JP2006218367A - Gas-hydrate feeding method to pressure gasification tank - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To provide an energy saving type pellet supplying method which does not need a compressor to boost the pressure of a low pressure gas. <P>SOLUTION: The energy saving type pellet supplying method is a method to supply the gas-hydrate and water after mixing with a mixer to the high pressure gasification tank. The method comprises a charging step (1) of supplying the gas-hydrate (a) to the mixer 18 under normal pressure, a pressurized water injection step (2) of generating swirling flow by supplying the pressurized water w' from the high pressure gasification tank 17 to a swirling chamber 34 in the mixer, swirling the gas-hydrate in an agitation turbulance chamber 33 under the swirling chamber which rides on the swirling flow and compressing the gas g generated in the mixer by utilizing the elevation of the water level, a discharging step (3) of supplying a mixed matter b of the gas-hydrate and the pressurized water which is swirling in the agitation discharging chamber and a water injection degassing step (4) of introducing the high pressure gas g' collected at the upper part of the mixer utilizing the pressurized water from the high pressure gasification tank after withdrawing the gas-hydrate in the mixer into the high pressure gasification tank. <P>COPYRIGHT: (C)2006,JPO&NCIPI

Description

  The present invention relates to a method and apparatus for supplying gas hydrate to a high-pressure gasification tank, and more particularly, a gasification tank held at a high pressure to cope with a gas pressure required by a gas demand side such as a gas turbine power generation facility. The present invention relates to a method and apparatus for supplying gas hydrate to a high-pressure gasification tank that efficiently supplies gas hydrate.

  Natural gas hydrate (NGH) not only has a high gas storage property (that is, a volume of 1/170 with respect to natural gas), but also minus 162 like liquefied natural gas (LNG). There is no need to keep it at an extremely low temperature of ° C. For example, it has a characteristic that it can be transported or stored while being kept at a very low temperature of about minus 10 ° C to minus 30 ° C at room temperature.

  For this reason, natural gas hydrate is attracting attention from the energy industry as a new means of transporting or storing natural gas in place of LNG.

  For example, this natural gas hydrate is considered to be transported or stored after being processed into pellets having a diameter of about 10 to 50 mm. It is conceivable that the natural gas hydrate is heated and pyrolyzed into natural gas and water, and the natural gas obtained by this pyrolysis is transported to the consumption area.

  For example, in a distributed cogeneration type facility using gas hydrate, the natural gas hydrate is transported by a transport container, and the natural gas hydrate is intermittently sent from the transport container to the high pressure container. A method is adopted in which gas hydrate is pyrolyzed into natural gas and water by circulating water heated by the air conditioning load of the air conditioning equipment, and the resulting high-pressure natural gas is supplied to gas consuming equipment such as a gas turbine. (For example, refer to Patent Document 1).

In addition, water was added to the solidified natural gas hydrate and pressurized and supplied to the decomposition vessel, and the natural gas hydrate was heated to decompose into natural gas and water inside the decomposition vessel. A gas supply method has been proposed in which natural gas is taken out from a decomposition vessel with high pressure and supplied to an external utilization facility (see, for example, Patent Document 2).
Japanese Patent Laid-Open No. 2003-254084 JP 2003-322296 A

  As described above, the natural gas hydrate can be stored at a temperature that is not so low, for example, about minus 10 ° C. to minus 30 ° C. under normal pressure. For example, it is necessary to increase the pressure to about 35 ata (3.43 MPa) and supply it to the gas turbine combustor.

  At that time, by adopting a method of supplying natural gas obtained by pyrolyzing natural gas hydrate in a pressure vessel to gas consuming equipment such as a gas turbine combustor as it is or by adjusting the pressure, Since it is not necessary to increase the pressure again by the compressor, it is possible to prevent the driving power loss of the gas compressor.

  However, when the pressure vessel is maintained at a high pressure of 35 ata or higher as described above, natural gas hydrate is supplied into the pressure vessel at or near normal pressure. Is extremely difficult.

  That is, the high-pressure gas in the pressure vessel reversely flows, and it is necessary to recompress the gas that has flowed in through the knockout drum, which also hinders the operation of gas turbines and the like that have caused fluctuations in the pressure vessel pressure Because. Although a method of pushing in with high-pressure water is also conceivable, natural gas hydrate has a lighter specific gravity than water and is likely to float, so a high-pressure vessel with a higher pressure than a transport vessel containing natural gas hydrate Even if it is simply supplied, only water is supplied, and the essential natural gas hydrate is left behind. Therefore, a method using a mixer for supplying natural gas hydrate is conceivable.

