TW201718413A - Device for producing eluted functional water containing mineral component, and method of producing eluted functional water - Google Patents

Abstract

A technique is provided for easily and stably producing eluted functional water which has a beneficial effect by containing a prescribed mineral component. This eluted functional water producing device 100 is provided with a first treatment tank 110 and a second treatment tank 150 arranged in series in the vertical direction, a water supply tube 117 which supplies water to the first treatment tank 110, a linking passage 158 which links the first treatment tank 110 and the second treatment tank 150, and a water discharge passage 153 for discharging eluted functional water formed in the second treatment tank 150. The first treatment tank 110, positioned above, houses an elution-type ceramic that has a mineral component having an electromagnetic wave-emitting action immobilized in an elutable manner, and the second treatment tank 150, positioned below, houses a non-eluting-type ceramic that contains, in a non-elutable manner, a mineral component having an electromagnetic wave-emitting action.

Description

Manufacturing device for melting functional water containing mineral component and method for producing soluble functional water

The present invention is based on the Japanese Patent Application No. 2015-173941, Japanese Patent Application No. 2015-173942, and Japanese Patent Application No. 2015-173943, which are incorporated herein by reference. All contents of the special purpose 2015-173941, Japan's special wish 2015-173942, and Japan's special wish 2015-173943 are used in this case.

The present invention relates to a manufacturing technique for dissolving functional water containing a mineral component having beneficial effects.

In water containing mineral components, there is a possibility of effects such as soil modification, plant growth, decomposition of harmful chemicals, deodorization, air purification, etc. In the past, various mineral-containing waters and Mineral water manufacturing equipment was developed.

The inventors of the present invention have developed a mineral-containing water producing apparatus (A) including a conductive wire coated with an insulator and a mineral-imparting material (A) immersed in water to conduct a direct current to the conductive wire. Conductive in the foregoing The water around the line generates a water flow in the same direction as the DC current, imparts ultrasonic vibration to the water to form a raw material mineral aqueous solution (A), and irradiates far infrared rays to the formed raw mineral aqueous solution (A) to form The far infrared ray generating means of the mineral-containing water (A) (refer to Patent Document 1).

Further, the inventors of the present invention have also developed a mineral water manufacturing facility comprising a mineral water-containing water producing device (A) and a mineral-containing water producing device (B), and the mineral water-containing water producing device (B) And a plurality of water-passing containers filled with mineral material-imparting materials (B) having different types; and a water-feeding path in which a plurality of the water-passing containers are connected in series; and in a state in which a plurality of the water-passing containers are juxtaposed a bypass water passage connected to the water supply path; and a water flow switching valve provided in a branching portion of the water supply path and the bypass water passage (refer to Patent Document 2). Further, it is described that when the mineral water-producing equipment is used, it is possible to produce mineral functional water (far-infrared-generated water) having a function of generating far-infrared rays having a characteristic wavelength.

In addition, in the apparatus described in Patent Document 2, the types and blending ratios of the raw materials (mineral imparting materials) used in the mineral-containing water producing apparatuses (A) and (B) are complicated. In the meantime, it is not possible to know which kind of mineral-based material to be used, and it is possible to obtain mineral-functional water which has an effect. However, the inventors of the present invention used the mineral-functional water-making apparatus disclosed in Patent Document 2, As a result of the review, the mineral functional water produced under certain conditions has excellent pest control effects against single-celled organisms and viruses (Patent Document 3) and the body. Activation (Patent Document 4), combustion promotion of hydrocarbons (Patent Document 5), and resistance Oxidation (Patent Document 6) and the like.

[Advanced technical literature]

[Patent Literature]

[Patent Document 1] Japanese Patent No. 4817817

[Patent Document 2] Japanese Laid-Open Patent Publication No. 2011-56366

[Patent Document 3] WO2016/043213

[Patent Document 4] WO2016/043214

[Patent Document 5] PCT/JP2016/058141

[Patent Document 6] PCT/JP2016/058362

The manufacturing apparatus described in Patent Document 2 is suitable for producing a useful mineral water, but has a complicated structure, a large size, and is not easily moved. Therefore, it is desirable to be able to develop a manufacturing apparatus that manufactures a miniaturization of beneficial function water in a simpler configuration.

Accordingly, it is an object of the present invention to provide a technique for easily and stably producing functional water having beneficial effects by containing a mineral component.

The present invention provides the following techniques.

<1> A device for producing a leaching machine water, which is a device for producing a leaching machine water containing a mineral component, comprising: two or more treatment tanks, wherein the treatment tank has a water inlet path and a water outlet a path for internally flowing water flowing from the water inlet path or an extraction solvent mainly composed of water toward the water outlet path; and a connection path connecting the water outlet path of one of the treatment tanks to the water inlet path of the other treatment tank The two or more treatment tanks are connected in series via the connection path, and at least one of the treatment tanks contains a dissolution type ceramic material in which a mineral component is immobilized in a soluble manner.

The manufacturing apparatus according to the above <1>, wherein the manufacturing apparatus is provided with a water injection path that communicates with the processing tank in which the eluted ceramic material is accommodated.

(3) The manufacturing apparatus according to the above-mentioned <1> or <2>, wherein the processing tank other than the processing tank in which the eluted ceramic material is accommodated contains a mineral component which is immobilized without elution. Non-lead-type ceramic material.

(4) The manufacturing apparatus according to the above-mentioned <3>, wherein at least one of the treatment tanks in which the elution-type ceramic material is accommodated is disposed in a treatment tank in which the non-lead-type ceramic material is accommodated. Upstream side.

<5> The manufacturing apparatus according to <3> or <4>, wherein the two processing tanks are connected in series via the connecting path.

(6) The manufacturing apparatus according to the above [5], wherein the processing tank located on one of the upstream sides of the connecting path is disposed in the foregoing The other side of the processing tank is at a higher position.

The production apparatus according to the above-mentioned <5> or <6>, wherein the water discharge path of the processing tank located on the downstream side of the connection path is provided at the uppermost portion of the processing tank.

<8> A method for producing a water for emulsification, which is characterized in that, in the production apparatus according to any one of the above items <1> to <7>, water or water-based extraction solvent is supplied. And a process of contacting water or a water-based extraction solvent with the aforementioned dissolution-type ceramic material of one of the treatment tanks contained in the treatment tank.

<9> A method for producing a water for emulsification, which is characterized in that, in the manufacturing apparatus described in any one of the above <3> to <7>, water or water-based extraction solvent is supplied. And a process of bringing water or a water-based extraction solvent into contact with the eluted ceramic material and the non-lead-type ceramic material of one of the treatment tanks contained in the treatment tank.

<10> The method for producing a functional water according to the above <9>, which further comprises the following process, and even if water or an extraction solvent mainly composed of water is contacted with the eluted ceramic material, and then eluted A process in which a ceramic material is contacted with water or a water-based extraction solvent is contacted with a non-lead-type ceramic material.

The production method according to any one of the above <5> to <7>, wherein the manufacturing apparatus according to any one of the above <5> to <7> is used.

According to the present invention, it is possible to provide a technique for easily and stably producing a solvent-soluble water having a beneficial effect from a mineral component eluted from a ceramic material holding a mineral component.

1‧‧‧Mineral functional water manufacturing equipment

2‧‧‧Mineral water (A) manufacturing equipment

3‧‧‧Mineral water (B) manufacturing equipment

10‧‧‧Methods for the production of raw materials and mineral aqueous solutions

11, W‧‧‧ water

12‧‧‧ Mineral Substance (A)

13‧‧‧Reaction container

13a‧‧‧ wall

14‧‧‧Insulator

15‧‧‧Flexible wire

16‧‧‧Ultrasonic generation means

17‧‧‧DC power supply unit

18a, 18b, 18c‧‧ cycle path

19‧‧‧Drainage

20, 23‧‧‧ opening adjustment valve

21, 25‧‧‧Drain valve

22‧‧‧ housing trough

24‧‧‧Drainage pipe

26‧‧‧Water temperature meter

29,29a~29g, 29s, 29t‧‧‧ conductive cable

30‧‧‧ Terminal

31‧‧‧ storage container

31f‧‧‧ hook

40‧‧‧Processing container

41‧‧‧ Raw material mineral aqueous solution (A)

42‧‧‧Agitating blades

43‧‧‧ far infrared ray generation means

44‧‧‧ Mineral water (A)

45‧‧‧ Mineral water (B)

46‧‧‧ mixing tank

47‧‧‧Mineral functional water

51‧‧‧1st water container

51a~56a‧‧‧ Body Department

51b~56b‧‧‧Switch button

51c~56c‧‧‧Axis

51d~56d‧‧‧ cover

51f~56f‧‧‧Flange

51m~56m‧‧‧ Mineral Substance (B)

51p~56p‧‧‧迂回回路

51v~56v‧‧‧Water flow switching valve

52‧‧‧2nd water container

53‧‧‧3rd water container

54‧‧‧4th water container

55‧‧‧5th water container

56‧‧‧6th water container

57, 57x, 57y‧‧‧ water supply path

57a‧‧‧ Inlet

57b‧‧‧Water outlet

57c‧‧‧Filter

57d‧‧‧Automatic air valve

58‧‧‧Operation panel

59‧‧‧Signal cable

60‧‧‧ 台台

61‧‧‧ casters

62‧‧‧Level adjuster

63‧‧‧ original sink

100‧‧‧Soliding machine water manufacturing device (double treatment tank)

110‧‧‧First treatment tank

111, 151‧‧‧ shell

111a, 111b, 151a, 151b‧‧‧Flange

111x‧‧‧Upper space

111y‧‧‧low space

112, 152‧‧‧ water path

112a, 153a‧‧‧ openings

113,153‧‧‧Water path

114‧‧‧Water injection path

114a‧‧‧Upper opening

114b‧‧‧Bottom opening

115,116,155,156‧‧‧ cover

117‧‧‧Water supply pipe

118‧‧‧ next door

118a‧‧‧through hole

119‧‧‧Drainage path

120,154b‧‧‧Opening valve

121‧‧‧Float

122‧‧‧ Arm

125‧‧‧ pillar

150‧‧‧Second treatment tank

154a‧‧‧Operation lever

155a‧‧‧ below

157‧‧‧ casters

158‧‧‧Link path

159‧‧‧Outlet

160‧‧‧Soliding machine water manufacturing device (three treatment tanks)

170‧‧‧Soliding machine water manufacturing device (parallel double treatment tank)

160A~160C, 170A~170C‧‧‧Processing tank

162,172‧‧‧Water path

163,173‧‧‧Water path

167,177‧‧‧Water supply pipe

168, 178‧‧‧ link path

169,179‧‧‧Outlet

B‧‧‧ bubble

C1‧‧‧Solidized ceramic materials

C2‧‧‧ Non-leolysis ceramic materials

DC‧‧‧ DC current

DW‧‧‧ tap water

G‧‧‧ Ground

N‧‧‧ water-permeable bag body

P‧‧‧ cushion

R‧‧‧Water flow

W1‧‧‧Solution water

W2‧‧‧Solution water

W3‧‧‧Solution water

Fig. 1 is a front elevational view showing a device for producing a melt-dissolving water (double treatment tank) according to an embodiment of the present invention.

Fig. 2 is a partially cutaway front elevational view showing the vicinity of a first treatment tank constituting the apparatus for producing a solvable water shown in Fig. 1.

Fig. 3 is a partially cutaway front elevational view showing the vicinity of a second treatment tank constituting the apparatus for producing a solvable water shown in Fig. 1.

Figure 4 is a partial enlarged view of the second processing tank shown in Figure 3.

Fig. 5 is a schematic view showing another structure (three treatment tanks) of the apparatus for producing a water soluble in the present invention.

Fig. 6 is a schematic view showing another structure (parallel double treatment tank) of the apparatus for producing a solvable water of the present invention.

Fig. 7 is a block diagram showing the schematic structure of a mineral water manufacturing facility.

Fig. 8 is a schematic view showing a part of a mineral-containing water (A) manufacturing apparatus which constitutes the mineral-functional water producing apparatus shown in Fig. 7, that is, a means for producing a mineral-containing aqueous solution.

Figure 9 is a partially omitted cross-sectional view taken along line A-A of Figure 8.

Figure 10 is a diagram showing the use of a raw material mineral aqueous solution as shown in Figure 8. A perspective view of the storage container of the mineral material (A) of the manufacturing means.

Fig. 11 is a perspective view showing a reaction state in the vicinity of a conductive wire of the raw material mineral aqueous solution manufacturing means shown in Fig. 8.

Fig. 12 is a schematic cross-sectional view showing a far infrared ray irradiation apparatus which is a part of the apparatus for producing mineral water (A) constituting the mineral water manufacturing apparatus shown in Fig. 7.

Fig. 13 is a block diagram showing a manufacturing apparatus for mineral-containing water (B) constituting the mineral-functional water producing apparatus shown in Fig. 7.

Fig. 14 is a front elevational view showing the apparatus for producing mineral-containing water (B) constituting the mineral-functional water producing apparatus shown in Fig. 7.

Fig. 15 is a side view showing the apparatus for producing mineral-containing water (B) shown in Fig. 14.

Fig. 16 is a partially omitted perspective view showing the structure of the apparatus for producing mineral-containing water (B) shown in Fig. 14.

Fig. 17 is a side view showing a water-passing container constituting the apparatus for producing mineral-containing water (B) shown in Fig. 14;

Fig. 18 is a graph showing the ratio of the emission of the ceramic sintered body containing the mineral component (Example 1) and the ceramic sintered body (control sample) to the black body at 25 °C.

In the following, the present invention is described in detail with reference to the embodiments, and the present invention is not limited to the embodiments described below, and can be arbitrarily changed without departing from the scope of the invention.

<Definition of terms>

In the present specification, [mineral functional water] means water containing a mineral component and capable of producing at least one or more effective effects.

Further, in the present specification, [mineral-containing water] means raw material water in a previous stage when mineral water is produced, and mineral-containing water also contains a mineral component. The details of the method for producing the mineral functional water of the present invention will be described later. Furthermore, mineral-containing water itself may have effective efficacy or may not have effective efficacy.

