JP2005313158A - Hot spring water treating device removing solid substance such as sulfur oxide in hot spring water - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To provide a hot spring water treating device that suppresses a decrease in hot spring effect of a hot spring water, further, largely improves the reduction of works such as routine maintenance of conduit sections, plugs or the like in hot spring water facilities, the replacement costs of members and a running cost and is effective for the reduction of costs such as initial costs including a secondary effect of elongated endurance of devices and the running cost or the like. <P>SOLUTION: The hot spring water treating device comprises a precipitation tank 17, a retention tank 18 and a storage tank 19, the tank 18 is provided with a flow regulating plate 13 and a settling acceleration plate 14, solid matters are separated from the hot spring water in the tank 17 and tank 18, and the solid matters are discharged from outlets 15 provided at the bottoms of the tank 17 and tank 18. <P>COPYRIGHT: (C)2006,JPO&NCIPI

Description

The present invention relates to a hot spring water treatment apparatus that removes solid substances such as sulfur oxides, which are hot spring water-soluble substances, using a difference in specific gravity and a precipitation separation method.

Japanese Patent Application Laid-Open No. 2003-181488 (hereinafter referred to as Patent Document 1) “Solid-liquid separation of an aeration tank in which organic waste water is introduced and an aerobic biological treatment is performed with activated sludge, and a suspension sent from the aeration tank. In an organic wastewater treatment apparatus having a settling tank, a return means for directly or indirectly returning sludge precipitated in the settling tank to an aeration tank, and a dehydrator for extracting and dewatering a part of the returned sludge as excess sludge And a means for adjusting the amount of returned sludge when returning the sludge extracted from the settling tank to the aeration tank to be 1.5 to 10 times the amount of organic waste water, and surplus sludge extracted from the settling tank Claim of the organic waste water treatment apparatus, wherein the dehydrator for performing dehydration without adding a chemical effective for dehydration after concentration to an effective amount is a filter press type dehydrator having an electroosmotic function. Of FIG. Mounting there is.

Japanese Patent Laid-Open No. 2003-300077 (hereinafter referred to as “Patent Document 2”), “Inclination for separating and removing coarse solids S1 in wastewater W0 containing heavy metals, dioxins, and solids if shown with reference numerals in the drawings. Separator 1, precipitation tank 2 for precipitating fine solids S2 in waste water that has passed through the inclined separator 1, and liquid W1 in the precipitation tank 2 are introduced to insolubilize and flock heavy metal components in the liquid The reaction coagulation tank 3, the sedimentation separation tank 4 that settles and separates the floc F in the liquid sent from the reaction coagulation tank 3, and the suspended particles in the liquid are captured by passing through the liquid W2 of the sedimentation separation tank 4. Filter (cartridge filter) 5A, 5B, and an activated carbon adsorber 6 that adsorbs and separates harmful components in the liquid that has passed through the filter. The inclined separator 1 includes a wastewater inlet (introduction nozzle) 11. Leaning wastewater W0 supplied by Coarse solids that are guided to the channel 10 and flow down to the opening 20a of the sedimentation separation tank 2 disposed below through the trapezoidal water inlet 12 provided on the bottom surface of the ramp 10 and do not pass through the inlet 12 S1 is configured to be discharged from the lower end discharge port 13 of the ramp 10, and the reaction flocculation tank 3 includes a reaction tank portion 31 that performs a reaction with a chemical agent, and a flocculation tank portion 33 that performs flocking using a flocculant. There is a description example of FIG. 3 and FIG. 4 (paragraph 0007 of Patent Document 2).

Japanese Patent Application Laid-Open No. 2003-62410 (hereinafter referred to as Patent Document 3) states that “a casing, a filter medium that has flexibility and is provided sideways or obliquely in a slack state inside the casing, and the filter medium. Liquid supply means for supplying the treatment liquid to the lower side of the filter, drainage means for discharging the treatment liquid from the upper side of the filter medium, and sediment discharge means for discharging the solid substance filtered and precipitated by the filter medium; There is a description example of “a wastewater treatment apparatus characterized in that (paragraph 0014 of Patent Document 3)”.

