US2009263312A1PendingUtilityA1
Hydrogen Sulfide Conversion to Hydrogen
Est. expiryApr 21, 2028(~1.7 yrs left)· nominal 20-yr term from priority
Inventors:James A. Wasas
B01D 53/8612C01B 17/0469Y02E60/36C01B 5/00Y02P20/151B01D 2256/16B01D 2255/20723C01B 3/04C01B 17/0495B01D 2255/20761B01D 2257/504C01B 17/046C01B 17/0465B01D 2257/304
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Claims
Abstract
A process and system for substantially eliminating contaminants from a gas and a gas produced therefrom.
Claims
exact text as granted — not AI-modified1 . A process for substantially eliminating contaminants from a gas comprising:
providing the gas having hydrogen sulfide and hydrocarbon in a reactor; passing the gas through a heated area having a temperature of about 50° C.-700° C., the heated area produced by a heating element comprising at least one of a catalyst and a resistance wire; converting the hydrogen sulfide to sulfur and hydrogen; separating the sulfur from the gas.
2 . The process of claim 1 wherein the hydrocarbon comprises methane.
3 . The process of claim 1 wherein the gas comprises at least one of a natural gas, industrial gas and refining gas.
4 . The process of claim 1 wherein the temperature comprises about 400-700° C.
5 . The process of claim 1 wherein the temperature comprises about at least 115° C.
6 . The process of claim 1 wherein the reactor comprises a pressure of about atmospheric pressure up to 20,684 kPa.
7 . The process of claim 1 further comprising feeding the gas into a hydrogen permeable reactor.
8 . The process of claim 1 wherein the hydrogen permeable reactor comprises a ceramic.
9 . The process of claim 1 further comprising:
providing carbon dioxide at a ratio of about 2 moles of hydrogen sulfide to one mole of carbon dioxide; converting the carbon dioxide to water and at least one of carbon and carsuls; reducing the carbon dioxide with hydrogen; and separating the water and the at least one of carbon and carsuls from the gas.
10 . The process of claim 1 further comprising:
oxidizing the hydrogen; and releasing energy in an exothermic process yielding 10-12 times an absorbed energy required in an endothermic process of converting the hydrogen sulfide to sulfur and hydrogen.
11 . A gas produced from the process of claim 1 .
12 . A process for substantially eliminating contaminants from a gas comprising:
providing the gas having hydrogen sulfide, hydrocarbon and carbon dioxide in a reactor; passing the gas through a heated area having a temperature of about 50° C.-700° C., the heated area produced by a heating element comprising at least one of a catalyst and a resistance wire; converting the hydrogen sulfide to sulfur and hydrogen; reacting the hydrogen with the carbon dioxide to form water and at least one of carbon and carsuls; and oxidizing the hydrogen with the oxygen of the carbon dioxide; and separating the sulfur, water and at least one of carbon and carsuls from the gas.
13 . The process of claim 12 wherein the hydrocarbon comprises methane.
14 . The process of claim 12 wherein the gas comprises at least one of a natural gas, industrial gas and refining gas.
15 . The process of claim 12 wherein the temperature comprises about 400-700° C.
16 . The process of claim 12 wherein the temperature comprises about at least 59° C.
17 . The process of claim 12 wherein the reactor comprises a pressure of about atmospheric pressure up to 20,684 kPa.
18 . The process of claim 12 further comprising releasing energy in an exothermic process yielding 10-12 times an absorbed energy required in an endothermic process of converting the hydrogen sulfide to sulfur and hydrogen.
19 . The process of claim 12 wherein the gas comprises a ratio of about 2 moles of hydrogen sulfide to one mole of carbon dioxide.
20 . A process for providing hydrogen as a fuel comprising:
storing a gas, having hydrogen sulfide, as a liquefied gas in a container; providing a reactor that connects to the container, the reactor having a heating element comprising at least one of a catalyst and a resistance wire; releasing the gas from the container to the reactor; passing the gas through a heated area, having a temperature of about 50° C.-700° C., produced by the heating element; converting the hydrogen sulfide to sulfur and hydrogen; and separating the sulfur from the gas.
21 . The process of claim 20 further comprising filtering the hydrogen through at least one of a hydrogen only permeable membrane and a bed of hydrogen sulfide absorbent.
22 . The process of claim 20 wherein the reactor comprises a hydrogen permeable reactor.
23 . A gas substantially free of contaminants, the contaminants removed by a process comprising:
providing a gas having hydrogen sulfide and hydrocarbon in a reactor; passing the gas through a heated area having a temperature of about 50° C.-700° C., the heated area produced by a heating element comprising at least one of a catalyst and a resistance wire; converting the hydrogen sulfide to sulfur and hydrogen; and separating the sulfur from the gas.
24 . A system for substantially eliminating contaminants from a gas comprising:
a reactor for receiving the gas, having hydrogen sulfide and hydrocarbon; and a heating element, having at least one of a catalyst and a resistance wire, within the reactor that contacts the gas to produce products substantially free of the hydrogen sulfide.Join the waitlist — get patent alerts
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