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Process for removing hydrogen sulphide from process gases using solid acceptors, process for cyclic regenerating the used acceptors at high temperature, as well as process for preparing acceptors, which are suitable for this process

Assignee: Nederlandse Organisatie voor Toegepast Natuurwetenschappelijk Onderzoek TNO
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Filing: 1982-10-29
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Granted: 1984-12-18
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Expires: 2002-10-29
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Abstract

Abstract An acceptor of MnO x or iron oxide, wherein x has a value of from 1 to 1.5, supported on a (γ)-alumina carrier which may contain silica, is used to remove hydrogen sulfide from process gases. The acceptor is regenerated with steam in a reducing atmosphere at a temperature of from 300° C. to 700° C.

Inventors

  • 👤 Willem A. de Jong
  • 👤 Berend J. van der Linde

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-29 18:27
CPC Classifications
B; B01; B01D; B01D53/00; B01D53/34; B01D53/46; B01D53/48; B01D53/52; Y; Y10; Y10S; Y10S502/00; Y10S502/515; Y10S502/517

Claims Analysis

Total Claims: 16
Claim 1
Independent Claim 70 words
A regenerative method for removing hydrogen sulphide from process gases which comprises: (a) contacting said gases with an MnO x or iron oxide acceptor, wherein x has a value of from 1 to 1.5, and wherein said acceptor is supported on a (γ)-alumina carrier, and (b) regenerating the acceptor by contacting the acceptor with steam at a temperature of from 300° C. to 700° C., wherein said steam contains hydrogen.
Claim 2
Dependent Claim 70 words
A regenerative method for removing hydrogen sulphide from process gases which comprises: (a) contacting said gases with an MnO x or iron oxide acceptor, wherein x has a value of from 1 to 1.5, and wherein said acceptor is supported on a (γ)-alumina carrier, and (b) regenerating the acceptor by contacting the acceptor with steam at a temperature of from 300° C. to 700° C., wherein said steam contains hydrogen.
Claim 3
Dependent Claim 11 words
A method according to claim 1 wherein said carrier contains silica.
Claim 4
Dependent Claim 11 words
A method according to claim 1 wherein said acceptor is MnO.
Claim 5
Dependent Claim 11 words
A method according to claim 2 wherein said acceptor is MnO.
Claim 6
Dependent Claim 20 words
A method according to claim 1 wherein 2-20 percent of said acceptor is Mn or Fe or a combination thereof.
Claim 7
Dependent Claim 20 words
A method according to claim 2 wherein 2-20 percent of said acceptor is Mn or Fe or a combination thereof.
Claim 8
Dependent Claim 20 words
A method according to claim 1 wherein 7-10 percent of said acceptor is Mn or Fe or a combination thereof.
Claim 9
Dependent Claim 20 words
A method according to claim 2 wherein 7-10 percent of said acceptor is Mn or Fe or a combination thereof.
Claim 10
Dependent Claim 21 words
A method according to claim 1 wherein conditions for said removal include a temperature of from 300° C. to 750° C.
Claim 11
Dependent Claim 21 words
A method according to claim 2 wherein conditions for said removal include a temperature of from 300° C. to 750° C.
Claim 12
Dependent Claim 21 words
A method according to claim 1 wherein conditions for said removal include a temperature of from 400° C. to 475° C.
Claim 13
Dependent Claim 21 words
A method according to claim 2 wherein conditions for said removal include a temperature of from 400° C. to 475° C.
Claim 14
Dependent Claim 28 words
A method according to claim 1 wherein water is present and comprises up to 10 percent of the volume of a container in which said method is performed.
Claim 15
Dependent Claim 28 words
A method according to claim 2 wherein water is present and comprises up to 10 percent of the volume of a container in which said method is performed.
Claim 16
Dependent Claim 21 words
A method according to claim 1 wherein said steam is present at a temperature of from 400° C. to 575° C.

References Cited (Backward Citations)

NL120806C Cited
US2950229A Cited
NL7507102A Cited
US4008174A Cited
US4273748A Cited
DE2738383A1 Cited
US4273749A Cited
US4233276A Cited
US4283374A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1987-12-18 1988-06-18 1988-12-18 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1991-12-18 1992-06-18 1992-12-18 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1995-12-18 1996-06-18 1996-12-18 $7700.00 Window Closed / Lapsed

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