JPH0834709A - Tricogen, its preparation and its manufacturing apparatus - Google Patents

Abstract

PURPOSE: To promote hair growing at the depilated part of hair. CONSTITUTION: This hair growing agent is characterized by inclusion of an active ingredient of malt, and the active ingredient is obtained by the following method or apparatus: (a): a step for reducing 2 pressure of malt; (b) a step for forming water or other liquids into an atomized fine particles and/or a vapor; (c) a step for heating the atomized fine particles and/or the vapor to a temperature 5a higher than the malt under the reduced pressure, charging 5 the heated atomized fine particles and/or the heated vapor to a space under the reduced pressure and storing the malt to bringing the heated atomized fine particles or the heated vapor into contact with the malt, to allow the heated atomized fine particles or the heated vapor to form dew, and further to allow the active ingredient of the malt to migrate on the surface thereof; (d) a step for transferring 6 the active ingredient migrated to the surface to the exterior of the space under the reduced pressure in a vaporized state by allowing the vaporized active ingredient to be absorbed and held by other atomized fine particles forming the dew or without forming the dew, and passing through the space under the reduced pressure; (e) a step for cooling (3) the gas transferred to the exterior of the space under the reduced pressure while holding the active ingredient of the malt obtained at the step (d) to obtain a liquid 9 containing the active ingredient of the malt.

Description

Detailed Description of the Invention

[0001]

BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a hair growth agent containing malt and / or a malt extract component as an active ingredient, a method for producing the same, and an apparatus for extracting malt and other active ingredients.

[0002]

BACKGROUND OF THE INVENTION Malt is a germinated barley which contains a large amount of amylase and is used as a raw material for producing beer, starch syrup and the like. However, the present inventor, while conducting various studies on malt, its mechanism of action is unknown, but surprisingly malt has an excellent hair-growth action, is extremely effective in improving baldness and hair loss. I found that. Conventionally, the causes of baldness and hair loss are activation of male hormones in organs such as hair roots and sebaceous glands, reduction in blood flow to hair follicles, excessive secretion of sebum, generation of peroxides, and bacterial growth on the scalp. Abnormal,
Genetic factors, neurosis due to stress, secondary diseases and aging are considered. Therefore,
In conventional hair growth agents and hair growth agents, substances having an action of removing or reducing the above causes are used as active ingredients.

However, the procedures for hair loss and hair growth are very complicated and simply prevent the activation of male hormones,
It was not possible to prevent baldness and hair loss simply by increasing the blood flow rate of the hair follicle, and it was almost impossible to renew the hair at that point once baldness had occurred. The present inventor, in the process of repeating studies on malt extract, focusing on the fact that the skin in contact with the malt extract becomes smooth and alive, the purpose of improving the skin of the head and preventing the occurrence of dandruff When I washed my head with the extract and felt itchy only on the hair loss area. Therefore, it was found that when the application of the extract was continued only to the hair-removed portion, thin down hair was first vegetated and then this hair was changed to normal hair by the application of the extract.

[0004]

SUMMARY OF THE INVENTION The hair growth agent according to the present invention is characterized by containing an active ingredient of malt, and the malt used is PILSNER MALT, CRYSTAL MAH.
LT / LIGHT, MILD ALE MALT, VI
ENNA MALT, KLAGES MALT, PAL
E MALT, LAGER MALT, etc. for beer production may be used.

Malt can be used as it is as an active ingredient of a hair growth agent, but it is desirable to extract and use the active ingredient from malt. And, the active ingredient of malt used for this hair growth agent, using a solvent such as water, methanol, ethanol and acetone, there is almost no effect when extracted by a known method, and the following extraction method Effective results have been obtained only when using the malt extract obtained by.

That is, a: depressurizing malt, b: turning water or other liquid into atomized fine particles and / or vapor, c: heating the atomized fine particles and / or vapor to a temperature higher than that of malt under reduced pressure Then, the step of feeding these into a depressurized space in which malt is stored to cause dew condensation on the surface of malt and leaching the active ingredient of koji to the surface of koji, d: the active ingredient leached to the surface of malt Is absorbed and held by the above-mentioned dew condensation and other atomized fine particles and / or vapor that pass through the depressurized space without dew condensation, and is transferred to the outside of the depressurized space in a vaporized state, e: The active ingredient of malt is retained in the step d. The step of cooling the gas transferred to the outside of the reduced pressure space to obtain a liquid containing the active ingredient of malt.

