法国专利FR3014197A1 MONITORING A SEALED AND THERMALLY INSULATING TANK

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专利摘要:
A method of monitoring a sealed and thermally insulating vessel (1) for containing a low temperature liquefied fuel gas, wherein a wall of the vessel comprises a thermally insulating barrier (3) disposed between the sealing membrane and the wall carrier, the thermally insulating barrier comprising insulating solids and a gas phase maintained at a negative relative pressure, the method comprising: obtaining a diluted gas sample by taking a sample of the gas phase at the negative relative pressure in the barrier thermally insulating through a sampling line (11) and adding a controlled quantity of inert gas to the gaseous phase to be withdrawn or withdrawn, raising the pressure of the diluted gas sample to an operating pressure a gas analyzer (25), and measuring a concentration of the fuel gas in the sample of diluted gas with the gas analyzer.
公开号:FR3014197A1
申请号:FR1361899
申请日:2013-11-29
公开日:2015-06-05
发明作者:Laurent Spittael；Bruno Deletre；Fabrice Lombard；Nicolas Haquin；Abdoulaye Diouf；David Beauvais；Eric Biederman；Raphael Prunier
申请人:Gaztransport et Technigaz SARL；
IPC主号:

专利说明:

[0001] TECHNICAL FIELD The invention relates to the field of monitoring sealed and thermally insulating vessels intended to contain a liquefied combustible gas at low temperature, in particular in the case of a membrane vessel in which a wall of the vessel comprises a multilayer structure mounted on a carrier wall, the multilayer structure comprising a sealing membrane in contact with the liquefied fuel gas contained in the tank and a thermally insulating barrier disposed between the sealing membrane and the carrier wall, and in which the barrier thermally insulating comprises insulating solid materials and a gaseous phase maintained under a negative relative pressure by a suction device connected to the thermally insulating barrier. BACKGROUND OF THE INVENTION Sealed and thermally insulating vessels can be used to store and / or transport liquefied combustible gases at a low temperature, for example a gas with a high methane content commonly known as Liquefied Natural Gas (LNG), the point of which is boiling is at about -162 ° C at atmospheric pressure. In the membrane tank technology, a wall of the vessel comprises a multilayer structure mounted on a carrier wall and comprising at least one sealing membrane and at least one thermally insulating barrier disposed between the sealing membrane and the supporting wall. . The or each thermally insulating barrier comprises insulating solids forming a support surface for the or each sealing membrane. In order to increase the insulating power of the or each thermally insulating barrier, it has been proposed in FR-A-2535831 to maintain the gaseous phase of the secondary thermally insulating barrier at an absolute pressure lower than the ambient atmospheric pressure. i.e., negative relative pressure. Furthermore, the operation of such a tank of combustible liquefied gas assumes to guarantee strict safety conditions, and in particular to detect possible leaks of a membrane as effectively as possible.
[0002] For example, some regulations require that the contents of insulation spaces be analyzed at least every 30 minutes. Summary An idea underlying the invention is to provide methods and monitoring devices adapted to effectively detect the presence of fuel gas in the thermally insulating barrier, including when the gas phase is maintained under negative relative pressure. . According to one embodiment, the invention provides a sealed and thermally insulating uno cuvo monitoring method for containing a low temperature liquefied gas fuel, wherein a wall of the vessel comprises a multilayer structure mounted on a carrier wall the multilayer structure comprising a sealing membrane in contact with the liquefied fuel gas contained in the vessel and a thermally insulating barrier disposed between the sealing membrane and the carrier wall, the thermally insulating barrier comprising insulating solids and a a gaseous phase maintained at a negative relative pressure, the process comprising: obtaining a sample of diluted gas by taking a sample of the gas phase at the negative relative pressure in the thermally insulating barrier 20 through a sampling line leading to the outside of the tank wall and by adding a controlled quantity of inert gas in the gaseous phase to be taken or removed, compressing, ie raising the pressure of, the diluted gas sample to an operating pressure of a gas analyzer, and measuring a concentration of the fuel gas in the gas sample diluted with the gas analyzer. According to embodiments, such a monitoring method may include one or more of the following features. According to one embodiment, the method further comprises: determining a concentration of the fuel gas in the gas phase of the thermally insulating barrier as a function of the measured concentration and the amount of inert gas added to the gas phase.
[0003] The fuel gas may be liquefied natural gas, liquefied petroleum gas (LPG), ethylene or the like. The use of an inert gas makes it possible to increase the amount of material in the sample to be analyzed without the risk of producing an explosive mixture. For example, the inert gas may be selected from the group consisting of dinitrogen, helium, argon and mixtures thereof. According to embodiments, the negative relative pressure corresponds to an absolute pressure of less than 10 kPa, preferably less than 1 kPa. According to embodiments, the operating pressure of the gas analyzer is from 80 kPa to 120 kPa, preferably from 86 kPa to 108 kPa. With these operating pressures, it is possible to use relatively inexpensive and readily available gas analyzers. The concentration measurement of the fuel gas can be carried out according to various known detection techniques. For example, the gas analyzer may comprise a combustible gas detector selected from the group consisting of catalytic wire detectors, infrared detectors, particularly those operating by absorbance and / or transmittance measurement, and detector detectors. electrochemical cell. Two methods can be employed to dilute the low pressure gaseous phase present in the insulating