BIOHYDROGEN PRODUCTION METHOD AND REACTOR
A method for producing H 2 , VFAs and alcohols from organic material is disclosed, including the steps of introducing organic material and microorganisms into a completely mixed bioreactor for producing H 2 , CO 2 , VFAs, and alcohols; sequestering CO 2 in the headspace of the reactor; recovering H 2 from the headspace; and recovering a first liquid effluent including microorganisms, VFAs, and alcohols. Also disclosed is a system for producing H 2 , VFAs and alcohols from organic material, including a completely mixed bioreactor for dark fermentation; an input for supplying microorganisms and the organic material to be broken down; a CO 2 trap in the headspace and including a solid hydroxide for sequestration of the CO 2 gas from the headspace; and a gas output for removal of a gas effluent including H 2 gas from the headspace. The system and method provide higher H 2 production rates and a H 2 stream is substantially free of CO 2 .
1 . A method for producing hydrogen by dark fermentation from organic material, comprising the steps of
introducing organic material and microorganisms into a completely mixed bioreactor for breaking down the organic material into products including H 2 gas, CO 2 gas, volatile fatty acids, and alcohols by dark fermentation;
continuously sequestering CO 2 gas within a headspace of the bioreactor for capturing the CO 2 as bicarbonate within the headspace; and
recovering at least a portion of the H 2 gas from the headspace under vacuum, whereby the recovered H 2 gas is substantially free of CO 2 .
2 . The method of claim 2 , wherein the H 2 gas is continuously recovered from the headspace.
3 . The method of claim 2 , wherein the step of continuously sequestering CO 2 within the headspace includes the further step of discontinuously removing at least a portion of the bicarbonate from the headspace.
4 . The method of claim 1 , wherein the step of continuously capturing CO 2 includes continuously maintaining a metal hydroxide in the headspace for binding of the gaseous CO 2 as metal bicarbonate within the headspace.
5 . The method of claim 5 , wherein the metal hydroxide is used in solid form.
6 . The method of claim 6 , wherein the metal hydroxide is an alkali metal hydroxide.
7 . The method of claim 7 , wherein the metal hydroxide is KOH or NaOH.
8 . The method of claim 8 , wherein the metal hydroxide is in the form of 100% pure KOH or NaOH pellets.
9 . The method of claim 1 , comprising the further step of maintaining a concentration of microorganisms in the completely mixed bioreactor at a preselected value.
10 . The method of claim 10 , comprising the further step of controlling the pH of the completely mixed bioreactor.
11 . The method of claim 11 , wherein the pH of the completely mixed bioreactor is maintained within a range of 3 to 6.8.
12 . The method of claim 12 , wherein the pH is maintained at about 5.2.
13 . A system for producing hydrogen, methane, volatile fatty acids, and alcohols from organic material, comprising:
a completely mixed bioreactor for dark fermentation;
an input for supplying to the bioreactor microorganisms and the organic material to be broken down into products including H 2 gas, CO 2 gas, volatile fatty acids (VFA) and alcohols;
a CO 2 trap in a headspace of the reactor, the CO 2 trap including a solid hydroxide for sequestration of the CO 2 gas from the headspace and capture of the CO 2 as bicarbonate within the headspace;
a gas output for removal of a gas effluent including H 2 gas from the headspace; and
a liquid output for removing a first liquid effluent including at least a portion of the microorganisms, the volatile fatty acids, and the alcohols from the bioreactor.
14 . The system of claim 14 , 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.
15 . The system of claim 14 , wherein the trap includes a solid metal hydroxide.
16 . The system of claim 16 , wherein the trap includes a solid alkali metal hydroxide.
17 . The system of claim 17 , wherein the trap includes KOH, or NaOH.
18 . The system of claim 18 , wherein the KOH is in the form of pellets of 100% KOH, or NaOH.
19 . The system of claim 14 , comprising two or more CO 2 traps separately removable from the headspace for removal of the bicarbonate during continuous operation of the reactor.
20 . The system of claim 14 , further comprising a gravity settler in fluid communication with the liquid output for separating the first liquid effluent into a settled out 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 alcohols and the microorganisms; and means for feeding the first biomass from the gravity settler to the completely mixed bioreactor for maintaining a concentration of microorganisms in the completely mixed bioreactor at a preselected value.
21 . The system of claim 21 , further comprising a dispenser for dispensing chemicals for pH adjustment into the completely mixed bioreactor.
22 . The system of claim 22 , further comprising a temperature controller for controlling a temperature of the bioreactor.