  FIG. 7 is a configuration diagram of a conventional gas hydrate supply device devised by the present inventors, in which a hollow cylindrical mixer 8 is provided above a high-pressure gasification tank 17 which is a pressure-resistant vessel. The mixer 8 has an NGH inlet pipe 11 having an NGH inlet valve 1 at the upper part thereof, and connects the bottom of the mixer 8 and the upper part of the gasification tank 7 by an NGH outlet pipe 14 having an NGH outlet valve 4. ing. Further, the bottom of the gasification tank 7 and the side of the mixer 8 are connected by a water injection pipe 12 having a circulating water pump 9 and a water injection valve 2. Further, a low-pressure degassing pipe 16 having a pressure equalizing valve 6 is provided on the side of the mixer 8.

  FIG. 8 is an operation explanatory view of this natural gas hydrate supply device. With reference to this figure, the natural gas hydrate p processed into a pellet and exposed to normal pressure is pressurized by the mixer 8. A method of intermittently charging the gasification tank 7 will be described.

  FIG. 8A shows an NGH filling process after the water injection valve 2, the NGH discharge valve 4 and the pressure equalizing valve 6 are closed and the inside of the mixer 8 having a predetermined amount of water w is maintained at normal pressure. In this step, the NGH charging valve 1 is opened to supply a predetermined amount of NGH (p) under normal pressure into the mixer 8.

  FIG. 8B shows a pressurized water injection process, in which the NGH charging valve 1 is closed, the water injection valve 2 is opened, and high-pressure (for example, about 35 data) pressurized water w ′ is injected into the mixer 8 from the water injection pipe 12. Then, the pressure inside the mixer 8 is increased, and the natural gas g generated by pyrolysis by raising the water surface is pressurized as the water surface rises.

  FIG. 8 (c) shows an NGH discharge process. While injecting pressurized water w ′ having a high pressure (for example, about 35 ata) into the mixer 8 from the water injection pipe 12, the NGH discharge valve 4 is opened to perform gasification (not shown). The state which discharges the mixture b of pressurized water w 'and NGH (p) in the tank is shown.

  FIG. 8D is a process subsequent to the NGH discharge process, and shows a state where all NGH (p) in the mixer 8 is discharged into a gasification tank (not shown).

  FIG. 8 (e) shows a pressure release process, in which the water injection valve 2 and the NGH discharge valve 4 are closed, and the pressure equalizing valve 6 is opened so that the high-pressure (for example, about 35 ata) natural gas g in the mixer 8 is removed. The pressure is reduced and recovered in a knockout drum (not shown). However, in this case, the water w flows out together with the natural gas g because the water surface is above the joint portion of the low-pressure degassing pipe 16 at the start of the pressure release process.

  FIG. 8 (f) shows a state in which, after the pressure equalizing valve 6 is closed, the NGH closing valve 1 can be opened to drop NGH (p).

  When supplying the low-pressure gas recovered in the knockout drum to the gas turbine power generation facility, after separating the water together, it is again set to a predetermined gas pressure (for example, about 35 data) by a compressor (not shown). It was necessary to boost the pressure. For this reason, a gas-liquid separator and a compressor are required, and further, there is a problem that driving power of the compressor is required.

  The present invention has been made to solve such a conventional problem, and an object of the present invention is to provide an energy-saving pellet supply method and apparatus that does not require a compressor for boosting low-pressure natural gas. Is to provide.

  In order to solve the above problems, the present invention is configured as follows.

The present invention according to claim 1 is a method of mixing gas hydrate and water in a mixer and supplying the mixture to a high-pressure gasification tank.
(1) a gas hydrate filling step of supplying gas hydrate to the mixer under normal pressure;
(2) Supplying high-pressure water from the high-pressure gasification tank to a swirl chamber provided in the mixer to generate a swirl flow, and riding the swirl flow in a turbulent turbulence chamber below the swirl chamber A pressurized water injection step of rotating the gas hydrate and compressing the gas generated in the mixer using the rise of the water level,
(3) a gas hydrate discharge step of supplying a mixture of gas hydrate swirling in the disturbance discharge chamber and high-pressure water to the high-pressure gasification tank;
(4) After discharging the gas hydrate in the mixer to the high-pressure gasification tank, the high-pressure gas accumulated in the upper part of the mixer is utilized using high-pressure water supplied from the high-pressure gasification tank. This is a gas hydrate supply method to a high-pressure gasification tank comprising a water injection gas venting step leading into the high-pressure gasification tank.

