Maximizing production of hydrogen from waste materials by active removal of hydrogen

Patent metadata

Field	Value
Publication number	US-10030254-B2
Application number	US-201515324605-A
Country	US
Kind code	B2
Filing date	Sep 2, 2015
Priority date	Sep 11, 2014
Publication date	Jul 24, 2018
Grant date	Jul 24, 2018

Abstract

The present invention provides a method of producing hydrogen from a waste material, comprising steps of fermenting 100 a fermentation mixture comprising the waste material in a reactor 1 with a headspace 1a under anaerobic conditions, removing 200 hydrogen from a gas from the headspace 1a during fermentation to produce a hydrogen gas and a remainder gas and recirculating 300 at least a portion of the remainder gas back to the headspace 1a. An apparatus for producing hydrogen and recirculating at least a portion of the remainder gas to the headspace 1a is also provided.

First claim

What is claimed is:

1. A method of producing hydrogen from a waste material, comprising steps of:
a) fermenting a fermentation mixture comprising the waste material in a reactor with a headspace under anaerobic conditions;
b) removing hydrogen from a gas generated in the headspace during fermentation to provide hydrogen and a remainder gas; and
c) recirculating at least a portion of the remainder gas to the reactor.

2. The method of claim 1 , further comprising a step of introducing at least one microorganism into the fermentation mixture.

3. The method of claim 2 , wherein the at least one microorganism is selected from the bacteria genera Acetivibrio, Acetoanaerobium, Acetofilamentum, Acetogenium, Acetothermus, Acidaminobacter, Anaerobiospirillum, Anaerorhabdus, Anaerovibrio, Atopobium, Bacteroides, Bifidobacterium, Bilophila, Butyrivibrio, Campylobacter, Catonella, Centipeda, Dialister, Dichelobacter, Fervidobacterium, Fibrobacter, Fusobacterium, Halanaerobacter, Halanaerobium, Ilyobacter, Johnsonella, Lachnobacterium, Leptotrichia, Malonomonas, Megamonas, Mitsuokella, Oxalobacter, Pectinatus, Pelobacter, Porphyromonas, Prevotella, Propionibacterium, Propionigenium, Propionispira, Rikenella, Roseburia, Ruminobacter, Sebaldella, Selenomonas, Sporomusa, Succinimonas, Succinivibrio, Syntrophobacter, Syntrophomonas, Sutterella, Saponavida, Thermobacteroides, Thermosipho, Thermotoga, Tissierella, Wolinella, Zymophilus, Desulfobacter, Desulfobacterium, Desulfobulbus, Desulfococcus, Desulfomicrobium, Desulfomonas, Desulfomonile, Desulfonema, Desulfosarcina, Desulfotomaculum, Desulfovibrio, Desulfurella, Desulfuromonas, Thermodesulfobacterium, Acidaminococcus, Megasphaera, Syntrophococcus, Veillonella, Coprococcus, Peptococcus, Peptostreptococcus, Ruminococcus, Sarcina, Clostridium, Amoebobacter, Chromatium, Lamprobacter, Thiocapsa, Thiocystis, Thiodictyo, Thiopedia, Thiospirillum, Ectothiorhodospira, Rhodobacter, Rhodocyclus, Rhodomicrobium, Rhodopila, Rhodopseudomonas, Rhodospirillum, Erythrobacter, Methanobacterium, Methanobrevibacter, Methanococcu, Methanococcoides, Methanolobus, Methanolacinia, Methanomicrobium, Methanogenium, Methanospirillum, Methanoplanus, Methanothrix, Methanothermus, Methanocorpusculum, Methanoculleus, Methanohalobium, Methanohalophilus, Methanosarcina, Methanosphaera, Eubacterium, Abiotrophia, Atopobium, Gemella, Granulicatella, Finegoldia, Lactobacillus, Actinomyces, Arcanobacterium, Bulleidia, Collinsella, Cryptobacterium, Holdemania, Rothia, Pseudoramibacter, Mogibacterium, Slackia , and Eggerthella.

4. The method of claim 1 , wherein the fermentation mixture has a pH in a range of from about 3 to about 6.5.

5. The method of claim 4 , further comprising a step of maintaining a substantially constant pH in the fermentation mixture during the fermenting step.

6. The method of claim 4 , further comprising a step of monitoring the pH in the fermentation mixture continuously or periodically during the fermenting step.

7. The method of claim 1 , wherein the fermentation mixture has a temperature in a range of from about 25° C. to about 40° C. during the fermentation step.

8. The method of claim 1 , further comprising a step of adding a nitrogen source to the fermentation mixture.

9. The method of claim 8 , wherein the nitrogen source is added to the fermentation mixture in an amount sufficient to provide an amount of nitrogen in the fermentation mixture in a range of from about 0.01 wt. % to about 10 wt. % of the fermentation mixture.

10. The method of claim 1 , further comprising a step of adding one or more vitamins to the fermentation mixture, wherein the one or more vitamins are selected from thiamine, cobalamine, riboflavine, niacinamide, pantothenic acid, biotin, ascorbic acid, retinol, procalciol, tocopherol, folic acid and pyridoxamine.

11. The method of claim 1 , wherein the fermenting step is a continuous fermentation process.

12. The method of claim 1 , wherein the fermentation mixture is agitated during the fermenting step.

13. The method of claim 1 , further comprising the steps of monitoring a partial pressure of hydrogen in the headspace of the reactor and adjusting the partial pressure of hydrogen based on the monitored partial pressure of hydrogen in the headspace of the reactor.

14. The method of claim 1 , wherein removing hydrogen is carried out using an apparatus selected from a molecular sieve, an adsorbent and a selective membrane.

15. The method of claim 1 , further comprising a step of removing carbon dioxide from the gas in the headspace.

16. The method of claim 1 , wherein the fermentation mixture has a pH of from about 4 to about 5.5.

17. The method of claim 1 , wherein the fermentation mixture has a temperature in a range of from about 29° C. to about 37° C.

18. The method of claim 1 , wherein the nitrogen source is added to the fermentation mixture in an amount sufficient to provide an amount of nitrogen in the fermentation mixture in a range of from about 2 wt. % to about 7 wt. %.

19. The method of claim 1 , wherein the fermentation mixture has a pH in a range of from about 3 to about 6.5, a temperature in a range of from about 25° C. to about 40° C. and the nitrogen source is added to the fermentation mixture in an amount sufficient to provide an amount of nitrogen in the fermentation mixture in a range of from about 0.1 wt. % to about 10 wt. %.

20. The method of claim 1 , wherein the fermentation mixture has a pH of from about 4 to about 5.5, a temperature in a range of from about 29° C. to about 37° C. and the nitrogen source is added to the fermentation mixture in an amount sufficient to provide an amount of nitrogen in the fermentation mixture in a range of from about 2 wt. % to about 7 wt. %.

Assignees

• Haas Charles Nathan
• Univ Drexel

Inventors

• Haas Charles Nathan

Classifications

• C01B2203/041

  In-situ membrane purification during hydrogen production · CPC title

• C01B2203/0425

  In-situ adsorption process during hydrogen production · CPC title

• C12P3/00 Primary

  Preparation of elements or inorganic compounds except carbon dioxide {(recovery of carbon dioxides as by-products C12F3/02)} · CPC title

• C12M41/26

  of pH · CPC title

• C12M29/24

  Recirculation of gas · CPC title