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    • 专利摘要:
    A floating structure comprises a sealed and thermally insulating tank (1). An upper support wall (7) carries a turret (15, 21) for passing cargo handling equipment (16, 22). The turret has an inner sealed wall forming a sheath (22) engaged through the opening of the upper support wall (7) and sealingly connected with the primary sealing membrane (13) of the upper vessel wall all around. of the sheath. A primary or secondary exhaust device allows gas to escape from the primary or secondary space of the turret. A gas tank containing an incondensable tracer gas or having a condensing temperature lower than the low temperature of the liquefied gas contained in the tank is connected via a control valve to one of the primary exhaust system and the secondary exhaust device. A gas detector capable of detecting the tracer gas is in communication with the other.
    公开号:FR3019520A1
    申请号:FR1453115
    申请日:2014-04-08
    公开日:2015-10-09
    发明作者:Mael Bleomelen；Pierre Jolivet；Mathieu Petitpas；Julien Glory；Jean-Paul Goncalves；Julien Ollivier
    申请人:Gaztransport et Technigaz SARL；
    IPC主号:
    专利说明:

    [0001] TECHNICAL FIELD The invention relates to the field of sealed and thermally insulating vessels for storing a liquefied gas at low temperature, and more particularly to devices and methods for detecting leaks in a secondary sealing membrane of such a vessel. BACKGROUND In a vessel of a LNG carrier, the upper wall of the vessel has structures called a vapor dome and a liquid dome which are in the form of two turrets or chimneys protruding from an outer surface of the upper supporting wall and for passing cargo handling equipment for handling a liquid phase and a vapor phase of the liquefied gas contained in the vessel. Due to this geometry, leak detection methods based on the observation of abnormally hot or abnormally cold zones can be defeated, in particular because of the influence of external climatic conditions and because the temperature fields in and in the vicinity of these turrets are too complex. SUMMARY An idea underlying the invention is to provide devices and methods for detecting leaks in a sealed and thermally insulating vessel in and around these protruding structures. According to one embodiment, the invention provides a floating structure comprising a shell including bearing walls defining a polyhedral space inside the shell, the floating structure comprising a sealed and thermally insulating tank housed in the polyhedral space. for storing a low temperature liquefied gas, wherein an upper hull bearing wall has an opening and carries a turret projecting from an outer surface of the upper bearing wall around the opening, the opening and the turret being for passing cargo handling equipment for handling a liquid phase and / or a vapor phase of the liquefied gas contained in the vessel, wherein the vessel has a plurality of vessel walls attached to the hull carrying walls, in wherein an upper vat wall has a multilayer structure attached to an inner surface of the wall upper carrier, the multilayer structure being formed of a primary sealing membrane intended to be in contact with the liquefied gas contained in the tank, a secondary sealing membrane disposed between the primary sealing membrane and the upper supporting wall, a secondary insulating barrier disposed between the secondary sealing membrane and the upper supporting wall and a primary insulating barrier disposed between the secondary sealing membrane and the primary sealing membrane, wherein the turret comprises: an internal sealing wall forming a sheath engaged through the opening of the upper supporting wall and sealingly connected with the primary sealing membrane of the upper tank wall all around the sheath, an outer sealing wall disposed around the sheath at a distance from the sheath parallel to the sheath, the outer sealing wall being sealed to the upper support wall around the opening, a partition wall arranged between the outer impervious wall and the inner tight wall of the turret and dividing the space defined between the outer impervious wall and the internal tight wall of the turret. on the one hand, a secondary space communicating through the opening of the upper supporting wall with the secondary insulating barrier of the upper tank wall disposed around the opening and, on the other hand, a primary space communicating with through the opening of the upper carrier wall with the primary insulating barrier of the upper vessel wall disposed around the opening, a primary exhaust device having a primary pressure relief valve and a primary exhaust pipe communicating directly with with the primary space of the turret and crossing the outer wall of the turret to allow a gas escape from the space primal in response to an opening of the primary pressure relief valve, a secondary exhaust device having a secondary pressure relief valve and a secondary exhaust pipe communicating directly with the secondary space of the turret and passing through the outer watertight wall of the turret to allow exhaust gas from the secondary space in response to an opening of the secondary pressure relief valve, the floating structure further comprising: a gas tank containing an incondensable tracer gas or having a condensing temperature lower than the low temperature of the liquefied gas contained in the tank, the gas tank being connected by means of a control valve to one of the primary exhaust system, in particular the primary exhaust pipe, and the secondary exhaust, in particular the secondary exhaust pipe, and a gas detector capable of detecting the tracer gas, the gas detector being in communication with the other one of the primary exhaust device, in particular the primary exhaust pipe, and the secondary exhaust device, in particular the secondary exhaust pipe. Thanks to these characteristics, it is possible to detect a leakage gap between the primary space and the secondary space of the turret and / or between the primary insulating barrier and the secondary insulating barrier of the upper tank wall. In addition, the use of the primary and secondary exhaust devices for injection and tracer gas detection makes the implementation of leak detection particularly simple. According to embodiments, such a floating structure may include one or more of the following features. Exhaust devices can be designed in different ways. According to one embodiment, the primary or secondary exhaust device further comprises a primary or secondary control line which communicates directly with the primary or secondary space of the turret and which passes through the outer tight wall of the turret to control the primary or secondary pressure relief valve according to the pressure in the primary or secondary space, and wherein the gas reservoir is in direct communication with the primary or secondary control line. Alternatively, the gas tank can be connected directly to the primary or secondary exhaust pipe.
    [0002] According to one embodiment, the primary or secondary exhaust device further comprises a primary or secondary control line which communicates directly with the primary or secondary space of the turret and which passes through the outer tight wall of the turret to control the primary or secondary overpressure valve as a function of the pressure in the primary or secondary space, and wherein the gas detector is in direct communication with the primary or secondary control line. Alternatively, the gas detector can be connected directly to the primary or secondary exhaust pipe.
