Bioreactors with integrated catalytic nitrogen fixation
Nitrogen in a form suitable for feeding a population of microbes in a bioreactor is produced by reacting nitrogen gas and hydrogen gas to form ammonia plus an unreacted gas stream under conditions favorable to having little unreacted nitrogen gas in the unreacted gas stream. The ammonia, or a compound derived from the ammonia is fed to the microbes and the unreacted gas stream is optionally fed back into the reaction, or fed into the bioreactor. Oxygen can be produced, such as by electrolysis, and also provided to the microbes. Hydrogen from the electrolysis can be added to the hydrogen being reacted with nitrogen gas, and/or can be added to the bioreactor. Where nitrogen gas is produced from air separation, the residual gases can be another source of oxygen.
1. A system comprising: a nitrogen separator that separates air into a nitrogen-rich gas stream and an oxygen-rich gas stream;
a nitrogen fixation reactor in fluid communication with the nitrogen separator to receive the nitrogen-rich stream, and further configured to receive hydrogen, and configured to react nitrogen with hydrogen to produce an ammonia stream; and
a bioreactor comprising a liquid medium including a population of microbes, the bioreactor in fluid communication with the nitrogen fixation reactor to receive a stream of a fixed nitrogen compound derived from the ammonia stream to support growth of the population of microbes; and
wherein the nitrogen separator is in fluid communication with the bioreactor to supply at least some of the oxygen-rich stream produced by the nitrogen separator to the bioreactor.
2. The system of claim 1 wherein the nitrogen fixation reactor produces an unreacted gas stream comprising hydrogen, wherein the nitrogen fixation reactor is in a second fluid communication with the bioreactor to provide at least some of the unreacted gas stream to the bioreactor, and wherein at least some of the microbes of the population comprise hydrogenase enzymes capable of deriving energy through hydrogen oxidation.
3. The system of claim 1 further comprising a control system configured to vary the ratio of hydrogen to nitrogen entering the nitrogen fixation reactor.
4. The system of claim 1 further comprising
a steam methane reformer configured to perform both a steam methane reformation reaction and a water-gas shift reaction to produce a stream including both hydrogen and CO 2 , and
a separator in fluid communication with the steam methane reformer and configured to separate the stream including both hydrogen and CO 2 into a hydrogen stream and a CO 2 stream,
wherein the separator is in fluid communication with the bioreactor to provide at least some of the CO 2 stream to the bioreactor, and wherein the separator is also in fluid communication with the nitrogen fixation reactor to provide at least some of the hydrogen stream to the nitrogen fixation reactor.
5. The system 1 further comprising
a gasifier configured to gasify a carbon-containing substrate to produce a gas stream including carbon monoxide.
6. The system of claim 1 further comprising a water splitter configured to receive a flow of water and to produce from the water both a hydrogen stream and an oxygen stream, and wherein the water splitter is in fluid communication with the nitrogen fixation reactor to provide at least some of the hydrogen stream to the nitrogen fixation reactor.
7. The system of claim 6 wherein the water splitter is in fluid communication with the bioreactor to provide at least some of the oxygen stream produced by the water splitter to the bioreactor.
8. The system of claim 1 further comprising
a nitrogen sensor disposed within the bioreactor; and
a control system configured to regulate the introduction of ammonia into the bioreactor based on a signal from the nitrogen sensor.
9. The system of claim 8 wherein
the nitrogen fixation reactor is further configured to produce an unreacted gas stream and is in further fluid communication with the bioreactor to provide at least some of the unreacted gas stream to the bioreactor, and
the system further comprises a hydrogen sensor dispersed within the bioreactor and connected to the control system, wherein the control system is further configured, responsive to a signal from the hydrogen sensor in addition to that from the nitrogen sensor, to regulate the nitrogen fixation reactor, and to regulate the introduction of the unreacted gas stream and the stream of the fixed nitrogen compound into the bioreactor.
10. The system of claim 1 further comprising an ammonia reservoir disposed between the nitrogen fixation reactor and the bioreactor.
11. The system of claim 1 wherein the nitrogen fixation reactor comprises an insulated tubular reactor, wherein the bioreactor is additionally in fluid communication with the tubular reactor to receive an unreacted hydrogen stream separately from the stream of the fixed nitrogen compound.
12. The system of claim 11 wherein the tubular reactor includes a first exit valve and a second exit valve at opposite ends thereof.
13. A system comprising:
a kiln used in the production of a mineral product;
a nitrogen fixation reactor configured to produce an ammonia stream and an unreacted gas stream;
a nitrogen separator configured to produce a nitrogen-rich stream and an oxygen-rich stream;
a water splitting system configured to produce a hydrogen stream and an oxygen stream;
a bioreactor comprising a liquid medium including a population of microbes, the bioreactor in fluid communication with the nitrogen fixation reactor to receive a stream of a fixed nitrogen compound derived from the ammonia stream to support growth of the population of microbes; and
a solar concentrator system configured to
provide heat to the kiln,
provide heat to the water splitting system, and
provide heat to the nitrogen fixation reactor, wherein
the nitrogen separator is in fluid communication with the bioreactor to provide at least some of the oxygen-rich stream to the bioreactor, or the water splitting water system is in fluid communication with the bioreactor to provide at least some of the oxygen stream to the bioreactor,
the kiln is in fluid communication with the bioreactor to provide at least some of the CO 2 produced by the kiln to the bioreactor,
the water splitting water system is in fluid communication with the nitrogen fixation reactor to provide at least some of the hydrogen stream to the nitrogen fixation reactor, and
the nitrogen fixation reactor is in further fluid communication with the bioreactor to provide at least some of the unreacted gas stream to the bioreactor.
14. The system of claim 13 wherein the water splitting system comprises an electrolyzer, the system further comprising
a renewable electricity source configured to at least partially supply electricity to the kiln, and further configured to supply electricity to the electrolyzer.