METHOD AND SYSTEM FOR SUPPLYING LIQUEFIED GAS

Abstract

The present invention relates to a method and a system for supplying liquefied gas source tank (110) to a liquefied gas consumer tank (200) and/or liquefied gas consumer, wherein the liquefied gas is supplied via a transfer line (130, 140, 210) to the liquefied gas consumer tank (200) and/or the liquefied gas consumer, and wherein after having supplied liquefied gas to the liquefied gas consumer tank (200) and/or liquefied gas consumer, residual liquefied gas remaining in at least a part of the transfer line (130, 140, 210) is drained into a liquefied gas holding tank (120) and a pressurized gas is then fed into the liquefied gas holding tank (120) in order to return at least a part of the residual liquefied gas in the holding tank via a return line (160) back into the liquefied gas source tank (110).

Claims

1. A method of supplying liquefied gas from a liquefied gas source tank (110) to a liquefied gas consumer tank (200) and/or liquefied gas consumer, wherein the liquefied gas is supplied via a transfer line (130, 140, 210) to the liquefied gas consumer tank (200) and/or the liquefied gas consumer, and wherein after having supplied liquefied gas to the liquefied gas consumer tank (200) and/or liquefied gas consumer, residual liquefied gas remaining in at least a part of the transfer line (130, 140, 210) is drained into a liquefied gas holding tank (120) and a pressurized gas is then fed into the liquefied gas holding tank (120) in order to return at least a part of the residual liquefied gas in the holding tank via a return line (160) back into the liquefied gas source tank (110).

2. The method of claim 1, wherein the residual liquefied gas remaining in at least a part of the transfer line is drained into the liquefied gas holding tank (120) via at least one drain line (180, 190).

3. The method of claim 1, wherein the pressurized gas is fed into the liquefied gas holding tank (120) via a pressurized gas feeding line (150) connected to the ullage space of the liquefied gas holding tank (120).

4. The method of claim 1, wherein a first inert gas and/or boil-off gas from the liquefied gas source tank (110) is used as the pressurized gas.

5. The method of claim 1, wherein residual liquefied gas is returned to the liquefied gas source tank (110) via the return line (160) connected to the liquid space of the liquefied gas holding tank (120).

6. The method of claim 1, wherein after having returned the residual liquefied gas back into the liquefied gas source tank (110), the liquefied gas holding tank (120) is purged with a second inert gas.

7. The method according to claim 1, wherein the liquefied gas is liquefied natural gas.

8. A system (100) for supplying liquefied gas from a liquefied gas source tank (110) to a liquefied gas consumer tank (200) and/or a liquefied gas consumer, said system comprising the liquefied gas source tank (110) having liquefied gas stored therein, a transfer line (130, 140, 210) connecting a liquid space of the source tank with the liquefied gas consumer tank (200) and/or the liquefied gas consumer, wherein the system (100) further comprises a liquefied gas holding tank (120) connected to the transfer line (130, 140, 210) for draining residual liquefied gas remaining in at least a part of the transfer line (130, 140, 210) after having supplied liquefied gas to the consumer tank (200) and/or consumer into the liquefied gas holding tank (120), a pressurized gas feeding line (150) connected to the liquefied gas holding tank (120) for feeding pressurized gas into the liquefied gas holding tank (120), and a return line (160) connecting the liquefied gas holding tank (120) with the liquefied gas source tank (110) for feeding residual liquefied gas from the liquefied gas holding tank (120) back to the liquefied gas source tank (110).

9. The system (100) of claim 8, wherein the transfer line (120, 130, 210) is connected to the liquefied gas holding tank (120) via at least one drain line (180, 190).

10. The system (100) of claim 8, wherein the transfer line comprises a first transfer line (130) and a second transfer line (140) connected by a connection member (210).

11. The system (100) of claim 10, wherein the connection member (210) is a flexible connection member.

12. The system of claim 9 wherein the transfer line comprises a first transfer line (130) and a second transfer line (140) connected by a connection member (210), and the at least one drain line comprises a first drain line (190) connecting the first transfer line (130) to the liquefied gas holding tank (120), and a second drain line (180) connecting the second transfer line (140) to the liquefied gas holding tank (120).

13. The system (100) of claim 12, wherein the first drain line (190) comprises a first valve (V1) and the second drain line (180) comprises a second valve (V2).

14. The system (100) of claim 8, wherein the pressurized gas feeding line (150) comprises a third valve (V3).

15. The system (100) of claim 8, wherein the return line (160) comprises a fourth valve (V4) and/or an orifice (170).

16. The system (100) of claim 8, wherein the transfer line (120, 130, 210) and the return line (160), in part, share the same line.

17. The system (100) of claim 8, wherein the liquefied gas holding tank (120) is located at a lower level with respect to the source tank (110) and/or with respect to the consumer tank (200) and/or the consumer.

18. The system of claim 9, wherein the connection member (210) is a flexible connection member, and the at least one drain line comprises a first drain line (190) connecting the first transfer line (130) to the liquefied gas holding tank (120), and a second drain line (180) connecting the second transfer line (140) to the liquefied gas holding tank (120).

Description

BRIEF DESCRIPTION OF THE DRAWING

[0025] FIG. 1 schematically shows an embodiment of a system according to the present invention for implementing the method according to the present invention.

