System and method of biocatalytic conversion for production of alcohols, ketones, and organic acids

Abstract

Biocatalytic conversion systems and methods of producing and using same that have improved yields are disclosed. The systems and methods involve co-fermentation of sugars and gaseous substrates for alcohol, ketone, and/or organic acid production. The systems and methods may include biocatalytically converting at least one sugar substrate into at least one of alcohol, at least one ketone, and/or at least one organic acid. The systems and methods may further include biocatalytically converting gases that comprise CO2 and H2 to at least one alcohol and/or at least one organic acid, thereby adding extra revenue to biorefineries.

What is claimed is: 
     
         1 . A biocatalytic conversion system that utilizes a co-fermentation process for sugar and gaseous substrates, the biocatalytic conversion system comprising:
 a first reactor comprising at least one fermentation medium containing at least one first microorganism, wherein the at least one fermentation medium comprises at least one sugar substrate, and wherein the at least one first microorganism comprises a sugar fermenting species that converts sugars into at least one of acetone, butanol, ethanol, isopropanol, acetic acid, and butyric acid, and wherein a gaseous substrate comprising CO 2  and H 2  gases is produced during the fermentation process;   a second reactor comprising at least one medium containing at least one second microorganism, wherein the at least one second microorganism comprises a gas fermenting species that converts CO 2  and H 2  gases into at least one of an alcohol and an organic acid; and   a gas line connecting the first reactor to the second reactor for feeding the gaseous substrate produced in the first reactor into the second reactor.   
     
     
         2 . The biocatalytic conversion system of  claim 1 , wherein each of the first and second microorganisms comprises one or more species of microorganisms, and wherein each species is from a genus selected from the group consisting of  Clostridium, Butyribacterium, Eubacterium, Moorella, Acetobacterium, Enterobacter, Bacillus, Anaerobaculum, Alkalibaculum , and combinations thereof. 
     
     
         3 . The biocatalytic conversion system of  claim 2 , wherein at least one of:
 the first microorganism comprises at least one of  Clostridium acetobutylicum, Bacillus firmus, Anaerobaculum hydrogeniformans , and  Clostridium beijerinckii ; and   the second microorganism comprises at least one of  Clostridium ragsdalei, Clostridium autoethanogenum, Clostridium carboxidivorans, Clostridium ljungdahlii , and  Alkalibaculum bacchi.      
     
     
         4 . The biocatalytic conversion system of  claim 3 , wherein at least one of:
 the at least one first microorganism comprises  Clostridium acetobutylicum  ATCC 824;   the at least one second microorganism comprises  Clostridium ragsdalei  P11, and wherein ethanol, acetic acid, and isopropanol are produced in the reactor containing the at least one second microorganism; and   the at least one second microorganism comprises  Clostridium carboxidivorans , and wherein ethanol, butanol, hexanol, butyric acid, acetic acid, and hexanoic acid are produced in the reactor containing the at least one second microorganism.   
     
     
         5 . The biocatalytic conversion system of  claim 1 , wherein the at least one sugar substrate present in the fermentation medium is selected from the group consisting of glucose, fructose, sucrose, xylose, galactose, arabinose, mannose, and combinations thereof. 
     
     
         6 . The biocatalytic conversion system of  claim 1 , wherein the at least one fermentation medium comprises at least one raw material selected from the group consisting of a sugar, a starch, cellulose, hemicellulose, other carbohydrates, glucan, xylan, galactan, mannan, cellobiose, lignocellulosic biomass, and combinations thereof. 
     
     
         7 . The biocatalytic conversion system of  claim 1 , wherein the at least one fermentation medium contains a feedstock selected from the group consisting of switchgrass, forage sorghum, redcedar, woody materials, and combinations thereof, and wherein the feedstock has been pretreated and hydrolyzed prior to placement of the feedstock in the at least one fermentation medium. 
     
     
         8 . The biocatalytic conversion system of  claim 1 , wherein the biocatalytic conversion system produces at least one alcohol, at least one ketone, and at least one organic acid. 
     
     
         9 . The biocatalytic conversion system of  claim 1 , wherein the gas line connects a headspace of the first reactor to a headspace of the second reactor. 
     
