WO2013035832A1 - Method for producing green and dried eucommia leaf product - Google Patents

Method for producing green and dried eucommia leaf product Download PDF

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Publication number
WO2013035832A1
WO2013035832A1 PCT/JP2012/072867 JP2012072867W WO2013035832A1 WO 2013035832 A1 WO2013035832 A1 WO 2013035832A1 JP 2012072867 W JP2012072867 W JP 2012072867W WO 2013035832 A1 WO2013035832 A1 WO 2013035832A1
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Prior art keywords
green
leaves
dried
drying
leaf
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PCT/JP2012/072867
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French (fr)
Japanese (ja)
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智恵子 安間
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有限会社 碧山園
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    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23LFOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
    • A23L2/00Non-alcoholic beverages; Dry compositions or concentrates therefor; Their preparation
    • A23L2/385Concentrates of non-alcoholic beverages
    • A23L2/39Dry compositions
    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23BPRESERVING, e.g. BY CANNING, MEAT, FISH, EGGS, FRUIT, VEGETABLES, EDIBLE SEEDS; CHEMICAL RIPENING OF FRUIT OR VEGETABLES; THE PRESERVED, RIPENED, OR CANNED PRODUCTS
    • A23B7/00Preservation or chemical ripening of fruit or vegetables
    • A23B7/005Preserving by heating
    • A23B7/01Preserving by heating by irradiation or electric treatment
    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23BPRESERVING, e.g. BY CANNING, MEAT, FISH, EGGS, FRUIT, VEGETABLES, EDIBLE SEEDS; CHEMICAL RIPENING OF FRUIT OR VEGETABLES; THE PRESERVED, RIPENED, OR CANNED PRODUCTS
    • A23B7/00Preservation or chemical ripening of fruit or vegetables
    • A23B7/02Dehydrating; Subsequent reconstitution
    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23BPRESERVING, e.g. BY CANNING, MEAT, FISH, EGGS, FRUIT, VEGETABLES, EDIBLE SEEDS; CHEMICAL RIPENING OF FRUIT OR VEGETABLES; THE PRESERVED, RIPENED, OR CANNED PRODUCTS
    • A23B7/00Preservation or chemical ripening of fruit or vegetables
    • A23B7/02Dehydrating; Subsequent reconstitution
    • A23B7/0205Dehydrating; Subsequent reconstitution by contact of the material with fluids, e.g. drying gas or extracting liquids
    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23FCOFFEE; TEA; THEIR SUBSTITUTES; MANUFACTURE, PREPARATION, OR INFUSION THEREOF
    • A23F3/00Tea; Tea substitutes; Preparations thereof
    • A23F3/34Tea substitutes, e.g. matè; Extracts or infusions thereof

Definitions

  • the present invention relates to a method for producing a green dried product of Tochu Naka, and more particularly to a method for drying Tochu Leaf while exhibiting a bright green color and without decomposing high-functional components contained in Tochu Tea.
  • Tochu's bark has long been prized as one of the five major Chinese herbal medicines, but in recent years, the high functionality and usefulness of components such as iridoids and polyphenols contained in Tochu's leaves have attracted attention.
  • iridoids have been shown to be useful for blood pressure lowering action, analgesic action, and improvement of lipid metabolism (see Non-Patent Document 1 and Non-Patent Document 2), and are currently drunk mainly as tea.
  • the iridoids are known as compounds having 1-isopropyl-2,3-dimethylcyclopentane in the structure.
  • the iridoids contained in the dried green product of Tonaka green obtained by the present invention are geniposide acid and asperoside.
  • the polyphenol compound is known as a compound having a plurality of phenolic hydroxyl groups in its structure.
  • the polyphenol compound contained in the dried green rice leaf product obtained by the present invention is chlorogenic acid or flavonoids such as rutin, quercetin, nicotiflorin and kaempferol.
  • Patent Document 1 discloses a method for producing green potato Nakaba containing about 3.2% of geniposide acid.
  • Patent Document 2 green leaves containing geniposidic acid at a high concentration are obtained through a process including drying after a roasting process in which fresh leaves of Tochu are used as a raw material and fumigated at 300 to 350 ° C. A method for producing Tochu tea leaves is proposed. Further, in Patent Document 3, an iridoid having a bright green color is obtained by intermittently applying microwave heating or high-frequency heating and performing a drying treatment under conditions where the leaf temperature is 50 to 100 ° C. It has been found that a dried green leafy green powder containing high-functional components such as sucrose and polyphenols at a high concentration can be obtained.
