JP2008161663A - Hot spring water generation system - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To provide a hot spring water generation system, effectively eluting ions (calcium ions and hydrogen carbonate ions) with a suitable concentration from hot spring minerals to achieve spring quality of water. <P>SOLUTION: This hot spring water generation system includes: a dissolution assisting vessel; a mixing vessel; a water source; a main dissolution vessel; and a storage tank. The dissolution assisting vessel stores at least one dissolution assisting material. The mixing vessel is connected to the dissolution assisting vessel. The water source is connected to the dissolution assisting vessel and the mixing vessel to cause tap water to flow into the dissolution assisting vessel and the mixing vessel. The tap water flowing into the dissolution assisting vessel forms a dissolution assisting agent with the dissolution assisting material, and the dissolution assisting agent flows into the mixing vessel to be mixed with the tap water in the mixing vessel, thereby forming a dissolution assisting liquid. The main dissolution vessel is connected to the mixing vessel, and stores at least one mineral. The dissolution assisting liquid flows from the mixing vessel into the main dissolution vessel to interact with the mineral, thereby forming hot spring water. The storage tank for hot spring water is connected to the main dissolution vessel to preserve the hot spring water. <P>COPYRIGHT: (C)2008,JPO&INPIT

Description

  The present invention relates to a hot spring water generation system, and more particularly to a hot spring water generation system that achieves a water quality improvement effect.

  In recent years, entertainment such as sightseeing has also been emphasized due to the improvement of quality of life, and among them, hot springs are one of the entertainment that people prefer.

  However, a large amount of hot spring resources have been developed, and the water for hot springs has become scarce. Furthermore, the distance between the city and the hot spring resort is far, and people have to go to the hot spring resort by means of transportation. Therefore, an artificial hot spring machine needs to exist. The artificial hot spring machine can compensate for the shortage of hot spring resources, and can prevent problems such as land subsidence and deterioration of spring quality caused by pumping geothermal water. In addition, the emergence of artificial hot springs will reduce the congestion of hot springs and the deterioration of hot springs.

  In particular, the current artificial hot spring machine has the main function of removing chlorine and produces a hot spring with an effect of qualitatively. In addition, many artificial hot spring machines generate functional hot spring water and cannot generate mineral hot spring water. Therefore, the hot spring water generated by the artificial hot spring machine does not meet the water quality standards stipulated in the hot spring law.

  An object of the present invention is to provide a hot spring water generation system and to effectively elute ions (calcium ions and hydrogen carbonate ions) at appropriate concentrations from hot spring minerals to achieve water quality. .

  The hot spring water generation system according to the present invention includes a dissolution auxiliary tank, a mixing tank, a water source, a main dissolution tank, and a storage tank. The dissolution aid tank contains at least one dissolution aid substance. The mixing tank is connected to the dissolution auxiliary tank. The water source is connected to the dissolution auxiliary tank and the mixing tank, and tap water flows into the dissolution auxiliary tank and the mixing tank. The tap water that has flowed into the dissolution auxiliary tank forms a dissolution auxiliary substance and a dissolution auxiliary agent, and the dissolution auxiliary agent flows into the mixing tank and is mixed with the tap water in the mixing tank to form a dissolution auxiliary liquid. The main dissolution tank is connected to the mixing tank and contains at least one mineral. The solubilizing liquid flows from the mixing tank into the main dissolving tank and reacts with minerals to form hot spring water. The hot spring water storage tank is connected to the main dissolution tank to store hot spring water.

  The hot spring water generation system according to the present invention further includes a water pressure adjusting device connected between the dissolution auxiliary tank and the water source and installed on the dissolution auxiliary tank, and adjusts the flow rate of tap water flowing into the dissolution auxiliary tank. To do.

  Further, the water pressure adjusting device has a first micro flow control element, a first water discharge pipe, and a second water discharge pipe, the first micro flow control element is connected to the dissolution auxiliary tank, and the first water discharge pipe is connected to the first water discharge pipe. It is preferable that it is located on the flow control element and extends into the mixing tank, and the second water discharge pipe is located on the first water discharge pipe and extends into the mixing tank.

  The first micro flow control element includes a filter membrane, a fiber filter cloth, or a precision ceramic plate.

  Moreover, it is preferable to have a 1st flow control valve which is installed on a 1st water discharge pipe and controls the flow volume of the tap water which flows through a 1st water discharge pipe.

