VAPOR PRESSURE REGULATOR FOR CRYOGENIC LIQUID STORAGE TANKS AND TANKS INCLUDING THE SAME

Abstract

Gas pressure actuated fill termination valves for cryogenic liquid storage tanks and storage tanks containing the same.

Claims

1. A cryogenic liquid storage tank, comprising: a vessel for containing a cryogenic liquid; a fill pipe in communication with the vessel wherein the vessel is filled with the cryogenic liquid via the fill pipe; a heat exchanger located within the vessel, the heat exchanger having a heat exchanger passageway in fluid communication with the fill pipe, wherein the cryogenic liquid flows through the heat exchanger passageway during filling of the vessel.

2. The cryogenic liquid storage tank of claim 1 wherein heat exchanger comprises a coil heat exchanger.

3. The cryogenic liquid storage tank of claim 1 wherein the heat exchanger comprises a serpentine heat exchanger.

4. The cryogenic liquid storage tank of claim 1 wherein the heat exchanger comprises a tube heat exchanger.

5. The cryogenic liquid storage tank of claim 1 wherein the vessel has an ullage and the heat exchanger is at least partially located in the ullage.

6. The cryogenic liquid storage tank of claim 5 wherein the heat exchanger includes an outlet end in fluid communication with the heat exchanger passageway, the outlet end being configured to dispense the cryogenic liquid into the vessel.

7. The cryogenic liquid storage tack of claim 6 wherein the outlet end is located below the ullage.

8. The cryogenic liquid storage tank of claim 6 wherein the outlet end is configured to dispense cryogenic liquid into an existing volume of the liquid in the vessel.

9. The cryogenic liquid storage tank of claim 1 wherein the heat exchanger condenses gases within the vessel.

10. The cryogenic liquid storage tank of claim 1 wherein the heat exchanger assists in maintaining a selected vapor pressure within the tank.

11. A method of filling a cryogenic liquid storage tank with a cryogenic liquid, the method comprising: flowing cryogenic liquid into a vessel of the tank; flowing the cryogenic liquid into a heat exchanger, wherein the heat exchanger is located within the tank; flowing the cryogenic liquid out of the heat exchanger and into the tank.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

[0008] FIG. 1 illustrates one embodiment of a storage tank having a vapor pressure regulator in accordance with the present disclosure.

DETAILED DESCRIPTION OF EMBODIMENTS

[0009] FIG. 1 illustrates an implementation of a storage tank 100. In the illustrate embodiment, the storage tank 100 is a vertical storage tank. In other embodiments, the storage tank 100 may be a horizontal storage tank. The storage tank 100 may be a cryogenic liquid storage tank. The storage tank 100 includes an inner vessel 102. The inner vessel 102 is enclosed by an outer vessel 104. The inner vessel 102 can enclose an interior chamber 106. The inner vessel 102 is joined to the outer vessel 104 by an inner vessel support member 105. The inner vessel support member 105 may be connected, at its top end, to an outer component (for example, outer knuckle or outer joint) 107 or to an outer vessel. The inner chamber 106 receives the liquefied gas through a fill pipe 108, stores the liquefied gas, and provides fluid to a use device (for example, a laser cutter, a welder, a food refrigeration device, or any other suitable device) through a withdrawal pipe 110. The fill and withdrawal pipes may be any suitable conduit for conveying or allowing the flow of fluid therethrough. Excess vapor can be exhausted through a vent line 112. The fill pipe 108, the withdrawal pipe 110, and the vent line 112 pass through the inner vessel support member 105, which is open from both top and bottom. In one implementation, the stay and support members can be tubes. In some other implementations, the members can be other types of similar structures, such as passages, pipes, or the like. The cross-sections of these tubes and other structures can have various shapes, such as a circle, ellipsis, square, triangle, pentagon, hexagon, polygon, and other shapes.

[0010] When the tank 100 is employed to store cryogenic liquids, the liquids may be liquefied gases. For example, the cryogenic liquids can be at least one of nitrogen, helium, neon, argon, krypton, hydrogen, methane, liquefied natural gas, and oxygen, although other types of gases are within the scope of this disclosure.

[0011] The tank 100 may include a heat exchanger 114 that has a heat exchanger passageway therethrough. The heat exchange passageway is in fluid communication with the fill pipe 108 so that cold liquid coming in through fill pipe 108 flows through the heat exchanger 114. The heat exchanger 114 includes an outlet end 116 in fluid communication with the heat exchanger passageway, wherein the liquid 120 is dispensed from the outlet end and into the vessel 102 to fill the tank 100. In one embodiment the outlet end 116 is positioned or located so as to dispense the incoming liquid into an existing liquid volume of the tank, which is similar to a traditional bottom fill system.

[0012] The heat exchanger 114 may be the illustrated coiled heat exchanger 118. In other embodiments, the heat changer may be a serpentine heat exchanger or tube heat exchanger. The heat exchanger 114 is located in the vessel 102, and is preferably located in the ullage or headspace of the tank. As the cold incoming liquid flows through the heat exchanger 114, the heat exchanger condenses the hotter gas around, thus reducing the vapor pressure within the tank 100. Additionally, as liquid 120 is dispensed out of the outlet end 116 of the heat exchanger near the bottom of the vessel 102, vapor pressure builds within the tank 100, similar to that of a traditional bottom fill. As the level of liquid 120 increases, the gas space compresses, and the pressure in the tank rises as a result. The heat exchanger, e.g. coil, serpentine or tube, can be differently sized and shaped depending on the tank and the type of liquid the tank is designed to store. The heat exchanger may be designed so that the pressure reducing effect from the heat exchanger and the pressure increasing effect from the liquid level increase cancel each other out. This may result in the tank maintaining its pre-fill vapor pressure consistently throughout the filling process.

[0013] The heat exchanger may eliminate the need to monitor the pressure and the need to adjust the throttling of the fill line valves. Because the valves do not need to be throttled, they can be removed, saving cost and reducing potential leak points on the tank. Also, since the operator filling the tank will not need to closely monitor the pressure, he/she can allocate more time to other aspects of the filling process, such as safety.

[0014] While the preferred embodiments of the disclosure have been shown and described, it will be apparent to those skilled in the art that changes and modifications may be made therein without departing from the spirit of the disclosure, the scope of which is defined by the following claims.