  • JP-A-10-150961 Japanese Patent No. 4340812 JP 2010-158230 A JP 2011-250725 A
  • Tochu leaves have a strong vein covered with the fiber component Guttavelka, and therefore the drying time differs greatly between the leaf portion and the vein. Therefore, in the processing method of Patent Document 3 described above, it took 1 hour 30 minutes to 2 hours to dry the veins.
  • Guttavelca contains a large amount of geniposide acid, which is a unique component of Tochu, so drying of the veins is an important problem, and it is desirable to shorten the drying time.
  • the present invention has been made in view of the present situation, and the processing time, which conventionally took 120 minutes, is suppressed to a quarter or less, and the leaves are not subjected to as much temperature as possible during drying and pulverization. It is an object of the present invention to provide a processing method for producing fine powdered tea, having beautiful green and sweet ingredients with high numbers without wrinkles, and a green fine powder made from the processing method.
  • the cause of this is not clear, for example, as seen in gardenia pigments, the production of natural pigments by iridoids can be considered.
  • iridoid glycosides and glucosidase play an important role in protein denaturation due to insect damage in the mosquito family Ibota. Because of the tendency of discoloration from damaged or strained or stressed parts, the glucosidase, polyphenol oxidase and other enzymes contained in the organelles dissipate out of the endoplasmic reticulum for some reason. It is possible that the iridoid glycosides contained in the leaf act as a protein cross-linking agent and bind to the protein to produce a pigment.
  • the leaves are arranged at almost equal intervals so that the leaves do not touch each other, and far-infrared rays are irradiated while maintaining the state of the arranged leaves, so that the moisture in the leaves is 30% or less of the moisture content before drying. It has been found that it is dried until it has become, and has already been proposed (Patent Document 4).
  • the present inventor in order to quickly absorb heat when performing drying until the moisture in the leaves becomes 3% or less of the moisture content before drying by irradiation with far-infrared rays of the green leaves
  • the leaf surface temperature must be 60 ° C. or lower, preferably 50 ° C. or lower, and for that purpose, while blowing air at 0 to 60 ° C., preferably 0 to 40 ° C., more preferably 5 to 15 ° C. It has been found that by irradiating far infrared rays, the water content in the leaf can be reduced to 3% or less of the water content before drying within 30 minutes after the start of heating.
  • [3] The method for producing a green dried green product of [1] or [2], wherein the far infrared heating and drying apparatus is heated and dried at a set temperature of 200 to 600 ° C. from the start to the end of the heat treatment. .
  • [4] Any one of [1] to [3], wherein the leaf surface temperature measured with an infrared non-contact thermometer is 60 ° C. or less from the start to the end of the heat drying treatment.
  • Method for producing dried green leaves [5] The method for producing a dried dried green product of [1] to [4], wherein the drying is performed in an atmosphere of 30% or less from the start to the end of the heat drying treatment.
  • a green product characterized in that it comprises a step of pulverizing the green dried green leaf product obtained by any one of the methods [1] to [8] to a powder at a temperature of 0 to 70 ° C. or lower.
  • a method for producing Tochu's powdered beverage [10] The method for producing a green Bunchu powdered drink according to [9], wherein the air is blown at 0 to 70 ° C. in the pulverizing step. [11] The method for producing a green Tochu powder drink according to [10], wherein liquid nitrogen is used for the blowing.
  • the production method of the present invention it is possible to quickly remove the water in the leaf required for the enzymatic reaction and autolysis action in a short time, with almost no stress on the leaf, thus maintaining a bright green color,
  • a decrease in high-functional components such as geniposide acid, iridoids, and polyphenols is suppressed to a low level, and a dried Nakanaka green product containing these high-functional components at a high concentration is obtained.
  • the method for producing a dried dried green leaf product according to the present invention is a method in which dried dried leaves are irradiated with far-infrared rays, and the dried dried leaves are heated to 0 to 60 ° C, preferably 0 to 40 ° C. More preferably, heating is performed by irradiating far infrared rays while blowing air at 5 to 15 ° C., and heating and drying until the moisture content in the leaf becomes 3% or less of the moisture content before drying within 30 minutes after the start of heating. It is a feature.
  • the bamboo leaves used as a raw material mean the company leaves before being subjected to heat drying treatment after harvesting, and even if they are produced by cultivation, It may be produced.
  • fresh leaves collected before the fall of the current year in Kanagawa Prefecture, for example, fresh leaves collected from April to October, preferably from May to August, more preferably from July to August can be used.
  • Tochu Nakaba is easily self-destructing and deteriorates quickly. Further, the cut Nakaba leaves rapidly deteriorated simultaneously with the cutting. Therefore, it must be dried quickly to prevent fermentation.
