FR3073601B1 - DEVICE FOR INERTING A LIQUEFIED GAS STORAGE TANK FOR A TRANSPORT VESSEL OF THIS GAS - Google Patents

Abstract

Device for inerting a liquefied gas storage tank for a vessel carrying this gas, comprising: - a tank (1) for liquefied gas storage isolated by a primary isolation space forming an inner envelope around the tank, and a secondary isolation space forming an outer envelope around the tank, each of the spaces comprising an insulator and being intended to be filled with an inert gas, said tank being arranged between two watertight partitions (2c) and above a bottom (2a), - a drainage box (20) located under the tank, this box being connected to a passage (22) extending between the bottom of the tank and the outer shell so that fluids can flow by gravity from the bottom of the tank to the drainage box, means for supplying nitrogen to the primary and secondary spaces, and / or evacuation of nitrogen from these spaces, characterized in that that said drainage box is in fluid communication with the passage and said secondary space, and in that said means for supplying and / or discharging said secondary space comprise a nitrogen line (30) which is connected to said drainage box so that the nitrogen supplying this space and / or evacuated from this space flows through the drainage box.

Description

Device for inerting a liquefied gas storage tank for a vessel carrying this gas

TECHNICAL FIELD The invention relates to a device for inerting a liquefied gas storage tank for a vessel carrying this gas, and a vessel comprising at least one such device. The invention may particularly apply to the inerting of a membrane tank which is used for the storage of liquefied natural gas (LNG).

STATE OF THE ART

A liquefied gas transport vessel comprises one or more sealed and thermally insulating vessels for the storage of liquefied natural gas. Each tank comprises a tank wall having successively, in the direction of the thickness, from the inside to the outside of the tank, a primary sealing membrane intended to be in contact with the liquefied natural gas, a heat barrier primary insulation, a secondary waterproofing membrane, a secondary heat-insulating barrier and a supporting structure defining the general shape of the vessel.

The primary and secondary waterproofing membranes delimit between them a primary space which contains the primary insulating barrier and which is intended to be filled with an inert gas, in general nitrogen. Inert gas also supplies the secondary space defined by the secondary sealing membrane.

The carrying structure of the tank is formed on the one hand by watertight transverse bulkheads called "cofferdam" located on at least two opposite sides of the tank, and a bottom of tank which extends under the tank and defines with it This is a passage in which fluids such as condensation water or LNG may leak if leakage occurs. These fluids usually flow by gravity into a drainage box before being evacuated.

The sealing membranes of such a tank may indeed have leaks causing the passage of liquefied natural gas from inside the tank to the thermally insulating barriers, primary and secondary. However, when a combustible gas is in the presence of an oxidizing gas and the concentration of combustible gas is in a concentration range between its lower explosive limit (LEL) and its upper explosive limit (LSE) and that the oxidizing gas is in a suitable concentration range, the combustible gas is likely to ignite and explode. The inerting of the primary and secondary spaces, that is to say their putting in an inert atmosphere, avoids accidents. Thus, the combustible and oxidizing gases, which could be present in the thermally insulating barriers, are diluted in such a way that the explosive conditions are not reached.

In the current technique, each of the primary and secondary spaces is connected to a nitrogen line which supplies nitrogen to the space but also to evacuate nitrogen from this space. It is therefore a bi-directional line that is connected to a space at one or two fluid communication ports.

There are several tank technologies. The tank can be completely "buried" and be covered by the double deck of the ship. In another configuration, the inner and outer casing of the vessel protrudes from the double deck of the vessel to form vapor and liquid domes that are in the form of two turrets or chimneys for passing cargo handling equipment for handling a liquid phase and a vapor phase of the liquefied gas contained in the tank.

With this technology, it is easier to access the primary and secondary spaces at the domes and connect them to the nitrogen lines. This is not the case with the first technology in which the nitrogen lines must cross the double bridge to connect the spaces to be interfered with. This problem is the same for the safety pilot valves that equip the tanks.

A tank is equipped with such valves to avoid overpressure in the primary and secondary spaces. In the aforementioned first technology, the valves must pass through the upper double deck to be connected to the spaces.

Generally, crossings of the double bridge and the supporting structure of the tank must be avoided because they can facilitate leakage and cause significant additional cost of design and production of the tank.

The present invention proposes an improvement allowing in particular in a simple, effective and economical way, to allow the inerting of a secondary space of any type of tank without dedicated crossing of its supporting structure.