barrier. A first method consists in mixing the inert gas with the gas phase upstream of the sampling of the sample, namely in the insulating barrier. A second method consists in mixing the inert gas with the gaseous phase downstream of the sampling of the sample, namely in the monitoring device. These two methods can be combined. According to an embodiment corresponding to the above-mentioned first method, the step of obtaining the diluted gas sample comprises: adding a controlled quantity of inert gas to the gas phase in the thermally insulating barrier to increase the relative pressure of the phase gaseous 30 in the thermally insulating barrier from a first negative value to a second negative value, and take a sample of the gas phase under the relative pressure equal second negative value in the thermally insulating barrier through the sampling line leading to outside the vessel wall to obtain the diluted gas sample, and decrease the relative pressure of the gas phase in the thermally insulating barrier from the second negative value to the first negative value after taking the sample of the gas phase. According to embodiments, the first negative value is less than 1 kPa, preferably less than or equal to 0.1 kPa, and the second negative value is greater than or equal to 1 kPa. According to an embodiment corresponding to the above-mentioned second method, the step of obtaining the diluted gas sample comprises: taking a sample of the gas phase under the negative relative pressure in the thermally insulating barrier through the sampling line opening out of the vessel wall, and adding a controlled amount of inert gas to the withdrawn gas phase sample. In this case, the steps of sampling, diluting and compressing the sample can be carried out jointly by means of a Venturi suction device, the Venturi suction device comprising: a main pipe having an inlet connected to a source of the pressurized inert gas and an outlet connected to a measurement chamber or an intermediate chamber, and a suction line having an upstream side connected to the sampling line and a downstream side opening laterally in a convergent-divergent of the main pipe so that a flow of inert gas in the main pipe produces a vacuum in the suction pipe. According to one embodiment, the step of sampling the sample comprises: pumping the gas phase sample through the sampling line to an intermediate chamber, and isolating the intermediate chamber from the thermally insulating barrier. According to another embodiment corresponding to the above-mentioned second method, the controlled quantity of inert gas is added to the intermediate chamber, the step of compressing the diluted gas sample comprising: pumping the diluted gas sample from the intermediate chamber to a measuring chamber coupled to the gas analyzer. In embodiments, the step of compressing the diluted gas sample may include: storing the gaseous phase sample taken from an intermediate chamber connected to the sampling line, and moving a movable wall in the intermediate chamber to contain the diluted gas sample in a measuring chamber of smaller capacity than the intermediate chamber.
[0004] For example, the measurement chamber consists of an end portion of the intermediate enclosure or a smaller enclosure connected to the intermediate enclosure. According to one embodiment, the steps of diluting and compressing the sample are performed by means of a Venturi suction device, the Venturi suction device comprising: a main pipe having an inlet connected to a source of the inert gas under pressure and an output connected to a measuring chamber, and a suction pipe having an upstream side connected to the intermediate chamber and a downstream side opening laterally in a convergent-diverging main pipe a flow of inert gas in the main line produces a vacuum in the suction line. According to one embodiment, the invention also provides a monitoring device suitable for a sealed and thermally insulating vessel for containing a low temperature liquefied gas fuel, wherein a wall of the vessel has a multilayer structure mounted on a wall carrier, the multilayer structure comprising a sealing membrane in contact with the liquefied fuel gas contained in the vessel and a thermally insulating barrier disposed between the sealing membrane and the carrier wall, the thermally insulating barrier comprising insulating solids and a gaseous phase maintained under a negative relative pressure, the monitoring device comprising: a sampling pipe connecting the thermally insulating barrier to the outside of the tank wall, a measurement chamber connected directly or indirectly to the sampling line by the intermediate of a vann e isolation, a gas analyzer coupled to the measuring chamber for measuring a concentration of combustible gas in the measurement chamber, a pumping device connected to the sampling line and able to take a sample of the gas phase under the negative relative pressure in the thermally insulating barrier and transferring the sample from the gas phase to the measurement chamber, an inert gas reservoir arranged to add a quantity of inert gas to the gaseous phase to be withdrawn or having been withdrawn , and a measuring device for measuring the amount of inert gas added to the gas phase. According to embodiments, such a monitoring device may include one or more of the following features. According to one embodiment, the device further comprises a data processing system capable of determining a concentration of the fuel gas in the gaseous phase of the thermally insulating barrier as a function of the concentration measured by the gas analyzer and the amount of inert gas added to the gas phase. The pumping device can be made in a variety of ways. According to one embodiment, the pumping device comprises a vacuum pump, for example Roots or other type. The pumping device may be dedicated to the monitoring device or, for reasons of economy, the pumping device may be shared between the monitoring device and a device for regulating the pressure of the insulating barrier serving to permanently maintain the pumping device. negative relative pressure in the insulating barrier. According to one embodiment, the pumping device comprises a Venturi suction device, the Venturi suction device comprising: a main pipe having an inlet connected to the inert gas reservoir and an outlet connected to the measurement chamber, and a suction pipe having an upstream side connected directly or indirectly to the sampling pipe and a downstream side opening laterally in a convergent-divergent main pipe so that a flow of inert gas in the pipe main produces a vacuum in the suction line.
