Controlled cryogenic liquid delivery

• US 4,715,187 A
• Filed: 09/29/1986
• Issued: 12/29/1987
• Est. Priority Date: 09/29/1986
• Status: Expired due to Term

• Current Assignee: Vacuum Barrier Corp.
• Original Assignee: Vacuum Barrier Corp.
• Inventors: Stearns, Thornton
• Primary Examiner(s): Capossela, Ronald C.
• Application Number:
  US06/912,923
• Time in Patent Office: 456 Days
• Field of Search: 62/55, 62/514 R, 62/511
• US Class Current: 62/50.1
• CPC Class Codes: F17C 2201/0109 with exteriorly curved end-piece
• CPC Class Codes: F17C 2201/0119 with flat end-piece
• CPC Class Codes: F17C 2201/032 with substantially vertical main axis
• CPC Class Codes: F17C 2203/0391 by vacuum
• CPC Class Codes: F17C 2203/0629 Two walls
• CPC Class Codes: F17C 2205/0341 Filters
• CPC Class Codes: F17C 2221/014 Nitrogen
• CPC Class Codes: F17C 2223/0161 cryogenic, e.g. LNG, GNL, PLNG
• CPC Class Codes: F17C 2225/0169 subcooled
• CPC Class Codes: F17C 2250/0413 with floats
• CPC Class Codes: F17C 2260/024 Improving metering
• CPC Class Codes: F17C 2270/059 Mass bottling, e.g. merry belts
• CPC Class Codes: F17C 9/00 Methods or apparatus for discharging liquefied or solidified gases from vessels not under pressure

Abstract

A controlled stream of liquid cryogen is delivered from a system comprising: (a) a source of liquid cryogen at a substantially constant pressure, remote from the outlet; (b) a conduit connecting the liquid cryogen source to the outlet; (c) means to maintain cryogen flowing through the conduit sub-cooled at all points along the conduit (i.e., at any given point in the conduit, the cryogen'"'"'s equilibrium vapor pressure is below the pressure experienced at that point in the conduit), and to deliver the cryogen to the outlet at a temperature equal to or below its boiling point at atmospheric pressure; and (d) a flow-rate control restriction, positioned in the conduit. By maintaining the cryogen sub-cooled, the flow is kept substantially (at least about 95% by volume) liquid. Therefore, the flow in the conduit is controlled reliably as to pressure, flow rate, and size. Specifically, the rate at which liquid cryogen is delivered at the outlet is controlled by the cross-sectional area of the flow-control restriction, and severe flashing at the outlet is avoided.

Claims

1. System for delivering a controlled stream of liquid cryogen from an outlet, the system comprising:

(a) a source of liquid cryogen at substantially constant pressure, remote from the outlet;

(b) a conduit connecting the source of liquid cryogen to the outlet;

(c) a flow-rate control restriction positioned in the conduit; and

(d) means to maintain cryogen substantially entirely in liquid phase as it flows through the conduit, and out of the outlet, and to maintain said flowing cryogen at a temperature substantially equal to or below the cryogen'"'"'s boiling point at atmospheric pressure;

whereby the cross-sectional area of the restriction controls the rate of liquid cryogen delivered at the outlet, and cryogen is reliably delivered at the outlet without severe flashing.

2. The system of claim 1 wherein the system comprises a velocity-control chamber downstream from the flow-rate control restriction, the chamber having a cross-sectional area larger than said restriction which is selected to control the velocity of the liquid cryogen stream delivered at the outlet.

3. The system of claim 2 wherein the velocity-control chamber is elongated to impart a direction to the stream delivered from the delivery outlet.

4. The system of claim 3 wherein the velocity-control chamber is generally horizontal.

5. The system of claim 1 wherein the conduit comprises insulating means to prevent heat leak substantially along its length.

6. The system of claim 5 wherein the conduit is jacketed by a chamber adapted to contain liquid cryogen.

7. The system of claim 6 wherein the liquid cryogen jacket chamber is surrounded by a vacuum chamber along substantially the entire length of the conduit, and, at the end of the conduit having the delivery outlet, the vacuum chamber is surrounded by a dry gas jacket and a heater, to prevent condensation and oxygen enrichment at the delivery outlet.