In addition, in the present specification, [mineral component] does not mean the definition of minerals in a narrow sense, that is, [inorganic components (including trace elements) other than four elements (carbon, hydrogen, nitrogen, oxygen)], but The aspect in which the inorganic component coexists may also include the aforementioned four elements (carbon, hydrogen, nitrogen, oxygen) excluding the narrow definition. Therefore, for example, [a mineral component derived from a plant] is also a concept including an inorganic component derived from a plant such as calcium and an organic component derived from a plant.

In addition, examples of the inorganic component (constituting the mineral component) include sodium, potassium, calcium, magnesium, and phosphorus. Examples of the trace element include iron, zinc, copper, manganese, iodine, selenium, and chromium. And molybdenum, etc., but are not limited to this.

In the present specification, [a mineral component derived from mineral functional water] means a mineral component remaining after removing a solvent component from the target mineral water. However, as described above, the mineral component derived from a plant contains not only an inorganic component but also an organic component derived from a plant.

In the present specification, the [solumetric ceramic material] refers to a ceramic material in which a mineral component is immobilized in a soluble manner. [The mineral component is immobilized in a soluble state] When the ceramic material to be used is brought into contact with an extraction solvent (generally a solvent mainly composed of water), the mineral component gradually dissolves and eventually does not remain in the ceramic. The state of the material (except for the inevitable residuals).

In the following description, the eluted ceramic material is referred to as [the ceramic material of the present invention] or simply as the [ceramic material].

In the present specification, the [non-lead-type ceramic material] refers to a ceramic material in which a mineral component is immobilized on a ceramic material to be a substrate without being eluted. [(Mineral component) is immobilized in a non-sedimented state] When the ceramic material to be contacted is brought into contact with water, the mineral component does not substantially elute and remains in the ceramic material. The non-lead-type ceramic material has electromagnetic wave irradiance from a mineral component that has been immobilized.

In addition, in the following, the non-lead-type ceramic material is referred to as [ceramic sintered body of the present invention] or simply [ceramic sintered body].

In the present specification, [solubilizing function water] means a functional water containing a mineral component which is eluted from an elution-type ceramic material by contact with an extraction solvent, and means having at least one or more. Functional water for effective performance. Further, the solute functional water may also be referred to as one type of mineral functional water, but the functional water containing the mineral component eluted from the eluted ceramic material is referred to herein as the solvating water. Functional water is called mineral water to distinguish it.

Furthermore, depending on the kind of the ceramic material to be the carrier, the extraction solvent Although the type, the extraction conditions, and the like are different, there is a case where the entire mineral component cannot be extracted from the eluted ceramic material even if it is in contact with the extraction solvent. Therefore, the composition of the mineral functional water used for the immobilization of the mineral component and the composition of the dissolution functional water obtained by the dissolution are generally not completely identical.

<1. Manufacturing device for eluting functional water>

The apparatus for producing a melt-dissolving functional water of the present invention (hereinafter referred to as the "manufacturing apparatus of the present invention") is a device for producing a water for concentrating functional water containing a mineral component, and is characterized in that: More than one processing tank, the treatment tank has a water inlet path and a water outlet path, and may internally supply water flowing from the water inlet path or an extraction solvent mainly composed of water toward the water outlet path; and effluent of one of the treatment tanks a connection path connecting the path to another water inlet path of the processing tank, wherein the two or more processing tanks are connected in series via the connecting path, and at least one of the processing tanks contains a mineral component soluble The immobilized ceramic material is immobilized.

Furthermore, the other processing tanks described above are generally processing tanks adjacent to one of the processing tanks.

By having such a structure, by supplying water or an extraction solvent mainly composed of water, the mineral component is eluted from the eluted ceramic material to water or an extraction solvent mainly composed of water, thereby producing a mineral-containing component. The solution is water. The eluted ceramic material may be contained in at least one of the treatment tanks of the treatment tank.

The extract (solution water) after contact with the eluted ceramic material contains a part or all of the mineral component held in the eluted ceramic material.

[Extraction solvent mainly composed of water] is a liquid containing 50% by weight or more of water, and a component other than water, and an organic solvent having compatibility with water such as ethanol. Further, in the extraction solvent, an optional component such as a pH adjuster may be contained in a range that does not impair the effects of the present invention.

In the following description, when water is an extraction solvent, water is used as [water and extraction solvent mainly composed of water].

As the eluted ceramic material, a cement hardened body containing a mineral component derived from mineral functional water or a ceramic porous body containing the mineral component in a pore can be used. The details are described in <2-1. Solvent-type ceramic material (ceramic material)>.

The type and capacity of the eluted ceramic material can be determined in accordance with the elution function water of the intended purpose. For example, it is preferable to consider the type of the mineral component to be contained in the eluted ceramic material to be accommodated, the amount of water to be distributed, the volume of the processing container, the number and arrangement of the processing containers, and the like.

In the manufacturing apparatus of the present invention, it is preferable to provide a water injection path that communicates with the processing tank in which the eluted ceramic material is accommodated. In such a configuration, an arbitrary component can be supplied from the water injection path as needed.

In the manufacturing apparatus of the present invention, the processing tank other than the processing tank in which the above-described eluted ceramic material is accommodated is housed and fixed in a non-dissolved manner. A non-lead-type ceramic material having a mineral component is preferred. In this way, by making the water as the extraction solvent not only in contact with the elution-type ceramic material but also in contact with the non-lead-type ceramic material having electromagnetic wave irradiation properties, the water-soluble performance of the electrolyte can be improved. For the reason that the reason is unknown, it is presumed that it is an action of activation of mineral components (including organic components derived from plants) contained in the water for the dissolution of the functional water.

As the non-lead-type ceramic material, a ceramic sintered body containing a mineral component derived from mineral water can be preferably used. The details are described in <2-2. Non-lead-type ceramic material (ceramic sintered body)>.

At least one of the treatment tanks in which the above-described eluted ceramic material is accommodated is disposed on the upstream side of the treatment tank in which the non-lead-type ceramic material is accommodated. According to this configuration, since the mineral component eluted from the eluted ceramic material is directly in contact with the non-lead-type ceramic material, the performance of the water for the electrolyte is further improved.

The type and capacity of the non-lead-type ceramic material can be determined in accordance with the elution function water of the intended purpose. For example, it is preferable to consider the type of the mineral component to be contained in the eluted ceramic material to be accommodated, the amount of water to be distributed, the volume of the processing container, the number and arrangement of the processing containers, and the like.

In the manufacturing apparatus of the present invention, the two or more processing tanks may be connected in series via the connecting path, and the number and arrangement of the processing tanks may be appropriately determined depending on the purpose.

Among them, it is possible to make two processing tanks in a compact form via the aforementioned connection It is preferred that the junction paths are connected in series. The details of the manufacturing apparatus according to the embodiment of the present invention will be described later.

In the manufacturing apparatus having such a configuration, it is desirable that at least one of the processing tanks in which the eluted ceramic material is accommodated is disposed on the upstream side of the processing tank in which the non-lead-type ceramic material is accommodated. In particular, it is preferable that the processing tank located on one of the upstream sides of the connecting path is disposed at a position higher than the processing tank of the other one.

The method for producing a leaching machine water of the present invention is characterized in that the manufacturing apparatus of the present invention using one of the foregoing is used.

The first aspect of the method for producing a water for dissolving functional water of the present invention has a process of supplying water or a water-based extraction solvent to the production apparatus of the present invention, and water or a water-based extraction solvent and a process of contacting the aforementioned elutive ceramic material in one of the processing tanks in the processing tank.

A second aspect of the method for producing a water for emulsification of the present invention is a process for supplying water or a water-based extraction solvent to the production apparatus of the present invention, and water or a water-based extraction solvent and a process of contacting the eluted ceramic material of the one of the treatment tanks in the treatment tank with the non-lead-type ceramic material. In this case, it is preferable to have the following processes, and even if water or a water-based extraction solvent is contacted with the eluted ceramic material, the water in contact with the eluted ceramic material or the water-based extraction solvent is used. Process in contact with non-lead-type ceramic materials. In the second aspect, it is preferable to use a manufacturing apparatus in which two processing tanks to be described later in the embodiment are connected in series via the connecting path.

Hereinafter, a manufacturing apparatus in which two processing tanks are connected in series via a connecting path, and a method of using the same according to a preferred embodiment of the apparatus for producing a melt-dissolving water according to the present invention will be described with reference to the drawings. It is not limited to this embodiment.

Hereinafter, a mineral water-producing apparatus 100 according to an embodiment of the present invention will be described with reference to Figs. 1 to 4 .

As shown in Fig. 1, the mineral water-producing apparatus 100 of the present embodiment includes a first treatment tank 110 and a second treatment tank 150 which are arranged in series in the vertical direction, and a water supply for supplying water to the first treatment tank 110. The tube 117; a communication path 158 that connects the first treatment tank 110 and the second treatment tank 150; and a water discharge path 153 that outputs the elution functional water W2 (see FIG. 3) formed in the second treatment tank 150.

The first treatment tank 110 is formed by attaching the circular lids 115 and 116 to the flanges 111a and 111b of the upper and lower ends of the substantially cylindrical casing 111 via the donut disk-shaped spacer P, respectively. . Similarly, the second processing tank 150 is attached to the circular lids 155 and 156 via the donut disc-shaped spacers P at the upper and lower end flanges 151a and 151b of the substantially cylindrical outer casing 151. To form. The first processing tank 110 is the same as the size, shape, and the like of the second processing tank 150, but is not limited thereto.

The flange 111b and the lid 116 below the first treatment tank 110 located above and the flange 151a and the lid 155 above the second treatment tank 150 located below are connected via a plurality of pillars 125, so that The processing tank 110 and the second processing tank 150 are arranged in series in a vertical direction in a state of being separated by a predetermined distance from the length of the supporting pillar 125. on. A plurality of casters 157 are attached to the lower surface side of the cover 156 below the second processing tank 150 located below.

As shown in FIG. 2, the first treatment tank 110 is provided with a water inlet path 112 for flowing water transported through the water supply pipe 117 into the outer casing 111, and for discharging the melt water W1 formed in the outer casing 111. The water outlet path 113. The water inlet path 112 is provided to penetrate the upper portion of the outer casing 111 (portion close to the flange 111a), and the water discharge path 113 is provided to penetrate the lid body 116 below the outer casing 111.

The elbow portion of the water inlet path 112 that protrudes in the outer casing 111 is provided with an opening and closing valve 120 that opens and closes the water inlet path 112 by the arm 122 that is undulated by the rise and fall of the float 121. When the water level in the outer casing 111 of the first treatment tank 110 is lowered, the float 121 is lowered to open the opening and closing valve 120, and water is discharged from the opening portion 112a of the water inlet path 112 toward the outer casing 111. When the water level in the casing 111 rises by the water discharged from the opening 112a of the water inlet path 112, the float 121 rises and the opening and closing valve 120 is closed, and the water is stopped from being discharged from the opening 112a.

The inside of the casing 111 is partitioned into an upper space 111x and a lower space 111y by a partition wall 118 which is disposed in parallel with the lid 116 from a portion of the lid 116 which is disposed in parallel with the lid 116. A plurality of through holes 118a are formed in the partition wall 118, and a plurality of water permeable bag bodies N are accommodated in the upper space 111x above the partition wall 118, and the water permeable bag body N is provided with a dissolution type ceramic material C1.

The water injection path 114 in the outer casing 111 connected to the first treatment tank 110 is a cover body penetrating from the outside of the first treatment tank 110 The mode of 115 is provided in the casing 111. The upper end opening portion 114a of the water injection path 114 is located outside the first processing tank 110, and the lower end side of the water injection path 114 is a through hole 118a penetrating the partition wall 118, and the lower end opening portion 114b is located in the lower space 111y.

A portion of the outer casing 111 which is adjacent to the upper cover 115 (a portion having the same height as the water inlet path 112) is provided with a drainage path 119 communicating with the inside of the outer casing 111. When the opening and closing valve 120 is closed or the like, water excessively flows into the casing 111 from the opening portion 112a, and when the water level in the casing 111 rises, excess water can overflow from the drainage path 119.

As shown in FIG. 3, the second processing tank 150 is provided with a water inlet path 152 for flowing the elution functional water W1 conveyed from the first processing tank 110 (see FIG. 1) via the connecting path 158 into the outer casing 151; And a water discharge path 153 for discharging the elution function water W2 formed in the outer casing 151. The water inlet path 152 communicates with the inside of the casing 151 through the lower portion of the casing 151 (portion close to the flange 151b), and the water discharge path 153 passes through the lid 155 above the casing 151 to communicate with the inside of the casing 151. Inside the outer casing 151, a plurality of water-permeable bag bodies N are housed, and the water-permeable bag body N is provided with a non-lead-type ceramic material C2.

The opening portion 153a of the water discharge path 153 in the outer casing 151 is provided at a position offset from the center of the lid body 155 (a position eccentric toward the outer circumferential side of the lid body 155). The lower surface 155a of the lid body 155 (the surface on the inner side of the outer casing 151) has an umbrella shape recessed toward the opening portion 153a, and the opening portion 153a is located at the uppermost portion thereof. In the water outlet path 153, it is provided to be manually operated by the operating lever 54a. The operated opening and closing valve 154b is connected to an outlet pipe 159 on the downstream side thereof.

In the mineral water-producing device 100, the eluted ceramic material C1 contained in the outer casing 111 of the first treatment tank 110 located above the second treatment tank 150 is a mineral component derived from mineral functional water. A ceramic material that is immobilized (held) by elution. In the eluted ceramic material C1, a cement hardened body containing the above-described mineral component is used, but a ceramic porous body in which the above-described mineral component is supported in the pores may be used.

In the mineral water-producing device 100, the non-lead-type ceramic material C2 accommodated in the outer casing 151 of the second treatment tank 150 located below the first treatment tank 110 contains mineral-containing substances having electromagnetic radiation. A ceramic sintered body of the composition.