  • a far-infrared drying method is desirable as a method for rapid drying. And in order to shorten the drying time in far-infrared heating, the difference between the far-infrared and the leaf surface temperature must be made as large as possible. However, if the leaves are frozen, when they are heated, they are deteriorated by stress and discolored to purple, so they cannot be frozen.
  • the heat-drying treatment is started by irradiating far-infrared rays with the far-infrared rays while heating them at 0-60 ° C, preferably 0-40 ° C, more preferably 5-15 ° C.
  • the leaf surface temperature is kept at 60 ° C. or lower, preferably 50 ° C. or lower, more preferably 40 ° C. or lower, and heat is absorbed quickly.
  • the method for blowing air at the predetermined temperature is not particularly limited.
  • the outside air may be simply blown, or the air may be blown by using an electric device.
  • liquid nitrogen for air blowing air blowing at 0 to 40 ° C., preferably 0 to 20 ° C., can be performed efficiently.
  • Nakasei leaves may be heat-dried after cutting until the moisture content in the leaves is 3% or less of the moisture content before drying. It may be cut after drying until the moisture content in the leaf is 3% or less of the moisture content before drying.
  • ⁇ ⁇ ⁇ When cutting Nakasei leaves, they must be cut sharply so as not to stress the leaves, and the veins should be cut into squares of 2 cm or less, 1 cm squares, or rectangular shapes of 2 cm or less and 1 cm or less in a direction perpendicular to the veins. I must.
  • the heat drying in the present invention is performed using a far infrared heater equipped with a blower and an air conditioner.
  • the set temperature is 200 to 600 ° C., preferably 0 to 500 ° C., more preferably. Is dried at 300-400 ° C.
  • the far-infrared heater may be a conveyor type or a multi-stage type, and the wavelength of the far infrared ray to be irradiated is, for example, in the range of 1 to 1000 ⁇ m, preferably 2.5 to 50 ⁇ m. Can be appropriately selected.
  • the leaves are arranged substantially evenly so that the leaves are not in contact with each other, and the far infrared rays are maintained in a state where the arranged leaves are maintained. Irradiation is preferred. For example, if you put a cocoon leaf in a rotary drum of a rotary drying furnace and heat and dry it with the leaf rotated, distortion or pressure will occur due to contact between the nakanaka leaf and the drum or between the leaves. Discoloration of ⁇ ⁇ tends to occur.
  • the leaves or the leaves and the device contact each other by irradiating far-infrared rays while maintaining the state of the arranged leaves in a substantially uniform manner so that the leaves do not touch each other.
  • the water in the leaves can be quickly removed in a state where there is almost no stress due to the occurrence of stress due to, and a green dried green product that contains vivid green and contains useful components at a high concentration is obtained. It is done.
  • far infrared rays may be irradiated in a state where the leaves are arranged on three upper and lower drying shelves.
  • the heat drying treatment with far-infrared rays is performed until at least the moisture content of the Tochu Naka leaf is 3% or less of the moisture content before drying.
  • the moisture content before drying means the moisture content contained in the Tochu-nakaba immediately before being subjected to the heat drying treatment by far infrared rays. That is, in the production method of the present invention, for example, when the amount of water contained in the bamboo leaf before being subjected to the heat-drying treatment is 100 g, the far-infrared rays until the amount of water remaining in the leaves becomes 3 g or less.
  • the heat drying process by is performed.
  • the progress of the enzymatic reaction and the self-digestion action is significantly hindered by quickly reducing the water content in the leaves to 3% or less of the water content before drying.
  • the heat drying process using infrared rays it is desirable to perform the drying process in an atmosphere with a humidity of 30% or less, more preferably 10% or less, from the start to the end of the heat treatment.
  • a humidity of 30% or less more preferably 10% or less
  • moisture evaporates from the leaf surface, so that the atmospheric humidity increases with the progress of drying.
  • the atmospheric humidity exceeds 10% during the heat-drying process using far infrared rays, it is difficult to evaporate moisture from the leaf surface, and it becomes difficult to remove moisture in the leaf in a short time.
  • the atmospheric humidity significantly increases due to the evaporation of moisture in the leaves.
  • the blowing means in the heat drying treatment with far infrared rays, it is desirable to appropriately control the blowing means so that the maximum leaf temperature measured by the infrared non-contact thermometer is 60 ° C. or less, more preferably 50 or less.
  • the conveyor-type far-infrared heating and drying apparatus 10 is provided with a far-infrared irradiation unit 14 and a blower 16 inside a drying chamber 12. Moreover, the conveyor 18 is provided so that it can move from the one side through the drying chamber 12 and continuously with the other side.
