Moving bed biofilm reactor (MBBR) process for conversion of syngas components to liquid products
View Patent ↗A process for converting a feed gas containing at least one of CO, CO 2 , and/or H 2 to a liquid product using biomass that grow on the surface of carriers suspended in a fermentation broth within the vessel of a moving bed bioreactor (MMBR). An injector is used to at least partially dissolved the feed gas in the fermentation broth, at least partially entrain the gas in the broth as microbubbles and to introduce the mixture of the entrained gas and broth into the vessel in a substantially horizontal direction. The injection of the mixture creates eddy current in the surrounding liquid for thoroughly mixing the fermentation broth in the vessel and for keeping the biomass carrier moving to provide sufficient shear so as to maintain a biofilm thickness on the carrier in a desirable range.
1. A process for converting a feed gas containing at least one of CO, H 2 , CO 2 and a mixture of CO 2 , H 2 and CO to a liquid product, said process comprising:
a) passing a feed gas into a vessel that retains a fermentation broth and microorganisms therein under anaerobic conditions with the fermentation broth supplying nutrients to the microorganisms that produce a liquid product from the feed gas, wherein an injector at least partially entrains the feed gas in a liquid medium as microbubbles before the feed gas enters the vessel;
b) delivering the entrained feed gas and liquid medium to the fermentation broth as a plume wherein the plume is injected into the vessel in a substantially horizontal direction and the plume travels upwardly and horizontally through the vessel after the substantially horizontal injection of the plume from the injector, so that at least a part of the plume travels in a horizontal direction at least half way across the vessel so that the broth and microorganisms receive feed gas across the full cross section of the vessel;
c) retaining inert microorganism carriers having a surface supporting a biofilm of the microorganisms in the vessel, wherein said carriers are arranged for circulation throughout the fermentation broth in the vessel;
d) circulating the carriers containing the microorganisms and the broth in the vessel, so that a portion of the carriers and the broth directly contacts the plume at the location where the plume enters the vessel in the substantially horizontal direction;
e) withdrawing the fermentation broth containing the liquid products from the vessel through a carrier retainer to impede the withdrawal of the carriers with the broth; and,
f) recovering the liquid product from the withdrawn broth.
2. The process of claim 1 wherein injector comprises a contact chamber, at least a portion of the liquid medium comprises the fermentation broth, and the plume is injected from the contact chamber into the vessel, wherein said plume comprises a mixture of the microbubbles and a liquid containing dissolved feed gas.
3. The process of claim 2 wherein the plume provides a mixing intensity that controls the thickness of the biofilm on the carriers.
4. The process of claim 1 wherein at least a portion of the plume, after the substantially horizontal injection, changes direction and travels vertically through the fermentation broth for a distance of at least 9 meters.
5. The process of claim 1 wherein the carriers have a relative density of 0.9 to 0.98 with respect to the fermentation broth.
6. The process of claim 1 wherein the carriers fill at least 30 to 70% of a wetted volume of the vessel.
7. The process of claim 1 wherein the liquid product comprises at least one of ethanol, n-butanol, acetic acid and butyric acid.
8. The process of claim 1 wherein the microorganisms comprises a mono-culture or a co-culture of any of Clostridium ragsdalei, Butyribacterium methylotrophicum, Clostridium Ljungdahl, Clostridium autoethanogenum, or Clostridium Coskatii.
9. The process of claim 1 wherein the carriers have a ratio of protected surface to total surface of at least 60%.
10. The process of claim 1 wherein the microbubbles have a diameter of from 0.1 to 1.0 mm.