    [0003] According to one embodiment, the turret is a steam dome of the tank, the sheath engaged through the opening of the upper bearing wall being a collecting pipe connected to a main steam collector of the floating structure. Thanks to these characteristics, it is possible to detect a leakage gap between the primary space and the secondary space of the steam dome and / or between the primary insulating barrier and the secondary insulating barrier of the upper tank wall in the vicinity. steam dome. The steam dome can be designed in different ways. Preferably in this case, the turret partition wall forms a primary bleed pipe extending parallel to the header in the space defined between the outer wall and the inner wall of the turret and having one end. interior opening into the primary insulating barrier of the upper tank wall and an outer end opening directly into the primary exhaust device, the primary space of the turret having the inner space of the primary sampling line. According to another embodiment, the turret is a liquid dome of the vessel further comprising a top wall disposed on an upper end of the outer wall of the liquid dome and having an opening aligned with a central zone of the opening of the the upper supporting wall, the sheath formed by the inner sealing wall of the liquid dome being a primary sealing membrane having an upper edge sealingly attached to an edge of the apex wall all around the opening of the wall of the Mountain peak. Thanks to these characteristics, it is possible to detect a leakage fault between the primary space and the secondary space of the liquid dome and / or between the primary insulating barrier and the secondary insulating barrier of the upper tank wall in the vicinity of the liquid dome. The liquid dome can be designed in different ways. Preferably in this case, the partition wall comprises a secondary sealing membrane extending all around the sheath between the outer sealing wall and the sheath and having an inner end sealingly connected to the secondary sealing membrane of the upper vessel wall all around the sheath and an outer end sealingly connected to the apex wall all around the opening of the top wall of the liquid dome.
    [0004] According to one embodiment, the tank comprises the aforementioned provisions on both the liquid dome and the steam dome to be able to detect leaks in these two areas of the tank. According to one embodiment, the wall of the liquid dome comprises a multilayer structure fixed on an inner surface of the outer wall, the multilayer structure being formed of the primary sealing membrane of the liquid dome, the secondary sealing membrane of the dome liquid, a secondary insulating barrier of the liquid dome disposed between the secondary sealing membrane and the outer sealing wall and a primary insulating barrier disposed between the secondary sealing membrane and the primary sealing membrane of the liquid dome. Preferably in this case, the floating structure further comprises a connecting plate disposed between the outer end of the secondary sealing membrane of the liquid dome and the top wall, the connecting plate comprising a main branch extending parallel to the external sealing wall between the external sealing wall and the sheath formed by the internal sealed wall of the liquid dome, the main branch having an upper end attached to the top plate and a lower end extending by a bent flange to the interior of the liquid dome with respect to the main channel, the outer end of the secondary sealing membrane being sealingly attached to the rim, wherein the secondary insulating barrier of the liquid dome comprises a fibrous liner disposed between the main branch of the the connecting plate and the outer waterproof wall, and in which the escape pipe secondary layer opens into the fibrous lining. Thanks to these characteristics, the pressure drop induced by the fibrous lining in the zone of the secondary space where the tracer gas is injected or removed is relatively low, which facilitates the circulation of the tracer gas, especially around the liquid dome. According to a corresponding embodiment, the primary exhaust duct passes through the main branch of the connecting plate and opens into the primary insulating barrier between the main branch of the connecting plate and the primary sealing membrane of the liquid dome. Preferably, the floating structure further comprises a nitrogen distribution system including a nitrogen gas reservoir and a distribution network, the distribution network comprising a primary distribution pipe extending from an upper deck of the a structure floating through the primary space of the liquid dome and through the primary insulating barrier of a transverse wall of the vessel to a bottom zone of the vessel, and a secondary distribution pipe extending from the upper bridge of the structure floating through the secondary space of the liquid dome and through the secondary insulation barrier of the transverse wall of the tank to the bottom zone of the tank. Advantageously, the nitrogen distribution system further comprises pressure regulating means for regulating the pressure prevailing in the primary insulation barrier and the secondary insulating barrier of the walls of the vessel by means of the primary distribution pipes. and secondary. With such pressure control means it is possible to avoid damaging the sealing barriers by the effect of accidental overpressures. According to one embodiment, these pressure regulating means are used to generate a pressure difference between the zone where the tracer gas is injected and the zone where the tracer gas is sought so as to show more quickly the leaks or faults. sealing. Such a tank can be used to store all kinds of liquefied gases at atmospheric pressure, for example butane, propane, ethane, ethylene, methane and the like. According to one embodiment, the liquefied gas contained in the tank is liquefied natural gas (LNG), namely a gas with a high methane content, stored at a temperature of about -162 ° C. Different chemical bodies can be used as tracer gas, particularly depending on the nature and temperature of the liquefied gas stored. According to one embodiment, suitable in particular for a tank of LNG, the tracer gas is selected from argon, helium and mixtures thereof. According to one embodiment, the tracer gas reservoir and / or the gas detector are removably attached to the primary or secondary exhaust device. Thanks to these characteristics, it is possible to dismantle the tracer gas tank and / or the gas detector from the access of the exhaust device to which it is attached, for example a pipe or a flange, so as to release this access of the exhaust device for another use outside the phases where the leak detection is implemented. The invention also provides a method of operating a buoyant structure 15, comprising: injecting the tracer gas through one of the primary and secondary exhaust devices into the primary or secondary space of the turret without exceeding the opening pressure of the primary or secondary pressure relief valve, detecting the tracer gas through the other of the primary and secondary exhaust devices in the primary or secondary space of the turret, and diagnose a leak in the air barrier; secondary sealing of the tank top wall and / or in the separation wall of the turret in response to detection of the tracer gas. According to one embodiment, the tracer gas is injected into the secondary space through the secondary exhaust device and detected in the primary space through the primary exhaust device, the method further comprising: maintaining a pressure higher total in the secondary space than in the primary space by injecting nitrogen gas into the secondary space, without exceeding the opening pressure of the secondary pressure relief valve. Reverse operation is also possible, where the tracer gas is injected into the primary space through the primary exhaust and detected in the secondary space through the secondary exhaust. The pressure levels can be reversed in this case. In one embodiment, the step of diagnosing a leak includes one of the measures selected from the group consisting of recording the presence of a leak, measuring a quantity or a concentration of the tracer gas to determine a flow rate of the leak, and measuring a time delay between the injection and the tracer gas detection to determine a position of the leak. Such a tank can be part of a land storage facility, for example to store LNG or be installed in a floating structure, coastal or deep water, including a LNG tank, a floating storage and regasification unit (FSRU) , a floating production and remote storage unit (FPSO) and others. According to one embodiment, the invention also provides a method of loading or unloading such a floating structure, in which liquefied gas is conveyed through isolated pipes to or from a floating or land storage facility to or from the waterproof and thermally insulating tank. According to one embodiment, the invention also provides a transfer system for liquefied gas at low temperature, the system comprising a floating structure above, insulated pipes arranged to connect the sealed tank and thermally insulating to a floating storage facility or terrestrial and a pump for driving a flow of cold liquid product through the insulated pipelines from or to the floating or land storage facility to or from the vessel vessel.