  • Nakasei leaves 20 to be subjected to a heat drying process using far infrared rays are arranged on the conveyor 18 at substantially equal intervals so that the leaves do not contact each other. Then, the green leaves 20 arranged on the conveyor 18 are sent into the drying chamber 12 while maintaining the state of the arranged leaves. Inside the drying chamber 12, far-infrared rays are radiated from the up-and-down direction to the cocoon leaves 20 by the far-infrared ray irradiation unit 14. Then, the foliage leaves 20 irradiated with far-infrared rays have a leaf temperature that rises, moisture is vaporized, and the amount of moisture decreases.
  • the inside of the drying chamber 12 is blown by the blower 16 so that the atmospheric humidity and the atmospheric temperature in the room are kept almost constant. That is, in normal cases, the moisture in the leaves is vaporized by heating to become water vapor, so that the humidity and temperature in the drying chamber 12 are increased. However, the water is exhausted to the outside by being blown by the blower unit 16. The humidity and temperature in the drying chamber 12 are kept almost constant.
  • the dried green leaves 20 dried in the drying chamber 12 are sent to the outside of the drying chamber 12 by the conveyor 18.
  • moisture content of the foliage leaf 20 has decreased to 3% or less of the water content before drying within 30 minutes after the start of far-infrared irradiation.
  • the far-infrared irradiation intensity by the far-infrared irradiation unit 14 so that the indoor atmospheric humidity, the atmospheric temperature, and the leaf surface temperature are within the preferable numerical ranges shown above, and It is desirable to adjust the blowing temperature and the blowing amount by the blowing unit 16. That is, using the far-infrared heating and drying apparatus 10 of FIG. 1, the operating conditions of the far-infrared irradiation unit 14 and the blower unit 16 are adjusted, and the atmospheric temperature, atmospheric humidity, leaf surface temperature, etc. in the drying chamber 12 are adjusted. By appropriate control, the leaves are dried until the moisture content of the leaves becomes 3% or less of the moisture content before drying within 30 minutes after the start of heating.
  • the leaves are arranged at substantially equal intervals so as not to contact each other, the leaves are heated uniformly and efficiently by irradiation with far infrared rays, and the leaves or leaves There is no distortion or pressure due to the contact of the apparatus, and the leaves are hardly stressed, so discoloration is unlikely to occur during the drying process.
  • free water In order for the enzymatic reaction and self-digestion to proceed, it is considered that free water must be included as the moisture in the leaves, and until the moisture content in the leaves becomes 3% or less of the moisture content before drying. In dried Tochu leaves, almost all of the free water contained in the leaves has been removed, so there is almost no discoloration or decrease in useful components.
  • the chunaka leaf under the condition of humidity of 50% or less, more preferably 30% or less, until the pickled chunaka leaf is made into a product. If Nakanakayo is placed under high humidity exceeding 50% humidity, it may cause a decrease in high-functional components such as iridoids and polyphenols. In addition, the leaves turn purple and green The product may not be obtained.
  • the leaves of Tochu are grown to 30 cm or more, and the veins are 5 mm or more in thickness.
  • a difference in water evaporation occurs between the vein portion and the portion other than the leaf vein in the drying process, and the leaf vein becomes purple due to self-digestion. This is considered to be due to the structure being stressed around the veins and the cells of the veins being destroyed in a state sufficiently containing water.
  • useful components such as iridoids are decomposed to reduce the content, and in addition, the green color is lost due to discoloration.
  • the veins contain a lot of highly functional components, the drying of the veins is extremely important.
  • the conventional drying method it is very difficult to quickly dry a vein portion having a thickness of 5 mm or more.
  • it is divided into the leaf vein part and other parts of Tochu Naka leaf, changing the heating temperature and treatment time, etc., and performing the drying treatment according to each, discoloration due to self-digestion action, thermal decomposition caused by excessive heating, etc.
  • the loss of high-functional components can be kept low.
  • the types and amounts of components contained in the vein portion and other portions are different.
  • the vein portion contains a large amount of geniposide acid and the other portions contain a large amount of chlorogenic acid. Therefore, it is possible to separate a product derived from the vein portion and a product derived from another portion according to the desired type of active ingredient.
  • the freshly-cured Toka Nakasei leaves which have been appropriately collected without cutting in advance, are heat-dried with far-infrared rays until the water content of the leaves becomes 3% or less of the water content before drying.
  • the pruned leaves of the shrunken leaves are cut into two pieces, the vein and the parts on both sides of the leaves, they can be heated and dried with far infrared rays until the moisture content is 3% or less of the moisture content before drying. Is possible.
  • the content of iridoids and polyphenols contained in the Tochu Naka leaf varies depending on individual differences in Tochu Nakamoto, harvest time, etc., but in the dried green product of Tochu Naka leaf obtained by the present invention, the content of the iridoids, It is considered that about 70% by mass or more of the content (in terms of dry mass) of iridoids contained in the company Nakasei leaves immediately after harvest used as a raw material is maintained.
