JP2006219391A - Deep water powder and deep water tablet - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To pulverize liquid bittern and a material separated from deep water to facilitate their utilization for dried products and the like. <P>SOLUTION: The deep water powder of the present invention is characterized by pulverizing one selected from fresh water 1b and concentrated sea water 2b separated from ocean deep water B with a reverse osmotic membrane apparatus 2, fresh water b1 and concentrated deep water b2 separated with a multistage electrodialyzer 1, mineral-concentrated water b3 and concentrated salt water b4, with a pulverization means 3. The powder bittern of the present invention is characterized by pulverizing one selected from sea water-based bittern water a5 obtained from sea water A, deep water-based bittern water b5 obtained from ocean deep water B, inherent cold water-based bittern water c5 obtained from cold water C inherent to Toyama bay, and rock salt-based bittern water d5 obtained from a rock salt D, with a pulverization means 3. <P>COPYRIGHT: (C)2006,JPO&NCIPI

Description

This invention relates to deep water powder and deep water tablets made from deep sea water (cold cold water of Toyama Bay) as a raw material,
Deep water powder is powdered fresh water and concentrated seawater from which deep sea water is separated by reverse osmosis membrane, and fresh water, concentrated deep water, mineral concentrate and concentrated salt water from which deep sea water is separated by multistage electrodialysis. The deep water tablet is a tablet of deep water powder.

  Deep ocean water does not undergo photosynthesis at a depth that does not reach the sun's rays, is matured over many years under high water pressure, and nutrient salts (phytoplankton's nutrient source) are not consumed. It has more minerals than surface water and is rich in inorganic nutrients necessary for biological maintenance (eutrophication). That is, it contains abundant nutrient salts such as nitrogen and phosphorus compared to surface water, has a well-balanced mineral, and is clean with less organic matter and bacteria (general bacteria are 1/100 to 1/1000 of surface water) It is known that it is almost stable at low temperatures throughout the year without contamination by chemical substances from the land or the atmosphere.

  On the other hand, as a means for obtaining drinking water from seawater, a desalination means using a reverse osmosis membrane method or an ion exchange membrane method is known. The ion exchange membrane method has been established as a method for obtaining sodium hydroxide and chlorine gas from the electrolysis of saline using a cation exchange membrane (a membrane that allows only cations to pass through). When the saline is electrolyzed in a multi-tank electrolytic cell in which the anion exchange membrane and the anion exchange membrane are alternately arranged, electrodialysis occurs in the intermediate tank, and a saline solution that is thicker and thinner than the stock solution is obtained in the alternate bath. This system can be used to make the salt water thinner, so it is used as a desalination plant that obtains drinking water from seawater.

  The difficulty in ingesting minerals into the human body is that all dozens of mineral components must be balanced. Calcium, sodium, potassium, and the like, which are known as main components, can be obtained relatively easily from foods and dietary supplements, but magnesium tends to be deficient. The amount of magnesium required for an adult is about 300 mg per day, but the intake of Japanese is about 100 mg short. Potassium ion, which is a relatively large component of deep ocean water, is said to have a pungent taste several times that of sodium ion, and has a negative effect on taste (eggumi). It is said that it is better to have as little as possible for overdose of the elderly.

  Some scholars call it “middle water” based on the idea that deep ocean water on the Pacific side is in the open ocean and is affected by surface water because it varies depending on the season. On the other hand, Toyama Bay is composed of coastal surface water with low salinity affected by river water, Tsushima warm current water with a thickness of 200 to 300m below it, and deep ocean water deeper than 300m. The temperature is low at 2 ° C or less throughout the year, there is almost no fluctuation in water temperature, and the water quality, seawater composition, etc. (salinity is 34.0-34.1 psu) hardly change, and low temperature stability Compared with surface seawater, it is extremely rich in nutrient salts (eutrophication), and organic matter and bacteria are less than tap water (cleanliness).

