Membrane supported bioreactor for conversion of syngas components to liquid products

Abstract

Ethanol and other liquid products are produced by contacting syngas components such as CO or a mixture of CO 2 and H 2 with a surface of a membrane under anaerobic conditions and transferring these components into contact with a biofilm on the opposite side of the membrane. These steps provide a stable system for producing liquid products such as ethanol, butanol and other chemicals. The gas fed on the membrane's gas contact side transports through the membrane to form a biofilm of anaerobic microorganisms that converted the syngas to desired liquid products. The system can sustain production with a variety of microorganisms and membrane configurations.

1 . A process for converting a feed gas containing at least one of CO or a mixture of CO 2  and H 2  under anaerobic conditions to a liquid product comprising at least one of ethanol, propanol, n-butanol, acetic acid, propionic acid and butyric acid:
 a) passing a feed gas comprising a mixture of at least one of CO or a mixture of CO 2  and H 2  under anaerobic conditions to a gas contacting side of a bio-support membrane for transferring the feed gas across the membrane to a biofilm support side of the bio-support membrane;   b) circulating a fermentation liquid on a biofilm support side of the bio-support membrane, the fermentation liquid having a redox potential of less than −200 mV;   c) maintaining a biofilm consisting essentially of anaerobic microorganisms on the biofilm support side of the bio-support membrane to convert at least a portion of the feed gas components to a liquid product comprising at least one of ethanol, propanol, n-butanol, acetic acid, propionic acid and butyric acid;   d) maintaining a pressure differential across the bio-support membrane that avoids the formation of bubbles in the fermentation liquid; and,   e) recovering a liquid product from the fermentation liquid.   
     
     
         2 . The process of  claim 1  wherein the bio-support membranes comprises a micro porous membrane and/or a non-porous membrane. 
     
     
         3 . The process of  claim 1  wherein the microorganism produces a liquid product comprising ethanol. 
     
     
         4 . The process of  claim 1  wherein the feed gas is synthesis gas having an oxygen concentration of less than 1000 ppm, the fermentation liquid has a redox potential in the range of −300 mV to −500 mV and the biofilm support side of the membrane supports a microorganism that produces ethanol. 
     
     
         5 . The process of  claim 1  wherein the fermentation liquid contains one or more dissolved gases for contact with the biofilm and the dissolved gases include at least one of CO and CO 2  and H 2 . 
     
     
         6 . The process of  claim 1  wherein the fermentation liquid is agitated against the biofilm support side of the biosupport membrane to provide shear forces to control the thickness of the biofilm. 
     
     
         7 . The process of  claim 1  wherein the feed gas passes serially through multiple bio-support membranes, the process includes at least one feed gas chamber for each bio-support membrane and CO 2  is removed from the feed gas as it passes between bio-support membranes. 
     
     
         8 . The process of  claim 1  wherein the bio-support membrane is hydrophobic. 
     
     
         9 . The process of  claim 1  wherein the bio-support membrane comprises a plurality of hollow fiber membranes and a feed gas chamber that includes the collective lumen volume of the fibers distributes the feed gas to lumens of the membranes in the bio-support membrane. 
     
     
         10 . The process of  claim 7  wherein a liquid chamber retains the fermentation liquid on the gas contacting side of the bio-support membrane and the liquid chamber includes hollow fibers membranes for removing dissolved CO 2  from the liquid phase. 
     
     
         11 . The process of  claim 1  wherein the microorganisms maintained on the bio-support membrane consist essentially of a mono-culture or a co-culture of at least one of  Clostridium Ragsdalei, Clostridium autoethanogenum, Clostridium Coskatii, Butyribacterium methylotrophicum , and  Clostridium Ljungdahlii.    
     
     
         12 . The process of  claim 1  wherein the microorganisms maintained on the bio-support side of the membrane consist essentially of anaerobic microorganisms from the genus  Clostridium.    
     
     
         13 . The process of  claim 1  wherein the microorganisms consist essentially of a mono-culture of anaerobic microorganisms from the genus  Clostridium.    
     
     
         14 . The process of  claim 1  wherein a continuous flow of feed gas having an oxygen concentration of less than 100 ppm passes across the gas contact side of the bio-support membrane. 
     
     
         15 . A process for converting a feed gas containing at least one of CO or a mixture of CO 2  and H 2  to a liquid product comprising:
 a) delivering feed gas to a gas distribution chamber;   b) distributing the feed gas from the distribution chamber to the lumens of a plurality of hollow fiber membranes;   c) surrounding the plurality of hollow fiber membranes with a fermentation liquid having a redox potential of less than −200 mV;   d) maintaining a biofilm consisting essentially of anaerobic microorganisms from the genus  Clostridium  on the outer surface of the plurality of hollow fiber membranes for producing liquid products from the synthesis gas;   e) diffusing feed gas from the lumens across the membrane and into the biofilm to convert at least a portion of the synthesis gas to liquid products comprising at least one of ethanol, propanol, n-butanol, acetic acid, propionic acid and butyric acid;   f) maintaining a pressure differential across the bio-support membrane that prevents the formation of bubbles of feed gas components from the lumens in the fermentation liquid; and   g) passing a portion of the fermentation broth to a separation zone and recovering liquid products from the separation zone.   
     
     
         16 . The process of  claim 15  wherein the hollow fiber membranes comprise a micro porous membrane and/or a non-porous membrane. 
     
     
         17 . The process of  claim 15  wherein the feed gas comprises synthesis gas and the microorganisms produce a liquid product comprising at least one of ethanol, n-butanol, acetic acid, and butyric acid. 
     
     
         18 . The process of  claim 15  wherein the feed gas has an oxygen concentration of less than 100 ppm, the fermentation liquid has a redox potential in the range of from −300 mV to −500 mV, the microorganism produces ethanol and the separation zone recovers an ethanol containing liquid. 
     
     
         19 . The process of  claim 15  wherein the fermentation liquid contains one or more dissolved gases comprising one or more components of the synthesis gas that enter the fermentation liquid in solution. 
     
     
         20 . The process of  claim 15  wherein feed gas passes serially through a plurality of gas distribution chambers that each distribute feed gas to a plurality of hollow fiber membranes, the process includes a collection chamber for each distribution chamber that serially receives feed gas discharged from the lumens of the plurality of hollow fiber membranes, and CO 2  is removed from the feed gas as it passes from at least one collection chamber to at least one distribution chamber. 
     
     
         21 . The process of  claim 15  wherein the microorganism maintained on the bio-support membrane consist essentially of a mono-culture or a co-culture of at least one of  Clostridium Ragsdalei, Clostridium autoethanogenum, Clostridium Coskatii , and  Clostridium Ljungdahlii.