[0005] According to one embodiment, the invention also provides a sealed and thermally insulating tank intended to contain a liquefied combustible gas at low temperature and equipped with a monitoring device mentioned above, in which a wall of the tank comprises a multilayer structure mounted on a carrier wall, the multilayer structure comprising a primary sealing membrane in contact with the liquefied fuel gas contained in the vessel, a secondary sealing membrane disposed between the primary sealing membrane and the carrier wall, a primary thermal insulation barrier disposed between the primary sealing membrane and the secondary sealing membrane, and a secondary thermal insulating barrier disposed between the secondary sealing membrane and the supporting wall, and wherein one or each thermally insulating barrier comprises insulating solids and a gaseous phase kept under a negative relative pressure, the monitoring device comprising a first sampling pipe opening into the primary thermally insulating barrier and a second sampling pipe opening into the secondary thermally insulating barrier. 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, a vessel for the transport of a cold liquid product comprises a double hull and a aforementioned tank disposed in the double hull.
[0006] According to one embodiment, the invention also provides a method of loading or unloading such a vessel, in which a cold liquid product is conveyed through isolated pipes from or to a floating or land storage facility to or from the vessel vessel.
[0007] According to one embodiment, the invention also provides a transfer system for a cold liquid product, the system comprising the abovementioned vessel, insulated pipes arranged to connect the vessel installed in the hull of the vessel 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. Some aspects of the invention are based on the idea of facilitating the analysis of a gaseous phase available under low pressure, and therefore in a small quantity, by limiting the costs of the sampling means and / or the means of sampling. analysis. BRIEF DESCRIPTION OF THE DRAWINGS The invention will be better understood, and other objects, details, features and advantages thereof will become more clearly apparent from the following description of several particular embodiments of the invention, given solely to illustrative and non-limiting, with reference to the accompanying drawings. - Figure 1 is a schematic representation of a membrane vessel and a monitoring device of this vessel. FIG. 2 is a schematic representation of a measuring chamber that can be used in the monitoring device of FIG. 1. FIG. 3 is a representation similar to FIG. 1 showing a device for monitoring the tank in another mode. of realization. FIG. 4 is an enlarged sectional representation of the zone IV of FIG. 4. FIG. 5 is a representation similar to FIG. 1 showing a device for monitoring the vessel according to another embodiment. FIG. 6 is a temporal diagram showing a variation of pressure that can be achieved in the insulating barrier of the tank of FIG. 5. FIG. 7 is a schematic artist's view showing a tank of a cut-off LNG carrier that can be equipped with a monitoring device and a terminal for loading / unloading this tank.
[0008] DETAILED DESCRIPTION OF EMBODIMENTS Referring to FIG. 1, a diaphragm tank 1 is shown very schematically in section. It comprises a bearing structure 2 defining a cavity in which the tank is constructed, an insulating barrier 3 comprising insulating elements fixed on the inner surfaces of the supporting structure 2, and a membrane 4 impervious to liquid and gas, for example sheet metal metallic, covering the entire inner surface of the tank. According to an embodiment shown in Figure 5, a secondary waterproof membrane may be interposed between the carrier structure 2 and the sealed membrane 4, so as to separate two insulating barriers on either side of the secondary waterproof membrane. This arrangement is not shown in Figure 1. The carrier structure 2 is also made substantially gas tight. Thus, the insulating barrier 3 is arranged in an isolation space which is isolated from the ambient pressure by the sealed membrane 4 and by the supporting structure 2. Unrepresented pressure control devices can be used to maintain a low pressure. gas in the insulation space, for example of the order of 0.1 to 1 kPa, so as to further lower the thermal conductivity of the insulating barrier 3.
[0009] A monitoring device can be used to perform the monitoring of the gas phase composition in the isolation space, in order to detect a possible leak in the waterproof membrane 4. The monitoring of the single space isolation 3 which is going to be described below can be performed in the same manner in each of the isolation spaces in the case of a tank having several successive membranes. For this, the monitoring device 10 of Figure 1 comprises a sampling pipe 11 which passes through the carrier structure 2 and which opens into the insulating barrier 3 to suck a sample of the gas phase at this location. Multiple unrepresented sampling lines can be arranged in the same way at different locations in the tank to be able to sample the gas phase in several corresponding zones of the insulating barrier 3. The sampling pipe 11 connects the insulating barrier 3 to a chamber intermediate 12 via a vacuum pump 13 or and an isolation valve 14. A connecting line 18 further connects a pressure nitrogen tank 15 to the intermediate chamber 12 via An isolating valve 16 is provided. A sensor system 17 is provided to measure a quantity of nitrogen introduced from the pressurized nitrogen container 15 into the intermediate chamber 12. Suitable sensors for this purpose are, for example, a flowmeter coupled to the connecting pipe 18 and / or temperature and pressure sensors coupled to the intermediate enclosure 12.