(1) The cold water of Toyama Bay has more dissolved oxygen than the deep water on the Pacific side, indicating that the age of deep water is young.
(2) Comparing both deep waters with surface water, Toyama Bay natural cold water has more inorganic nutrients such as phosphorous phosphorus and nitrate nitrogen, and the temperature of Toyama Bay natural cold water is Compared to about 6 ° C. or lower, it is stable throughout the year.
(3) The number of general viable bacteria and fungi in Toyama Bay-specific cold water was considerably less than surface water.
JP2002-272430 JP 2002-218955 A JP 2002-17317 A

  When a seawater desalination system using the reverse osmosis membrane method is used for the separation of deep water, the reverse osmosis membrane (reverse osmotic pressure membrane) salt rejection is usually around 99.5-8%, which is equivalent to the salinity. As a result of removing other trace minerals, when chlorine (cl) and sodium (Na) having an overwhelmingly large component ratio are separated, other trace minerals are also removed at substantially the same rate as the separation of chlorine and sodium. For this reason, the content of minerals has little change between seawater and fresh water after separation, and there is a drawback that it contains almost no useful mineral components of deep seawater. Incidentally, the ultrapure water device is obtained by treating a reverse osmosis membrane in two stages.

Deep ocean water has more minerals than surface water, but still contains less than 1% of sodium and chlorine. Therefore, the content of sodium, chlorine, and minerals does not change by simply filtering deep sea water or separating it with a reverse osmosis membrane. Therefore, the mineral content of fresh water separated by filtration or reverse osmosis membrane is equivalent to that of tap water for seawater desalination in remote islands, etc. As a product to replenish, it was insufficient. When using deep ocean water as it is, it is necessary to use the salt content (chlorine ion and sodium ion, etc.) with an overwhelmingly large component ratio in consideration of the salty taste, taking into consideration the upper limit of compounding (excessive collection of sodium, etc.). However, there was a drawback that the useful trace minerals were relatively rare.
Since the deep sea water isolate is in liquid form, it can be easily mixed into the liquid, but it is inconvenient to mix into the dry, and many of the deep water isolates are in the air. There was a problem that it was easy to absorb moisture.
Therefore, the present invention has been made in view of such problems of the prior art, and the object of the present invention is to pulverize the deep sea water separation and use it for liquid or dry matter. While making it easy, it is further tableted to enable easy handling.

In order to achieve the above object, the deep water powder according to the present invention comprises, as claimed in claim 1, fresh water and concentrated seawater obtained by separating ocean deep water by a reverse osmosis membrane device, and fresh water and concentrated deep water separated by a multistage electrodialysis device. Further, it is characterized in that one kind selected from mineral concentrated water and concentrated salt water is directly powdered by rapid powder / tablet means.
As claimed in claim 2, one kind of powder selected from fresh water and concentrated seawater separated by reverse osmosis membrane device, fresh water separated by multistage electrodialysis device, concentrated deep water, mineral concentrated water and concentrated salt water After heating with tableting means to obtain a heated concentrate, the heated concentrate and the dehydrated component were mixed, the mixture was dried and sized, and the powdered material after sized was powdered with a differentiator It is characterized by.
According to a third aspect of the present invention, in the deep water powders of the first and second aspects, the deep ocean water is Toyama Bay inherent cold water.

Here, deep water powder refers to a powdered product of deep sea water that contains many kinds of minerals beneficial to the human body, and is used as a seasoning and additive for various processed foods and confectionery. There are a wide range of uses such as drinking water and cooking.
Here, the reverse osmosis membrane device refers to a device that separates seawater and deep seawater into fresh water and concentrated seawater, and the multistage electrodialysis method is an electrodialysis method previously invented by the applicant and is a first treatment. The device separates deep ocean water into fresh water and concentrated deep water, and the second treatment device separates concentrated deep water into mineral concentrate and concentrated salt water. Selected and selected from the membrane species that can remove minerals that may be useful to the human body and the removal of monovalent ions (sodium ion, chloride ion, potassium ion, etc.) that may be harmful to the human body It is. In particular, the mineral concentrate contains a well-balanced and abundant amount of mineral components similar to those of the human body.
Here, the rapid powder / tablet means means freeze-drying, spray-drying or the like that directly powders a liquid material, and the powder / tablet means means a process until obtaining a powder or tablet from the liquid material.

