# US 8,541,214 B2 · Method of conversion of syngas using microorganism on hydrophilic membrane > Agents: this data is available as JSON from the patentgrep API and MCP server — see https://patentgrep.com/llms.txt - Number: US 8,541,214 B2 - Document ID: US8541214B2 - Status: Granted - Kind: B2 - Application number: 13/084,318 - Filed: 2011-04-11 - Published: 2011-07-28 - Granted: 2013-09-24 - Earliest claimed: 2007-06-08 - Assignees: Coskata, Inc. - Applicants: Robert Hickey; Rahul Basu; Rathin Datta; Shih-Perng Tsai - Inventors: Robert Hickey; Rahul Basu; Rathin Datta; Shih-Perng Tsai - Web page: https://patentgrep.com/patent/US8541214B2 ## CPC - C12M 29/16: {Hollow fibers (hollow fiber modules in general B01D63/02)} - C12M 21/12: {for producing fuels or solvents (C12M21/04 takes precedence; liquid carbonaceous fuels C10L1/00, solid fuels C10L5/00)} - C12M 25/10: {Hollow fibers or tubes (hollow fiber modules in general B01D63/02)} - C12P 7/04: acyclic - Y02E 50/10: Biofuels, e.g. bio-diesel - C12M: APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; {APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS} - C12P: FERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE {(brewing of beer C12C; producing vinegar C12J; producing specific peptides or proteins C07K; producing enzymes C12N9/00; DNA or RNA concerning genetic engineering, vectors, e.g. plasmids, or their isolation, preparation or purification C12N15/00; measuring or testing processes involving enzymes or microorganisms C12Q; measuring or testing processes involving nucleic acid amplification reactions C12Q1/6844; fermentation processes to form a food composition, A21 or A23; compounds in general, see the relevant compound class, e.g. C01, C07)} - Y02E: REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION ## Abstract A stable system for producing liquid products such as ethanol, butanol and other chemicals from syngas components contacts CO or a mixture of CO2 and H2 with a hydrophilic membrane under anaerobic conditions and transfers these components into contact with microorganisms contained as a biofilm on the membrane. Maintaining the microorganisms as a biolayer on the surface of the membrane facilitates cleaning of the membrane surface that retains the biofilm. In addition the shell gas space that surrounds the membranes may be flooded to reduce or remove the biofilm. Agitation of the liquid, by for example the bubbling of gas in the surrounding shell space, can fully or partially remove the biofilm from the membrane. ## Claims ### Claim 1 A process for converting a feed gas comprising syngas and containing at least one of CO or a mixture of CO2 and H2 to a liquid product under anaerobic conditions, said process comprising: a) passing an aqueous seeding solution comprising a monoculture of microorganisms into contact with a gas contacting side of a hydrophilic membrane, passing a liquid portion of the aqueous seeding solution through the membrane and retaining, on the gas contacting side of the membrane, the microorganisms consisting essentially of a monoculture of an anaerobic microorganism, with the gas contacting side serving as an exclusion surface to inhibit penetration of the microorganisms into the membrane and to provide the anaerobic microorganisms as immobilized microorganisms; b) growing a biofilm comprising the immobilized microorganisms of the monoculture on the surface of the gas contacting side of the membrane by passing a feed gas comprising CO or a mixture of CO2 and H2 into contact with the monoculture of microorganisms on the gas contact side of the membrane and permeating a fermentation liquid from a liquid contacting side of the membrane, defined by the face of the membrane opposite the gas contacting side, through the membrane and into contact with the immobilized microorganisms wherein the gas contacting side of the membrane serves as a biofilm exclusion surface to inhibit penetration of the biofilm into the membrane, and the feed gas has an oxygen concentration of less than 1000 ppm; c) producing liquid products under autotrophic conditions by contacting the biofilm with the feed gas, permeating the fermentation liquid from the liquid contacting side through the membrane and into contact with the biofilm, and permeating liquid products from the biofilm across the membrane and into the fermentation liquid, wherein a liquid retention chamber retains the fermentation liquid into contact with the liquid contacting side of the membrane, and the fermentation liquid has a redox potential of less than −200 mV; and, d) collecting fermentation liquid containing liquid products from the liquid retention chamber to recover liquid products from the process. ### Claim 2 (depends on 1) The process of claim 1 wherein the biofilm exclusion surface has pores with effective diameters of no greater than 0.5 μm to inhibit penetration of the biofilm into the