  • the dried green leaves of the Nakanaka leaf obtained by the production method of the present invention contain high concentrations of iridoids and polyphenol compounds, these highly functional components are extracted after being once treated as a dried Nakanaka leaf product. It is also useful as an extraction method.
  • the dried dried green leaves of dried Nakanaka leaves are preferably made into a finely pulverized powder having an average diameter of 3 to 14 ⁇ m.
  • the pulverization method is not particularly limited, and for example, a jet mill pulverizer, an airflow pulverizer, or the like can be used.
  • the pulverization temperature is 0 to 70 ° C. or less, preferably 0 to It is preferable to grind at 40 ° C. or lower, more preferably 0 to 20 ° C. or lower.
  • the green powder of green liquor made in this way becomes a fine powder of 3-14 ⁇ m, preferably 6 ⁇ m on average, with a refreshing green and beautiful sweetness, which is not only suitable for drinking but also geniposide peculiar to liquor
  • a health food containing a large amount of acid, chlorogenic sun, asperroside, folic acid, vitamin E, and vitamin A can be provided.
  • Example 1 Uncut cocoon leaves were arranged evenly on a far-infrared conveyor dryer equipped with a blower so that the leaves would not touch each other, and dried for 12 minutes and 30 seconds at a set temperature of 350 ° C. while blowing air at 25 ° C.
  • the maximum temperature of the leaf surface during the drying treatment was about 46.5 ° C., and the moisture content after drying was 3% of the moisture content before drying.
  • the obtained dried leaves were pulverized for 10 to 20 minutes using a cyclone mill to obtain a green dry fine powder having an average of 7 ⁇ m.
  • Example 2 It dried for 13 minutes and 30 seconds like Example 1 except having set it as 20 degreeC ventilation.
  • the maximum temperature of the leaf surface during the drying treatment was about 37.0 ° C., and the moisture content after drying was 3% of the moisture content before drying. From the obtained dried leaves, a green dry fine powder having an average of 7 ⁇ m was obtained in the same manner as in Example 1.
  • Example 3 Drying was carried out for 10 minutes in the same manner as in Example 1 except that the set temperature was 400 ° C. and liquid nitrogen was used for blowing air and 5 ° C. cold air was used for blowing air.
  • the maximum temperature of the leaf surface during the drying treatment was about 15.0 ° C., and the moisture content after drying was 3% of the moisture content before drying.
  • the resulting dried leaves were pulverized using a cyclone mill while feeding cold air at 5 ° C. using liquid nitrogen to obtain a green dry fine powder having an average of 6 ⁇ m.
  • Example 1 (Comparative Example 1) Using the apparatus of Example 1, the set temperature was set to 170 ° C. and dried for 10 minutes without blowing. The maximum temperature of the leaf surface during the drying treatment was about 70 ° C., and the moisture content after drying was 47.3% of the moisture content before drying. The shelf dryer was set to 60 ° C. and dried for 30 minutes. From the obtained dried leaves, a green dry fine powder having an average of 7 ⁇ m was obtained in the same manner as in Example 1.
  • Example 2 (Comparative Example 2) Using the apparatus of Example 1, the set temperature was set to 230 ° C., and drying was performed for 15 minutes without blowing. The maximum temperature of the leaf surface during the drying treatment was about 110 ° C., and the moisture content after drying was 3% of the moisture content before drying, but it was partially burnt. However, the stem could not be dried. From the obtained dried leaves, a green dry fine powder having an average of 7 ⁇ m was obtained in the same manner as in Example 1.
  • Example 3 Drying was carried out for 20 minutes in the same manner as in Example 1 except that the set temperature was 140 ° C. and the ventilation was 120 ° C. The maximum temperature of the leaf surface during the drying treatment was about 130 ° C., and the moisture content after drying was 3% of the moisture content before drying. From the obtained dried leaves, a green dry fine powder having an average of 7 ⁇ m was obtained in the same manner as in Example 1.
  • Table 1 shows the results of color, taste, and component analysis of the dry powders obtained in Examples 1 to 3 and Comparative Examples 1 to 3.
  • the component analysis was measured by HPLC (high performance liquid chromatography; methanol extraction). All units are ⁇ g / g (active ingredient amount / sample mass).
  • the surface temperature of the leaves is kept at 60 ° C. or lower by irradiating far-infrared leaves while blowing air at 0 to 60 ° C. from the start to the end of the heat drying treatment, and heating starts.
