Method and system for production of hydrogen, methane, volatile fatty acids, and alcohols from organic material
A method for producing H 2 , methane, VFAs and alcohols from organic material, including the steps of introducing organic material and microorganisms into a completely mixed bioreactor for producing H 2 , CO 2 , VFAs, and alcohols; recovering H2 and CO2; recovering a first liquid effluent including microorganisms, VFAs, and alcohols; introducing the first liquid effluent into a gravity settler for separating into a first biomass including microorganisms and a second liquid effluent including VFAs, alcohols and microorganisms; introducing the second liquid effluent into a separation module for separating into a second biomass including microorganisms and a third liquid effluent including VFAs and alcohols; recovering at least a portion of the third liquid effluent; and providing a recovered biomass by recovering at least a portion of the first biomass, the second biomass, or both, and introducing the recovered biomass into a biomethanator for production of CH 4 and CO 2 .
1. A method for acetone-butanol-ethanol (ABE) fermentation of organic material, comprising the steps of:
a) conducting an ABE fermentation of the organic material in a completely mixed bioreactor to produce acetone, butanol, ethanol (ABE), volatile fatty acids, H 2 and CO 2 , wherein the ABE fermentation step includes introducing organic material and ABE producing microorganisms into a completely mixed bioreactor and controlling a pH of the completely mixed bioreactor to maintain the pH at 3.5-5.5 for breaking down the organic material into products including acetone butanol, ethanol (ABE), volatile fatty acids, H 2 and CO 2 ;
b) recovering at least a portion of the H 2 and of the CO 2 from the completely mixed bioreactor;
c) maintaining a biomass concentration in the completely mixed bioreactor, wherein the step of maintaining a biomass concentration includes recovering a first liquid effluent from the completely mixed bioreactor, the first liquid effluent including at least a portion of the microorganisms, the volatile fatty acids, and the ABE;
d) introducing the first liquid effluent into a gravity settler for separating at least a portion of the first liquid effluent into a first biomass including at least a portion of the microorganisms and a second liquid effluent including at least a portion of the volatile fatty acids, the ABE and the microorganisms;
e) recirculating at least a portion of the first biomass into the completely mixed bioreactor to maintain a concentration of microorganisms in the completely mixed bioreactor at a preselected value;
f) producing methane in a biomethanator from the first biomass extracted from the first liquid effluent of the ABE fermentation step, wherein the step of producing methane further includes introducing at least a portion of the second liquid effluent into a separation module for separating at least a portion of the second liquid effluent into a second biomass, including at least a portion of the microorganisms, that is broken down to generate methane and a third liquid effluent including at least a portion of the volatile fatty acids and the ABE;
h) recovering the volatile fatty acids and ABE from the third liquid effluent; and
i) providing a recovered biomass by recovering at least a portion of the first biomass, the second biomass, or both, and introducing the recovered biomass into the biomethanator for the production of CH 4 and CO 2 .
2. The method of claim 1 , further comprising controlling a pH of the biomethanator.
3. The method of claim 2 , wherein controlling the pH comprises adding pH adjustment compounds to the completely mixed bioreactor, the biomethanator, or both.
4. The method of claim 1 , further comprising controlling a temperature of the completely mixed bioreactor, the biomethanator, or both.
5. The method according to claim 4 , wherein the temperature of the completely mixed bioreactor is maintained at a temperature range from about 25° C. to about 37° C.
6. The method according to claim 4 , wherein the temperature of the biomethanator is maintained in a temperature range from about 25° C. to about 37° C.
7. The method according to claim 1 , wherein the microorganisms include one or more of the species selected from the group consisting of Clostridium butyricum, Clostridium beijerinckii, Clostridium acetobutyricum, Clostridium bifermentants, Enterobacter aerogenes, Bacillus megaterium, Bacillus thuringiensis , and Rhodobacter sphaeroides.
8. The method according to claim 1 , wherein the completely mixed bioreactor is a reactor selected from the group consisting of a single continuously stirred tank reactor, a multi-stage continuously stirred tank reactor, an up-flow anaerobic sludge blanket reactor, an expanded bed granular sludge blanket reactor, a down-flow anaerobic granular media reactor, an up-flow anaerobic granular media reactor, an anaerobic baffled tank reactor, an anaerobic migrating blanket reactor, and an anaerobic fluidized bed bioreactor.