JP4444084B2 - Gas hydrate pellet transfer device and transfer method - Google Patents

Description

  The present invention relates to an apparatus and method for transferring a slurry after pelletizing a gas hydrate such as natural gas.

  Conventionally, taking natural gas as an example, when transporting from a production area with a natural gas field (natural gas mining area) to a consumption area, when transporting distance is short, it is transported by pipeline, and when transporting distance is long A method of transporting natural gas as LNG (Liquefied Natural Gas) at an extremely low temperature (minus 162 ° C.) by an LNG ship is generally performed.

  However, when natural gas is transported as ultra-low temperature LNG, it requires a large initial investment in its liquefaction facilities, transport facilities, and regasification facilities, so there is currently only a very large natural gas field. Since it is not targeted for development, a large number of small and medium-sized natural gas fields remain undeveloped around the world.

  On the other hand, in recent years, the self-preservation effect of gas hydrates such as natural gas (in the following explanation, Natural Gas Hydrate: “NGH”) has been announced. As a technology that has the potential to develop medium- and small-scale natural gas fields, which are considered difficult to develop in terms of equipment profitability, LNG has been attracting attention.

This NGH has a crystal structure in which gas molecules are contained one by one in a cage made of water molecules. For example, in pure methane hydrate, gas molecules that enter the water molecule cage in view of the occupancy usually component in methane hydrate 1 m ³ of the solid it is said to methane of about 150 meters ³ and water 0.79 m ^3. Further, it is said that this NGH is stabilized at minus 80 ° C. under atmospheric pressure.

In addition, 1m ³ of LNG includes natural gas equivalent to about 600m ³ , but in the case of NGH, it is solid, so it varies depending on the cargo filling rate, but it becomes 1/4 to 1/6 of LNG with 1m ³ of NGH cargo. Natural gas is included, and the specific gravity is about 0.42 to 0.47 for LNG, while the apparent specific gravity for NGH is about 0.62 to 0.90 (corresponding to a porosity of 30% to 0%). Value).

  Such a self-preserving effect of NGH is that even if the NGH melts at a temperature higher than minus 80 ° C., the surface water formed by the melting of the NGH freezes to become ice to insulate the NGH. According to the NGH phase diagram, this self-preserving effect suppresses the decomposition and dissociation of NGH even at sub-zero temperatures under normal pressure, for example, about minus 20 ° C. .

  Therefore, in the case of NGH, since ultra-low temperature equipment like LNG is not required, it is possible to greatly reduce the cost in terms of equipment, and as described above, there is a possibility of developing a small and medium-sized natural gas field, In recent years, it has attracted attention.

  As a conventional technology of this type, natural gas transportation in which gas hydrate is stored in a transport container at the loading site, loaded and transported on a transport ship while maintaining the temperature of the transport container, and the transport container is unloaded at the loading site. There is a method (for example, refer to Patent Document 1).

  In addition, as another conventional technique, there is a technique in which gas hydrate is formed into a pellet and is mechanically transported by a conveyor or the like (see, for example, Patent Document 2).

  Furthermore, as another prior art, there is one in which a pellet-like gas hydrate is tried to be conveyed by a pressurized gas supplied from a pressure tank (see, for example, Patent Document 3).

In addition, as another conventional technique, there is a technique in which pellet-like gas hydrate pellets are mixed with a slurry mother liquor and transferred into a slurry (see, for example, Patent Document 4).
JP 2003-343798 A (page 4, FIG. 2) Japanese Patent Laying-Open No. 2003-170892 (page 4, FIG. 2) Japanese Patent Laying-Open No. 2003-170891 (page 4-5, FIG. 2) JP 2003-171678 A (page 4, FIG. 1)

  By the way, although the weight per unit volume of NGH is about 1.4 to 2.0 times that of LNG, depending on the cargo filling rate, natural gas equivalent to LNG transport ships is converted to NGH and transported. If it tries to do so, the NGH transport ship will inevitably have a larger volume than the LNG transport ship, and the required draft will increase due to the increase in weight, making it difficult to touch the existing quay. Moreover, in the case of NGH, since it cannot be transported from offshore by pipeline like liquid cargo, it is difficult to transport when transporting by transport ship.

  In addition, as shown in the schematic diagram of the configuration showing the application example for transferring the gas hydrate pellets in FIG. 12, the NGH production facility 101 provided in the production area where the natural gas field 100 is located is used as a loading area, and the consumption of the natural gas is performed. When the regasification facility 102 provided on the ground is used as a loading site, for example, the distance between the natural gas field 100 and the NGH manufacturing facility 101 at the loading site, or the NGH manufacturing apparatus 103 of the NGH manufacturing facility 101 When the distance L1 from the NGH storage tank 104 for storing the produced NGH pellets to the NGH storage tank 106 of the NGH transport ship 105 is large, and regasification is performed from the NGH storage tank 106 of the NGH transport ship 105 at the landing site. If the distance L2 from the facility 102 to the NGH storage tank 107 is long, the Distance L1, L2 or the like may become a long distance number km in some cases from a short, it is difficult transfer of NGH between the transfer distance. In other words, the distance at which NGH pellets must be transferred varies greatly depending on the state of the sea area, equipment conditions, etc., at both the loading and unloading sites, and it is difficult to stably transfer NGH between the transfer distances. .

  In addition, in the said patent document 1, when the loading facility provided with the large crane which can handle a transport container and a unloading facility are needed, and a transfer distance becomes long, a transport container is made to a crane position, or A separate transport means for transporting to the frozen storage facility is required, resulting in a significant increase in equipment costs. Moreover, since combustible NGH is handled for every container, a lot of time is required for work.

  In Patent Document 2, since natural gas is generated when NGH is decomposed, in order to suppress this decomposition and prevent diffusion of the generated gas, a sealed structure that keeps the entire machine transport device at minus several tens of degrees Celsius It is difficult to do so, and when the transfer distance becomes long, the apparatus becomes large. In the case of machine transportation, the equipment is complicated by the cargo collection, distribution, and route changing unit.

  Further, when trying to carry gas as in Patent Document 3, a gas velocity that can carry a conveyed product with gas kinetic energy is required, so the gas velocity in the pipe is set to a gas velocity of several tens of m / s. The size of the NGH pellet is restricted in order to suppress it to be several times the final speed (floating speed) of the conveyed product. Moreover, in order to carry NGH pellets by gas, a gas of minus several tens of degrees Celsius must be supplied, and the final speed increases as the diameter of the conveyed product increases, so it is as large as NGH pellets with a diameter of several centimeters. It is difficult to convey a solid object by gas.

  Moreover, in the said patent document 4, although the method of dropping and pelletizing a pellet from a tank in piping downstream of a pump is shown, in this structure, when the transfer distance of NGH pellet is long as mentioned above, Since the back pressure due to the resistance in the transportation pipeline acts on the outlet side of the tank, it becomes difficult to make a slurry by dropping, and long-distance transportation of NGH pellets becomes difficult.

