US4002720A
Expired / Lapsed
US
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Gas desulfurization
Assignee: ExxonMobil Technology and Engineering Co
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Filing: 1974-12-24
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Granted: 1977-01-11
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Expires: 1994-12-24
Abstract
Abstract Hydrogen sulfide and its precursors can be selectively sorbed from gas streams containing the same by contacting the gas stream at elevated temperatures with a regenerable sorbent comprising a steam-treated support composited with a rare earth metal component. Presteaming the support lowers the amount of rare earth metal component needed to achieve a given activity level for hydrogen sulfide removal. Subsequent to sorption, the sorbent composite may be desorbed and regenerated by treatment with steam (desorption) and an oxidizing gas (regeneration). The sorbent capacity may be increased by the use of alkali or alkaline earth metal components as promoters. A preferred sorbent comprises lanthanum composited with presteamed alumina.
Inventors
- 👤 Kenneth S. Wheelock
- 👤 Geoffrey R. Say
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-03 07:34
CPC Classifications
B; B01; B01D; B01D53/00; B01D53/34; B01D53/46; B01D53/48; B01D53/52; B01D53/02; B01D53/04; C; C10; C10K; C10K1/00; C10K1/20; B01D2253/00; B01D2253/10; B01D2253/104; B01D2253/106; B01D2253/108; B01D2253/112; B01D2257/00; B01D2257/30; B01D2257/304; B01D2257/308; B01D2259/00; B01D2259/40; B01D2259/40083; B01D2259/40088; B01D2259/4009; B01D2259/402
Claims Analysis
Total Claims: 20
Claim 1
Independent Claim
70 words
A process for removing by sorption at least a portion of acidic gases selected from the group consisting of hydrogen sulfide, carbonyl sulfide and mixtures thereof from a gaseous mixture containing the same, which process comprises: contacting said gaseous mixture with a sorbent comprising (i) a pre-steamed inorganic oxide support selected from the group consisting of alumina, silica-alumina, zirconia, magnesia, boria and vanadia and (ii) a rare earth metal component.
Claim 2
Dependent Claim
70 words
A process for removing by sorption at least a portion of acidic gases selected from the group consisting of hydrogen sulfide, carbonyl sulfide and mixtures thereof from a gaseous mixture containing the same, which process comprises: contacting said gaseous mixture with a sorbent comprising (i) a pre-steamed inorganic oxide support selected from the group consisting of alumina, silica-alumina, zirconia, magnesia, boria and vanadia and (ii) a rare earth metal component.
Claim 3
Dependent Claim
26 words
The process of claim 1, wherein said rare earth metal component is an individual rare earth metal component or a mixture of rare earth metal components.
Claim 4
Dependent Claim
13 words
The process of claim 1, wherein said rare earth metal component comprises lanthanum.
Claim 5
Dependent Claim
24 words
The process of claim 1, wherein said rare earth metal component is a mixture of rare earth metal components comprising lanthanum, praseodymium, and neodymium.
Claim 6
Dependent Claim
12 words
The process of claim 1, wherein said inorganic oxide support is alumina.
Claim 7
Dependent Claim
22 words
The process of claim 1, wherein said gas mixture is contacted with said sorbent at a temperature in excess of 300° F.
Claim 8
Dependent Claim
29 words
The process of claim 1, wherein said sorbent additionally contains a promoter selected from the group consisting of an alkali metal component, an alkaline earth component and mixtures thereof.
Claim 9
Dependent Claim
44 words
The process of claim 1 wherein after said contacting step whereby at least a portion of said acidic gases are sorbed on said sorbent, the additional step of desorbing the sorbed acidic gases from said sorbent by contacting the acidic gas-loaded sorbent with steam.
Claim 10
Dependent Claim
30 words
The process of claim 8, wherein the desorbed sorbent is regenerated by contacting the desorbed sorbent with an oxidizing gas for a period of time sufficient to regenerate the sorbent.