In order to achieve the above object, a deep water tablet according to the present invention comprises, as claimed in claim 4, fresh water and concentrated seawater obtained by separating ocean deep water by a reverse osmosis membrane device, and fresh water and concentrated deep water separated by a multistage electrodialysis device. Further, it is characterized in that one kind selected from mineral-concentrated water and concentrated salt water is directly pulverized by a rapid powder / tablet means, and the deep water powder is formed into a solid and solidified.
As claimed in claim 5, one kind of powder selected from fresh water and concentrated seawater separated by reverse osmosis membrane device, fresh water, concentrated deep water, mineral concentrated water and concentrated salt water separated by multistage electrodialysis device After heating by tableting means to obtain a heated concentrate, the heated concentrate and the dehydrated component are mixed, the first mixture is dried and sized, and the solidified component is added to the powdery material obtained from the sized particle. Mixing was performed to obtain a second mixture, which was tableted.
As a sixth aspect of the present invention, in the deep water tablet according to the fourth or fifth aspect, the deep sea water is Toyama Bay specific cold water.

Here, the deep-water tablet is a tablet that inhibits the absorption of moisture, and is a tablet that can be swallowed directly, for example, a diameter of 8 mm and a weight of 250 mg.
Here, the dehydrated component refers to a component that can be eaten and consumed and has a moisture absorption capability, and particularly a component having a strong water absorption capability, such as lactose, starch, pregelatinized starch, and the like.
Here, the solidifying component refers to a component that can be eaten and eaten and is useful for solidifying a powdery substance, and particularly inexpensive and easy-to-handle components such as glycerin and crystalline cellulose are preferable.
Here, Toyama Bay Indigenous Cold Water (also referred to as Japan Sea Indigenous Cold Water) is deep water collected from a depth of about 320 m offshore of Toyama Bay. Satisfaction of both sexuality and eutrophication, especially for low temperature, it is 2 ° C throughout the year, compared to the 8-10 ° C deep water temperature currently collected in Japan. It is very low. This also leads to a decrease in the density of the growing seafood counties, so the number of microorganisms is small and the “cleanliness” is increased.

Since the deep water powder according to the present invention is as described above, the following effects can be obtained.
Since the deep water powder of claim 1 is powdered, it is easy to handle, convenient to store and transport, and can be easily mixed with raw materials such as processed foods and confectionery. Moreover, since the separated material from deep sea water containing many kinds of mineral components, particularly trace minerals, is used as a raw material, it is useful for replenishment of trace minerals. That is, it can be expected to compensate for trace minerals that tend to be deficient.
The deep water powder according to claim 2 is obtained by mixing dehydrated components, drying and granulating the mixture, and pulverizing the mixture, so that it can be pulverized in a stable state.
In addition to the characteristics of claims 1 and 2, the deep water powder of claim 3 is a natural cold water of Toyama Bay, so it is low temperature throughout the year, so that a highly clean raw material can be stably obtained. Can do.

Since the deep water tablet by this invention is as above-mentioned, there exists an effect described below.
Since the deep water tablet of claim 4 is solidified, it has a low water absorption, and is easy to handle and convenient for storage and transportation. Moreover, it can be taken directly and contains many kinds of mineral components, particularly trace minerals, which is beneficial for replenishment of trace minerals. That is, it can be expected to compensate for trace minerals that tend to be deficient.
The deep water tablet of claim 5 is obtained by mixing the dehydrated components to obtain the first mixture, then drying and sizing the first mixture, and mixing the solidified component with the powdered material obtained by sizing, Since the second mixture is obtained and solidified, it can be easily solidified and manufactured in a stable state.
In addition to the features of claims 4 and 5, the deep water tablet of claim 6 is a natural cold water of Toyama Bay, so that it can be obtained at low temperatures throughout the year, so that a highly clean raw material can be stably obtained. Can do.