  The dissolution auxiliary tank has at least one first space and at least one second space, the first space is located on the second space, and stores the dissolution auxiliary substance, and the second space is a mixing tank. It is preferable that the plurality of porous bioballs are accommodated and the solubilizing agent flows into the mixing tank through the second space and the porous bioball.

  Furthermore, it has a first transport pipe connected between the second space and the mixing tank, and the dissolution aid preferably flows into the mixing tank through the second space, the porous bioball, and the first transport pipe. .

  Moreover, it is preferable that a dissolution auxiliary | assistance tank has further at least 1 2nd micro flow control element installed between 1st space and 2nd space.

  The second micro flow control element preferably includes a filter membrane, a fiber filter cloth, or a precision ceramic plate.

  The mixing tank preferably contains a plurality of porous bioballs.

  Further, in the present invention, it further includes a liquid level sensing element that is installed in the hot spring water storage tank and is electrically connected to the water source, and the liquid level sensing element controls the level of the hot spring water in the storage tank. It senses and controls the water source and flows tap water into the dissolution auxiliary tank and the mixing tank.

  Furthermore, it has a second transport pipe and a pump, the second transport pipe is connected to the mixing tank and the main dissolution tank, the pump is connected to the second transport pipe, and the dissolution auxiliary liquid in the mixing tank is pumped by the pump. Preferably, it is taken and flows into the main dissolution tank via the second transport pipe.

  Furthermore, it has an air collection conduit communicating with the main dissolution tank and the second transport pipe, and the dissolution auxiliary gas generated by the main dissolution tank is collected by the gas collection conduit, and the second transport pipe is accompanied by the dissolution auxiliary liquid. It is preferably transported to the main dissolution tank and reacts with hot spring minerals to form hot spring water.

  Moreover, it is preferable to have a gas-liquid mixer connected between the air collection conduit and the second transport pipe, and to mix the dissolution auxiliary gas in the air collection conduit and the dissolution auxiliary liquid in the second transport pipe.

  In addition, the air collecting conduit is preferably extended into the mixing tank.

  Furthermore, it is preferable to have a first horizontal transport pipe connected between the second transport pipe and the mixing tank, and to adjust the flow rate of the dissolution auxiliary liquid flowing in the main dissolution tank.

  Furthermore, it is preferable to have a second flow rate control valve installed on the first horizontal transport pipe and to control the flow rate of the solubilizing liquid flowing through the first horizontal transport pipe.

  Furthermore, it is preferable to have a second lateral transport pipe connected between the second transport pipe and the storage tank.

  Moreover, it is preferable to have the 3rd flow control valve installed on a 2nd horizontal transport pipe.

  Moreover, it has a 3rd transport pipe connected between a main dissolution tank and a storage tank, and it is preferable that the hot spring water in a main dissolution tank flows in into a storage tank from a 3rd transport pipe.

  According to the hot spring water generation system of the present invention, the dissolution rate of hot spring minerals can be effectively increased, and tap water can be converted into hot spring water that meets the spring quality standards within a short time.

  Referring to FIG. 1, the hot spring water generation system 100 of the present embodiment mainly includes a dissolution auxiliary tank 105, a mixing tank 110, a water source 115, a main dissolution tank 120, a hot spring water storage tank 125, a water pressure adjusting device 130, a first. Flow control valve 135, first transport pipe 140, liquid level sensing element 145, second transport pipe 150, pump 155, air collection conduit 160, gas-liquid mixer 165, first lateral transport pipe 170, second flow control valve 175, a second lateral transport pipe 180, a third flow rate control valve 185, and a third transport pipe 190.

  As shown in FIG. 1, the water source 115 is connected to the dissolution auxiliary tank 105 and the mixing tank 110 by a water discharge pipe 195, and tap water flows into the dissolution auxiliary tank 105 and the mixing tank 110. Specifically, the tap water provided by the water source 115 flows into the dissolution auxiliary tank 105 and the mixing tank 110 through the water pressure adjusting device 130, and flows into the mixing tank 110 directly.