    [0005] Some aspects of the invention start from the idea of limiting the distance to be traveled by the tracer gas between the injection point and the detection point, so that the detection of leaks in the turret zone can be implemented. relatively quickly and with a relatively small amount of tracer gas relative to the volume of all the walls of the tank. Some aspects of the invention start from the idea of proposing a test method that can be performed at sea with the tank in cold, so as to avoid immobilizing the floating structure in dry dock.
    [0006] BRIEF DESCRIPTION OF THE DRAWINGS The invention will be better understood, and other objects, details, features and advantages thereof will become more apparent in the following description of several particular embodiments of the invention, given only in connection with the invention. illustrative and non-limiting, with reference to the accompanying drawings. - Figure 1 is a block diagram of a LNG vessel tank seen in section along a longitudinal axis of the vessel. - Figure 2 is a functional diagram of a liquid dome of the tank of Figure 1, seen from above. FIG. 3 is a broken isometric perspective view of a transverse wall delimiting a front side of the liquid dome of FIG. 2. FIG. 4 is an enlarged view of the zone IV of FIG. 1 according to one embodiment. FIG. 5 is a functional diagram of a steam dome of the tank of FIG. 1, viewed from above. FIG. 6 is an enlarged view of the zone VI of FIG. 1 according to one embodiment; FIG. 7 is a cutaway schematic representation of a tank of a LNG carrier and a loading / unloading terminal of this tank; . DETAILED DESCRIPTION OF EMBODIMENTS Referring to FIG. 1, there is shown schematically a longitudinal section of the hull 2 of a LNG tanker in which is disposed a sealed and insulating tank 1 made according to the technology of the membrane tanks. The vessel 1 is disposed between two transverse partitions 3 generally called "cofferdam" which divide the inner space of the shell into a plurality of polyhedral compartments for each to accommodate a respective tank.
    [0007] A vessel may thus comprise one or more similar vessels, as sketched on the right of FIG. 1. The hull 2 is a double wall delimiting a ballast space represented in FIG. 4 for the lower part of the vessel. The tank 1 is built on the inner wall 5 of the shell 2 which serves as a load-bearing wall. The upper wall 6 of the vessel 1 is similarly carried by an upper supporting wall 7 forming part of the shell 2. The vessel 1 has a generally polyhedral geometry and all the walls of the vessel consist of a multilayer structure known elsewhere in the technique of membrane tanks. It suffices to recall that this multilayer structure comprises successively a secondary insulating barrier 10, a secondary waterproof membrane 11, a primary insulating barrier 12 and a primary waterproof membrane 13 which directly contains the LNG stored in the tank 1. This multilayer structure can be realized according to various techniques, for example techniques marketed by the applicant company under the name Mark Ill®. FIG. 1 shows that the upper supporting wall 7 is interrupted in two places where the tank wall forms a projecting structure in the form of a turret or a chimney. The first turret is a liquid dome 15 which serves as a point of penetration for various LNG handling equipment, namely in the example shown a filling line 16, an emergency pumping line 17, unloading lines connected to discharge pumps 18, a spray line 20 and a feed line connected to a spraying pump 19. The second turret is a steam dome 21 which serves as a point of entry for a vapor collection pipe 22. The operation of this equipment is known elsewhere. With reference to FIGS. 2 to 4, characteristics of the liquid dome 15 will now be described more precisely. The elements similar or identical to those of FIG. 1 bear the same reference number increased by 100.
    [0008] As best seen in FIG. 2, the liquid dome has a square section formed of four similar vertical walls in which the above-mentioned multilayer structure, namely carrier wall 103, secondary insulating barrier 110, secondary waterproof membrane 111, barrier, is found each time. primary insulation 112 and primary waterproof membrane 113. Since the waterproofing membranes 111 and 113 are relatively fragile elements that are not designed to withstand high tearing forces, the liquid dome is equipped with a primary exhaust device 25 to protect the primary waterproof membrane 113 against overpressure and a secondary exhaust device 35 to protect the secondary waterproof membrane 111 against overpressure. More specifically, the primary exhaust device 25 comprises an exhaust pipe I opening on one side inside the primary insulating barrier 112 of the liquid dome and on the other side in an exhaust mast towards the atmosphere 30 disposed outside on the deck of the ship. A pressure relief valve 27 is arranged on the pipe I, which is closed by default. The valve 27 opens under the control of a valve driver 26 when the total pressure in the primary insulating barrier 112 exceeds a predefined level, for example 30 mbar or 3kPa. The valve driver 26 is connected to the pressure of the primary insulating barrier 112 by a control line N. Thus, the gas phase present in the primary insulating barrier 112 escapes automatically to the exhaust mast 30 when its pressure exceeds the predefined level.
    [0009] In the same way, the secondary exhaust device 35 has an exhaust pipe K opening on one side inside the secondary insulating barrier 110 of the liquid dome and on the other side in an exhaust line towards the atmosphere 40. A pressure relief valve 37 is arranged on the pipe K, which is closed by default. The valve 37 opens under the control of a valve driver 36 when the total pressure in the secondary insulating barrier 110 exceeds a predefined level, for example 30 mbar or 3kPa. The valve driver 36 is connected to the pressure of the secondary insulating barrier 110 by a control line M. Thus, the gas phase present in the secondary insulating barrier 110 escapes automatically to the exhaust line 40 when its pressure exceeds the predefined level. The opening pressures of the valves 27 and 37 may be equal or different. In order to detect leaks or leaks in the secondary waterproof membrane 111 at the level of the liquid dome 15, a device for injecting and detecting a tracer gas is used in the liquid dome 15. This device comprises a tracer gas tank 41 which is connected to the control line M via a valve 42 so as to be able to transfer tracer gas to the secondary insulating barrier 110 when the valve 42 is open. The tracer gas is for example argon or helium or any other gas or gas mixture that is not likely to liquefy during operation. This device also comprises a gas detector 43 capable of detecting the tracer gas and connected to the exhaust pipe I so as to be able to detect the presence of the tracer gas in the gas phase present in the primary insulating barrier 112. The principle The basic principle of the detection is that since the secondary waterproof membrane 111 is supposed to gas-tight isolate the secondary insulating barrier 110 of the primary insulating barrier 112, a positive detection of the tracer gas in the primary insulating barrier 112 while this gas has been injected only into the secondary insulating barrier 110 necessarily betrays the existence of a leak. Alternatively, the tank 41 can be connected to the pipe K and / or the detector 43 can be connected to the pipe N without changing the operating principle. FIG. 2 also shows nitrogen feed lines entering the vessel at the liquid dome to control the total pressure in the secondary 110 and primary 112. These feed lines are from a reservoir. of nitrogen gas symbolized at numeral 45. They include a secondary nitrogen line V opening into the secondary insulating barrier 110 at the bottom of the vessel and a primary nitrogen line 44 which branches out into a plurality of distribution lines. nitrogen A, B, C, D, E, F, G, H, J, L all opening into the primary insulating barrier 112 at the bottom of the tank. Figure 3 shows further details on the possible route of the gaseous dinitrogen feed lines in the vessel wall. It shows in particular that these lines open at the bottom of the tank at a considerable distance from the liquid dome and the steam dome. The gaseous dinitrogen feed lines can serve in particular to render the vessel walls inert and to