JP 2003-181488 A JP 2003-300077 A JP 200362410 A

However, Patent Document 1 performs an aerobic biological treatment of organic wastewater with activated sludge, solid-liquid separation in a sedimentation tank, returns the precipitated sludge directly or indirectly to the aeration tank, and extracts a part thereof as sludge for dehydration treatment. This is an organic wastewater treatment method, in which treated water is discharged from the upper part of the tank and aerated from the bottom of the tank, and the connecting tank is simply shielded by a wall, and the precipitate cannot be separated.

Patent Document 2 is a wastewater treatment apparatus that separates and removes coarse solids in wastewater containing heavy metals and dioxins and solids, and precipitates and separates fine solids in wastewater and flocates with a flocculant. The waste liquid overflowed from the upper layer is drained by a pump, further agglomerated, and the supernatant of the sedimentation tank is drained, so a drainage device such as a pump is required and can be applied to hot spring water. Can not.

Patent Document 3 is a wastewater treatment apparatus that removes suspended solids from wastewater and can produce clean water, and is a wastewater treatment apparatus that adds a flocculant to the backwashing operation of the filter medium and the treatment liquid. However, the flow rate cannot be adjusted by these tanks. Cannot be applied to hot spring water because of the filtering material.

The present invention suppresses a decrease in hot spring effect of hot spring water. In addition, the initial cost including secondary effects such as the release of pipes and plugs for hot spring water facilities from daily maintenance work, the cost of replacing parts, running costs, etc., and the durability of the equipment will increase. An object of the present invention is to provide a hot spring water treatment apparatus that is effective in reducing costs such as running costs.

The present invention constitutes a sedimentation separation tank, a stagnation tank, and a storage tank, and the hot spring water treatment method by the control mechanism of the rectifying plate and the sedimentation promotion plate and the sedimentation separation mechanism by the specific gravity difference also inhibits the hot spring effect that is the point. The original purpose was realized.

The treatment method of the hot spring water according to the present invention is a precipitation separation method based on a difference in specific gravity, which is a method that removes dissolved substances and solids in the hot spring water, increases the purification degree of the hot spring water, and does not inhibit the hot spring effect.
The hot spring water treatment apparatus used in the present invention is a thing using a precipitation separation method based on a difference in specific gravity, and specifically comprises a precipitation separation tank, a stagnation tank, and a storage tank, and includes a partition tank shape. It is. The hot spring water treatment of the invention is characterized in that the treatment effect is enhanced by the device of the shape of the partition tank.

The hot spring water treatment apparatus of the present invention includes a sedimentation tank, a stagnation tank, and a storage tank. The hot spring water treatment apparatus of the present invention includes an inflow pipe, a rectifying plate, a precipitation promoting plate, a communication valve, a communication pipe, an overflow pipe, a vent pipe, a discharge port, and a suction port. The present invention includes a constant flow valve, a ball tap, and an in-tank level gauge.

Moreover, the hot spring water treatment apparatus of this invention contains a sedimentation tank, a stagnation tank, a storage tank, and a baffle plate as a processing tank. For example, a hot spring water treatment apparatus including a first tank sedimentation tank, a second tank stagnation tank, a third tank storage tank, and three tanks is also the present invention. The hot spring water treatment apparatus of the present invention includes a rectifying plate having a flow path in the lower part between the sedimentation separation tank and the stagnation tank and a precipitation promoting plate having a flow path in the middle upper part of the stagnation tank.
Furthermore, the hot spring water treatment apparatus of the present invention includes a discharge port through which solid matter such as sulfur oxides and / or inorganic matter precipitated in the lower part of the sedimentation tank and the lower part of the stagnation tank, and part of the liquid is discharged together with the solid liquid. . The lower part of the rectifying plate and the bottom surface provided between the settling tank and the stagnation tank, the upper part of the precipitation promoting plate provided in the middle of the stagnation tank, the effective water level interval, and the rectifying plate provided between the stagnation tank and the storage tank The hot spring water treatment apparatus according to the present invention also includes an interval between the upper portion and the effective water level that includes a difference in specific gravity of solids containing sulfur oxides, a sedimentation speed, and a stagnation time.