  As shown in FIGS. 1 and 2, the water pressure adjusting device 130 is connected between the dissolution auxiliary tank 105 and the water source 115, and the water pressure adjusting device 130 is installed on the dissolution auxiliary tank 105 and flows into the dissolution auxiliary tank 105. Adjust the flow rate of the tap water. More specifically, the water pressure adjusting device 130 includes a first micro flow control element 130a, a first water discharge pipe 130b, and a second water discharge pipe 130c. The first micro flow control element 130a is connected to the upper part of the dissolution assisting tank 105, and the first micro flow control element 130a is made of a filter membrane, a fiber filter cloth, or a precision ceramic plate. For example, the first micro-flow control element 130a is composed of a filter membrane having a cell gap of 1 to 5 μm or a fiber filter cloth having a cell gap of 10 μm. The first drain pipe 130 b is located on the first micro flow control element 130 a, and the first drain pipe 130 b extends into the mixing tank 110. The second water discharge pipe 130 c is located on the first water discharge pipe 130 b and the second water discharge pipe 130 c extends into the mixing tank 110. In addition, the 1st flow control valve 135 is installed on the 1st water discharge pipe 130b, and controls the flow volume of the tap water which flows through the 1st water discharge pipe 130b. It should be noted that the flow rate of tap water flowing through the first drain pipe 130b is preferably smaller than the flow rate of tap water flowing through the second drain pipe 130c, and the adjustment is performed by the first flow control valve 135. As described above, due to the limitation of the first micro flow control element 130a and the presence of the first water discharge pipe 130b and the second water discharge pipe 130c, most of the tap water flowing into the water pressure adjusting device 130 is the first water discharge pipe. 130b and the second outlet pipe 130c flow into the mixing tank 110, and a very small portion of tap water flows from the first microflow control element 130a into the dissolution auxiliary tank 105.

  With continuing reference to FIGS. 1 and 2, the dissolution auxiliary tank 105 is connected to the mixing tank 110, and the dissolution auxiliary tank 105 includes two first spaces 105a and second spaces 105b, and two second microflow control elements 105c. Have The second micro flow control element 105c is installed between the first space 105a and the second space 105b, and the second micro flow control element 105c is also composed of a filter membrane, a fiber filter cloth, or a precision ceramic plate. For example, the second micro flow control element 105c is configured by a filter membrane having a cell gap of 1 to 5 μm or a fiber filter cloth having a cell gap of 1 μm. The two first spaces 105a are located on the second space 105b, and each contain two different solubilizing substances S or homologous solubilizing substances S (shown in FIG. 1). For example, the two first spaces 105a contain acidic and alkaline solubilizing substances S, respectively. The second space 105b communicates with the mixing tank 110, and a plurality of porous bioballs (or porous gap balls) B are accommodated in the second space 105b. More specifically, the first transport pipe 140 is connected between the second space 105 b and the mixing tank 110, and the second space 105 b is connected to the mixing tank 110 by the first transport pipe 140. In addition, a plurality of porous bioballs (or porous gap balls) B are stored in the mixing tank 110.

  The main dissolution auxiliary tank 120 is connected to the mixing tank 110. More specifically, the second transport pipe 150 is connected to the mixing tank 110 and the main dissolution tank 120, and the pump 155 is connected to the second transport pipe 150. As described above, the main dissolution tank 120 is connected to the mixing tank 110 by the second transport pipe 150. In addition, the main dissolution tank 120 stores a variety of different hot spring minerals. More specifically, as shown in FIG. 1, the main dissolution auxiliary tank 120 is selectively divided into three regions, and stores three different hot spring minerals M1, M2, and M3. For example, the hot spring minerals M1, M2, and M3 are not limited to the following, but are barleystone, tourmaline, and activated carbon, respectively. The hot spring minerals M1, M2, and M3 are different mineral types depending on the actual spring quality. And have a correlation.

  The hot spring water storage tank 125 is connected to the main dissolution auxiliary tank 120 and stores hot spring water. More specifically, the third transport pipe 190 is connected between the main dissolution auxiliary tank 120 and the storage tank 125. Therefore, the storage tank 125 is connected to the main dissolution tank 120 by the third transport pipe 190.

  The liquid level sensing element 145 is installed in the storage tank 125 and electrically connected to the water source 115, where the liquid level sensing element 145 mainly senses the water level of the hot spring water in the storage tank 125, A sensing signal is transmitted to the water source 115 to control water supply of the water source 115. That is, the liquid level sensing element 145 senses the water level of the hot spring water in the storage tank 125 and determines whether the water source 115 continues to flow the tap water into the dissolution auxiliary tank 105 and the mixing tank 110.

