US2015104835A1PendingUtilityA1

Static solid state bioreactor and method for using same

Assignee: GEOSYNFUELS LLCPriority: Apr 14, 2009Filed: Sep 16, 2014Published: Apr 16, 2015
Est. expiryApr 14, 2029(~2.7 yrs left)· nominal 20-yr term from priority
C05F 17/979C05F 17/95C05F 17/986Y02P20/145Y02P20/582C12M 23/36C12P 5/023C12M 33/14C12P 7/06C12M 21/16C12P 19/02C12P 7/14C12M 29/02C12P 3/00C12M 33/16C12M 23/02C12M 21/04B09B 3/60B09B 3/65Y02W30/40Y02E50/30Y02E50/10
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Claims

Abstract

A static solid state bioreactor and method of using same. The bioreactor comprises a vessel having an upper end and a lower end, the upper end having a sealable opening. A gas distribution system in communication with the upper end and the lower end of the vessel. A liquid distribution system in communication with the upper end of the vessel. A liquid recovery system in communication with the lower end of the vessel. A material removal system disposed at the lower end of the vessel for removing biomass from the vessel.

Claims

exact text as granted — not AI-modified
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         17 . A method of performing static solid state fermentation, the method comprising the steps of:
 a. mixing a bulking agent with a biomass to form a mixture;   b. adding the mixture to a static solid state bioreactor;   b. irrigating the mixture with an aqueous solution;   c. flowing a gas through the mixture; and,   d. maintaining a microorganism supporting environment within the mixture by calculating a specific heat of an aqueous solution flow, calculating a specific heat of a gas flow, and balancing the aqueous solution flow with the gas flow.   
     
     
         18 . The method according to  claim 17 , further comprising the step of maintaining a ratio of mass flow per cross sectional area per unit time of the gas flow to the aqueous solution flow between 0.25 and 0.4. 
     
     
         19 . The method according to  claim 17 , further comprising the step of adding an inoculum comprising at least one microorganism to the biomass prior to the step of mixing a bulking agent with a biomass. 
     
     
         20 . The method according to  claim 19 , further comprising the step of adding one or more enzymes to the biomass prior to the step of adding an inoculum to the biomass. 
     
     
         21 . The method according to  claim 20 , further comprising the step of adding an antibiotic to the biomass prior to the step of adding enzymes to the biomass. 
     
     
         22 . The method according to  claim 17 , further comprising the step of collecting the liquid solution from a lower end of the biomass and recycling the liquid solution back on to an upper end of the mixture. 
     
     
         23 . The method according to  claim 22 , further comprising the step of treating the liquid solution to improve quality before recycling the liquid solution back on to an upper end of the mixture. 
     
     
         24 . The method according to  claim 17 , wherein the bulking agent maintains a hydraulic conductivity of the mixture greater than 10 −4  cm/sec. 
     
     
         25 . The method according to  claim 17 , wherein the bulking agent limits the gas flow back-pressure to less than 200 mm of water head. 
     
     
         26 . The method according to  claim 17 , further comprising the step of reversing the direction of a gas flow through the mixture. 
     
     
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