  Then, an object of this invention is to provide the apparatus and method which can transfer a NGH pellet stably.

To achieve the above object, the gas hydrate pellets transfer device of the present invention has a gas hydrate by mixing the slurry medium cooled to a predetermined temperature in the gas hydrate pellets pelletized allowing slurry transport Gasuhaido A slurry pump for transferring the rate pellet slurry, a plurality of extrusion pipes for transferring the gas hydrate pellet slurry, and a high pressure gas cooled to a temperature for maintaining the gas hydrate in a stable state in the plurality of extrusion pipes, respectively. An operation of transferring a gas hydrate pellet slurry to a plurality of extrusion pipes by the slurry pump, and an operation of pressing a high pressure gas into the gas hydrate pellet slurry in the plurality of extrusion pipes by the compressor Between the gas hydrate pellet slurry. It may be configured to discharge the incoming high pressure gas from the extruded tube alternately at a predetermined position. In this way, the gas hydrate pellet slurry transferred by a plurality of extruded pipes can be transported over a long distance by reducing the pipe frictional resistance per unit length of the pipe length by the high-pressure gas. , a forced at a pressure of the high pressure gas can be long-distance transport.

  Further, in this gas hydrate pellet transfer device, the gas hydrate is injected into the gas hydrate pellet slurry in the pipe line after the high pressure gas press-fitted between the gas hydrate pellet slurry is discharged from the extrusion pipe at a predetermined position. If the high-pressure gas cooled to a temperature that maintains a stable state is mixed and the gas hydrate pellet slurry is configured to be transferred to the pipeline, the high-pressure gas reduces the frictional resistance per unit length of the pipeline. Further long-distance transfer can be achieved.

  Furthermore, a slurry pump for transferring a gas hydrate pellet slurry, which is made to be able to transfer a slurry by mixing a slurry medium cooled to a predetermined temperature with a gas hydrate pellet obtained by pelletizing the gas hydrate, and the gas hydrate pellet slurry A plurality of extruding pipes, and a pump for respectively injecting a high pressure liquid cooled to a temperature that keeps the gas hydrate in a stable state into the plurality of extruding pipes. The operation of transferring the rate pellet slurry and the operation of pressing the high pressure liquid into the gas hydrate pellet slurry in the plurality of extrusion pipes by the pump alternately at predetermined intervals, and the high pressure press-fitted between the gas hydrate pellet slurry. Constructed to discharge liquid from the extrusion tube alternately at a specified position It may be. In this way, the gas hydrate pellet slurry can be continuously forcedly transferred with a high-pressure liquid.

  Further, in this gas hydrate pellet transfer apparatus, if the extrusion tube is composed of at least three, the gas hydrate pellet slurry can be continuously forcedly transferred with an incompressible high-pressure liquid.

In addition, in these gas hydrate pellet transfer devices, the gas hydrate storage tank for storing the gas hydrate pellets in a stable state, and the slurry medium cooled to a temperature for keeping the gas hydrate in a stable state are stored. A slurry medium supply pump for supplying to the tank, and a plurality of the slurry medium is discharged radially from the upper part of the supply port to the supply port provided at the lower part of the gas hydrate storage tank. a mixing nozzle, an auxiliary Roh nozzle you release the slurry medium toward the discharge direction of the gas hydrate pellets supplied from the supply port, a mixer equipped with a provided to the gas hydrate pellets in the mixer If the slurry medium is mixed to form a slurry, the slurry is supplied at the supply port of the gas hydrate storage tank. Since the Lee medium is discharged and mixed, gas hydrate pellets can be stably slurried at the gas hydrate pellet outlet of the gas hydrate storage tank and transferred to the pipeline. It can be carried out stably from slurrying to long distance transfer.

  Furthermore, a separator that separates the gas hydrate pellet slurry into gas hydrate pellets and a slurry medium, a gas hydrate storage tank that stably stores the gas hydrate pellets separated by the separator, and the separation If a slurry medium tank for storing the slurry medium is provided and the separator is configured to separate the gas hydrate pellet slurry that has been pipeline-transferred by any of the gas hydrate pellet transfer devices, the gas hydrate pellets After the slurry is transferred to a slurry, the gas hydrate pellet slurry can be separated into gas hydrate pellets and a slurry medium and stored.

  Further, in this gas hydrate pellet transfer device, a pipeline for reusing the slurry medium stored in the slurry medium tank as a slurry medium to be mixed when slurrying the gas hydrate pellets and a slurry medium transfer pump are provided. If provided, the slurry medium can be effectively used in a closed circuit.

On the other hand, gas hydrate pellets transportation method of the present invention, gas hydrate pellets of gas hydrate pellets in a mixture of slurry medium is cooled to a predetermined temperature the slurry transportable in gas hydrate pellets slurry multiple The operation of transferring to the extrusion pipe and the operation of injecting the high-pressure gas cooled to a temperature that keeps the gas hydrate in a stable state into the gas hydrate pellet slurry in the plurality of extrusion pipes are performed alternately. the gas hydrate pellets slurry was transferred by a plurality of extruded tube at a pressure, and to discharge alternately from extruded tube high-pressure gas that is press-fitted between the gas hydrate pellets slurry at a predetermined position.

  Furthermore, in this gas hydrate pellet transfer method, the gas hydrate is injected into the gas hydrate pellet slurry in the pipeline after the high-pressure gas press-fitted between the gas hydrate pellet slurry is discharged from the extrusion pipe at a predetermined position. The gas hydrate pellet slurry may be transferred by mixing a high-pressure gas cooled to a temperature that maintains a stable state.

  Further, the gas hydrate pellets obtained by pelletizing the gas hydrate are mixed with a slurry medium cooled to a predetermined temperature to transfer the gas hydrate pellet slurry, which can be transferred to a plurality of extrusion pipes, and the plurality of extrusions. The gas hydrate pellet slurry in the gas hydrate pellet slurry in the tube is alternately injected with a high pressure liquid cooled to a temperature that keeps the gas hydrate in a stable state. The high-pressure liquid that has been transferred by the pressure and press-fitted between the gas hydrate pellet slurry may be alternately discharged from the extrusion tube at a predetermined position.

  According to the present invention, the gas hydrate pellets can be slurried and transferred in accordance with the transfer distance by means as described above, and the gas hydrate pellets can be stably transferred.

  Hereinafter, an embodiment of the present invention will be described with reference to the drawings. In the following embodiments, the NGH pellets are transferred from the NGH storage tank 104 of the NGH production facility 101 to the NGH storage tank 106 of the NGH transport ship 105 at the loading place shown on the left side of FIG. The present invention is applicable to both cases where NGH pellets are transferred from the NGH storage tank 106 of the NGH transport ship 105 to the NGH storage tank 107 of the regasification facility 102 at the loading site.

FIG. 1 is a configuration diagram showing a gas hydrate pellet transfer device according to a first reference example of the present invention, and FIG. 2 is a cross-sectional view in side view showing a mixer of the gas hydrate pellet transfer device shown in FIG. 3 is a sectional view of the gas hydrate storage tank on the loading side shown in FIG. The first reference example is an example in which an NGH pellet slurry is transferred by a slurry pump system.

