US4290272A
Expired / Lapsed
US
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Means and method for independently controlling vapor compression cycle device evaporator superheat and thermal transfer capacity
Assignee: Trane International Inc
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Filing: 1979-07-18
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Granted: 1981-09-22
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Expires: 1999-07-18
Abstract
Abstract A vapor compression cycle device with variable thermal capacity is provided with a means and a method for controlling device capacity modulation and evaporator superheat. Multi-component working fluid liquid flow from each of a pair of accumulators in a closed circuit device is regulated either in response to sensed thermal demand or in response to sensed working fluid vapor superheat.
Inventors
- 👤 Himanshu B. Vakil
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-29 07:35
CPC Classifications
F; F25; F25B; F25B9/00; F25B9/002; F25B9/006; F25B49/00; F25B49/02; F25B5/00; F25B2600/00; F25B2600/21
Claims Analysis
Total Claims: 15
Claim 1
Independent Claim
146 words
A method for controlling the capacity and evaporator superheat of a vapor compression cycle device comprising the steps of: compressing vapor of a miscible multicomponent working fluid mixture comprising at least two refrigerants having different boiling points, circulating the mixture vapor through a condensing heat exchanger, circulating mixture from the condensing heat exchanger to a high pressure accumulator, circulating a controlled amount of the mixture from the high pressure accumulator to a first evaporator stage in response to a sensed household thermal demand, circulating mixture from the first evaporator stage to a low pressure accumulator, controlling the circulation of the mixture from the low pressure accumulator to a second evaporator stage in response to the degree of mixture vapor superheat sensed at a point intermediate the second evaporator stage inlet and a compressor, and circulating the mixture exiting from the second evaporator stage to the compressor.
Claim 2
Independent Claim
146 words
A method for controlling the capacity and evaporator superheat of a vapor compression cycle device comprising the steps of: compressing vapor of a miscible multicomponent working fluid mixture comprising at least two refrigerants having different boiling points, circulating the mixture vapor through a condensing heat exchanger, circulating mixture from the condensing heat exchanger to a high pressure accumulator, circulating a controlled amount of the mixture from the high pressure accumulator to a first evaporator stage in response to a sensed household thermal demand, circulating mixture from the first evaporator stage to a low pressure accumulator, controlling the circulation of the mixture from the low pressure accumulator to a second evaporator stage in response to the degree of mixture vapor superheat sensed at a point intermediate the second evaporator stage inlet and a compressor, and circulating the mixture exiting from the second evaporator stage to the compressor.
Claim 3
Dependent Claim
42 words
A method for controlling vapor compression cycle device capacity and evaporator superheat as in claim 1 wherein the amount of the mixture allowed to circulate from the high pressure accumulator to the first evaporator stage is increased with increasing household thermal demand.
Claim 4
Independent Claim
50 words
A method for controlling vapor compression cycle device capacity and evaporator superheat as in claims 1 or 2 wherein the amount of the mixture allowed to circulate from the low pressure accumulator to the second evaporator stage is increased a predetermined amount corresponding to sensed increases in mixture vapor superheat.
Claim 5
Independent Claim
147 words
A method for controlling vapor compression cycle device capacity and evaporator superheat comprising the following steps: compressing vapor of a miscible multicomponent working fluid mixture comprising at least two refrigerants having different boiling points, circulating mixture vapor to a condensing heat exchanger, circulating the mixture liquid from the condensing heat exchanger to a high pressure accumulator, controlling the circulation of the mixture from the high pressure accumulator to a first evaporator stage in response to the degree of mixture vapor superheat sensed at a point in the device intermediate the inlet of a second evaporator stage and a compressor, circulating the mixture from the first evaporator stage to a low pressure accumulator, controlling the circulation of the mixture from the low pressure accumulator to the second evaporator stage in response to sensed household thermal demand, and circulating the mixture from the second evaporator stage to the compressor.
Claim 6
Independent Claim
147 words
A method for controlling vapor compression cycle device capacity and evaporator superheat comprising the following steps: compressing vapor of a miscible multicomponent working fluid mixture comprising at least two refrigerants having different boiling points, circulating mixture vapor to a condensing heat exchanger, circulating the mixture liquid from the condensing heat exchanger to a high pressure accumulator, controlling the circulation of the mixture from the high pressure accumulator to a first evaporator stage in response to the degree of mixture vapor superheat sensed at a point in the device intermediate the inlet of a second evaporator stage and a compressor, circulating the mixture from the first evaporator stage to a low pressure accumulator, controlling the circulation of the mixture from the low pressure accumulator to the second evaporator stage in response to sensed household thermal demand, and circulating the mixture from the second evaporator stage to the compressor.
Claim 7
Dependent Claim
44 words
A method for controlling vapor compression cycle device capacity and evaporator superheat as in claim 4 wherein said circulation of mixture from the high pressure accumulator to the first evaporator stage is increased a predetermined amount corresponding to sensed increases in mixture vapor superheat.
Claim 8
Dependent Claim
41 words
A method for controlling vapor compression cycle device capacity and evaporator superheat as in claim 4 or 5 wherein said circulation of the mixture from the low pressure accumulator to the second evaporator stage is decreased with increasing household thermal demand.