  • the green dried products of Tonaka tea leaves of Examples 1 to 3 obtained by quickly drying and removing the moisture in the leaves until the moisture content in the leaves became 3% or less of the moisture content before drying within 30 minutes later were asperoside and geniposide It can be seen that they contain a large amount of iridoids such as acids. Moreover, high content is also obtained about chlorogenic acid which is a kind of polyphenol.
  • the green dried product of Example 3 green tea of Example 3 performed at 5 ° C. using liquid nitrogen in the cold air of 5 ° C. using liquid nitrogen and pulverizing after drying is more suitable.
  • the contents of chlorogenic acid, asperoside and geniposide acid were increased as compared with the green dried green tea leaves obtained in Examples 1 and 2.
  • the dried green tea leaves of comparative example 1 obtained by drying for the same time at a set temperature lower than those of Examples 1 to 3 without blowing air gave a taste free of wrinkles, but were dried.
  • the color was purple and dark green, and the contents of chlorogenic acid, asperoside and geniposide acid were all low.
  • comparison was obtained by setting the temperature higher than that of Comparative Example 1 and drying and removing the moisture in the leaf until the drying time was 1.5 times and the moisture content in the leaf was 3% or less of the moisture content before drying.
  • the dried green tea leaf green product of Example 2 had a savory taste and a green color, but the contents of asperoside and geniposide acid were both lower than those of Comparative Example 1.
  • the obtained green dried green tea leaves of Comparative Example 3 had a refreshing green color, but had a bitter taste and had very low contents of chlorogenic acid, asperloside, and geniposide acid.

Abstract

The purpose of the present invention is to provide a processing method, whereby a green tea micropowder having a pure green color and high sweetness and containing a large amount of useful components can be produced while shortening the production time by 1/4 (compared with a conventional method requiring 120 minutes) and minimizing the heating of leaves in drying and milling, and a green micropowder produced by the processing method. A method for heating and drying fresh eucommia leaves by far infrared ray irradiation, said method comprising: irradiating fresh eucommia leaves with far infrared ray under blowing an air stream at 0-60oC thereto from start to finish of the heating and drying treatment; and thus conducting the heating and drying treatment in such a manner that the moisture content of the leaves is reduced to 3% or less, relative to the moisture content thereof prior to drying, within 30 minutes after starting the heating, thereby giving a green and dried eucommia leaf product.

Description

杜仲葉の緑色乾燥品の製造方法Manufacturing method of green dried products
 本発明は、杜仲葉の緑色乾燥品の製造方法に関し、特に、鮮やかな緑色を呈するとともに、杜仲茶に含まれる高機能成分を分解することなく、杜仲葉を乾燥させる方法に関する。 The present invention relates to a method for producing a green dried product of Tochu Naka, and more particularly to a method for drying Tochu Leaf while exhibiting a bright green color and without decomposing high-functional components contained in Tochu Tea.
 杜仲の樹皮は、中国五大漢方薬のひとつとして古来より珍重されてきたが、近年では、杜仲葉に含有されるイリドイド類、ポリフェノール等の成分の高機能性・有用性が注目されている。特に、イリドイド類は血圧降下作用や鎮痛作用、脂質代謝の改善に有用であることが示されており(非特許文献1、非特許文献2参照)、現在、主に茶として飲用されている。
 なお、イリドイド類とは、その構造中に1-イソプロピル-2,3-ジメチルシクロペンタンを有する化合物として知られているものである。本発明により得られた杜仲葉緑色乾燥品に含まれるイリドイド類はゲニポシド酸及びアスペルロシドである。
 また、ポリフェノール化合物とは、その構造中にフェノール性水酸基を複数有する化合物として知られているものである。本発明により得られた杜仲葉緑色乾燥品に含まれるポリフェノール化合物はクロロゲン酸、又はルチン、クエルセチン、ニコチフロリン及びケンフェロール等のフラボノイド類である。
Tochu's bark has long been prized as one of the five major Chinese herbal medicines, but in recent years, the high functionality and usefulness of components such as iridoids and polyphenols contained in Tochu's leaves have attracted attention. In particular, iridoids have been shown to be useful for blood pressure lowering action, analgesic action, and improvement of lipid metabolism (see Non-Patent Document 1 and Non-Patent Document 2), and are currently drunk mainly as tea.
The iridoids are known as compounds having 1-isopropyl-2,3-dimethylcyclopentane in the structure. The iridoids contained in the dried green product of Tonaka green obtained by the present invention are geniposide acid and asperoside.
The polyphenol compound is known as a compound having a plurality of phenolic hydroxyl groups in its structure. The polyphenol compound contained in the dried green rice leaf product obtained by the present invention is chlorogenic acid or flavonoids such as rutin, quercetin, nicotiflorin and kaempferol.