adjust the total pressure therein by means of a pressure control system which is known elsewhere. This pressure control system can be used to improve the operation of leak detection. According to a corresponding embodiment, the leak detection can be implemented as follows: Injecting the tracer gas into the secondary space 110 of the liquid dome Set the pressure to a slightly higher level in the secondary space 110 in the primary space 112, preferably without reaching the opening pressure of the secondary exhaust valve 37 to avoid damaging the secondary diaphragm 111. These two steps can also be performed simultaneously or in another order. Detect the presence of the tracer gas in the primary space 112. Thanks to the slight difference in pressure, the tracer gas transfer can be accelerated, which makes it possible to reduce the duration of the leak detection test. For example, the pressure in the primary barrier is set to 10mbar (100kPa) relative and the pressure in the secondary barrier is set to 17mbar (170kPa) relative, a difference of 70kPa. This difference can be higher, for example up to 250 kPa, to accelerate the implementation of the test. The complete duration of the test can thus be less than 4 hours per dome, and preferably of the order of 60 minutes. In a mode not shown, the positions of the gas detector 43 and the tracer gas tank 41 are exchanged and the pressure differences are reversed. The gas detector may be a commercially available gas analyzer operating according to any suitable technology, for example by mass spectrometry or the like. To refine the diagnosis of leaks, it is preferable to measure over time the concentration of tracer gas present in the primary space 112. Thus, the duration and the amount of tracer gas make it possible to obtain information on: the existence of a leak, if the tracer gas is detected in a significant amount, - the flow of the leak (s) by integrating the amount of tracer gas over time, - the location on the liquid dome of the leakage, by measuring the time of first detection of the tracer gas with respect to the travel time in the insulating barriers. Since the tank wall in the liquid dome has a relatively small volume relative to the entire tank, for example about 2 m 3, the leak test can be carried out with a relatively small volume of tracer gas. for example about 3 m3 of argon. Figure 4 shows further details of implementation of the liquid dome in an embodiment using Mark Ill® technology. For the sake of brevity only one pipe has been shown to illustrate the line K or M of the secondary exhaust device 35 and only one pipe has been shown to illustrate the pipe N or I of the primary exhaust device 25. In addition have been represented in the same plan. However, these pipes are four in a real implementation and it is not necessary that they are in the same plane, as shown in Figure 2. In addition, it is possible to provide one or more additional tracer gas injection points to improve test execution speed, especially for a large liquid dome. These additional injection points can be evenly distributed around the periphery of the liquid dome 15. In the liquid dome 15 of FIG. 4, the support structure comprises a vertical supporting wall 103 called surbau which rises above the bridge. 107 of the vessel and a horizontal wall 46 at the top of the carrier wall 103. The horizontal wall 46 extends all around the liquid dome and supports a tank cover 47. The cover 47 consists essentially of a metal wall lid 48 and a thermal insulation 49 which fits into the top of the liquid dome. The horizontal wall 46 carries a profiled metal plate 48 shaped L 30 which is welded to the inner face of the wall 46 and extends downwards. Prefabricated panels are attached to the carrier wall 103 to form the primary heat-insulating barrier, the secondary sealing barrier and the secondary heat-insulating barrier.
    [0010] In the stopping zone of the secondary membrane 111, a flexible sealed composite ply 50 sealingly connects the waterproof ply of the prefabricated panel to the bent rim 51 of the plate 48. The bonding of the ply 50 to the flange 51 is carried out at using a suitable adhesive, for example polyurethane type. A glass wool pad 52 is inserted between the metal plate 48 and the carrier wall 103 to extend the secondary insulating barrier 110, which is essentially made of insulating foam panels. A layer of putty 53, for example epoxy resin, is crushed between the underside of the flange 51 and the last insulating foam panel to precisely fix and position the panel. A second layer of putty 54, for example also epoxy resin, is carried by the upper face of the flange 51 and is crushed between the flange 51 and a wooden beam 55 which is arranged horizontally along the plate 48. The beam 55 may be bolted to the plate 20. Other insulating foam blocks 56 are disposed between the top of the beam 55 and the horizontal wall 46 of the supporting structure to extend the primary insulation barrier. The end of the primary sealing barrier 113 is sealingly attached to the supporting structure by welding to a U-section profile member 57 which is carried by the end of the horizontal wall 46. In this embodiment , the glass wool packing 52 which is all around the liquid dome is a preferred passage area for the tracer gas which has passed a leak, due to the low pressure drop. Thus, it is possible to detect leaks at any location around the liquid dome itself with only one or a small number of gas detection points. The methods described above for performing leak detection in a liquid dome may be carried out analogously in a steam dome, as will now be described with reference to FIGS. 5 and 6. As best seen in FIG. the vapor dome has a circular section in which there is found, at least functionally, the aforementioned multilayer structure, namely carrier wall 203, secondary insulating barrier 210, secondary waterproof membrane 211, primary insulating barrier 212 and primary waterproof membrane 213.
    [0011] Since the waterproofing membranes 211 and 213 are relatively fragile elements that are not designed to withstand high tearing forces, the steam dome is equipped with a primary exhaust device 125 to protect the primary waterproof membrane 213 against the overpressures and a secondary exhaust device 135 to protect the secondary waterproof membrane 211 against overpressures. More specifically, the primary exhaust device 125 comprises an exhaust pipe Q opening on one side inside the primary insulating barrier 212 of the steam dome and on the other side in the exhaust mast towards the atmosphere 30 of Figure 2, as symbolized by the arrow 130 of Figure 5. A relief valve 127 is arranged on the pipe Q, which is closed by default. The valve 127 opens under the control of a valve driver 126 when the total pressure in the primary insulating barrier 212 exceeds a predefined level, for example 30 mbar or 3kPa. The valve driver 126 is connected to the pressure of the primary insulating barrier 212 by a control line R. Thus, the gas phase present in the primary insulating barrier 212 escapes automatically to the exhaust mast 30 when its pressure exceeds the predefined level. In the same way, the secondary exhaust device 135 has an exhaust pipe S opening on one side inside the secondary insulating barrier 210 of the steam dome and on the other side in an exhaust line to the atmosphere 140. A relief valve 137 is arranged on the pipe S, which is closed by default. The valve 137 opens under the control of a valve driver 136 when the total pressure in the secondary insulating barrier 210 exceeds a predefined level, for example 30 mbar or 3kPa. The valve pilot 136 is connected to the pressure of the secondary insulating barrier 210 by a control line T. Thus, the gas phase present in the secondary insulating barrier 210 escapes automatically to the exhaust line 140 when its pressure exceeds the predefined level. The opening pressures of the valves 127 and 137 may be equal or different. In order to detect leaks or leaks in the secondary waterproof membrane 211 at the vapor dome 21, a device for injecting and detecting a tracer gas is used. This device comprises a tracer gas reservoir 141 which is connected to the exhaust pipe S via a valve 142, so as to transfer tracer gas to the secondary insulating barrier 210 when the valve 142 is open. The tracer gas is for example Argon or Helium or any other gas or mixture of gases that is not likely to liquefy during operation.
