Process for fermenting co-containing gaseous substrates

1. A process for fermenting a carbon monoxide (CO)-containing gaseous substrate comprising:

growing an inoculum of acetogenic bacteria cells on a first medium that includes a first substrate to provide a cell density of about 0.02 g/L or more, wherein the first medium has a pH of 5.5 to 7.0 and the first substrate includes a carbon source that is selected from the group consisting of yeast extract, carbohydrates, alcohol, amino acids, peptone, peptides, protein, fatty acids, lipid and mixtures thereof, wherein the inoculum of acetogenic bacteria has no measurable consumption of a (CO)-containing gaseous substrate;

sporulating at least a portion of the inoculum of bacteria by reducing an amount of the first substrate to provide bacterial spores;

germinating the bacterial spores by replacing at least a portion of the first medium with a production medium having a pH of 4.1 to 5 and by replacing at least a portion of the first substrate with a CO-containing gaseous substrate, wherein the CO is a sole carbon source in the production medium; and

supplying the CO-containing gaseous substrate to maintain a specific CO uptake of about 0.25 mmol per g cells or more;

wherein the process of fermenting CO provides a specific STY (space time yield) of about 1 g of ethanol/(L day gram cells) or more.

2. The process of claim 1 wherein the CO containing gaseous substrate is syngas.

3. The process of claim 2 wherein the syngas has a CO/CO 2 molar ratio of at least about 0.75.

4. The process of claim 1 wherein the acetogenic bacteria is selected from the group consisting of Acetogenium kivui, Acetoanaerobium noterae, Acetobacterium woodii, Alkalibaculum bacchi CP11 (ATCC BAA-1772), Blautia producta, Butyribacterium methylotrophicum, Caldanaerobacter subterraneous, Caldanaerobacter subterraneous pacificus, Carboxydothermus hydrogenoformans, Clostridium aceticurn, Clostridium acetobutylicum, Clostridium acetobutylicum P262 (DSM 19630 of DSMZ Germany), Clostridium autoethanogenum (DSM 19630 of DSMZ Germany), Clostridium autoethanogenum (DSM 10061 of DSMZ Germany), Clostridium autoethanogenum (DSM 23693 of DSMZ Germany), Clostridium autoethanogenum (DSM 24138 of DSMZ Germany), Clostridium carboxidivorans P7 (ATCC PTA-7827), Clostridium coskatii (ATCC PTA-10522), Clostridium drakei, Clostridium ljungdahlii PETC (ATCC 49587), Clostridium ljungdahlii ERI2 (ATCC 55380), Clostridium ljungdahlii C-01 (ATCC 55988), Clostridium ljungdahlii O-52 (ATCC 55889), Clostridium magnum, Clostridium pasteurianum (DSM 525 of DSMZ Germany), Clostridium ragsdali P11 (ATCC BAA-622), Clostridium scatologenes, Clostridium thermoaceticum, Clostridium ultunense, Desulfotomaculum kuznetsovii, Eubacterium limosum, Geobacter sulfurreducens, Methanosareina acetivorans, Methanosarcina barkeri, Morrella thermoacetica, Morrella thermoautotrophica, Oxobacter pfennigii, Peptostreptococcus products, Ruminococcus productus, Thermoanaerobacter kivui , and mixtures thereof.

5. The process of claim 1 wherein the process includes

reducing the first substrate is reduced in an amount effective for causing sporulation; and

determining a spore number to cell number ratio by visual inspection and counting using a hemocytometer,

wherein the process is effective for providing a spore number to cell number ratio of about 0.05 or more as determined by visual inspection and counting using a hemocytometer.

6. The process of claim 1 wherein the process includes

replacing the first substrate with the production medium in an amount effective for germination;

determining a spore number to cell number ratio by visual inspection and counting using a hemocytometer,

wherein the process is effective for providing a spore number to cell number ratio of at least about 0.04 or less as determined by visual inspection and counting using a hemocytometer.

7. The process of claim 1 wherein the production medium comprises:

at least about 112 mg of nitrogen per gram of cells,

at least about 10.5 mg of phosphorous per gram of cells, or

at least about 26 mg of potassium per gram of cells.

8. The process of claim 1 further comprising adding a co-feed of a carbon source.

9. The process of claim 8 wherein the co-feed is added prior to sporulation.

10. The process of claim 8 wherein the carbon source is selected from the group consisting of yeast extract, carbohydrates, alcohol, amino acids, peptone, peptides, protein, fatty acids, lipid and mixtures thereof.