Patent Application
20210108761
The present invention relates to a method and a system of supplying liquefied gas from a liquefied gas source tank to a liquefied gas consumer tank and/or liquefied gas consumer. It is of particular reference and benefit to the supply of liquefied fuel gas from a source of liquefied natural gas (LNG), especially in ocean-going tankers and other barges or boats. The present invention is primarily described herein with the reference to this application. It is, however, to be understood that it is also applicable to other cryogenic liquids or liquid mixtures, and especially to tanks containing such cryogenic liquids or liquid mixtures, which tanks and/or their pipework need to be purged by an inert gas after having withdrawn at least a part of its liquefied gas content.
A typical exemplary arrangement which can be regarded a starting point for the present invention, comprises an elevated LNG fuel tank on a deck of a river barge, which tank is used as a source tank to fill a secondary tank on a pusher tug or similar boat. The elevation of the source tank means that the temporary flexible connection between the two vessels is placed at a lower level than the main source tank. During bunkering, liquefied gas is withdrawn from the source tank vessel by means of a liquefied gas pump and conducted through a transfer line. After bunkering has taken place, the transfer line from the top of the LNG source tank will be filled with LNG. It is necessary to remove the LNG fuel and purge with inert gas prior to a disconnection of the flexible coupling. A rapid removal is necessary to avoid unnecessary delays in vessel operations particularly also because regulations will not allow the transfer of LNG during navigation. The LNG in the transfer line will vaporize and the LNG fuel source tank, however, cannot contain the volume of boil-off gas which will result if the LNG is allowed to vaporize in the line. It would then be necessary to dispose of the additional volume of gas which cannot be contained within the LNG source tank.
It is therefore an object of the present invention to provide an efficient method and a corresponding system for providing liquefied gas from a liquefied gas source tank to a consumer and/or consumer tank avoiding the above disadvantages, especially when purging is necessary after having supplied the liquefied gas.
According to the present invention there is provided a method for supplying liquefied gas from a liquefied gas source tank to a consumer and/or consumer tank, and a corresponding system according to the independent claims. Preferred embodiments are given in the respective dependent claims and the following description.
According to the present invention there is provided a method of supplying liquefied gas from a liquefied gas source tank to a liquefied gas consumer/liquefied gas consumer tank, wherein the liquefied gas is first supplied via a transfer line to the liquefied gas consumer tank/liquefied gas consumer, and wherein after having supplied liquefied gas to the liquefied gas consumer tank/liquefied gas consumer, residual liquefied gas remaining in at least a part of the transfer line is drained into a liquefied gas holding tank and a pressurized gas is then fed into the liquefied gas holding tank in order to return at least a part of the residual liquefied gas in the holding tank via a return line back into the liquefied gas source tank.
Typically, by way of example, the liquefied gas source tank is an LNG fuel storage tank typically located on the deck of a river barge. LNG fuel is withdrawn from the source tank and conducted to a consumer tank, typically and again by way of example only, a small LNG fuel tank on a pusher tug. It can also be considered to conduct the LNG fuel directly to an LNG consumer like a fuel engine e.g. for the propulsion of the pusher tug itself. The liquefied gas holding tank can be a simple type of sump pot with sufficient volume to contain the contents of all pipework above it.
After having supplied liquefied gas to the consumer/consumer tank it is advantageous to completely drain the pipework before liquid begins to vaporize. To this end, residual liquefied gas remaining in at least a part of the transfer line is drained via at least one drain line into the liquefied gas holding tank. After draining is completed, a pressurized gas like pressurized inert gas or boil-off gas is fed into the liquefied gas holding tank at a pressure level sufficient to return at least a part, preferably the main part, more preferably essentially all of the liquefied gas in the holding tank via the return line back into the liquefied gas source tank.
The following advantages and improvements are achieved by the present invention.
The motive power to return the remaining liquefied gas to the source tank is provided by pressurized inert gas or boil-off gas such that installation of a pump is avoided. The simple removal of residual liquid reduces the need for additional boil-off gas handling. The removal of LNG/liquefied gas before its vaporization will reduce the amount of purging gas consumed. Priming and starting of a cryogenic pump in a small vessel like the holding tank would be difficult to control. Pump cool down time is avoided. A pump would lose prime as the level drops, causing it to trip, leaving a certain amount of liquid which cannot be removed. The system according to the present invention only requires simple valves and control system.
