IP Library Granted Patent US 10,054,262
Granted Patent B2
US 10,054,262 · App. 14/687,449 · Granted Aug 21, 2018

Pressurized sub-cooled cryogenic system

Inventors: John M. Baust (Owego, NY); Joshua T. Smith (Owego, NY); Anthony T. Robilotto (Binghamton, NY); Jennie F. McKain (Endicott, NY)
Assignee: CPSI Holdings LLC
F17C1/00F17C5/02
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Quick Facts
Patent No.
US 10,054,262
App. No.
14/687,449
Granted
Aug 21, 2018
Kind
B2
Abstract

A cryogenic system as well as a method of generating a pressurized, sub-cooled mixed-phase cryogen and a method of delivering such a cryogen to a cryoprobe are disclosed. In an embodiment, the cryogenic system includes a reservoir containing a liquid cryogen and a sub-cooling coil immersed in the liquid cryogen. The cryogen is supplied to the sub-cooling coil and is cooled under pressure to produce a pressurized mixed phase cryogen within the sub-cooling coil. This pressurized mixed phase cryogen is provided via supply line to a cryo-device for use.

Claims (66)

1. A cryogenic system comprising:

a reservoir containing a liquid cryogen;

a heat exchange coil immersed in the liquid cryogen, the heat exchange coil being configured to cool a cryogen therein under pressure to produce a pressurized mixed phase cryogen within the heat exchange coil, wherein the cryogen is supplied to the heat exchange coil at a first pressure, and exits the heat exchange coil at a second, lower pressure;

a cryo-device fluidly connected to the heat exchange coil by a supply line such that the pressurized mixed phase cryogen is delivered to the cryo-device; and

a return line for conducting used cryogen away from the cryo-device, wherein the return line further conducts the used cryogen into the reservoir for collection.

2. The cryogenic system of claim 1 , wherein the return line further conducts the used cryogen as bulk fluid into a cryogen gas pressure cylinder.

3. The cryogenic system of claim 1 , wherein the return line further conducts the used cryogen to a heat exchanger venting system to warm and evaporate the cryogen prior to release into the atmosphere.

4. The cryogenic system of claim 1 , further comprising a boiling chamber disposed at a distal tip of the cryo-device, the boiling chamber being configured to produce a drop in a pressure of the pressurized mixed phase cryogen within the boiling chamber.

5. The cryogenic system of claim 1 , wherein the cryo-device is a cryoprobe.

6. The cryogenic system of claim 5 , further comprising an enclosure in which the reservoir is disposed; and

wherein the cryoprobe further comprises:

an umbilical line coupled to the enclosure;

a probe handle coupled to the umbilical line; and

a probe shaft having an outer sheath disposed thereon, the probe shaft extending from the probe handle,

wherein the supply line is disposed within the umbilical, the probe handle, and the probe shaft, placing the cryoprobe in fluid communication with the heat exchange coil within the enclosure.

7. The cryogenic system of claim 6 , further comprising a vacuum lumen disposed within the probe shaft, the vacuum lumen being in fluid connection with a vacuum pump disposed within the enclosure.

8. The cryogenic system of claim 1 , further comprising at least one pressurized gas cryogen supply including:

a pressurized cryogen cylinder for supplying the cryogen to the heat exchange coil.

9. The cryogenic system of claim 8 , wherein the at least one pressurized gas cryogen supply further comprises: two or more pressurized cryogen cylinder linked together in series or in parallel.

10. The cryogenic system of claim 8 , further comprising at least one pressurized gas cryogen supply including: a low pressure cryogen supply and a compressor for pressurizing the cryogen.

11. The cryogenic system of claim 1 , wherein the liquid cryogen contained within the reservoir is a liquefied gas cryogen and is one of: nitrogen, argon, oxygen, helium, hydrogen, propane, ethylene glycol, propanediol, or alcohol.

12. The cryogenic system of claim 1 , further comprising:

at least one sensor for monitoring one or more of:

a pressure of a pressurized cryogen supplied to the heat exchange coil,

a pressure of the pressurized mixed phase cryogen output from the heat exchange coil,

a temperature of a pressurized cryogen supplied to the heat exchange coil,

a temperature of the pressurized mixed phase cryogen output from the heat exchange coil,

a temperature of the liquid cryogen contained within the reservoir,

a temperature of a tip of the cryo-device,

a flow rate of the pressurized cryogen supplied to the heat exchange coil,

a flow rate of the pressurized mixed phase cryogen output from the heat exchange coil,

a vessel fluid level in the reservoir, or

a vessel fluid level in a pressurized cryogen supply.

