Production of epoxides such as propylene oxide using packed catalytic bed containing moist resting cells exhibiting oxygenase activity

Claim 2

A process for advancing the oxidation state of a gaseous, oxidizable organic substrate through contact with a gaseous source of oxygen and a biocatalyst comprising: passing through a packed catalytic bed comprising moist, resting cells exhibiting oxygenase activity a gaseous, oxidizable organic substrate and a gaseous source of oxygen until the oxidative state of at least a portion of said substrate is increased, while maintaining the relative humidity in said bed at such a level that said cells remain moist and catalytically active until spent.

Claim 3

The process of claim 1 wherein said gaseous organic substrate is a C 1 to C 4 alkane or a C 2 to C 4 alkene, and the temperature of the bed is maintained in the range from about 15° C. to about 80° C.

Claim 4

A process according to claim 2 wherein said catalytic bed comprises a mass of catalytic materials produced by applying a paste of cells and water to particles of an inert carrier.

Claim 5

The process of claim 3 wherein said carrier particles are porous glass beads.

Claim 6

The process of claim 3 wherein said carrier particles are silica particles.

Claim 7

The process of claim 3 wherein the carrier particles are not over 2 mm. in their largest dimension.

Claim 8

The process of claim 3 wherein the cells are those of a methylotrophic microorganism.

Claim 9

The process of claim 7 wherein the cells are obtained by culturing on a C-1 compound.

Claim 10

The process of claim 7 wherein said cells are obtained by culturing on a lower alkane.

Claim 11

The process of claim 1 including the step of restoring at least a part of spent catalytic activity of the cells in situ.

Claim 12

The process of claim 10 wherein the step of restoring catalytic activity comprises blowing a gaseous, nutrient carbon-containing compound and a gaseous source of oxygen through said bed.

Claim 13

The process of claim 11 wherein said nutrient carbon-containing compound is methane or one of its metabolites.

Claim 14

The process of claim 11 wherein said nutrient carbon-containing compound is methanol.

Claim 15

The process of claim 10 comprising restoring spent catalytic activity by restoring the reducing power of the cells.

Claim 16

The process of claim 1, 2, 3 or 7, comprising recovering the oxidized substrate by chilling the effluent gaseous stream to condense the oxidized substrate product.

Claim 17

The process of claim 15 including the step, after condensing the product from the effluent, of recycling residual gas through the process.

Claim 18

A process for advancing the oxidation state of a gaseous, oxidizable organic substrate through contact with a biocatalyst and with a gaseous source of oxygen comprising: passing through a packed biocatalytic bed comprising moist, resting cells exhibiting oxygenase activity a gaseous source of oxygen together with a gaseous, oxidizable organic substrate selected from the group consisting of saturated and unsaturated compounds being not more than four carbon atoms, at a temperature in the range from about 15° C. to about 80° C., while maintaining the relative humidity conditions in the bed so that the cells remain moist and catalytically active, maintaining the reactor and operating temperature at a temperature level within said range at which the effluent, containing oxidized substrate, remains gaseous, and passing the gaseous effluent through a chilled condenser that converts the oxidized product to a liquid while any unoxidized substrate remains gaseous.

Claim 19

A process for advancing the oxidation state of a gaseous, oxidizable organic substrate through contact with a biocatalyst and with a gaseous source of oxygen comprising: passing through a packed biocatalytic bed comprising moist, resting cells exhibiting oxygenase activity a gaseous source of oxygen together with a gaseous, oxidizable organic substrate selected from the group consisting of saturated and unsaturated compounds being not more than four carbon atoms, at a temperature in the range from about 15° C. to about 80° C., while maintaining the relative humidity conditions in the bed so that the cells remain moist and catalytically active, maintaining the reactor and operating temperature at a temperature level within said range at which the effluent, containing oxidized substrate, remains gaseous, and passing the gaseous effluent through a chilled condenser that converts the oxidized product to a liquid while any unoxidized substrate remains gaseous.

Claim 20

The process of claim 17 including recycling any unoxidized substrate gas through the process.

Claim 21

The process of claim 1, 2, 3, 7, 10 or 17 wherein the microorganism is from the group of genera consisting of Methylosinus, Methylocystis, Methylomonas, Methylobacter, Methylococcus, and Methylobacterium.

Claim 22

The process of claim 19 wherein said microorganism is a species selected from the group consisting of Methylosinus trichosporium, Methylosinus sporium, Methylocystis parvus, Methylomonas methanica, Methylomonas albus, Methylmonas spectobacterium, Methylomonas agile, Methylomonas rubrum, Methylomonas rosaceus, Methylobacter chroocuccum, Methylobacter bovis, Methylobacter capsulatus, Methylobacter vinelandii, Methylococcus capsulatus, Methylococcus minimus and Methylobacterium organophilum.

Claim 23

The process of claim 20 wherein the microorganism is a strain selected from the group consisting of: Methylosinus trichosporium (NRRL B-11,196); Methylosinus sporium (NRRL B-11,197); Methylocystis parvus (NRRL B-11,198); Methylomonas methanica (NRRL B-11,199); Methylomonas albus (NRRL B-11,200); Methylobacter capsulatus (NRRL B-11,201); Methylobacterium organophilum sp nov. (ATCC 27,886); Methylomonas sp AJ-3670 (FERM P-2400); Methylococcus sp (NCIB Accession No. 11,083); or Methylomonas sp (NCIB Accession No. 11,084).

Claim 24

The process of claim 1, 2, 3, 7 or 17 comprising maintaining the humidity by passing the gaseous substrate and the gaseous source of oxygen through a body of water before passing them through said bed.

Claim 25

The process of claim 1, 2, 3, 7 or 17 wherein the oxidizable organic substrate is propylene and the oxidized product produced is propylene oxide.

Claim 26

A process for converting propylene to propylene oxide through contact with a gaseous source of oxygen and a biocatalyst comprising: passing gaseous propylene through a packed catalytic bed comprising inert solid carrier particles having disposed thereon moist, resting cells exhibiting enzymatic activity capable of converting the propylene to propylene oxide in the presence of oxygen, and simultaneously passing through the packed bed with the propylene a gaseous source of oxygen, maintaining the gaseous materials in contact with the bed until at least some of the propylene is converted to propylene oxide, while maintaining the relative humidity of the propylene and of the gaseous source of oxygen at such a level that said cell remain moist, maintaining the bed at a temperature in the range from about 15° C. to about 80° C., said cells being those of a methane-grown microorganism from the group of genera consisting of Methylosinus, Methylocystis, Methylomonas, Methylobacter, and Methylobacterium, and recovering the propylene oxide from the gaseous effluent by chilling the effluent to condense the propylene oxide.

Claim 27

A process for converting propylene to propylene oxide through contact with a gaseous source of oxygen and a biocatalyst comprising: passing gaseous propylene through a packed catalytic bed comprising inert solid carrier particles having disposed thereon moist, resting cells exhibiting enzymatic activity capable of converting the propylene to propylene oxide in the presence of oxygen, and simultaneously passing through the packed bed with the propylene a gaseous source of oxygen, maintaining the gaseous materials in contact with the bed until at least some of the propylene is converted to propylene oxide, while maintaining the relative humidity of the propylene and of the gaseous source of oxygen at such a level that said cell remain moist, maintaining the bed at a temperature in the range from about 15° C. to about 80° C., said cells being those of a methane-grown microorganism from the group of genera consisting of Methylosinus, Methylocystis, Methylomonas, Methylobacter, and Methylobacterium, and recovering the propylene oxide from the gaseous effluent by chilling the effluent to condense the propylene oxide.