The best mode of the deep water powder according to the present invention will be described in detail with reference to FIG. 1. Mineral deep water B pumped from a depth of 200 meters or less below the sea surface is separated by a multistage electrodialyzer 10 and the mineral obtained from the general device 10 is obtained. This is a deep water powder 4B obtained by pulverizing the concentrated water b5 with the powder / tablet means 9, and the multistage electrodialysis apparatus 10 has been invented and filed by the applicant, and uses a ion exchange membrane. The deep sea water B was separated into concentrated deep water b4 containing a large amount of ions and fresh water b3 containing almost no ions in one treatment apparatus 11, and then an ion exchange membrane having excellent monovalent ion selectivity was used. In the second treatment device 12, the concentrated deep water b4 separated in the first treatment device 11 is concentrated with concentrated salt water b6 obtained by concentrating monovalent chlorine ions, sodium ions, etc. (including a high salt content), and monovalent ions. Gained by removing It is separated into mineral concentrated water b5 consisting mainly of useful trace minerals (mostly containing salt) containing minerals of polyvalent ions (contains Ca and Mg in a concentrated manner). b5 is heated and concentrated to form a heated concentrate 1B, and the dehydrated component 7 is stirred and mixed with the roughly heated concentrate 1B with, for example, a high-speed mixer to obtain a mixture 2B. The dried mixture 2B is sized, and the sized powder 3B is pulverized with a differentiator.
The mineral concentrate b5 separated by the multistage electrodialysis apparatus 10 is desalted and contains many kinds of mineral components, particularly trace mineral components.

The first embodiment of the deep layer water powder according to the present invention will be described in terms of differences from the best mode. The deep layer water powder 14B of the first embodiment is obtained by converting the deep ocean water B into the fresh water b1 and the concentrated seawater by the reverse osmosis membrane device 20. b2 and the fresh water b1 is directly pulverized by the rapid powder / tablet forming means 19, and as the rapid powder / tablet forming means 19, for example, spray drying, freeze drying, or heating dryer is used. Use.
Separation by the reverse osmosis membrane device 20 separates the deep ocean water B into fresh water b1 having a salinity of less than 0.1% and concentrated seawater b2 having a salinity of 5% or more. The separated fresh water b1 and concentrated seawater b2 are characterized in that the salt composition of the deep ocean water B is concentrated and diluted almost as it is.

When the second embodiment of the deep water powder according to the present invention is described in terms of differences from the first embodiment, the deep water powder 14B of the second embodiment is obtained by converting the deep sea water B into the fresh water b1 by the reverse osmosis membrane device 20. The concentrated seawater b2 is separated into concentrated seawater b2, and the concentrated seawater b2 is directly powdered by the rapid powder / tablet forming means 19.
The mineral component of the concentrated seawater b2 is contained in a much larger amount than the fresh water b1 of the first embodiment, but has a higher salt content, so it is desirable to use it for processed foods that require salt.

The third embodiment of the deep water powder according to the present invention will be described in terms of differences from the first and second embodiments. The deep water powder 14B according to the third embodiment is obtained by converting the deep sea water B into the multistage electrodialysis apparatus 10. The fresh water b3 obtained from the general apparatus 10 is directly powdered by the rapid powder / tablet forming means 19.
The fresh water b3 separated by the multistage electrodialysis apparatus 10 seems to have fewer mineral components than the fresh water b1 separated by the reverse osmosis membrane apparatus 20.

The fourth embodiment of the deep water powder according to the present invention will be described in terms of the differences from the third embodiment. The deep water powder 14B of the fourth embodiment is obtained by separating the deep sea water B by the multistage electrodialysis apparatus 10. The concentrated deep water b4 obtained from the general device 10 is directly powdered by the rapid powder / tablet forming means 19.
The concentrated deep water b4 separated by the multistage electrodialysis apparatus 10 is also concentrated in mineral components, but has a high salt concentration.

The fifth embodiment of the deep water powder according to the present invention will be described in terms of differences from the third and fourth embodiments. The deep water powder 14B according to the fifth embodiment is obtained by converting the deep sea water B into the multistage electrodialysis apparatus 10. The mineral concentrated water b5 obtained from the general apparatus 10 is directly powdered by the rapid powder / tablet forming means 19.
The mineral concentrated water b5 separated by the multistage electrodialysis apparatus 10 has many kinds of mineral components, and particularly contains a very small amount of minerals in a well-balanced manner, and is therefore suitable for replenishment of minerals accordingly.

The sixth embodiment of the deep layer water powder according to the present invention will be described in terms of differences from the third to fifth embodiments. The deep layer water powder 14B of the sixth embodiment is obtained by converting the deep ocean water B into the multistage electrodialysis apparatus 10. The concentrated salt water b6 obtained from the general apparatus 10 is directly powdered by the rapid powder / tablet forming means 19.
Concentrated salt water b6 separated by the multistage electrodialysis apparatus 10 is suitable for replenishment of minerals because there are many kinds of mineral components, but the salt concentration is higher than that of the fourth embodiment.