8. The system of claim 1 wherein the source of constant pressure liquid cryogen comprises a bath of liquid cryogen, surrounding a tube supplying liquid cryogen to the conduit, the tube being positioned to be in heat exchanging contact with liquid cryogen contained in the bath.

9. The system of claim 8 wherein the conduit jacket insulated along its length by a jacket adapted to contain liquid cryogen, and the jacket is in communication with the bath.

10. The system of claim 8 wherein the pressure of cryogen in the bath is maintained below the atmospheric pressure at the delivery outlet.

11. The system of claim 8 wherein the tube in the bath is supplied liquid cryogen from a phase separator positioned above the bath to establish an accurately controlled pressure head.

12. The system of claim 11 wherein a preliminary restriction is provided upstream from the flow-rate control restriction, so that the entire pressure head is not communicated to the flow-control restriction.

13. The system of claim 12 wherein the preliminary restriction is an externally adjustable needle valve.

14. The system of claim 1 further characterized in that the system is adapted for delivery of liquid cryogen to pressurized containers moving along an assembly line toward a capping station, the cross-sectional area of the flow-rate control restriction being selected to deliver a desired amount of liquid cryogen to each container.

15. The system of claim 14 wherein the system comprises a velocity-control chamber downstream from the flow-control restriction, the velocity control chamber being generally horizontal and having a cross-sectional area selected to provide a liquid cryogen stream velocity and direction generally matching the velocity and direction of container movement.

16. The system of claim 1 comprising a source of flowing liquid cryogen cooled to a temperature substantially equal to or below the cryogen'"'"'s boiling point at atmospheric pressure, and means to split said source of flowing cryogen into at least two flow paths,

the first of said flow paths comprising said delivery conduit communicating with said outlet and comprising means to maintain liquid cryogen in said delivery conduit above atmospheric pressure to support cryogen flow to said outlet, and

the second of said flow paths being a jacket concentrically positioned around said first flow path, said means to split said source of flowing cryogen comprising means to maintain pressure in said jacket below the pressure in said delivery conduit, whereby said jacket maintains liquid cryogen flowing in said delivery conduit at a temperature substantially equal to or below the cryogen'"'"'s boiling point at atmospheric pressure.

17. The system of claim 16 comprising:

(a) a cryogen supply line supplying cryogen to a heat exchanging bath and to said first flow path, said heat-exchanging bath communicating with, and supply cryogen to, said jacket, said bath comprising means to maintain cryogen contained therein at a pressure below the cryogen pressure in said first flow path,

whereby cryogen flow in said supply line is split between said bath and said delivery conduit, and said jacket is supplied with cryogen from said bath at a pressure that enables the jacket to sub-cool cryogen in said delivery conduit.

18. The system of claim 1 comprising a jacket surrounding said conduit and means to maintain cryogen pressure in said jacket at a pressure below the pressure in the conduit, said cryogen pressure in said jacket being two inches above atmospheric pressure, or less.

19. Apparatus for delivery of a controlled amount of liquid cryogen to pressurized containers moving along an assembly line toward a capping station, said apparatus comprising;

(a) a source of liquid cryogen at substantially constant pressure, remote from the outlet;

(b) a conduit connecting the source of liquid cryogen to the outlet;

(c) a flow-rate control restriction positioned in the conduit; and

(d) means to maintain cryogen substantially entirely in liquid phase as it flows through the conduit, and out of the outlet, and to maintain said flowing cryogen at a temperature substantially equal to or below the cryogen'"'"'s boiling point at atmospheric pressure;

whereby the cross-sectional area of the restriction controls the rate of liquid cryogen delivered at the outlet, and cryogen is reliably delivered from the outlet substantially as a liquid without severe flashing.

20. The apparatus of claim 29 comprising a velocity-control chamber downstream from the flow-rate control restriction and having a larger cross-sectional area than said flow-rate control restriction, said velocity control chamber being generally horizontal and having a cross-sectional area selected to provide a liquid cryogen stream velocity and direction generally matching the velocity and direction of container movement.