13. The cryogenic system of claim 12 , further comprising:

a control center including a computer-readable storage medium which, when executed by a computing device, causes the computing device to carry out:

receiving feedback from the at least one sensor; and

based on the feedback, controlling at least one operation parameter of the cryogenic system, the at least one operation parameter including one or more of:

the pressure of the pressurized cryogen supplied to the heat exchange coil,

the pressure of the pressurized mixed phase cryogen output from the heat exchange coil,

the temperature of the pressurized cryogen supplied to the heat exchange coil,

the temperature of the pressurized mixed phase cryogen output from the heat exchange coil,

the temperature of the liquid cryogen contained within the reservoir,

the temperature of the tip of the cryo-device,

the flow rate of the pressurized cryogen supplied to the heat exchange coil,

the flow rate of the pressurized mixed phase cryogen output from the heat exchange coil,

the vessel fluid level in the reservoir, or

the vessel fluid level in the pressurized cryogen supply.

14. The cryogenic system of claim 2 , wherein the cryogen gas pressure cylinder is used as a source for the cryogen supplied to the heat exchange coil.

15. The cryogenic system of claim 4 , wherein the return line axially extends a first distance into the boiling chamber, and the supply line axially extends a second, longer distance into the boiling chamber, such that the supply line terminates nearer to the distal tip of the cryo-device than the return line.

16. The cryogenic system of claim 1 , wherein the first pressure is between about 500 psi and about 2,500 psi.

17. The cryogenic system of claim 16 , wherein the first pressure is between about 1,000 psi and about 1,500 psi.

18. The cryogenic system of claim 1 , wherein the second, lower pressure is lower than the first pressure by a difference of about 200 psi or more.

19. A cryogenic system comprising:

a reservoir containing a liquid cryogen;

a heat exchange coil immersed in the liquid cryogen, the heat exchange coil being configured to cool a cryogen therein under pressure to produce a pressurized mixed phase cryogen within the heat exchange coil, wherein the cryogen is supplied to the heat exchange coil at a first pressure, and exits the heat exchange coil at a second, lower pressure; and

a cryo-device fluidly connected to the heat exchange coil by a supply line such that the pressurized mixed phase cryogen is delivered to the cryo-device, wherein the first pressure is between about 500 psi and about 2,500 psi.

20. A cryogenic system comprising:

a reservoir containing a liquid cryogen;

an enclosure in which the reservoir is disposed;

a heat exchange coil immersed in the liquid cryogen, the heat exchange coil being configured to cool a cryogen therein under pressure to produce a pressurized mixed phase cryogen within the heat exchange coil, wherein the cryogen is supplied to the heat exchange coil at a first pressure, and exits the heat exchange coil at a second, lower pressure;

a cryoprobe fluidly connected to the heat exchange coil by a supply line such that the pressurized mixed phase cryogen is delivered to the cryoprobe, wherein the cryoprobe further comprises:

an umbilical line coupled to the enclosure;

a probe handle coupled to the umbilical line;

a probe shaft having an outer sheath disposed thereon, the probe shaft extending from the probe handle, and

a vacuum lumen disposed within the probe shaft, the vacuum lumen being in fluid connection with a vacuum pump disposed within the enclosure,

wherein the supply line is disposed within the umbilical, the probe handle, and the probe shaft, placing the cryoprobe in fluid communication with the heat exchange coil within the enclosure.

Assignments (1)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Apr 16, 2015
From: BAUST, JOHN M.; SMITH, JOSHUA T.; ROBILOTTO, ANTHONY T.; MCKAIN, JENNIE F.
To: CPSI HOLDINGS LLC
Reel/Frame 035422/0849 →
Continuity (2)
Provisional Application 61980396 · Apr 16, 2014
Related Publication 20150300569A1 · Oct 22, 2015
Cited By (5)
US 12,215,680 US 12,215,811 US 12,426,934 US 12,527,613 US 12,624,799