Fermentation of oxygenated hydrocarbon compounds with thermophilic microorganisms

Claim 3

A process for the production of microbial cells which comprises aerobically culturing under thermophilic fermentation conditions a strain of Bacillus species derived from NRRL B-8065 or NRRL B-8066 in a culture medium containing an oxygenated hydrocarbon as the main carbon and energy source, nutrients, and a nitrogen source.

Claim 4

A process for the production of microbial cells which comprises aerobically culturing under thermophilic fermentation conditions a strain of Bacillus species derived from NRRL B-8065 or NRRL B-8066 in a culture medium containing an oxygenated hydrocarbon as the main carbon and energy source, nutrients, and a nitrogen source.

Claim 5

The process of claim 2 further comprising the further step of separating and recovering said microbial cells so produced from said culture medium.

Claim 6

The process of claim 3 wherein said strain is derived from said NRRL B-8065.

Claim 7

The process according to claim 3 wherein said strain is derived from said NRRL B-8066.

Claim 8

The process of claim 2 wherein said process of culturing is conducted at a fermentation temperature in the range of about 45° to 65° C.

Claim 9

The process according to claim 6 wherein said oxygenated hydrocarbon carbon and energy source material comprises one or more alcohols, ketones, esters, ethers, acids, or aldehydes, characterized as substantially water-soluble in character, and of up to about 10 carbon atoms per molecule.

Claim 10

The process according to claim 7 wherein said oxygenated hydrocarbon is selected from the group consisting of methanol, ethanol, propanol, butanol, pentanol, hexanol, 1,7-heptanediol, 2-heptanol, 2-methyl-4-pentanol, pentanoic acid, 2-methylbutanoic acid, 2-pentanol, 2-methyl-4-butanol, 2-methyl-3-butanol, 2-butanol, 2-methyl-1-propanol, 2-methyl-2-propanol, 2-propanol, formic acid, acetic acid, propanoic acid, formaldehyde, acetaldehyde, propanal, butanal, 2-methylpropanal, butanoic acid, 2-methylpropanoic acid, pentanoic acid, glutaric acid, hexanoic acid, 2-methylpentanoic acid, heptanedioic acid, heptanoic acid, 4-heptanone, 2-heptanone, octanoic acid, 2-ethylhexanoic acid, glycerine, ethylene glycol, propylene glycol, 2-propanone, 2-butanone, diethyl ether, methyl ethyl ether, dimethyl ether, di-n-propyl ether, n-propyl isopropyl ether, or mixture.

Claim 11

The process according to claim 7 wherein said carbon and energy source material comprises a water-soluble aliphatic monohydric hydrocarbyl alcohol.

Claim 12

The process according to claim 9 wherein said alcohol contains 1 to 4 carbon atoms per molecule.

Claim 13

The process according to claim 10 wherein said alcohol is ethanol or methanol.

Claim 14

The process according to claim 11 wherein said culturing is conducted at a fermentation temperature in the range of about 50° to 60° C.

Claim 15

The process according to claim 12 wherein said carbon and energy source material is maintained at a concentration of about 0.01 to 5 volume/volume percent in said culture medium.

Claim 16

The process according to claim 13 wherein said concentration is in the range of about 0.01 to 0.5 volume/volume percent.

Claim 17

The process according to claim 13 wherein said aerobic culturing of said strain includes fermentation conditions employing about 0.02 to 2.1 volumes of oxygen per minute per volume of liquid in said culture medium, and wherein said culture medium is maintained under a pressure of about 0.1 to 100 atmospheres and a pH in the range of about 5 to 9.

Claim 18

The process according to claim 15 wherein said oxygen is supplied at least in part as air.

Claim 19

The process according to claim 9 wherein said oxygenated hydrocarbon carbon and energy source material contains aldehyde, and wherein said aldehyde containing oxygenated hydrocarbon carbon and energy source material is treated with ammonia or an ammonium compound in a ratio of about 0.01 to 10 mol equivalents per mol of aldehyde prior to employing said carbon and energy source material in said culture medium.

Claim 20

The process according to claim 15 wherein said culture medium is treated with a manganous compound during said culturing.

Claim 21

The process of claim 15 wherein said culturing is conducted in a substantially foam-filled fermentation means under foam-filled fermentation conditions.

Claim 22

The process according to claim 15 wherein said microorganism is said NRRL B-8065 species, said carbon energy source material comprises methanol, said fermentation is conducted at a pH in the range of about 6.2-6.8.

Claim 23

The process according to claim 15 wherein said microorganism is said NRRL B-8066 species, said carbon energy source material comprises methanol, said fermentation is conducted at a pH in the range of about 6.2-6.5.

Claim 24

The process according to claim 15 wherein said strain is said NRRL B-8066, culturing is conducted at a pH in the range of about 6.7-6.9, said culturing or fermentation temperature is about 55° C., ammonium hydroxide is employed as nitrogen source.

Claim 25

The process according to claim 15 wherein said strain is said NRRL B-8066, fermentation pH in said culture medium is maintained in the range of about 7-7.2 employing ammonium hydroxide for pH control and as nitrogen source, and said culturing fermentation temperature was about 53° C., and said carbon energy source material is methanol.

Claim 26

The process according to claim 15 wherein said Bacillus species is said NRRL B-8065 species, the carbon and energy source substrate is methanol, said fermentation temperature was about 54° C., culture medium fermentation condition pH was in the range of about 6.3-6.6, and ammonium hydroxide is nitrogen source.