  As shown in FIG. 1, an NGH storage tank 2 for storing pelletized NGH pellets 1 is provided on the left loading side. For example, the NGH storage tank 2 shown in FIG. NGH pellets 1 are stored. The NGH storage tank 2 is not particularly limited in terms of a tank system, a heat insulation system, or the like, and may be any structure that can stably store NGH pellets. Moreover, as the NGH pellet 1, it is formed in the particle size of about 5-50 mm, for example.

  A slurry medium tank 4 for supplying a slurry medium 3 to be mixed with the NGH pellets 1 stored in the NGH storage tank 2, a slurry medium supply pump 5 for supplying the slurry medium 3 from the slurry medium tank 4, and the slurry medium 3 And a cooler 6 that cools the NGH to a temperature that keeps the NGH in a stable state. These are connected by a slurry medium supply pipe 7, and the slurry medium supply pipe 7 is provided with an on-off valve 8. As the slurry medium 3, naphtha, aircraft kerosene, kerosene, etc. that maintain a liquid state around −20 ° C. are preferable, and light oil, dimethyl ether, or the like can also be used.

  The slurry medium 3 supplied from the slurry medium tank 4 is supplied from a shower 9 provided in the upper part of the NGH storage tank 2 and a mixer 10 provided in the lower part and mixed with the NGH pellets 1. Has been.

  A slurry pump 12 is provided in an NGH pellet slurry supply pipe 11 provided in the lower part of the NGH storage tank 2. The slurry pump 12 is a pump having a lift so that the NGH pellet slurry mixed in the mixer 10 of the NGH storage tank 2 can be transferred by a predetermined distance by the transport pipe 17.

  Moreover, since the gas space part of the tank upper part of these NGH storage tank 2 and the slurry medium tank 4 is filled with natural gas, in order to prevent these natural gas from being diffused in air | atmosphere at the time of cargo handling, A gas pipe 13 is provided to connect all the gas space portions above these tanks in a closed manner. The gas pipe 13 is provided with a compressor 14, a gas tank 15, and a cooler 16 for keeping the pressure of the gas space in the upper part of the tank constant at almost atmospheric pressure. Thus, if the pressure in the gas space at the upper part of the tank rises above a predetermined pressure, the gas in the gas pipe 13 is pumped by the compressor 14 and stored in the gas tank 15, and the pressure in the gas space at the upper part of the tank is increased. If the pressure falls below the predetermined pressure, the gas accumulated in the gas tank 15 is cooled to a predetermined temperature by the cooler 16 and then released into the gas pipe 13 to be kept at the predetermined pressure.

  As shown in FIG. 2, the mixer 10 provided in the NGH storage tank 2 is provided in the upper part of the supply port 18 provided in the lower end of the NGH storage tank 2, and the NGH in the lower part of the NGH storage tank 2. The slurry medium 3 is mixed with the pellet 1 (a part is shown in the figure). The mixer 10 includes an umbrella-like structure 20 supported by a support column 19, a plurality of mixing nozzles 21 provided radially from the lower part of the umbrella-like structure 20 outward in the radial direction, and the supply port. A plurality of auxiliary nozzles 22 provided downward toward 18 are provided. Further, the mixing nozzle 21 and the auxiliary nozzle 22 are connected to circular nozzle tubes 23 and 24 provided at the end portions of the slurry medium supply tube 7 rising along the support columns 19. .

  Further, an auxiliary nozzle 25 for injecting the slurry medium 3 from the slurry medium supply pipe 7 toward the NGH pellet slurry supply pipe 11 is provided at the position of the supply port 18 at the end of the slurry medium supply pipe 7. . By providing the auxiliary nozzle 25 and the auxiliary nozzle 22, the mixing and discharging of the NGH pellets 1 and the slurry medium 3 in the vicinity of the supply port 18 at the start of cargo handling are made more reliable.

  On the other hand, on the loading side on the right side, a separator 27 that separates the NGH pellet slurry 26 transferred from the NGH storage tank 2 into NGH pellets 1 and a slurry medium 3, and NGH pellets separated by the separator 27 NGH storage tank 28 storing 1 and slurry medium tank 29 storing slurry medium 3 are provided.

  The separator 27 separates the NGH pellet slurry 26 into the NGH pellets 1 and the slurry medium 3, and the NGH pellet slurry 26 fluidized by the slurry medium 3 passes over a separation network 30 having a predetermined opening. By doing so, the NGH pellets 1 are separated on the net and the slurry medium 3 is separated below the net. The separator 27 is not limited to such a configuration, and any separator that can separate the NGH pellet slurry 26 into the NGH pellet 1 and the slurry medium 3 may be used.

  The NGH storage tank 28 is connected to an input pipe 31 for supplying the NGH pellets 1 separated by the separator 27 at the top. In addition, a liquid return pipe 32 for returning the slurry medium 3 that has entered the tank together with the NGH pellets 1 is provided in the lower part.

  As shown in FIG. 3, the liquid return pipe 32 includes a liquid return inlet pipe 34 having a mesh-like film 33 on the lower surface, and a return rise pipe 35 through which the slurry medium 3 entering the liquid return inlet pipe 34 rises. It consists of and. The upper end of the return riser 35 is open in the tank, and the slurry medium 3 that has risen in the return riser 35 is moved to a predetermined position (a height position equal to or less than the maximum storage amount of NGH pellets). A return overflow pipe 36 for returning to the tank 29 is provided. In addition, when the capability of separating the NGH pellet 1 and the slurry medium 3 by the liquid return pipe 32 is sufficient, the separator 27 can be omitted.

In this reference example , a discharge pipe 37 is provided below the slurry medium tank 29 and is connected to the slurry medium tank 4 on the loading side. Through this discharge pipe 37, the slurry medium 3 separated on the loading side is sent to the loading-side slurry medium tank 4 by the slurry medium transfer pump 38 and circulated. The slurry medium 3 may be configured not to circulate. In addition, 39 is a connection part of each pipe | tube, and in the case of the application example shown in FIG. 12 mentioned above, it becomes a connection part between the NGH storage tank 104 of the NGH manufacturing equipment 101 and the NGH storage tank 106 of the NGH transport ship 105. .

In this reference example , the transfer lines for these NGH pellets 1 and slurry medium 3 are all configured in a closed manner.

  According to the gas hydrate pellet transfer device 40 configured as described above, when the NGH pellets 1 stored in the NGH storage tank 2 on the loading side are supplied from the NGH storage tank 2, Since the slurry medium 3 is reliably mixed by the provided mixer 10 to form an NGH pellet slurry 26 that can be transferred to the pipeline, the NGH pellet slurry 26 can be transferred to the pipeline according to the pump head by the slurry pump 12. is there.