Here, next, a method of manufacturing the melt water of the mineral water manufacturing apparatus 100 will be described with reference to FIGS. 1 to 4 . As shown in FIG. 1, the mineral water manufacturing apparatus 100 is installed on the floor G, and the upstream side of the water supply pipe 117 is connected to a water supply source (for example, a tap of tap water, etc.), and the water outlet path of the second processing tank 150 is provided. The opening and closing valve 154b of 153 is set to a predetermined opening degree. Then, when water supply is performed from the water supply source via the water supply pipe 117, the water flows into the inside of the outer casing 111 of the first treatment tank 110 via the water inlet path 112, so that the eluted ceramic material C1 comes into contact with water.

When the water is in contact with the eluted ceramic material C1 in the outer casing 111, the mineral component that has been immobilized on the eluted ceramic material C1 is eluted into water as an extraction solvent to form the elution functional water W1.

Further, when the eluted ceramic material C1 is immobilized, the mineral machine disclosed in Patent Document 3 (WO2016/043213), which is described later in detail, is incorporated. When the eluted ceramic material of the mineral component of the water (mineral functional water (1) to be described later) is formed, the electrolytic solution water W1 whose pH is raised to about 10.5 to 11.5 is formed.

The elution functional water W1 formed by contact with the eluted ceramic material C1 in the first treatment tank 110 flows into the outer casing 151 of the second treatment tank 150 via the water discharge path 113, the connection path 158, and the water inlet path 152. It is in contact with the non-lead-type ceramic material C2 in the outer casing 151. Since a pH meter (not shown) is provided in the water discharge path 13, the pH of the elution function water W1 flowing in the water discharge path 13 can always be detected.

When the elution functional water W1 is in contact with the non-lead-type ceramic material C2 in the outer casing 151, the mineral contained in the melt water W1 is dissolved by the electromagnetic wave emitted from the non-solubilized ceramic material C2. The component is activated to form the elution functional water W2, and is supplied to a predetermined place via the water discharge path 153 and the outlet pipe 159 above the casing 151. The detailed reason for the activation of the mineral component by the non-lead-type ceramic material C2 is still unknown, but it is presumed that it is the mineral component contained in the soluble functional water W1 (including organic components derived from plants). The role of ionization travel, etc.

Since a pH meter (not shown) is provided in the water discharge path 153, the pH of the elution function water W2 flowing in the water discharge path 153 can always be detected.

Further, when the non-lead-type ceramic material C2 is a mineral which is immobilized with mineral functional water (mineral functional water (1)) disclosed in Patent Document 3 (WO2016/043213), which is described later in detail. Insoluble ceramic material At the time of the material, the electrolytic solution water W2 whose pH rises to about 12 is formed.

As shown in FIG. 1, in the elution functional water producing apparatus 100, the first processing tank 110 located on the upstream side of the communication path 158 is disposed at a position higher than the second processing tank 150 (directly above the second processing tank 150). . Therefore, when water is supplied to the first treatment tank 110, water is sequentially flowed inside the first treatment tank 110 and inside the second treatment tank 150 by gravity, whereby a predetermined dissolution function can be formed. Water W2. In other words, the mineral water-producing device 100 can be easily and stably manufactured by containing a predetermined mineral by using a power source that can supply water to the first treatment tank 110 without using a power source or other power source. The composition has a beneficial performance of the soluble functional water W2.

In the mineral water-producing device 100, the opening degree of the opening and closing valve 154b is adjusted by operating the operation lever 154a of the water discharge path 153 provided in the upper portion of the second treatment tank 150, and the amount of water flowing from the water discharge path 153 can be increased or decreased. By adjusting the residence time (reaction time) of the water supplied to the mineral water-producing device 100 via the water-intake path 112 in the first treatment tank 110 and the second treatment tank 150, it is possible to produce a suitable pH-soluble solvent water W2. .

Since the opening and closing valve 120 that is actuated by the raising and lowering of the float 121 is provided in the outer casing 111 of the first treatment tank 110, it is possible to prevent excess water from flowing into the casing 111 from the water inlet path 112. Further, when it is assumed that excess water flows into the casing 111 from the water inlet path 112, since the remaining water is discharged from the drainage path 119 to the outside, the first treatment tank 110, the second treatment tank 150, and the like are not present. Damaged by water pressure.

Further, an optional component may be injected from the upper end opening portion 114a of the water injection path 114 that protrudes from the upper portion of the first treatment tank 110 as needed.

For example, the eluted ceramic material C1 and the non-lead-type ceramic material C2 are each a precipitated ceramic material or a non-lead-type ceramic material in which a mineral component derived from the mineral functional water (1) is immobilized. The following operation methods are mentioned.

When the pH of the elution functional water W1 formed in the first treatment tank 110 and flowing out from the water discharge path 113 is low (when the pH is less than 10.5), the dissolution function discharged from the water discharge path 153 of the second treatment tank 150 is discharged. A part of the water W2 is injected from the upper end opening portion 114a of the water injection path 114 that protrudes from the upper portion of the first treatment tank 110. Therefore, the elution functional water W2 having a pH of about 12 is supplied to the lower space 111y of the outer casing 111 of the first treatment tank 110 through the lower end opening portion 114b of the water injection path 114, and is mixed into the solute functional water W1. The pH of the elution functional water W1 flowing out from the first treatment tank 110 via the water discharge path 113 can be set to a predetermined value.

As shown in FIGS. 3 and 4, the lower surface 155a of the lid body 155 for closing the outer casing 151 of the second treatment tank 150 has an umbrella shape recessed toward the opening portion 153a of the water discharge path 153, and the opening portion 153a is located at the lower surface 155a. The top of the. Therefore, as shown in FIG. 4, the bubble B generated in the elution functional water W2 inside the outer casing 151 rises to the lower surface 155a of the lid body 155, and then moves upward along the inclination of the lower surface 155a, from the opening portion 153a. It is quickly discharged through the water discharge path 153 together with the dissolution functional water W2. Therefore, the disadvantage that the bubble B is gradually stored into the outer casing 151 can be prevented. produce.

As shown in FIG. 1 and FIG. 3, a plurality of casters 157 are provided on the lower surface of the cover 156 below the outer casing 151. Therefore, the melt water-producing device 100 can be easily moved while being grounded to the ground G. Good convenience.

The lids 115 and 155 of the first treatment tank 110 and the second treatment tank 150 constituting the melt water-producing device 100 can be attached to and detached from the outer casings 111 and 151, respectively, so that the electrolytic ceramic materials C1 and C can be easily formed. The extraction and replacement work of the eluted ceramic material C2 or the like.

In the above, a preferred embodiment of the apparatus for producing a solvable water according to the present invention has been described. However, the present invention is not limited to the embodiments, and any configuration may be employed in addition to the above-described preferred embodiment. In particular, in the embodiments disclosed herein, items that are not explicitly disclosed, such as operating conditions, operating conditions, various parameters, size, weight, volume, etc. of the components, are used without exceeding the scope generally practiced by the industry. A value that can be easily imagined by a general practitioner.

Further, the elution functional water producing apparatus 100 described with reference to FIGS. 1 to 4 is an example of the present invention, and the eluting functional water producing apparatus of the present invention is not limited to the above-described electrolytic solvable water producing apparatus 100. The elution functional water producing apparatus 100 includes one first processing tank 110 and one second processing tank 150. However, three or more processing tanks may be provided depending on the purpose, and they may be arranged arbitrarily.

For example, as shown in the schematic diagram of FIG. 5, three processing tanks may be used. As shown in the schematic diagram of FIG. 6, the upstream processing tanks are arranged in parallel, and the processing tanks are connected in series to the downstream processing tanks, and the like, as long as two or more processing tanks are connected in series. The mode connection is included in the concept of the manufacturing apparatus of the present invention.

Further, in the production apparatus of the present invention, even if it has two or more processing tanks, it is sufficient to contain a elution-type ceramic material in one or more processing tanks. For example, in the case of the analysis of the functional water W1, the non-leolysis-type ceramic material can be stored in the second treatment tank 150, and the elution-type ceramic material C1 can be used to obtain the elution function. Water W1.

<2. Solvent-type ceramic materials and non-lead-type ceramic materials>

The eluted ceramic material and the non-lead-type ceramic material used in the above-described production apparatus of the present invention will be described below. In the following description, the case of [solubility-type ceramic material] is referred to as [ceramic material of the present invention] or simply [ceramic material], and the same meaning is given. In addition, the case of [non-lead-type ceramic material] is referred to as [ceramic sintered body of the present invention] or simply as [ceramic sintered body], and the same meaning is given.

<2-1. Solvent-type ceramic material (ceramic material)>

The ceramic material of the present invention is a dissolution type ceramic material in which a mineral component is immobilized (held) in a form of elution, and can be roughly classified into the following two aspects.

The first aspect of the ceramic material (solubolytic ceramic material) of the present invention is a cement hardened body containing a mineral component derived from mineral functional water.

Further, the second aspect of the ceramic material of the present invention is a ceramic porous body in which a mineral component derived from mineral functional water is supported in pores.

The first aspect and the second aspect of the ceramic material of the present invention are ceramic materials in which the mineral component is immobilized and dissolved. Here, [the mineral component is immobilized by elution] means that when the target ceramic material is brought into contact with an extraction solvent (generally a solvent mainly composed of water), the mineral component is gradually dissolved and eventually becomes not formed. Remains in the state of ceramic materials (except for unavoidable residual components).

The mineral component immobilized on the ceramic material of the present invention is preferably a mineral component derived from mineral functional water. Further, the mineral functional water will be described later in conjunction with the production method thereof.

Hereinafter, the ceramic material of the first aspect and the second aspect will be described in detail together with the production method.

(1) The first aspect (cement hardened body)

The first aspect of the ceramic material of the present invention is a cement hardened body containing a mineral component (hereinafter referred to as "the cement hardened body of the present invention"). The cement hardened body according to the first aspect of the ceramic material of the present invention has an advantage that the mineral component can be held in a larger amount than the ceramic porous body of the second aspect.

The cement hardening system of the present invention can be produced by solidifying a cement mixture using mineral functional water containing a mineral component.

That is, the cement hardened body of the present invention is characterized in that the mineral functional water containing the mineral component is mixed with the cement composition to obtain water. a mixing process of the mud mixture; and a curing process for curing the obtained cement mixture for curing.

In addition, the term "cement mixture" as used herein refers to a material in which a cement powder is mixed, and [cement mixture] means a fluidity in which a cement mixture is hydrated and uncured. Further, the [cement hardened body] of the present invention means that the cement mixture is hardened, and generally includes the concept of mortar and concrete having components other than cement powder.

The [cement mixture] of the mixing process can be a conventional cement powder or a mixed material (aggregate or the like) used for the production of a cemented body.

The type of cement body of cement powder is not particularly limited, and general Portland cement, early strength Portland cement, super early strong Portland cement, moderate hot Portland cement, low heat Portland cement, and resistance can be used. Portland cement and alumina cement such as sulfate Portland cement and white Portland cement (white cement).

Further, blast furnace cement in which fine powder of blast furnace slag is mixed with Portland cement, fly ash cement in which fly ash (incineration ash of lime produced in a thermal power plant or the like) and Portland cement are mixed may be used.

The mixture of the aggregates and the like which are mixed with the cement powder may be a mixture of the conventionally produced cement hardened body, and examples thereof include calcium carbonate powder containing cerium oxide powder or limestone such as vermiculite. Wait.

The mixing ratio of the mineral functional water and the cement powder can be considered as the amount of the mineral component contained in the mineral functional water, the pH, etc., and the type and amount of the aggregate of the cement powder, etc., which are necessary for the cement mixture. Viscosity, etc. are determined. As an ideal example of blending, the amount of water is 15 to 30% by weight and 40 to 60% by weight of the cement powder (the remaining part is a component such as a mixed material).

The method of mixing the mineral functional water and the cement powder is not particularly limited, and it may be sufficiently mixed and synthesized using a conventional mixing device. In addition, water can be added in case of insufficient water. The water to be added may be water other than the mineral water. Further, conventionally used components for the production of a cemented body can be added as needed. The additive is not particularly limited as long as it does not impair the object of the present invention, and examples thereof include a pH adjuster, a water reducing agent, and a curing accelerator.

As a curing process, the cement mixture obtained in the aforementioned mixing process is cured and solidified to form a cement hardened body. The curing conditions are various conditions such as the cement powder to be used for the purpose of the cement hardened body, the type of the mixed material, the hardness of the cement hardened body to be used, the amount of the mineral component to be retained, and the like, and it is suitable to select the room temperature curing, Conventional curing methods such as heat curing, steam curing, and the like.

The shape of the cement hardened body of the present invention is not particularly limited, and it can be used in an ideal shape for use in the application, and examples thereof include a powder, a pellet, and a plate. The size is also arbitrary and can be appropriately determined depending on the purpose of use. The molded body or the unformed mass may be pulverized and used as a powder, a granule or the like.

(2) The second aspect (ceramic porous body)

The second aspect of the ceramic material of the present invention is a ceramic porous body that supports a mineral component in pores (hereinafter referred to as [ceramic porous body of the present invention] The case of plastid].

In the ceramic porous body of the second aspect of the ceramic material of the present invention, the absolute amount of the mineral component that can be retained is small, but the cement hardened body of the first aspect cannot be regenerated after the mineral component is eluted. The ceramic porous body of the second aspect has the advantage that it can be reused after the mineral component is eluted and then re-impregnated with the mineral functional water and then dried.

The mineral component of the ceramic porous body of the present invention contains a ceramic porous body as a carrier, and is fixed by elution.

The type of the oxide which is a raw material of the ceramic porous body is not particularly limited as long as it is an oxide having moderate sinterability. Examples of the oxide to be used as such a raw material include cerium oxide, titanium oxide, aluminum oxide, and a composite oxide thereof. Further, clays such as diatomaceous earth (main component: cerium oxide), kaolin (main component: cerium oxide-alumina), and hydrotalcite may be preferably used. Rocks containing such clays can also be pulverized and used as a raw material for ceramic carriers. For example, the rock powder produced by the Amakusa Oyao Island used in the examples described later is an ideal example of a ceramic carrier raw material.