[0010] The intermediate chamber 12 can be operated as follows: A sample of the gas phase present in the insulating barrier 3 is transferred by the vacuum pump 13 into the intermediate chamber 12. The sample can be a very small amount of the gas phase, depending on the power of the vacuum pump 13 and / or the time available to perform the sampling. The valve 14 is closed to isolate the intermediate chamber 12. - A determined amount of nitrogen is added from the tank 15 in the intermediate chamber 12 by means of the valve 16. For example, the amount of dinitrogen can be measured by the intermediate measurements of pressure and temperature in the intermediate chamber 12 before and after the addition of dinitrogen. The addition of dinitrogen in the chamber 12 dilutes the sample to both obtain a larger amount of material to be analyzed and somewhat increase the pressure of the gas phase to be analyzed.
[0011] The pressure in the intermediate chamber 12 is then greater than that prevailing in the insulating barrier 3. It is for example of the order of 1 to 10 kPa. This is not necessarily sufficient for easy chemical analysis, as the most common gas analyzers operate at pressures near atmospheric pressure. It is therefore possible either to carry out the analysis of the diluted gas directly in the intermediate chamber 12, or to previously carry out an additional compression of the diluted gas in order to be able to use a faster and / or less expensive gas analysis apparatus. .
[0012] To achieve this additional compression, there is shown in Figure 1 a connecting pipe 24 connecting the intermediate chamber 12 to a measuring chamber 21 of smaller size via a second pump 20 and two valves of Isolation 22 and 23. The connecting pipe 24 can be exploited as follows: - After the addition of dinitrogen in the intermediate chamber 12, the valves 14 and 16 remain closed and the valves 22 and 23 are open and the pump 20 is activated to compress and transfer the diluted gas from the intermediate chamber 12 to the measurement chamber 21. When the pressure in the measurement chamber 21 reaches a value sufficient for the operation of the gas analyzer 25, the valve 23 is closed and the concentration of methane in the diluted gas is measured with the gas analyzer 25. Gas analyzers 25 for measuring a concentration of methane are for example available from the company. Swedish summer Consilium AB.
[0013] A data processing system 30 can then be used to calculate the concentration of methane in the insulating barrier 3 before dilution, from the measurement signals provided by the gas analyzer 25, shown schematically by the arrow 31, and signals measurements provided by the sensor system 17, shown schematically by the arrow 32. The data processing system 30, for example a programmed computer, can additionally fulfill an alarm function by emitting an alarm signal when the concentration methane in the insulating barrier 3 exceeds a predetermined threshold. Similarly, concentrations of other gases, including oxygen, water vapor, or other hydrocarbons can be found in the withdrawn gas phase. Corresponding gas analyzers are available on the market to produce these measurements. The hydrocarbon products are generally detectable by means of an infrared analyzer.
[0014] FIG. 1 shows two pumps 13 and 20 located one upstream and the other downstream of the intermediate enclosure 12. In a variant, only one of the two pumps 13 and 20 is provided and used to carry out all steps, ie, taking the initial sample and then compressing the diluted sample.
[0015] One of the pumps 13 and 20 can cumulatively fulfill the function of maintaining the low operating pressure in the isolation space 3. For this, a discharge pipe to the atmosphere and a corresponding control valve must be provided. Alternatively, an additional pump, not shown, is provided on line 18 to transfer the dinitrogen. FIG. 4 represents another embodiment of the monitoring device, in which the additional compression of the diluted gas can be carried out directly in the intermediate enclosure. The elements similar or identical to those of FIG. 1 carry a reference numeral increased by 100 with respect to FIG. 1. In the embodiment of FIG. 4, the measurement chamber 121 is adjacent to one end of the intermediate housing 112 and a piston 120 is mounted in a sealed manner in the intermediate chamber 112 to push the diluted gas contained in the intermediate chamber 112 to the measuring chamber 121. The left view shows the piston 120 at the beginning of the compression step and the right view shows the piston 120 at the end of the compression step. For the rest, the operation is similar to the monitoring device of Fig. 1. There are different ways to cause the aspiration of the sample to be analyzed through the sampling line. In the embodiment of FIG. 3, a suction device with a Venturi effect, represented in an enlarged manner in FIG. 4, is used which makes it possible simultaneously to draw a quantity of the gas phase into the insulating barrier. and diluting this sample in an amount of inert gas. The elements similar or identical to those of FIG. 1 carry an increased reference numeral of 200 with respect to FIG. 1. The Venturi suction device 220 comprises a main pipe 35 having a convergent-divergent geometry and having a the inlet side connected by the connecting line 218 to the pressure nitrogen tank 215 and an outlet side connected by the connecting line 224 to the measuring chamber 221. An isolation valve 216 is provided on the link 218 for controlling the distribution of nitrogen from the tank 215. A sensor system 217 is provided for measuring the amount of nitrogen introduced from the pressurized nitrogen container 215 in the main line 35. An isolation valve 223 is provided. on the connecting line 224 to be able to close the measuring chamber 221 during the duration of the measurement by the gas analyzer 225. The operation is as follows: When the valves 216 and 223 are open, a stream of pressurized dinitrogen enters the inlet-side of the convergent-divergent, as indicated by the arrows 37, and causes by the Venturi effect a vacuum in the lateral line 36 of the suction device. Venturi 220 which is connected to the sampling pipe 211. It follows the suction of a quantity of the gas phase contained in the insulating barrier 203, as indicated by the arrow 38. The gas phase flow sucked and the flow of dinitrogen are mixed in the outlet side of the convergent-divergent, as indicated by the arrows 39 and flow to the measuring chamber 221 through the connecting line 224.