[0007]

BEST MODE FOR CARRYING OUT THE INVENTION The present invention will be specifically described based on Examples. Example 1: Hair Growth Experiment Fifteen male test subjects were divided into three groups A, B, and C, each having five test subjects, and the test liquids a, b, and c were given to the test subjects in each group for comparison. The relationship between the test solution and each group is shown in Experiment 1. It should be noted that the male test subjects each selected a person having a baldness with a diameter of about 7 cm on the top of the head, and the average age is 50 years old.

Experiment 1 Group of subjects Test solution A a B b C c

Next, the contents of the test liquids a, b and c are shown below. Test liquid: a 1000 g of malt was pulverized with a pulverizer to a particle size of 200 μm or less, and the pulverized malt was stirred in 4000 cc of water to form a paste. Test liquid: b An ethanol extract obtained by immersing 1000 g of malt in 4 times the amount of ethanol for 12 hours and then filtering. Test liquid: c An extract produced from 1000 g of malt by the following method. a: a step of depressurizing malt, b: a step of turning water into atomized fine particles and / or steam, c: heating the atomized fine particles and / or steam to a temperature (35 to 65 ° C.) higher than that of malt under reduced pressure, and Is fed into a depressurized space in which malt is stored to cause dew condensation on the surface of malt, and the active ingredient of malt is leached on the surface of malt, d: the dew condensation of the active ingredient leached on the surface of malt And a step of absorbing and holding by other atomized fine particles and / or vapor passing through the depressurized space without dew condensation, and transferring to the outside of the depressurized space in a vaporized state, e: holding the active ingredient of malt in the d step and depressurized space A step of cooling the gas transferred to the outside to obtain an aqueous solution containing an active ingredient of malt.

To produce the malt extract by the above method,
The apparatus shown in FIGS. The data at the time of extraction are as follows. Rice malt 1000g Decompression value 130mmAg Extraction time 7 minutes / 1 cycle x 4 times = 28 minutes Extraction amount 300cc / 1 cycle x 4 times = 1
200 cc

The test liquids a, b and c described above were applied to the subjects A, B and C in the groups A, B and C twice in the morning and in the evening, directly on the entire head, centering on the bald portion, and hand massaged. Used by The amount of each test solution used once is 3 to 7c.
It was around c. The observation results of this experiment are shown below.

Experiment 2 days A group B group C group (test solution a) (test solution b) (test solution c) 1 no change no change 3 days when hair loss started to stop 4 to no change no change of bald part The color of the skin changes to a tan color, and Kayumi 5th can be felt a little.
10 No change No change Pores on the bald parts become noticeable ~ While Ubu hair grows. 3 weeks Hair loss is reduced Hair loss is reduced Ubu hairs start to appear at intervals in the bald areas, and the growth of Ubu hairs that occurs at an early stage begins to remarkably change to normal hair. Therefore, at this point, the bald portion has a diameter of about 3 cm. 5 weeks Ubu hairs on bald area Ubu hairs on bald area There are gaps between Ubu hairs at the bald area. Occurrence of hair is observed, and Ubu has already occurred. The hair grows to normal hair, and the bald spots appear thin but are covered with hair. 2 Ubal hairs in bald area Growth of bristles in bald areas is favorable, bald months continue to occur, but bub hairs continue to be almost inconspicuous, but normal Ubu hair continues Less conversion to hair Less conversion to hair

From the above experimental results, it was found that the test liquid c had the best hair growth effect. Next, an apparatus for extracting an active ingredient of malt will be described with reference to the drawings. 1 to 3
It is a diagram showing an embodiment of the invention according to claims 5 to 7,
The invention according to claims 3 to 4 will also be described based on these drawings. In addition, in this embodiment, as the extraction target,
Malt was used.

FIG. 1 is a diagram showing the basic construction of an extracting device according to a fifth aspect. In the figure, U is a malt extraction unit, H is a malt hopper, and L is a malt conveying means installed in a direction perpendicular to the extraction unit U. This embodiment has four extraction units U and a hopper-L
From the malt fed from the transport means L to the transport means L, the active ingredients are extracted by the transport means L in the four extraction units while moving vertically from the upper side to the lower side.