The ceramic porous body of the present invention may contain a conventional component which can be used for a ceramic porous body composed of an oxide. The optional component is not particularly limited as long as it does not impair the object of the present invention.

The shape of the ceramic porous body of the present invention is not particularly limited, and it can be used in an ideal shape for use in the application, and examples thereof include a powder form. Granular, plate-like, etc. The size is also arbitrary and can be appropriately determined depending on the purpose of use. The molded body or the unformed mass may be pulverized and used as a powder, a granule or the like.

The ceramic porous body of the present invention is a method in which a mineral functional water is immobilized on a carrier composed of a ceramic porous body by a physical action or a chemical action.

That is, the method for producing a ceramic porous body of the present invention comprises a process of mixing a liquid for mixing and a ceramic powder for a carrier into a clay-like mixture (I); and heat-treating the clay-like mixture to obtain a ceramic porous body The process (II); and the process (III) of allowing the mineral water to permeate the pores of the ceramic porous body and then drying the mineral component to the ceramic porous body.

According to the production method of the present invention, the ceramic porous body of the present invention described above can be produced. In particular, the ceramic porous body obtained before the process (II) (before the mineral component is immobilized) has a large number of pores, and the mineral component derived from the mineral functional water can be held inside the pores, thereby improving the present invention. The ceramic porous material is the content of the mineral component of interest.

Hereinafter, each process of the method for producing a ceramic porous body of the present invention will be described.

The process (I) is a process in which a mixing liquid (mixing dispersion medium) and a carrier ceramic powder are mixed to form a clay-like mixture.

The oxide of the raw material of the ceramic powder for carrier is the same as the oxide described as the ceramic carrier, and has an appropriate sinter oxidation. The material is not particularly limited.

Examples of the oxide to be used as such a raw material include cerium oxide, titanium oxide, aluminum oxide, and a composite oxide thereof. Further, clays such as diatomaceous earth (main component: cerium oxide), kaolin (main component: cerium oxide-alumina), and hydrotalcite may be preferably used. Rocks containing such clays can also be pulverized and used as a raw material for ceramic carriers. For example, the rock powder produced by the Amakusa Oyao Island used in the examples described later is an ideal example of a ceramic carrier raw material.

The ceramic powder for the carrier is preferably a ceramic powder. The particle diameter of the powder is selected in a favorable range such as moldability and sinterability, and is generally 100 μm or less.

The liquid to be mixed is a liquid to be added when the ceramic powder for a carrier is mixed, and any liquid can be used. However, water or a liquid mainly composed of water is generally used. [Liquid-based liquid] A liquid containing 50% by weight or more (including 100% by weight) of water, and a component other than water, and an organic solvent having compatibility with water such as ethanol. Further, the mixing liquid may contain an optional component such as a pH adjuster in a range that does not impair the effects of the present invention.

The mixing method of the ceramic powder for the carrier and the liquid for mixing may be carried out by any method, and may be carried out by hand, or may be carried out by using a conventional mixing device.

In addition, the mixing ratio of the ceramic powder for carrier and the liquid for mixing is set within a range in which the viscosity can be maintained, and the weight of the ceramic powder for the carrier is 100 parts by weight, and the liquid for mixing is generally 5 parts by weight or more and 500. The weight portion or less is preferably 10 parts by weight or more and 300 parts by weight or less.

Further, in the clay-like mixture, in addition to the carrier ceramic powder and the mixing liquid, it may contain a conventional tackifier, a pore generating agent, and a pH adjustment for use in ceramics, without damaging the effects of the present invention. Any component such as a agent.

The process (II) is a process in which the obtained clay-like mixture is formed into a predetermined shape as needed, and then heat-treated to obtain a ceramic porous body having a plurality of pores.

Since the formation of the clay-like mixture is viscous, it is easy to carry out, and the appropriate shape can be controlled depending on the intended use. When it is formed into a particulate form, it can adjust to about 50-500 micrometers, for example. Further, the clay-like mass may be dried, and then pulverized to adjust the particle diameter, followed by heat treatment. In this manner, since the ceramic powder for the carrier can be formed into a clay-like mixture of an arbitrary shape and then formed into a heat treatment, the ceramic porous body having the desired shape can be easily obtained.

The heat treatment can be carried out by a conventional firing device. The heat treatment temperature is determined so that the obtained ceramic porous body has sufficient pores and has a degree of mechanical strength which can be used in a post-process, and is determined by the type of the ceramic powder for the carrier, and is usually 500 ° C or more. Below °C, it is preferably 700 ° C or more and 900 ° C or less. Further, the environment at the time of heat treatment is not particularly limited, but is generally an atmospheric environment. The heat treatment time can be appropriately determined depending on the heat treatment temperature, the porosity of the object, the degree of sintering, and the like.

Process (III) is to dry the mineral water containing the mineral component in the pores of the ceramic porous body, and then dry it. The process of immobilizing a mineral component on the ceramic porous body. By this process, the mineral component is retained in the ceramic porous body in a soluble manner.

Since the ceramic porous body has a large number of pores, the fine pores contain the mineral functional water and then dried, and the mineral components contained in the mineral functional water can be contained in a larger amount.

Further, the mineral functional water containing the mineral component will be described later together with the production method thereof.

The method of allowing the mineral water to permeate the pores of the ceramic porous body is arbitrary, and for example, a method of immersing the ceramic porous body in the mineral functional water is not limited thereto. Further, by repeating the operation of allowing the mineral functional water to permeate the ceramic porous body and allowing the mineral water to permeate again after the solvent (water) evaporates, more mineral components can be immobilized.

The amount of mineral functional water impregnated in the porous ceramic body is determined by considering the type and concentration of the mineral component contained in the mineral functional water, depending on the pore physical properties and porosity of the ceramic porous body, but generally The weight of the ceramic porous body is 15% by weight or more.

When the ceramic porous body of the present invention of the second aspect of the ceramic material of the present invention is brought into contact with an extraction solvent mainly composed of water, the mineral component contained in the ceramic porous body of the present invention can be eluted into the foregoing. Extract solvent. Here, [the extraction solvent mainly composed of water] is as described in the above (1) cement hardened body, and thus the description thereof is omitted here.

The extract liquid (solubilization function water) after contact with the ceramic porous body of the present invention contains a mineral component held in the ceramic porous body Part or all.

The ceramic porous body of the present invention after use (after extracting the mineral component) can be regenerated by performing the process (III) again.

<2-2. Non-lead type ceramic material (ceramic sintered body)>

The ceramic sintering system of the present invention refers to a non-lead-type ceramic material contained in a state in which a mineral component is immobilized on a ceramic sintered body serving as a substrate without being eluted.

Here, [the state in which the (mineral component) is immobilized in a non-sedimented state] means that when the intended ceramic sintered body is brought into contact with water, the mineral component does not substantially elute and remains in the ceramic sintered body. Aspect.

That is, the ceramic sintered body of the present invention is clearly different from the mineral material-soluble ceramic material in which the mineral component is dissolved and fixed. Here, [the mineral component is immobilized by elution] means that when the target ceramic material is brought into contact with an extraction solvent (generally a solvent mainly composed of water), the mineral component is gradually dissolved and eventually becomes not formed. Remains in the state of ceramic materials (except for unavoidable residual components).

The electromagnetic wave radiation of the ceramic sintered body of the present invention is a ceramic sintered body containing a mineral component to be measured and a ceramic containing no mineral component by measuring [emissibility] and [spectral emissivity] by the following method. The spectroscopic spectroscopy spectrum of the sintered body (blank) was compared.

Here, the [radiation rate] refers to the ratio of the radiation divergence of the radiator to the radiation divergence of the black body at the same temperature as the radiation (JIS Z 8117). The radiance] indicates the ratio of the radiation of the sample when the emissivity of the black body at this temperature is 100%. Furthermore, the sample to be evaluated has a specific spectroradiance spectrum. The measurement method of the spectroradiance spectrum is defined by JIS R 180, and can be measured by using an emissivity measuring system having Fourier transform type infrared spectrophotometry (FTIR) according to the device configuration of JIS R 180. An ideal example of the emissivity measuring system is a far-infrared radiance measuring device (JIR-E500) manufactured by JEOL Ltd. Specific examples of the method for measuring the spectroradiance spectrum of the ceramic sintered body of the present invention, evaluation of electromagnetic wave radiation, and the like will be described later.

The mineral component immobilized in the ceramic sintered body of the present invention is preferably a mineral component derived from mineral functional water. Further, the mineral functional water will be described later in conjunction with the production method thereof.

The mineral component of the ceramic sintered body of the present invention is contained in a ceramic sintered body (ceramic carrier) as a carrier, and is fixed without being eluted. The type of the oxide which is a raw material of the ceramic sintered body is not particularly limited as long as it is sinterable and does not impair the electromagnetic radiation emitted by the mineral component derived from the mineral functional water. Examples of the oxide to be used as such a raw material include cerium oxide, titanium oxide, aluminum oxide, and a composite oxide thereof. Further, clays such as diatomaceous earth (main component: cerium oxide), kaolin (main component: cerium oxide-alumina), and hydrotalcite may be preferably used. Rocks containing such clays can also be pulverized and used as a raw material for ceramic carriers. For example, the rock powder produced by the Amakusa Oyao Island used in the examples described later is an ideal example of a ceramic carrier raw material.

The ceramic sintered body of the present invention may contain a conventional component which can be used for an oxide ceramic sintered body. The optional component is not particularly limited as long as it does not impair the object of the present invention.

The ceramic sintered body of the present invention may have a glaze layer covering the entire surface or a part of its surface. By having the glaze layer, the elution of the mineral component immobilized on the ceramic sintered body can be further suppressed.

The type of the glaze constituting the glaze layer is not particularly limited, and examples thereof include a lime glaze, a lime glaze, a zinc glaze, and a gray glaze.

The thickness of the glaze layer is also not particularly limited, and is generally designed to have a film thickness of about 0.1 to 3 mm.

Further, when the glaze layer is thickened, the electromagnetic wave intensity is weakened, so that the intensity of the electromagnetic wave emitted by the ceramic sintered body of the present invention can be controlled by suppressing the thickness of the glaze layer to be formed. Further, even in the case where the glaze layer is formed, in order to further increase the electromagnetic wave irradiation, it is preferable that the glaze layer contains a mineral component derived from the mineral functional water. The mineral component is preferably a mineral component derived from the mineral functional water of the present invention. The mineral component of the glaze layer may be the same mineral component as the internal ceramic sintered body, or may be a different mineral component.

The shape of the ceramic sintered body of the present invention is not particularly limited, and it can be used in an ideal shape for application, and examples thereof include a powder, a pellet, and a plate. The size is also arbitrary and can be appropriately determined depending on the purpose of use. The molded body or the unformed mass may be pulverized and used as a powder, a granule or the like.

<3. Mineral functional water and its manufacture>

<3-1. Mineral function water>

In the above-described eluted ceramic material (ceramic material of the present invention) and non-lead-type ceramic material (ceramic sintered body of the present invention), mineral components derived from mineral functional water are respectively fixed. In addition, the mineral component derived from [mineral functional water] refers to a mineral component remaining after the solvent component is removed from the target mineral water. However, as described above, the mineral component derived from a plant contains not only an inorganic component but also an organic component derived from a plant.

The mineral components immobilized on the eluted ceramic material and the non-leaved ceramic material are generally mineral components derived from mineral functional water, but may also be minerals derived from different mineral functional waters. ingredient.

The mineral component immobilized on the eluted ceramic material (ceramic material of the present invention) and/or the non-leaved ceramic material (ceramic sintered body of the present invention) of the present invention is derived from the formation of 1:5~ The ratio of 1:20 (weight ratio) contains mineral-containing water (A) formed by the following process (1), and ore-containing water (B) formed by the following process (2) The mineral component of the material function water is preferred.

Process (1):

a conductive material covered with an insulator, a plant material composed of a plant of the family Asteraceae, and a plant of the family Rosaceae, and one or more woody plants selected from maple, birch, pine, and cedar. Constituent The mineral-imparting material (A) of the woody plant material is immersed in water to conduct a direct current to the conductive wire, and the water around the conductive wire generates a water flow in the same direction as the direct current, thereby imparting ultrasonic vibration to the water. Forming a raw material mineral aqueous solution (A), and then irradiating the raw material mineral aqueous solution (A) with far infrared rays (wavelength 6 to 14 μm) to form a mineral-containing water (A) process, wherein the mineral imparting material (A) The amount of water added is 10 to 15% by weight, and the current value and voltage value of the direct current that is conducted to the conductive wire are in the range of 0.05 to 0.1 A and 8000 to 8600 V, respectively;

Process (2):

A process for forming mineral-containing water (B) containing mineral water (B) by passing water through six water-passing containers, wherein the six water-passing containers are filled with inorganic mineral-affecting materials different in type (B) The first water-passing container to the sixth water-passing container connected in series: the mineral-importing material (B1) in the first water-passing container is 70% by weight of limestone and 15% by weight of coral fossil, respectively. a mixture of shells of % by weight; the mineral-imparting material (B2) in the second water-passing container contains 40% by weight of limestone, 15% by weight of coral fossil, 40% by weight of shells, and 5% by weight of activated carbon. The mixture; the mineral-importing material (B3) in the third water-passing container is a mixture containing 80% by weight of limestone, 15% by weight of coral fossil, and 5% by weight of shells; and the mineral in the fourth water-passing container is given Material (B4) contains 90 respectively a mixture of % by weight of limestone, 5% by weight of coral fossil, and 5% by weight of shells; and the mineral-imparting material (B5) in the fifth water-passing container contains 80% by weight of limestone and 10% by weight of coral fossils, respectively. A mixture of shells of 10% by weight; the mineral-imparting material (B6) in the sixth water-passing container is a mixture containing 60% by weight of limestone, 30% by weight of coral fossils, and 10% by weight of shells, respectively.