In addition, the flow path interval at the bottom of the rectifying plate provided in the precipitation separation tank constituting the treatment tank is set to 1/10 to 1/15 of the effective water level of the treatment tank, and the height of the precipitation promoting plate provided in the stagnation tank is set. The treatment device for hot spring water with the height of 1/4 to 1/5 of the effective water level of the treatment tank and the height of the rectifying plate dividing the stagnation tank and the storage tank to 1/2 to 3/4 of the effective water level of the treatment tank It is.
The position and size of the two outlets provided at the bottom of the treatment tank are provided at the bottom of the rectifying plate that divides the sedimentation separation tank and the stagnation tank, and the bottom is 1/100 to 1/50 toward the outlet. Provide a slope, provide a discharge port with a diameter corresponding to the capacity of the treatment tank and the amount of sediment deposited as the size of the discharge port, and the discharge port at the bottom of the rectifying plate that divides the stagnation tank and the storage tank It is also a hot spring water treatment device.
A communication pipe and a communication valve provided between the stagnation tank and the storage tank constituting the treatment tank are provided, and when a large amount of hot spring water in the storage tank is released, a device for temporarily supplying the shortage from the stagnation tank What has is also the hot-water treatment apparatus of the present invention.

The hot spring water treatment method of the present invention uses a stainless steel / plastic material which is a material having corrosion resistance, rust prevention, heat resistance, acid resistance, etc. in the final tank storage tank of the hot spring water treatment tank, heat exchange. A heating pipe having a function is installed, and the temperature of the hot spring water is controlled by flowing the hot spring water from the source into the heating pipe and leading it to the first tank settling tank.
The hot spring water treatment apparatus of the present invention uses a stainless steel / plastic material that is a material having corrosion resistance, rust resistance, heat resistance, acid resistance, etc. in the final tank storage tank of the hot spring water treatment tank, heat exchange. A heating pipe having a function and a device for controlling the temperature of the hot spring water by flowing the hot spring water from the source into the heating pipe and leading to the first tank settling tank are inserted.

As described above, according to the present invention, the hot spring water treatment apparatus capable of meeting the demands of the market eliminates the plugging of the faucets and sufficiently fulfills the function of the facility.
In addition, it eliminates the need for routine maintenance of pipes and plugs, and there is no need to replace filter media, so running costs are greatly improved, and running costs including secondary effects that increase the durability of equipment are included. This is a tenth and a significant cost reduction.
The sulfur oxides contained in the hot spring water were completely removed, the purification of the hot spring water was increased, and the original purpose was achieved without hindering the hot spring effect.

After investigating the actual conditions of hot spring water facilities,
a) The inside of the stopper was completely covered with “Yu no Hana”.
b) The bent part of the pipe and the connecting part with the appliances are “yuhana” and there is almost no gap.
c) “Yuna no Hana” accumulates on the edge of the bathtub and the open-air bath, and in the washing area, and a large amount of water erupts at the bottom.

Since the pipes and faucets of the hot spring facilities of the resort hotel hot springs that are 6 months old are clogged, it is necessary to take the following measures to remove hot water.
a) No cost b) Easy maintenance c) Durable d) Don't change the quality of hot springs

In consideration of the above issues, the hot spring flower removal and the facilities were examined. First, the existing hot spring facilities in Kagoshima Prefecture were surveyed and the quality of the hot springs was analyzed. Some hot springs were not corrosive to some extent depending on the quality of the springs, and there were no special facilities. However, as a pretreatment, the existing hot springs generally use sand filters, diatomaceous earth. Filters, cartridge filters, etc. are used, and as a hot spring water treatment measure, a removal method using a filter medium is used. In the surveyed area, no effective hot water removal device has yet been found as a hot water removal measure.