Claim 9
Dependent Claim
225 words
In a vapor compression cycle device having a miscible multicomponent working fluid comprising at least two refrigerants with different boiling points which is circulated by a compressor through a condensing heat exchanger to a high pressure accumulator, an evaporator assembly connected at its inlet to said high pressure accumulator through a first flow restricting device and connected at its exhaust to said compressor, said evaporator assembly including a low pressure accumulator connected intermediate a first evaporator stage and a second evaporator stage with said connection to said second evaporator stage including a second flow restricting device, a means for controlling the capacity and the evaporator superheat of said vapor compression cycle device comprising: a first actuation assembly including means for sensing working fluid vapor superheat at a point in the device intermediate said second flow restricting device and said compressor and an actuating means in cooperative engagement with said first flow restricting device for regulating the amount of working fluid flowing through said first flow restricting device in response to a signal from said vapor superheat sensing means; and a second actuation assembly including a thermal demand sensing means and an actuating means in cooperative engagement with said second flow restricting device for regulating the amount of working fluid flowing through said flow restricting device in response to a signal from said demand sensing means.
Claim 10
Dependent Claim
225 words
In a vapor compression cycle device having a miscible multicomponent working fluid comprising at least two refrigerants with different boiling points which is circulated by a compressor through a condensing heat exchanger to a high pressure accumulator, an evaporator assembly connected at its inlet to said high pressure accumulator through a first flow restricting device and connected at its exhaust to said compressor, said evaporator assembly including a low pressure accumulator connected intermediate a first evaporator stage and a second evaporator stage with said connection to said second evaporator stage including a second flow restricting device, a means for controlling the capacity and the evaporator superheat of said vapor compression cycle device comprising: a first actuation assembly including means for sensing working fluid vapor superheat at a point in the device intermediate said second flow restricting device and said compressor and an actuating means in cooperative engagement with said first flow restricting device for regulating the amount of working fluid flowing through said first flow restricting device in response to a signal from said vapor superheat sensing means; and a second actuation assembly including a thermal demand sensing means and an actuating means in cooperative engagement with said second flow restricting device for regulating the amount of working fluid flowing through said flow restricting device in response to a signal from said demand sensing means.
Claim 11
Dependent Claim
214 words
In a vapor compression cycle device having a multicomponent working fluid circulated by a compressor through a condensing heat exchanger to a high pressure accumulator, an evaporator assembly connected at its inlet to said high pressure accumulator through a first flow restricting device and connected at its exhaust to said compressor, said evaporator assembly including a low pressure accumulator connected intermediate a first evaporator stage and a second evaporator stage with said connection to said second evaporator stage including a second flow restricting device, a means for controlling the capacity and the evaporator superheat of said vapor compression cycle device comprising: a first actuation assembly including means for sensing working fluid vapor superheat at a point in the device intermediate said second flow restricting device and said compressor and an actuating means in cooperative engagement with said second flow restricting device for regulating the amount of working fluid flowing through said second flow restricting device in response to a signal from said vapor superheat sensing means; and a second actuation assembly including a thermal demand sensing means and an actuating means in cooperative engagement with said first flow restricting device for regulating the amount of working fluid flowing through said first flow restricting device in response to a signal from said demand sensing means.
Claim 12
Dependent Claim
214 words
In a vapor compression cycle device having a multicomponent working fluid circulated by a compressor through a condensing heat exchanger to a high pressure accumulator, an evaporator assembly connected at its inlet to said high pressure accumulator through a first flow restricting device and connected at its exhaust to said compressor, said evaporator assembly including a low pressure accumulator connected intermediate a first evaporator stage and a second evaporator stage with said connection to said second evaporator stage including a second flow restricting device, a means for controlling the capacity and the evaporator superheat of said vapor compression cycle device comprising: a first actuation assembly including means for sensing working fluid vapor superheat at a point in the device intermediate said second flow restricting device and said compressor and an actuating means in cooperative engagement with said second flow restricting device for regulating the amount of working fluid flowing through said second flow restricting device in response to a signal from said vapor superheat sensing means; and a second actuation assembly including a thermal demand sensing means and an actuating means in cooperative engagement with said first flow restricting device for regulating the amount of working fluid flowing through said first flow restricting device in response to a signal from said demand sensing means.
Claim 13
Dependent Claim
27 words
A means for controlling vapor compression cycle device capacity and evaporator superheat as in claim 7 or 8 wherein said vapor superheat sensing means is a thermistor.
Claim 14
Dependent Claim
36 words
A means for controlling vapor compression cycle device capacity and evaporator superheat as in claim 7 or 8 wherein said vapor superheat sensing means is disposed intermediate said second evaporator stage inlet and said compressor inlet.
Claim 15
Dependent Claim
26 words
A means for controlling vapor compression cycle device capacity and evaporator superheat as in claim 7 or 8 wherein said demand sensing means is a thermostat.
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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) | 1984-09-21 | 1985-03-23 | 1985-09-22 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1988-09-21 | 1989-03-23 | 1989-09-22 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1992-09-21 | 1993-03-23 | 1993-09-22 | $7700.00 | Window Closed / Lapsed |