[0016] The diluted gas sample obtained in the measurement chamber 221 is then analyzed in the same manner as previously described. Preferably, a not shown valve is also provided on the sampling line 211 which is opened only after establishing a stable flow of nitrogen at an appropriate speed in the main pipe 35. This avoids reflux of the dinitrogen in the direction of the insulating barrier 203 during the start-up phase of the dinitrogen stream. In the same way, it is possible to close this valve at the end of the sampling before interrupting the flow of dinitrogen. The Venturi suction device 220 of FIG. 4 may also be used in conjunction with an intermediate enclosure located upstream of the lateral pipe 36. In a corresponding embodiment, not shown, the monitoring device 210 of FIG. is connected to the intermediate chamber 12 of FIG. 1, so that the lateral duct 36 of the Venturi suction device 220 takes the place of the connecting pipe 24 of FIG. 1. The function of the pump 20 can then be performed by the Venturi suction device 220 which replaces the pump 20, and which further performs the dilution of the sample in the dinitrogen. Consequently, a prior addition of dinitrogen in the intermediate chamber 12 is not essential in this case and the tank 15 of the figurel can be optionally removed. The embodiments described above provide an addition of dinitrogen in the gas phase sample taken from the insulating barrier. Alternatively, a supply of dinitrogen may be made in the insulating barrier before taking the sample to be analyzed. A corresponding embodiment will now be described with reference to FIGS. 5 and 6. The elements similar or identical to those of FIG. 1 carry an increased reference number of 300 with respect to FIG. 1. FIG. 5 highlights a tank 301 with a double sealing membrane, in which a secondary sealing membrane 40 separates the insulating barrier into a primary insulating barrier disposed in a primary insulation space 41 located between the primary membrane 304 and the secondary membrane 40 and a secondary insulating barrier disposed in a secondary insulation space 42 located between the secondary membrane 40 and the carrier walls 302. First, a monitoring device 310 is disclosed for monitoring the composition of the gas phase in the primary space 41. sampling duct 311 opens on one side into the primary space 41 and on the other side into a gas manifold 4 6 and carries an isolation valve 45. The gas manifold 46 is connected to the suction side of a vacuum pump 320 which thus makes it possible to draw a sample of the gas phase present in the primary space 41 when the valve 45 is open. The discharge side of the vacuum pump 320 is connected by the connecting pipe 324 provided with a valve 323 to the measurement chamber 321 equipped with the gas analyzer 325. The valve 323 makes it possible to close the enclosure of measure 321 after taking the sample to be analyzed and for the duration of the measurement.
[0017] A bypass line 47 provided with a valve 48 branches on the connecting pipe 324 upstream of the valve 323 and makes it possible to direct the flow of gas discharged by the pump 320 to other installations than the measurement chamber. 321, especially to a degassing mast opening into the ambient atmosphere or any other evacuation system, possibly through a system of reprocessing gases to avoid pollution. This arrangement makes it possible in particular to purge and evacuate the entire gas sampling circuit before each sample taking, in order to make the sampling and analysis operation both more accurate and faster. This arrangement can be provided in the same manner in the other embodiments described above. An evacuation pipe 49 provided with a valve 50 may also be provided for connecting the measuring chamber 321 to the degassing mast or other evacuation system. This arrangement makes it possible to release the gas sample after analysis without mobilizing the bypass line 47. It also makes it possible to carry out a gas sweep through the measuring chamber 321, for example with an inert gas in order to avoid the accumulation of traces of gas likely to distort the successive analyzes. The monitoring device 310 may be used in the following manner: Assuming that the gas sampling circuit has been initially purged and that the valves 48 and 50 have been closed, the first step is to activate the pump 320, unless it operates continuously, and open the valve 45 and the valve 323 to cause suction of a quantity of the gaseous phase of the primary space 41 in the measurement chamber 321. When the pressure in the measuring chamber 321 reaches a value compatible with the operation of the gas analyzer 325, the valve 323 is closed and the analysis of the sample gas is carried out as described above. After the analysis, the measuring chamber 321 is purged by evacuating. The analysis equipment 51 comprising the vacuum pump 320, the gas analyzer 325, the measurement chamber 321 and its auxiliary circuits can be embodied in the form of a portable mobile device. The gas manifold 46 enables the analysis equipment 51 to be pooled for several sampling lines opening into different zones of the primary space 41 and possibly of the secondary space 42. FIG. 5 thus shows two sampling lines leading to different zones of the primary space 41. The sample collection can thus be carried out successively in the different zones by sequentially opening the various valves 45. The rise in pressure in the measurement chamber 321 can be very slow depending on the power of the the vacuum pump 320 and the gas pressure in the insulating barrier 3. To limit the duration of the sampling and analysis process, it is possible to manage the pressure in the primary space 41 so as to temporarily increase the pressure whenever a sample to be analyzed is to be taken. For this purpose, FIG. 5 shows an injection device comprising a pressurized nitrogen container 315, a primary injection line 55 provided with a valve 56 and connecting the dinitrogen reservoir 315 to the primary space 41 and a control duct. secondary