Next, we requested the Kagoshima Prefectural Environmental Technology Association to analyze the quality of the hot spring. In the spring quality test, as a result of analysis by various methods such as microscopic observation, combustion test, and fluorescent X-ray analysis, it was estimated that the mineral was mainly used. When measured by fluorescent X-ray analysis, it was found that inorganic substances such as sulfur, silicon, aluminum and calcium were contained, and in particular, 35 wt% of sulfur was contained. When this result is converted into the form of sulfur trioxide, it is actually 87 wt%.
In addition, because it is a fumarole molded hot spring that is created by injecting hot spring fumarole into the water during the hot spring water creation process, it is a liquid that is formed by absorbing sulfur contained in the hot spring fumarole and has a yellow fluidity. There was also a sulfur element with a structure in which a certain element of sulfur (called lambda sulfur) was linked or entangled. From the above results, the hot spring water is very hot and solid, and is corrosive at high temperatures.

In order to examine the treatment method for the solid matter or the deposit of soluble inorganic matter, hot spring water was placed in a container and allowed to stand for 40 minutes. As a result, precipitation separation was confirmed.
Therefore, it was confirmed that soluble minerals containing solids by precipitation separation due to specific gravity differences were removed, and hot spring water was further stored, and solid substances were included by precipitation separation methods based on specific gravity differences based on the above matters. Worked on the development of a device for removing dissolved substances.
The treatment method of the hot spring water is to achieve the original purpose without obstructing the hot spring effect as a point. A schematic diagram of a hot spring water treatment method and an apparatus according to one embodiment of the present invention is shown in FIG.

In FIG. 1, 11 is hot spring water flowing into the treatment tank, 20 is a constant flow valve for adjusting the amount of hot spring water inflow to a constant flow rate, and 12 and 25 are inlets that flow into the first tank settling tank constituting the treatment tank. , 28 is a treatment tank, 17 is a sedimentation tank that precipitates and separates the hot spring water that has flowed in, 15 is a sedimentation tank, a discharge port that discharges a sediment containing part of the stagnation tank 18a, and 27 is a discharge of sediment from the discharge port. The discharge valve 13a is a rectifying plate that makes the hot spring water flowing into the settling tank a constant flow.

In FIG. 1, reference numeral 24 denotes an air vent 21 through which air / evaporated air separated in the treatment tank is released is an overflow port of the entire tank.
In FIG. 1, reference numeral 14 denotes a precipitation promoting plate for accelerating precipitation in a settling tank including solid matter and a rectifying plate in hot spring water that has not been removed in the settling tank and has flowed into the stagnation tank, and 18 a is a stagnation. A flow tank, 18b is a part of a stagnation tank, and 21 is an overflow port of the entire treatment tank.

In FIG. 1, reference numeral 14 denotes a precipitation promoting plate that promotes precipitation by retaining the solid matter of hot spring water that has flowed into the stagnation tank without being removed in the precipitation separation tank.
In FIG. 1, 19 is a storage tank which stores the processed hot spring water which comprises a processing tank. 23 and 26 are communications for temporarily replenishing the storage tank with the hot spring water in the stagnation tank when the balance between the hot spring water flowing into the settling tank and the hot spring treatment water in the storage tank is lost due to usage conditions. The valve 26 and the communication pipes 23 and 16 are pumps or a suction port under natural flow, and 22 is a tank level gauge.

In FIG. 2, a discharge port 15 and a discharge valve 27 for discharging solid matter containing sulfur oxides and the like separated and precipitated in the sedimentation tank bottom 17 and the stagnation tank bottom part 18a are provided directly below the rectifying plate 13a, and the sedimentation tank bottom and A solid substance containing sulfur oxides and the like separated and precipitated in a part of the bottom part of the turbulent tank surrounded by the precipitation promoting plate 14 is discharged.

In FIG. 3, the discharge tank 15 and the discharge valve 27 for discharging the solid matter containing the sulfur oxide substance separated and settled on the bottom part 18b of the stagnation tank surrounded by the precipitation promoting plate 14 and the bottom part of the storage tank are directly below the rectifying plate 13b. The solid matter containing sulfur oxides separated and precipitated at the bottom part of the stagnation tank surrounded by the precipitation promoting plate 14 and the bottom part of the storage tank is discharged.

In FIG. 4, when the balance between the hot spring water flowing into the settling tank and the hot spring treatment water in the storage tank is lost due to the usage situation, the hot spring water in the stagnant tank is temporarily replenished into the storage tank. A communication valve 26 and a communication pipe 23.