The system for supplying liquefied gas from a liquefied gas source tank to a liquefied gas consumer tank and/or liquefied gas consumer according to the present invention comprises the liquefied gas source tank having liquefied gas stored therein, a transfer line connecting a liquid space of the source tank with the liquefied gas consumer tank and/or the liquefied gas consumer. The system further comprises a liquefied gas holding tank connected to the transfer line for draining residual liquefied gas remaining in at least a part of the transfer line after having supplied liquefied gas to the consumer tank/consumer into the liquefied gas holding tank, a pressurized gas feeding line connected to the liquefied gas holding tank for feeding pressurized gas into the liquefied gas holding tank, and a return line connecting the liquefied gas holding tank with the liquefied gas source tank for feeding residual liquefied gas from the liquefied gas holding tank back to the liquefied gas source tank. The above method according to the present invention is preferably performed with the above system according to the second aspect of the present invention.
Regarding advantages and embodiments of the system according to the present invention reference is explicitly made to the statements in connection with the method according to the present invention and vice versa.
In a preferred embodiment of the present invention, the transfer line is connected to the liquefied gas holding tank via at least one drain line. Residual liquefied gas remaining in at least a part of the transfer line can be drained into the liquefied gas holding tank via the at least one drain line. One single drain line is sufficient, especially if placed low enough to drain the whole transfer line.
In a preferred embodiment of the present invention, the transfer line comprises a first transfer line and a second transfer line connected by a connection member, particularly a removable flexible connection member. In this embodiment, the first transfer line can particularly be a line from the source tank to a place where the holding tank is located, and the second transfer line can be a line from the place where the holding tank is located to the consumer tank/consumer.
In this embodiment it is advantageous to have a first drain line connecting the first transfer line to the liquefied gas holding tank, and to have a second drain line connecting the second transfer line to the liquefied gas holding tank. After having supplied liquefied gas to the gas consumer/consumer tank, liquefied gas remaining in the pipework can be drained through the first and second drain lines into the holding tank. It is expedient to connect the lowest points of each of the first and second transfer lines to the liquefied gas holding tank via the first and second drain lines, respectively.
Again, one single drain line might be sufficient if placed low enough to drain the connection line, i.e. the connection member, which is advantageously placed at the lowest point of or at least partly even lower than the first and second transfer lines. When using two drain lines, the above second drain line connecting the holding tank and the consumer tank should have to have its own removable flexible connection.
In this embodiment, the first drain line preferably comprises a first valve and the second drain line preferably comprises a second valve which valves are closed during the supply of liquefied gas and are open during draining.
The return line and the transfer line can, in part, share the same line. It is, for example, possible to use the first drain line and the first transfer line as the return line. In this case, no separate return line is necessary. The return line would then have to extend to the bottom, i.e. liquid space, of the holding tank. In another preferred embodiment, a separate return line is provided connecting the liquid space of the holding tank with the source tank. In this embodiment, the return line can be connected to the ullage space of the source tank or be connected to the first transfer line especially at the entry to the source tank.
In a preferred embodiment, the pressurized gas is fed into the liquefied gas holding tank via a pressurized gas feeding line connected to the ullage space of the holding tank. Accordingly, the pressurized gas feeding line comprises a third valve which is open when pressurized gas is fed into the holding tank.
Draining becomes more efficient if the liquefied gas holding tank is located at a lower level with respect to the source tank and/or with respect to the consumer tank and/or the consumer.
It is expedient to use an inert gas and/or boil-off gas as the pressurized gas. Inert gas can be supplied at the necessary pressure, boil-off gas from the ullage space of the source tank will have to be pressurized to the necessary pressure by means of appropriate compressors.
In a preferred embodiment, after having returned the liquefied gas, i.e. the residual liquid back into the source tank, the holding tank and optionally at least a part of the first and second transfer lines and of the return line are purged with a second inert gas which can be the same as the first inert gas used as the pressurized gas.
Further advantages and preferred embodiments of the invention are disclosed in the following description and figures.
It is understood by a person skilled in the art that the preceding and the following features are not only disclosed in the detailed combinations as discussed or shown in a figure, but that also other combinations of features can be used without exceeding the scope of the present invention.
The invention will now be further described with reference to the accompanying drawing showing a preferred embodiment.
The embodiment shown in
To solve this problem, the system 100 according to
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.
In more detail, the system 100 according to the embodiment of
As can be seen from
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.
After the bunkering process is completed, valves V1 and V2 are opened and residual liquid will thus accumulate in the small holding tank 120.
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 m3/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.
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.
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/m3.
Alternatively, compressed boil-off gas from the ullage space of source tank 110 can be used instead of pressurized inert gas.
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
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.
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.
| Number | Date | Country | Kind |
|---|---|---|---|
| 18305122.6 | Feb 2018 | EP | regional |
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/EP2019/051490 | 1/22/2019 | WO | 00 |