injection 57 provided with a valve 58 and connecting the dinitrogen reservoir 315 to the secondary space 42. The valve 56 can be controlled to regulate the pressure in the primary space as illustrated in FIG. 6. Figure 6 shows the gas pressure 65 in the primary space as a function of time during a sampling cycle of a sample to be analyzed. Outside the sampling period, the pressure is maintained at a low pressure P1, for example of the order of 0.1 to 1 kPa, in order to maximize the thermal insulation. The means used to maintain this low pressure may be a system not shown completely independent of the monitoring device 25 described here. For example, they are vacuum pumps regulated by a PLC with a pressure setpoint and able to start the pumps when this instruction is crossed from the top and to stop the pumps when this instruction is crossed from below, from preferably with hysteresis to improve the stability of the assembly. In one embodiment, this low pressure maintenance may instead be a second function of the vacuum pump 320, in order to save material.
[0018] A few moments before the effective sampling of the sample, the sampling cycle is started at time t0 by deactivating the means used to maintain the low pressure, which causes a first rise in pressure, relatively slow, because of leaks of the primary space 41, during the duration 60. At time t1, the valve 56 is opened to cause an injection of gaseous dinitrogen in the primary space 41. This injection is carried out until obtaining a high pressure P2 at time t2. The valve 56 is then closed. Then a waiting time 61 is provided until time t3 for the gas phase is homogenized sufficiently by natural diffusion. The pressure P2 is a negative relative pressure less than P1, for example of the order of 0.5 to 10 kPa. The higher the pressure P2, the higher the energy expenditure necessary to restore the primary space 41 to the pressure P1 will be high.
[0019] At time t3, the vacuum pump 30 is activated and the valve 45 and the valve 323 are opened to cause suction of a quantity of the gaseous phase of the primary space 41 in the measurement chamber 321 during a sampling phase 62. The pressure in the primary space 41 then begins to decrease. At time t4, the valve 323 is closed and the pressurizing means are reactivated to lower the pressure in the primary space 41 to the pressure value P1 and keep it there until the next cycle. sample. This sampling cycle can be reduced to a total duration of a few minutes. By precisely measuring the pressure and the temperature in the primary space 41 by means of the sensor system 317, it is possible to accurately measure the dilution ratio caused by the addition of nitrogen in the primary space 41, and therefore of calculate a posteriori the concentration of gas before dilution. The data processing system 330 is used for this. The temperature measurement in the tank can be performed by a fiber optic system or the like. The monitoring of the secondary space 42 can be carried out in the same way with means similar to those described with reference to the primary space 41. For this purpose, a device for monitoring the secondary space can be realized independently of the device. As a variant, certain means can be shared for the surveillance of the two spaces 41 and 42. For example, in an embodiment not shown, the equipment of FIG. analysis 51 can be shared by connecting the sampling pipe 69 provided with the valve 68 to the collector 46. In a not shown embodiment, the measurement chamber 321 of the monitoring device 310 can be made in a manner similar to the enclosure intermediate 112 of Figure 2, so as to perform a rise in pressure of the gas in the measuring chamber 321 before analysis. An additional addition of dinitrogen in the measurement chamber 321 is possible but is not required, so that line 118 of Figure 2 may be omitted in this embodiment. This measuring chamber incorporating the compression means can be used in combination with the vacuum pump 320 or preferably without a vacuum pump at all, which reduces the cost of the monitoring device.
[0020] In one embodiment, all or part of the monitoring device, in particular the vacuum pump 320, is disposed inside a double transverse partition called cofferdam separating two tanks of a LNG tanker. This arrangement facilitates the pooling of the pump with several sampling points located at different locations of one or both tanks. In one embodiment, there are eight collection points per tank, preferably connected to the same collection manifold. Although the above description refers only to dinitrogen and methane, other pairs of fuel gas and inert gas may be employed in a similar manner. The gas used to dilute the gaseous phase taken must be chosen so as to avoid any dangerous chemical reaction, especially explosive, and to avoid disturbing the concentration measurement of the desired chemical species. The techniques described above for making an isolation space monitoring device can be used in different types of tanks, for example to monitor the primary space and / or the secondary space of an LNG tank in a terrestrial installation. or in a floating structure such as a LNG tanker or other.
[0021] Referring to Figure 10, 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 a cargo of LNG from or to the tank 71. Figure 10 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 comprising a movable arm 74 and a tower 78 which supports the movable arm 74. The movable arm 74 carries a bundle of insulated flexible pipes 79 which 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 fitted to the shore installation 77 and / or pumps fitted to the loading and unloading station 75 are used.
[0022] Although the invention has been described in connection with several particular embodiments, it is obvious that it is not limited thereto and that it comprises all the technical equivalents of the means described and their combinations if they are within the scope of the invention.
[0023] 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 "a" or "an" for an element or a step does not exclude, unless otherwise stated, the presence of a plurality of such elements or steps.
[0024] In the claims, any reference sign in parentheses can not be interpreted as a limitation of the claim.

