NOVELTY - Multiphase method for processing organic material in less than 15 days comprises: (a) a first phase where the organic material is hydrolyzed; (b) a second phase overlapping with the first phase where the hydrolyzed material of (a) is subjected to acidogenesis and acetogenesis to obtain material comprising hydrogen, carbon dioxide, volatile organic acids and methanogenic precursors; (c) a third phase overlapping with the second phase; and (d) a fourth phase overlapping with the third phase where the material from (c) is subject to stabilization and reversion.    USE - The multiphase methods are useful for processing organic material in less than 15 days; and for producing microbial output from organic material (all claimed).    ADVANTAGE - The multi-phased bioreactor recognizes the onset and conclusion of biological phases by analysis of phase profiles. Phase profiles and associated phase data sets provide effective controls to recognize phase onset, intra-phase changes, and phase conclusion. The multi-phased bioreactor supports alteration of biological phase occurrences in situ to optimize discrete optimized micro-environments. It provides a comprehensive mechanism to monitor and adapt a physical system to maintain and foster biological phases in an optimum productive environment supporting manufacture of a liquid combination of beneficial bacteria output stabilized as a product.    DETAILED DESCRIPTION - Multiphase method for processing organic material in less than 15 days comprises: (a) a first phase where the organic material is hydrolyzed; (b) a second phase overlapping with the first phase where the hydrolyzed material of (a) is subjected to acidogenesis and acetogenesis to obtain material comprising hydrogen, carbon dioxide, volatile organic acids and methanogenic precursors; (c) a third phase overlapping with the second phase where the methanogenic precursors in the material in (b) are converted to methane and the material in (b) is further subjected to denitrification; and (d) a fourth phase overlapping with the third phase where the material from (c) is subject to stabilization and reversion. INDEPENDENT CLAIMS are: (1) a multiphase bioreactor system for production of a product comprising a microbial consortium from organic material comprising: (a) a first phase space for hydrolysis of organic material; (b) a second phase space for acidogenesis/acetogenesis of organic material from the first phase space, where the second phase space overlaps with the first phase space of (a); (c) a third phase space for methanogenesis of organic material from the second phase space, where the third phase space overlaps from the second phase space of (b); and (d) a fourth phase space for stabilization and reversion of the organic material of (c), where the fourth phase space overlaps with the third phase space of (c); (2) a method for producing microbial output from an organic material comprising applying organic material and working fluid to the multiphase system under conditions sufficient to produce the microbial output in less than about 15 days; or a method for producing microbial output from an organic material comprising applying organic material and working fluid to the bioreactor under conditions sufficient to produce the microbial output in less than about 15 days; (3) a multiphase bioreactor comprising a containment system comprising: (a) a holding tank for mixing working fluid; (b) a complete mix reactor connected to the holding tank for recirculating working fluid; (c) a clarifier connected to the complete mix reactor for separating solids from the working fluid; (d) four or more packed bed reactors for hydrolysis, acidogenesis, acetogenesis, methanogenesis, stabilization and reconstitution of organic material, where each packed bed reactor comprises fixed media, where each packed bed reactor is in fluid communication with at least the adjacent packed bed reactor and where the clarifier connected to the complete mix reactor is in fluid communication with a first packed bed reactor, a packed bed reactor adjacent to the complete mix reactor coupled with a clarifier, where fixed media is secured to the inside of each packed reactor; and (e) a container for deposition of the processed organic material from the reactors and operatively connected to a final packed bed reactor, a packed bed reactor which is at least a fourth packed bed reactor; and (4) a soil amendment obtained by the process; or a soil amendment having the following characteristics: (a) has a pH of about 7.5 to 8; (b) chemical oxygen demand (COD) range of less than about 150 mg/L; (c) conductivity range of about 600 mu S to 1400 mu S; (d) color clear amber between about 500 platinum to cobalt (pt/co) units to about 700 pt/co units in pt/co scale; (e) comprises Syntrophus, Desulfovibrio, Symbiobacterium, Georgfuschia, Thauera, Nitrosomonas, Bellilinea, Sulfuritalea, and Owenweeksia; (f) has a biomass greater than 107 microbes per ml; (g) contains between about 10-60 ng/ml DNA; and (h) comprises at least eight microbial species.