In the above, an ideal mineral water which is a raw material of a mineral component produced by the above-described method for producing mineral water can be exemplified, but is not limited thereto. The details of the production method will be described as <3-2. Method for producing mineral functional water>.

Examples of the ideal mineral functional water used for the production of the eluted ceramic material (the ceramic material of the present invention) and the non-lead-type ceramic material (the ceramic sintered body of the present invention) include the mine developed by the inventors. Material function water (in the case of [mineral functional water of the present invention]). The mineral functional water of the present invention has excellent control effects (WO2016/043213), body activation (WO2016/043214), and combustion promotion of hydrocarbons (PCT/JP2016/058141), for example, for single-celled organisms, viruses, and the like. , beneficial effects of antioxidant effects (PCT/JP2016/058362).

Further, as a common feature of the mineral functional water of the present invention, a mineral component derived from a plant (particularly, an organic component derived from a plant) may be mentioned.

One of the ideal mineral functional waters is as in Patent Document 3 The mineral functional water (in the present specification, referred to as [mineral functional water (1)) in the present invention, which has an excellent control effect on cell organisms, viruses, and the like, as described in WO 2016/043213. The content of the method for producing the mineral functional water will be described later.

Further, the mineral functional water (1) meets all of the following requirements (i) to (iv): (i) a sample in which the weight of the mineral water is 15 parts or more and the weight of the ceramic carrier 100 is fixed. The average emission ratio (measuring temperature: 25 ° C) of the black body between the wavelengths of 5 to 7 μm and the wavelength of 14 to 24 μm is 90% or more; (ii) the functional water of the mineral is pH 12 or higher; (iii) having a single cell organism and The prevention and control of at least one of the viruses; (iv) the inclusion of mineral components derived from plants (especially organic components derived from plants).

The dissolving functional water obtained by contacting the ceramic material of the present invention containing the mineral component derived from the mineral functional water (1) with the extraction solvent mainly composed of water (hereinafter referred to as [solution water] (1) In the case of one of its useful efficacies, it has a control action of single-celled organisms, viruses, and the like which are causes of infectious diseases of humans and/or animals. Furthermore, [having a preventive effect] includes not only the single-celled organism, the virus, and the like as a target, but also a single-celled organism, a virus, and the like, which can suppress hyperplasia. Therefore, by using the lysing machine water for the single-celled organism and/or virus to be controlled, it is possible to perform single-cell growth of the subject. Prevention of substances and / or viruses.

Furthermore, the dissolution of the functional water (1), when compared with the mineral functional water (1), is relatively low in the prevention and control of single-celled organisms and/or viruses, so that it is directly It is preferred to apply and apply it by application, spraying, or the like.

In the present specification, [single cell organism] is a concept including bacteria, fungi, protozoa, and the like. The single-celled organism to be controlled by the elution functional water (1) is a bacteria that can be inactivated (extinct) by the action of the components contained in the water (1) of the elution function. The single-cell pathogenic bacteria such as fungi and protozoa are not particularly limited. Further, the virus to be controlled is not particularly limited as long as it can be inactivated (extinct) by the action of the component contained in the water (1) of the elution function.

One of the ideal mineral functional waters is mineral functional water (hereinafter referred to as [mineral functional water (2)] having a body activation action such as that promotes blood circulation as described in Patent Document 4 (WO2016/043214). Case). The content of the method for producing the mineral functional water will be described later. The dissolving functional water (solvent water (2)) obtained by contacting the ceramic material of the present invention containing the mineral component derived from the functional water of the mineral with the extraction solvent, and the mineral functional water (2) The same mineral ingredients help to promote body activation such as blood circulation.

One of the ideal mineral functional waters is a mineral functional water having a combustion-promoting action of a hydrocarbon type as described in Patent Document 5 (WO2016/043214) (hereinafter referred to as [mineral functional water (3)]. Happening). The content of the method for producing the mineral functional water will be described later.

The dissolving functional water (solvent water (3)) obtained by contacting the ceramic material of the present invention containing the mineral component derived from the functional water of the mineral with the extracting solvent, and the mineral functional water (3) The same mineral composition.

One of the ideal mineral functional waters is a mineral functional water (hereinafter referred to as [mineral functional water (4)) having an antioxidant action as described in Patent Document 6 (WO2016/058362). The content of the method for producing the mineral functional water will be described later.

The dissolving functional water (solvent water (4)) obtained by contacting the ceramic material of the present invention containing the mineral component derived from the functional water of the mineral water with the extracting solvent, and the mineral functional water (4) The same mineral composition.

<3-2. Method for producing mineral functional water>

Mineral functional water containing a mineral component used in the production of the ceramic material (solubilized ceramic material) of the present invention and the ceramic sintered body (non-lead-type ceramic material) of the present invention (hereinafter referred to as [this] In the case of the mineral functional water of the invention, the production method is not particularly limited, and it is preferable to use the apparatus disclosed in the above-mentioned Patent Document 2 (JP-A-2011-56366), and The method of the disclosed method is manufactured.

In addition, the production method is not particularly limited as long as the mineral functional water containing a beneficial mineral component can be obtained in addition to the production method using the production apparatus.

In the following, the device disclosed in Patent Document 2 (JP-A-2011-56366) is used to manufacture the present invention. An ideal embodiment of a method for producing mineral water. In the following description, for example, various mineral functional waters can be produced by appropriately changing the manufacturing conditions including raw materials.

As shown in Fig. 7, the mineral water manufacturing facility 1 is provided with: a mineral water (A) manufacturing apparatus 2; a mineral water (B) manufacturing apparatus 3; and a mixing tank 46 as a mixing means, the mixing tank The mineral-containing water (B) 45 produced in the mineral-containing water (B) manufacturing apparatus 3 is mixed with the mineral-containing water (A) 44 produced in the mineral-containing water (A) manufacturing apparatus 2 to form Mineral function water 47.

In the mineral water (A) manufacturing apparatus 2, the water 11 supplied from the water pipe and the mineral material (A) 12 (see FIG. 10) to be described later are used as raw materials to form a raw material of the raw material mineral aqueous solution (A) 41. The mineral aqueous solution production means 10; and the far-infrared rays generating means 43 which irradiates the far-infrared rays with the raw material mineral aqueous solution (A) 41 obtained by the raw material mineral aqueous solution manufacturing means 10, and changes to the mineral-containing water (A) 44.

The mineral water (B) manufacturing apparatus 3 has a function of forming a water containing a mineral component from a mineral-containing material by passing water W supplied from the outside through the water-passing containers 51 to 56. Mineral water (B) 45 function.

Hereinafter, the mineral-containing water (A) manufacturing apparatus 2 and the mineral-containing water (B) manufacturing apparatus 3 will be described in detail.

(3-2-1: Mineral-containing water (A) manufacturing device)

Next, with reference to FIG. 8 to FIG. 12, the description will be made regarding the constitution shown in FIG. The mineral water (A) manufacturing apparatus 2 of the mineral water manufacturing equipment 1. As shown in Fig. 7, the mineral water (A) manufacturing apparatus 2 forms a raw material mineral aqueous solution by using the water 11 supplied from the water pipe and the mineral providing material (A) 12 (see Fig. 10) to be described later as a raw material. (A) 41 raw material mineral aqueous solution manufacturing means 10 (refer to FIG. 8); and the mineral-containing water (A) solution 41 obtained by the raw material mineral aqueous solution manufacturing means 10 is irradiated with far infrared rays, and is changed into mineral-containing water. The far infrared ray generating means 43 of (A) 44 (refer FIG. 12).

As shown in FIG. 8 and FIG. 9, the raw material mineral aqueous solution manufacturing means 10 is provided with the reaction container 13 which can accommodate the water 11 and the mineral-grant material (A) 12, and is immersed in the reaction container in the state covered with the insulator 14. a conductive line 15 in the water 11 in the 13; an ultrasonic generating means 16 for imparting ultrasonic vibration to the water 11 in the reaction vessel 13, a direct current power source means 17 for conducting a direct current DC to the conductive line 15, and a conductive line The water 11 around the 15 generates circulation paths 18a and 18b and a circulation pump P of the means of the water flow R in the same direction as the direct current DC. The DC power supply unit 17, the ultrasonic generating means 16 and the circulating pump P are all operated by power supply from a general commercial power source.

The reaction container 13 has an inverted conical tubular shape with an upper opening, and a drain port 19 is provided at a bottom portion corresponding to the apex thereof, and a circulation path 18a communicating with the suction port P1 of the circulation pump P is connected to the drain port 19 at the drain port. Immediately below the 19, an opening degree adjusting valve 20 for adjusting the amount of displacement toward the circulation path 18a, and a drain valve 21 for discharging water or the like in the reaction vessel 13 are provided.

A proximal end portion of the circulation path 18b is connected to the discharge port P2 of the circulation pump P, and a distal end portion of the circulation path 18b is connected to the accommodation groove 22. A proximal end portion for conveying the water 11 in the storage tub 22 to the circulation path 18c in the reaction container 13 is connected in the vicinity of the bottom of the outer periphery of the housing groove 22, and the distal end portion of the circulation path 18c is disposed in the opening facing the reaction container 13. The location. An opening degree regulating valve 23 for adjusting the amount of water sent from the storage tub 22 to the reaction container 13 is provided in the circulation path 18c.

At the bottom of the storage tub 22, a drain pipe 24 having a drain valve 25 and a water temperature gauge 26 is connected in a hanging manner. When the drain valve 25 is opened as needed, the water in the storage tub 22 can be discharged from the lower end portion of the drain pipe 24. At this time, the temperature of the water 11 passing through the drain pipe 24 can be measured by the water temperature gauge 26.

As shown in FIG. 11, the plurality of conductive cables 29 (29a to 29g) composed of the conductive wire 15 and the insulator 14 covering the conductive wire are arranged in an annular shape so as to have different depths in the reaction container 13 At these positions, the annular conductive cables 29a to 29g are disposed slightly coaxially with the reaction container 13. The inner diameters of the respective conductive cables 29a to 29g are gradually reduced in diameter in accordance with the inner diameter of the reaction container 13 having an inverted cone shape, and are formed to have inner diameters corresponding to the respective arrangement portions. Since the respective conductive cables 29a to 29g are detachably connected to the insulating terminal device 30 provided in the wall body 13a of the reaction container 13, the annular portion can be removed or attached from the terminal device 30 as needed.

A bottomed cylindrical storage container 31 formed of an insulating mesh body is disposed in a portion corresponding to the axial center of the reaction container 13 and is disposed therein. The storage container 31 is filled with a mineral imparting material (A) 12. The storage container 31 is detachably locked to the upper edge portion of the wall body 13a of the reaction container 13 by a hook 31f provided on the upper portion thereof.

As shown in Fig. 8, on the outer circumferences of the circulation paths 18a and 18b, the conductive cables 29s and 29t are spirally wound, and DC current DC is supplied from the DC power supply unit 17 to the conductive cables 29s and 29t. The direction of the direct current DC flowing through the conductive cables 29s and 29t is set to substantially coincide with the direction of the water flow flowing through the circulation paths 18a and 18b.

In the raw material mineral aqueous solution production means 10, a predetermined amount of water 11 is placed in the reaction container 13 and in the storage tank 22, and the storage container 31 filled with the mineral-importing material (A) 12 is attached to the reaction container 13. After the center, the circulation pump P is actuated, and the opening degree adjustment valve 20 at the bottom of the reaction vessel 13 and the opening degree adjustment valve 23 of the circulation path 18c are adjusted, and the water 11 is passed from the reaction vessel 13 through the drain port 19, the circulation path 18a, The circulation pump P, the circulation path 18b, the storage tank 22, and the circulation path 18c are circulated again so as to return to the upper portion of the reaction container 13. When the DC power source device 17 and the ultrasonic wave generating means 16 are actuated, the mineral component starts from the elution reaction of the mineral material (A) 12 in the storage container 31 toward the water 11.

The working conditions in the case of producing the raw material mineral aqueous solution (A) using the raw material mineral aqueous solution production means 10 are not particularly limited. However, in the present embodiment, the raw material mineral aqueous solution (A) is produced under the following working conditions.

(1) DC current with voltage of 8000~8600V and current of 0.05~0.1A The DC is conducted through the conductive cables 29, 29s, 29t. Further, the insulator 14 constituting the conductive cable 29 and the like is formed of a polytetrafluoroethylene resin.

(2) The mineral-importing material (A) 12 filled in the reaction container 13 is filled with water 11 at a mass ratio of 10 to 15%. The specific description of the mineral-imparting material (A) 12 will be described later.

(3) The water 11 may be a catalyst containing a DC current DC. For example, sodium carbonate which dissolves about 10 g of electrolyte for 100 liters of water can be used, and if it is groundwater, it can be used as it is.

(4) The ultrasonic wave generating means 16 is a means for supersonic waves having a frequency of 30 to 100 kHz, and the ultrasonic wave generating portion (not shown) is placed in direct contact with the water 11 in the reaction container 13 to oscillate the ultrasonic wave. Means 16.

When the raw material mineral aqueous solution manufacturing apparatus 10 is operated under such conditions, the water flow R sucked by the drain port 19 while rotating in the left spiral direction is generated in the reaction container 13, and the water 11 discharged from the drain port 19 passes through the foregoing. The state in which the circulation paths 18a, 18b, and the like are returned to the reaction vessel 13 again continues.

Therefore, the action of the water flow R, the action of the direct current flowing through the conductive cable 29, and the ultrasonic vibration imparted by the ultrasonic wave generating means 16 to the water 11 can make the mineral component from the mineral material (A) 12 By rapidly dissolving into the water 11, the raw material mineral aqueous solution (A) in which the desired mineral component is moderately dissolved can be efficiently produced.

