US2008196305A1PendingUtilityA1
Continuous hydrogen and alcohol generator from coal
Est. expiryMar 24, 2025(expired)· nominal 20-yr term from priority
Inventors:Sten R. Gerfast
C10J 2200/152C10J 2300/093C10J 2300/1665C10J 2200/09C10J 2300/0956C10J 3/42C10J 2200/15C10J 3/30C10J 2300/0973
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Claims
Abstract
A gas generator with the sole input of air, water and coal that continuously produces hydrogen and carbon monoxide and further reacts these two gases into alcohol. This gas generator/reactor is using its own by-products and is therefore also self sustaining.
Claims
exact text as granted — not AI-modified1 . A continuous, self-sustaining hydrogen and carbon monoxide gas generator comprising:
A rotating gas injector disc having a cylindrical extension with internal passages to a first air injection nozzle and a second steam injector nozzle, and said extension is fitted to a first ring-shaped air supply line fixed to a tower, and said extension is also fitted to a second ring-shaped steam supply line, also fixed to said tower, alternately but continuously injecting air and steam at changing injection angles into said tower containing a hot bed of coke, reducing it to hydrogen and carbon monoxide.
2 . A continuous, self-sustaining gas generator and reactor producing alcohol comprising:
A rotating gas injector disc having a cylindrical extension with internal passages to a first air injection nozzle and a second steam injector nozzle, and said extension is fitted to a first ring-shaped air supply line fixed to a tower, and said extension is also fitted to a second ring-shaped steam supply line, also fixed to said tower, alternately but continuously injecting air and steam into said tower containing a hot bed of coke, reducing it to hydrogen and carbon monoxide, further reacting said gases into methyl alcohol in the presence of a catalyst.
3 . The continuous self-sustaining gas generator as defined in claim 1 wherein a charge of coke is loaded into said tower, said coke is ignited and air is injected through said disc's first said nozzle until said coke has achieved at least 800 degree C., when steam is injected through said second nozzle, reducing the hot coke into hydrogen and carbon monoxide that exits into output pipes in said tower, with the injection disc's rotation providing a constantly renewed air injection and steam injection to maintain correct reducing temperature and maximizing gas production in said tower.
4 . A continuous gas generator and reactor producing alcohol as defined in claim 2 having a rotating gas injector disc with a first air injection nozzle, and a second steam injector nozzle alternately but continuously injecting air and steam into a tower containing a hot bed of coke, providing a constantly renewed air and steam injection, reducing said coke to hydrogen and carbon monoxide and further reacting said gases into methyl alcohol in the presence of a metal oxide catalyst.
5 . A continuous gas generator as defined in claim 1 wherein said first nozzle is circumscribing 180 degrees on the upper part of said disc, and said second nozzle is circumscribing the other 180 degrees on the lower part of said disc.
6 . A continuous gas generator as defined in claim 5 wherein said circumscribed 360 degrees can be split into different angles for said first and second nozzles.
7 . A continuous gas generator as defined in claim 1 wherein said steam supply line is connected to a heat exchanger that is using the heat from said tower to heat water to steam.
8 . A continuous gas generator as defined in claim 2 wherein said cylindrical extension is fixed to a drive gear driven through an idler gear in the wall of said tower, into a smaller gear on the outside of said tower.
9 . A continuous gas generator as defined in claim 1 wherein said rotating disc is having a central shaft fixed to the base of said tower on one end and the other end of said shaft fixed to a centrally located deflector supported with rods to the top of said tower.
10 . A continuous gas generator as defined in claim 9 wherein said disc's dual nozzles are fitted into slots in said deflector.
11 . A continuous gas generator/reactor as defined in claim 2 wherein said hot bed is conducting heat to the outside of said tower where said heat is conducted into “the hot cylinder” of a heat engine such as a Stirling heat engine producing rotation on its output shaft.
12 . A continuous gas generator as defined in claim 11 wherein said output shaft is driving a fan for compressing air for usage in said air nozzle.
13 . A continuous gas generator as defined in claim 11 wherein said output shaft is driving said gear on said disc.
14 . A continuous gas generator as defined in claim 11 wherein said shaft, gears and all rotating parts are having bearings and support washer made from heat resistant graphite material such as graphite or other materials with service temperature of 3500 degree F. or greater.
15 . A continuous gas generator as defined in claim 1 wherein said bed of coke is replenished as needed by a controlled loading trap.
16 . A continuous gas generator as defined in claim 1 wherein the sole input to said gas generator is air, water and coke and the output is hydrogen and carbon monoxide.
17 . A continuous gas generator as defined in claim 2 wherein the output of said generator is hydrogen and carbon monoxide that is further fed into a reactor container reacting these two gases under pressure into an alcohol.
18 . A continuous gas generator/reactor as defined in claim 2 wherein the output of said reactor is pressurized, containing a catalyst, and the reduction product is methyl alcohol.
19 . A continuous gas generator as defined in claim 3 wherein output pipes have control valves, and input of air, water, steam and coke have controlling devices controlled by a micro controller.
20 . A continuous gas generator as defined in claim 1 wherein said internal passages terminate at a first fixed ring-shaped air outlet at the top of said tower, and also terminates at a second fixed ring-shaped gas outlet at the top of said tower.
21 . A continuous gas generator as defined in claim 20 wherein said air outlet is connected below the water level of a water filled tank, and said tank is connected to a air suction device exhausting air to the atmosphere, and said suction device is having a control device.
22 . A continuous gas generator as defined in claim 20 wherein said gas outlet is connected to an internal pipe in a heat exchanger, and the gas in said pipe is connected to a reaction container.
23 . A continuous gas generator as defined in claim 20 wherein
said gas outlet is connected to a combustion engine turning an electric generator.
24 . A continuous gas generator as defined in claim 20 wherein said gas outlet is connected to a reaction container, containing catalysts, to form liquid hydro carbon products or artificial fuels.
25 . A continuous gas generator as defined in claim 21 wherein said tanks contains fly-ash residue and nitrogen-rich bubbling air that becomes fertilizer.Join the waitlist — get patent alerts
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