DETAILED DESCRIPTION OF THE DRAWING

[0026] The embodiment shown in FIG. 1 relates to an application of supplying fuel gas from an LNG source tank, but it is appreciated that a person skilled in the art can easily transfer this embodiment to other applications involving other cryogenic liquids or liquid mixtures.

[0027] FIG. 1 schematically shows a system 100 for supplying LNG from a source tank 110 to a consumer tank 200. The source tank 110 may be installed on the deck of a river barge, while the consumer tank 200 may be a small tank on a pusher tug. Typically, the small tank on the pusher tug is filled quickly every two days from the LNG source tank 110. After pumping any liquid in a downward sloping or flexible pipe or hose, there is inevitably liquid remaining in the pipework after the process is stopped. Since LNG will vaporize and the LNG source tank 110 cannot contain the volume of boil-off gas which will result if the LNG is allowed to vaporize in the line, it is desirable to return liquid instead of gas back to the original tank 110.

[0028] To solve this problem, the system 100 according to FIG. 1 provides a small holding tank 120 which may be a simple type of sump pot with sufficient volume to contain the contents of all pipework connected to it and with a series of inlet and discharge control valves and a control supply of pressurized gas to provide the motive power to push all residual liquid in the holding tank 120 back to the top of the LNG fuel tank 110.

[0029] A sequence of valve openings and closings will allow accumulation of the residual liquid prior to removal of the same and later inert gas purging.

[0030] In more detail, the system 100 according to the embodiment of FIG. 1 comprises a transfer line 130, 140, 210 for supplying the consumer tank 200 with LNG. In order to easily connect and disconnect the consumer tank 200 to the source tank 110, the transfer line comprises two parts connected by a connection member 210, namely a first transfer line 130 and a second transfer line 140 connected by the connection member 210 which preferably is flexible and removable. In order to be able to easily remove residual LNG from the first and second transfer lines 130 and 140, at lower ends of the transfer lines, preferably at the lowest ends, drain lines 190 and 180 are connected. The drain lines 190 and 180 end in a liquefied gas holding tank 120 where the residual LNG is collected. Valves V1 and V2 in the drain lines 190 and 180 are open during draining.

[0031] As can be seen from FIG. 1, the first transfer line 130 extends from the source tank 110 to the holding tank 120, more precisely to the first drain line 190 at the top of the vessel, and the second transfer line 140 extends from the consumer tank 200 to the holding tank 120, more precisely to the second drain line 180 at the top of the vessel. The second drain line 180 comprises a removable flexible connection (not shown) for disconnecting the second drain line 180 from the holding tank 120.

[0032] The liquefied gas holding tank 120 comprises a valve V1 on the first drain line inlet at the top of the vessel, a valve V2 at the second drain line inlet at the top of the vessel, and a valve V3 in the pressurized gas feeding line 150 connected to the vapor space of the holding tank 120.

[0033] After the bunkering process is completed, valves V1 and V2 are opened and residual liquid will thus accumulate in the small holding tank 120.

[0034] During bunkering, in this embodiment LNG at approximately −155 degree Celsius will be pumped from the source tank 110 (original storage tank) to the receiving consumer fuel tank 200 at a flow in the range of approximately 5 to 20 m.sup.3/h at a pressure of 1 to 10 bar to overcome any pressure in the receiving tank 200. Lower pressures are preferable for reducing the risk for leaks and product loss in case of a leak. During the bunkering process, valves V1 and V2 and V3 are closed. LNG is conducted through the first transfer line 130, the connection member 210 and the second transfer line 140 to the receiving tank 200.

[0035] After pumping, ambient temperatures will tend to vaporize the liquid remaining in the pipework. Since LNG has a vapor to liquid ratio of approximately 600:1 it is preferable to return the liquid to the source tank 110 before it vaporizes. After pumping has stopped, the pressure in the source tank 110, pipework and receiving fuel tank 200 will settle-out to a value lower than the highest pressure of the tank-pipework-tank-network. The liquid remaining in the pipework, typically in the range of 200 l, will run down to the lowest point and—with valves V1 and V2 open—collect in a suitably sized drain pot in the form of the small holding tank 120.

[0036] In this embodiment, the top of the source tank 110 is approximately 5 m above the lowest point of the pipework. Thus, in order to raise the liquid column from the lower point of the holding tank 120 to the top of the source tank 110, a pressurized gas supply of approximately 5 bar through the pressurized gas feeding line 150 with valve V3 open should be sufficient, as the density of LNG is in the order of 0.5 kg/m.sup.3.

[0037] Alternatively, compressed boil-off gas from the ullage space of source tank 110 can be used instead of pressurized inert gas.

[0038] Introducing inert gas of sufficient pressure through line 150 into the holding tank 120 will thus return most of the liquid in the holding tank 120 back to the source tank 110 through the return line 160 (valve V4 open). During pressurization via line 150 valve V4 remains closed. The entry of the return line 160 to the storage tank 110 can either be separate from the first transfer line 130 such that the return line 160 is connected to the ullage space of the storage tank 110, or it can be connected to the entry of the first transfer line 130 to the storage tank 110. Both alternatives are shown in FIG. 1.

[0039] Further, the return line 160 is fitted with an orifice 170 at a high level to avoid two-phase flow of the return liquid back to the source tank 110.

[0040] The solution described provides a method to completely drain the pipework of system 100 before LNG starts to vaporize. The described solution avoids the need for a pump and relies on simple valve control and compressed inert gas supply.