  When the seventh embodiment of the deep layer water powder according to the present invention is described in terms of differences from the best mode, the deep layer water powder 4B according to the seventh embodiment is a reverse osmosis membrane, like the powder / tablet means 9 of the best mode. The fresh water b1 separated in the apparatus 20 is heated and concentrated to form a heated concentrate 1B. The dehydrated component 7 is stirred and mixed with the heated concentrate 1B using, for example, a high-speed mixer to obtain a mixture 2B. It is dried for 3 to 5 hours in a drying room at 50 to 60 ° C., the dried mixture 2B is sized, and the sized powder 3B is pulverized with a differentiator.

  When the eighth embodiment of the deep water powder according to the present invention is described in terms of differences from the seventh embodiment, the deep water powder 4B of the eighth embodiment is the concentrated seawater b2 separated by the reverse osmosis membrane device 20, Similarly to the powder / tablet forming means 9 of the seventh embodiment, the concentrated seawater b2 is heated and concentrated to form the heated concentrate 1B, and the dehydrated component 7 is stirred and mixed with the almost heated concentrate 1B to obtain a mixture 2B. Then, this is dried in a drying chamber, the dried mixture 2B is sized, and the sized powdered product 3B is pulverized with a differentiator. That is, the material to be powdered is simply changed to the concentrated seawater b2.

  When the ninth embodiment of the deep layer water powder according to the present invention is described in terms of differences from the seventh and eighth embodiments, the deep layer water powder 4B of the ninth embodiment is separated by the multistage electrodialysis apparatus 10 and fresh water b3. As with the powder / tablet means 9 of the seventh and eighth embodiments, the fresh water b3 is heated and concentrated to form a heated concentrate 1B, and the dehydrated component 7 is stirred and mixed with the roughly heated concentrate 1B, and the mixture After 2B is obtained, this is dried in a drying chamber, the dried mixture 2B is sized, and the sized powder 3B is pulverized with a differentiator. That is, the material to be powdered is simply changed to fresh water b3.

  The tenth embodiment of the deep water powder according to the present invention will be described in terms of differences from the seventh to ninth embodiments. The deep water powder 4B of the tenth embodiment is separated by the multistage electrodialysis apparatus 10 and concentrated deep layers. Concentrated deep water b4 is heated and concentrated to form heated concentrate 1B in the same manner as the powder and tableting means 9 of the seventh to ninth embodiments, and the dehydrated component 7 is stirred into the heated concentrate 1B. After mixing and obtaining the mixture 2B, this is dried in a drying chamber, the dried mixture 2B is sized, and the sized powdered product 3B is pulverized with a differentiator. That is, only the material to be powdered is changed to the concentrated deep water b4.

  The eleventh embodiment of the deep layer water powder according to the present invention will be described in terms of differences from the seventh to tenth embodiments. The deep layer water powder 4B of the eleventh embodiment is separated by the multistage electrodialyzer 10. In the same manner as the powder / tablet means 9 of the seventh to tenth embodiments, concentrated brine b6 is heated and concentrated to form heated concentrate 1B, and dehydrated component 7 is added to almost heated concentrate 1B. After stirring and mixing to obtain a mixture 2B, this is dried in a drying chamber, the dried mixture 2B is sized, and the sized powdered product 3B is pulverized with a differentiator. That is, the material to be powdered is simply changed to concentrated salt water b6.

Explaining the twelfth embodiment of the deep water powder according to the present invention from the points different from the first to sixth embodiments, the deep water powder 14C of the twelfth embodiment is Toyama Bay natural cold water as the deep sea water B. The Toyama Bay cold water C is separated into fresh water c1 and concentrated seawater c2 by the reverse osmosis membrane device 20, and fresh water c3, concentrated deep water c4 and mineral concentrated water c5 are separated by the multistage electrodialysis device 10. It is separated into concentrated salt water c6 and directly powdered by the rapid powder / tablet forming means 19.
The cold water C in Toyama Bay occupies about 65% of the volume of Toyama Bay, and as described in JP 2000-290168, JP 2000-290161, etc. As a property, there is almost no change in water temperature at a low temperature of 2 ° C. or less throughout the year, the salt content is 34.0-34.1 psu, and it is rich in nutrients compared to surface water, organic matter and bacteria The feature is that there is very little.

