a process comprising centrifugation, variation in pressure, ultrasonification, heating, and adding to the multi-phase suspension an oil-water demulsifying agent. The partitioning step is performed at 25-200 degrees C, 55-180 degrees C or 70-170 degrees C. The partitioning step further includes the step of applying a process comprising electric fields and pulsed electric fields to expedite the separation of polar and non-polar phases. The step (c) is further defined as recovering cell products and products derived from it from the non-polar solvent solution by a process comprising conventional distillation, extractive distillation, azeotropic distillation, evaporation, selective absorption, membrane filtration, centrifugation or filtration, where the non-polar solvent solution is lipid products, hydrocarbon chains or organic compounds (toluene, xylene, styrene, trimethyl-benzene, 2-ethyl-toluene, 1-methyl-3-propopyl-benzene, tetramethyl-benzene, methyl-propenyl-benzene, naphthalene, alkyl substituted naphthalene, heptadecane, heptadecene, 2,2,6,6-tetramethylheptane, 2,5-dimethylheptane, 2,4,6-trimethylheptane, 3,3-dimethyl octane, 2,2,3-trimethylhexane, 2,2,6,6-tetramethylheptane, 2,2,3,4-tetramethylpentane, 2,2-dimethyldecane, 2,2,4,6,6-pentamethylheptane, 2,4,4-trimethylhexane, 4-methyldecene, 4-methyldecane, 3,6-dimethyloctane, 2,6-dimethylundecane, 2,2-dimethylheptane, 2,6,10-trimethyldodecane, 5-ethyl-2,2,3-trimethylheptane, 2,5,6-trimethyldecane, 2,6,11-trimethyldodecane or their isomers). The step (c) is further defined as recovering cell products and cell derived products from the polar biomass solution comprising soluble monosaccharides, disaccharides, oligosaccharides, polysaccharides, glycerols, amino acids, soluble proteins, peptides, fibers, nutrients, phosphocholine, phosphate, growth media, or residual solid algae cell structural particles. The step (c) further includes the step of transesterifying acylglycerols and esterifying free fatty acids. The method further includes the step of recovering the polar biomass solution for use as a base media or aggregate substrate via biological or microbiological digestive processes; and supplementing the polar biomass solution selectively with fixed carbon and nutrients. The method further uses the polar biomass solution post-extraction as liquefaction and saccharification for augmenting solution with cellulosic sugar, fixed carbon and neutralization. In the method, prior to the permeability conditioning step, adding modified starch to the biomass, and making the starch available for biological digestive processes. The method, after step (c), further includes fermenting the polar biomass solution and recovering alcohols, carbon dioxide, lipids or proteins. The method further includes recycling the alcohols back to the conditioning and intimately contacting steps; transesterifying acylglycerols and esterifying free fatty acids, and recycling the alcohols back to the transesterifying step; recycling the carbon dioxide back to algae cultivation; obtaining a post-fermentation fraction and performing iterative fractionation to obtain additional lipids and proteins; and using the base media for biological production comprising heterotrophic feeding algae, bacteria or fungus, where the using step is further described as operating a biological production system that does not consume residual lipid contained within cellular debris enabling iterative or repeat fractionation and operating a biological production system that further liberates valuable nutrients comprising phosphorus, nitrogen or inorganic salts. The method comprises: step (a); intimately contacting the conditioned biomass with at least one non-polar solvent and an alcohol and simultaneously transesterifying acylglycerols and esterifying free fatty acids, partitioning to obtain non-polar solvent solution and a polar biomass solution; step (c); and fermenting the polar biomass solution for recovering products. The method comprises: steps (a) and (b); concentrating valuable compounds dissolved and suspended within the polar biomass solution resulting in a concentrated solution; providing for supplemental fixed carbon and nutrients via liquefaction and saccharification of biomass solids by beneficial use of process acid waters and/or enzymatic hydrolysis; and obtaining a concentrated supplemented media solution. The method comprises: steps (a) and (b); and utilizing a concentrated polar biomass solution as a growth media with an organism comprising a mixotroph, heterotroph, or chemoautotroph. The method comprises: steps (a) and (b), concentrating the polar biomass solution, biologically digesting or fermenting the water based polar solution, and repeating the fractionation process to obtain additional cell products and cell derived products, where the method further includes obtaining residual solids and/or liquids, and recycling to any step in the method; and obtaining purified water and recycling to any step in the method. In the method-1, the growth media contains soluble carbohydrates, proteins, organic acids or phosphates. The method comprises steps (a) and (b), converting organic phosphorus into inorganic phosphate, and recovering the inorganic phosphate. Preferred Components: The polar solvent is a combination of water and one or more polar solvents comprising low molecular weight aldehydes, ketones, fatty acids, methanol, ethanol, propanol, butanol, formic acid, acetic acid, propionic acid or amphipathic solvents. The polar solvent in addition to water is an alcohol comprising amyl alcohols, propanols or butanols, and further includes the step of simultaneously transesterifying acylglycerols and esterifying free fatty acids. The polar biomass solution is alcohols or carbon dioxide. EXAMPLE - Nannochloropsis spp. biomass containing 18.9% dry weight solids, was resuspended in water and the pH was adjusted to 2 by adding a combination (1.3 g) of 50% phosphoric acid and 50% sulfuric acid in a beaker. The mixture was heated to 60 degrees C for 15 minutes with agitation. This combination of chemical and mechanical treatment of algae cells generated a population of partially disrupted (50% cells were disrupted) microalgae cells. Subsequently, a non-polar solvent, hexane, was added to the sample and the mixture was transferred into 1 l hopper and intensely mixed with a high shear mixer for 15 minutes at 40 degrees C. Following the high shear mixing, the mixture was heated to 80 degrees C for 15 minutes in a flask that was connected to a water-cooling reflux condenser for phase partitioning. The phases, once partitioned, were separated by centrifugation. The lipid containing non-polar (hexane) solution formed a layer above an interface layer containing conditioned microalgae cells and residual insolubles and the lower aqueous layer. The non-polar solution was transferred to a clean flask with a pipette, the hexane was distilled and the lipids were collected. The recovered hexane was added back to the mixture containing the microalgae cells, residual insolubles, and the aqueous solution, and then subjected to the high shear mixing once again to fractionate the remaining lipid components. Similar partitioning and phase separation steps were repeated and the second batch of fractionated lipids was combined to the first fractionation to determine the total yield. As result, 33% yields of lipids were harvested.