权利要求:
Claims (23)
[0001]
REVENDICATIONS1. A method of monitoring a sealed and thermally insulating vessel (1, 201, 301) for containing a low temperature liquefied fuel gas, wherein a vessel wall comprises a multilayer structure mounted on a carrier wall, the multilayer structure comprising a sealing membrane in contact with the liquefied fuel gas contained in the vessel and a thermally insulating barrier (3, 203, 41, 42) disposed between the sealing membrane and the carrier wall, the thermally insulating barrier comprising solids and a gas phase maintained at a negative relative pressure, the method comprising: obtaining a diluted gas sample by taking a sample of the gas phase at the negative relative pressure in the thermally insulating barrier through a sampling line (11); , 111, 211, 311, 69) opening out of the tank wall and adding a qua a controlled quantity of inert gas in the gaseous phase to be withdrawn or taken, raising the pressure of the diluted gas sample to an operating pressure of a gas analyzer (25, 125, 225, 325), and measuring a concentration of the fuel gas in the gas sample diluted with the gas analyzer.
[0002]
2. The method of claim 1, further comprising: determining a concentration of the fuel gas in the gas phase of the thermally insulating barrier as a function of the measured concentration and the amount of inert gas added to the gas phase. 25
[0003]
3. Method according to one of claims 1 to 2, wherein the fuel gas is composed of methane.
[0004]
4. Process according to one of claims 1 to 3, wherein the inert gas is selected from the group consisting of dinitrogen, helium, argon and mixtures thereof. 30
[0005]
5. Method according to one of claims 1 to 4, wherein the negative relative pressure corresponds to an absolute pressure of less than 10 kPa, preferably less than 1 kPa.
[0006]
6. Method according to one of claims 1 to 5, wherein the operating pressure of the gas analyzer (25, 125, 225, 325) is between 80kPa and 120kPa, preferably between 86 kPa and 108 kPa.
[0007]
The method according to one of claims 1 to 6, wherein the gas analyzer comprises a combustible gas detector selected from the group consisting of catalytic wire detectors, infrared detectors and electrochemical cell detectors.
[0008]
The method according to one of claims 1 to 7, wherein the step of obtaining the diluted gas sample comprises: adding a controlled amount of inert gas to the gas phase in the thermally insulating barrier to increase the relative pressure (65) of the gaseous phase in the thermally insulating barrier from a first negative value (P1) to a second negative value (P2), and taking a sample of the gaseous phase under the relative pressure equal to the second negative value in the thermally insulating barrier through the sampling line (11, 111, 211, 311, 69) opening out of the vessel wall to obtain the diluted gas sample, and decreasing the relative pressure (65) of the gas phase in the thermally insulating barrier from the second negative value to the first negative value after taking the sample from the gas phase.
[0009]
9. The method of claim 8, wherein the first negative value is less than 1 kPa, preferably less than or equal to 0.1 kPa, and the second negative value is greater than or equal to 1 kPa.
[0010]
The method of claim 8 or 9, wherein the step of compressing the diluted gas sample comprises: storing the gas phase sample taken from an intermediate chamber (112, 321) connected to the sampling line, and moving a movable wall in the intermediate enclosure to confine the diluted gas sample in a measuring chamber (121) of smaller capacity than the intermediate enclosure.
[0011]
11. The method according to one of claims 1 to 10, wherein the step of obtaining the sample of diluted gas comprises: taking a sample of the gas phase under the negative relative pressure in the thermally insulating barrier through the pipeline of sampling opening outside the vessel wall, and add a controlled amount of inert gas to the sample gas phase taken.
[0012]
The method according to claim 11, wherein the steps of sampling, diluting and compressing the sample are performed by means of a Venturi suction device (220), the Venturi suction device comprising: main pipe (35) having an inlet connected to a source of the pressurized inert gas and an outlet connected to a measuring chamber or an intermediate chamber, and a suction pipe (36) having an upstream side connected to the pipe and a downstream side opening laterally into a convergent-diverging main pipe so that a stream of inert gas in the main pipe produces a vacuum in the suction pipe.
[0013]
The method of claim 11 or 12, wherein the step of collecting the sample comprises: pumping the gas phase sample through the sampling line (11, 111, 211, 311) to an intermediate chamber (12). , 112, 221, 321), and isolating the intermediate enclosure from the thermally insulating barrier.
[0014]
The process according to claim 13, wherein the controlled amount of inert gas is added to the intermediate chamber (12, 112), the step of compressing the diluted gas sample comprising: pumping the diluted gas sample from the intermediate chamber to a measurement chamber (21, 121) coupled to the gas analyzer.
[0015]
The method of claim 13, wherein the steps of diluting and compressing the sample are performed by means of a Venturi suction device (220), the Venturi suction device comprising: a conduit main device (35) having an input connected to a source of the inert gas under pressure and an output connected to a measuring chamber, and a suction line (36) having an upstream side connected to the intermediate chamber and a downstream side opening laterally in a convergent-divergent main pipe so that a flow of inert gas in the main pipe produces a vacuum in the suction pipe.
[0016]
16. A monitoring device (10, 210, 310, 410) suitable for a sealed and thermally insulating tank (1, 201, 301) for containing a low temperature liquefied gas, wherein a wall of the tank comprises a multilayer structure mounted on a carrier wall, the multilayer structure comprising a sealing membrane in contact with the liquefied fuel gas contained in the tank and a thermally insulating barrier (3, 203, 41, 42) disposed between the waterproofing membrane and the carrier wall, the thermally insulating barrier comprising insulating solids and a gaseous phase maintained under a negative relative pressure, the monitoring device comprising: a sampling line (11, 111, 211, 311, 69) connecting the heat barrier insulation outside the tank wall, a measuring chamber (21, 121, 221, 321) directly or indirectly connected to the pre-pipe by means of an isolation valve (14, 22, 23, 223, 323, 45), a gas analyzer (25, 125, 225, 325) coupled to the measuring chamber for measuring a concentration fuel gas in the measurement chamber, a pumping device (20, 112, 220, 320) connected to the sampling line and able to take a sample of the gas phase under the negative relative pressure in a thermally insulating barrier and transferring the gas phase sample to the measuring chamber (21, 121, 221, 321), an inert gas tank (15, 215, 315) arranged to add a quantity of inert gas to the gas phase taken or taken, and a measuring device (17, 217, 317) for measuring the amount of inert gas added to the gas phase.
[0017]
17. Apparatus according to claim 16, further comprising a data processing system (30, 330) capable of determining a concentration of the fuel gas in the gaseous phase of the thermally insulating barrier as a function of the concentration measured by the analyzer. of gas and the amount of inert gas added to the gas phase.
[0018]
18. Device according to one of claims 16 to 17, wherein the pumping device comprises a vacuum pump (20, 320).
[0019]
19. Device according to one of claims 16 to 18, wherein the pumping device comprises a Venturi suction device (220), the Venturi suction device comprising: a main pipe (35) having a inlet connected to the inert gas tank 5 and an outlet connected to the measuring chamber, and a suction line (36) having an upstream side connected directly or indirectly to the sampling line and a downstream side opening laterally in a convergent divide the main pipe so that a flow of inert gas in the main pipe produces a vacuum in the suction pipe.
[0020]
20. A sealed and thermally insulating vessel (71) for containing a liquefied fuel gas at low temperature and equipped with a monitoring device (10, 210, 310, 410) according to one of claims 16 to 19, wherein a The wall of the vessel comprises a multilayer structure mounted on a carrier wall (302), the multilayer structure comprising a primary sealing membrane (304) in contact with the liquefied fuel gas contained in the vessel, a secondary sealing membrane ( 40) disposed between the primary sealing membrane and the carrier wall, a primary heat-insulating barrier (41) disposed between the primary sealing membrane and the secondary sealing membrane, and a secondary heat-insulating barrier (42) disposed therein between the secondary waterproofing membrane and the carrier wall, and wherein one or each thermally insulating barrier comprises insulating solids and a gaseous phase maintained under a negative relative pressure, the monitoring device comprising a first sampling line (311) opening into the primary thermally insulating barrier and a second sampling line (69) opening into the secondary thermally insulating barrier.
[0021]
21. Ship (70) for the transport of a cold liquid product, the ship having a double hull (72) and a tank (71) according to claim 20 disposed in the double hull.
[0022]
A method of loading or unloading a vessel (70) according to claim 21, wherein a cold liquid product is conveyed through insulated pipes (73, 79, 76, 81) to or from a floating storage facility or earth (77) to or from the vessel (71).
[0023]
23. Transfer system for a cold liquid product, the system comprising a ship (70) according to claim 21, insulated pipes (73, 79, 76, 81) arranged to connect the tank (71) installed in the hull. the vessel to 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 vessel.