  The transferred NGH pellet slurry 26 is separated into NGH pellet 1 and slurry medium 3 by a separator 27, the NGH pellet 1 is stored in an NGH storage tank 28, and the slurry medium 3 is transferred from the slurry medium tank 29 to the slurry medium. It is returned to the slurry medium tank 4 on the loading side by the transfer pump 38.

  In this way, the NGH pellets 1 can be stably transferred from the loading-side NGH storage tank 2 to the loading-side NGH storage tank 28.

  Moreover, since the pipes 11 and 17 (line) for transferring the NGH pellet slurry 26 and the pipes 7 and 37 (line) for the slurry medium all form a closed-type pipe line, the cooler 6 always reduces it to minus 20 ° C. The slurry can be transferred while keeping the NGH pellet 1 in a stable state with a small amount of the slurry medium 3 kept below.

In the case of the first reference example , the NGH storage tank 2 has only the function on the loading side, and the NGH storage tank 28 has only the function on the loading side, but these NGH storage tanks have both functions. If equipped, the NGH pellet slurry is loaded at the loading place as the NGH storage tank 106 of the NGH transport ship 105 as shown in FIG. 12 and the NGH pellet slurry is unloaded at the loading place in the same tank. Can do.

FIG. 4 is a configuration diagram showing a gas hydrate pellet transfer device according to a second reference example of the present invention, and FIG. 5 is a schematic diagram showing a pressure feeding portion in the gas hydrate pellet transfer device. The second reference example is an example in which the NGH pellet slurry is transferred by a mixed pressure feeding method. Since the configuration on the loading side is the same as that of the first reference example described above, the same reference numeral is given to the same configuration, and the detailed description thereof is omitted.

As shown in FIG. 4, in the second reference example , a high-pressure gas is mixed into the NGH pellet slurry 26 to be transferred on the downstream side of the slurry pump 12 in the first reference example described above. This is an embodiment in which the transfer distance of the NGH pellet slurry 26 is increased by reducing the duct friction resistance per unit. In this specification and claims, “high-pressure gas” is a gas compressed to a pressure capable of transferring the NGH pellet slurry 26 by a predetermined distance to the pipe. In response, it is compressed to a predetermined pressure.

  As a configuration for mixing the high-pressure gas, a gas pipe 41a is branched from the cooling gas pipe 13, and a compressor 42, a cooler 43, and a gas tank 44 are provided in the gas pipe 41a, and a compressor outlet is provided. The mixed-pressure inlet pipe 41 b through which the high-pressure gas on the side flows is connected to the transport pipe 17. As this high-pressure gas, natural gas or the like compressed to a pressure at which the NGH pellet slurry 26 can be transferred to the pipeline is used.

  As shown in FIG. 5, the connecting portion of the mixed pressure inlet pipe 41b with the transport pipe 17 is connected to the mixed pressure inlet pipe 41b at a predetermined acute angle toward the transfer direction R of the NGH pellet slurry 26. The NGH pellet slurry 26 is pushed out in the transfer direction R by the high-pressure gas 45 supplied from the mixed pressure inlet pipe 41b. At this time, by making the discharge force of the slurry pump 12 larger than the discharge force of the compressor 42, the NGH pellet slurry 26 can be discharged in the transfer direction R even if the high-pressure gas 45 is mixed. I am doing so.

In addition, since slurry flows in the pump of the slurry pump 12, it is difficult to make a multi-stage pump due to the pump structure if the pump is to be used with a long life. According to the second reference example , the high-pressure gas 45 is continuously mixed on the downstream side of the slurry pump 12 to form the plug flow of the NGH pellet slurry 26. Therefore, the frictional resistance is much smaller than that in the case of liquid contact in all the pipe lines, so even if a slurry pump having the same lift as that of the first reference example described above is used, it is longer than the first reference example. Distance transfer is possible.

Furthermore, in the case of this configuration, the NGH pellet 1 and the slurry 26 are transferred by the pressure of the high pressure gas 45 and the expansion force by which the high pressure gas 45 expands with 45a and 45b. Even if it is higher than one reference example, it can be transferred and the transfer efficiency can be increased.

According to the gas hydrate pellet transfer device 46 configured as described above, the pipe friction per unit length of the pipe length by the high-pressure gas mixed in the NGH pellet slurry 26 transferred by the slurry pump 12 as described above. Since the resistance can be reduced, a longer distance transfer is possible as compared with the gas hydrate pellet transfer apparatus 40 in the first reference example .

In the second reference example , each of the NGH storage tanks 2 and 28 may be provided with a loading side function and a loading side function. Further, since other functions and effects are the same as those of the first reference example described above, detailed description thereof is omitted.

FIG. 6 is a block diagram showing the gas hydrate pellet transfer apparatus according to the first embodiment of the present invention, and FIGS. 7A to 7D are basic views of the gas hydrate pellet transfer apparatus shown in FIG. FIG. 8A and FIG. 8B are explanatory views of an operation cycle by the gas hydrate pellet transfer apparatus shown in FIG. The first embodiment is an example in which a plurality of extruded pipes are provided, and NGH pellet slurry alternately filled in the extruded pipes is alternately transferred by the gas pressure method. Since the configuration on the loading side is the same as that of the first reference example described above, the same reference numeral is given to the same configuration, and the detailed description thereof is omitted.

As shown in FIG. 6, in the first embodiment, the NGH pellet slurry 26 to be transferred is alternately filled into a plurality of extruded tubes with high-pressure gas 45 on the downstream side of the slurry pump 12 in the second reference example described above. This is an embodiment in which the transfer distance of the NGH pellet slurry 26 is increased by the pressure of the high-pressure gas 45 by extrusion.

In the first embodiment, the high-pressure gas 45 is press-fitted in order to pump the NGH pellet slurry 26 almost continuously. The downstream line of the slurry pump 12 is made up of two branch supply pipes 47, 48, and these branch supply pipes 47, 48 are connected to the upstream sides of the two extrusion pipes 49, 50, respectively. These extrusion pipes 49 and 50 are for extruding the NGH pellet slurry 26 supplied from the slurry pump 12 with the pressure of the high-pressure gas 45, and a high-pressure gas supply pipe 51 is disposed upstream of the extrusion pipes 49 and 50. Is connected. The high-pressure gas supply pipe 51 is a pipe equivalent to the mixed-pressure inlet pipe 41b in the second reference example . Further, gas return pipes 52 and 53 are provided on the downstream side of the extrusion pipes 49 and 50, respectively, and the high pressure gas 45 press-fitted into the extrusion pipes 49 and 50 by the gas return pipes 52 and 53 is supplied to the NGH. It is connected so as to return to the storage tank 2.

  The branch supply pipes 47 and 48 have on-off valves 54 and 55, the gas return pipes 52 and 53 have on-off valves 56 and 57, and the push-out pipes 49 and 50 have upstream connection points of the branch supply pipes 47 and 48. Open / close valves 58 and 59 are provided on the side, and open / close valves 60 and 61 are provided downstream of the connection points of the gas return pipes 52 and 53, respectively. These on-off valves 54 to 61 are controlled to open and close by a control device (not shown). The high-pressure gas supply pipe 51 is provided with a compressor 42, a cooler 43, and a gas tank 44, and the downstream sides of the extrusion pipes 49 and 50 are connected to one transport pipe 17. These constitute the extruded tube device 62.