  Explaining the thirteenth embodiment of the deep water powder according to the present invention from the best mode and the seventh to eleventh embodiments, the deep water powder 4C of the thirteenth embodiment is the ocean deep water B. Toyama Bay specific cold water C is used, fresh water c1 and concentrated seawater c2 separated by the reverse osmosis membrane device 20 from Toyama Bay specific cold water C, fresh water c3 and concentrated deep water c4 separated by the multistage electrodialysis device 10 Mineral concentrated water c5 and concentrated salt water c6 are pulverized in the same manner as the powder / tablet forming means 9 of the seventh to eleventh embodiments. For example, they are heated and concentrated with an electric heater or the like to obtain a heated concentrate 1C. After that, the roughly heated concentrate 1C and the dehydrated component 7 are stirred and mixed to produce the first mixture 2C, which is dried in a drying chamber, and the powdery product 3C is sized from the dry mixture 2C. 3C is powdered with a differentiator.

  The first embodiment of the deep water tablet according to the present invention will be described with reference to FIG. 1. The deep water tablet 16B of the first embodiment includes fresh water b1 obtained by separating the deep sea water B by the reverse osmosis membrane device 20 and concentrated seawater b2. One of the fresh water b3, the concentrated deep water b4, the mineral concentrated water b5, and the concentrated salt water b6 separated by the multistage electrodialysis apparatus 10 is directly powdered by the rapid powder / tablet means 19, and the deep water powder 14B is obtained. After being obtained, the deep water powder 14B is directly tableted, and well-known means are used for tableting.

  When the second embodiment of the deep water tablet according to the present invention is described in terms of differences from the first embodiment, the deep water tablet 6B of the second embodiment is obtained by using fresh water b1 and concentrated seawater b2 separated by the reverse osmosis membrane device 20. , And one kind of fresh water b3, concentrated deep water b4, mineral concentrated water b5 and concentrated salt water b6 separated by the multistage electrodialysis apparatus 10 is heated and concentrated in a powder / tablet means 9 to reduce the water content. 1B, almost heated concentrate 1B is stirred and mixed with dehydrated component 7 to obtain first mixture 2B, and then dried in a drying chamber to dehydrate water from first mixture 2B. The particles are sized to obtain a powdery product 3B. Next, the powdery product 3B is mixed with the solidifying component 8 to obtain the second mixture 5B, and then the second mixture 5B is tableted.

  When the third embodiment of the deep water tablet according to the present invention is described in terms of differences from the first embodiment, the deep water tablet 16C of the third embodiment uses Toyama Bay natural cold water C as the deep sea water B. Fresh water c1 and concentrated seawater c2 separated by the reverse osmosis membrane device 20 or fresh water c3, concentrated deep water c4, mineral concentrated water c5, and concentrated salt water c6 separated by the multistage electrodialyzer 10 The raw material is directly powdered by the rapid powder / tablet forming means 19 to obtain the deep water powder 14C, and then the deep water powder 14C is directly compressed.

  When the fourth embodiment of the deep water tablet according to the present invention is described in terms of differences from the second embodiment, the deep water tablet 6C of the fourth embodiment uses Toyama Bay natural cold water C as the deep sea water B. Fresh water c1 and concentrated seawater c2 separated by the reverse osmosis membrane device 20 or fresh water c3, concentrated deep water c4, mineral concentrated water c5, and concentrated salt water c6 separated by the multistage electrodialyzer 10 After being heated and concentrated in powder / tablet means 9 to form a heated concentrate 1C with reduced water content, the almost heated concentrate 1C is stirred and mixed with the dehydrated component 7 to obtain a first mixture 2C. Then, in order to dehydrate water from the first mixture 2C, drying is performed in a drying chamber, and the dried mixture 2C is sized to obtain a powdery material 3C. Next, the powdery material 3C is mixed with the solidifying component 8 to obtain the second mixture 5C, and then the second mixture 5C is tableted.

