Processes for bioconverting syngas to oxygenated hydrocarbonaceous compounds
View Patent ↗Continuous processes for the anaerobic bioconversion of syngas to oxygenated hydrocarbonaceous products, in particular lower alkanols, are disclosed in which nutrients, including micronutrients, and lower carboxylate anion are recovered from at least a portion of an aqueous distillation fraction from a distillation unit operation to recover lower alkanols by using a “tight” ultrafiltration membrane. At least about 75 percent of the water permeates the ultrafiltration membrane. The tight ultrafiltration membrane rejects sufficient components that are adverse to the microorganisms used in the bioconversion that continuous fermentation operations over long durations can be achieved.
1. A continuous process for the anaerobic bioconversion of a gas substrate comprising carbon monoxide, hydrogen and carbon dioxide in an aqueous broth containing microorganisms suitable for converting said substrate to oxygenated hydrocarbonaceous compound, which process comprises:
a. continuously contacting said gas substrate with said aqueous broth under acidic, anaerobic fermentation conditions including the presence of nutrients to bioconvert gas substrate to oxygenated hydrocarbonaceous compound and provide an oxygenated hydrocarbonaceous compound-containing broth and a depleted gas phase, said anaerobic fermentation conditions also producing a co-produced, lower carboxylate anion and metabolites adverse to said microorganisms;
b. continuously withdrawing the depleted gas phase from said aqueous broth;
c. continuously or intermittently withdrawing a portion of said aqueous broth for recovery of said oxygenated hydrocarbonaceous compound, said withdrawal being sufficient to maintain the oxygenated hydrocarbonaceous compound in said aqueous broth below a concentration that unduly adversely affects the microorganisms;
d. continuously separating by distillation the oxygenated hydrocarbonaceous compound from the withdrawn portion of said aqueous broth to provide an oxygenated hydrocarbonaceous compound fraction rich in said oxygenated hydrocarbonaceous compound and an aqueous distillation fraction containing said co-produced, lower carboxylate anion and said adverse metabolites, wherein said distillation denatures said aqueous broth and generates free proteins;
e. optionally recycling a portion of the aqueous distillation fraction to step (a);
f. subjecting a portion of the aqueous distillation fraction to ultrafiltration to permeate at least about 75 percent of the water contained in said subjected portion, said ultrafiltration using an ultrafiltration membrane having a cut-off in the range of between 750 and 8000 Daltons to provide permeate including said co-produced, lower carboxylate anion; and
g. recycling the permeated of step (f) to step (a).
2. The process of claim 1 wherein solids are removed prior to being passed to step (d) and/or prior to being passed to step (e) or step (f).
3. The process of claim 2 wherein the ultrafiltration membrane has a cut-off between about 800 and 7500 Daltons.
4. The process of claim 3 wherein at least about 85 percent of the water in the portion of the aqueous distillation fraction subjected to ultrafiltration is permeated in step (f).
5. The process of claim 3 wherein the aqueous distillation fraction contains potassium and ammonium anion and the permeate has a concentration of each of the potassium and ammonium cations of at least about 90 percent of that in the portion of the aqueous distillation fraction subjected to ultrafiltration.
6. The process of claim 3 wherein the aqueous distillation fraction contains sulfur and phosphorus-containing components and the permeate has a concentration of each of the sulfur and phosphorus-containing components of at least about 70 mass percent of that in the portion of the aqueous distillation fraction subjected to ultrafiltration.
7. The process of claim 3 wherein the concentration of proteins in the permeate is less than about 20 mass percent of that in the portion of the aqueous distillation fraction subjected to ultrafiltration.
8. The process of claim 7 wherein at least about 60 percent of the lower carboxylate anion in the portion of the aqueous distillation fraction subjected to ultrafiltration is contained in the permeate of step (f).
9. The process of claim 2 wherein the solids removed are subjected to anaerobic digestion to produce methane and an aqueous discharge, subjecting the aqueous discharge to a solids removal unit operation to provide an aqueous liquor and a solids-rich fraction, and passing at least a portion of the aqueous liquor to step (f).
10. The process of claim 1 wherein oxygenated hydrocarbonaceous compound is a oxygenated hydrocarbon.
11. The process of claim 10 wherein the oxygenated hydrocarbon is a lower alkanol.
12. A continuous process for the anaerobic bioconversion of a gas substrate comprising carbon monoxide, hydrogen and carbon dioxide in an aqueous broth containing microorganisms suitable for converting said substrate to lower alkanol, which process comprises:
a. continuously contacting said gas substrate with said aqueous broth under acidic, anaerobic fermentation conditions including the presence of nutrients to bioconvert gas substrate to lower alkanol and provide a lower alkanol-containing broth and a depleted gas phase, said anaerobic fermentation conditions also producing a co-produced, lower carboxylate anion and metabolites adverse to said microorganisms;
b. continuously withdrawing the depleted gas phase from said aqueous broth;
c. continuously or intermittently withdrawing a portion of said aqueous broth for recovery of said lower alkanol, said withdrawal being sufficient to maintain the lower alkanol in said aqueous broth below a concentration that unduly adversely affects the microorganisms;
d. continuously separating by distillation the lower alkanol from the withdrawn portion of said aqueous broth to provide an alkanol fraction rich in said lower alkanol and an aqueous distillation fraction containing said co-produced, lower carboxylate anion and said adverse metabolites, wherein said distillation denatures said aqueous broth and generates free proteins;
e. optionally recycling a portion of the aqueous distillation fraction to step (a);
f. subjecting a portion of the aqueous distillation fraction to ultrafiltration to permeate at least about 75 percent of the water contained in said subjected portion, said ultrafiltration using an ultrafiltration membrane having a cut-off in the range of between 750 and 8000 Daltons to provide permeate including said co-produced, lower carboxylate anion; and
g. recycling the permeated of step (f) to step (a).
13. The process of claim 12 wherein solids are removed prior to being passed to step (d) and/or prior to being passed to step (e) or step (f).
14. The process of claim 13 wherein the ultrafiltration membrane has a cut-off between about 800 and 7500 Daltons.
15. The process of claim 14 wherein at least about 85 percent of the water in the portion of the aqueous distillation fraction subjected to ultrafiltration is permeated in step (f).
16. The process of claim 14 wherein the aqueous distillation fraction contains potassium and ammonium anion and the permeate has a concentration of each of the potassium and ammonium cations of at least about 90 percent of that in the portion of the aqueous distillation fraction subjected to ultrafiltration.
17. The process of claim 14 wherein the aqueous distillation fraction contains sulfur and phosphorus-containing components and the permeate has a concentration of each of the sulfur and phosphorus-containing components of at least about 70 mass percent of that in the portion of the aqueous distillation fraction subjected to ultrafiltration.
18. The process of claim 14 wherein the concentration of proteins in the permeate is less than about 20 mass percent of that in the portion of the aqueous distillation fraction subjected to ultrafiltration.
19. The process of claim 18 wherein at least about 60 percent of the lower carboxylate anion in the portion of the aqueous distillation fraction subjected to ultrafiltration is contained in the permeate of step (f).
20. The process of claim 13 wherein the solids removed are subjected to anaerobic digestion to produce methane and an aqueous discharge, subjecting the aqueous discharge to a solids removal unit operation to provide an aqueous liquor and a solids-rich fraction, and passing at least a portion of the aqueous liquor to step (f).