US4331632A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Catalytic cartridge SO3 decomposer
Assignee: United States Department of Energy
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Filing: 1980-11-18
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Granted: 1982-05-25
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Expires: 2000-11-18
Abstract
Abstract A catalytic cartridge surrounding a heat pipe driven by a heat source is utilized as a SO 3 decomposer for thermochemical hydrogen production. The cartridge has two embodiments, a cross-flow cartridge and an axial flow cartridge. In the cross-flow cartridge, SO 3 gas is flowed through a chamber and incident normally to a catalyst coated tube extending through the chamber, the catalyst coated tube surrounding the heat pipe. In the axial-flow cartridge, SO 3 gas is flowed through the annular space between concentric inner and outer cylindrical walls, the inner cylindrical wall being coated by a catalyst and surrounding the heat pipe. The modular cartridge decomposer provides high thermal efficiency, high conversion efficiency, and increased safety.
Inventors
- 👤 Terry R. Galloway
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-31 10:47
CPC Classifications
F; F28; F28D; F28D15/00; F28D15/02; C; C01; C01B; C01B13/00; C01B13/02; C01B13/0203; C01B3/00; C01B3/02; C01B3/06; C01B3/103; C01B4/00; Y; Y02; Y02E; Y02E60/00; Y02E60/30; Y02E60/36
Claims Analysis
Total Claims: 9
Claim 1
Independent Claim
179 words
A cross-flow SO 3 decomposer for thermochemical hydrogen production, comprising: a cartridge comprising a plurality of walls defining a chamber therebetween, and a cylindrical tube mounted in the chamber and extending through the chamber from one wall of the chamber to an opposing wall thereof, the outer surface of the cylindrical tube being coated with a catalyst for promoting SO 3 decomposition reactions; a heat pipe extending into the cylindrical tube and in thermal proximity therewith, the heat pipe adapted to be driven by a heat source for transferring heat to the catalyst for heating the catalyst; and an inlet port and an outlet port in opposing walls of the cartridge, the inlet port and outlet port being provided at opposite sides of the tube substantially perpendicular to the longitudinal axis of the tube, whereby SO 3 gas may be flowed through the inlet port in a direction substantially normal to the tube across the catalyst to contact the catalyst and thereby produce SO 3 decomposition into SO 2 and O 2 which are removable through the outlet port.
Claim 2
Dependent Claim
179 words
A cross-flow SO 3 decomposer for thermochemical hydrogen production, comprising: a cartridge comprising a plurality of walls defining a chamber therebetween, and a cylindrical tube mounted in the chamber and extending through the chamber from one wall of the chamber to an opposing wall thereof, the outer surface of the cylindrical tube being coated with a catalyst for promoting SO 3 decomposition reactions; a heat pipe extending into the cylindrical tube and in thermal proximity therewith, the heat pipe adapted to be driven by a heat source for transferring heat to the catalyst for heating the catalyst; and an inlet port and an outlet port in opposing walls of the cartridge, the inlet port and outlet port being provided at opposite sides of the tube substantially perpendicular to the longitudinal axis of the tube, whereby SO 3 gas may be flowed through the inlet port in a direction substantially normal to the tube across the catalyst to contact the catalyst and thereby produce SO 3 decomposition into SO 2 and O 2 which are removable through the outlet port.
Claim 3
Dependent Claim
168 words
An axial-flow SO 3 decomposer for thermochemical hydrogen production, comprising: a cartridge comprising a pair of concentric cylindrical tubes and a pair of end walls, the tubes being mounted at each end to an end wall, the concentric tubes and end walls defining an annular space therebetween, the outer surface of the inner concentric tube being coated with a catalyst for promoting SO 3 decomposition reactions; a heat pipe extending into the inner concentric cylindrical tube and in thermal proximity therewith, the heat pipe adapted to be driven by a heat source for transferring heat to the catalyst for heating the catalyst; and an inlet port and outlet port at opposing ends of the outer concentric tube whereby SO 3 gas may be flowed through the inlet port and through the annular space between the tubes in an axial direction with respect to the tubes to contact the catalyst and thereby produce SO 3 decomposition into SO 2 and O 2 which are removed through the outlet port.
Claim 4
Dependent Claim
168 words
An axial-flow SO 3 decomposer for thermochemical hydrogen production, comprising: a cartridge comprising a pair of concentric cylindrical tubes and a pair of end walls, the tubes being mounted at each end to an end wall, the concentric tubes and end walls defining an annular space therebetween, the outer surface of the inner concentric tube being coated with a catalyst for promoting SO 3 decomposition reactions; a heat pipe extending into the inner concentric cylindrical tube and in thermal proximity therewith, the heat pipe adapted to be driven by a heat source for transferring heat to the catalyst for heating the catalyst; and an inlet port and outlet port at opposing ends of the outer concentric tube whereby SO 3 gas may be flowed through the inlet port and through the annular space between the tubes in an axial direction with respect to the tubes to contact the catalyst and thereby produce SO 3 decomposition into SO 2 and O 2 which are removed through the outlet port.
Claim 5
Dependent Claim
12 words
The decomposer of claims 1 or 2 wherein the catalyst is platinum.
Claim 6
Dependent Claim
12 words
The decomposer of claims 1 or 2 wherein the catalyst is CuO.
Claim 7
Dependent Claim
16 words
The decomposer of claims 1 or 2 wherein the catalyst is Fe 2 O 3 .
Claim 8
Dependent Claim
21 words
The decomposer of claims 1 or 2 wherein the heat pipe is a tritium-concentrating heat pipe driven by a fusion reactor.
Claim 9
Dependent Claim
45 words
The decomposer of claim 7 wherein the cylindrical tube into which the heat pipe extends is separated from the heat pipe by a narrow annular space therebetween, and further including means for flowing helium gas through the narrow annular space to sweep out permeated tritium.
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USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1985-05-24 | 1985-11-23 | 1986-05-25 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1989-05-24 | 1989-11-23 | 1990-05-25 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1993-05-24 | 1993-11-23 | 1994-05-25 | $7700.00 | Window Closed / Lapsed |