US2002041842A1PendingUtilityA1
Apparatus and process for improved hydrogen sulfide removal
Est. expirySep 29, 2020(expired)· nominal 20-yr term from priority
B01D 2257/308B01J 2220/42B01J 20/10B01D 53/02B01D 2257/304B01J 20/3236B01J 20/28004Y10S502/517B01D 2253/304B01D 2253/112B01J 20/28045B01J 20/103B01D 2257/30B01J 20/16B01J 20/0251B01D 53/52B01J 20/041B01D 2259/4146B01D 2259/40001B01D 2253/10B01J 20/3289B01J 20/08B01J 20/18B01D 2257/306B01J 20/28042B01J 20/3078B01D 2253/342B01J 20/06B01J 20/3204B01J 20/02B01J 20/28016
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Claims
Abstract
Provided is a trap and method for removing hydrogen sulfide from a gas stream. The hydrogen sulfide trap includes a monolith substrate on which is disposed zinc oxide, and a second metal or oxide thereof. In some aspects, the hydrogen sulfide trap is advantageously incorporated into systems for producing hydrogen for PEM fuel cells.
Claims
exact text as granted — not AI-modifiedWhat is claimed:
1 . A hydrogen sulfide trap comprising: a monolith substrate on which is disposed,
zinc oxide; and a second metal or oxide thereof selected from the group consisting of copper, nickel, iron, manganese, and combinations thereof dispersed on a support.
2 . The hydrogen sulfide trap of claim 1 , wherein the support is selected from the group consisting of zinc oxide, ceria, titania, zirconia, alumina, oxides of iron and combinations thereof.
3 . The hydrogen sulfide trap of claim 1 , wherein the support comprises zinc oxide.
4 . A hydrogen sulfide trap comprising a monolith substrate on which is disposed zinc oxide, and
copper or an oxide thereof dispersed on a support.
5 . The hydrogen sulfide trap of claim 4 , wherein the supported copper or oxide thereof forms a first layer adhering to the monolith substrate, and the zinc oxide forms a second layer overlying and adhering to the first layer.
6 . The hydrogen sulfide trap of claim 4 , wherein the zinc oxide forms an upstream zone disposed on an upstream segment of the monolith substrate, and the supported copper or oxide thereof forms a downstream zone on a downstream segment of the monolith substrate.
7 . The hydrogen sulfide trap of claim 4 , wherein the support comprises a second portion of zinc oxide.
8 . The hydrogen sulfide trap of claim 7 , wherein the zinc oxide and the zinc oxide-supported copper or oxide thereof form a layer adhering to the monolith substrate.
9 . The hydrogen sulfide trap of claim 7 , wherein the zinc oxide-supported copper or oxide thereof is in the form of a first layer adhering to the monolith substrate, and the zinc oxide is in the form of a second layer overlying and adhering to the first layer.
10 . The hydrogen sulfide trap of claim 7 , wherein the zinc oxide forms an upstream zone disposed on an upstream segment of the monolith substrate, and the zinc oxide supported copper or copper oxide thereof forms a downstream zone disposed on a downstream segment of the monolith substrate.
11 . The hydrogen sulfide trap of claim 4 , further comprising a binder.
12 . A process for removing hydrogen sulfide in a gas stream comprising hydrogen sulfide, the process comprising: contacting the gas stream with a hydrogen sulfide trap comprising a monolith substrate on which is disposed;
zinc oxide, and a second metal or oxide thereof selected from the group consisting of copper, nickel, iron, manganese, and combinations thereof dispersed on a support.
13 . The process of claim 12 , wherein the second metal or oxide thereof is copper.
14 . The process of claim 12 , wherein the second metal or oxide thereof is copper and the support is zinc oxide.
15 . The process of claim 14 , wherein the zinc oxide and the zinc oxide supported copper or oxide thereof is in the form of a layer.
16 . The process of claim 12 , wherein the gas stream has a space velocity of at least 300 hr −1.
17 . The process of claim 12 , wherein the gas stream has a temperature below about 500° C.
18 . The process of claim 12 , wherein the gas stream has a sulfur concentration of no more than 10 ppm.
19 . The process of claim 18 , wherein the gas stream has a sulfur concentration of no more than 100 ppb.
20 . In a system for producing hydrogen for a PEM fuel cell, the system having a hydrocarbon reformer reactor, a water-gas shift reactor, and a selective carbon monoxide oxidation reactor, the improvement comprising:
a monolith substrate on which is disposed zinc and a second metal oxide selected from the group consisting of copper, nickel, iron, manganese, and combinations thereof dispersed on a support, wherein the monolith substrate is downstream and in train with the hydrocarbon reformer reactor, and upstream and in train with the water-gas shift reactor.
21 . The system of claim 20 , wherein the second metal or oxide thereof is copper.
22 . The system of claim 21 , wherein the support comprises a second portion of zinc oxide.Join the waitlist — get patent alerts
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