FIG. 2 is a diagram showing the configuration of the extraction unit U. In the figure, 1 is an atomization chamber for generating vaporized fine particles of water or other liquid 1b, 2 is a decompression chamber, 3 is a cooling means, and 4 is a high-pressure multistage blower as a decompression means. The atomization chamber 1 and the decompression chamber 2 are connected by a first circulation pipe 5, and the atomized fine particles passing through this first circulation pipe are heated to a predetermined temperature by the first heating means 5a.
The decompression chamber 2 and the decompression means 4 are connected by a second circulation pipe 6. The second circulation pipe 6 is composed of a plurality of thin tubes in order to enhance the cooling effect. 7 is a third circulation pipe connecting the decompression means 4 and the atomization chamber 1,
It has a second heating means 7a.

Reference numeral 8 is a tank for storing the malt extract 9, 1a is an oscillator of an ultrasonic oscillator provided in the liquid 1b of the atomizing chamber 1, and 10 is water or other liquid in the atomizing chamber 1. 1b
Is a heater for heating. The cooling means 3 is
It is composed of a blower fan 3a and a cooling chamber 3b having a cooler 3c. Reference numeral 4a denotes a decompression adjustment valve for finely adjusting the decompression value. Further, the conveying means L is a conveying duct 11 provided vertically, a pressing means 12 for moving the malt downward, a gas circulation portion 13, and a pressure adjusting means 14.
It consists of As shown in the figure, the transport duct 11 penetrates the decompression chamber 2 of the extraction unit U.

The transfer duct 11 has a gas flow section 13 in the decompression chamber 2 for passing atomized fine particles on its side. In this embodiment, the pressing means 12 is a motor.
It is composed of a piston driven by a rotor and is provided at the upper end of the transport duct 11. Further, the pressure adjusting means 14 provided at the lower end of the transport duct 11 is
It is composed of a pressure dispersion plate and a pressure damper, and adjusts the falling speed of malt in the transport duct 11. The transport duct 11 is provided with a plurality of vibration motors (not shown) to prevent malt from adhering to the inner surface of the duct.

Next, the operation of extracting the active ingredient of malt by the extraction unit U will be described. First, water is put in the atomization chamber 1 and malt is set in the decompression chamber 2. By turning on the switch, the water in the atomization chamber 1 heated by the heater 10 becomes atomized fine particles by the operation of the vibrator 1a.
Fills in. The amount of atomized fine particles generated can be adjusted by the number of vibrators, heating temperature, and the like. High pressure blower
As the pressure of the decompression chamber 2 is reduced by 4, the atomized fine particles are sucked from the atomization chamber 1 into the decompression chamber 2 through the first circulation pipe 5.
The atomized fine particles are heated to a temperature higher than that of the malt in the decompression chamber 2 by the heater 5a as the first heating means while moving from the atomization chamber 1 to the decompression chamber 2. The atomized fine particles that have flowed into the decompression chamber 2 adhere to the surface of the malt at a temperature lower than this to cause dew condensation, but part of the atomized fine particles pass through the malt surface without dew condensation.

On the other hand, since the malt in the decompression chamber 2 has already been subjected to the decompression action, the active ingredient inside is leached on the surface, and this active ingredient is eluted during the condensation. Condensation that retains the active ingredient undergoes vaporization again under reduced pressure,
While passing through the second circulation pipe together with other passing particles,
It is rapidly cooled by the cooling means 3, condensed and liquefied, and is dripped into the tank 8. The liquid thus collected in the tank 8 is the extract 9 containing the active ingredient of malt. In addition, gas such as atomized fine particles that were not liquefied during the cooling process,
It is sent to the atomization chamber 1 through the third circulation pipe 7 by the high pressure blower-4, and during this time, the heater which is the second heating means.
It is heated by 7a.

FIG. 3 is a perspective view showing the relationship between the transfer duct 11 and the decompression chamber 2. As shown in the figure, a gas flow portion 13 is formed on the side surface of the transfer duct 11 penetrating the decompression chamber 2, and a passage amount adjusting means for controlling the passage amount of atomized fine particles at the opening portion thereof. Nets 15 and 15
Is provided, and the active ingredient is extracted while the malt Q passes through the gas circulation unit 13. The amount of atomized fine particles that pass through can be controlled by changing the size of the mesh of the mesh 15.

