Process for the elimination of nitrates by means of a microbiological conversion in the presence of hydrogen gas

Claim 2

A microbiological denitrification process consisting essentially of the steps of (a) directing an aqueous stream comprising at least one nitrate into contact with a first denitrifying biomass contained in a cell, said denitrifying biomass having an affinity for hydrogen and also being contacted by hydrogen gas introduced as a gas into said cell, wherein a portion of said hydrogen gas is recycled for use in subsequent denitrification via said process; (b) directing said aqueous stream into contact with a second denitrifying biomass, such that hdyrogen introduced into said stream during step (a) is consumed and then (c) directing said aqueous stream into contact with a nitrifying biomass which is also contacted with a fluid containing oxygen or at least one constituent which, upon contact with said aqueous stream, releases oxygen, such that all nitrogenous components in said aqueous stream are converted to nitrate to produce potable water.

Claim 3

A process according to claim 1, wherein step (a) comprises bringing said hydrogen gas into contact with said denitrifying biomass from a direction which is opposite the direction of said aqueous stream, whereby said hydrogen gas and said aqueous stream are oriented in countercurrent relation.

Claim 4

A process according to claim 1, wherein step (a) comprises bringing said hydrogen gas into contact with said denitrifying biomass from a direction which parallels the direction of said aqueous stream.

Claim 5

A process according to claim 1, wherein step (b) comprises bringing said fluid into contact with said nitrifying biomass from a direction which parallels the direction of said aqueous stream.

Claim 6

A process according to claim 1, wherein step (b) comprises bringing said fluid into contact with said nitrifying biomass from a direction which is opposite to the direction of said aqueous stream.

Claim 7

A process according to claim 1, wherein said second denitrifying biomass comprises bacteria selected from the group consisting of an Alcaligenous eutrophic strain, Pseudomonas denitrificans and Micrococcus denitrificans.

Claim 8

A process according to claim 1, wherein steps (b) and (c) are carried out in contiguous reaction zones.

Claim 9

A process according to claim 7, wherein step (a) is carried out in a reaction zone that is not contiguous with the reaction zones for steps (b) and (c), respectively.

Claim 10

A process according to claim 1, wherein said nitrifying biomass comprises organoaerobic bacteria and/or chemolitotropic aerobic bacteria.

Claim 11

A process according to claim 1, wherein said nitrifying biomass comprises bacteria of the genus Nitrobacter.

Claim 12

A process according to claim 1, wherein said first denitrifying biomass comprises bacteria selected from the group consisting of an Alcaligenous eutrophic strain, Pseudomonas denitrificans and Micrococcus denitrificans.

Claim 13

Apparatus for microbiological denitrification, consisting essentially of: (a) a first reaction zone containing a first denitrifying biomass in a volume of fluid, said biomass having an affinity for hydrogen; (b) means fluidly connected to a source of hydrogen gas for contacting said first denitrifying biomass with hydrogen gas; (c) means for contacting said first denitrifying biomass with an aqueous stream comprising at least one nitrate; (d) a second reaction zone containing a nitrifying biomass in a volume of fluid, said second reaction zone being in communication with said first reaction zone; (e) means for contacting said nitrifying biomass with a fluid containing oxygen or at least one constituent which, upon contact with said aqueous stream, releases oxygen; (f) means for withdrawing treated effluent from the second reaction zone; (g) inlet means for introducing a nitrate-containing fluid into said first reaction zone; (h) a third reaction zone in communication with both of said first and second reaction zones, said third reaction zone containing a second denitrifying biomass in a volume of fluid; and (i) means for recycling hydrogen gas from said first reaction zone to use in contacting said first denitrifying biomass.

Claim 14

Apparatus for microbiological denitrification, consisting essentially of: (a) a first reaction zone containing a first denitrifying biomass in a volume of fluid, said biomass having an affinity for hydrogen; (b) means fluidly connected to a source of hydrogen gas for contacting said first denitrifying biomass with hydrogen gas; (c) means for contacting said first denitrifying biomass with an aqueous stream comprising at least one nitrate; (d) a second reaction zone containing a nitrifying biomass in a volume of fluid, said second reaction zone being in communication with said first reaction zone; (e) means for contacting said nitrifying biomass with a fluid containing oxygen or at least one constituent which, upon contact with said aqueous stream, releases oxygen; (f) means for withdrawing treated effluent from the second reaction zone; (g) inlet means for introducing a nitrate-containing fluid into said first reaction zone; (h) a third reaction zone in communication with both of said first and second reaction zones, said third reaction zone containing a second denitrifying biomass in a volume of fluid; and (i) means for recycling hydrogen gas from said first reaction zone to use in contacting said first denitrifying biomass.

Claim 15

Apparatus according to claim 12, wherein said first and second reaction zones are contiguous.

Claim 16

Apparatus according to claim 12, wherein said first and second reaction zones are each provided in separate reactors, there being conduit means for communicating between said reactors.

Claim 17

Apparatus according to claim 12, wherein said first and third reaction zones are contiguous.

Claim 18

Apparatus according to claim 12, wherein said second and third reaction zones are contiguous.

Claim 19

Apparatus according to claim 12, wherein said first, second and third reaction zones are each provided in a separate pressurized reactor, the reactors containing said first and second reaction zones each being maintained at pressures greater than the pressure maintained in the reactor containing said third reaction zone.

Claim 20

Apparatus according to claim 17, wherein said first reaction zone is not contiguous with said second or third reaction zones.

Claim 21

Apparatus according to claim 12, wherein means (b) comprises a fermenter containing at least one culture of bacteria selected from the group consisting of Rhodobacter capsulatus, Rhodospirillum rubrum, Rhodomicrobium vannielii, and a species of genus Clostridium.