Method of purifying fischer-tropsch derived water

• US 7,166,219 B2
• Filed: 12/16/2004
• Issued: 01/23/2007
• Est. Priority Date: 06/18/2002
• Status: Active Grant

• Current Assignee: Sasol Technology Limited (Sasol Limited)
• Original Assignee: Sasol Technology Limited (Sasol Limited)
• Inventors: Koper, Edward Ludovicus, Phillips, Trevor David, Kohler, Luis Pablo Fidel Dancuart, Du Toit, Francois Jacobus, Du Plessis, Gert Hendrik, Van Der Walt, Janette
• Primary Examiner(s): Barry; Chester T
• Application Number:
  US11/015,654
• Publication Number:
  US 20050131086A1
• Time in Patent Office: 768 Days
• Field of Search: 210/601, 210615-617, 210/620, 210/622, 210/631
• US Class Current: 210/601
• CPC Class Codes: C02F 1/04 by distillation or evaporation
• CPC Class Codes: C02F 1/26 by extraction
• CPC Class Codes: C02F 2101/32 Hydrocarbons, e.g. oil
• CPC Class Codes: C02F 2101/34 containing oxygen
• CPC Class Codes: C02F 3/00 Biological treatment of water, waste water, or sewage C02F1/006 takes precedence
• CPC Class Codes: C02F 9/00 Multistage treatment of water, waste water or sewage

Abstract

A process for the production of highly purified water 44 from Fischer-Tropsch reaction water 12 includes distillation 14 as a primary treatment stage, biological treatment including anaerobic digestion 20 and aerobic digestion 22 as a secondary treatment stage, solid-liquid separation 32 as a tertiary treatment stage and a dissolved salt and organic removal stage 40 as final treatment stage.

Claims

1. A process for the production of a purified water from a Fischer-Tropsch reaction water comprising one or more components selected from the group consisting of oxygenated hydrocarbons, aliphatic, aromatic and cyclic hydrocarbons, inorganic compounds, and mixtures thereof, wherein the process comprises the steps of:

a) distilling the Fischer-Tropsch reaction water in a primary treatment stage, whereby at least a fraction of non-acid oxygenated hydrocarbons are removed from the Fischer-Tropsch reaction water to produce a primary water enriched stream;

b) conducting a biological treatment of the primary water enriched stream in a secondary treatment stage, whereby at least a fraction of acidic oxygenated hydrocarbons are removed from at least a portion of the primary water enriched stream to produce a secondary water enriched stream; and

c) removing at least some solids from at least a portion of the secondary water enriched stream in a tertiary treatment stage, whereby a purified water is obtained, the purified water comprising an aqueous stream having a chemical oxygen demand of from 20 to 500 mg/l, a pH of from 6.0 to 9.0, a suspended solids content of less than 250 mg/l, and a total dissolved solids content of less than 600 mg/l.

2. The process as claimed in claim 1, wherein the non-acid oxygenated hydrocarbons are selected from the group consisting of alcohols, aldehydes, ketones, and mixtures thereof, and wherein the acidic oxygenated hydrocarbons are selected from the group consisting of formic acid, acetic acid, propionic acid, butyric acid, valeric acid, hexanoic acid, heptanoic acid, octanoic acid, and mixtures thereof.

3. The process as claimed in claim 1, wherein the primary treatment stage comprises degassing the Fischer-Tropsch reaction water before further processing in the primary treatment stage, whereby compounds having a very low boiling point and dissolved gases are removed from the Fischer-Tropsch reaction water.

4. The process as claimed in claim 1, wherein the biological treatment comprises at least one of anaerobic treatment and aerobic treatment.

5. The process as claimed in claim 4, wherein the aerobic treatment employs an apparatus or process selected from group consisting of activated sludge processes, biological aerated filters, trickling filters, rotating biological contacters, high-rate compact reactors, membrane bioreactors, fluidised bed reactors, and combinations thereof.

6. The process as claimed in claim 4, wherein the anaerobic treatment employs an apparatus or process selected from the group consisting of up-flow anaerobic sludge blanket processes, fixed bed systems, fluidized bed reactors, stirred tank reactors, membrane bioreactors, baffled reactors, and combinations thereof.

7. The process as claimed in claim 1, wherein the tertiary treatment stage comprises removing suspended solids from the secondary water-enriched stream produced during the biological treatment.