Next, the operation of the apparatus for extracting the active ingredient of malt will be described with reference to FIGS. When the switch is turned on, the pressing means 12 operates and the malt in the hopper-H is filled in the transport duct 11 and moves downward at a predetermined speed.
The four extraction units also start operation. Since the decompression chamber 2 through which the malt Q passes is decompressed by the high-pressure blower-4, the atomized fine particles heated by the heater 5a flow into the decompression chamber 2. The atomized fine particles thus flowing in adhere to the surface of the malt that moves at a constant speed between the nets 15, 15 in the gas circulation portion 13 to form dew. On the other hand, the active ingredient leached on the surface of malt by the depressurization action is eluted during the condensation. The dew condensation holding the active ingredient is vaporized again and, while passing through the thin tube 6 serving as the second circulation pipe, is cooled by the cooling means 3 and liquefied and stored in the tank 8. The atomized fine particles that have not been liquefied are returned to the atomization chamber 1 by the high-pressure blower-4, while being heated by the heater 7a.

In this way, malt is extracted as a liquid in the four decompression chambers 2 while moving from the upper side to the lower side in the transport duct 11. The movement speed of the malt is set to be about 7 minutes before entering and leaving the decompression chamber 2. Further, the temperature of the atomized fine particles flowing into the decompression chamber 2 needs to be higher than that of malt,
A temperature of 35 to 65 ° C is suitable. The extract 9 obtained as described above is used as it is or after being appropriately diluted and used as a hair-growing agent, and exhibits excellent effects.

Next, one embodiment of the invention according to claims 8 to 11 will be described with reference to FIGS. In this example,
Malt or koji is used as the extraction target. FIG.
FIG. 9 is a diagram showing a basic configuration of an extraction device according to a seventh aspect. In the figure, U is an extraction unit of koji or malt as an extraction object, H is a koji or malt hopper, L is a koji or malt conveying means, D is a conveyor for drying koji or malt, and M is a conveying means. It is a motor as a drive source of L. This embodiment has five extraction units U, and the koji or malt fed from the hopper H to the transportation means L is moved by the transportation means L while the active ingredients are extracted in the five extraction units. It The koji or malt from which the active ingredient has been extracted is transferred from the conveying means L to a conveyor D as a drying means and is dried while moving.

FIG. 5 is a diagram showing the structure of the extraction unit U. In the figure, 1 is an atomization chamber for generating vaporized fine particles of water or other liquid 1b, 2 is a decompression chamber for decompressing by an appropriate means such as a rotary fan, a suction pump, and 3 is a cooling chamber. The atomization chamber 1, the decompression chamber 2, and the cooling chamber 3 are connected to each other by a circulation pipe 41, and the circulation pipe 4 that connects the atomization chamber 1 and the decompression chamber 2 is provided with a heater 51. A rotary fan 61 is provided in the circulation pipe 4 that connects the atomization chamber 1 and the cooling chamber 3. 7
1 is a tank for storing the koji or malt extract 8; 9 is a heater for heating water or other liquid 1b in the atomization chamber 1; 10 is water or other liquid 1b in the atomization chamber 1 It is a supply pipe for supplying. Reference numeral 1a is a vibrator of an ultrasonic oscillator provided in the liquid 1b of the atomization chamber 1.

Next, the operation of extracting the active ingredient of koji or malt by the extraction unit U will be described. First, atomization chamber 1
Pour water into and put malt or malt in the decompression chamber 2. When the switch is turned on, the water in the atomization chamber 1 heated by the heater 9 is atomized by the operation of the vibrator 1a and becomes atomized fine particles, which fills the atomization chamber 1 and the decompression chamber 2 by the rotary fan 61. The atomized fine particles are circulated in the circulation pipe 41 due to the depressurization of
Through the atomization chamber 1 to the decompression chamber 2. While the atomized fine particles move from the atomization chamber 1 to the decompression chamber 2, the heater 51
Is heated to a temperature higher than that of koji or malt in the decompression chamber 2. The atomized fine particles that have flowed into the decompression chamber 2 adhere to the surface of koji or malt at a temperature lower than this to cause dew condensation,
Some of them pass through the surface of koji or malt without condensation. On the other hand, since the koji or malt in the decompression chamber 2 has already been subjected to the decompression action, the active ingredient inside is leached on the surface, and this active ingredient is eluted during the condensation of the atomized fine particles. The dew condensation holding the active ingredient is vaporized again in a depressurized state, and together with other passing atomized fine particles, the circulation pipe 4
1 to the cooling chamber 3. The atomized fine particles are rapidly cooled in the cooling chamber 3, condensed, liquefied, and dropped into the tank 71. The liquid thus collected in the tank 71 is the extract liquid 81 containing the active ingredient of koji or malt. The atomized fine particles that have not been liquefied in the cooling chamber 3 are returned to the atomization chamber 1 by the rotary fan 61.