    [0012] This device also comprises a gas detector 143 capable of detecting the tracer gas and connected to the exhaust pipe Q, so as to detect the presence of the tracer gas in the gas phase present in the primary insulating barrier 212. For the rest , the operation of the leak detection in the vapor dome is identical to the case of the liquid dome described above. FIG. 6 shows further details of implementation of steam dome 221 in one embodiment using Mark Ill® technology. Elements similar or identical to those of Figure 1 bear the same reference numeral increased by 200.
    [0013] For the sake of brevity only one pipe has been shown to illustrate the S or T pipe of the secondary exhaust device 135. In addition, this pipe has been shown in a same plane as the pipes R and Q of the primary exhaust system. 125. However, there are four such channels Q, R, S, T in a real implementation and it is not necessary that they be in the same plane, as shown in FIG. in addition, it is possible to provide one or more additional tracer gas injection points to improve the speed of execution of the test, especially for a large steam dome. These additional injection points can be distributed evenly around the periphery of the steam dome 221.
    [0014] In the steam dome 221 of FIG. 6, the upper supporting wall 207 has a circular opening 31 around which is welded a shank 32 which extends outside the upper supporting wall 207. A metal vapor collecting duct 222 is anchored inside the barrel 32 and is intended to extract the vapors produced by the evaporation of the fluid in the tank. For this purpose, the collecting duct 222 passes through the vessel wall in the center of the circular opening 31 as well as the sealed membranes 211 and 213 and the insulating barriers 210 and 212 to open into the vessel. This collecting duct 222 is connected in particular to a steam collector outside the vessel which extracts this vapor and forwards it, for example, to the propulsion device of the vessel to feed the propulsion of the vessel or to a liquefaction device for reintroduction then the fluid in the tank. The primary sealing barrier 213 is sealingly connected to the collecting duct 222. Similarly, the secondary sealing barrier 211 is sealingly connected to the collecting duct 222 except in two passages 58 and 59 allowing the fluid to be present. between the two sealing barriers to flow to the sampling lines 60 and 61. The absence of the secondary waterproof membrane at this location is symbolized by the dashed lines in the passages 58 and 59. In this way, the space between the secondary watertight barrier 211 and the primary watertight barrier 213 forms a sealed primary space connected to the two exhaust pipes 60 and 61. Furthermore, the shaft 32 is sealingly connected to the upper supporting wall 7 and the collecting pipe. 222. The collecting pipe comprises an insulating layer 62 uniformly distributed over its outer surface which has a smaller diameter than the opening. In this way, the spacing between the insulating layer 62 and the circular opening 31 allows the flow of gas between the secondary insulating barrier 210 and an intermediate space 64 between the can 32 and the insulating layer 62. as indicated by the arrow 99. The intermediate space 20 and the secondary insulating barrier 210 thus form a secondary sealing space. The two sampling lines 60 and 61 extend parallel to the collecting duct 222 in the insulating layer 62 from the outside of the barrel 32 to the primary sealing space. Line 61 opens into line Q of FIG. 5 and makes it possible to make a passage between the primary sealing space and the not shown pressure relief valve. The pipe 60 opens into the pipe R of Figure 5 and allows a passage between the primary space and the valve driver not shown. Two other pipes represented by the reference S, T are welded to the barrel 32 and open into the barrel 32 into the secondary sealed space to allow also fluid management and pressure measurement in the secondary sealed space. . It will be noted that, in the barrel 32 of the steam dome 221, the structure of the tank wall is not rigorously a multilayer structure such as it exists in the walls of the tank, since the primary space is here limited to the passage section of two sampling lines 60 and 61 which pass entirely within the secondary space. However, the structure remains that of a primary space and a secondary space supposed to be isolated from each other by a gas-tight separation, so that the leak detection tests described above retain all their meaning in this slightly different structure. The above-mentioned leak detection methods can be implemented in the steam dome 221 of FIG. 6 by injecting the tracer gas through the S or T line and detecting the tracer gas through the line Q or R. The arrows 63 of Figure 6 schematically illustrate the path of the tracer gas in the intermediate space 64 between the S or T pipe which injects the tracer gas and the secondary insulating barrier 210 of the tank top wall where it can penetrate. Other details of implantation of a steam dome can be found in the publication FR-A-2984454. The technique described above for producing a leak detection device in a protruding part of the tank wall can be used in different types of tanks, for example to form the liquid dome or the steam dome of an LNG tank in a land installation or in a floating structure such as a LNG tank or other. Referring to Figure 7, a cutaway view of a LNG tank 70 shows a sealed and insulated tank 71 of generally prismatic shape mounted in the double hull 72 of the ship. The wall of the tank 71 comprises a primary sealed barrier intended to be in contact with the LNG contained in the tank, a secondary sealed barrier arranged between the primary waterproof barrier and the double hull 72 of the ship, and two insulating barriers arranged respectively between the primary watertight barrier and the secondary watertight barrier and between the secondary watertight barrier and the double hull 72. In a manner known per se, loading / unloading pipes 73 arranged on the upper deck of the ship may be connected, by means of appropriate connectors, at a marine or port terminal for transferring an LNG cargo from or to the tank 71. Figure 7 shows an example of a marine terminal including a loading and unloading station 75, an underwater pipe 76 and an onshore installation. 77. The loading and unloading station 75 is a fixed off-shore installation bile 74 and a tower 78 which supports the movable arm 74. The movable arm 74 carries a bundle of insulated flexible pipes 79 that can be connected to the loading / unloading pipes 73. The movable arm 74 can be adapted to all the LNG carriers . A connection pipe (not shown) extends inside the tower 78. The loading and unloading station 75 enables the loading and unloading of the LNG tank 70 from or to the shore facility 77. liquefied gas storage tanks 80 and connecting lines 81 connected by the underwater line 76 to the loading or unloading station 75. The underwater line 76 allows the transfer of the liquefied gas between the loading or unloading station 75 and the onshore installation 77 over a large distance, for example 5 km, which makes it possible to keep the tanker vessel 70 at great distance from the coast during the loading and unloading operations. In order to generate the pressure necessary for the transfer of the liquefied gas, pumps on board the ship 70 and / or pumps equipping the shore installation 77 and / or pumps equipping the loading and unloading station 75 are used. Although the invention has been described in connection with a number of particular embodiments, it is obvious that it is in no way limited thereto and that it includes all the technical equivalents of the means described and their combinations if These are within the scope of the invention. The use of the verb "to include", "to understand" or "to include" and its conjugated forms does not exclude the presence of other elements or steps other than those set out in a claim. The use of the indefinite article "un" or "un" for an element or step does not exclude, unless otherwise stated, the presence of a plurality of such elements or steps. In the claims, any reference sign in parentheses can not be interpreted as a limitation of the claim. 30
