Purifying oil shale retort water

Claim 2

A process for purifying oil shale retort water having a substantial amount of organic content, said retort water having sufficient inorganic components, including sulfate, to enable the growth of anaerobic bacteria, comprising: (a) lowering the alkalinity of said retort water to a pH in the range of about 6.5-7.5 and adding to said retort water anaerobic bacteria for reducing said sulfate to sulfide, said bacteria being capable of growth by utilizing said organic content; (b) producing in said retort water under anaerobic conditions a growth of cell biomass of said bacteria aggregated into a flocculent mass, and reducing said sulfate to sulfide; and thereafter (c) removing said aggregated cell biomass from said retort water; and (d) oxidizing said sulfide to sulfate.

Claim 3

The process of claim 1 in which said sulfide is oxidized to sulfate after said cell biomass has been removed from said retort water.

Claim 4

The process of claim 1 in which said alkalinity is lowered by recycling at least part of the sulfate from step (d) to said retort water.

Claim 5

The process of claim 1 including the step of neutralizing at least part of the sulfate product in step (d).

Claim 6

The process of claim 4 in which sulfate in said retort water is neutralized by reaction with the inorganic matrix of retorted oil shale.

Claim 7

The process of claim 5 including the step of separating said reacted matrix from said retort water.

Claim 8

The process of claim 1 in which step (d) comprises adding to said retort water aerobic bacteria capable of oxidizing said sulfide to sulfate, and aerating said retort water with oxygen-containing gas to effect said oxidation.

Claim 9

The process of claim 9 in which said oxygen-containing gas is air.

Claim 10

The process of claim 1 in which at least part of the cell biomass from step (c) is recycled to said retort water prior to step (c) as nutrient for growth of said bacteria.

Claim 11

The process of claim 1 in which said anaerobic bacteria are members of the Desulfovibrio family of bacteria.

Claim 12

The process of claim 10 in which said anaerobic bacteria are Desulfovibrio desulfuricans.

Claim 13

The process of claim 11 in which said anaerobic bacteria are subspecies aestuarii.

Claim 14

The process of claim 11 in which said anaerobic bacteria are subspecies desulfuricans.

Claim 15

The process of claim 10 in which said anaerobic bacteria are Desulfovibrio africanus.

Claim 16

The process of claim 10 in which said anaerobic bacteria are Desulfovibrio gigas.

Claim 17

The process of claim 10 in which said anaerobic bacteria are Desulfovibrio salexigens.

Claim 18

The process of claim 10 in which said anaerobic bacteria are Desulfovibrio vulgaris.

Claim 19

The process of claim 17 in which said anaerobic bacteria are subspecies oxamicus.

Claim 20

The process of claim 17 in which said anaerobic bacteria are subspecies vulgaris.

Claim 21

The process of claim 7 in which said aerobic bacteria are members of the Thiobacillus family of bacteria.

Claim 22

The process of claim 7 in which said aerobic bacteria are Thiobacillus thioxidans.

Claim 23

The process of claim 9 in which said aerobic bacteria are Thiobacillus concretivorous.

Claim 24

The process of claim 7 in which said aerobic bacteria are Thiobacillus sulfooxidans.

Claim 25

The process of claim 7 in which said aerobic bacteria are Thiobacillus ferroxidans.

Claim 26

The process of claim 7 in which said aerobic bacteria are Thiobacillus thioparus.

Claim 27

The process of claim 7 in which said aerobic bacteria are Thiobacillus intermedius.

Claim 28

The process of claim 7 in which said aerobic bacteria are Thiobacillus novellus.

Claim 29

The process of claim 7 in which said aerobic bacteria are Thiobacillus thermitanus.

Claim 30

The process of claim 7 in which said aerobic bacteria are Thiobacillus umbonatus.

Claim 31

The process of claim 7 in which said aerobic bacteria are Thiobacillus lobatus.

Claim 32

The process of claim 7 in which said aerobic bacteria are Thiobacillus crenatus.

Claim 33

The process of claim 7 in which said aerobic bacteria are Thiobacillus neopolitans.

Claim 34

A process for purifying oil shale retort water having a substantial amount of organic content, said retort water having sufficient inorganic components, including sulfate, to enable the growth of anaerobic bacteria, comprising: (a) adding to said retort water bacteria of the Desulfovibrio family of bacteria capable of growth by utilizing said organic content; (b) producing in said retort water under anaerobic conditions a growth of cell biomass of said bacteria aggregated into a fluocculent mass, and reducing said sulfate to sulfide; and thereafter (c) removing said aggregated cell biomass from said retort water; (d) adding to said retort water after step (c) bacteria of the Thiobaccillus family of bacteria and aerating said retort water with oxygen-containing gas to oxidize said sulfide to sulfate; and ((e) recycling at least part of the sulfate from step (d) to said retort water prior to step (b) in an amount sufficient to neutralize said retort water to a pH in the range of about 6.7-7.5.

Claim 35

A process for purifying oil shale retort water having a substantial amount of organic content, said retort water having sufficient inorganic components, including sulfate, to enable the growth of anaerobic bacteria, comprising: (a) adding to said retort water bacteria of the Desulfovibrio family of bacteria capable of growth by utilizing said organic content; (b) producing in said retort water under anaerobic conditions a growth of cell biomass of said bacteria aggregated into a fluocculent mass, and reducing said sulfate to sulfide; and thereafter (c) removing said aggregated cell biomass from said retort water; (d) adding to said retort water after step (c) bacteria of the Thiobaccillus family of bacteria and aerating said retort water with oxygen-containing gas to oxidize said sulfide to sulfate; and ((e) recycling at least part of the sulfate from step (d) to said retort water prior to step (b) in an amount sufficient to neutralize said retort water to a pH in the range of about 6.7-7.5.