FIG. 6 is a diagram showing the construction of the transport means L and the relationship between the extraction unit U and the transport means L. As shown in FIG. The carrying means L is composed of a carrying pipe 11, a carrying screw 12 driven by a motor M, a gas circulating unit 13, a stirring device 14, and an adjusting plate 15. As shown in the figure, the transfer pipe 11 horizontally penetrates the decompression chamber 2 of the extraction unit U. Then, the transfer pipe 11 has a gas flow section 13 for passing atomized fine particles at the bottom in the decompression chamber 2. The carrying screw 12 is provided at the end of the carrying pipe 11 and moves the malt or malt Q supplied from the hopper H to the carrying pipe 11 toward the decompression chamber 2. A known stirring device 14 is provided in the transfer pipe 11 to loosen the koji or malt into pieces, and to allow the atomized fine particles to uniformly adhere to the surface of the koji or malt in the decompression chamber 2. By passing through the adjusting plate 15, the malt or malt has a uniform thickness in the decompression chamber 2. When the koji or malt having a uniform thickness passes through the gas circulation portion 13 of the transport pipe 11 in the decompression chamber 2, the atomized fine particles adhere to the surface of the koji or malt.

FIG. 7 is a perspective view showing the relationship between the transfer pipe 11 and the decompression chamber 2. As shown in the figure, a gas circulation portion 13 is formed at the bottom of a transfer pipe 11 that penetrates the decompression chamber 2 in the horizontal direction, and a passage amount adjustment for controlling the passage amount of atomized fine particles is formed in the opening portion thereof. A net 16 is provided as means for moving the koji or malt Q on the net 16. The amount of atomized fine particles passing through can be controlled by changing the size of the mesh.

Next, the operation of the active ingredient extracting device according to this embodiment will be described with reference to FIGS. 4 and 6. When the switch is turned on, the conveying screw 12 starts to rotate, and as described above with reference to FIG. 5, the five extraction units also start operating. The koji or malt sent to the extraction unit by the carrying screw 12 is loosened by the stirrer 14 into pieces, and then passes through the adjusting plate 15 to have a predetermined thickness and is moved into the decompression chamber 2. Since the decompression chamber 2 is decompressed by the rotary fan 61,
The atomized fine particles that have passed through the heater 51 are from below in the decompression chamber 2.
Flows into. The atomized fine particles flowing in this way are
Dew forms on the surface of koji or malt that moves at a constant speed on the net 16.

On the other hand, the active ingredient leached on the surface of koji or malt by the action of reducing pressure is eluted during the condensation. The dew condensation holding the active ingredient is vaporized again and is sent to the cooling chamber 3 through the circulation pipe above the decompression chamber 2 and is liquefied. In this way, the malt or malt is moved along the transport pipe 11 while
In one decompression chamber 2, the active ingredient is extracted as a liquid. The moving speed of koji or malt is set to be about 7 minutes until the koji or malt enters and leaves the decompression chamber 2. The temperature of the atomized fine particles flowing into the decompression chamber 2 needs to be higher than that of koji or malt, and the temperature is preferably 35 ° C to 65 ° C although it depends on koji or the like. As described above, the above-mentioned device can efficiently and continuously extract the active ingredient of koji or malt.
Moreover, since this apparatus has a plurality of extraction units, different extraction conditions can be set for each extraction unit.

Next, an experimental example using the extraction device shown in FIG. 5 will be described. First, a required amount of liquid such as pure water or distilled water is supplied to the atomization chamber 1 through the supply pipe 10. And 50 g of malted malt is stored in the decompression chamber 2. In this state, the rotary fan 61 is rotated, and the vibrator 1a of the ultrasonic oscillator is operated to balance the atmospheric pressures in the decompression chamber 2 and the atomization chamber 1 to maintain a constant atmospheric pressure difference. That is, the liquid acts as atomized fine particles to fill the atomizing chamber 1 by the action of the vibrator 1a, and a desired vapor pressure is generated to obtain pressurized atomized fine particles. The atomized fine particles flow into the decompression chamber 2 through the circulation pipe 41, but are heated by the heater 51 in the circulation pipe 41, and the atomized fine particles flow into the decompression chamber 2 because their molecular activity becomes more active. . The decompression chamber 2 is in a kind of decompressed state due to the exhausting action performed by the rotation of the rotary fan 61. However, the size of the decompressed state can be freely changed according to the strength of the rotating action of the rotary fan 61. You can In addition, the malt cell tissue can be kept as it is without any damage.