The basic principle of the pumping by the gas hydrate pellet transfer device 63 configured as described above will be described with reference to FIGS. In this description, only the extruded tube 49 will be described as an example. Moreover, although this 1st Embodiment is an example of the gas pumping using the high pressure gas 45, in these figures, since the liquid pumping in 3rd Embodiment mentioned later is made into an example, in each structure, it mentions 3rd mentioned later. Only the opening / closing timing of the on-off valve and the flow of the NGH pellet slurry 26 and the high-pressure liquid 67 will be described with reference to the embodiment.

  First, as shown in (a), the on-off valve 58 and the on-off valve 60 are closed, and the on-off valve 54 and the on-off valve 75 are opened. In this state, the slurry pump 12 supplies the NGH pellet slurry 26 to the extrusion pipe 49, whereby the slurry medium 3 in the extrusion pipe 49 is returned from the liquid return pipe 71 to the slurry medium tank 4, and the NGH pellets are put into the extrusion pipe 49. Slurry 26 is filled.

  Next, as shown in (b), when the NGH pellet slurry 26 is filled in the extruded tube 49, the on-off valve 54 and the on-off valve 75 are closed. The fact that the NGH pellet slurry 26 is filled in the extrusion tube 49 may be detected by the discharge amount of the slurry pump 12.

Next, as shown in (c), the on-off valve 60 and the on-off valve 58 are opened. As the opening timing, the opening / closing valve 60 is opened slightly earlier than the opening / closing valve 58. Thereby, the NGH pellet slurry 26 filled in the extrusion pipe 49 is extruded into the transport pipe 17 by the high-pressure liquid 67 (in the first embodiment, the high-pressure gas 45) supplied from the high-pressure pump 80. The amount of the high pressure liquid 67 supplied into the extrusion tube 49 may be detected by the discharge amount of the high pressure pump 80.

  Next, as shown in (d), when the NGH pellet slurry 26 is completely pushed out from the extrusion tube 49, the on-off valve 58 and the on-off valve 60 are closed. Thereby, the NGH pellet slurry transfer cycle per one extrusion tube 49 is completed. Thereafter, this cycle is repeated. In this way, the NGH pellet slurry 26 is pumped to the transport pipe 17 by the pressure of the high pressure liquid 67 extruded by the high pressure pump 80.

  According to the gas hydrate pellet transfer device 63 of FIG. 6 configured to pump the NGH pellet slurry 26 by such a basic principle, as shown in FIGS. 8 (a) and 8 (b), NGH The pellet slurry 26 can be transferred almost continuously with a high-pressure gas. In FIG. 8B, the horizontal direction is the time axis, the upper side shows the extruded tube 49, and the lower side shows the extruded tube 50. Since the basic principle is as shown in FIGS. 7 (a) to (d), the valve opening / closing timing will be mainly described below. In FIG. 8 (a), a configuration for storing NGH pellet slurry transfer gas having a total gas volume at the top of each tank is schematically shown as a tank 64.

  In the state shown in FIG. 8A, the slurry pump 12 supplies the NGH pellet slurry 26 from the NGH pellet slurry supply pipe 11 to the extrusion pipe 50 via the branch supply pipe 48 and the on-off valve 55, and the inside of the extrusion pipe 50. The gas 45 a is returned to the NGH storage tank 2 through the on-off valve 57 and the gas return pipe 53. At this time, even if the NGH pellet slurry 26 flows into the gas return pipe 53, it is returned to the NGH storage tank 2.

  On the other hand, the high-pressure gas 45 is simultaneously pressed into the extrusion pipe 49 from the compressor 42 through the high-pressure gas supply pipe 51 and the opening / closing valve 58, and the NGH pellet slurry 26 in the extrusion pipe 49 passes through the opening / closing valve 60. 17 extruded. In this state, the on-off valves 54, 56, 59, 61 are closed.

  As shown in FIG. 8B, the supply of the NGH pellet slurry 26 and the press-fitting of the high-pressure gas 45 into the two extruded tubes 49 and 50 are performed as follows. The on-off valves 58 and 60 are closed from the state in which the high-pressure gas 45 is being pressed into the extrusion pipe 49 shown on the upper side of the figure, and then the on-off valves 54 and 56 are opened. At this time, in the extrusion pipe 50 shown on the lower side, the on-off valves 55 and 57 supplying the NGH pellet slurry 26 are closed, and then the on-off valve 59 is opened while the on-off valve 61 is opened. As a result, the extrusion pipe 49 is switched from the press-fitting of the high-pressure gas 45 to the operation of supplying and filling the NGH pellet slurry 26, and the extrusion pipe 50 is switched from the supply of the NGH pellet slurry 26 to the press-fitting of the high-pressure gas 45.

Thereafter, the on-off valves 59 and 61 of the extruded tube 50 are closed, and then the on-off valves 55 and 57 are opened. At this time, the on-off valves 54 and 56 are closed in the extrusion pipe 49 shown on the upper side, and then the on-off valve 58 is opened while the on-off valve 60 is opened. As a result, the extrusion pipe 50 is switched from the press-fitting of the high-pressure gas 45 to the operation of supplying and filling the NGH pellet slurry 26, and the extrusion pipe 49 is switched from the supply of the NGH pellet slurry 26 to the press-fitting of the high-pressure gas 45. Thus, in the case of the first embodiment, the NGH pellet slurry 26 is transferred by the pressure of the high-pressure gas 45.

  The switching of the on-off valves 54 to 61 and the drive control of the slurry pump 12 and the compressor 42 are performed by a control device (not shown). Thereafter, these cycles are repeated.

In the case of the first embodiment, as shown in FIG. 8 (b), the NGH pellet slurry 26 is almost continuously extruded by the two extrusion tubes 49 and 50, but the high pressure gas 45 is injected or shut off. Therefore, when the on-off valve is switched, the gas flow is interrupted. However, the pressure fluctuation of the high-pressure gas 45 at this time is a compressible gas and can be absorbed by the gas tank 44 (FIG. 8 (a)).

Furthermore, by providing the push-out pipe device 62 for switching the on-off valves 58 and 59 provided on the outlet side of the gas compressor 42 in this way and using the on-off valves for switching, the discharge pressure of the gas compressor 42 is reduced. Since the slurry pump 12 and the gas compressor 42 can be used separately so as not to act on the discharge side of the slurry pump 12, the slurry pump 12 can supply the NGH pellet slurry 26 to the extrusion pipes 49 and 50. A low-lift pump of the order is sufficient, and the gas compressor 42 can be set to a higher pressure than the second reference example described above, and the NGH pellet slurry 26 can be transferred for a longer distance.