 しかしながら、杜仲の葉に含まれるイリドイド類等の高機能成分は葉を収穫した段階から、自己消化作用によってその減少が始まってしまう。また、現在、杜仲茶として市販されているものの多くは、褐色の発酵茶葉であり、発酵過程において、イリドイド類の高機能成分の含有量が大幅に減少し、さらに苦味なども増加してしまうことになる。このため、一般に広く流通している飲料用乾燥茶葉において、イリドイド類の含有量は茶葉全体の1%にも満たない。 However, high functional components such as iridoids contained in Tochu leaves start to decrease due to self-digestion from the stage of harvesting the leaves. In addition, most of the products currently marketed as Tochu tea are brown fermented tea leaves, and during the fermentation process, the content of high-functional components of iridoids is greatly reduced, and bitterness is also increased. become. For this reason, in the dry tea leaves for beverages that are generally widely distributed, the content of iridoids is less than 1% of the total tea leaves.
 そこで、これらの高機能成分を豊富に含有する杜仲乾燥茶葉の製法が検討されている。近年、日本茶と同様にして製造した緑色の杜仲乾燥茶葉が、褐色の発酵茶と比較して、イリドイド類、ポリフェノール類等の有用成分を多く含有することがわかってきた。
 例えば、特許文献1には、ゲニポシド酸3.2%程度を含む緑色杜仲葉の製法が開示されている。この方法は、杜仲の葉を約2cmの幅に荒切り裁断した後、日本茶と同様に茶葉の蒸煮する工程、該蒸煮した杜仲木の葉を冷却する工程、該冷却した杜仲葉を粗乾燥する工程、その後該杜仲葉を約5mm以下の幅に細断する工程、細断した杜仲葉を粗揉しながら精乾燥しかつ精揉する工程、精乾燥しかつ精揉した後遠赤外線を熱源として焙煎する工程を有するものである。ここで、杜仲の場合、蒸煮加熱により酵素を失活させて発酵の進行を抑えることで、緑色を保持し、且つ自己消化作用を抑止して経時による劣化を防ぐことができると考えられる。しかしながら、ゲニポシド酸、イリドイド類、ポリフェノール類等の高機能成分は、熱劣化や蒸気による溶出・散逸で減少してしまうため、従来から行われてきた蒸煮加熱は、これら高機能成分の減少を招くものと考えられる。
Then, the manufacturing method of the Tochu dry tea leaf which contains these high functional ingredients abundantly is examined. In recent years, it has been found that green Tochu dry tea leaves produced in the same manner as Japanese tea contain more useful components such as iridoids and polyphenols than brown fermented tea.
For example, Patent Document 1 discloses a method for producing green potato Nakaba containing about 3.2% of geniposide acid. In this method, after roughly cutting the bamboo leaf to a width of about 2 cm, a step of steaming the tea leaf in the same manner as Japanese tea, a step of cooling the steamed bamboo leaf, and a step of roughly drying the cooled bamboo leaf Thereafter, the step of chopping the cocoon leaf to a width of about 5 mm or less, the step of scouring and scouring the chopped bamboo leaf, and then drying and scouring the far infrared rays as a heat source It has a process of roasting. Here, in the case of Tochu, it is considered that by suppressing the progress of fermentation by inactivating the enzyme by steaming heating, it is possible to maintain the green color and suppress the self-digestion action to prevent deterioration over time. However, high-performance components such as geniposide acid, iridoids, and polyphenols decrease due to thermal degradation and elution / dissipation due to steam, so the conventional steaming heating causes a decrease in these high-performance components. It is considered a thing.
 本発明者は、こうした問題を解決するために、これまでに種々の検討を重ねてきた。
 その1つとして、特許文献2では、杜仲の生葉を原料として用い、排蒸しながら、300~350℃で炒る炒り工程に次いで、乾燥を含む工程を経て、ゲニポシド酸を高濃度に含有する緑色の杜仲茶葉を製造する方法を提案している。
 また、特許文献3では、マイクロ波加熱又は高周波加熱を間歇的に作用させ、且つ葉の温度が50~100℃となる条件下で乾燥処理を行なうことによって、鮮やかな緑色を有しつつ、イリドイド類やポリフェノール等の高機能成分を高濃度で含有する杜仲葉緑色乾燥粉末が得られることを見出している。
The present inventor has made various studies so far in order to solve such problems.
As one of them, in Patent Document 2, green leaves containing geniposidic acid at a high concentration are obtained through a process including drying after a roasting process in which fresh leaves of Tochu are used as a raw material and fumigated at 300 to 350 ° C. A method for producing Tochu tea leaves is proposed.