     
         10 . The biocatalytic conversion system of  claim 1 , wherein at least one of:
 the first reactor is maintained at a temperature in a range of from about 20° C. to about 45° C., and a pH of the at least one fermentation medium is maintained in a range of from about 4 to about 7.5, and wherein the second reactor is maintained at a temperature in a range of from about 20° C. to about 45° C., and a pH of the at least one fermentation medium is maintained in a range of from about 4 to about 7; and   external CO and/or H 2  gas is fed into the reactor containing the at least one second microorganism.   
     
     
         11 . A method of biocatalytic conversion that utilizes a co-fermentation process for sugar and gaseous substrates, the method comprising the steps of:
 contacting at least one fermentation medium with at least one first microorganism in a first reactor, wherein the at least one fermentation medium comprises at least one sugar substrate, and wherein the at least one first microorganism converts the at least one sugar substrate into at least one of acetone, butanol, ethanol, isopropanol, acetic acid, and butyric acid, and wherein a gaseous substrate comprising CO 2  and H 2  gases is produced during the fermentation process; and   feeding the gaseous substrate produced in the first reactor into a second reactor, the second reactor comprising at least one medium containing at least one second microorganism, wherein the at least one second microorganism converts CO 2  and H 2  gases into at least one of an alcohol and an organic acid.   
     
     
         12 . The method of  claim 11 , wherein each of the first and second microorganisms comprises one or more species of microorganisms, wherein each species is from a genus selected from the group consisting of  Clostridium, Butyribacterium, Eubacterium, Moorella, Acetobacterium, Enterobacter, Bacillus, Anaerobaculum, Alkalibaculum , and combinations thereof. 
     
     
         13 . The method of  claim 12 , wherein at least one of:
 the first microorganism comprises at least one of  Clostridium acetobutylicum, Bacillus firmus, Anaerobaculum hydrogeniformans , and  Clostridium beijerinckii ; and   the second microorganism comprises at least one of  Clostridium ragsdalei, Clostridium autoethanogenum, Clostridium carboxidivorans, Clostridium ljungdahlii , and  Alkalibaculum bacchi.      
     
     
         14 . The method of  claim 13 , wherein at least one of:
 the at least one first microorganism comprises  Clostridium acetobutylicum  ATCC 824;   the at least one second microorganism comprises  Clostridium ragsdalei  P11, and wherein ethanol, acetic acid, and isopropanol are produced in the reactor containing the at least one second microorganism; and   the at least one second microorganism comprises  Clostridium carboxidivorans , and wherein ethanol, butanol, hexanol, butyric acid, acetic acid, and hexanoic acid are produced in the reactor containing the at least one second microorganism.   
     
     
         15 . The method of  claim 11 , wherein the at least one sugar substrate present in the fermentation medium is selected from the group consisting of glucose, fructose, sucrose, xylose, galactose, arabinose, mannose, and combinations thereof. 
     
     
         16 . The method of  claim 11 , wherein the at least one fermentation medium comprises at least one raw material selected from the group consisting of a sugar, a starch, cellulose, hemicellulose, other carbohydrates, glucan, xylan, galactan, mannan, cellobiose, lignocellulosic biomass, and combinations thereof. 
     
     
         17 . The method of  claim 11 , wherein the at least one fermentation medium contains a feedstock selected from the group consisting of switchgrass, forage sorghum, redcedar, woody materials, and combinations thereof, and wherein the method further comprises the step of pretreating and hydrolyzing the feedstock prior to contact with the at least one first microorganism. 
     
     
         18 . The method of  claim 11 , further defined as producing at least one alcohol, at least one ketone, and at least one organic acid. 
     
     
         19 . The method of  claim 11 , wherein the first reactor is maintained at a temperature in a range of from about 20° C. to about 45° C., and a pH of the at least one fermentation medium is maintained in a range of from about 4 to about 7.5, and wherein the second reactor is maintained at a temperature in a range of from about 20° C. to about 45° C., and a pH of the at least one fermentation medium is maintained in a range of from about 4 to about 7. 
     
     
         20 . The method of  claim 11 , further comprising the step of feeding additional CO and/or H 2  gas into the reactor containing the at least one second microorganism.