DESCRIPTION OF THE INVENTION The invention proposes a device for inerting a liquefied gas storage tank for a vessel carrying this gas, comprising: a liquefied gas storage tank successively comprising, from the inside towards the outside of the tank, a primary sealing membrane intended to be in contact with the liquefied gas, a primary heat-insulating barrier, a secondary sealing membrane, a secondary heat-insulating barrier and a bearing structure defining the general shape of the the vessel, said primary and secondary sealing membranes defining with said primary heat-insulating barrier a primary isolation space forming an inner envelope around the vessel, and said secondary sealing membrane defining with said secondary thermally insulating barrier and said structure carrier a secondary isolation space forming an envelop external pe around the tank, each space having an insulator and being intended to be filled with an inert gas, and said tank being disposed between two bulkheads and above a tank bottom, said watertight bulkheads and said bottom of tank forming part of said supporting structure, - a drainage box located under the tank, this box being connected to a passage extending between the bottom of the tank and the outer casing so that fluids can flow by gravity from the bottom of the tank to the drainage box, means for supplying nitrogen to the primary and secondary spaces, and / or evacuation of nitrogen from these spaces, characterized in that the said drainage box is in fluidic communication with said passage and said secondary space, and in that said means for supplying and / or evacuating said secondary space comprise a line of nitrogen which is connected to said drainage box afi n that the nitrogen supplying this space and / or evacuated from this space circulates through the drainage box. The invention thus proposes to connect the nitrogen line to the secondary space via the drainage box. The drainage box is connected to the passage extending between the vessel bottom and the outer shell to be able to collect fluids that are likely to flow into this passage. The drainage box is further connected to the secondary space to provide fluid communication between the nitrogen line and the secondary space. The secondary space therefore no longer needs to be equipped with ports dedicated to the connection with the nitrogen line, which simplifies the design of the tank. The nitrogen line can have a dual function namely to supply the secondary space with nitrogen for its inerting but also to supply nitrogen to the drainage box itself. This avoids accidental explosions in both the secondary space and the drainage box that is likely to receive LNG in case of leakage. Nitrogen supply of the secondary space through the drainage box also facilitates the evacuation of gas, such as methane, secondary space. This gas is then removed from the secondary space by nitrogen which, because of its lightness relative to methane, will tend to drive the methane up the tank where is usually a fluid communication port.

The device according to the invention may comprise one or more of the following characteristics, taken separately from one another or in combination with each other: said drainage box is connected to a drainage and nitrogen circulation pipe which opens in said passage and said secondary space, the device further comprises at least one safety valve, preferably controlled, which is connected directly to said nitrogen line; it is thus understood that the safety valve or valves that secure the secondary space can be mounted directly on the nitrogen line and no longer on the tank; there are therefore fewer crossings of the tank, which is advantageous for the reasons explained in the foregoing; Moreover, the displacement of the valve or valves on the nitrogen line has a clear advantage of reactivity compared to the prior art, which will be explained in more detail in the following, - said at least one safety valve comprises a main line comprising a main valve and a pilot line comprising a pilot valve, at least one of said main and pilot lines being connected directly to said nitrogen line, the device comprises two safety-piloted valves, at least one of said main lines and pilot of each of these valves being connected directly to said nitrogen line, - the main and pilot lines of the or each valve are connected directly to said nitrogen line, - the device further comprises at least one safety valve preferably driven, which is directly connected to said secondary space; this safety valve confers additional safety by avoiding an excessive pressure increase in the secondary space; at the upper end of the tank, the outer casing extends completely over the inner casing; alternatively, at the upper end of the tank, the inner and outer shells are projecting on a double bridge covering the tank, to form domes.

The present invention also relates to a liquefied gas transport vessel, comprising at least one device as described above.

BRIEF DESCRIPTION OF THE FIGURES The invention will be better understood and other details, characteristics and advantages of the present invention will appear more clearly on reading the description which follows, given by way of nonlimiting example and with reference to the appended drawings. in which: - Figure 1 is a very schematic view of an inerting device of a liquefied gas transport tank, - Figure 2 is a schematic view of a drainage box and a bowl portion. and illustrates one embodiment of the invention, - Figures 3 to 5 are very schematic views of alternative embodiments of the invention, for a type of tank, - Figures 6 and 7 are very schematic views of embodiments of the invention, for another type of tank, - Figure 8 is a schematic sectional view of a pilot type safety valve, and - Figures 9 and 10 are very schematic views of a c equipped with a safety pilot valve.