The atomized fine particles that have flowed into the decompression chamber 2 adhere to the surface of the malt Q, which has a lower temperature than this, and most of them condense, but part of them pass through the surface as they are and the upper part of the decompression chamber 2 To the circulation pipe 41. Although the malt temperature was room temperature in this experiment, it may be cooled. Since the koji in the decompression chamber 2 has already been subjected to the decompression action, the active ingredient has a leaching tendency and leaches on the surface of the malt, so that the koji is immediately eluted in the condensed liquid. In the state where the active ingredient is held, the dew condensation is again vaporized, passes through the circulation pipe 41, reaches the inside of the cooling chamber 3, and is rapidly cooled. Therefore,
The vaporized component is condensed and liquefied, and flows down into the tank 71, where the extract liquid 8 containing the active ingredient of koji can be obtained. The vaporized component that has not condensed in the cooling chamber 3 is returned to the atomization chamber 1 by the rotary fan 61. The extract 81 thus obtained is used as it is or after being appropriately diluted and used as a hair-growing agent, and exhibits excellent effects.

The above experimental data are as follows. Malt 50g Reduced pressure value 130mmAg Extraction time 7 minutes / 1 cycle x 4 times = 28 minutes Extraction amount 15cc / 1 cycle x 4 times = 6
0 cc Temperature of atomized fine particles 35 ° C to 45 ° C, 45 ° C to 50
Experiments were carried out at three stages of 50 ° C and 50 ° C to 65 ° C. Burning of Extract Liquid The obtained extract liquid was subjected to heat treatment at a temperature of 65 ° C. to 80 ° C. for the purpose of stopping fermentation, sterilizing and the like.

The hair-growth agent in the above-mentioned examples was shown only when malt extract was used.
It has been found from experiments that extracts from koji, barley, soybeans, red beans, sesame, kelp, shiitake mushrooms, leaves of Konotega wrinkle, etc. also show extremely excellent hair growth effects. However, these extracts show a hair-growth effect only when they are extracted by the same method as the step described in claim 3 or 4, specifically, by any of the devices according to claims 5 to 11. This fact is
A common trace substance contained in malt, koji, barley, soybean, adzuki bean, sesame, kelp, shiitake mushroom, Konotega wrinkle, etc. has a hair-growth effect, and this trace substance is the method according to claim 3 to 11. Or that it is extracted only by the device. However, since the extracted substance is extremely minute, it is difficult to analyze and identify it. Therefore, in the present application, the substance must be simply expressed as an active ingredient.

[0034]

As described above, the invention according to this application provides an extremely effective hair-growth agent, a method for producing the same, and an active-ingredient extraction device that is essential for carrying out these inventions.

[Brief description of drawings]

FIG. 1 is a side view showing an embodiment of a device for extracting an active ingredient such as malt.

FIG. 2 is a side view showing the relationship between the extraction unit and the conveying means in the embodiment shown in FIG.

FIG. 3 is a perspective view showing a relationship between a decompression chamber and a transfer duct.

FIG. 4 is a side view showing another embodiment of the apparatus for extracting an active ingredient such as malt.

5 is a side view showing an embodiment of the extraction unit shown in FIG. 4. FIG.

FIG. 6 is a side view showing the relationship between the extraction unit and the conveyance means in FIG.

FIG. 7 is a perspective view showing the relationship between the decompression chamber and the transfer pipe in FIG.

[Explanation of symbols]

 H Hopper-L Conveying means U Extraction unit 1 Atomizing chamber 2 Depressurizing chamber 3 Cooling means 4 Depressurizing means 5 First circulation pipe 5a First heating means 6 Second circulation pipe 7 Third circulation pipe 7a Second heating means 8 Tank D Drying means H Hopper L Conveying means U Extraction unit M Motor 1 Atomizing chamber 2 Depressurizing chamber 3 Cooling chamber 41 Circulating pipe 51 Heating means 61 Rotating fan 71 Tank 81 Extracting liquid 11 Conveying pipe 12 Conveying screw 13 Gas circulating part 14 Stirring means 15 Adjustment plate 16 Gas flow rate adjusting means

Claims (11)

