US4152400A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Method for treating sulfur dioxide with sorbent
Assignee: ExxonMobil Technology and Engineering Co
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Filing: 1977-07-26
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Granted: 1979-05-01
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Expires: 1997-07-26
Abstract
Abstract Process for preparing shaped base materials for use in solid catalysts for commercial processes. The solid contact material is prepared by pre-soaking a porous solid particulate carrier material in an organic liquid, immersing the carrier without drying in a dilute acid solution for a given time interval, washing, drying and calcining the impregnated carrier. After calcination, the carrier is impregnated with an active material.
Inventors
- 👤 Martin O. Gernand
- 👤 Dale D. Maness
- 👤 Neville L. Cull
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-29 22:25
CPC Classifications
B; B01; B01D; B01D53/00; B01D53/34; B01D53/46; B01D53/48; B01D53/50; B01D53/508; B01D53/02; B01D53/74; B01D53/86; B01D53/8621; B01D53/8625; B01D53/8628; B01J; B01J37/00; B01J37/02; B01J37/0201; B01J37/0207
Claims Analysis
Total Claims: 13
Claim 1
Independent Claim
209 words
A process for the removal of sulfur dioxide from a gas stream containing sulfur dioxide and oxygen which comprises contacting said gas stream in a reaction zone, at the sulfurization conditions, with a particulate sorbent comprising a sorbing metal or metal oxide or a mixture of metals or metal oxides impregnated upon a porous, solid inorganic refractory carrier, said sorbent prepared by a process comprising: (a) immersing particles of said porous, solid inorganic refractory carrier in a polar organic presoak liquid so as to substantially completely fill the pores of the carrier, said presoak liquid being capable of wetting the carrier and capable of displacement by the acid etching solution used in step (c) at a rate slow enough to permit control of the extent of acid attack; (b) separating said carrier plus absorbed presoak liquid from said presoak liquid; (c) immersing said carrier in an acid solution, said acid solution being substantially immiscible with said presoak liquid; (d) removing said acid solution from said carrier; (e) impregnating the acid solution treated carrier with an impregnating solution containing a decomposable metal compound; and (f) drying said carrier and converting said decomposable metal compound to said desired sorbing metal or metal oxide or a mixture of metals or metal oxides.
Claim 2
Dependent Claim
209 words
A process for the removal of sulfur dioxide from a gas stream containing sulfur dioxide and oxygen which comprises contacting said gas stream in a reaction zone, at the sulfurization conditions, with a particulate sorbent comprising a sorbing metal or metal oxide or a mixture of metals or metal oxides impregnated upon a porous, solid inorganic refractory carrier, said sorbent prepared by a process comprising: (a) immersing particles of said porous, solid inorganic refractory carrier in a polar organic presoak liquid so as to substantially completely fill the pores of the carrier, said presoak liquid being capable of wetting the carrier and capable of displacement by the acid etching solution used in step (c) at a rate slow enough to permit control of the extent of acid attack; (b) separating said carrier plus absorbed presoak liquid from said presoak liquid; (c) immersing said carrier in an acid solution, said acid solution being substantially immiscible with said presoak liquid; (d) removing said acid solution from said carrier; (e) impregnating the acid solution treated carrier with an impregnating solution containing a decomposable metal compound; and (f) drying said carrier and converting said decomposable metal compound to said desired sorbing metal or metal oxide or a mixture of metals or metal oxides.
Claim 3
Dependent Claim
14 words
The process of claim 1 wherein said porous solid inorganic refractory carrier is alumina.
Claim 4
Dependent Claim
14 words
The process of claim 1 wherein said porous, solid inorganic refractory carrier is hydrophilic.
Claim 5
Dependent Claim
13 words
The process of claim 1 wherein said sorbing metal oxide is copper oxide.
Claim 6
Dependent Claim
22 words
The process of claim 1 wherein said presoak liquid comprises one or more aliphatic monohydric alcohols containing 4 to 12 carbon atoms.
Claim 7
Dependent Claim
17 words
The process of claim 1 wherein the impregnating solution employed in step (e) is an aqueous solution.
Claim 8
Dependent Claim
28 words
The process of claim 1 wherein the acid employed in step (c) is a water soluble acid having an ionization constant of at least about 1.0×10 -3 .
Claim 9
Dependent Claim
20 words
The process of claim 1 wherein the acid component of the acid solution employed in step (c) is hydrochloric acid.
Claim 10
Dependent Claim
215 words
A process for the removal of sulfur dioxide from a gas stream containing oxygen and from 0.1 to 0.5 vol. % sulfur dioxide which comprises passing said gas stream at a temperature of from 600° to 900° F. into a reaction zone and contacting the same therein with a particulate sorbent comprising copper oxide impregnated upon alumina at a space velocity of no more than about 10,000 volumes of said gas stream per volume of particulate sorbent per hour, said sorbent prepared by a process comprising: (a) immersing alumina particles in a polar organic presoak liquid so as to substantially completely fill the pores of said alumina, said presoak liquid being capable of wetting the alumina and capable of displacement by the acid etching solution used in step (c) at a rate slow enough to permit control of the extent of acid attack; (b) separating said alumina plus absorbed presoak liquid from said presoak liquid; (c) immersing said alumina in an acid solution, said acid solution being substantially immiscible with said presoak liquid; (d) removing said acid solution from said alumina; (e) impregnating said acid solution treated alumina with an impregnating solution containing a copper compound which is decomposable to copper oxide; and (f) drying said alumina and converting said copper compound to copper oxide.
Claim 11
Dependent Claim
215 words
A process for the removal of sulfur dioxide from a gas stream containing oxygen and from 0.1 to 0.5 vol. % sulfur dioxide which comprises passing said gas stream at a temperature of from 600° to 900° F. into a reaction zone and contacting the same therein with a particulate sorbent comprising copper oxide impregnated upon alumina at a space velocity of no more than about 10,000 volumes of said gas stream per volume of particulate sorbent per hour, said sorbent prepared by a process comprising: (a) immersing alumina particles in a polar organic presoak liquid so as to substantially completely fill the pores of said alumina, said presoak liquid being capable of wetting the alumina and capable of displacement by the acid etching solution used in step (c) at a rate slow enough to permit control of the extent of acid attack; (b) separating said alumina plus absorbed presoak liquid from said presoak liquid; (c) immersing said alumina in an acid solution, said acid solution being substantially immiscible with said presoak liquid; (d) removing said acid solution from said alumina; (e) impregnating said acid solution treated alumina with an impregnating solution containing a copper compound which is decomposable to copper oxide; and (f) drying said alumina and converting said copper compound to copper oxide.
Claim 12
Dependent Claim
17 words
The process of claim 9 wherein said gas stream contains from 1 to 4 vol. % oxygen.
Claim 13
Dependent Claim
33 words
The process of claim 9 wherein said presoak liquid comprises one or more aliphatic monohydric alcohols containing 4 to 12 carbon atoms and wherein the acid employed in step (c) is hydrochloric acid.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1982-04-30 | 1982-10-30 | 1983-05-01 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1986-04-30 | 1986-10-30 | 1987-05-01 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1990-04-30 | 1990-10-30 | 1991-05-01 | $7700.00 | Window Closed / Lapsed |