In FIG. 5, it is the experiment tank used before performing Example 1. FIG. With reference to the hot spring water analysis table, paying attention to the specific weight of the components, hot spring water was stored in the test tank, and the state of solid matter containing sulfur oxides in the hot spring water was observed. After a while, a part of the solids in the hot spring water began to separate and settled, and volumeed on the bottom of the experimental tank. After storage, about 10 minutes were separated and settled, and solids in the hot spring water were deposited approximately 100% in about 120 minutes.

Based on the above experimental results, various modes were assumed and simulations were made. Table 1 shows the relationship between the amount of inflow and the amount of use, the size of the tank, the stagnation time, and the amount of storage.

Hereinafter, embodiments of the hot spring water treatment apparatus according to the present invention will be described with reference to the drawings.
In designing this facility, we aim for 100% removal of solids such as hot spring flowers based on the conditions such as the supply of hot spring water of 40 l / min, the existing facility for the bathtub, and the actual number of employees (50 people / person). The treatment tank shown in FIG. 1 was designed. In FIG. 1, the hot spring water treatment apparatus is made of stainless steel having a width of 1 m, a height of 2.5 m, and a depth of 2.5 m, and has a volume of 6.25 m ³ and an effective volume of 5.0 m ³ . The flow rate in the tank was 0.05 m / min, and the stagnation time was 240 minutes.

The items that were devised in the development of hot spring water treatment equipment were confirmed by checking the temperature effect in the design of the hot spring water treatment equipment, reducing the facility installation management costs, achieving the purpose of removing solids such as certain hot spring flowers, The followings were devised to make clean hot spring water without change.
To enhance the precipitation separation effect, make the hot water flow as static as possible. Therefore, the hot spring water treatment tank was divided into three tanks, and a current plate was installed between them. The flow straightening plate between the first and second tanks is provided with a gap of 200 mm at the bottom, and between the second and third flow straightening plates up to a height of 400 mm below the inlet water level. A precipitation promoting plate was provided in the second tank to make the initial flow static.

The flow path interval below the rectifying plate provided in the treatment tank first tank precipitation separation tank is set to 1/10 to 1/15 of the treatment tank effective water level. Moreover, the height of the precipitation acceleration | stimulation board provided in the 2nd tank stagnation tank shall be 1 / 4-1 / 5 of a processing tank effective water level. The height of the rectifying plate that divides the second tank stagnation tank and the third tank storage tank is set to 1/2 to 3/4 of the effective water level of the processing tank.

Next, in the hot spring water treatment tank, the first tank was a precipitation separation tank, the second tank was a stagnation tank, and the third tank was a storage tank.
In order to precipitate almost all solid substances and dissolved substances in the settling tank, a rectifying plate was installed at the bottom to make the inflow of hot spring water a static flow, and a device was devised to enhance the precipitation effect of dissolved substances and solid substances.
The rectifying plate between the second tank and the third tank was installed higher in the upper direction than in the lower part. This is because the flow in the first tank and the second tank is rectified, the stagnation time is lengthened, and the precipitation in the first tank and the second tank is promoted.
Hot spring water flowing into the third tank overflows the upper part of the current plate between the second tank and the third tank, is stored in the third tank, and is supplied to the facility from the suction port by a natural flow or the like. The

The feature of this hot spring water treatment installation is the shape of the partition tank in order to efficiently remove dissolved substances and contained substances in the hot spring water.
In order to prevent temporary shortage of hot spring water in the storage tank at the start of use of the treated hot spring water, a connecting pipe is provided in two stages between the stagnant tank and the storage tank, and it is opened and closed appropriately. Open and close according to usage. This is an emergency, and it is not necessary to open and close because it is usually designed in consideration of supply and usage.