  The present invention described in claim 2 is the gas hydrate supply method to the high-pressure gasification tank according to claim 1, wherein the gas hydrate is a gas hydrate processed into a pellet form.

The present invention described in claim 3 is a mixer for forming a mixture of gas hydrate and high-pressure water and supplying the mixture to a high-pressure gasification tank, a high-pressure gasification tank having a watering pipe inside, and the high-pressure gas tank. A hot water circulation path connecting the gasification tank and the watering pipe, and a pipe for supplying gas separated in the high-pressure gasification tank to the gas consuming equipment,
The mixer has a cylindrical main body, a cone disposed on the upper portion of the main body, a swirling chamber provided on the upper portion of the conical body, and a high-pressure water supply pipe disposed in a tangential direction of the swirling chamber. And
And after paying out the gas hydrate in the mixer to the high-pressure gasification tank, the gas accumulated in the upper part of the mixer is used in the high-pressure gasification tank using high-pressure water supplied from the high-pressure gasification tank. The gas hydrate to the high-pressure gasification tank is provided with a gas extraction pipe at the top of the mixer, and a drain pipe for introducing residual water to the high-pressure gasification tank at the lower part of the mixer It is a supply device.

The present invention described in claim 4 is a mixer for forming a mixture of gas hydrate and high-pressure water and supplying the mixture to a high-pressure gasification tank, a high-pressure gasification tank having a watering pipe inside, and the high-pressure gasification tank. A hot water circulation path connecting the gasification tank and the watering pipe, and a pipe for supplying the gas separated in the high-pressure gasification tank to the gas consuming equipment,
The mixer body has a cylindrical swirl chamber at the top and a cone at the bottom.
A high-pressure water supply pipe arranged in a tangential direction of the swirl chamber;
After the gas hydrate in the mixer is discharged to the high-pressure gasification tank, the gas accumulated in the upper part of the mixer is supplied into the high-pressure gasification tank using high-pressure water supplied from the high-pressure gasification tank. A degassing tube at the top of the mixer,
The apparatus for supplying gas hydrate to a high-pressure gasification tank is characterized in that a drain pipe for introducing residual water to the high-pressure gasification tank is provided in the mixer.

  As described above, the invention according to claim 1 is a method of mixing gas hydrate and water in a mixer and supplying the mixture to a high-pressure gasification tank. (1) Gas hydrate in the mixer under normal pressure A gas hydrate filling step of supplying the gas, and (2) supplying a high-pressure water from the high-pressure gasification tank to a swirl chamber provided in the mixer to generate a swirl, and riding on the swirl A pressurized water injection step of swirling the gas hydrate in the turbulent turbulent flow chamber below the swirl chamber and compressing the gas generated in the mixer using the rise in water level; and (3) in the turbulent discharge chamber. A gas hydrate discharging step of supplying a mixture of swirling gas hydrate and high pressure water to the high pressure gasification tank; and (4) after discharging the gas hydrate in the mixer to the high pressure gasification tank. The reservoir at the top of the mixer Since the high-pressure gas that has been used is composed of a water-injecting degassing step for introducing the high-pressure gas into the high-pressure gasification tank using the high-pressure water supplied from the high-pressure gasification tank, the gas accumulated in the mixer There is no need to store in a tank such as a knockout drum. That is, the gas-liquid separator or recompression of the above-mentioned released gas is unnecessary, which is very economical.

  The invention according to claim 2 is characterized in that, in claim 1, the shape of the gas hydrate is a pellet. For this reason, it is not necessary to shape | mold into a special shape, The pellet which is a normal formation form can be used as it is.

