Patent US973925A successfully refreshed from Google Patents.
Patent US4924676A successfully refreshed from Google Patents.
US4924676A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Adsorption cooler
Assignee: Zeo Tech Zeolith Technologie GmbH
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Filing: 1986-06-12
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Granted: 1990-05-15
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Expires: 2006-06-12
Abstract
Abstract An adsorption cooler operating in accordance with the periodical adsorption principle and consisting of at least one adsorption container filled with zeolite. At least one condenser with a collecting container for the water which desorbs from the zeolite and an insulated cooling container which may be closed by a shut-off member are serially connected with the adsorption container. In the cooling container, the adsorption cooler generates ice in stages which acts as a cold buffer. The system is usable for example in solar cooling systems, vehicle air conditioning units and air conditioning insulation as well as beverage coolers.
Inventors
- 👤 Peter Maier-Laxhuber
- 👤 Fritz J. Kaubek
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-01 17:42
CPC Classifications
B; B60; B60H; B60H1/00; B60H1/00492; B60H1/32; B60H1/3201; B60H1/32014; F; F25; F25B; F25B17/00; F25B17/08; F25B17/083; F25B27/00; F25B27/002; F25B27/007; F25B27/02; Y; Y02; Y02A; Y02A30/00; Y02A30/27; Y02A30/274; Y02A40/00; Y02A40/90; Y02A40/963; Y02A40/966
Claims Analysis
Total Claims: 29
Claim 1
Independent Claim
270 words
A periodically operating dry adsorption cooler comprising: an adsorption container containing a solid adsorption substance in the adsorption container, the solid adsorption substance being capable of desorbing an operating substance in the form of vapor at a relatively high vapor pressure and adsorbing during the subsequent adsorbing phase at a relatively low vapor pressure; a condenser for liquefying the operating substance and being connected to the adsorption container; a collection container connected to the condenser, and the adsorption container, condenser, and collection container being arranged so that the operating substance liquefied in the condenser is collected in the collection container; an insulated cooling container for receiving the liquid operating substance from the collection container, the storage capacity of the insulated cooling container being sufficiently large so that the cooling container is capable of receiving therein operating substance in a sufficient quantity so that operating substance remains in the cooling container during the adsorption phase and at least a portion of the non-adsorbed liquefied operating substance solidifies in the insulated cooling container; and a selectively operable shut-off member which can be opened and closed independently of the temperature and pressure of said adsorption cooler, and being located between the collection container and the insulated cooling container, whereby when the shut-off member is opened during the adsorption phase, the liquid operating substance in the collection container can flow into the insulated cooling container wherein a portion of the liquid operating substance evaporates into vapor, and the liquid operating substance can flow through the shut-off member in the form of vapor and be adsorbed back into the adsorption substance during the adsorption phase.
Claim 2
Dependent Claim
270 words
A periodically operating dry adsorption cooler comprising: an adsorption container containing a solid adsorption substance in the adsorption container, the solid adsorption substance being capable of desorbing an operating substance in the form of vapor at a relatively high vapor pressure and adsorbing during the subsequent adsorbing phase at a relatively low vapor pressure; a condenser for liquefying the operating substance and being connected to the adsorption container; a collection container connected to the condenser, and the adsorption container, condenser, and collection container being arranged so that the operating substance liquefied in the condenser is collected in the collection container; an insulated cooling container for receiving the liquid operating substance from the collection container, the storage capacity of the insulated cooling container being sufficiently large so that the cooling container is capable of receiving therein operating substance in a sufficient quantity so that operating substance remains in the cooling container during the adsorption phase and at least a portion of the non-adsorbed liquefied operating substance solidifies in the insulated cooling container; and a selectively operable shut-off member which can be opened and closed independently of the temperature and pressure of said adsorption cooler, and being located between the collection container and the insulated cooling container, whereby when the shut-off member is opened during the adsorption phase, the liquid operating substance in the collection container can flow into the insulated cooling container wherein a portion of the liquid operating substance evaporates into vapor, and the liquid operating substance can flow through the shut-off member in the form of vapor and be adsorbed back into the adsorption substance during the adsorption phase.
Claim 3
Dependent Claim
49 words
An adsorption cooler in accordance with claim 1 wherein the adsorption substance is a zeolite selected from the group consisting of Mg-A, Na-Y, H-Y, Y-72 and Y-52, and wherein said operating substance is water, and the non-evaporated portion of which in the insulated cooling container solidifies to form ice.
Claim 4
Dependent Claim
35 words
An adsorption cooler in accordance with claim 1 wherein a second shut-off member and subsequent thereto a further collecting container and condenser and a further zeolite filled adsorption container are connected to said cooling container.
