Biogasification of coal to methane and other useful products

• US 9,102,953 B2
• Filed: 12/10/2010
• Issued: 08/11/2015
• Est. Priority Date: 12/18/2009
• Status: Expired due to Fees

• Current Assignee: Ciris Energy, Inc.
• Original Assignee: Ciris Energy, Inc.
• Inventors: Downey, Robert A., Jin, Song, Fallgren, Paul H.
• Primary Examiner(s): Weber, Jon P
• Assistant Examiner(s): JOHNSON, KARA D
• Application Number:
  US12/965,285
• Publication Number:
  US 20110151533A1
• Time in Patent Office: 1,705 Days
• Field of Search: 435/167
• US Class Current: 1/1
• CPC Class Codes: C12M 21/04 for producing gas, e.g. biogas digesters for manure with production of biogas A01C3/028, biological treatment of water, waste water or sewage C02F3/00, C02F11/02, preparation of natural gas or syngas C10L3/06, C10L3/10
• CPC Class Codes: C12M 45/04 Phase separators; Separation of non fermentable material; Fractionation
• CPC Class Codes: C12P 5/023 Methane
• CPC Class Codes: Y02E 50/30 Fuel from waste, e.g. synthetic alcohol or diesel

Abstract

Method of bioconversion of coal to methane, carbon dioxide, and other valuable gaseous and liquid products in a multi-step process that may include particle size reduction, separation of non-coal materials, addition of chemicals, and multi-stage anaerobic fermentation are disclosed.

Claims

1. A process for converting coal ex situ, comprising:

(a) treating coal with a liquid that solubilizes at least a portion of the coal to form a product that is a substrate for a hydrolytic microbial population,

(b) treating at least a portion of the product of step (a) with the hydrolytic microbial population to produce a product containing fatty acids or fatty acid esters, and

(c) treating at least a liquid portion of the product from step (b) with an anaerobic microbial population that generates methane to produce a product containing methane,

wherein steps (a), (b) and (c) are performed separately.

2. The process of claim 1, wherein steps (a), (b) and (c) are performed in different vessels.

3. The process of claim 1, wherein the coal used in step (a) is pulverized coal.

4. The process of claim 1, wherein the coal used in step (a) is coal that has been treated to remove at least a portion of non-coal impurities.

5. The process of claim 1, wherein step (a) comprises the steps of:

(i) treating coal with an alkali;

(ii) treating coal with a C₁-C₄ carboxylic acid, benzoic acid, or salt or ester of such acid, or a combination thereof; and

(iii) treating coal with hydrogen peroxide in the presence of iron, and wherein the order of such steps is not essential.

6. The method of claim 5, wherein said alkali is sodium hydroxide or potassium hydroxide.

7. The process of claim 1, wherein the hydrolytic microbial population of step (b) includes an acetogen.

8. The process according to claim 1, wherein the anaerobic process may consist of a single phase, two phases or more than two phases of hydrolysis and biogasification.

9. The process of claim 1, wherein more than one hydrolysis phase vessel is utilized.

10. The process of claim 1, wherein more than one biogasification phase vessel is utilized.

11. The process of claim 1, wherein the coal is lignite, sub-bituminous coal, bituminous coal, semi-anthracite coal, anthracite coal or a combination thereof.

12. The process according to claim 1, wherein said hydrolytic microbial population of step (b) is a member selected from the group consisting of Acetivibrio, Clostridium, Lactobacillus, Ruminococcus, Zootermopsis, and other Firmicutes, Proteobacteria and a combination of these.

13. The process of claim 1, wherein said microbial population of step (c) is a member selected from the group consisting of Aerobacter, Aeromonas, Alcaligenes, Bacillus, Bacteroides, Clostridium, Escherichia, Klebsiella, Leptospira, Micrococcus, Neisseria, Paracobacterium, Proteus, Pseudomonas, Rhodopseudomonas, Sarcina, Serratia, Streptococcusand Streptomyces, Methanobaeterium omelianskii, Mb. Formieium, Mb. Sohngenii, Methanosarcina barkeri, Ms. Methaniea, Me. Masei, Methanobaeterium the rmoautotrophieum, Methanobaeterium bryantii, Methanobrevibaeter smithii, Methanobrevibaeter arboriphilus, Methanobrevibaeter ruminantium, Methanospirillum hungatei, Methanoeoeeus vannie iii, Methanothrix soehngenii, Methanothrix sp., Methanosareina mazei, Methanosareina thermophila, Methanobaeteriaeeae, Methanosareinaeeae, Methanosaetaeeae, Methanoeorpuseulaeeae, Methaanomierobiaeeae, other arehaea and a combination of these.

14. The process of claim 1, wherein one or more of said treating steps is performed in a tank, hydrolysis vessel or bioreactor that is agitated, stirred or mixed either continuously or intermittently.

15. The process of claim 1, wherein step (c) occurs in a container that contains within it a material that provides a medium for growth of methanogenic bacteria and which provides a surface area for said growth.

16. The process of claim 1, including a device to separate the effluent solids and liquids from a biogasification reactor, such that the solids may be disposed of or put to a beneficial use, and such that the liquids may be further treated, if necessary, and recycled to a chemical pretreatment tank.

17. The process of claim 1, wherein the anaerobic microbial population of step (c) includes methanogenic bacterial cells.

18. The process of claim 17, wherein the methanogenic bacterial cells are separated from the effluent liquid and solids and retained within a reactor.

19. The process of claim 1, wherein the liquid of step (a) fs includes acridine, anthracene, fluorene, chrysene, fluoranthene, pyrene or catechol.

20. The process of claim 1, wherein the liquid of step (a) includes a member selected from an alkali, a carboxylic acid, a salt of a carboxylic acid, an ester of a carboxylic acid, phosphorous acid, an ester of phosphorous acid, phosphoric acid, an ester of phosphoric acid and a peroxide.

21. The process of claim 20, wherein said liquid is an alkali.

22. The process of claim 21, wherein said alkali is NaOH or KOH.

23. The process of claim 21, wherein said alkali is a Lewis base.

24. The process of claim 20, wherein said member is a C₁-C₄ carboxylic acid, a salt of a C₁-C₄ carboxylic acid or an ester of a C₁-C₄ carboxylic acid.

25. The process of claim 24, wherein said member is acetic acid or a salt or ester of acetic acid.

26. The process of claim 20, wherein said member is phosphorous acid or an ester of phosphorous acid.

27. The process of claim 20, wherein said member is a peroxide.

28. The process of claim 27, wherein said peroxide is hydrogen peroxide.

29. The process of claim 28, wherein said treatment is with hydrogen peroxide in the presence of iron.

30. The process of claim 1, wherein step (a) comprises the steps of:

(i) treating coal with sodium hydroxide;

(ii) treating at least a portion of the product from (i) with acetic acid or a salt or ester of acetic acid, and

(iii) treating at least a portion of the product from (ii) with hydrogen peroxide in the presence of iron.

31. The process of claim 1, wherein the liquid of step (a) includes a member selected from the group consisting of aryl alcohols, metal ions, and phosphite esters.

32. The process of claim 1, wherein the liquid of step (a) includes a member selected from the group consisting of aryl alcohols, sodium hydroxide and hydrogen peroxide.