The invention described in claim 3 is a mixer for forming a mixture of gas hydrate and high-pressure water and supplying the mixture to a high-pressure gasification tank, a high-pressure gasification tank having a watering pipe inside, and A hot water circulation path connecting the high-pressure gasification tank and the watering pipe, and a pipe for supplying gas separated in the high-pressure gasification tank to the gas consuming equipment,
The mixer has a cylindrical main body, a cone disposed on the upper portion of the main body, a swirling chamber provided on the upper portion of the conical body, and a high-pressure water supply pipe disposed in a tangential direction of the swirling chamber. And
And after paying out the gas hydrate in the mixer to the high-pressure gasification tank, the gas accumulated in the upper part of the mixer is used in the high-pressure gasification tank using high-pressure water supplied from the high-pressure gasification tank. A gas extraction pipe is installed at the top of the mixer, and a drain pipe that guides residual water to the high-pressure gasification tank is provided at the bottom of the mixer. In addition, there is no need to store it once. As a result, there is no need to pressurize the gas whose pressure has been reduced by the knockout drum, so that a compressor for boosting is not necessary, which is very economical.

  Furthermore, the invention described in claim 4 has a structure in which the mixer described in claim 3 is further simplified. Thereby, it has the mixing discharge performance equivalent to the mixer of Claim 3, and also can manufacture a mixer easily.

  Hereinafter, embodiments of the present invention will be described with reference to the drawings. In this embodiment, natural gas hydrate (NGH) processed into a pellet is taken as an example.

  FIG. 1 is an overall view of an NGH gasification system including a pellet supply device to a high-pressure gasification tank according to the present invention. An NGH feed drum 21, a mixer 18, a high-pressure gasification tank 17, and heat exchange A vessel 20 and a mist separator 22 are provided.

  A method for gasifying the NGH pellet p will be described with reference to FIG.

  First, the NGH pellet p is charged into the mixer 18 through the NGH charging pipe 11 and the NGH charging valve 1 at normal pressure.

  Next, the water in the high-pressure gasification tank 17 is injected into the mixer 18 from the water injection pipe 12 having the pump 19, the water injection valve 2, and the pump 23, so that the inside of the mixer 18 is the same as the high-pressure gasification tank 17. Pressurize until pressure is reached. At this time, the pump 23 is not necessarily required if the discharge pressure of the pump 19 is sufficient.

  After the pressurization is completed, the NGH discharge valve 4 is opened, and the NGH pellets p in the mixer 18 are sent to the high-pressure gasification tank 17 while pouring water.

  After the NGH pellet p in the mixer 18 disappears, the high-pressure gas vent valve 3 is opened, and all the high-pressure gas accumulated in the upper portion of the mixer 18 is discharged to the high-pressure gasification tank 17 through the high-pressure gas vent pipe 13. To do.

  Thereafter, the pressure equalizing valve 6 and the drain valve 5 are opened, and the water in the mixer 18 is sent to the high-pressure gasification tank 17 by the pump 24. At this time, it is preferable to introduce natural gas into the mixer 18 from the pressure equalizing valve 6 and the pressure equalizing pipe 16.

  Thereafter, the NGH pellet p is again fed from the NGH feed drum 21, and the above steps are sequentially performed and intermittently sent to the high-pressure gasification tank 17. Here, by providing a plurality of mixers 18, the NGH pellets p can be continuously charged into the high-pressure gasification tank 17.

  On the other hand, in the high-pressure gasification tank 17, the water in the high-pressure gasification tank 17 is circulated through the pump 19, the pipe 25, and the heat exchanger 20, and sprayed on the NGH pellet p. At this time, since the circulating water is heated by the heat exchanger 20, it can be efficiently gasified. Furthermore, if condensate generated in an NGH plant (not shown) is used as a heat medium for the heat exchanger, it is possible to recover heat from low-temperature waste water.

  The natural gas gasified in the high-pressure gasification tank 17 is supplied as a high-pressure gas g ′ to a customer (not shown) via the mist separator 22. The water (mist) w separated by the mist separator 22 is returned to the high-pressure gasification tank 17 through the pipe 30.

  FIG. 2 is a configuration diagram of a gas hydrate supply apparatus according to the present invention. Here, the upper part of the mixer 18 and the upper part of the high-pressure gasification tank 17 are connected by a high-pressure gas vent pipe 13 having the high-pressure gas vent valve 3, and the bottom part of the mixer 18 and the high-pressure gasification tank 17 are connected to the water distribution pipe 5. By connecting with the water distribution pipe 15 having the pump 24, the NGH pellet p can be sent to the high-pressure gasification tank 17 without using a conventional knockout drum or compressor. The operation of supplying the NGH pellet p will be described in detail later.

