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US4128619A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for desulfurization using particulate zinc oxide shapes of high surface area and improved strength

Assignee: Manufacturers Hanover Trust Co
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Filing: 1978-01-13
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Granted: 1978-12-05
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Expires: 1998-01-13
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Abstract

Abstract A desulfurization process is provided using particulate zinc oxide shapes of high surface area and improved crushing strength prepared without extraneous binder by a process including forming normal surface area zinc oxide into shapes without binder, converting at least a portion of the zinc oxide to basic zinc carbonate by exposing the shapes in the presence of moisture, to a carbon dioxide-containing atmosphere and effecting substantially complete decomposition of the basic zinc carbonate. Conditions of bulk density, moisture content and temperature are controlled.

Inventors

  • 👤 Victor S. Robinson

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-31 01:19
CPC Classifications
B; B01; B01D; B01D53/00; B01D53/34; B01D53/46; B01D53/48; B01J; B01J20/00; B01J20/02; B01J20/06

Claims Analysis

Total Claims: 9
Claim 1
Independent Claim 156 words
A process for desulfurizing sulfur-containing gases, said process including the steps of: a. providing a bed of high surface area and high crush strength particulate zinc oxide formed by the steps of: (1) forming normal zinc oxide having a specific surface area less than 10 square meters per gram into pre-determined shapes without the addition of extraneous binding material; (2) exposing said normal zinc oxide shapes to a carbon dioxide-containing atmosphere including water vapor; (3) converting at least about 45% of said zinc oxide into basic zinc carbonate; and (4) decomposing substantially all of said basic zinc carbonate into particulate zinc oxide shapes such that said particulate zinc oxide shapes have a crushing strength between about five and about thirty times greater than the crushing strength of the pre-determined zinc oxide shapes; b. passing said sulfur containing gas over said bed in order to remove the sulfur from said gas; and c. collecting said desulfurized gas.
Claim 2
Dependent Claim 156 words
A process for desulfurizing sulfur-containing gases, said process including the steps of: a. providing a bed of high surface area and high crush strength particulate zinc oxide formed by the steps of: (1) forming normal zinc oxide having a specific surface area less than 10 square meters per gram into pre-determined shapes without the addition of extraneous binding material; (2) exposing said normal zinc oxide shapes to a carbon dioxide-containing atmosphere including water vapor; (3) converting at least about 45% of said zinc oxide into basic zinc carbonate; and (4) decomposing substantially all of said basic zinc carbonate into particulate zinc oxide shapes such that said particulate zinc oxide shapes have a crushing strength between about five and about thirty times greater than the crushing strength of the pre-determined zinc oxide shapes; b. passing said sulfur containing gas over said bed in order to remove the sulfur from said gas; and c. collecting said desulfurized gas.
Claim 3
Dependent Claim 17 words
The process of claim 1 wherein said bed is maintained at a temperature of about 340° C.
Claim 4
Dependent Claim 24 words
The process of claim 1 wherein said gas is passed over said bed at a space velocity up to about 1350 hr. -1 .
Claim 5
Dependent Claim 55 words
The process of claim 1 wherein said particulate zinc oxide shapes have: a. a specific surface area between about 30 and about 50 square meters per gram; b. a crushing strength of between about 1500 and about 2710 grams; and c. a bulk density of between about 50 and about 90 pounds per cubic foot.
Claim 6
Dependent Claim 110 words
A process for desulfurizing sulfur-containing gases, said process including the step of: (a) providing a bed of particulate zinc oxide, said particulate zinc oxide having been formed into pre-determined shapes without an extraneous binder material, wherein each of said particulate oxide shapes have: (1) a specific surface area of between about 30 and 50 square meters per gram; (2) a crushing strength of between about 1500 and about 2710 grams; and (3) a bulk density of between about 50 and about 90 lbs. per cubic foot; (b) passing said sulfur containing gas over said bed in order to remove the sulfur from said gas; and (c) collecting said desulfurized gas.
Claim 7
Dependent Claim 110 words
A process for desulfurizing sulfur-containing gases, said process including the step of: (a) providing a bed of particulate zinc oxide, said particulate zinc oxide having been formed into pre-determined shapes without an extraneous binder material, wherein each of said particulate oxide shapes have: (1) a specific surface area of between about 30 and 50 square meters per gram; (2) a crushing strength of between about 1500 and about 2710 grams; and (3) a bulk density of between about 50 and about 90 lbs. per cubic foot; (b) passing said sulfur containing gas over said bed in order to remove the sulfur from said gas; and (c) collecting said desulfurized gas.
Claim 8
Dependent Claim 140 words
A process for desulfurizing sulfur containing gases, said process including the steps of: (a) providing a bed of particulate zinc oxide, said particulate zinc oxide having been formed into pre-determined shapes without an extraneous binder material, wherein each of said particulate zinc oxide shapes have: (1) a specific surface area of between about 30 and about 50 square meters per gram; (2) a crushing strength of between about 1500 and about 2710 grams; and (3) a bulk density of between about 50 and about 90 lbs. per cubic foot; (b) maintaining said bed at a temperature of between about 200° C. and about 400° C.; (c) passing said sulfur containing gas over said bed at a space velocity of up to about 1350 hr. -1 in order to remove the sulfur from said gas; and (d) collecting said desulfurized gas.
Claim 9
Dependent Claim 140 words
A process for desulfurizing sulfur containing gases, said process including the steps of: (a) providing a bed of particulate zinc oxide, said particulate zinc oxide having been formed into pre-determined shapes without an extraneous binder material, wherein each of said particulate zinc oxide shapes have: (1) a specific surface area of between about 30 and about 50 square meters per gram; (2) a crushing strength of between about 1500 and about 2710 grams; and (3) a bulk density of between about 50 and about 90 lbs. per cubic foot; (b) maintaining said bed at a temperature of between about 200° C. and about 400° C.; (c) passing said sulfur containing gas over said bed at a space velocity of up to about 1350 hr. -1 in order to remove the sulfur from said gas; and (d) collecting said desulfurized gas.

References Cited (Backward Citations)

US3441370A Cited
US4071609A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1981-12-04 1982-06-05 1982-12-05 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1985-12-04 1986-06-05 1986-12-05 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1989-12-04 1990-06-05 1990-12-05 $7700.00 Window Closed / Lapsed

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