  The air collection conduit 160 communicates with the main dissolution tank 120 and the second transport pipe 150, and the air collection conduit 160 extends into the mixing tank 110. In the present embodiment, the air collection conduits 160 communicate with the three regions of the main dissolution tank 120, respectively.

  The gas-liquid mixer 165 is connected between the air collection conduit 160 and the second transport pipe 150.

  The first lateral transport pipe 170 is connected between the second transport pipe 150 and the mixing tank 110, and the second flow rate control valve 175 is installed on the first lateral transport pipe 170.

  The second lateral transport pipe 180 is connected between the second transport pipe 150 and the storage tank 125, and the third flow control valve 185 is installed on the second lateral transport pipe 180.

  Next, the operation method of the hot spring water generation system 100 will be described.

  Referring to FIG. 1, first, tap water provided by the water source 115 flows directly into the mixing tank 110 and also flows into the dissolution auxiliary tank 105 by the water pressure adjusting device 130. It should be noted that when tap water flows into the water pressure adjusting device 130, the tap water in the water pressure adjusting device 130 is limited by the restriction of the first micro flow control element 130a and the presence of the first water discharge pipe 130b and the second water discharge pipe 130c. Most of the water flows into the mixing tank 110 from the first outlet pipe 130b and the second outlet pipe 130c, and a very small part of the tap water flows into the first micro-flow control element 130a (fiber filter cloth having a cell gap of 10 μm). ) Into the dissolution auxiliary tank 105. Subsequently, a small amount of tap water flowing into the dissolution auxiliary tank 105 flows through the dissolution auxiliary substance S in the two first spaces 105a, dissolves the dissolution auxiliary substance S, and forms a dissolution auxiliary agent. Here, both the first spaces 105a selectively contain acidic and alkaline solubilizing substances S, and adjust the pH of the solubilizing agent by the action of acidic alkaline. For example, when both the first spaces 105a are all acidic solubilizing substances S, an acidic solubilizing agent is formed. Thereafter, the solubilizer flows into the second space 105b through the second micro flow control element 105c (fiber filter cloth having a cell gap of 1 μm), and a plurality of porous bioballs (or porous holes) in the second space 105b. It flows into the mixing tank 110 through the cell gap ball) B and the first transport pipe 140. It should be noted that the saturated solubilizing agent flowing into the second space 105b through the second micro flow control element 105c (fiber filter cloth having a cell gap of 1 μm) is a plurality of porous bioballs (or porous cell gap balls). Mix with water at B (because the progression path and mixing time of the solubilizer increases) to form a uniform solubilizer.

  In addition, in this embodiment, since the hydraulic pressure between the dissolution auxiliary tank 105 and the first transport pipe 140 must maintain an equilibrium, the amount of the dissolution auxiliary agent flowing into the mixing tank 110 is adjusted by the water pressure adjusting device 130. This is similar to the amount of tap water flowing into the dissolution auxiliary tank 105 through the first microflow control element 130a (filter cloth having a cell gap of 10 μm). More specifically, when the water source 115 stops transporting tap water into the water pressure regulator 130 (or when the hot spring water generation system 100 is not activated), the dissolution aid tank 105 is a mixing tank for any dissolution aid. Do not flow into 110.

  After the solubilizer flows into the mixing tank 110, the solubilizer and the tap water in the mixing tank 110 are mixed to form a solubilizing liquid. Here, due to the arrangement of the plurality of porous bioballs (or porous cell gap balls) B in the mixing tank 110, the dissolution aid is mixed with tap water in the mixing tank 110 to form a uniform dissolution aid. . Subsequently, the dissolution auxiliary liquid flows into the main dissolution auxiliary tank 120 from the second transport pipe 150 by being pumped by the pump 155. Here, the dissolution auxiliary liquid flows from the bottom to the top through the hot spring minerals M1, M2, and M3 in the main dissolution tank 120 and reacts to form hot spring water. That is, the solubilizing solution elutes ions (calcium ions, hydrogen carbonate ions, hydrogen ions, etc.) having an appropriate concentration in the hot spring minerals M1, M2, and M3. For example, the solubilizing solution promotes the ionization and electrolysis of hot spring minerals M1 (barley stone) and M2 (tourmaline), and has a pH of 5 to 6 and an oxidation-reduction potential of 250 mV due to the adsorption action of the hot spring mineral M3 (activated carbon). Forms hot spring water. Thereafter, the hot spring water in the main dissolution tank 125 flows into the storage tank 125 through the third transport pipe 190. Finally, the hot spring water in the storage tank 125 is output by the output pipe 196 and used.