  As shown in FIG. 3, the mixer 18 is provided with a cone 32 inside a cylindrical body 31 with a bottom, a disturbance discharge chamber 33 at the bottom, and a cylindrical swirl chamber 34 at the top. The water injection pipe 12 and the low pressure vent pipe 16 are connected to the outer peripheral surface of the swirl chamber 34, and the NGH input pipe 11 and the high pressure vent pipe 13 are connected to the upper part, respectively. Further, the NGH discharge pipe 14 and the water distribution pipe 15 are connected to the bottom of the main body 31. Further, at the side of the main body 31, there is a stagnant gas discharge pipe 13 'for removing the gas accumulated between the cone 32 and the main body 31.

  FIG. 4 is a mode in which the high-pressure gas discharge pipe 13 is provided in the NGH input pipe 11 in the mixer 18 of FIG. By doing so, not only the upper part of the swirl chamber but also the high-pressure gas accumulated in the NGH input pipe 11 can be sent to the high-pressure gasification tank 17.

  FIG. 5 shows a mode in which, in the mixer 18 in FIG. 3 or FIG. By doing so, the swirl flow generated in the swirl chamber 34 can be directly guided to the NGH discharge pipe 14. Here, the high-pressure gas discharge pipe 13 can also be provided in the NGH input pipe 11.

  Next, the operation of supplying NGH pellets will be described in detail using the mixer of FIG. 3 as an example.

  FIG. 6A shows an NGH filling process, in which the water injection valve 2, the high-pressure degassing valves 3, 3 ′, the NGH discharge valve 4, and the drain valve 5 are in the “closed” state, and the mixer 18 In a state in which a predetermined amount of water w is stored, the pressure equalizing valve 6 is “opened” and the inside of the mixer 18 is brought to normal pressure, and then the NGH inlet valve 1 is “opened” and processed into pellets. (P) is fed into the mixer 18 from the feed drum 21 (see FIG. 1).

  FIG. 6B shows a pressurized water injection process. After the NGH charging valve 1 and the pressure equalizing valve 6 are switched from “open” to “closed”, the water injection valve 2 is switched from “closed” to “open”. When the high-pressure water (for example, about 35 data (3.43 MPa)) w ′ from the gasification tank 17 (see FIG. 1) is supplied from 12 to the swirl chamber 34 of the mixer 18, an arrow appears in the swirl chamber 34 of the mixer 18. A swirling flow such as a is generated, and NGH (p) in the turbulent flow chamber 33 also swirls on this swirling flow. At this time, the water level of the mixer 18 rises, and the gas g (the gas flowing in from the pressure equalizing valve 6 and a small amount of natural gas generated in the mixer 18) at the top of the mixer 18 is compressed and increased in pressure (for example, , About 35ata).

  FIG. 6C shows an NGH discharge process. When the NGH discharge valve 4 is opened while injecting high-pressure water w ′ from the gasification tank 17 into the mixer 18 from the water injection pipe 12, the mixer 18 is disturbed. A mixture b of NGH (p) swirling in the discharge chamber 33 and high-pressure water w ′ is supplied through the NGH discharge pipe 14 into the high-pressure (for example, about 35 data) gasification tank 17.

  FIG. 6 (d) is a continuation process of the NGH discharging process of FIG. 6 (c), and mixing is performed by continuously supplying high-pressure water w ′ from the gasification tank 17 into the mixer 18 from the water injection pipe 12. All the NGH (p) in the vessel 18 is supplied into the gasification tank 17 together with the high-pressure water w ′.

  FIG. 6 (e) shows a water injection gas venting process. After the NGH discharge valve 4 is switched from "open" to "closed", the high-pressure gas vent valves 3, 3 'are "opened". The high-pressure natural gas g accumulated between the upper part and the cone and the main body is returned to the gasification tank 17 through the high-pressure degassing pipe 13 together with the high-pressure water w ′ while maintaining the pressure. This eliminates the need for the pressurizing compressor and knockout drum already described.

  FIG. 6F shows a drainage process. When the water injection valve 2 is switched from “open” to “closed” and the pressure equalizing valve 6 and the drain valve 5 are switched from “closed” to “open”, the inside of the mixer 18 is changed. Becomes a normal pressure, and the high-pressure water w ′ remaining in the mixer 18 is returned into the gasification tank 17 by the pump 24 (see FIG. 1). When the water w in the mixer 18 reaches a predetermined amount, the drain valve 5 is closed. Hereinafter, the steps of FIGS. 6A to 6F are repeated.