FIG. 9 is a block diagram showing a gas hydrate pellet transfer apparatus according to the second embodiment of the present invention. The second embodiment is an example in which the NGH pellet slurry is transferred by combining the gas pressure feeding of the first embodiment and the mixed pressure feeding of the second reference example described above, as in the first embodiment. The mixed gas pressure feed in the second reference example described above is added to the NGH pellet slurry that has been gas pressure fed and transferred. Since the configuration on the loading side is the same as that of the first reference example described above, the same reference numeral is given to the same configuration, and the detailed description thereof is omitted. The same reference numerals are given to the same components as those in the second reference example and the first embodiment described above, and detailed description thereof will be omitted.

As shown in the figure, in the second embodiment, a mixed pressure inlet pipe 41b is connected to the transport pipe 17 on the downstream side of the extruded pipes 49 and 50 in the first embodiment. As shown in FIG. 5 of the second reference example described above, the mixed pressure inlet pipe 41b is connected to the transport direction R of the transport pipe 17 at a predetermined acute angle. An upstream side of the mixed pressure inlet pipe 41 b is connected to a high pressure gas supply pipe 51, and the high pressure gas 45 is press-fitted into the NGH pellet slurry 26 from the high pressure gas supply pipe 51. In addition, an open / close valve 65 for supplying or shutting off the high-pressure gas 45 is provided in the mixed pressure inlet pipe 41b. Since other configurations are the same as those of the first embodiment described above, detailed description thereof is omitted.

According to the gas hydrate pellets transfer device 66 of the second embodiment constructed in this manner, as in the first embodiment described above, the extruded tube 49 and 50 of the two by using the pressure of the high pressure gas 45 Since the NGH pellet slurry 26 is alternately extruded into the transport pipe 17 and the high-pressure gas 45 is mixed into the NGH pellet slurry 26 extruded into the transport pipe 17 from the mixed pressure inlet pipe 41b, the pressure feeding using the push-out pipe device 62 is performed. Further, by reducing the pipe line friction of the high-pressure gas 45 mixed in the NGH pellet slurry 26, it is possible to transfer the NGH pellet slurry 26 over a longer distance.

FIG. 10 is a block diagram showing a gas hydrate pellet transfer apparatus according to a third embodiment of the present invention. FIGS. 11 (a) and 11 (b) show the operation cycle of the gas hydrate pellet transfer apparatus shown in FIG. It is explanatory drawing. The third embodiment is an example in which the NGH pellet slurry is transferred by a liquid pumping method. Since the configuration on the loading side is the same as that of the first reference example described above, the same reference numeral is given to the same configuration, and the detailed description thereof is omitted. Moreover, the same code | symbol is attached | subjected also to the structure same as 1st Embodiment, and the detailed description is abbreviate | omitted.

As shown in FIG. 10, in the third embodiment, the NGH pellet slurry 26 to be transferred is transferred to the high-pressure liquid 67 (in this embodiment, the slurry medium tank 4 in the downstream side of the slurry pump 12 in the first embodiment. The accumulated slurry medium 3 is used, but with different signs.) By continuously extruding, the transfer distance of the NGH pellet slurry 26 is further increased by the pressure of the high-pressure liquid 67. In this specification and claims, the “high pressure liquid” is a liquid having a pressure capable of transferring the NGH pellet slurry 26 by a predetermined distance, and is determined according to the transfer distance, the pipe resistance, and the like. Discharged with pressure.

In the third embodiment, the high-pressure liquid 67 is continuously supplied in order to continuously pump the NGH pellet slurry 26. The downstream pipe line of the slurry pump 12 is made up of three branch supply pipes 47, 48, 68, and these branch supply pipes 47, 48, 68 are arranged upstream of the three extrusion pipes 49, 50, 69, respectively. Connected. These extrusion pipes 49, 50, and 69 are for extruding the NGH pellet slurry 26 supplied from the slurry pump 12 with the pressure of the high-pressure liquid 67. A liquid is provided upstream of the extrusion pipes 49, 50, and 69. A supply pipe 70 is connected.

In the third embodiment, since the slurry medium 3 is used for the high-pressure liquid 67, the slurry medium 3 stored in the slurry medium tank 4 is transferred from the liquid supply pipe 70 as the high-pressure liquid 67 to the extrusion pipes 49, 50, 69. Are supplied to each. Furthermore, liquid return pipes 71, 72, 73 are provided on the downstream side of these extrusion pipes 49, 50, 69, respectively, and these liquid return pipes 71, 72, 73 are provided in the extrusion pipes 49, 50, 69. The pressurized high-pressure liquid 67 is connected so as to return to the slurry medium tank 4.

  The branch supply pipes 47, 48, 68 are provided with on-off valves 54, 55, 74, the liquid return pipes 71, 72, 73 are provided with on-off valves 75, 76, 77, and the extrusion pipes 49, 50, 69 are branched. Open / close valves 58, 59, 78 are provided upstream of the connection points of the supply pipes 47, 48, 68, and open / close valves 60, 61, 79 are provided downstream of the connection points of the liquid return pipes 71, 72, 73, respectively. ing. These on-off valves 54, 55, 58 to 61, and 74 to 79 are controlled to be opened and closed by a control device (not shown). The liquid supply pipe 70 is provided with a high-pressure pump 80 and a cooler 81, and downstream sides of the extrusion pipes 49, 50 and 69 are connected to one transport pipe 17. These constitute the extruded tube device 82.

According to the gas hydrate pellet transfer device 83 in the third embodiment, the NGH pellet slurry 26 can be continuously transferred as a liquid as shown in FIGS. 11 (a) and 11 (b). Since the basic principle is as shown in FIGS. 7 (a) to (d), the following description will mainly explain the opening / closing timing of the valve.

  In the state shown in FIG. 11 (a), the NGH pellet slurry 26 is supplied from the NGH pellet slurry supply pipe 11 to the extrusion pipe 50 through the branch supply pipe 48 and the on-off valve 55 by the slurry pump 12. The high pressure liquid 67 is returned to the slurry medium tank 4 via the on-off valve 76 and the liquid return pipe 72. Thereby, the slurry medium 3 used as the high-pressure liquid 67 is circulated.

  On the other hand, the high-pressure liquid 67 is simultaneously pressed into the extrusion pipe 69 from the high-pressure pump 80 through the liquid supply pipe 70 and the on-off valve 78, and the NGH pellet slurry 26 in the extrusion pipe 69 passes through the on-off valve 79. Extruded. In this state, the on-off valves 54, 74, 75, 77, 58, 59, 61 are closed. In this figure, the open / close valve 60 is opened while the open / close valve 79 is open.

  In this way, in one of the three extruded tubes 49, 50, 69, the NGH pellet slurry 26 is filled, and the high-pressure liquid 67 that was in the extruded tube is returned to the slurry medium tank 4, At the same time, the NGH pellet slurry 26 is extruded into the transport pipe 17 by the high-pressure liquid 67 in one extrusion pipe.