pores. ### Claim 3 (depends on 1) The process of claim 1 wherein the biofilm exclusion surface has pores with a sufficient tortuosity to inhibit penetration of the biofilm into the pores. ### Claim 4 (depends on 1) The process of claim 1 wherein the biofilm extends into the biofilm exclusion surface by no more than 10 μm. ### Claim 5 (depends on 1) The process of claim 1 wherein a feed gas chamber in fluid communication with the gas contacting side of the membrane supplies the feed gas to the membrane. ### Claim 6 (depends on 1) The process of claim 1 wherein the hydrophilic membrane comprises a monolayer having a thickness of from 0.05 to 0.8 mm and an effective pore diameter of from 0.01 to 0.5 μm. ### Claim 7 (depends on 1) The process of claim 1 wherein the anaerobic microorganism produces a liquid product comprising at least one of ethanol, n-butanol, hexanol, acetic acid, and butyric acid. ### Claim 8 (depends on 1) The process of claim 1 wherein the feed gas is synthesis gas having an oxygen concentration of less than 100 ppm, the biofilm comprises microorganisms that produce ethanol and a liquid recovery chamber retains an ethanol containing liquid. ### Claim 9 (depends on 1) The process of claim 1 wherein the hydrophilic membrane comprises a plurality of hollow fiber membranes with the fermentation liquid and liquid product flowing through the lumens of the hollow fiber membranes and the feed gas flowing over the outside of the hollow fiber membranes. ### Claim 10 (depends on 8) The process of claim 8 wherein the feed gas passes serially through multiple assemblies of hollow fiber membranes, at least one feed gas chamber supplies feed gas for each hollow fiber membrane assembly and CO2 is removed from the gas as it passes between assemblies through the system. ### Claim 11 (depends on 1) The process of claim 1 wherein the microorganisms comprise a mono-culture of one of Clostridium ragsdalei, Butyribacterium methylotrophicum, Clostridium ljungdahlii, Clostridium autoethanogenum, Clostridium woodii and Clostridium carboxydivorans. ### Claim 12 (depends on 1) The process of claim 1 wherein the hydrophillic membrane comprises at least one of poly(vinylidene fluoride) (PVDF), polyethylene (PE), polypropylene (PP), poly(vinyl chloride) (PVC), polysulfone (PS), and polyethersulfone (PES). ### Claim 13 (depends on 1) The process of claim 1 wherein the hydrophilic membrane comprises a composite having a biofilm support layer and a liquid contacting layer of two different materials. ### Claim 14 (depends on 1) The process of claim 1 wherein the biofilm exclusion surface comprises a skin having a thickness of no more than 5 μm on the outside of a membrane layer and the skin has a pore size of less than 0.5 μm. ### Claim 15 (depends on 1) The process of claim 1 wherein the gas contacting side of the membrane is temporarily flooded with liquid to remove at least a portion of the biofilm or material from the biofilm. ### Claim 16 (depends on 15) The process of claim 15 wherein a gas stream is passed along the gas contacting side of the membrane while it is in the flooded condition to create turbulence in the liquid adjacent the biofilm to remove the biofilm or control its thickness. ### Claim 17 (depends on 1) The process of claim 1 wherein the pressure difference between the liquid stream and the feed gas is regulated to control the liquid flow through the membrane to the biofilm and control its thickness. ### Claim 18 A process for converting a feed gas comprising syngas and containing at least one of CO or a mixture of CO2 and H2 to a liquid product under anaerobic conditions and recovering the liquid product with a fermentation liquid, said process comprising: a) passing a seeding solution comprising the liquid of the seeding solution and a monoculture of anaerobic microorganisms into contact with the outside side surface of a hydrophilic hollow fiber membrane having a central lumen, draining the liquid of the seeding solution from the outside surface of membrane through the central lumen to immobilize the microorganisms and retaining immobilized microorganisms consisting essentially of the monoculture of anaerobic microorganisms on the outside surface of the membrane which serves as an exclusion surface to inhibit penetration of the microorganisms into the membrane; b) growing a biofilm comprising the immobilized microorganisms of the monoculture on the outside surface of the membrane by passing a feed gas comprising CO or a mixture of CO2 and H2 into contact with the monoculture of microorganisms on the outside surface of the membrane and permeating a fermentation liquid from the outside surface through the membrane and into contact with the immobilized microorganisms wherein the outside surface of the membrane serves as an exclusion surface to inhibit penetration of the biofilm to no more than 10 μm beyond the membrane surface into the membrane