DETAILED DESCRIPTION

Referring to Figure 1, there is shown schematically a tank 1 for storing a liquefied gas. Each wall of the vessel 1 comprises a multilayer structure comprising, from the outside towards the inside of the vessel 1, a carrier structure 2 defining the general shape of the vessel 1, a secondary thermally insulating barrier 3 comprising insulating elements against the carrier structure 2, a secondary sealing membrane 4, a primary thermally insulating barrier 5 comprising insulating elements resting against the secondary sealing membrane 4 and a primary sealing membrane 6 intended to be in contact with the liquefied fuel gas contained in the tank 1.

In the description which follows, the term "primary space", the space containing the primary insulating thermal barrier 5, and "secondary space", the space containing the secondary insulating thermal barrier 3 as seen in the drawing. , the primary space forms an inner envelope which is surrounded by the outer envelope formed by the secondary space, and which is itself surrounded by the supporting structure 2.

The supporting structure 2 may in particular be a self-supporting metal sheet and / or be formed by the hull or the double hull of a ship.

Thermally insulating barriers 3, 5 comprise insulating solids and a gas phase. According to one embodiment, the thermally insulating barriers 3, 5 are formed of heat insulating boxes, not shown. The boxes include a bottom panel and a cover panel, for example plywood, and a plurality of spacers interposed between the bottom and top panels. Compartments for housing a heat-insulating lining are provided between the spacers. The heat insulating lining may be made of any material having appropriate thermal insulation properties. By way of example, the heat-insulating lining is chosen from materials such as perlite, glass wool, polyurethane foam, polyethylene foam, polyvinyl chloride foam, aerogels or others.

Primary and secondary waterproofing membranes 4, 6 are gas and liquid tight. The supporting structure 2 is also waterproof. Therefore, within the meaning of the present description and the claims, the term "sealed barrier" covers both the waterproofing membranes 4, 6 and the supporting structure 2. Thus, the secondary heat-insulating barrier 3 is arranged in a sealed space which is isolated from the ambient pressure, on the one hand, by a first sealed barrier constituted by the secondary sealing membrane 4, on the other hand, by a second sealed barrier constituted by the supporting structure 2.

The liquefied gas comprises a chemical body or a mixture of chemical bodies which has been placed in a liquid phase at low temperature and which occurs in a vapor phase under normal temperature and pressure conditions. The liquefied gas 3 can in particular be a liquefied natural gas (LNG), that is to say a gaseous mixture comprising mainly methane and one or more other hydrocarbons, such as ethane, propane, n- butane, Ί-butane, n-pentane, i-pentane, and nitrogen in a small proportion. Liquefied natural gas is stored at atmospheric pressure at a temperature of about -162 ° C.

The liquefied gas may also be ethane or a liquefied petroleum gas (LPG), that is to say a mixture of hydrocarbons from petroleum refining comprising mainly propane and n-butane. The fuel gas may also be ethylene.

In order to avoid that, due to leakage of liquefied natural gas through the waterproofing membranes 4, 6 and / or air through the supporting structure 2, a gaseous mixture is present in explosive proportions in the walls of the tank 1, they are subjected to a process known to those skilled in the art, and for example described in the application WO-A1-2015 / 124536.

In the example shown, the inerting device is more particularly intended to ensure the inerting of the secondary space. The inerting device further comprises an inert gas injection equipment 11 for scanning the thermally insulating barrier 3 with an inert gas. The injection equipment 11 comprises a pressurized inert gas generator 12 connected to an inert gas supply pipe 14 opening inside the secondary space. The pressurized inert gas generator 12 is connected to the pipe 14 by a valve 16 making it possible to regulate the flow and / or the pressure of the injection of inert gas inside the thermally insulating barrier 3. The inert gas is preferentially nitrogen and more precisely dinitrogen or a mixture containing this gas.

The pipe 14 may also be equipped with an additional pump 13, optional, to ensure the injection of inert gas from inert gas generator 12. The invention proposes an improvement to this technology of feeding the secondary space of the tank in dinitrogen via the drainage box 20 of this tank (see Figure 2).

The drainage box 20 is located under the tank 1 and is connected to a passage 22 extending between the bottom of the tank 2a of the supporting structure 2 and the outer casing so that fluids can flow by gravity from the bottom. from tank to the drainage box. The box 20 is thus connected to one end of a first pipe 24, the opposite end of which opens onto an upper surface of the bottom of the tank. The box 20 is also connected to one end of a second pipe 26 for discharging collected fluids out of the box, this second pipe being able to be equipped with a valve 28.