ミネラル濃縮水ｃ５＝１００ｍｌを２０ｍｌになるまで加熱濃縮したものである。
乳糖＝粉末化の基材である。
α化澱粉（ＫＺＲ−１０１）＝日澱化学製、
ＫＺＲ−１０の微細粉末タイプであり、粒子がこまかいので、滑らかな食感が特に要求される場合に最適である。しかも、優れた吸水、保水能力を持つα化澱粉で、僅かの添加量で、より多くの水溶液を吸水できるメリットがある。
ラクトイウエイ２＝松谷化学工業製
液状エキスや調味料の吸着剤として使われ、ＫＺＲほどではないが、普通の馬鈴薯澱粉よりも液状成分の吸着性は良くなっている。７０℃で溶け、吸湿安定性に優れている。
水分含量を低く抑えることにより、他の素材から効率的に水分を吸着することを可能にした食品用澱粉。低粘性であり、食品の持つ風味、テクスチャーに影響を与えない。また、粉末化と造粒を一工程で行えるので、製造コストを低く抑えることができるし、加熱操作を伴わないので、芳香成分の散逸、風味の劣化及び色沢の変化等がほとんどない。 Experimental example 1: Deep water powder

Mineral concentrated water c5 = 100 ml is heated and concentrated to 20 ml.
Lactose is a powdered base material.
pregelatinized starch (KZR-101) = manufactured by Nissho Chemical
It is a fine powder type of KZR-10, and the particles are fine, so it is optimal when a smooth texture is particularly required. Moreover, it is a pregelatinized starch having excellent water absorption and water retention ability, and has the advantage of being able to absorb more aqueous solution with a small addition amount.
Lactoiway 2 = manufactured by Matsutani Chemical Industry Co., Ltd. Used as an adsorbent for liquid extracts and seasonings. Although not as good as KZR, the adsorbability of liquid components is better than ordinary potato starch. It melts at 70 ° C and has excellent moisture absorption stability.
A starch for foods that allows moisture to be efficiently adsorbed from other materials by keeping the water content low. Low viscosity and does not affect the flavor and texture of food. Moreover, since powderization and granulation can be performed in one step, the production cost can be kept low, and since there is no heating operation, there is almost no loss of aromatic components, deterioration of flavor, change of color, and the like.

In the heating and concentration step, an electric heater is used.
In the stirring and mixing step, lactose, starch (Lactoiway 2), and pregelatinized starch (KZR-101) are dehydrated, and this is stirred and mixed with the heated concentrate 1B and a high speed mixer FS-GS30 of Fukae Industry Co., Ltd. .
In the drying step, the first mixture 2B obtained in the stirring and mixing step is dried at 50 ° C. for 3 hours using a sanitary box dryer SPH-200DL manufactured by Matsui Seisakusho.
In the sizing step, the dried first mixture 2B is sized using a flash mill FL200G sizing machine manufactured by Fuji Paudal Co., Ltd., and the powdered product 3B of 16-21 mesh is sample milled K2W-1 of Fuji Powdal Co., Ltd. Powderize using a fine grinder.

「含有量」１ｇ（４粒）当たりの主要成分含有量（計算値） Experimental Example 2: Deep water tablet

"Content" Main ingredient content per 1g (4 grains) (calculated value)

In the drying step, the first mixture 2B obtained in the stirring and mixing step is dried at 55 ° C. for 5 hours or longer using a sanitary box dryer SPH-200DL manufactured by Matsui Seisakusho.
In the mixing step, 1 to 5% of crystalline cellulose, sucrose fatty acid ester, glycerin fatty acid ester and the like are mixed as the solidifying component 7 into the sized 21 mesh powder 3B.
In the tableting process, a rotary tableting machine COLLECT36HUK manufactured by Kikusui Seisakusho is used to form cylindrical tablets having a diameter of 8 mm, a weight of 250 mg, and a hardness of 5 kg or more.
The solidifying component 7 also has a property as a lubricant.

  The deep water powder of the present invention includes fresh water b3, mineral concentrated water b5 and concentrated salt water b6 obtained by separating the deep sea water B by the multistage electrodialyzer 10, and fresh water b1 obtained by separating the deep sea water B by the reverse osmosis membrane device 20. And concentrated seawater b2 are mixed, for example, fresh water b3 and mineral concentrated water b5, fresh water b3 and concentrated salt water b6, mineral concentrated water b5 and concentrated salt water b6 are mixed, and the mixed water is powdered and tableted. It is also possible to pulverize by means 9 and 19.

