Processes for the acidic, anaerobic conversion of hydrogen and carbon oxides to oxygenated organic compound
View Patent ↗Processes for the bioconversion of syngas to oxygenated organic compound are disclosed that reliably, cost-effectively and efficiently supply sulfur nutrient to microorganisms contained in acidic, aqueous fermentation menstrua. In the processes of this invention, basic, aqueous solution used to maintain the pH of the aqueous fermentation menstruum is used to remove hydrogen sulfide from the off-gas from the fermentation menstruum for recycle to the fermentation menstruum.
1. A continuous process for the anaerobic bioconversion of a gas substrate comprising carbon monoxide, hydrogen and carbon dioxide to an oxygenated organic compound in an aqueous menstruum containing microorganisms suitable for converting said substrate to oxygenated organic compound, comprising:
a. continuously contacting said gas substrate with said aqueous menstruum under acidic, anaerobic fermentation conditions including the presence of sulfur nutrient to bioconvert said gas substrate to said oxygenated organic compound thereby providing an oxygenated organic compound-containing menstruum and a depleted gas phase containing hydrogen sulfide;
b. continuously or intermittently introducing into said aqueous menstruum a basic, aqueous solution in an amount sufficient to maintain the aqueous menstruum above a pH that unduly adversely affects the microorganisms;
c. continuously or intermittently withdrawing a portion of said aqueous menstruum for recovery of said oxygenated organic compound, said withdrawal being sufficient to maintain the oxygenated organic compound in said aqueous menstruum below a concentration that unduly adversely affects the microorganisms;
d. continuously withdrawing the depleted gas phase from said aqueous menstruum; and
e. continuously contacting at least a portion of the depleted gas phase withdrawn from said aqueous menstruum with at least a portion of the basic, aqueous solution prior to its introduction into said aqueous menstruum in step (b) thereby reducing the concentration of hydrogen sulfide in the depleted gas phase and providing sulfhydryl anion to the basic, aqueous solution.
2. The process of claim 1 wherein the basic, aqueous solution comprises a caustic, aqueous solution.
3. The process of claim 1 wherein the basic, aqueous solution prior to contacting the off depleted gas phase comprises at least one of makeup water and water sourced from the process.
4. The process of claim 3 wherein the withdrawn aqueous fermentation menstruum is subjected to distillation to provide an oxygenated organic compound product and a still bottoms, and at least a portion of the water sourced from the process comprises water from the still bottoms.
5. The process of claim 3 wherein water sourced from the process is used to lower the pH of the basic, aqueous solution.
6. The process of claim 1 wherein the pH of the basic, aqueous solution prior to contacting the off gas is between about 7.5 and 14.
7. The process of claim 1 wherein the pH of the basic, aqueous solution prior to contacting the depleted gas phase is between about 8 and 13.
8. The process of claim 1 wherein the off depleted gas phase after contacting the basic, aqueous solution contains less than about 150 parts per million by volume hydrogen sulfide.
9. The process of claim 1 wherein the off depleted gas phase after contacting the basic, aqueous solution contains less than about 50 parts per million by volume hydrogen sulfide.
10. The process of claim 1 wherein the basic, aqueous solution after contacting the depleted gas phase is directly introduced into a bioreactor containing the aqueous fermentation menstruum.
11. The process of claim 10 wherein a portion of the aqueous fermentation menstruum is continuously withdrawn from the bioreactor, cooled and returned to the bioreactor, and at least a portion of the basic, aqueous solution after contacting the depleted gas phase is combined with the withdrawn aqueous fermentation menstruum prior to being returned to the bioreactor.
12. The process of claim 1 wherein the depleted gas phase comprises carbon dioxide, and at least a portion of the carbon dioxide is removed during the contacting with the basic, aqueous solution.
13. The process of claim 12 wherein the withdrawn aqueous fermentation menstruum is subjected to distillation to provide an oxygenated organic compound product and a still bottoms, and the still bottoms is used, at least in part, to adjust the pH of the basic, aqueous solution.
14. The process of claim 1 wherein the basic, aqueous solution is introduced at a rate sufficient to maintain the pH of the aqueous fermentation menstruum above about 4.5.
15. The process of claim 14 wherein the pH of the aqueous fermentation menstruum is between about 4.5 and 6.