  As shown in FIG. 11 (b), the supply of the NGH pellet slurry 26 and the press-fitting of the high-pressure liquid 67 into the three extruded tubes 49, 50, and 69 are performed as follows. In a state where the NGH pellet slurry 26 is supplied to the extrusion pipe 50 shown in the center of the figure, the on-off valve 58 is opened in the extrusion pipe 49 shown in the upper part of the figure, and the high-pressure liquid 67 is pressed into the extrusion pipe 49. At this time, the open / close valve 78 and the open / close valve 79 are closed in the extruded tube 69 shown in the lower part of the figure. Then, the on-off valves 55 and 76 of the central extruding pipe 50 are closed, and the on-off valves 74 and 77 of the lower extruding pipe 69 are opened, and the NGH pellet slurry 26 is supplied and filled into the extruding pipe 69. At this time, press-fitting of the high-pressure liquid 67 is continued in the extruded tube 49.

  Thereafter, the opening / closing valve 59 is opened while opening the opening / closing valve 61 of the central extrusion pipe 50, and the opening / closing valves 58, 60 of the upper extrusion pipe 49 are closed. At this time, the NGH pellet slurry 26 is supplied and filled in the lower extrusion tube 69. Then, the open / close valves 54 and 75 of the upper push pipe 49 are opened, and the open / close valves 74 and 77 of the lower push pipe 69 are closed. At this time, press-fitting of the high-pressure liquid 67 is continued in the central extruded tube 50.

  Thereafter, the on-off valve 78 is opened while opening the on-off valve 79 of the lower extrusion pipe 69, and the on-off valves 59, 61 of the central extrusion pipe 50 are closed. At this time, filling of the NGH pellet slurry 26 is continued in the upper extrusion tube 49. As a result, the high-pressure liquid 67 is pressed into the lower extrusion tube 69.

  Thereafter, the on-off valves 54 and 75 of the upper extrusion pipe 49 are closed, and the on-off valves 55 and 76 of the central extrusion pipe 50 are opened, and an operation of supplying and filling the NGH pellet slurry 26 to the extrusion pipe 50 is performed. Is called. At this time, the press-in of the high-pressure liquid 67 is continued in the lower extrusion tube 69.

  In this way, the filling of the NGH pellet slurry 26 into the central extrusion tube 50, the filling of the NGH pellet slurry 26 into the lower extrusion tube 69, and the filling of the NGH pellet slurry 26 into the upper extrusion tube 49 are continued. At the same time, the operation of pressing the high pressure liquid 67 into the extrusion pipe not filled with the NGH pellet slurry 26 and extruding the NGH pellet slurry 26 to the transport pipe 17 with the pressure of the high pressure liquid 67 is repeated.

  In this manner, the three high-pressure pumps 80 can be continuously operated by sequentially switching the on-off valves 54, 55, 58 to 61, and 74 to 79 at predetermined timings by using the three extruded pipes 49, 50, and 69. The pellet slurry 26 can be transferred over a long distance. Switching of these on-off valves 54, 55, 58 to 61, 74 to 79 and drive control of the slurry pump 12 are performed by a control device (not shown). Thereafter, these cycles are repeated.

Also according to the third embodiment, the high pressure pump 80 is provided by providing the push-out pipe device 82 for switching the on-off valves 58, 59, 78 provided on the outlet side of the high-pressure pump 80 and switching the on-off valves. Since the slurry pump 12 and the high-pressure pump 80 can be used separately so that the discharge pressure of the slurry does not act on the discharge side of the slurry pump 12, the slurry pump 12 is connected to the extrusion pipes 49, 50 and 69 with the NGH pellets. A low-lift pump capable of supplying the slurry 26 may be used, and a high-pressure pump 80 may be provided to transfer the NGH pellet slurry 26 for a longer distance.

Further, in the third embodiment, the example in which the NGH pellet slurry 26 is continuously transferred using the three extrusion tubes 49, 50, 69 has been described. However, at least three extrusion tubes 49, 50, 69 are provided. If so, the NGH pellet slurry 26 can be continuously transferred so as not to cause a change in cross section, and the number of extruded tubes is not limited to the above embodiment.

In the first to third embodiments described above, the natural gas is converted into NGH, then pelletized and then transported by sea from the storage tank of the NGH production facility at the gas producer when transported by sea. In the case of transferring NGH to the tank, or after transporting by sea, the gas hydrate pellet transfer device for transferring NGH from the storage tank of the NGH transport ship to the storage tank of the regasification facility in the consumption area has been described. 12 can also be applied to transfer between the NGH production apparatus 103 and the NGH storage tank 104, between the NGH storage tank 107 and the regasification apparatus 108, and the like.

In the first to third embodiments described above, the transfer distance of the NGH pellet slurry 26 can be increased in order. However, the gas pumping and the liquid pumping are made different, or a plurality of embodiments are combined. You may combine them.

  Furthermore, the above-described embodiment shows an example, and various modifications can be made without departing from the spirit of the present invention, and the present invention is not limited to the above-described embodiment.

  The gas hydrate pellet transfer apparatus according to the present invention transfers NGH from a storage tank of an NGH production facility at a gas producer to a storage tank of an NGH transport ship that transports the sea, such as when the gas hydrate pellets are transported by sea. On the contrary, it can be used when NGH is transferred from the storage tank of the NGH transport ship to the storage tank of the regasification facility in the consumption area.

It is a block diagram which shows the gas hydrate pellet transfer apparatus which concerns on the 1st reference example of this invention. It is sectional drawing of the side view which shows the mixer of the gas hydrate pellet transfer apparatus shown in FIG. It is sectional drawing of the gas hydrate storage tank by the side of loading shown in FIG. It is a block diagram which shows the gas hydrate pellet transfer apparatus which concerns on the 2nd reference example of this invention. It is a schematic diagram which shows the pumping part in the gas hydrate pellet transfer apparatus shown in FIG. It is a block diagram which shows the gas hydrate pellet transfer apparatus which concerns on 1st Embodiment of this invention. (a)-(d) is explanatory drawing which shows the basic pumping method in the gas hydrate pellet transfer apparatus shown in FIG. (a), (b) is explanatory drawing of the operation cycle by the gas hydrate pellet transfer apparatus shown in FIG. It is a block diagram which shows the gas hydrate pellet transfer apparatus which concerns on 2nd Embodiment of this invention. It is a block diagram which shows the gas hydrate pellet transfer apparatus which concerns on 3rd Embodiment of this invention. (a), (b) is explanatory drawing of the operation cycle by the gas hydrate pellet transfer apparatus shown in FIG. It is a schematic diagram of the structure which shows the application example which transfers a gas hydrate pellet.