and the feed gas has an oxygen concentration of less than 1000 ppm; c) producing liquid products under autotrophic conditions by contacting the biofilm with the feed gas, permeating the fermentation liquid from the lumen of the membrane through the membrane and into contact with the biofilm, and permeating liquid products from the biofilm across the membrane and into the fermentation liquid, wherein a liquid retention chamber retains the fermentation liquid, and the fermentation liquid has a redox potential of less than −200 mV; d) collecting fermentation liquid containing liquid products from the liquid retention chamber to recover liquid products from the process; and, e) periodically increasing the pressure of the fermentation liquid to create liquid flow from the central lumen through the membrane and to the outside of the membrane to purge microorganisms from the membrane. ### Claim 19 (depends on 18) The process of claim 18 wherein the feed gas passes serially through multiple assemblies of hollow fiber membranes, at least one feed gas chamber supplies feed gas for each hollow fiber membrane assembly and CO2 is removed from the feed gas as it passes from one assembly to the next through the system. ### Claim 20 (depends on 1) The process of claim 1 wherein the microorganisms comprise a mono-culture of one of Clostridium ragsdalei, Butyribacterium methylotrophicum, Clostridium ljungdahlii, Clostridium autoethanogenum, Clostridium woodii and Clostridium carboxydivorans. ### Claim 21 (depends on 18) The process of claim 18 wherein a continuous flow of feed gas having an oxygen concentration of less than 100 ppm passes across the gas contact side of the hydrophilic membrane. ### Claim 22 (depends on 19) The process of claim 19 wherein the hydrophilic membrane comprises at least one of poly(vinylidene fluoride) (PVDF), polyethlylene (PE), polypropylene (PP), poly(vinchloride) (PVC), polysulfone (PS), and polyethersulfone (PES). ### Claim 23 (depends on 18) The process of claim 18 wherein a feed gas chamber houses the hollow fiber membrane and the feed gas chamber is occasionally flooded with liquid to remove at least a portion of the biofilm or material from the biofilm and while the feed gas chamber is flooded a gas stream is passed through the feed gas chamber along the membrane to sparge the biofilm and control its thickness. ### Claim 24 A process for converting a feed gas comprising syngas and containing at least one of CO or a mixture of CO2 and H2 to a liquid product under anaerobic conditions and recovering the liquid product with a fermentation liquid, said process comprising: a) passing a seeding solution comprising a monoculture of microorganisms to a feed gas chamber that houses a plurality of hydrophilic hollow fiber membranes and into contact with the outside side surface of hollow fiber membrane, raising the pressure on the outside of the membranes relative to the lumens to drain the liquid from feed gas chamber through a central lumen of the hollow fibers to immobilize the microorganisms and retaining immobilized microorganisms consisting essentially of the monoculture of an anaerobic microorganism on the outside surface of the membrane which has pores therein of a size of 0.5 μm or less for inhibiting penetration of the microorganisms into the pores such that the membrane surface provides an exclusion surface to inhibit penetration of the microorganisms into the membrane; b) growing a biofilm comprising the immobilized microorganisms of the monoculture on the outside surface of the membrane by passing a feed gas comprising CO or a mixture of CO2 and H2 into contact with the monoculture of microorganisms on the outside surface of the membrane and permeating a fermentation liquid from the outside surface through the membrane and into contact with the immobilized microorganisms wherein the outside surface of the membrane serves as an exclusion surface to inhibit penetration of the biofilm to no more than 10 μm beyond the membrane surface into the membrane and the feed gas has an oxygen concentration of less than 1000 ppm; c) producing liquid products under autotrophic conditions by contacting the biofilm with the feed gas, permeating the fermentation liquid from the lumen of the membrane through the membrane and into contact with the biofilm, and permeating liquid products from the biofilm across the membrane and into the fermentation liquid, wherein a liquid retention chamber retains the fermentation liquid, and the fermentation liquid has a redox potential of less than −200 mV; d) collecting fermentation liquid containing liquid products from the liquid retention chamber to recover liquid products from the process; and, e) periodically increasing the pressure of the fermentation liquid to create liquid flow from the central lumen through the membrane and to the outside of the membrane to purge microorganisms from the membrane.