In the raw material mineral aqueous solution manufacturing apparatus 10, a plurality of conductive cables 29a to 29g which are formed in an annular shape are disposed on substantially the same axis in the reaction container 13, and a spiral direction toward the left is generated in the reaction container 13. Rotating water flow R. Therefore, a relatively dense electric field can be formed in the reaction container 13 having a constant volume, and the raw material mineral aqueous solution (A) can be efficiently produced in the reaction container 13 having a small volume.

Further, since the reaction container 13 has an inverted conical tubular shape, it is easier and stable to generate a water flow R flowing along a plurality of annular conductive cables 29a to 29g, thereby facilitating elution of mineral components. . Further, since the flow rate of the water R flowing in the inverted conical tubular reaction vessel 13 increases toward the drain port 19 at the bottom of the reaction vessel 13, the frequency of contact with the mineral-importing material (A) 12 is also Increasing, the mass of the mineral that captures and ionizes the free electrons e present in the water 11 can be increased.

Further, since the storage tank 22 that discharges the water 11 while being stored is provided between the circulation paths 18b and 18c, the mineral elution reaction can be performed while circulating the water 11 exceeding the volume of the reaction container 13. . Therefore, the raw material mineral aqueous solution (A) can be mass-produced efficiently.

When the circulation pump P is continuously operated to continue the reaction, the raw material mineral aqueous solution (A) in which the mineral component is eluted can be finally produced. The water can be controlled by the size of the drain port 19 at the bottom of the reaction vessel 13, the amount of circulating water, the shape of the reaction vessel 13 (especially the angle γ formed by the axis C and the wall 13a as shown in Fig. 8), and the like. In the state of occurrence of the free electrons e in 11, the water content of the mineral component can be controlled by the action of the free electrons e on the mineral-imparting material (A) 12.

After forming the raw material mineral aqueous solution (A), the raw material ore is The aqueous substance solution (A) 41 is transferred to the processing container 40 as shown in FIG. In this case, the residue of the mineral-imparting material (A) 12 leaking from the storage container 31 in the reaction container 13 can be discharged from the drain valve 21 located at the bottom of the reaction container 13. The raw material mineral aqueous solution (A) 41 accommodated in the processing container 40 is irradiated with far infrared rays by the far infrared ray generating means 43 disposed in the processing container 40 while being slowly stirred by the stirring blade 42.

Further, the far-infrared ray generating means 43 may be a far-infrared ray having a wavelength of about 6 to 14 μm, and may be a heating method because it is not affected by materials, generating means, or the like. However, it is desirable to have a radiation ratio of 85% or more for black body radiation in a wavelength region of 6 to 14 μm at 25 °C.

In the raw material mineral aqueous solution manufacturing apparatus 10 shown in FIG. 8, the action of the water flow R, the action of the direct current DC flowing on the conductive wire 15, and the ultrasonic vibration can make the mineral-containing material (A) The mineral component in 12 is rapidly dissolved in the water 11, and the desired mineral component is appropriately dissolved, whereby the mineral aqueous solution 41 can be efficiently produced.

Further, in the far-infrared ray generating means 43 shown in FIG. 12, by irradiating the mineral aqueous solution 41 with far-infrared rays, the dissolved mineral component is fused with water molecules to form a mineral-containing water having improved electronegativity (A) 44. .

In the mineral-containing water (A) manufacturing apparatus 2, the mineral-containing water (A) 44 formed by the above-described process is transported to the mixing tank 46 via the water supply path 57y as shown in Fig. 7, and is mixed in the mixing tank 46. The mineral-containing water (B) 45 sent from the mineral water (B) manufacturing apparatus 3 is mixed.

Hereinafter, the mineral-imparting material (A) will be described.

The mineral-improving material (A) is a plant material containing a plant of the genus Compositae and a plant of the family Rosaceae; and one or more woody plants selected from maple, birch, pine, and saplings. The woody plant material that is composed. The site to be used is preferably a part which is easy to elute mineral components such as leaves, stems, flowers, and bark, and can be used as it is, or a dried product can be used.

Furthermore, in addition to the plants of the genus Compositae and Rosaceae, other plants may be included, but only plants of the genus Compositae and Rosaceae are preferred.

An example of the mineral-imparting material (A) is a mineral-imparting material (A'-1). By using the mineral-imparting material (A'-1), it is possible to obtain mineral functional water (corresponding to the aforementioned mineral functional water (1)) having a control action against at least one of a single-celled organism and a virus.

For the mineral-based material (A'-1), the scorpion (leaf, stem, and flower), wormwood (leaf and stem), and mountain daisy (leaf and stem) are respectively a dried pulverized material of a compositae plant which is mixed, dried, and pulverized in a ratio of 8 to 12% by weight, 55 to 65% by weight, and 27 to 33% by weight; and use of wild rose (leaf, flower), and bayberry ( Leaf and stem), raspberry (leaf, stem, and flower) are mixed, dried, and pulverized at a ratio of 17 to 23% by weight, 8 to 12% by weight, and 65 to 75% by weight, respectively. A dry pulverized material of a plant of the genus Rosaceae, which is obtained by mixing the dried pulverized material of the genus Compositae with the dried pulverized material of the genus Rosaceae with a plant material (A1-1) obtained by mixing 1:0.8 to 1:1.2 (weight ratio) The aforementioned plant material, From maple (leaf and stem), birch (leaf, stem, and bark), cedar (leaf, stem, and bark) to 22 to 28% by weight, 22 to 28, respectively The woody plant material (A2-1) composed of a dry pulverized product which is mixed, dried, and pulverized at a ratio of 45% by weight to 45% by weight is used as the raw material of the woody plant, and the plant material (A1-1) is used as the plant material. The mineral material is obtained by mixing the weight ratio of the woody plant material (A2-1) to a ratio of 1:2.7 to 1:3.3.

In the above-mentioned mineral-imparting material (A'-1), in particular, as the raw material of the plant, the cockroach (leaf, stem, and flower), wormwood (leaf and stem), and mountain daisy ( The leaf part and the stem part are mixed and dried, and then pulverized in a ratio of 10% by weight, 60% by weight, and 30% by weight, respectively, and dried pulverized plants of the compositae, and wild rose (leaf, flower), arbutus Drying of the Rosaceae plant (leaf and stem) and raspberry (leaf, stem, and flower) at a ratio of 20% by weight, 10% by weight, and 70% by weight, respectively, and then pulverized a plant material (A1-1) obtained by mixing the pulverized material at a ratio of 1:1 (weight ratio); and as a raw material of the aforementioned woody plant, from maple (leaf and stem), birch (leaf, stem) And the sap (the leaf part, the stem part, and the bark part) are mixed, dried, and pulverized by a dry pulverized product at a ratio of 25% by weight, 25% by weight, and 50% by weight, respectively. The woody plant material (A2-1) is obtained by mixing the plant material (A1-1) and the woody plant material (A2-1) in a weight ratio of 1:3. Sheet material which imparts better.

For example, the RIKEN Techno System Co., Ltd. product [P-100 (product number)] is used as the plant material (A1-1) which is a raw material of the mineral-based material (A'-1). For example, [P-200 (product number)] manufactured by Riken Chemical Technology Co., Ltd. is used as the woody plant material (A2-1). In addition, the mineral functional water CAC-717 [Tera Protect (product name), CAC-717 (product number)] manufactured by Riken Chemical Technology Systems Co., Ltd. is [P-100 (product number)], [P-200] (Product No.)] Mineral functional water.

Further, as an example of another preferable mineral-imparting material (A), a mineral-imparting material (A'-2) can be mentioned. By using the mineral-imparting material (A'-2), mineral functional water (corresponding to the aforementioned mineral functional water (2)) having body activation can be obtained.

The mineral-improving material (A'-2) is a mineral-imparting material, that is, as a plant material of the above-mentioned plant, a large scorpion (leaf, stem, and flower), wormwood (leaf and stem) (part), the succulent (the leaf part and the stem part), which are mixed, dried, and pulverized at a ratio of 10% by weight, 60% by weight, and 30% by weight, respectively, and dried smashed plants of the compositae, and wild rose (leaf, Flower part), bayberry (leaf part and stem part), raspberry (leaf part, stem part, and flower part) are mixed, dried, and pulverized at a ratio of 20% by weight, 10% by weight, and 70% by weight, respectively. a plant material (A1-2) obtained by mixing a dried pulverized plant of a Rosaceae plant at a ratio of 1:1 (weight ratio); and as a raw material of the aforementioned woody plant, a maple tree (deciduous), a birch tree (deciduous, The stem portion and the bark portion, and the cedar (deciduous, stem, and bark portions) are mixed at a ratio of 20% by weight, 60% by weight, and 20% by weight, respectively. The woody plant material (A2-2) composed of the dried and pulverized dried pulverized material is formed into a 1:5 weight ratio of the plant material (A1-2) to the wood material (A2-2). The mineral-donating material obtained by mixing is obtained.

For example, the RIKEN Techno System Co., Ltd. product [P-101 (product) is used as the raw material of the plant material (A1-2) which is a raw material of the mineral-based material (A'-2). In the case of the woody plant material (A2-2), for example, [P-201 (product number)] manufactured by Riken Chemical Technology Co., Ltd. is mentioned. In this way, the mineral functional water A20ACA-717 [Tera Support (trade name), A20ACA-717 (product number)] manufactured by Riken Chemical Technology Systems Co., Ltd. can be obtained.

Further, as an example of another preferable mineral-imparting material (A), a mineral-imparting material (A'-3) can be mentioned. By using the mineral-imparting material (A'-3), it is possible to obtain mineral functional water (corresponding to the aforementioned mineral functional water (3)) having a combustion-promoting action of hydrocarbons.

The mineral-improving material (A'-3) is a mineral-imparting material, that is, as a plant material of the above-mentioned plant, a large scorpion (leaf, stem, and flower), wormwood (leaf and stem) (part), the succulent (the leaf part and the stem part), which are mixed, dried, and pulverized at a ratio of 10% by weight, 60% by weight, and 30% by weight, respectively, and dried smashed plants of the compositae, and wild rose (leaf, Flower part), bayberry (leaf part and stem part), raspberry (leaf part, stem part, and flower part) are mixed, dried, and pulverized at a ratio of 20% by weight, 10% by weight, and 70% by weight, respectively. a plant material (A1-1) obtained by mixing a dry pulverized plant of a Rosaceae plant at a ratio of 1:1 (weight ratio); and As the raw material of the woody plant, the maple (leaf and stem), the birch (leaf, stem, and bark), the cedar (leaf, stem, and bark) are respectively 25 weights. a woody plant material (A2-1) composed of a dry pulverized product which is mixed, dried, and pulverized at a ratio of %, 25% by weight, and 50% by weight; and carbonized at a activation temperature of 1000 ° C as an activated carbon The activated carbon powder (A3-1) is composed of a mixture of the plant material (A1-1) and the wood material (A2-1) in a weight ratio of 1:3, and the activated carbon powder ( A3-1) A mineral-imparting material obtained by mixing in a form of 2 to 8 parts by weight.

Here, the activated carbon powder (A3-1) is an activated carbon powder obtained by carbonizing a coconut shell at an activation temperature of 1000 ° C in an inert gas atmosphere, and when it is added to pure water in a form of 10% by weight. The activated carbon powder having a pH of 9 to 11, preferably 9.5 to 10.5, more preferably pH 10.

Further, when the coconut shell is activated at a low temperature, the alkali tends to become strong, but when activated at 1000 ° C, it is formed into a weakly alkaline state.

The addition amount of the activated carbon powder (A3-1) is added to the mineral-imparting material (A-1) to form a pH of 11 to 12 when the mineral-containing water (A) and the mineral-containing water (B) are mixed. When the mixture of the plant material (A1-1) and the woody plant material (A2-1) is 100 parts by weight in a weight ratio of 1:3, it is formed into a range of 2 to 8 parts by weight. .

As the plant material (A1-1) which is a raw material of the mineral-imparting material (A'-3), for example, the Riken Chemical Technology System (RIKEN) [P-100 (product number)] manufactured by Techno System Co., Ltd., and as a woody plant material (A2-1), for example, [P-200 (product number)] manufactured by Riken Chemical Technology Co., Ltd. The carbon powder (A3-1) is, for example, [AS-100 (product number)] manufactured by Riken Chemical Technology Co., Ltd.

Further, as an example of another preferable mineral-importing material (A), a mineral-imparting material (A'-4) can be mentioned. By using the mineral-imparting material (A'-4), it is possible to obtain mineral functional water (corresponding to the aforementioned mineral functional water (4)) having an antioxidant action.

The mineral-improving material (A'-4) is a mineral-imparting material, that is, as a plant material of the above-mentioned plant, a large scorpion (leaf, stem, and flower), wormwood (leaf and stem) The part of the genus, the genus of the genus of the genus of the genus of the genus of the genus of the genus of the genus of the genus of the genus of the genus Part), bayberry (leaf and stem), raspberry (leaf, stem, and flower) are mixed, dried, and pulverized at a ratio of 20% by weight, 10% by weight, and 70% by weight, respectively. a plant material (A1-2) obtained by mixing a dry pulverized plant of a Rosaceae plant at a ratio of 1:1 (weight ratio); and as a raw material of the aforementioned woody plant, a maple tree (deciduous), a birch tree (deciduous, stalk) Wood, which is composed of dried pulverized material which is mixed, dried, and pulverized at a ratio of 20% by weight, 60% by weight, and 20% by weight, respectively, in cedar (deciduous, stalk, and bark) The plant material (A2-2); and the volcanic sulfur (A3-2) as a sulfur raw material, the plant material (A1-2) and the wood plant Starting material (A2-2) in a weight The mineral material obtained by mixing the volcanic sulfur (A3-2) to a weight of 2 to 8 parts by weight is formed by mixing 1:5.

Here, volcanic sulfur (A3-2) is a sulfur-containing substance present in a volcano. The volcanic sulphur (A3-2) is dissolved or dispersed when the water is circulated, and the sulphur component is dissolved in the mineral-containing water (A). When volcanic sulfur (A3-2) is used as sulfur, it is preferable to strongly produce the anti-inflammatory action and anti-oxidation characteristic characteristic of the mineral functional water of the present invention. It is preferred to pulverize the volcanic sulfur (A3-2) to form a powder.