Explanation of symbols

DESCRIPTION OF SYMBOLS 1 ... NGH pellet 2 ... NGH storage tank 3 ... Slurry medium 4 ... Slurry medium tank 5 ... Slurry medium supply pump 6 ... Cooler 7 ... Slurry medium supply pipe 8 ... On-off valve 10 ... Mixer 11 ... NGH pellet slurry supply pipe 12 ... Slurry pump 13 ... Gas pipe 14 ... Compressor 15 ... Gas tank 16 ... Cooler 17 ... Transport pipe 18 ... Supply port 21 ... Mixing nozzle 22 ... Auxiliary nozzle 25 ... Auxiliary nozzle 26 ... NGH pellet slurry 27 ... Separator 28 ... NGH storage tank 29 ... Slurry medium tank 30 ... Separation network 31 ... Input pipe 32 ... Liquid return pipe 33 ... Mesh-like membrane 34 ... Liquid return inlet pipe 35 ... Return rise pipe 36 ... Return overflow pipe 37 ... Discharge pipe 38 ... Slurry medium Transfer pump 39 ... Connection 40 ... Gas hydrate pellet transfer device 41a ... Gas distribution 41b ... Mixed pressure inlet pipe 42 ... Compressor 43 ... Cooler 44 ... Gas tank 45 ... High pressure gas 46 ... Gas hydrate pellet transfer device 47, 48 ... Branch supply pipe 49, 50 ... Extrusion pipe 51 ... High pressure gas supply pipe 52 53 ... Gas return pipes 54-61 ... Open / close valve 62 ... Extrusion pipe device 63 ... Gas hydrate pellet transfer device 64 ... Tank 65 ... Open / close valve 66 ... Gas hydrate pellet transfer device 67 ... High pressure liquid 68 ... Branch supply pipe 69 ... Extrusion pipe 70 ... Liquid supply pipes 71 to 73 ... Liquid return pipes 74 to 79 ... On-off valve 80 ... High-pressure pump 81 ... Cooler 82 ... Extrusion pipe device 83 ... Gas hydrate pellet transfer device

Claims (10)

  A slurry pump for transferring a gas hydrate pellet slurry into which the slurry is transferred by mixing a slurry medium cooled to a predetermined temperature with a gas hydrate pellet obtained by pelletizing the gas hydrate, and transferring the gas hydrate pellet slurry A plurality of extruding pipes, and a compressor for injecting a high pressure gas cooled to a temperature at which the gas hydrate is kept in a stable state into each of the plurality of extruding pipes. The operation of transferring the pellet slurry and the operation of press-fitting high-pressure gas into the gas hydrate pellet slurry in the plurality of extrusion pipes by the compressor are alternately performed at predetermined intervals, and the high pressure press-fitted between the gas hydrate pellet slurry. Gas configured to discharge gas from the extrusion tube alternately at a specified position Ido rate pellet transfer device. In the gas hydrate pellet transfer device according to claim 1 ,
The high-pressure gas cooled between the gas hydrate pellet slurry and the gas hydrate pellet slurry in the pipeline after the high-pressure gas injected between the gas hydrate pellet slurry is discharged from the extrusion pipe at a predetermined position and cooled to a temperature that keeps the gas hydrate stable. Is a gas hydrate pellet transfer device configured to transfer the gas hydrate pellet slurry in a pipeline.   A slurry pump for transferring a gas hydrate pellet slurry into which the slurry is transferred by mixing a slurry medium cooled to a predetermined temperature with a gas hydrate pellet obtained by pelletizing the gas hydrate, and transferring the gas hydrate pellet slurry A plurality of extruding pipes, and a pump for press-fitting each of the extruding pipes with a high-pressure liquid cooled to a temperature that keeps the gas hydrate in a stable state. The operation of transferring the slurry and the operation of press-fitting the high-pressure liquid into the gas hydrate pellet slurry in the plurality of extrusion tubes by the pump are alternately performed at predetermined intervals, and the high-pressure liquid press-fitted between the gas hydrate pellet slurry is Gas configured to be discharged from the extruded tube alternately at a predetermined position Ido rate pellet transfer device. In the gas hydrate pellet transfer device according to claim 3 ,
A gas hydrate pellet transfer apparatus comprising at least three extrusion tubes. In the gas hydrate pellet transfer device according to any one of claims 1 to 4,
A gas hydrate storage tank that stably stores the gas hydrate pellets, and a slurry medium supply pump that supplies the storage medium with a slurry medium cooled to a temperature that keeps the gas hydrate stable.
A plurality of mixing nozzles for discharging the slurry medium radially from the upper part of the supply port to a radially outer side to a supply port provided at a lower part of the gas hydrate storage tank, and a gas hydrate supplied from the supply port an auxiliary Bruno nozzle you release the slurry medium toward the discharge direction of the rate pellets, the mixer having a formed,
A gas hydrate pellet transfer device configured to mix a slurry medium with the gas hydrate pellets in the mixer to form a slurry. Separator for separating gas hydrate pellet slurry into gas hydrate pellets and slurry medium, gas hydrate storage tank for stably storing gas hydrate pellets separated by the separator, and the separated slurry medium And a separator for separating the gas hydrate pellet slurry transferred by the gas hydrate pellet transfer apparatus according to any one of claims 1 to 5 with the separator. Constructed gas hydrate pellet transfer device. In the gas hydrate pellet transfer device according to claim 6 ,
A gas hydrate pellet transfer apparatus provided with a pipe line and a slurry medium transfer pump for reusing the slurry medium stored in the slurry medium tank as a slurry medium to be mixed when slurrying the gas hydrate pellets.   A gas hydrate pellet obtained by pelletizing the gas hydrate is mixed with a slurry medium cooled to a predetermined temperature to transfer the gas hydrate pellet slurry to which the slurry can be transferred to a plurality of extrusion pipes, The gas hydrate pellet slurry is transferred to the gas hydrate pellet slurry through a plurality of extrusion pipes by alternately injecting the high pressure gas cooled to a temperature that keeps the gas hydrate stable in the gas hydrate pellet slurry. And a gas hydrate pellet transfer method in which the high-pressure gas press-fitted between the gas hydrate pellet slurries is alternately discharged from the extrusion tube at a predetermined position. In the gas hydrate pellet transfer method according to claim 8 ,
The high-pressure gas cooled between the gas hydrate pellet slurry and the gas hydrate pellet slurry in the pipeline after the high-pressure gas injected between the gas hydrate pellet slurry is discharged from the extrusion pipe at a predetermined position and cooled to a temperature that keeps the gas hydrate stable. A gas hydrate pellet transfer method in which gas hydrate pellet slurry is transferred by mixing the hydrate.   A gas hydrate pellet obtained by pelletizing the gas hydrate is mixed with a slurry medium cooled to a predetermined temperature to transfer the gas hydrate pellet slurry to which the slurry can be transferred to a plurality of extrusion pipes, The gas hydrate pellet slurry is transferred to the gas hydrate pellet slurry through a plurality of extrusion pipes by alternately pressing the high pressure liquid cooled to a temperature that keeps the gas hydrate stable in the gas hydrate pellet slurry. And a gas hydrate pellet transfer method in which the high-pressure liquid press-fitted between the gas hydrate pellet slurries is alternately discharged from the extrusion tube at a predetermined position.

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