  On the other hand, when the dissolution auxiliary liquid dissolves and reacts with the hot spring minerals M1, M2, and M3 in the three regions of the main dissolution tank 120, a dissolution auxiliary gas (for example, carbon dioxide gas) is usually generated. Improves the dissolution efficiency of hot spring minerals M1, M2, and M3. Therefore, the air collecting conduit 160 communicating with the three regions collects the dissolution auxiliary gas. In particular, due to the negative pressure or suction force provided when the second transport pipe 150 transports the solubilizing auxiliary liquid, the solubilizing gas in the air collecting conduit 160 is sucked into the gas-liquid mixer 165, and the second transport is performed. Mixing the solubilizing liquid in the tube 150 and gas-liquid mixing is performed. The solubilizing gas and the solubilizing liquid after the gas-liquid mixing are transported together into the main dissolving tank 120, and through the hot spring minerals M1, M2, and M3, the reaction is promoted to form hot spring water.

  In addition, the second flow rate control valve 175 on the first lateral transport pipe 170 is opened in order to prevent the flow rate of the dissolution auxiliary liquid transported to the main dissolution tank 120 by the second transport pipe 150 from being excessive. Then, the dissolution auxiliary liquid in the second transport pipe 150 is divided into the mixing tank 110 from the first horizontal transport pipe 170, whereby the flow rate of the dissolution auxiliary liquid flowing in the main dissolution tank 120 is adjusted.

  When the hot spring water in the storage tank 125 is thick (when the ion content in the hot spring water is high), the third flow control valve 185 on the second lateral transport pipe 180 is opened, and the hot spring water in the storage tank 125 is It is transported into the main dissolution tank 120 via the two horizontal transport pipes 180 and the second transport pipe 150, and again reacts with the hot spring minerals M1, M2, and M3. Finally, the hot spring water dissolved and reacted with the hot spring minerals M1, M2, and M3 again flows into the storage tank 125 through the third transport pipe 190.

  As described above, the hot spring water generation system of the present invention effectively increases the dissolution rate of hot spring minerals, and converts tap water into hot spring water that meets spring quality standards within a short time.

  The preferred embodiments of the present invention have been disclosed as described above. However, the present invention is not limited to these embodiments, and those skilled in the art will recognize various modifications and changes within the spirit and scope of the present invention. Modifications can be made, but it goes without saying that these are within the scope of the claims.

It is a top view of the hot spring water production | generation system of this invention. It is a three-dimensional view of the dissolution auxiliary tank and the water pressure adjusting device of the hot spring water generation system of the present invention.

Explanation of symbols

100 Hot Spring Water Generation System 105 Dissolution Auxiliary Tank 105a First Space 105b Second Space 105c Second Microflow Control Element 110 Mixing Tank 115 Water Source 120 Main Dissolution Tank 125 Hot Spring Water Storage Tank 130 Water Pressure Control Station 130a First Microflow Control Element 130b First outlet pipe 130c Second outlet pipe 135 First flow control valve 140 First transport pipe 145 Liquid level sensing element 150 Second transport pipe 155 Pump 160 Air collection pipe 165 Gas-liquid mixer 170 First lateral transport pipe 175 Second flow control valve 180 Second lateral transport pipe 185 Third flow control valve 190 Third transport pipe 195 Drain pipe 196 Output pipe B Porous bioballs M1, M2, M3 Hot spring mineral S Dissolving auxiliary substance

Claims (20)