The reference 23 designates a peripheral bead which is arranged in space and which guides the fluids to the drainage box 20. The bead is for example made of polymerizable resin and can extend continuously all around tank bottom 2a so that the fluids flowing on the peripheral walls of the supporting structure 2 are then conveyed to the drainage box. Alternatively, the cord could be made by metal profiles.

The reference 30 designates the nitrogen line of the secondary space, that is to say the line which allows both the nitrogen supply of the secondary space and the evacuation of nitrogen from this space that is to say in other words the circulation of nitrogen in the secondary space. This nitrogen line 30 is thus bidirectional and can therefore be considered as fulfilling the functions of the pipes 8 and 14 of FIG.

The nitrogen line 30 opens here directly into the drainage box 20 and its connecting pipe 24 to the passage 22 is further configured to be in fluid communication with the secondary space. In practice, the end of the pipe 24 located at the passage 22 may be extended and have a first orifice opening into the passage 22 and a second orifice opening into the secondary space. Alternatively, the secondary space could be in fluid communication with the passage 22 by at least one orifice provided in the outer casing and opening into the secondary space.

Figures 3 to 7 illustrate alternative embodiments of the invention.

Figures 3 to 5 relate to a first type of tank known as the "N096" and Figures 6 and 7 relate to a second type of tank known as "Mark".

The upper double deck 2b of the vessel of the carrying structure 2 of a tank N096 covers the entire tank, which is further isolated from other tanks or the rest of the ship by transverse bulkheads 2c called "cofferdam >> .

In the embodiment of FIG. 3, the secondary space of the tank 1 is equipped with two safety-controlled valves 32 which are intended to prevent an overpressure in this space. Although not shown, the primary space of the tank 1 is also equipped with one or two safety pilot valves. From a sizing point of view, it is clearly admitted by classes, shipyards and shipowners that the main cause of overpressure in the secondary space of a tank is the malfunction of the control valve 34 which equips the nitrogen line. 30. Another possible cause of overpressure is related to the reheating phase of the spaces.

A problem of the prior art is related to the distance between the source of pressure (the nitrogen line 30) and the valves 32. The sudden appearance of a high nitrogen flow (malfunction of the valve 34) could to induce a certain latency, because of the losses of loads, making that the valve has not yet detected the overpressure. In such a case, the valve would not open quickly enough and a rapid overpressure would occur in the secondary space near the nitrogen line.

To remedy this problem, one solution is to place at least one of the two valves 32 directly on the nitrogen line 30 which is identified as being the only source of pressure. Preferably, the valve or valves are arranged between the valve 34 and the drainage box 20. In the variant of Figure 4, a valve 32 is mounted on the line 30 and the other is mounted on the tank through the double bridge 2b. In the variant of Figure 4, the two valves 32 are mounted on the line 30.

The double upper deck 2b of the vessel of the bearing structure 2 of a tank Mark is traversed by portions of the inner and outer shell of the vessel which form domes 33a, 33b. The double bridge 2b is interrupted in two locations where the tank forms a protruding structure in the form of turret or chimney. The first turret is a liquid dome 33a which serves as a point of entry for various LNG handling equipment, for example a filling line, an emergency pumping line, unloading lines connected to unloading pumps, a spray line, a feed line connected to a spray pump, etc. The second turret is a steam dome 33b which serves as a point of penetration for example for a steam collecting pipe. The operation of this equipment is known elsewhere.

In FIGS. 6 and 7, the tank may be equipped with a dedicated line for evacuating the inert gas contained in the secondary space (represented by a dotted arrow 35). This evacuation line could be connected to a degassing mast to evacuate the inert gas to the atmosphere. Line 30 of this tank would then be an admission line and not bi-directional. A similar technology can equip the tank of Figures 3 to 5.

In the context of the present invention, the safety valves 34 are of the piloted type, that is to say that they comprise a main line 36 comprising a main valve and a pilot line 38 comprising a pilot valve (FIG. 8). . Conventionally, the main line 36 comprises an inlet and an outlet between which is disposed the main valve 36a. The inlet and the outlet of the main line are connected to a circulation duct of a fluid such as the nitrogen line 30.

The pilot line 38 includes an inlet and an outlet between which is disposed the pilot valve 38a. The input of the pilot line is connected to the aforementioned pipe and its output is connected to the main valve 36a.

