Systems and methods for anaerobic digestion and collection of products

1. A bioreactor system comprising:

(a) a first module comprising a first plurality of anaerobic bacteria;

(b) a second module comprising a second plurality of anaerobic bacteria;

(c) an output of the first module connected to an input of the second module and configured to carry liquid, biomass, and sludge from the first module to the second module;

(d) a first separator configured to remove volatile organic acids from the first module;

(e) a second separator configured to remove ammonia from the second module; and

(f) a monitor configured to activate the second separator in response to detecting a pH of the bioreactor system higher than 8.0, wherein the first plurality of anaerobic bacteria comprises a different mixture of anaerobic bacteria than the second plurality of anaerobic bacteria.

2. The bioreactor system of claim 1 , wherein a majority of the first plurality of anaerobic bacteria is acidogenic bacteria, and wherein a majority of the second plurality of anaerobic bacteria is acetogenic bacteria.

3. The bioreactor system of claim 1 , wherein a majority of the first plurality of anaerobic bacteria is acidogenic bacteria, and wherein a majority of the second plurality of anaerobic bacteria is methanogenic bacteria.

4. The bioreactor system of claim 1 , wherein without the removal of volatile organic acids, the pH is not maintained between 5.9 and 8.0.

5. The bioreactor system of claim 1 , wherein the first and second pluralities of anaerobic bacteria each comprise aquatic anaerobic bacteria and ruminant anaerobic bacterial.

6. The bioreactor system of claim 5 , wherein a majority of the first plurality of anaerobic bacterial is ruminant anaerobic bacteria, and wherein a majority of the second plurality of anaerobic bacteria is aquatic anaerobic bacteria.

7. The bioreactor system of claim 5 , wherein the first plurality of anaerobic comprises the ruminant anaerobic bacteria in a volume:volume ratio of about 100:1 to 1500:1 of the aquatic anaerobic bacteria, and wherein the second plurality of anaerobic bacteria comprises the aquatic anaerobic bacteria in a volume:volume ratio of about 100:1 to 1500:1 of the ruminant anaerobic bacteria.

8. The bioreactor system of claim 5 , wherein the ruminant anaerobic bacteria is selected from a group consisting of the following: Fibrobacter succinogenes, Butyrivibrio fibrisolvens, Ruminococcus albus, Clostridium locheadii, Bacteroides ruminicola, Ruminobacter amylophilus, Selenomonas ruminatium, Succinomonas amylolytica, Streptococcus bovis, Selenomonas lactilytica, Megasphaera elsdenii, Lachnospira multiparus, Neocalamastix , and a combination thereof.

9. The bioreactor system of claim 5 , wherein the aquatic anaerobic bacteria is selected from the group consisting of the following: Methanobrevibacter ruminantium, Methanomicrobium mobile, Syntrophomonas wolfei , and a combination thereof.

10. The bioreactor system of claim 1 , wherein the first module comprises an input configured to receive a feedstock.

11. The bioreactor system of claim 1 , wherein the first module comprises an output configured to collect volatile organic acids from the bioreactor system.

12. The bioreactor system of claim 1 , wherein the second module comprises an output configured to collect ammonia from the bioreactor system.

13. The bioreactor system of claim 1 , wherein the second module comprises an output configured to collect methane from the bioreactor system.

14. The bioreactor system of claim 1 , wherein the second separator is a distillation separator or a vaporizer.

15. A bioreactor system for converting cellulose-containing feedstock into products, wherein the system comprises:

(a) a first module comprising a feedstock input configured to receive a cellulose-containing feedstock, a first output and a second output, a first plurality of anaerobic microbes, and the cellulose-containing feedstock wherein the first plurality of anaerobic microbes digest the cellulose-containing feedstock to generate an organic acid product and a partially-digested feedstock;

(b) a first separator in communication with the first output of the first module, the first separator configured to remove the organic acid product from the partially-digested feedstock;

(c) a second module comprising a partially-digested feedstock input in communication with the second output of the first module, more than one output, and a second plurality of anaerobic microbes, wherein the partially-digested feedstock input receives a slurry of the partially-digested feedstock from the second output of the first module, and wherein the second plurality of anaerobic microbes digest the partially-digested feedstock to generate a methane product and an ammonia product; and

(d) a second separator in communication with the second module, wherein the second separator is configured to remove the ammonia product from the partially-digested feedstock and wherein the first plurality of anaerobic microbes comprises a different mixture of anaerobic microbes than the second plurality of anaerobic microbes.

16. The bioreactor system of claim 15 , wherein the first plurality of anaerobic microbes comprises ruminant anaerobic bacteria.

17. The bioreactor system of claim 15 , wherein the second plurality of anaerobic microbes comprises aquatic anaerobic bacteria.

18. The bioreactor system of claim 15 , wherein the first plurality of anaerobic microbes comprises a volume:volume ratio of about 100:1 to 1500:1 between ruminant anaerobic bacteria and aquatic anaerobic bacteria, and wherein the second plurality of anaerobic microbes comprises a volume:volume ratio of about 100:1 to 1500:1 between aquatic anaerobic bacteria and ruminant anaerobic bacteria.

19. A method of collecting products from cellulose-containing feedstock using the bioreactor system of claim 1 , the method comprising:

delivering a cellulose-containing feedstock to the first module of the bioreactor system;

transferring partially-digested cellulose-containing feedstock and at least a portion of the first plurality of anaerobic bacteria to the second module of the bioreactor system;

converting the cellulose-containing feedstock to usable products within the bioreactor system, wherein the usable products include the ammonia, volatile fatty acids, and methane; and

collecting at least one of the volatile fatty acids from the first module or the ammonia and methane from the second module.

20. The method of claim 19 , wherein the first plurality of anaerobic bacteria comprises ruminant anaerobic bacteria and the second plurality of anaerobic bacteria comprises aquatic anaerobic bacteria.

21. The method of claim 19 , wherein the first plurality of anaerobic bacteria comprises acidogenic bacteria and the second plurality of anaerobic bacteria comprises acetogenic bacteria, wherein the acidogenic bacteria and acetogenic bacteria are present in the bioreactor system at a ratio such to maintain the pH of the bioreactor system between 5.9 and 8.0.

22. The method of claim 19 , wherein 59% or greater of the cellulose-containing feedstock is converted to the usable products.

23. The method of claim 19 , further comprising collecting volatile fatty acids in response to the pH of the bioreactor system dropping below a threshold level.

24. The method of claim 19 , further comprising collecting ammonia in response to the pH of the bioreactor system increasing above a threshold level.

25. A method of converting biomass feedstock into products using the bioreactor system of claim 16 , the method comprising:

anaerobically digesting or breaking down the cellulose-containing feedstock in the first module to produce the organic acid product and the partially-digested feedstock;

separating the organic acid product from the partially-digested feedstock;

transferring the partially-digested feedstock to the second module;

anaerobically digesting or breaking down the partially-digested feedstock in the second module to produce the ammonia product and the methane product; and

removing the ammonia product and the methane product from the second module.