[Claims] 1. A hair-growing agent containing malt as an active ingredient. 2. A hair growth agent comprising an extract extracted from malt as an active ingredient. 3. The hair growing agent according to claim 2, wherein the extract extracted from malt is an extract produced by the following steps. a: a step of depressurizing malt, b: a step of turning water or other liquid into atomized fine particles and / or vapor, c: heating the atomized fine particles and / or vapor to a temperature higher than that of malt under reduced pressure, and malt these Is fed into the depressurized space in which the malt is contacted to cause dew condensation on the surface of the malt, and the active ingredient of malt is leached on the surface of the malt, d: the dew condensation and condensation of the active ingredient leached on the surface of malt Absorbing and holding in other atomized fine particles and / or vapor passing through the depressurized space without transferring, and transferring to the outside of the depressurized space in a vaporized state, e: In the step d, the active ingredient of malt is held and put out of the depressurized space. A step of cooling the transferred gas to obtain a liquid containing an active ingredient of malt. 4. A method for producing a hair growth agent, which comprises the following steps. a: a step of depressurizing malt, b: a step of turning water or other liquid into atomized fine particles and / or vapor, c: heating the atomized fine particles and / or vapor to a temperature higher than that of malt under reduced pressure, and malt these Is fed into the depressurized space in which the malt is contacted to cause dew condensation on the surface of the malt, and the active ingredient of malt is leached on the surface of the malt, d: the dew condensation and condensation of the active ingredient leached on the surface of malt Absorbing and holding in other atomized fine particles and / or vapor passing through the depressurized space without transferring, and transferring to the outside of the depressurized space in a vaporized state, e: In the step d, the active ingredient of malt is held and put out of the depressurized space. A step of cooling the transferred gas to obtain a liquid containing an active ingredient of malt. 5. An apparatus for extracting an active ingredient thereof from malt, koji or the like, comprising one or more extraction units and a conveying means for supplying an extraction object from a supply tank to the extraction unit. The extraction unit includes an atomization chamber for forcibly atomizing water or other liquid, and a decompression chamber for connecting the atomization chamber with the first circulation pipe to depressurize an object to be extracted. A decompression unit connected to the decompression chamber by a second circulation pipe; a third circulation pipe connecting the decompression unit to the atomization chamber; a first heating unit provided in the first circulation pipe; The pipe includes a cooling unit and a second heating unit provided in the third circulation pipe, and the transfer unit moves a transfer duct that vertically penetrates the decompression chamber and an object to be extracted in the transfer duct. The upper end of the carrier pipe to let A pressing means provided, the active ingredient extraction device, characterized in that is constituted by a pressure adjusting means provided at the lower end of the transport duct. 6. The active ingredient extracting device according to claim 5, wherein the means comprises first and second cooling means. 7. The active ingredient extracting device according to claim 5, wherein the depressurizing means comprises a rotary fan. 8. An apparatus for extracting the active ingredient thereof from malt, koji or the like, comprising one or more extraction units, and a conveying means for supplying an extraction object from a supply tank to the extraction unit. , A means for drying the extraction object carried out from the extraction unit after extracting the active ingredient, the extraction unit, the atomization chamber for forcibly atomizing water or other liquid, and the extraction A decompression chamber for decompressing an object, a cooling chamber, a circulation pipe connecting them, and heating atomized fine particles and / or steam of water or other liquid moving from the atomization chamber to the decompression chamber through the circulation pipe. And a suction fan provided in a circulation pipe connecting the atomizing chamber and the cooling chamber, the conveying unit is installed between the supply tank and the drying unit, and the decompressing chamber is installed. Horizontal It is characterized in that it is configured by a transport pipe penetrating through, a transport screw provided at the start end of the transport pipe for moving the extraction target in the transport pipe, and a gas circulation unit provided in the transport pipe in the decompression chamber. Active ingredient extractor. 9. The transport pipe according to claim 8, wherein the transport pipe has an adjusting plate for making the extraction object have a uniform thickness in the transport pipe, and a stirring plate for stirring the extraction object before transporting the extraction object to the decompression chamber. An active ingredient extraction device characterized by having a stirring device. 10. The active ingredient extracting device according to claim 8, wherein the gas flow section is provided with a gas passage amount adjusting means. 11. The active ingredient extracting apparatus according to claim 8, wherein the conveying means is always operated during the extracting operation, and the object to be extracted is moved in the decompression chamber at a constant speed.