    权利要求:
    Claims (16)
    [0001]
    REVENDICATIONS1. Floating structure comprising a shell including bearing walls (3, 5, 7) defining a polyhedral space inside the shell, the floating structure comprising a sealed and thermally insulating tank (1) housed in the polyhedral space for storing a low temperature liquefied gas, wherein an upper carrier wall (7, 107) of the shell has an opening and carries a turret (15, 21, 221) projecting from an outer surface of the upper carrier wall around the opening, the opening and the turret being for passing cargo handling equipment (16, 22, 222) for handling a liquid phase and / or a vapor phase of the liquefied gas contained in the vessel, wherein the vessel has a plurality of vessel walls attached to the carrier walls of the shell, wherein an upper vessel wall has a multilayer structure attached to an inner surface of the wall upper carrier, the multilayer structure being formed of a primary sealing membrane (13, 113, 213) intended to be in contact with the liquefied gas contained in the tank, a secondary sealing membrane (11, 111, 211) disposed between the primary sealing membrane and the upper supporting wall, a secondary insulating barrier (10, 110, 210) disposed between the secondary sealing membrane and the upper supporting wall and a primary insulating barrier (12, 112, 212 ) disposed between the secondary sealing membrane and the primary sealing membrane, in which the turret comprises: an inner tight wall forming a sheath (113, 222) engaged through the opening of the upper supporting wall (7, 107, 207) and sealingly connected with the primary sealing membrane (13, 213) of the upper vessel wall all around the sheath, an outer sealing wall (103, 32) disposed around the sheath away from the sheath parallel to the sheath, the outer impervious wall being sealingly bonded to the upper bearing wall around the opening, a separating wall (111, 60, 61) arranged between the outer impervious wall (103). , 32) and the internal tight wall (113, 222) of the turret and dividing the space defined between the outer wall and the inner wall of the turret into, on the one hand, a secondary space (110, 62, 64) communicating through the opening of the upper carrier wall with the secondary insulating barrier (10, 210) of the upper vessel wall disposed around the opening and, on the other hand, a primary space (112, 60, 61 ) communicating through the opening of the upper support wall with the primary insulating barrier (12, 212) of the upper vessel wall disposed around the opening, a primary exhaust device (25, 125) having a primary overpressure (27, 127) and one primary exhaust system (I, Q) communicating directly with the primary space of the turret and passing through the external tight wall of the turret to allow gas to escape from the primary space in response to an opening of the pressure relief valve primary, a secondary exhaust device (35, 135) having a secondary pressure relief valve (37, 137) and a secondary exhaust pipe (K, S) communicating directly with the secondary space of the turret and passing through the wall external sealing of the turret to allow exhaust gas from the secondary space in response to an opening of the secondary pressure relief valve, the floating structure further comprising: a gas reservoir (41, 141) containing an incondensable tracer gas or having a condensing temperature lower than the low temperature of the liquefied gas contained in the tank, the gas tank being connected via a valve control unit (42, 142) to one of the primary exhaust device and the secondary exhaust device and a gas detector (43, 143) for detecting the tracer gas, the gas detector 25 being in communication with the other one of the primary exhaust device, in particular the primary exhaust pipe, and the secondary exhaust system, in particular the secondary exhaust pipe.
    [0002]
    The floating structure according to claim 1, wherein the primary or secondary exhaust device further comprises a primary or secondary control line (M, N, R, T) which communicates directly with the primary or secondary space of the turret and which passes through the outer tight wall of the turret to control the primary or secondary pressure relief valve according to the pressure in the primary or secondary space, and in which gas tank (41, 141) is in direct communication with the primary or secondary command line.
    [0003]
    The floating structure according to claim 1 or 2, wherein the primary or secondary exhaust device further comprises a primary or secondary control line (M, N, R, T) which communicates directly with the primary space or secondary of the turret and which passes through the outer wall of the turret to control the primary or secondary pressure relief valve according to the pressure in the primary or secondary space, and wherein the gas detector (43, 143) is in direct communication with the primary or secondary control line.
    [0004]
    4. Floating structure according to one of claims 1 to 3, wherein the turret is a steam dome (221) of the tank, the sheath engaged through the opening of the upper bearing wall being a collecting duct (22, 222). ) connected to a main steam manifold of the floating structure, and wherein the turret partition wall forms a primary sampling pipe (60, 61) extending parallel to the collecting pipe in the space defined between the outer sealing wall (32) and the inner sealing wall (222) of the turret and having an inner end (58, 59) opening into the primary insulating barrier of the upper tank wall and an outer end (Q, R). opening directly into the primary exhaust device (125), the primary space of the turret having the interior space of the primary sampling line.
    [0005]
    Floating structure according to one of claims 1 to 3, wherein the turret is a liquid dome (15) of the vessel further comprising a top wall (46) disposed on an upper end of the outer watertight wall (103). ) of the liquid dome and having an opening aligned with a central zone of the opening of the upper supporting wall, the sheath formed by the inner sealing wall (113) of the liquid dome being a primary sealing membrane having an upper edge attached to sealingly on an edge (57) of the top wall all around the opening of the top wall, and wherein the partition wall comprises a secondary sealing membrane (111) extending all around the sheath between the outer sealing wall and the sheath (113) and having an inner end sealingly connected to the secondary sealing membrane (11) of the upper tank wall all around the sheath and a outer end (50) sealingly connected to the apex wall (46) all around the opening of the top wall of the liquid dome.
