Patent US4211085A successfully refreshed from Google Patents.
US4211085A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Systems for supplying tanks with cryogen
Assignee: Liquid Carbonic Corp
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Filing: 1978-07-14
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Granted: 1980-07-08
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Expires: 1998-07-14
Abstract
Abstract A system for filling transportable tanks with a cryogen, such as low pressure liquid carbon dioxide. A holding chamber is supplied with liquid CO 2 from a storage vessel system, and the pressure of liquid CO 2 is reduced to the triple point to create CO 2 snow and form a low-temperature coolant reservoir. CO 2 vapor from the chamber is compressed and returned to the storage vessel system. Liquid CO 2 can be supplied simultaneously to the tanks of several vehicles at below about 125 psig, and vapor from these tanks is promptly condensed by melting CO 2 snow in the holding chamber. Standby cooling of vehicle cargo compartments can also be effected with recovery of the CO 2 vapor using an auxiliary compressor.
Inventors
- 👤 Lewis Tyree, Jr.
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-25 07:37
CPC Classifications
F; F17; F17C; F17C5/00; F17C5/02; F17C7/00; F17C7/02; F25; F25D; F25D3/00; F25D3/12; F17C2250/00; F17C2250/01
Claims Analysis
Total Claims: 14
Claim 1
Independent Claim
101 words
A method for supplying tanks with liquid CO 2 , which method comprises creating a low-temperature coolant reservoir of solid carbon dioxide in a chamber at the triple point pressure or below, providing a source of liquid CO 2 at a higher pressure than said triple point pressure, supplying said higher pressure liquid CO 2 to a tank, removing CO 2 vapor from the tank as said higher pressure liquid CO 2 is being supplied and transferring said removed CO 2 vapor from the tank to said chamber and condensing said vapor by melting said solid CO 2 in said reservoir.
Claim 2
Independent Claim
101 words
A method for supplying tanks with liquid CO 2 , which method comprises creating a low-temperature coolant reservoir of solid carbon dioxide in a chamber at the triple point pressure or below, providing a source of liquid CO 2 at a higher pressure than said triple point pressure, supplying said higher pressure liquid CO 2 to a tank, removing CO 2 vapor from the tank as said higher pressure liquid CO 2 is being supplied and transferring said removed CO 2 vapor from the tank to said chamber and condensing said vapor by melting said solid CO 2 in said reservoir.
Claim 3
Dependent Claim
67 words
A method in accordance with claim 1 wherein said low-temperature coolant reservoir is created from liquid CO 2 by supplying said liquid CO 2 to said chamber from a high-pressure storage vessel system and lowering the pressure in the chamber, removing CO 2 vapor which is formed in the chamber and compressing said removed vapor, and returning said compressed CO 2 vapor to the storage vessel system.
Claim 4
Dependent Claim
55 words
A method in accordance with claim 1 wherein a pool of intermediate pressre liquid CO 2 is established as said source by withdrawing liquid CO 2 from a high pressure storage vessel system and lowering the pressure thereof and wherein liquid from said intermediate pool is supplied to the tank at a still lower pressure.
Claim 5
Independent Claim
29 words
A method in accordance with claiam 3 wherein said liquid CO 2 is supplied to the tank at a pressure between about 125 psig and the triple point pressure.
Claim 6
Independent Claim
29 words
A method in accordance with claiam 3 wherein said liquid CO 2 is supplied to the tank at a pressure between about 125 psig and the triple point pressure.
Claim 7
Dependent Claim
33 words
A method in accordance with claim 4 wherein a plurality of transportable tanks are simultaneously supplied with liquid CO 2 and wherein vapor from the tanks is combined and transferred to said chamber.
Claim 8
Dependent Claim
121 words
Apparatus for supplying a liquid cryogen to a transportable tank, which apparatus comprises a chamber, means for creating a low-temperature coolant reservoir of solid cryogen in said chamber by reducing the pressure of liquid cryogen to at least about the triple point pressure, a compressor for removing cryogen vapor which is formed as a result of said formation of solid cryogen, means for condensing said compressed cryogen vapor, a source of liquid cryogen at a relatively high pressure, means for supplying the tank with liquid cryogen from said source, means for removing cryogen vapor from said tank as liquid cryogen is supplied and transferring said removed cryogen vapor from the tank to said chamber where it condenses by melting solid cryogen.
Claim 9
Dependent Claim
121 words
Apparatus for supplying a liquid cryogen to a transportable tank, which apparatus comprises a chamber, means for creating a low-temperature coolant reservoir of solid cryogen in said chamber by reducing the pressure of liquid cryogen to at least about the triple point pressure, a compressor for removing cryogen vapor which is formed as a result of said formation of solid cryogen, means for condensing said compressed cryogen vapor, a source of liquid cryogen at a relatively high pressure, means for supplying the tank with liquid cryogen from said source, means for removing cryogen vapor from said tank as liquid cryogen is supplied and transferring said removed cryogen vapor from the tank to said chamber where it condenses by melting solid cryogen.
Claim 10
Dependent Claim
61 words
Apparatus in accordance with claim 6 wherein said liquid supplying means includes a plurality of disconnectable couplings having valve means associated with each of said couplings so that a plurality of transportable tanks can be simultaneously supplied with liquid cryogen and wherein said vapor transferring means includes a plurality of disconnectable couplings and valve means associated with each of said couplings.
Claim 11
Dependent Claim
91 words
Apparatus in accordance with claim 6 wherein a high pressure liquid cryogen storage vessel is provided to which said compressed cryogen vapor is fed, wherein an intermediate vessel which serves as said souce is provided between said high-pressure storage vessel and said liquid cryogen supply means, and wherein means is associated with said intermediate tank for maintaining a preselected pressure therein which is below the pressure of said storage vessel and above the pressure at which the tank is to be filled so that liquid cryogen flow occurs by pressure differential.
Claim 12
Dependent Claim
97 words
Mobile apparatus for supplying liquid cryogen to a transportable tank, which apparatus comprises a chambler containing a low-temperature coolant reservoir of solid cryogen at the triple point pressure or below, a supply tank holding liquid cryogen at a higher pressure, means, including coupling means, for transferring liquid cryogen from said supply tank to a transportable tank mounted on a vehicle and means, including coupling means, for removing cryogen vapor from said tank as liquid cryogen is being supplied for transferring said removed cryogen vapor from the tank to the chamber where is condenses by melting solid cryogen.
Claim 13
Dependent Claim
97 words
Mobile apparatus for supplying liquid cryogen to a transportable tank, which apparatus comprises a chambler containing a low-temperature coolant reservoir of solid cryogen at the triple point pressure or below, a supply tank holding liquid cryogen at a higher pressure, means, including coupling means, for transferring liquid cryogen from said supply tank to a transportable tank mounted on a vehicle and means, including coupling means, for removing cryogen vapor from said tank as liquid cryogen is being supplied for transferring said removed cryogen vapor from the tank to the chamber where is condenses by melting solid cryogen.
Claim 14
Dependent Claim
52 words
Apparatus in accordance with claim 9 wherein said vapor transferring means includes a line leading to the ullage of said supply tank, which line includes a pressure regulator which remains open so long as the pressure of the transportable tank is below a predetermined pressure which is above the triple point pressure.
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) | 1983-07-08 | 1984-01-07 | 1984-07-08 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1987-07-08 | 1988-01-07 | 1988-07-08 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1991-07-08 | 1992-01-07 | 1992-07-08 | $7700.00 | Window Closed / Lapsed |