Claim 5
Dependent Claim
23 words
An adsorption cooler in accordance with claim 1 wherein the adsorption container is made from glass and is suitable for adsorbing radiation heat.
Claim 6
Dependent Claim
13 words
An adsorption cooler in accordance with claim 4 wherein the zeolite is blackened.
Claim 7
Dependent Claim
18 words
An adsorption cooler in accordance with claim 4 wherein the zeolite contains admixtures of heavy light adsorbing substances.
Claim 8
Dependent Claim
26 words
An adsorption cooler in accordance with claim 1 wherein each adsorption container is in good heat conducting contact with an exhaust line of a motor vehicle.
Claim 9
Dependent Claim
18 words
An adsorption cooler in accordance with claim 1 wherein each condenser is designed for air and water cooling.
Claim 10
Dependent Claim
31 words
An adsorption cooler in accordance with claim 1 wherein a heat exchanger for passing fluids through the heat exchanger and adsorbing heat from the fluid, is contained in the cooling container.
Claim 11
Dependent Claim
41 words
An adsorption cooler in accordance with claim 1 wherein the heat exchanger mounted in the cooling container is connected with a conventional heat regulator of a motor vehicle heating system by means of the cooling water cycle of the motor vehicle.
Claim 12
Dependent Claim
59 words
An adsorption cooler in accordance with claim 1 wherein said insulated cooling container contains a heat exchanger for passing a fluid through said heat exchanger and adsorbing heat from said fluid, and wherein the shut-off member is a thermostat valve which during said adsorption phase, is controlled by the discharge temperature of said fluid passing through said heat exchanger.
Claim 13
Dependent Claim
108 words
An adsorption cooler in accordance with claim 1 wherein said insulated cooling container contains a heat exchanger for passing a fluid through said heat exchanger and adsorbing heat from said fluid, and wherein the shut-off member is an easy motion check valve which during the adsorption phase, can open and close in response to a predetermined temperature level of said fluid passing through said heat exchanger, the temperature of said fluid passing through said heat exchanger being sensed by a temperature sensing device, whereby said opening of said easy motion check valve permits said liquefied operating substance in said collection container to flow into said insulated cooling container.
Claim 14
Dependent Claim
50 words
An adsorption cooler in accordance with claim 3 wherein each shut-off member is adapted to be closed during the desorption phase and adapted to be opened at the start of the adsorption phase so that the liquefied operating substance can flow from each collection container into the insulated cooling container.
Claim 15
Dependent Claim
38 words
An adsorption cooler in accordance with claim 11 wherein the shut-off member is adapted to remain open during the adsorption phase only when the temperature of the liquid flowing through the heat exchanger exceeds a predetermined temperature value.
Claim 16
Dependent Claim
39 words
An adsorption cooler in accordance with claim 13 wherein the adsorption container is exposed to sun radiation during the day and is permitted to cool off during the night by emitting heat radiation and heat conductivity to the environment.
Claim 17
Dependent Claim
65 words
An adsorption cooler in accordance with claim 3 wherein the shut-off member is adapted to be closed during a predetermined length of time of interrupted operation and that, at first all shut-off members are adapted to be open during the start of the operation regardless of which phase either one of said adsorption containers had been in, at the end of the preceding operating phase.
Claim 18
Independent Claim
249 words
A method of operating a periodically operating dry adsorption cooler which includes an adsorption container filled with a solid operating substance which desorbs operating substance in the form of vapor at a relatively high pressure during a desorption phase, and adsorbs the operating substance during a subsequent adsorption phase at a relatively low pressure, a condenser for liquefying the operating substance at a subsequently disposed collection container, an insulated cooling container, and a selectively operable shut-off member located between the collection container and the insulated cooling container and which can be opened and closed independent of the temperature and pressure of said adsorption cooler, said method comprising: (a) selectively closing said shut-off member to prevent desorbed operating substance from passing to said insulated cooling container during the desorption phase; (b) heating the adsorption container during the desorption phase to cause the solid adsorption substance to desorb the operating substance; (c) passing the desorbed operating substance to the condenser for liquification thereof; and (d) selectively opening said shut-off member during the adsorption phase and directing the liquefied operating substance through the shut-off member into the insulated cooling container wherein the liquefied operating substance in the insulated cooling container evaporates during the adsorption phase and the evaporated portion of the liquefied operating substance is permitted to flow through the shut-off member in the form of vapor and be adsorbed back into the adsorption substance whereby at least a portion of the non-evaporated liquefied operating substance in the insulated cooling container solidifies.