The hot spring water that flows into the hot spring water treatment tank is initially assumed to be laminar, turbulent, or complex flow, and the flow of the hot spring water is rectified by the flow straightening plate in the settling tank. Separation starts due to the difference in specific gravity, and substances heavier than hot spring water settle down. The hot spring water that contains a part of the substance passes through the lower flow path of the rectifying plate and the flow is partially changed by the sedimentation promoting plate in the turbulence tank, and the remaining material in the remaining hot spring water is separated into the lower part. Precipitate. As the flow progresses, the hot spring water overflows the upper part of the sedimentation promotion plate, and the flow is blocked by the rectifying plate between the stagnation tank and the storage tank. Further, it is separated, and the vapor or the like is separated here and released from the vent pipe into the atmosphere.
Completely purified hot spring water overflows the upper part of the current plate and is stored in the storage tank.

The deposits containing the hot spring water were analyzed using fluorescent X-rays. The results are shown in Table 2.

実験用温泉水処理装置の実施例を図１に示す。

An embodiment of the experimental hot spring water treatment apparatus is shown in FIG.

In FIG. 1, it is an example hot spring water treatment apparatus manufactured to remove using a precipitation separation method based on a difference in specific gravity, focusing on the fact that deposits containing sulfur oxides are heavier than hot spring water as a result of analysis according to Table 1. .
[Comparative Example 1]

In FIG. 5, as a result of an actual experiment using hot spring water in an experimental hot spring water treatment apparatus not provided with a current plate, there is a need for room for improvement due to incomplete removal of deposits containing sulfur oxides by precipitation separation. there were.

The position and size of the two outlets provided at the bottom of the treatment tank are provided in the center of the bottom just below the rectifying plate that divides the precipitation separation tank and the stagnation tank, and the bottom opening is 1/100 to 1/50 toward the outlet. The size of the outlet for providing the gradient depends on the capacity of the treatment tank and the amount of sediment deposited, but an outlet having a diameter of 100 mm to 150 mm is provided. The same applies to the outlet directly under the current plate that divides the second tank stagnation tank and the third tank storage tank.

The treatment apparatus of the present invention is provided with a rectifying plate, a precipitation accelerating plate, a discharge port, a connecting pipe and the like inside the tank, and passes the flow of hot spring water in the tank up and down. It is a hot spring water treatment device having a function of allowing a direct discharge treatment through two discharge ports provided in the center of the bottom, with a partition tank shape that changes the height of the promotion plate. Table 3 shows the results of analyzing the treated hot spring water. It was the same as the result of the component analysis of the supernatant liquid naturally settled. Substances containing sulfur oxides removed by precipitation separation were analyzed using fluorescent X-rays. The results are shown in Table 4.

The treatment apparatus of Example 1 was manufactured as an experimental model (1/200), and an experiment for removing iron and manganese from hot spring water was newly conducted.

During the six months from October 2004 to March 2005, the height of the tank partition plate was adjusted and aeration was repeated. In the Example performed initially, aeration which blows air in a 1st tank sedimentation tank was performed. The iron precipitation was promoted by aeration. A little effect was seen on iron and almost no effect on manganese.

Table 5 below shows the results of experiments for removing iron and manganese from both hot spring water and non-executed hot spring water.

Tables 6 and 7 below show the modes of changes in the height, stagnation time, and storage time of the tank partition plates where aeration is not performed.

実験結果を下記表８に示す。

The experimental results are shown in Table 8 below.

A mesh (φ40) is attached to the treatment tank first tank precipitation tank inlet, and the results of the precipitation removal rate of iron and manganese in the hot spring water are shown in Table 9 below.

As a result of experiments such as aeration and mesh attachment, there was almost no change in the removal rate of iron and manganese. In particular, it was proved that 70% of iron was removed by proper time allocation of the stagnation time and the storage time.

It is a front view of the Example hot spring water treatment apparatus of this invention. It is sectional drawing of the discharge port which discharges | emits the sediment of a sedimentation tank of a hot spring water treatment apparatus of this invention, and a partial stagnation tank. It is sectional drawing of the discharge port which discharges the sediment of the stagnation tank part and storage tank of the hot spring water treatment apparatus of this invention. It is a connecting pipe front view which connects the stagnant tank and storage tank of this invention. It is a front view of the comparison figure of this invention Example.