The volcanic sulfur (A3-2) is added in an amount of 100 parts by mixing the plant material (A1-2) with the woody plant material (A2-2) in a weight ratio of 1:5. In the case of the part, it is formed in the range of 2 to 8 parts by weight.

As the grass plant material (A1-2), it is preferable to use [P-101 (product number)] manufactured by RIKEN Techno System Co., Ltd. as a woody plant material (A2-2). [P-201 (product number)] manufactured by Riken Chemical Technology Systems Co., Ltd. was used. Further, as the volcanic sulfur (A3-2), [S-100 (product number)] manufactured by Riken Chemical Technology Co., Ltd. can be preferably used.

(3-2-2: Mineral water (B) manufacturing equipment)

Next, the structure, function, and the like of the mineral-containing water (B) manufacturing apparatus 3 will be described with reference to Figs. 7 and 13 .

As shown in FIG. 7 and FIG. 13, the mineral water (B) manufacturing apparatus 3 is provided with the first water which is filled with the mineral material providing material (B) of a different type. The container 51 to the sixth water-passing container 56; the water supply path 57 that connects the first water-passing container 51 to the sixth water-passing container 56 in series; and the first water-passing container 51 to the sixth water-passing container 56 are arranged side by side. In the state, the bypass water passages 51p to 56p connected to the water supply path 57; and the water flow switching valves 51v to 56v provided in the branch portions of the respective bypass water passages 51p to 56p and the water supply path 57 are provided.

The switching operation of the water flow switching valves 51v to 56v can be performed by operating the six switching knobs 51b to 56b provided on the operation panel 58 connected to the water flow switching valves 51v to 56v by the signal cable 59. Since the six switching buttons 51b to 56b and the six water flow switching valves 51v to 56v correspond to individual numbers, when one of the switching buttons 51b to 56b is operated, the water flow switching valve 51v of the corresponding number is operated. The 56v is switched to change the direction of the water flow.

Further, the first water-passing container 51 is filled with a mineral-imparting material (B) 51m containing cerium oxide and iron oxide, and the second water-passing container 52 is filled with a cerium oxide-containing activated carbon ore. The material-imparting material (B) is 52 m, and the third water-passing container 53 is filled with a mineral-imparting material (B) 53 m containing cerium oxide and titanium nitride, and is filled in the fourth water-passing container 54 with two The mineral-supporting material (B) of cerium oxide and calcium carbonate is 54 m, and the fifth water-passing container 55 is filled with a mineral-imparting material (B) containing cerium oxide and magnesium carbonate (B) 55 m, and is in the sixth water-passing container 56. The inside was filled with a mineral-imparting material (B) containing cerium oxide and calcium phosphate (56 m).

Here, the mineral-imparting material (B) is 51 m to 56 m, and it is preferable to be produced by mixing raw materials containing limestone, coral fossils, and shells as a base material.

First, the components contained in limestone, coral fossils, and shells were analyzed, and the amounts of cerium oxide, iron oxide, activated carbon, titanium nitride, calcium carbonate, magnesium carbonate, and calcium phosphate contained in each of them were evaluated. In addition, limestone, coral fossils, and shells are mixed to prepare a mineral-importing material (B) of 51 m to 56 m based on the content of each component.

In addition, it is expected that the mineral-based material (B) 51m to 56m is controlled by the mixing ratio of limestone, coral fossil, and shell, but the limestone, coral fossil, and shell as raw materials may have a relationship with the place of origin. In the case where the content of the component is insufficient, the cerium oxide, the iron oxide, the activated carbon, the titanium nitride, the calcium carbonate, the magnesium carbonate, or the calcium phosphate may be added as needed. In particular, activated carbon is rarely contained in limestone, coral fossils, and shells, so it is generally added.

The mineral-importing material (B) is 51 m to 56 m, and the mineral-imparting material (B1) in the first water-passing container 51 contains 70% by weight of limestone, 15% by weight of coral fossil, and 15% by weight of shells. The mixture-providing material (B2) in the second water-passing container 52 is a mixture containing 40% by weight of limestone, 15% by weight of coral fossil, 40% by weight of shells, and 5% by weight of activated carbon; The mineral-imparting material (B3) in the water-passing container 53 is a mixture containing 80% by weight of limestone, 15% by weight of coral fossil, and 5% by weight of shells, and a mineral-donating material in the fourth water-passing container 54 ( B4) is 90% by weight of limestone, 5% by weight of coral fossil, and 5% by weight of shells The mixture-providing material (B5) in the fifth water-passing container 55 is a mixture containing 80% by weight of limestone, 10% by weight of coral fossil, and 10% by weight of shells, respectively; and 6th water-passing container 56 When the mineral-importing material (B6) is a mixture containing 60% by weight of limestone, 30% by weight of coral fossil, and 10% by weight of shells, it can be excellently detrimental when mixed with mineral-containing water (A). Mineral water (B) for biological control.

In particular, it is preferable that the limestone, the coral fossil, and the shell used for the mineral-imparting materials (B1) to (B6) are the following (1-1) to (1-3).

(1-1) Limestone:

About 3 cm of pebbles formed by pulverizing limestone in which volcanic sediments containing the following components are mixed

Calcium carbonate: 50% by weight or more

Iron oxide: 3~9 wt% iron

The total of titanium oxide, titanium carbide, and titanium nitride: 0.8% by weight or more

Magnesium carbonate: 7 to 10% by weight.

As such a limestone, [CC-200 (product number)] manufactured by Riken Chemical Technology Co., Ltd. can be preferably used.

(1-2) Coral fossils:

The following two kinds of coral fossils are mixed in a weight ratio of 1:9 and pulverized into granules formed by 3 to 5 mm.

A coral fossil that is produced from a depth of about 100 meters under the ground, which is made into a denatured crystal by heavy pressure; a coral fossil (a trace element containing calcium carbonate, calcium phosphate, etc.) produced from the land near Okinawa Oshima.

As such a coral fossil, [CC-300 (product number)] manufactured by Riken Chemical Technology Systems Co., Ltd. can be preferably used.

(1-3) Shell:

Abalone, nine-hole, and barnacle are mixed and pulverized into 3~5mm granules with the same weight.

As such a shell, [CC-400 (product number)] manufactured by Riken Chemical Technology Co., Ltd. can be preferably used.

(1-4) Activated carbon

As the activated carbon, those produced from any raw material can be used, but activated carbon produced by using coconut shell as a raw material is preferable. For example, [CC-500 (Product No.)] manufactured by Riken Chemical Technology Systems Co., Ltd., which is made from coconut shells made in Thailand.

When the switching knobs 51b to 56b of the operation panel 58 are operated and the water flow switching valves 51v to 56v are switched toward the water container side, the water flowing through the water supply path 57 is directed to the downstream side of the water flow switching valve that is already operated. When the first water-passing container 51 to the sixth water-passing container 56 are inflow, if the water-flow switching valves 51v to 56v are switched to the bypass waterway side, the water flowing through the water supply path 57 is directed to the water flow switching valve that is already operated. Downstream water The road 51p~56p flows in. Therefore, by selectively switching the water flow switching valves 51v to 56v by operating any of the switching buttons 51b to 56b, it is possible to form different mines for each of the first water passing containers 51 to the sixth water passing container 56. The material-imparting material (B) contains mineral water (B) 45 in which the mineral component eluted from 51 m to 56 m is selectively dissolved.

Next, the structure and function of the mineral-containing water (B) manufacturing apparatus 3 will be described with reference to Figs. 14 to 17 . Further, in FIGS. 14 to 16, the bypass water passages 51p to 56p, the water flow switching valves 51v to 56v, the operation panel 58 and the signal cable 59 are omitted.

As shown in FIG. 14 and FIG. 15, the mineral water-containing (B) manufacturing apparatus 3 includes a first water-passing container 51 to a sixth water-passing container 56 that are mounted on the gantry 60 in a substantially cylindrical shape; The water supply path 57 in which the first water-passing container 51 to the sixth water-passing container 56 are connected in series, and the raw water tank 63 for storing the water W supplied from the water pipe is disposed at the uppermost portion of the gantry 60. In the raw water tank 63, an inorganic porous body 64 having a function of adsorbing impurities in the water W is housed. At the bottom of the gantry 60, a plurality of casters 61 and a level adjuster 62 are provided. The first water-passing container 51 to the sixth water-passing container 56 having a substantially cylindrical shape are placed on the gantry 60 of the rectangular parallelepiped lattice structure while holding the respective axial centers 51c to 56c (see FIG. 15) in the horizontal direction. The first water-passing container 51 to the sixth water-passing container 56 can detach the gantry 60.

As shown in Fig. 16, the first water-passing container 51 to the sixth water-passing container 56 have the same structure, and the disk-shaped lid bodies 51d to 56d are attached to the cylindrical body portions 51a to 56a. Flange at both ends 51f~56f, forming an airtight structure. When the axial centers 51c to 56c are in a horizontal state, a water inlet 57a communicating with the water supply path 57 is provided at a portion located at the lowermost portion of the main body portions 51a to 56a, and a cover 51d at a position farther from the water inlet 57a. The uppermost portion of the ~56d is provided with a water outlet 57b that communicates with the water supply path 57, and a screen 57c is attached to the water outlet 57b. An automatic air valve 57d for detaching the gas in the first water-passing container 51 to the sixth water-passing container 56 is attached to a portion directly above the water outlet 57b on the outer circumference of the main body portions 51a to 56a.

The water supplied from the upstream water supply path 57 flows into the first water-passing container 51 to the sixth water-passing container 56 through the water inlet 57a, and the mineral-imparting material (B) filled in each of the interiors is 51 m to 56 m. After the contact, the mineral components are dissolved in the water. Therefore, the water is contained in the water containing the mineral component corresponding to the individual mineral material (B) 51m to 56m, and the water is supplied from the water outlet 57b to the downstream side. Path 57 flows out.

The mineral-containing water (B) manufacturing apparatus 3 shown in Figs. 14 to 16 is operated in the raw water tank 63 by operating one of the switching knobs 51b to 56b of the operation panel 58 as shown in Fig. 13. The water W passes through one or more water-passing containers in the first water-passing container 51 to the sixth water-passing container 56, and can form mineral-containing water (B) 45, which is selectively dissolved in individual water. The mineral component contained in the mineral-importing material (B) 51m to 56m filled in the first water-passing container 51 to the sixth water-passing container 56 is characteristic.

Further, in the mineral-containing water (B) manufacturing apparatus 3, the first water-passing container 51 to the sixth water-passing container 56 are connected in series by the water supply path 57. Therefore, by continuously flowing water to the water supply path 57, the mineral-containing water (B) 45 can be produced in a large amount, and the mineral-containing water (B) 45 is dissolved in the first water-passing container. The mineral material of the 51 to 6th water-passing container 56 (B) is a mineral component of 51 m to 56 m.

Further, the mineral-containing water (B) 45 formed in the mineral-containing water (B) manufacturing apparatus 3 is transported into the mixing tank 46 via the water supply path 57x located further downstream than the sixth water-passing container 56. In the inside thereof, it is mixed with the mineral-containing water (A) 44 produced by the mineral-containing water (A) manufacturing apparatus 2 shown in Fig. 7, thereby forming the mineral functional water 47.

The ratio of the mineral-containing water (A) to the mineral-containing water (B) is determined by considering the type of the raw material contained in the mineral-containing water (A) and the mineral-containing water (B) and the concentration of the dissolved components. Decide, however, that the weight ratio of mineral-containing water (A) to mineral-containing water (B) ([mineral water (A)]: [mineral water (B)]) is 1:5~ The range of 1:20 is ideally in the range of 1:7 to 1:12, and more preferably in the range of 1:10.

In the case of too little mineral water (A) (excessive mineral water (B)), and too much mineral water (A) (mineral water (B) too little), there will be mineral water The active ingredient is diluted and the effect of the desired purpose becomes insufficient.

In the above, a preferred embodiment of the method for producing mineral water according to the present invention is described. However, the present invention is not limited to the embodiments, and the mineral functional water of the present invention having the above configuration can be produced, and in addition to the above-described preferred embodiment. Various structures can also be used. In particular, in the embodiments disclosed herein, items that are not explicitly disclosed, such as operating conditions, The operating conditions, various parameters, the size, weight, volume, and the like of the components are those that do not exceed the scope generally practiced by the industry, and are generally conceivable values for the industry.

[Examples]

Hereinafter, the present invention will be specifically described by way of examples, but the invention is not limited to the examples.

The elution functional water manufacturing apparatus 100 disclosed in the embodiment of the present invention is used to produce the elution functional water. The eluted ceramic material used in the manufacturing apparatus, the non-lead-type ceramic material, and the mineral functional water fixed to the ceramic materials are prepared as follows.

[Example 1]

<1>Manufacture of mineral functional water

As the mineral functional water, the mineral functional water of Example 1 produced by the following raw materials and methods was used in the above-described mineral functional water producing apparatus (mineral functional water producing apparatus 1).

1. Manufacture of mineral-containing water (A)

The mineral-imparting material (A'-1) was used as the mineral-imparting material (A). As the plant material (A1-1) of the raw material of the mineral-importing material (A'-1) of the first embodiment, the RIKEN Techno System Co., Ltd. product [P-100 (product number)] was used. As a woody plant material (A2-1), [P-200 (product number)] manufactured by Riken Chemical Technology Systems Co., Ltd. was used.

[P-100] is a plant material obtained by mixing the dried ground material of the following Compositae plants with the dried ground material of the Rosaceae plant at a ratio of 1:1 (weight ratio), [P-200] is described below. Woody plant material.

(A1) Raw material of grass plants (dried plants)

(A1-1) Dry pulverized material of Compositae

The cockroach (leaf, stem, and flower), wormwood (leaf and stem), and gerbera (leaf and stem) were each 10% by weight, 60% by weight, and 30% by weight, respectively. The dried pulverized material is mixed, dried, and pulverized.

