Apparatus and methods for fertilizer production
Systems and apparatuses for converting nitrogen gas, such as from ambient air, into fertilizer via interaction with a controlled plasma field using low energy inputs. Mechanisms and methods for cooling splitter apparatuses during production of fertilizer from nitrogen gas. Methods of producing fertilizer from nitrogen gas, such as ambient air, via a splitter creating a plasma output, and for collecting produced fertilizer.
1. A system for producing fertilizer comprising:
a reactor vessel comprising a closed chamber, the reactor vessel comprising an upper outer dome and a lower outer dome, with the upper and lower domes forming a gas and liquid tight seal therebetween,
the closed chamber housing:
a collection liquid comprising water, the water having a water surface,
a reactor splitter configured to create a plasma output via electricity, the plasma output configured to split nitrogen, the reactor splitter having a two part electrode arrangement comprising
a large electrode positioned on an upper end of the reactor splitter and protruding through a top of the reactor vessel, the large electrode firing the plasma output onto the water surface,
a small electrode mounted adjacent a bottom of the reactor, the small electrode having an antenna, a tip of the antenna aligned below the plasma output of the large electrode, the small electrode and the antenna submerged below the water surface, the antenna focusing the plasma output into a plasma beam in the collection liquid to thereby increase efficiency of the reactor splitter,
wherein the large electrode has a diameter of about one-quarter inch, the large electrode being larger than the small electrode such that the large electrode is sized to withstand the amount of energy and heat required to generate the plasma output,
an output evacuation nozzle for evacuating collection liquid from the reactor vessel to a collection vessel,
a gas input configured to deliver nitrogen to the reactor vessel,
a collection vessel, the collection vessel positioned to collect collection liquid containing split nitrogen from the reactor vessel for recombination of split nitrogen into an aqueous nitric acid solution, and
a cooling arrangement for preventing the reactor splitter from overheating, wherein the cooling arrangement comprises the water in the reactor vessel and an input drip emitter in the reactor vessel for selectively introducing a flow of water into the reactor vessel, and removal of collection liquid to the collection vessel via the output evacuation nozzle.
2. The system of claim 1 , wherein the system is powered by conventional AC current.
3. The system of claim 1 , further comprising a solar panel providing the system with electricity.
4. A method of manufacturing fertilizer comprising:
providing a reactor vessel and collection vessel according to claim 1 ,
powering the reactor splitter via electricity to create the plasma output,
cooling the splitter during plasma output via the cooling arrangement to prevent over-heating,
providing a supply of gas containing nitrogen to the plasma output to thereby create split nitrogen,
collecting the split nitrogen in the water of the reactor vessel to form the collection liquid,
evacuating collection liquid containing split nitrogen to the collection vessel,
allowing the split nitrogen to recombine into nitric acid in the water in the collection vessel to form an aqueous nitric acid output, and
transferring the aqueous nitric acid to a secondary collection vessel for use as fertilizer.
5. The method of claim 4 , wherein the gas comprises ambient air.
6. The method of claim 4 , wherein the gas is from a compressed source.
7. The method of claim 4 , wherein the aqueous nitric acid output has a pH of between about 1.5 and about 1.0.
8. The method of claim 7 , further comprising introducing a source material into the aqueous nitric acid and allowing the aqueous nitric acid to breakdown the source material to produce a complex fertilizer end product.
9. The method of claim 7 , wherein the source material comprises a mineral.
10. The method of claim 7 , wherein the source material comprises an organic material.
11. The system of claim 1 , further comprising a temperature probe in the reactor vessel communicating with an external temperature control circuit to temporarily turn off the large electrode in the event of overheating in the reactor vessel.
12. The system of claim 11 , wherein the reactor vessel comprises PVC.
13. The method of claim 4 , further comprising a temperature probe in the reactor vessel communicating with an external temperature control circuit to temporarily turn off the large electrode in the event of overheating in the reactor vessel.
14. The method of claim 13 , wherein the reactor vessel comprises PVC.
15. The method of claim 4 , wherein the aqueous nitric acid output has a pH of between about 1.5 to 1.6.