Claim 11
Dependent Claim
181 words
A cyclic process for removing by sorption at least a portion of acidic gases selected from the group consisting of hydrogen sulfide, carbonyl sulfide and mixtures thereof from a gaseous mixture containing the same, which process comprises: a. contacting said gaseous mixture at a temperature of about 300° to 1,700° F. with a regenerable sorbent comprising (i) a pre-steamed inorganic oxide support selected from the group consisting of alumina, silica-alumina, zirconia, magnesia, boria and vanadia and (ii) a rare earth metal component selected from the group consisting of metals having an atomic number ranging from 57 to 71 and mixtures thereof; b. interrupting the flow of the gas stream at a predetermined time; c. contacting the sorbent with steam at a temperature ranging from about 300° to about 1,700° F. thereby desorbing said acid gases therefrom; d. contacting the desorbed sorbent with an oxidizing gas at a temperature of about 300° to about 1,700° F. for a period of time sufficient to regenerate said sorbent, and e. contacting the regenerated sorbent with the gas stream at the conditions of step (a).
Claim 12
Dependent Claim
181 words
A cyclic process for removing by sorption at least a portion of acidic gases selected from the group consisting of hydrogen sulfide, carbonyl sulfide and mixtures thereof from a gaseous mixture containing the same, which process comprises: a. contacting said gaseous mixture at a temperature of about 300° to 1,700° F. with a regenerable sorbent comprising (i) a pre-steamed inorganic oxide support selected from the group consisting of alumina, silica-alumina, zirconia, magnesia, boria and vanadia and (ii) a rare earth metal component selected from the group consisting of metals having an atomic number ranging from 57 to 71 and mixtures thereof; b. interrupting the flow of the gas stream at a predetermined time; c. contacting the sorbent with steam at a temperature ranging from about 300° to about 1,700° F. thereby desorbing said acid gases therefrom; d. contacting the desorbed sorbent with an oxidizing gas at a temperature of about 300° to about 1,700° F. for a period of time sufficient to regenerate said sorbent, and e. contacting the regenerated sorbent with the gas stream at the conditions of step (a).
Claim 13
Dependent Claim
25 words
The process of claim 10, wherein said inorganic oxide support has been steam-- treated prior to compositing the same with said rare earth metal component.
Claim 14
Dependent Claim
78 words
A process for removing by sorption at least a portion of acidic gases selected from the group consisting of hydrogen sulfide, carbonyl sulfide and mixtures thereof from a gaseous mixture containing the same, which process comprises: contacting said gaseous mixture with a sorbent prepared by first steam treating an inorganic oxide support selected from the group consisting of alumina, silica-alumina, zirconia, magnesia, boria and vanadia and subsequently compositing the steamed inorganic support with a rare earth metal component.
Claim 15
Dependent Claim
78 words
A process for removing by sorption at least a portion of acidic gases selected from the group consisting of hydrogen sulfide, carbonyl sulfide and mixtures thereof from a gaseous mixture containing the same, which process comprises: contacting said gaseous mixture with a sorbent prepared by first steam treating an inorganic oxide support selected from the group consisting of alumina, silica-alumina, zirconia, magnesia, boria and vanadia and subsequently compositing the steamed inorganic support with a rare earth metal component.
Claim 16
Dependent Claim
13 words
The process of claim 12, wherein said rare earth metal component comprises lanthanum.
Claim 17
Dependent Claim
19 words
The process of claim 12, wherein said rare earth metal component comprises a mixture of rare earth metal components.
Claim 18
Dependent Claim
19 words
The process of claim 12, wherein said rare earth metal component is a mixture comprising lanthanum, praseodymium, and neodymium.
Claim 19
Dependent Claim
10 words
The process of claim 12, said inorganic oxide is alumina.
Claim 20
Dependent Claim
29 words
The process of claim 12, wherein said sorbent additionally comprises a promoter selected from the group consisting of an alkali metal component, an alkaline earth component and mixtures thereof.
References Cited (Backward Citations)
US3864459A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1980-01-11 | 1980-07-12 | 1981-01-11 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1984-01-11 | 1984-07-12 | 1985-01-11 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1988-01-11 | 1988-07-12 | 1989-01-11 | $7700.00 | Window Closed / Lapsed |