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同族专利:

公开号 | 公开日

JP6487440B2|2019-03-20|

AU2014356483B2|2018-07-12|

KR20160091933A|2016-08-03|

SG11201604225UA|2016-07-28|

RU2667596C1|2018-09-21|

PH12016500981A1|2016-06-20|

EP3074744A1|2016-10-05|

ES2759496T3|2020-05-11|

CN105829855A|2016-08-03|

CN105829855B|2019-09-17|

AU2014356483A1|2016-06-23|

FR3014197B1|2017-11-17|

WO2015078972A1|2015-06-04|

KR102358359B1|2022-02-04|

JP2017508950A|2017-03-30|

EP3074744B1|2019-10-23|

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法律状态:
2015-10-09| RM| Correction of a material error|Effective date: 20150908 |

2015-11-27| CJ| Change in legal form|Effective date: 20151022 |

2015-11-30| PLFP| Fee payment|Year of fee payment: 3 |

2016-11-30| PLFP| Fee payment|Year of fee payment: 4 |

2017-11-30| PLFP| Fee payment|Year of fee payment: 5 |

2019-11-29| PLFP| Fee payment|Year of fee payment: 7 |

2020-11-30| PLFP| Fee payment|Year of fee payment: 8 |

2021-11-30| PLFP| Fee payment|Year of fee payment: 9 |

优先权:

申请号 | 申请日 | 专利标题

FR1361899A|FR3014197B1|2013-11-29|2013-11-29|MONITORING A SEALED AND THERMALLY INSULATING TANK|FR1361899A| FR3014197B1|2013-11-29|2013-11-29|MONITORING A SEALED AND THERMALLY INSULATING TANK|

EP14802918.4A| EP3074744B1|2013-11-29|2014-11-27|Monitoring of a sealed and thermally insulated vat|

AU2014356483A| AU2014356483B2|2013-11-29|2014-11-27|Monitoring of a sealed and thermally insulated vat|

CN201480064815.4A| CN105829855B|2013-11-29|2014-11-27|A kind of detection method and device of sealing and thermally insulated tank|

KR1020167016356A| KR102358359B1|2013-11-29|2014-11-27|Monitoring of a sealed and thermally insulated vat|

JP2016535000A| JP6487440B2|2013-11-29|2014-11-27|Sealed insulation tank monitoring|

ES14802918T| ES2759496T3|2013-11-29|2014-11-27|Supervision of a watertight and thermally insulating tank|

PCT/EP2014/075822| WO2015078972A1|2013-11-29|2014-11-27|Monitoring of a sealed and thermally insulated vat|

RU2016120685A| RU2667596C1|2013-11-29|2014-11-27|Monitoring of sealed and thermally insulated vat|

PH12016500981A| PH12016500981A1|2013-11-29|2016-05-26|Monitoring of a sealed and thermally insulated vat|

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