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US3780500A Expired / Lapsed US ⏱️ 0.0 years remaining

Removal of sulfur trioxide and acid mist from gaseous streams

Assignee: Rohm and Haas Co
•
Filing: 1973-02-15
•
Granted: 1973-12-25
•
Expires: 1993-02-15
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Abstract

Abstract Sulfur trioxide (SO)3 and/or sulfuric acid mist are removed from the gaseous effluents, particularly those from sulfuric acid plants, by contacting the gas containing such components with a crosslinked, macroreticular, polymeric ion exchange resin containing a vinylpyridine moiety. The resin is a macroreticular weak base resin which can be regenerated with an alkaline material.

Inventors

  • 👤 D Clemens
  • 👤 R Kunin

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-27 21:52
CPC Classifications
B; B01; B01D; B01D53/00; B01D53/34; B01D53/46; B01D53/48; B01D53/50

Claims Analysis

Total Claims: 15
Claim 1
Independent Claim 76 words
A process for removing SO3 and/or sulfuric acid mist from a first gaseous stream containing same which comprises contacting said stream with a crosslinked, dry macroreticular vinylpyridine weak base anion exchange resin, the vinylpyridine portion or moiety constituting at least 25 percent by weight of the resin, thereby removing said SO3 and/or sulfuric acid mist from said first gaseous stream to produce a second gaseous stream which is essentially free of SO3 and/or sulfuric acid mist.
Claim 2
Dependent Claim 19 words
A process according to claim 2 wherein the SO3 and/or sulfuric acid mist is removed by adsorption and demisting.
Claim 3
Dependent Claim 31 words
A process according to claim 3 wherein the SO3 and/or sulfuric acid mist is removed by the resin at a temperature in the range of about 50* C. to 100* C.
Claim 4
Dependent Claim 33 words
Process according to claim 3 wherein the SO3 and/or sulfuric acid mist is substantially continuously removed by the resin at a temperature in the range of about 75* C. to about 85* C.
Claim 5
Dependent Claim 16 words
Process according to claim 2 wherein the vinylpyridine is 2-vinylpyridine, 4-vinylpyridine or an alkyl substituted vinylpyridine.
Claim 6
Dependent Claim 15 words
Process according to claim 4 wherein the vinylpyridine is 2-vinylpyridine, 4-vinylpyridine or an alkylsubstituted vinylpyridine.
Claim 7
Dependent Claim 27 words
Process according to claim 5 wherein the vinylpyridine is 2-vinylpyridine, 4-vinylpyridine or an alkylsubstituted vinylpyridine, said vinylpyridine moeity constituting at least about 50 percent of the resin.
Claim 8
Dependent Claim 30 words
Process according to claim 5 wherein the resin contains about 91 percent 4-vinylpyridine, and has a porosity of about 0.59 ml./ml. and a surface area of about 6 sq. meters/gm.
Claim 9
Dependent Claim 15 words
Process according to claim 9 wherein the resin is crosslinked with about 7 percent divinylbenzene.
Claim 10
Dependent Claim 44 words
Process according to claim 10 wherein the resin has a capacity for SO3 and/or sulfuric acid of at least about 7 millimoles (H2SO4 + SO3) per gram of resin and after substantial exhaustion of said capacity, the resin is regenerated with an alkaline material.
Claim 11
Dependent Claim 25 words
Process according to claim 2 wherein the resin is in the form of a finely divided particles or beads arranged in a column or bed.
Claim 12
Dependent Claim 19 words
Process according to claim 12 wherein the mesh size of the resin is about 20 to about 70 mesh.
Claim 13
Dependent Claim 24 words
Process according to claim 2 wherein the resin preferentially removes SO3 and sulfuric acid mist in the presence of SO2 or other acid gases.
Claim 14
Dependent Claim 28 words
Process according to claim 14 wherein the SO3 and/or sulfuric acid mist are present in the first gaseous stream in an amount of up to about 100 ppm.
Claim 15
Dependent Claim 47 words
Process according to claim 14 wherein the SO3 and/or sulfuric acid mist are present in the first gaseous stream in an amount of about 15 to 50 ppm. and the second gaseous stream contains about zero (0) ppm. of SO3 and/or sulfuric acid mist (calculated as SO3).

References Cited (Backward Citations)

US2592523A Cited
US3299617A Cited
US3485014A Cited
US3346484A Cited
US3556716A Cited
US3498026A Cited
US3709977A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1976-12-24 1977-06-25 1977-12-25 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1980-12-24 1981-06-25 1981-12-25 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1984-12-24 1985-06-25 1985-12-25 $7700.00 Window Closed / Lapsed

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