    [0006]
    The floating structure according to claim 5, wherein the wall of the liquid dome (15) has a multilayer structure attached to an inner surface of the outer wall, the multilayer structure being formed of the primary waterproofing membrane (113). of the liquid dome, the secondary waterproofing membrane (111) of the liquid dome, a secondary insulating barrier (110) of the liquid dome disposed between the secondary sealing membrane and the outer sealing wall and a primary insulating barrier (112) disposed between the secondary waterproofing membrane and the primary waterproofing membrane of the liquid dome.
    [0007]
    The floating structure according to claim 6, further comprising a connecting plate (48) disposed between the outer end (50) of the secondary sealing membrane of the liquid dome and the top wall (46), the Link comprising a main branch extending parallel to the outer sealing wall between the outer sealing wall and the sheath formed by the inner sealed wall of the liquid dome, the main branch having an upper end attached to the top plate (46) . and a lower end extending through a rim (51) bent inwardly of the liquid dome with respect to the main body, the outer end (50) of the secondary sealing membrane being sealingly attached to the rim (51), wherein the secondary insulating barrier of the liquid dome comprises a fibrous liner (52) disposed between the main branch of the connecting plate (48) and the outer impervious wall (103), and wherein the Secondary exhaust (K, M) opens into the fibrous lining.
    [0008]
    A floating structure according to claim 7, wherein the primary exhaust pipe (N, I) passes through the main branch of the connecting plate (48) and opens into the primary insulating barrier between the main branch of the base plate connection and the primary sealing membrane (113) of the liquid dome.
    [0009]
    Floating structure according to one of claims 5 to 8, further comprising a nitrogen distribution system including a nitrogen gas reservoir (45) and a distribution network, the distribution network comprising a primary distribution conduit ( 44, AG, L, J) extending from an upper bridge of the floating structure through the primary space (112) of the liquid dome and through the primary insulation barrier (12) of a transverse wall of the tank to a bottom area of the tank, and a secondary delivery line (V) extending from the upper deck of the floating structure through the secondary space (110) of the liquid dome and through the secondary isolation barrier of the transverse wall of the vessel to the bottom zone of the vessel, and wherein the nitrogen distribution system further comprises pressure regulating means for regulating the pressure in the barrier 10 primary insulation and the barrier secondary insulation of the vessel walls by means of the primary and secondary distribution lines.
    [0010]
    10. Floating structure according to one of claims 1 to 9, wherein the tracer gas is selected from argon, helium and mixtures thereof.
    [0011]
    Floating structure according to one of claims 1 to 10, wherein the tracer gas reservoir (41, 141) is removably attached to the primary or secondary exhaust device.
    [0012]
    The method of operating a floating structure according to one of claims 1 to 11, comprising: injecting the tracer gas through one of the primary and secondary exhaust devices (25, 125, 35, 135). in the primary or secondary space of the turret (15, 221) without exceeding the opening pressure of the primary or secondary pressure relief valve, detecting the tracer gas through the other of the primary and secondary exhaust devices (25). , 125, 35, 135) in the primary or secondary space of the turret, and to diagnose a leak in the secondary sealing barrier (11, 211) of the tank top wall and / or in the partition wall ( 111, 60, 61) of the turret in response to detection of the tracer gas.
    [0013]
    The method of claim 12, wherein the tracer gas is injected into the secondary space through the secondary exhaust device (35, 135) and detected in the primary space through the primary exhaust device ( 25, 125), the method further comprising: maintaining a higher total pressure in the secondary space (110, 210) than in the primary space (112, 212) by injecting nitrogen gas into the secondary space, without exceed the opening pressure of the secondary pressure relief valve.
    [0014]
    The method of claim 12 or 13, wherein the step of diagnosing a leak includes one of the measures selected from the group consisting of recording the presence of a leak, measuring a quantity or a concentration of the tracer gas to determine a flow rate of the leak, and measuring a time delay between the injection and the tracer gas detection to determine a position of the leak.
    [0015]
    15. A method of loading or unloading a floating structure (70) according to one of claims 1 to 11, wherein liquefied gas is fed through insulated pipes (73, 79, 76, 81) from or to a floating or land storage facility (77) to or from the sealed and thermally insulating vessel (71).
    [0016]
    16. Transfer system for liquefied gas at low temperature, the system comprising a floating structure (70) according to one of claims 1 to 11, insulated pipes (73, 79, 76, 81) arranged to connect the vessel. watertight and thermally insulating vessel (71) at a floating or land storage facility (77) and a pump for driving a flow of cold liquid product through the insulated pipelines from or to the floating or land storage facility to or from the vessel of the ship.