Explanation of symbols

DESCRIPTION OF SYMBOLS 11 Hot spring water 12 Ball tap port 13a Current plate 13b Current plate 14 Precipitation plate 15 Discharge port 16 Suction port 17 First tank settling tank 18 Second tank spill tank 18a Spill tank part 18b Stagnation tank part 19 3rd Tank storage tank 20 Constant flow valve 21 Overflow port 22 In-tank liquid level gauge 23 Communication pipe 24 Vent 25 Inlet 26 Communication valve 27 Discharge valve 28 Treatment tank

Claims (10)

The hot spring water in which solids precipitate is introduced into the first tank settling tank, which is a treatment tank, and subjected to precipitation separation treatment due to the difference in specific gravity. Further, the hot spring water partially containing solids is precipitated and separated in at least one stagnant tank. A treatment method for hot spring water to be treated and stored in at least one storage tank, wherein the bottom of the precipitation separation tank, the bottom of the stagnation tank, and a solid substance containing a partial liquid precipitated on the bottom of the storage tank is provided at the bottom. The hot spring water treatment method is characterized in that the solid-liquid separation treatment is carried out. The method for treating hot spring water according to claim 1, wherein a flow regulating plate for controlling the flow of hot spring water is provided in the settling tank and the stagnation tank, and the function of promoting precipitation separation is provided. 2. A function of accelerating sedimentation separation by providing a sedimentation promoting plate for controlling the flow of hot spring water flowing into the stagnation tank through the lower flow path of the rectifying plate provided in the sedimentation tank to promote precipitation separation. The method for treating hot spring water according to claim 2. Predict that sediment containing solids discharged from the bottom outlet will be 30-50mm, and then discharge at intervals of 2 to 3 days, and aim for the same color as the hot spring color as the amount discharged at once from the outlet The method for treating hot spring water according to any one of claims 1 to 3. The hot spring water that overflowed the sedimentation promotion plate that controls the flow of hot spring water flowing into the stagnation tank was provided with a separation plate that divides the stagnation tank and the storage tank into a rectifying plate, and the precipitation promotion plate overflowed The hot spring water treatment method according to any one of claims 1 to 4, wherein the hot spring water is completely precipitated by causing the hot spring water to stay in the stagnation tank again with a current plate. The flow path interval below the rectifying plate provided in the precipitation separation tank constituting the treatment tank is set to 1/10 to 1/15 of the treatment tank effective water level, and the height of the precipitation promoting plate provided in the stagnation tank is set to The processing tank effective water level is set to 1/4 to 1/5, and the height of the rectifying plate dividing the stagnation tank and the storage tank is set to 1/2 to 3/4 of the processing tank effective water level. The hot spring water treatment device described in Crab. The position and size of the two outlets provided at the bottom of the treatment tank are provided at the bottom of the rectifying plate that divides the sedimentation separation tank and the stagnation tank, and the bottom is 1/100 to 1/50 toward the outlet. Provide a slope, provide a discharge port with a diameter corresponding to the capacity of the treatment tank and the amount of sediment deposited as the size of the discharge port, and the discharge port at the bottom of the rectifying plate that divides the stagnation tank and the storage tank The processing apparatus for hot spring water according to any one of claims 1 to 6. A communication pipe and a communication valve provided between the stagnation tank and the storage tank constituting the treatment tank are provided, and when a large amount of hot spring water in the storage tank is released, a device for temporarily supplying the shortage from the stagnation tank The treatment apparatus for hot spring water according to any one of claims 1 to 7. In the final tank storage tank of the hot spring water treatment tank, a heating tube with a heat exchange function that uses stainless steel and plastic materials, which have corrosion resistance, rust prevention, heat resistance, acid resistance, etc., is installed. The temperature of the hot spring water is controlled by flowing the hot spring water from the source into the heating pipe and leading it to the settling tank of the first tank. Processing method. A heating tube with a heat exchange function that uses a stainless steel or plastic material that has corrosion resistance, rust prevention, heat resistance, acid resistance, etc. in the final tank storage tank of the hot spring water treatment tank, and this heating An apparatus for controlling the temperature of hot spring water by inserting hot spring water from the source into the pipe and leading it to the settling tank of the first tank is inserted into the pipe. Hot spring water treatment equipment.

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