(A1-2) Dry pulverized material of Rosaceae plants

The ratio of 20% by weight, 10% by weight, and 70% by weight of wild rose (leaf, flower), bayberry (leaf and stem), and raspberry (leaf, stem, and flower) was used. The dried pulverized material is mixed, dried, and pulverized.

(A2) Woody plant material (dried woody plant)

Maple (leaf and stem), birch (leaf, stem, and bark), cedar (leaf, stem, and bark) are 25% by weight, 25% by weight, and 50, respectively. The dry pulverized material is mixed, dried, and pulverized in a ratio of % by weight.

The grass plant material (A1) and the woody plant material (A2) are mixed at a ratio of 1:3 (by weight) in a manner of 10 to 15% by weight of water. The formed mineral-imparting material (A) is placed in the raw material mineral aqueous solution manufacturing means 10 (refer to FIG. 8) in the mineral-containing water (A) manufacturing apparatus 2 shown in FIG. 7, and the direct current is further applied ( DC8300V, 100 mA) is conducted to the conductive wire of the raw material mineral aqueous solution manufacturing means 10, so that the water around the conductive wire generates a water flow in the same direction as the direct current, and then imparts ultrasonic vibration to the water (oscillation frequency: 50 kHz, amplitude: 1.5/1000 mm) Forming a raw material mineral aqueous solution (A). Then, the mineral-containing water (A) of Example 1 is irradiated with far-infrared rays (wavelength: 6 to 14 μm) by the raw material mineral aqueous solution (A) supplied to the far-infrared generation means 43 of the subsequent stage, thereby obtaining the mineral-containing water (A) of the first embodiment.

2. Manufacture of mineral-containing water (B)

As a raw material of the mineral-imparting material (B), a mixture in which limestone, coral fossil, shell, and activated carbon are pulverized and mixed is used. The raw material of the mineral-imparting material (B) and the mixture (mineral-imparting materials (B1) to (B6)) used in the first to sixth water-passing containers are as follows.

(1) Raw materials

(1-1) Limestone: manufactured by Riken Chemical Technology Systems Co., Ltd. [CC-200 (Product No.)]

About 3 cm of pebbles formed by pulverizing limestone in which volcanic sediments containing the following components are mixed

Calcium carbonate: 50% by weight or more

Iron oxide: 3~9 wt% iron

The total of titanium oxide, titanium carbide, titanium nitride: 0.8% by weight on

Magnesium carbonate: 7 to 10% by weight.

(1-2) Coral fossil: manufactured by Riken Chemical Technology Systems Co., Ltd. [CC-300 (Product No.)]

The following two kinds of coral fossils are mixed in a weight ratio of 1:9 and pulverized into granules formed by 3 to 5 mm.

A coral fossil that is produced from a depth of about 100 meters under the ground, which is made into a denatured crystal by heavy pressure; a coral fossil (a trace element containing calcium carbonate, calcium phosphate, etc.) produced from the land near Okinawa Oshima.

(1-3) Shell: manufactured by Riken Chemical Technology Systems Co., Ltd. [CC-400 (Product No.)]

The abalone, the nine holes, and the barnacle are mixed and pulverized into the granules of 3 to 5 mm with the same weight.

(1-4) Activated carbon (used only in the second water container): manufactured by Riken Chemical Technology Systems Co., Ltd. [CC-500 (product number)]

(2) Proportion of use in the first to sixth water containers

The first water container:

Mineral imparting material (B1): a mixture containing 70% by weight of limestone, 15% by weight of coral fossil, and 15% by weight of shells, respectively;

2nd water container:

Mineral material-imparting material (B2): a mixture of 40% by weight of limestone, 15% by weight of coral fossil, 40% by weight of shells, and 5% by weight of activated carbon (corresponding to cerium oxide and activated carbon);

3rd water container:

Mineral imparting material (B3): a mixture containing 80% by weight of limestone, 15% by weight of coral fossil, and 5% by weight of shells, respectively;

4th water container:

Mineral imparting material (B4): a mixture containing 90% by weight of limestone, 5% by weight of coral fossil, and 5% by weight of shells, respectively;

5th water container:

Mineral imparting material (B5): a mixture containing 80% by weight of limestone, 10% by weight of coral fossil, and 10% by weight of shells, respectively;

The sixth water container:

Mineral material-imparting material (B6): a mixture containing 60% by weight of limestone, 30% by weight of coral fossil, and 10% by weight of shells, respectively; and the mineral-functional water producing apparatus 1 structured as shown in Fig. 7 by circulating water The mineral water (B) is obtained by using the first to sixth water-passing containers of the mineral-imparting materials (B1) to (B6). (B1) to (B6) were set to 50 kg (total 300 kg), the amount of water flowing was 1000 kg, and the flow rate was 500 mL/40 s.

The mineral-containing water (A) of Example 1 and the mineral-containing water (B) which were carried out in the above method were mixed to form a 1:10 (weight ratio) to obtain the mineral functional water of Example 1. . Using a pH measuring device (Glass Electrode Hydrogen Concentration Indicator TPX-90 made by Dongxing Chemical Research Institute) The mineral functional water of Example 1 was measured, which was pH 12.5.

In addition, the mineral functional water of the first embodiment is equivalent to the mineral functional water CAC-717 manufactured by Riken Chemical Technology Co., Ltd. [Tera Protect (product name), CAC-717 (product number), development product number CA -C-01].

<2-1>Manufacture of hardened cement (solubility ceramic material)

20 parts by weight of the mineral functional water of the first embodiment, white cement (made of Pacific cement) as a cement composition: 50 parts by weight, vermiculite powder (SiO ₂ ) 15 parts by weight, limestone (containing 50% by weight of CaCO) ₃ of sedimentary rocks) to 15 wt mixer unit for mixing to obtain a cement mixing material. The obtained cement mixture was cured for 3 days and cured to obtain a cement hardened body of Example 1 (the eluted ceramic material of Example 1).

<2-2> Manufacture of ceramic sintered body (non-lead-type ceramic material)

A predetermined amount of water was added to 100 parts by weight of the ceramic powder for carrier (the rock powder of Amakusa Oyao Island) to obtain a clay-like mixture. The obtained clay-like mixture was formed into a flat plate shape having a circular surface having a thickness of about 5 mm and a diameter of 2 cm, and baked at 500 ° C for 8 hours to obtain a porous calcined body.

Next, the weight portion of the porous calcined body 100 was uniformly impregnated with 15 parts by weight of the mineral functional water of Example 1, and dried for several days. The glazing treatment for imparting a glaze equivalent to 5 parts by weight is carried out, followed by heat treatment (true firing) at 1200 ° C to obtain immobilized minerals. The ceramic sintered body of Example 1 of the functional component of the functional water (non-lead-type ceramic material of Example 1).

Further, as a control sample, a ceramic sintered body in which the porous calcined body was not subjected to mineral functional water and heat-treated was produced.

The spectral emissivity of the sample (ceramic sintered body) was measured by a far-infrared emissivity measuring device (JIR-E500 manufactured by JEOL Ltd.). The device is composed of a Fourier transform infrared spectrophotometer (FTIR) body, a black body furnace, a sample heating furnace, a temperature controller, and an attached optical system.

18 is a graph showing the results of evaluation of the ratio of the emission ratio of the ceramic sintered body of Example 1 and the ceramic sintered body of the uncured mineral component (control sample) to the black body at 25 ° C, which corresponds to when the radiation intensity of the black body is set to The ratio of the radiation intensity (radiation ratio) of each ceramic sintered body in the case of 100%.

It was confirmed that the ceramic sintered body of Example 1 containing the mineral component had a high emission ratio in the measured wavelength range and significantly generated electromagnetic wave radiation, compared to the control sample containing no mineral.

<3> Evaluation of dissolving functional water

<3-1 Solvent Test>

In the first treatment tank 110 of the elution functional water production apparatus 100, the cement hardened body (the eluted ceramic material) of the first embodiment is housed, and the ceramic sintered body of the first embodiment is housed in the second treatment tank 150 (non-lytic type) The ceramic material circulates water as an extraction solvent from the water supply pipe 117 of the first treatment tank 110. The amount of cement hardened body, ceramic sintered body and water to be circulated to be contained is The elution functional water W1 discharged from the first treatment tank 110 is adjusted to have a pH of 10.5 to 11.5, and the elution functional water W2 discharged from the second treatment tank 150 is formed to have a pH of 12 or more. The obtained elution functional water W2 is described below as the elution functional water of Example 1.

The component analysis of the solute functional water of Example 1 revealed that the mineral inorganic mineral component such as calcium ion, strontium ion, or sodium ion and the plant organic component (polyphenol) were eluted.

<3-2. Virus inactivation test>

The following virus was subjected to an inactivation test using the leaching functional water of Example 1.

‧Adenovirus 5 (ATCC VR-5)

‧ Herpes simplex virus 1 (ATCC VR-539)

‧Feline calicivirus (ATCC VR-782): Norovirus instead

‧ Influenza A virus (Influenza A virus, H1N1, ATCC VR-1469)

As a comparative example, the following liquids were used.

Comparative Example 1: sodium hypochlorite solution

Comparative Example 2: Phosphate buffered saline (PBS).

The virus inactivation test was carried out in the following manner.

(1) The capacity of the solvent functional water (or Comparative Examples 1, 2) of Example 1 (10 mL) was mixed with a virus solution 1 volume (0.1 mL). Stirring was carried out without using a test tube stirrer and allowed to act on the virus during 15 seconds.

(2) Next, the effect of the test water on the virus was stopped by diluting it to 10-fold with SCDLP supplemented with 0.1% sodium thiosulfate.

(3) The liquid of (2) was used as a stock solution for the sample for measuring the titer of infection titer, and the viral infection titer was measured.

The results of the inactivation test of adenovirus type 5 (Table 1), herpes simplex virus type 1 (Table 2), feline calicivirus (Table 3), and influenza A virus (Table 4) are shown below. The unit of infection titer was TCID ₅₀ /mL, the detection limit was 1.3 × 10 ¹ TCID ₅₀ /mL, and the log reduction value was log ₁₀ (initial infection titer / infection titer after 15 seconds of action).

In the leaching machine water of Example 1, it was confirmed that the virus was inactivated by PBS in each virus, and the effect was comparable to that of sodium hypochlorite.

[Industry use possibility]

The leaching machine water produced by the lysate water-making apparatus of the present invention can be widely used in various industries because it has an effective performance derived from the mineral components contained therein.

100‧‧‧Soliding machine water manufacturing device (double treatment tank)

110‧‧‧First treatment tank

111, 151‧‧‧ shell

111a, 111b, 151a, 151b‧‧‧Flange

112, 152‧‧‧ water path

113,153‧‧‧Water path

114‧‧‧Water injection path

115,116,155,156‧‧‧ cover

117‧‧‧Water supply pipe

119‧‧‧Drainage path

125‧‧‧ pillar

150‧‧‧Second treatment tank

154a‧‧‧Operation lever

154b‧‧‧Opening valve

157‧‧‧ casters

158‧‧‧Link path

159‧‧‧Outlet

G‧‧‧ Ground

P‧‧‧ cushion

Claims (11)

An apparatus for producing a water for dissolving functional water, which is a device for producing a water for solvating water containing a mineral component, comprising: two or more treatment tanks, wherein the treatment tank has a water inlet path and a water outlet path, and The water flowing in from the water inlet path or the extraction solvent mainly composed of water may flow inside the water outlet path; and a connection path connecting the water outlet path of one of the treatment tanks to the water inlet path of the other treatment tank, The plurality of processing tanks are connected in series via the connecting path, and at least one of the processing tanks contains a eluting ceramic material in which the mineral component is immobilized in an eluted manner. The apparatus for producing a melt-dissolving functional water according to the first aspect of the invention, wherein the manufacturing apparatus is provided with a water injection path that communicates with the processing tank in which the eluted ceramic material is accommodated. The apparatus for producing a melt-dissolving water according to the first aspect of the invention, wherein at least one of the treatment tanks other than the treatment tank containing the dissolution-type ceramic material contains a mineral component which is immobilized without elution Non-lead type ceramic material. The apparatus for producing a melt-dissolving functional water according to the third aspect of the invention, wherein at least one of the treatment tanks containing the eluted ceramic material is disposed in a treatment for storing the non-lead-type ceramic material The upstream side of the tank. The dissolution function as claimed in any one of claims 1 to 4 In the water manufacturing apparatus, the two processing tanks are connected in series via the connecting path. The apparatus for producing a melt-dissolving water according to the fifth aspect of the invention, wherein the processing tank located on one of the upstream sides of the connecting path is disposed at a position higher than the processing tank of the other one. The apparatus for producing a melt-dissolving water according to the fifth aspect of the invention, wherein the water discharge path of the processing tank located on the downstream side of the connecting path is provided at an uppermost portion of the processing tank. A method for producing a water for emulsification, which is characterized in that it has the following process, that is, a device for producing a water for dissolving functional water according to any one of claims 1 to 7, a water supply or a water-based extraction The solvent is a process for bringing water or a water-based extraction solvent into contact with the aforementioned eluted ceramic material of one of the treatment tanks contained in the treatment tank. A method for producing a water for dissolving functional water, characterized by having the following process, that is, a device for producing a water for dissolving functional water according to any one of claims 3 to 7, a water supply or a water-based extraction The solvent is a process in which water or a water-based extraction solvent is brought into contact with the above-described eluted ceramic material and the non-lead-type ceramic material of one of the treatment tanks contained in the treatment tank. The method for producing a water for dissolving functional water according to claim 9, wherein the method further comprises the following processes, and even if the water or the extraction solvent mainly composed of water is contacted with the eluted ceramic material, the decomposed ceramic is further used. A process in which a material in contact with water or a water-based extraction solvent is contacted with a non-lead-type ceramic material. The method for producing a water for solute water according to any one of claims 5 to 7, wherein the apparatus for producing a water for solute water is used.