Claim 19
Independent Claim
249 words
A method of operating a periodically operating dry adsorption cooler which includes an adsorption container filled with a solid operating substance which desorbs operating substance in the form of vapor at a relatively high pressure during a desorption phase, and adsorbs the operating substance during a subsequent adsorption phase at a relatively low pressure, a condenser for liquefying the operating substance at a subsequently disposed collection container, an insulated cooling container, and a selectively operable shut-off member located between the collection container and the insulated cooling container and which can be opened and closed independent of the temperature and pressure of said adsorption cooler, said method comprising: (a) selectively closing said shut-off member to prevent desorbed operating substance from passing to said insulated cooling container during the desorption phase; (b) heating the adsorption container during the desorption phase to cause the solid adsorption substance to desorb the operating substance; (c) passing the desorbed operating substance to the condenser for liquification thereof; and (d) selectively opening said shut-off member during the adsorption phase and directing the liquefied operating substance through the shut-off member into the insulated cooling container wherein the liquefied operating substance in the insulated cooling container evaporates during the adsorption phase and the evaporated portion of the liquefied operating substance is permitted to flow through the shut-off member in the form of vapor and be adsorbed back into the adsorption substance whereby at least a portion of the non-evaporated liquefied operating substance in the insulated cooling container solidifies.
Claim 20
Dependent Claim
62 words
The invention in accordance with claim 17, wherein said method further comprises prior to step (a), said method comprises providing a second zeolite filled adsorption container, a second collection container, a second condenser connected between said second zeolite filled adsorption container and said second collection container, and a second selectively operable shut-off member connecting said collection container with said insulated cooling container.
Claim 21
Dependent Claim
27 words
The invention in accordance with claim 17 wherein step (c) said liquification of said desorbed operating substance in said condenser involves one of air and water cooling.
Claim 22
Dependent Claim
58 words
The invention in accordance with claim 17 wherein the insulated cooling container contains a heat exchanger for passing a beverage therethrough and adsorbing heat from said beverage, and wherein step (d) upon the solidification of at least a portion of the non-evaporated operating substance in the insulated cooling container, said method further comprises adsorbing heat from said beverage.
Claim 23
Dependent Claim
53 words
The invention in accordance with claim 17 wherein step (d) further comprises connecting said heat exchanger with a conventional heat regulator of a motor vehicle heating system, by means of a cooling water cycle, so as to adsorb heat from cooling fluid passing through said heat exchanger connected in said cooling water cycle.
Claim 24
Dependent Claim
41 words
The invention in accordance with claim 20 wherein the shut-off member is a thermostat valve, and where during said adsorption phase, step (d) further comprises controlling said shut-off member by the discharge temperature of said beverage flowing through said heat exchanger.
Claim 25
Dependent Claim
115 words
The invention in accordance with claim 17 wherein said insulated cooling container contains a heat exchanger for passing a fluid through said heat exchanger and absorbing heat from said fluid, wherein the shut-off member is an easy motion check valve and where during the adsorption phase, step (d) further comprises opening and closing said easy motion check valve, in response to a predetermined temperature level of said fluid passing through said heat exchanger, the temperature of said fluid passing through said heat exchanger being sensed by a temperature sensing device, whereby said opening of said easy motion check valve permits said liquefied operating substance in said collection container to flow into said insulated cooling container.
Claim 26
Dependent Claim
55 words
The invention in accordance with claim 18 wherein step (d) comprises selectively closing each said shut-off member during the desorption phase and step (d) comprises selectively opening each said shut-off member at the start of the adsorption phase so that the liquefied operating substance can flow from the collection containers into said insulated cooling container.
Claim 27
Dependent Claim
37 words
The invention in accordance with claim 22 wherein step (d) comprises maintaining said shut-off member open during the adsorption phase only when the temperature of said beverage flowing through said heat exchanger exceeds a predetermined temperature value.
Claim 28
Dependent Claim
40 words
The invention in accordance with claim 17 wherein step (b) comprises exposing said adsorption container to sun radiation during the desorption phase, and during step (d), permitting said adsorption container to cool off by emitting heat radiation to the environment.
Claim 29
Dependent Claim
87 words
The invention in accordance with claim 18 wherein said method involves interrupting the operation of said adsorption cooler by closing each said shut-off member for a predetermined long period of time with each said adsorption container being in either said adsorption or desorption phase of operation, and then resuming operation of said adsorption cooler by first opening both shut-off members during the start of said operation regardless of which phase either one of said adsorption containers had been in at the end of the preceding operating phase.
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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) | 1993-05-14 | 1993-11-13 | 1994-05-15 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1997-05-14 | 1997-11-13 | 1998-05-15 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 2001-05-14 | 2001-11-13 | 2002-05-15 | $7700.00 | Window Closed / Lapsed |