8. The process as claimed in claim 7, wherein removing at least some solids from at least a portion of the secondary water enriched stream employs a method selected from the group consisting of sand filtration, membrane separation, sedimentation with the use of flocculants, sedimentation without the use of flocculants, dissolved air flotation with the use of flocculants, dissolved air flotation without the use of flocculants, centrifugation, and combinations thereof.

9. A process for the production of a highly purified water from a Fischer-Tropsch reaction water comprising one or more components selected from the group consisting of oxygenated hydrocarbons, aliphatic, aromatic and cyclic hydrocarbons, inorganic compounds, and mixtures thereof, wherein the process comprises the steps of:

a) distilling the Fischer-Tropsch reaction water in a primary treatment stage, whereby at least a fraction of non-acid oxygenated hydrocarbons are removed from the Fischer-Tropsch reaction water to produce a primary water enriched stream;

b) conducting a biological treatment of the primary water enriched stream in a secondary treatment stage, whereby at least a fraction of acidic oxygenated hydrocarbons are removed from at least a portion of the primary water enriched stream to produce a secondary water enriched stream;

c) removing by solid-liquid separation at least some solids from at least a portion of the secondary water enriched stream in a tertiary treatment stage to produce a tertiary water enriched stream; and

d) removing at least a portion of dissolved salts and residual organic species from at least a portion of the tertiary water enriched stream in a final treatment stage, whereby a highly purified water is obtained, the highly purified water comprising an aqueous stream having a chemical oxygen demand of less than 50 mg/l, a pH of from 6.0 to 9.0, a suspended solids content of less than 50 mg/l, and a total dissolved solids content of less than 100 mg/l.

10. The process as claimed in claim 9 wherein the non-acid oxygenated hydrocarbons are selected from the group consisting of alcohols, ketones, aldehydes, and mixtures thereof, and wherein the acidic oxygenated hydrocarbons are selected from the group consisting of formic acid, acetic acid, propionic acid, butyric acid, valeric acid, hexanoic acid, heptanoic acid, octanoic acid, and mixtures thereof.

11. The process as claimed in claim 9, wherein the primary treatment stage comprises degassing the Fischer-Tropsch reaction water before further processing in the primary treatment stage, whereby compounds having a very low boiling point and dissolved gases are removed from the Fischer-Tropsch reaction water.

12. The process as claimed in claim 9, wherein the biological treatment comprises at least one of anaerobic treatment and aerobic treatment.

13. The process as claimed in claim 12, wherein the aerobic treatment employs an apparatus or process selected from group consisting of activated sludge processes, biological aerated filters, trickling filters, rotating biological contacters, high-rate compact reactors, membrane bioreactors, fluidised bed reactors, and combinations thereof.

14. The process as claimed in claim 12, wherein the anaerobic treatment employs an apparatus or process selected from the group consisting of up-flow anaerobic sludge blanket processes, fixed bed systems, fluidized bed reactors, stirred tank reactors, membrane bioreactors, baffled reactors, and combinations thereof.

15. The process as claimed in claim 9, wherein the tertiary treatment stage comprises removing suspended solids from the secondary water-enriched stream produced during the biological treatment.

16. The process as claimed in claim 15, wherein removing at least some solids from at least a portion of the secondary water enriched stream employs a method selected from the group consisting of sand filtration, membrane separation, sedimentation with the use of flocculants, sedimentation without the use of flocculants, dissolved air flotation with the use of flocculants, dissolved air flotation without the use of flocculants, centrifugation, and combinations thereof.

17. The process as claimed in claim 16, wherein the membrane separation comprises at least one of microfiltration and ultrafiltration.

18. The process as claimed in claim 9, wherein residual organic species are removed in the final treatment stage by a method selected from the group consisting of chemical oxidation, reaction with ultraviolet light generated free radicals, adsorption processes, absorption processes, and combinations thereof.

19. The process as claimed in claim 18, wherein the adsorption process or absorption process comprises a method selected from the group consisting of activated carbon treatment, use of organic scavenging resins, and combinations thereof.

20. The process as claimed in claim 9, wherein dissolved salts resulting from a process conducted in the secondary treatment stage or from co-treatment of other process effluents are reduced in the final treatment stage by a method selected from the group consisting of ion exchange, reverse osmosis, nano-filtration, chemical precipitation processes, and combinations thereof.