A hot spring water generation system,
A solubilization tank containing at least one solubilizing substance; and
A mixing tank connected to the dissolution auxiliary tank;
It is connected to the dissolution auxiliary tank and the mixing tank, tap water is introduced into the dissolution auxiliary tank and the mixing tank to form a dissolution auxiliary agent, the dissolution auxiliary agent flows into the mixing tank, A water source mixed with tap water in a mixing tank to form a solubilizing solution;
A main dissolution tank that is connected to the mixing tank and contains at least one hot spring mineral, the dissolution auxiliary liquid of the mixing tank flows in, and reacts with the hot spring mineral to form hot spring water;
A hot spring water generation system comprising a storage tank connected to the main dissolution tank and storing hot spring water. Furthermore, it has a water pressure adjusting device connected between the dissolution auxiliary tank and the water source and installed on the dissolution auxiliary tank, and adjusts the flow rate of tap water flowing into the dissolution auxiliary tank. The hot spring water generation system according to claim 1. The water pressure adjusting device has a first micro flow control element, a first water discharge pipe, and a second water discharge pipe, the first micro flow control element is connected to the dissolution auxiliary tank, and the first water discharge pipe is It is located on the first micro flow control element and extends into the mixing tank, and the second drain pipe is located on the first drain pipe and extends into the mixing tank. The hot spring water generation system according to claim 2. The hot spring water generation system according to claim 3, wherein the first micro flow control element includes a filter membrane, a fiber filter cloth, or a precision ceramic plate. The hot spring water generation system according to claim 3, further comprising a first flow rate control valve that is installed on the first drain pipe and controls a flow rate of tap water flowing through the first drain pipe. The dissolution auxiliary tank has at least one first space and at least one second space, the first space is located on the second space, and stores the dissolution auxiliary substance, and the second space. 2 is connected to the mixing tank and contains a plurality of porous bioballs, and the dissolution aid flows into the mixing tank through the second space and the porous bioballs. The hot spring water generation system described. Furthermore, it has a first transport pipe connected between the second space and the mixing tank, and the solubilizing agent passes through the second space, the porous bioball, and the first transport pipe in the mixing tank. The hot spring water generation system according to claim 6, wherein The hot spring water generation system according to claim 6, wherein the dissolution auxiliary tank further includes at least one second micro flow control element installed between the first space and the second space. The hot spring water generation system according to claim 8, wherein the second micro flow control element includes a filter membrane, a fiber filter cloth, or a precision ceramic plate. The hot spring water generation system according to claim 1, wherein the mixing tank stores a plurality of porous bioballs. Further, the liquid level sensing element is installed in the hot spring water storage tank and electrically connected to the water source, and the liquid level sensing element senses the level of the hot spring water in the storage tank. The hot spring water generation system according to claim 1, wherein the water source is controlled to flow tap water into the dissolution auxiliary tank and the mixing tank. A second transport pipe and a pump; the second transport pipe is connected to the mixing tank and the main dissolution tank; the pump is connected to the second transport pipe; The hot spring water generation system according to claim 1, wherein the liquid is pumped by the pump and flows into the main dissolution tank through the second transport pipe. Furthermore, it has a gas collection conduit communicating with the main dissolution tank and the second transport pipe, the dissolution auxiliary gas generated by the main dissolution tank is collected by the gas collection conduit, along with the dissolution auxiliary liquid, The hot spring water generation system according to claim 12, wherein the hot spring water is transported from the second transport pipe into the main dissolution tank and reacts with hot spring minerals to form hot spring water. And a gas-liquid mixer connected between the gas collection conduit and the second transport pipe, and the dissolution auxiliary gas in the gas collection conduit and the dissolution auxiliary liquid in the second transport pipe The hot spring water generation system according to claim 13, wherein the hot spring water generation system is mixed. The hot spring water generation system according to claim 13, wherein the air collecting conduit extends into the mixing tank. 13. The method according to claim 12, further comprising a first horizontal transport pipe connected between the second transport pipe and the mixing tank, and adjusting a flow rate of the dissolution auxiliary liquid flowing in the main dissolution tank. Hot spring water generation system. The hot spring according to claim 16, further comprising a second flow rate control valve installed on the first horizontal transport pipe, wherein the flow rate of the dissolution auxiliary liquid flowing through the first horizontal transport pipe is controlled. Water generation system. The hot spring water generating system according to claim 12, further comprising a second horizontal transport pipe connected between the second transport pipe and the storage tank. The hot spring water generation system according to claim 18, further comprising a third flow rate control valve installed on the second lateral transport pipe. And a third transport pipe connected between the main dissolution tank and the storage tank, and the hot spring water in the main dissolution tank flows into the storage tank from the third transport pipe. The hot spring water generation system according to claim 1.

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