  The deep water powder and the deep water tablet of the present invention include fresh water b1 and concentrated seawater b2 obtained by separating the deep sea water B by the reverse osmosis membrane device 20, and fresh water b3 and mineral concentrated water b5 separated by the multistage electrodialysis device 10. Concentrated salt water b6, fresh water c1 and concentrated seawater c2 separated by reverse osmosis membrane device 20 from Toyama Bay cold water C, and fresh water c3, mineral concentrated water bc and concentrated salt water c6 separated by multistage electrodialysis device 10, It is also possible to mix at least two liquids and pulverize and tablet the mixed liquid by the powder / tablet means 9 and 19.

  One of the features of the deep water powder and deep water tablet of the present invention is that the mineral components contained in the desalted mineral concentrate b5 substantially match the mineral components constituting the human body, and the balance of the mineral components Is also an approximate point.

It is a block diagram which shows the example of a manufacturing process of the deep water powder and deep water tablet by this invention. It is a block diagram which shows the example of a manufacturing process of a powder and tableting means.

Explanation of symbols

1B, 1C Heated concentrate 2B, 2C First mixture 3B, 3C Powdery 4B, 4C, 14B, 14C Deep water powder according to the present invention 5B, 5C Second mixture 6B, 6C, 16B, 16C Deep water tablet according to the present invention 7 Dehydrated component 8 Solid component 9 Powder / tablet means, 19 Rapid powder / tablet means 10 Multistage electrodialyzer, 11 First treatment device, 12 Second treatment device 20 Reverse osmosis membrane device B Deep sea water C Toyama Indigenous cold water b1, c1, b3, c3 Fresh water b2, c2 Concentrated seawater b4, c4 Concentrated deep water b5, c5 Mineral concentrated water b6, c6 Concentrated salt water

Claims (6)

  Fresh water (b1) and concentrated seawater b2 separated from the deep ocean water (B) by the reverse osmosis membrane device (20), fresh water (b3) separated by the multistage electrodialysis device (10), concentrated deep water (b4) and minerals A deep water powder characterized in that one kind selected from concentrated water (b5) and concentrated salt water (b6) is directly powdered by a rapid powder / tablet means (19).   Fresh water (b1) and concentrated seawater b2 separated from the deep ocean water (B) by the reverse osmosis membrane device (20), fresh water (b3) separated by the multistage electrodialysis device (10), concentrated deep water (b4) and minerals One kind selected from concentrated water (b5) and concentrated salt water (b6) is heated in powder / tablet means (9) to obtain a heated concentrate (1B), and then dehydrated with heated concentrate (1B). Component (7) is mixed, the mixture (2B) is dried and sized, and the pulverized powder (3B) is pulverized with a differentiator.   The deep sea water powder according to claim 1 or 2, wherein the deep sea water (B) is Toyama Bay natural cold water (C).   Fresh water (b1) and concentrated seawater b2 separated from the deep ocean water (B) by the reverse osmosis membrane device (20), fresh water (b3) separated by the multistage electrodialysis device (10), concentrated deep water (b4) and minerals One kind selected from concentrated water (b5) and concentrated salt water (b6) was directly pulverized by rapid powder / tablet means (19), and the deep water powder (14B) was crushed and solidified. Deep water tablets featured.   Fresh water (b1) and concentrated seawater b2 separated from the deep ocean water (B) by the reverse osmosis membrane device (20), fresh water (b3) separated by the multistage electrodialysis device (10), concentrated deep water (b4) and minerals One kind selected from concentrated water (b5) and concentrated salt water (b6) is heated in powder / tablet means (9) to obtain a heated concentrate (1B), and then dehydrated with heated concentrate (1B). The component (7) is mixed, the first mixture (2B) is dried and sized, the solidified component (8) is mixed with the powdery product (3B) obtained by sizing, and the second mixture (5B) A deep-water tablet, characterized by being obtained and tableted.   The deep water tablet according to claim 4 or 5, wherein the deep sea water (B) is Toyama Bay natural cold water (C).

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