The pilot valve 38a is actuated by the high pressure P1 and the back pressure P2. The reference pressure PO in the pilot valve 38a is equal to the atmospheric pressure.

The main valve 26a is an opening valve. The high pressure P1 is exerted on the lower face of a cone 42. The pressure P1 also passes through a piston rod 43 to an upper chamber 44 of the valve, which exerts a pressure on the piston 45. piston surface is larger than that of the valve seat which, with the action of a spring, keeps the valve closed.

When the pressure P1 reaches the set pressure of the pilot valve, the opening begins. The pressure P2 increases in the pilot line and in the lower chamber 46 of the main valve. The pressure of the lower chamber is limited by the flow rate through the orifice 47. When the flow rate through the pilot valve exceeds the capacity of the orifice, the pressure increases in the chamber 46, which causes the opening of the main valve. When the pressure P1 decreases, the pilot valve closes, and the pressure P2 is equalized by the orifice 47. The spring then closes the main valve.

As can be seen in FIGS. 9 and 10, when a safety valve 32 is mounted on the line 30, its two main lines 36 and pilot 38 can be connected to the line 30 (FIG. 9) or only one of them. 'between them (Figure 10). In the case of Figure 10, the main line 36 is connected to the line 30 while the pilot line 38 is connected to the secondary space. This makes it possible not to undergo the effects of dynamic pressure, and measure only a static pressure of the volume. The invention thus makes it possible to simplify the design of a liquefied gas transport tank by optimizing its inerting device or even the safety (valve) associated with this device.

Claims (10)

1. Device for inerting a liquefied gas storage tank for a vessel carrying this gas, comprising: - a liquefied gas storage tank (1) comprising successively, from the inside to the outside of the tank, tank, a primary sealing membrane intended to be in contact with the liquefied gas, a primary thermally insulating barrier, a secondary sealing membrane, a secondary thermally insulating barrier and a bearing structure defining the general shape of the tank, said membranes primary and secondary sealing means defining with said primary heat-insulating barrier a primary insulation space forming an inner envelope around the vessel, and said secondary sealing membrane defining with said secondary heat-insulating barrier and said carrier structure a secondary space of insulation forming an outer shell around the tank, each of the spaces being intended to be filled with an inert gas, and said tank being disposed between two watertight bulkheads (2c) and above a bottom of tank (2a), said watertight bulkheads and said bottom of tank being part of said structure carrier, - a drainage box (20) located under the tank, this box being connected to a passage (22) extending between the bottom of the tank and the outer casing so that fluids can flow by gravity from the tank bottom up to the drainage box, - nitrogen supply means for the primary and secondary spaces, and / or nitrogen evacuation of these spaces, characterized in that said drainage box is in fluid communication with said passage and said secondary space, and in that said means for supplying and / or discharging said secondary space comprise a nitrogen line (30) which is connected to said drainage box so that the nitrogen feeding this space and / or eva cue from this space flows through the drainage box. 2. Device according to claim 1, wherein said drainage box (20) is connected to a pipe (24) for drainage and nitrogen circulation which opens into said passage (22) and said secondary space. 3. Device according to claim 1 or 2, wherein it further comprises at least one safety valve (32), preferably controlled, which is connected directly to said nitrogen line (30). 4. Device according to the preceding claim, wherein said at least one safety valve (32) comprises a main line (36) comprising a main valve (36a) and a pilot line (38) comprising a pilot valve (38a), to at least one of said main and pilot lines being directly connected to said nitrogen line (30). 5. Device according to the preceding claim, wherein it comprises two pilot operated safety valves (32), at least one of said main lines (36) and pilot (38) of each of these valves being connected directly to said nitrogen line ( 30). 6. Device according to claim 4 or 5, wherein the main lines (36) and pilot (38) of the or each valve (32) are connected directly to said nitrogen line (30). 7. Device according to one of the preceding claims, wherein it further comprises at least one safety valve (32), preferably controlled, which is connected directly to said secondary space. 8. Device according to one of the preceding claims, wherein, at the upper end of the vessel (1), the outer casing extends integrally above the inner casing. 9. Device according to one of claims 1 to 7, wherein, at the upper end of the tank (1), the inner and outer envelopes are projecting on a double bridge covering the tank, to form domes (33a , 33b). 10. Liquefied gas transport vessel, comprising at least one device according to one of the preceding claims.