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    同族专利:
    公开号 | 公开日
    CL2016002523A1|2017-04-21|
    SG11201608266SA|2016-11-29|
    US20170138536A1|2017-05-18|
    CN106170657B|2018-09-21|
    EP3129700A1|2017-02-15|
    JP6630288B2|2020-01-15|
    WO2015155377A1|2015-10-15|
    KR20160141780A|2016-12-09|
    CN106170657A|2016-11-30|
    KR102285764B1|2021-08-04|
    AU2015245422A1|2016-11-03|
    PH12016501956A1|2017-01-09|
    EP3129700B1|2018-12-19|
    MY181455A|2020-12-22|
    ES2715887T3|2019-06-06|
    AU2015245422B2|2017-11-30|
    FR3019520B1|2016-04-15|
    JP2017512953A|2017-05-25|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    FR2517802A1|1981-12-04|1983-06-10|Gaz Transport|Leak detector for liquefied gas storage vessel - has gas sampling pipes, at known points in vessel isolating barriers, connected to analyser|
    FR2960640A1|2010-06-01|2011-12-02|Gaztransp Et Technigaz|TEST OF SEALING OF A RESERVOIR IN RELATION TO A GAS HAVING AN INFRARED SIGNATURE|
    FR2984454A1|2011-12-20|2013-06-21|Gaztransp Et Technigaz|TANK WALL COMPRISING A CONDUIT|WO2017174938A1|2016-04-07|2017-10-12|Gaztransport Et Technigaz|Thermally-insulating sealed tank|
    WO2017216477A1|2016-06-15|2017-12-21|Gaztransport Et Technigaz|Gas dome structure for a sealed, thermally insulated vessel|
    FR3062703A1|2017-02-09|2018-08-10|Gaztransport Et Technigaz|GAS DOME STRUCTURE FOR A SEALED AND THERMALLY INSULATING TANK|
    FR3087537A1|2018-10-22|2020-04-24|Gaztransport Et Technigaz|MEMBRANE WATERPROOFING TEST METHOD AND RELATED LEAK DETECTION DEVICE|
    WO2020229777A1|2019-05-16|2020-11-19|Gaztransport Et Technigaz|Vessel for transporting and/or storing liquid gas|US4359958A|1978-06-28|1982-11-23|Durant Peter D|Cargo transport system|
    US4372340A|1980-09-29|1983-02-08|Chicago Bridge & Iron Company|Liquid storage tank|
    JPS61129884A|1984-11-29|1986-06-17|Toshiba Corp|Cryogenic container|
    HU9800578A1|1998-03-16|1999-11-29|István Szakály|Process and apparatus for eliminating filling and evaporation loss of volatile materials storaged in tank, and for protection of corrosion of the storaged product and tank|
    FR2847245B1|2002-11-19|2005-06-24|Coflexip|LIQUEFIED GAS TRANSFER INSTALLATION AND USE THEREOF|
    GB0320474D0|2003-09-01|2003-10-01|Cryostar France Sa|Controlled storage of liquefied gases|
    KR100787777B1|2007-03-09|2007-12-24|현대중공업 주식회사|Improved gas detection and ventilation system for boil-off gas treating facility in the confined room|
    CN102171094A|2008-10-09|2011-08-31|吉宝岸外与海事科技中心私人有限公司|Hull conversion of existing vessels for tank integration|
    FI123162B|2011-05-04|2012-11-30|Waertsilae Finland Oy|LPG removal system, LPG storage tank, LPG tank replacement method and LPG tank manufacturing method|CN104956140B|2012-12-14|2016-11-09|瓦锡兰芬兰有限公司|Fill method and the liquefied gas as fuel system of liquefied gas to fuel tank|
    FR3030014B1|2014-12-15|2017-10-13|Gaztransport Et Technigaz|INSULATING BLOCK SUITABLE FOR MAKING AN INSULATING WALL IN A WATERPROOF TANK|
    FR3035175B1|2015-04-20|2017-04-28|Gaztransport Et Technigaz|THERMALLY INSULATED AND WATERPROOF TANK EQUIPPED WITH A THROUGH ELEMENT|
    FR3069904B1|2017-08-07|2020-10-02|Gaztransport Et Technigaz|WATERPROOF AND THERMALLY INSULATION CONTAINING A GAS DOME STRUCTURE|
    FR3070747B1|2017-09-04|2021-01-08|Gaztransport Et Technigaz|WATERPROOF AND THERMALLY INSULATING TANK WITH ANTI-CONVECTIVE COVER STRIP|
    FR3070673B1|2017-09-07|2019-09-13|Gaztransport Et Technigaz|FLOATING WORK COMPRISING A TANK CAPABLE OF CONTAINING LIQUEFIED COMBUSTIBLE GAS|
    FR3090809B1|2018-12-19|2020-12-25|Gaztransport Et Technigaz|LEAK DETECTION PROCESS ON A SEALED AND THERMALLY INSULATED TANK|
    KR102335583B1|2020-06-18|2021-12-03|현대중공업 주식회사|liquefied gas tank and ship having the same|
    KR102350341B1|2020-06-18|2022-01-11|현대중공업 주식회사|liquefied gas tank and ship having the same|
    KR102335582B1|2020-06-18|2021-12-03|현대중공업 주식회사|liquefied gas tank and ship having the same|
    KR102335580B1|2020-06-18|2021-12-03|현대중공업 주식회사|liquefied gas tank and ship having the same|
    KR102335577B1|2020-06-18|2021-12-03|현대중공업 주식회사|liquefied gas tank and ship having the same|
    KR102335584B1|2020-06-18|2021-12-03|현대중공업 주식회사|liquefied gas tank and ship having the same|
    KR102335578B1|2020-06-18|2021-12-03|현대중공업 주식회사|liquefied gas tank and ship having the same|
    KR102335581B1|2020-06-18|2021-12-03|현대중공업 주식회사|liquefied gas tank and ship having the same|
    法律状态:
    2015-04-30| PLFP| Fee payment|Year of fee payment: 2 |
    2016-04-28| PLFP| Fee payment|Year of fee payment: 3 |
    2017-04-28| PLFP| Fee payment|Year of fee payment: 4 |
    2018-04-26| PLFP| Fee payment|Year of fee payment: 5 |
    2019-04-29| PLFP| Fee payment|Year of fee payment: 6 |
    2021-01-08| ST| Notification of lapse|Effective date: 20201205 |
    优先权:
    申请号 | 申请日 | 专利标题
    FR1453115A|FR3019520B1|2014-04-08|2014-04-08|WATERPROOF AND THERMALLY INSULATED TANK IN A FLOATING WORK|FR1453115A| FR3019520B1|2014-04-08|2014-04-08|WATERPROOF AND THERMALLY INSULATED TANK IN A FLOATING WORK|
    MYPI2016703641A| MY181455A|2014-04-08|2015-04-03|Sealed, heat-insulated vessel housed in a buoyant structure|
    US15/302,002| US20170138536A1|2014-04-08|2015-04-03|Sealed, heat-insulated vessel housed in a buoyant structure|
    AU2015245422A| AU2015245422B2|2014-04-08|2015-04-03|Sealed, heat-insulated vessel housed in a buoyant structure|
    SG11201608266SA| SG11201608266SA|2014-04-08|2015-04-03|Sealed, heat-insulated vessel housed in a buoyant structure|
    ES15715321T| ES2715887T3|2014-04-08|2015-04-03|Waterproof and thermally insulating tank housed in a floating building|
    JP2016560927A| JP6630288B2|2014-04-08|2015-04-03|Sealed and thermally insulated container housed in a floating structure|
    KR1020167030039A| KR102285764B1|2014-04-08|2015-04-03|Sealed, heat-insulated vessel housed in a buoyant structure|
    PCT/EP2015/097015| WO2015155377A1|2014-04-08|2015-04-03|Sealed, heat-insulated vessel housed in a buoyant structure|
    EP15715321.4A| EP3129700B1|2014-04-08|2015-04-03|Sealed, heat-insulated vessel housed in a buoyant structure|
    CN201580018633.8A| CN106170657B|2014-04-08|2015-04-03|Including the floating structure of sealing heat-insulation storage tank and the method for running the floating structure|
    PH12016501956A| PH12016501956A1|2014-04-08|2016-10-03|Sealed, heat-insulated vessel housed in a buoyant structure|
    CL2016002523A| CL2016002523A1|2014-04-08|2016-10-04|Leak detection system for a storage and transport tank of a liquefied gas on a floating structure, procedure|
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