US4601884A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Appliance for the production of gaseous products by decomposition of liquids
Assignee: Solvay Chimie SA
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Filing: 1984-06-26
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Granted: 1986-07-22
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Expires: 2004-06-26
Abstract
Abstract An appliance for continuous production of a gaseous product (12), and a liquid byproduct (16), at the same time by reacting a liquid reagent in a reactor (4). The positive difference between the pressure at an entrance to and the pressure at an outlet of the reactor (4) is kept constant. The appliance is used to generate oxygen by decomposition of hydrogen peroxide and this oxygen can be used in welding and cutting sets. The appliance includes a reactor comprising a horizontal reaction zone connected to a horizontal gas collection zone, located above the reaction zone, by vertical conduits.
Inventors
- 👤 Paul Coeckelberghs
- 👤 Willy Depoorter
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-04 23:19
CPC Classifications
B; B01; B01J; B01J7/00; B01J7/02; C; C01; C01B; C01B13/00; C01B13/02; C01B13/0203; C01B13/0211; C01B13/0214
Claims Analysis
Total Claims: 7
Claim 1
Independent Claim
279 words
An apparatus having an oxygen outlet for the production of oxygen by catalytic decomposition of hydrogen peroxide, comprising: a storage tank containing a hydrogen peroxide solution; a reactor having an inlet zone in communication with said storage tank and an outlet zone, said reactor containing a catalyst for the decomposition of the hydrogen peroxide; a liquid receiving vessel in communication with the outlet zone of the reactor; a hollow conduit; a heat exchanger; and a pressure regulating means; wherein the reactor comprises a horizontal reaction zone comprising the catalyst and a horizontal collection zone located above the reaction zone and connected to said reaction zone by at least one vertical conduit, the inlet zone of the reactor comprising a conduit leading into the reaction zone and the outlet zone of the reactor comprising two conduits, one leading into the reaction zone and the other leading into the collection zone; the hollow conduit is connected at one end to said liquid receiving vessel at a location in the upper portion thereof and at the other end to said heat exchanger at its entrance, and said heat exchanger at its exit is connected to the apparatus outlet; and wherein the pressure regulating means maintains the difference between the pressure in the inlet zone of said reactor and the pressure in the outlet zone of said reactor at a constant positive value; whereby the solution of hydrogen peroxide is introduced into the reactor, a mixture comprising oxygen and water vapor is formed by catalytic decomposition, the mixture passes to the heat exchanger where it is cooled and the water vapor is condensed, and the oxygen passes to the outlet of said apparatus.
Claim 2
Independent Claim
279 words
An apparatus having an oxygen outlet for the production of oxygen by catalytic decomposition of hydrogen peroxide, comprising: a storage tank containing a hydrogen peroxide solution; a reactor having an inlet zone in communication with said storage tank and an outlet zone, said reactor containing a catalyst for the decomposition of the hydrogen peroxide; a liquid receiving vessel in communication with the outlet zone of the reactor; a hollow conduit; a heat exchanger; and a pressure regulating means; wherein the reactor comprises a horizontal reaction zone comprising the catalyst and a horizontal collection zone located above the reaction zone and connected to said reaction zone by at least one vertical conduit, the inlet zone of the reactor comprising a conduit leading into the reaction zone and the outlet zone of the reactor comprising two conduits, one leading into the reaction zone and the other leading into the collection zone; the hollow conduit is connected at one end to said liquid receiving vessel at a location in the upper portion thereof and at the other end to said heat exchanger at its entrance, and said heat exchanger at its exit is connected to the apparatus outlet; and wherein the pressure regulating means maintains the difference between the pressure in the inlet zone of said reactor and the pressure in the outlet zone of said reactor at a constant positive value; whereby the solution of hydrogen peroxide is introduced into the reactor, a mixture comprising oxygen and water vapor is formed by catalytic decomposition, the mixture passes to the heat exchanger where it is cooled and the water vapor is condensed, and the oxygen passes to the outlet of said apparatus.
Claim 3
Dependent Claim
125 words
The apparatus according to claim 1, wherein the reactor is located at a lower level than the storage tank, and wherein the pressure regulating means comprises: an intermediary tank located at a level between the level of the storage tank and the level of the reactor; a hollow conduit connected at one end to the vessel at a location in the upper portion of the vessel and at the other end to the intermediary tank at a location in the upper portion of the tank so that the pressure between the vessel and the intermediary tank is equalized; and a one-way valve positioned and arranged in said hollow conduit so that direct passage of the contents of the intermediary tank to the vessel is prevented.
Claim 4
Dependent Claim
11 words
The apparatus of claim 1, wherein the vertical conduits have constrictions.
Claim 5
Dependent Claim
24 words
The apparatus of claim 1, wherein said at least one vertical conduit connecting the horizontal collection zone and the reaction zone includes cooling blades.
Claim 6
Dependent Claim
49 words
The apparatus of claim 1, wherein the pressure regulating means comprises: an adjustable pressure pump connected at its suction end, to the storage tank and, at its discharge end, to the reactor by separate hollow conduits; and a pressure measuring device connected to the outlet zone of said reactor.
Claim 7
Dependent Claim
20 words
The apparatus according to claim 5, wherein the storage tank has a safety valve which vents directly to the atmosphere.
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) | 1989-07-21 | 1990-01-20 | 1990-07-22 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1993-07-21 | 1994-01-20 | 1994-07-22 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1997-07-21 | 1998-01-20 | 1998-07-22 | $7700.00 | Window Closed / Lapsed |