  In the above description, the case where the number of the mixers 18 is single has been described, but a plurality of mixers 18 are provided for one gasification tank 17, and the operation timing of the mixers 18 is appropriately shifted so as to change the gas. NGH (p) can be supplied into the chemical conversion tank 17 almost continuously.

It is a general view of the NGH gasification system containing the pellet supply apparatus to the high pressure gasification tank which concerns on this invention. It is a block diagram of the gas hydrate supply apparatus by this invention. It is a perspective view containing the partial cross section of a mixer. It is a perspective view containing the partial cross section of a mixer. It is a perspective view containing the partial cross section of a mixer. (A) NGH filling process diagram, (b) pressurized water injection process diagram, (c) NGH discharge process diagram, (d) NGH discharge process diagram, (e) injected water degassing process diagram, (f) drainage process diagram. It is a block diagram of the pellet supply apparatus to the conventional high pressure gasification tank. (A) NGH filling process diagram, (b) pressurized water injection process diagram, (c) NGH discharge process diagram, (d) NGH discharge process diagram, (e) injected water degassing process diagram, (f) drainage process diagram.

Explanation of symbols

a Gas hydrate b Mixture of gas hydrate and high pressure water g 'High pressure gas w Water w' High pressure water p NGH pellet 17 High pressure gasification tank 18 Mixer 20 Heat exchanger 21 NGH feed drum 22 Mist separator 33 Disturbance turbulence chamber 34 Swirl chamber

Claims (4)

In a method of mixing gas hydrate and water with a mixer and supplying them to a high-pressure gasification tank,
(1) a gas hydrate filling step of supplying gas hydrate to the mixer under normal pressure;
(2) Supplying high-pressure water from the high-pressure gasification tank to a swirl chamber provided in the mixer to generate a swirl flow, and riding the swirl flow in a turbulent turbulence chamber below the swirl chamber A pressurized water injection step of rotating the gas hydrate and compressing the gas generated in the mixer using the rise of the water level,
(3) a gas hydrate discharge step of supplying a mixture of gas hydrate swirling in the disturbance discharge chamber and high-pressure water to the high-pressure gasification tank;
(4) After discharging the gas hydrate in the mixer to the high-pressure gasification tank, the high-pressure gas accumulated in the upper part of the mixer is utilized using high-pressure water supplied from the high-pressure gasification tank. A method for supplying gas hydrate to a high-pressure gasification tank comprising a water-injecting degassing step leading into the high-pressure gasification tank. The method for supplying gas hydrate to a high-pressure gasification tank according to claim 1, wherein the gas hydrate is a gas hydrate processed into a pellet form. A mixer for forming a mixture of gas hydrate and high-pressure water and supplying the mixture to the high-pressure gasification tank, a high-pressure gasification tank having a watering pipe inside, and connecting the high-pressure gasification tank and the watering pipe It consists of a hot water circulation path and piping for supplying gas separated in the high-pressure gasification tank to the gas consuming equipment,
The mixer has a cylindrical main body, a cone disposed on the upper portion of the main body, a swirling chamber provided on the upper portion of the conical body, and a high-pressure water supply pipe disposed in a tangential direction of the swirling chamber. And
And after paying out the gas hydrate in the mixer to the high-pressure gasification tank, the gas accumulated in the upper part of the mixer is used in the high-pressure gasification tank using high-pressure water supplied from the high-pressure gasification tank. The gas hydrate to the high-pressure gasification tank is provided with a gas extraction pipe at the top of the mixer, and a drain pipe for introducing residual water to the high-pressure gasification tank at the lower part of the mixer Feeding device. A mixer for forming a mixture of gas hydrate and high-pressure water and supplying the mixture to the high-pressure gasification tank, a high-pressure gasification tank having a watering pipe inside, and connecting the high-pressure gasification tank and the watering pipe It consists of a hot water circulation path and piping for supplying gas separated in the high-pressure gasification tank to the gas consuming equipment,
The mixer body has a cylindrical swirl chamber at the top and a cone at the bottom.
A high-pressure water supply pipe arranged in a tangential direction of the swirl chamber;
After the gas hydrate in the mixer is discharged to the high-pressure gasification tank, the gas accumulated in the upper part of the mixer is supplied into the high-pressure gasification tank using high-pressure water supplied from the high-pressure gasification tank. A degassing tube at the top of the mixer,
An apparatus for supplying gas hydrate to a high-pressure gasification tank, wherein the mixer is provided with a drain pipe for introducing residual water to the high-pressure gasification tank.

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