Further, in Patent Document 3, an iridoid having a bright green color is obtained by intermittently applying microwave heating or high-frequency heating and performing a drying treatment under conditions where the leaf temperature is 50 to 100 ° C. It has been found that a dried green leafy green powder containing high-functional components such as sucrose and polyphenols at a high concentration can be obtained.
特開平10-150961号公報JP-A-10-150961 特許第4340812号公報Japanese Patent No. 4340812 特開2010-158230号公報JP 2010-158230 A 特開2011-250725号公報JP 2011-250725 A
 しかしながら、前述の特許文献2に記載された、杜仲葉を、釜炒り機等を用いて直接葉を加熱処理し、酵素を失活させる方法は、葉の温度が高温になり過ぎてしまい、高機能性成分の熱分解を生じてしまうため、必ずしもこれら高機能成分が十分な含有量で保持されていたものとは言い難い。
 一方で、これら高機能性成分の熱劣化あるいは蒸気による溶出・散逸等を避けるために、比較的低温によって加熱処理を行なうことも考えられるものの、この場合、酵素の失活が十分でなく、加えて茶葉の乾燥に非常に長い時間を要してしまうため、処理中に酵素反応や自己消化作用が進行してしまうという問題がある。
 特に、杜仲葉は、繊維成分のグッタベルカで覆われた屈強の葉脈をもっており、その為、葉の部分と葉脈では、乾燥の時間を大きく異にする。そこで、前述の特許文献3の加工方法では、葉脈を乾燥させるために、1時間30分から2時間の時間を要していた。
 しかしながら、特にグッタベルカには、杜仲特有の成分であるゲニポシド酸が多く含まれている為、葉脈の乾燥は重要な問題であって、乾燥時間を短縮させることが望まれる。
However, in the method described in Patent Document 2 described above, the method in which the leaves are directly heat-treated using a kettle stirrer or the like to inactivate the enzyme causes the temperature of the leaves to become too high. Since the functional components are thermally decomposed, it is not always possible to say that these high-functional components are held in a sufficient content.
On the other hand, in order to avoid thermal degradation of these highly functional components or elution / dissipation due to vapor, it is possible to carry out heat treatment at a relatively low temperature. However, in this case, the enzyme is not sufficiently deactivated. Since it takes a very long time to dry tea leaves, there is a problem that an enzymatic reaction and an autodigestive action proceed during the treatment.
In particular, Tochu leaves have a strong vein covered with the fiber component Guttavelka, and therefore the drying time differs greatly between the leaf portion and the vein. Therefore, in the processing method of Patent Document 3 described above, it took 1 hour 30 minutes to 2 hours to dry the veins.
However, in particular, Guttavelca contains a large amount of geniposide acid, which is a unique component of Tochu, so drying of the veins is an important problem, and it is desirable to shorten the drying time.
 本発明は、こうした現状を鑑みてなされたものであって、従来120分かかっていた加工時間を4分の1以下に抑え、葉に、乾燥及び粉砕時に出来るだけ温度をかけないで、緑の微粉末茶を製造し、癖のない美しい緑で甘味の多い有用成分を高い数字で保有する加工方法及びその加工方法から出来た緑微粉末を提供することを、目的とするものである。 The present invention has been made in view of the present situation, and the processing time, which conventionally took 120 minutes, is suppressed to a quarter or less, and the leaves are not subjected to as much temperature as possible during drying and pulverization. It is an object of the present invention to provide a processing method for producing fine powdered tea, having beautiful green and sweet ingredients with high numbers without wrinkles, and a green fine powder made from the processing method.
 杜仲葉は、収穫後、放置すると次第に紫色を呈し、特に高湿度では紫色を呈しやすく、特に葉脈部は濃い紫色に変色する。この原因は明らかではないが、例えば、クチナシ色素に見られるように、イリドイド類による天然色素の生成が考えられる。また、最近では、モクセイ科の植物イボタで、昆虫の食害によりイリドイド配糖体とグルコシダーゼが蛋白質変性に重要な役割をすることが報告されている。杜仲葉は傷ついた部分、歪や圧力がかかった部分から変色が進みやすいことからも、細胞小器官に含まれるグルコシダーゼ、ポリフェノールオキシダーゼなどの酵素が何らかの理由で、小胞体の外に散逸し、杜仲葉に含まれるイリドイド配糖体が蛋白質の架橋剤となり、蛋白質と結合して色素を生成している可能性が考えられる。 杜 Nakanaka leaves gradually purple when left after harvesting, and tends to be purple especially at high humidity, and especially the veins turn dark purple. Although the cause of this is not clear, for example, as seen in gardenia pigments, the production of natural pigments by iridoids can be considered. Recently, it has been reported that iridoid glycosides and glucosidase play an important role in protein denaturation due to insect damage in the mosquito family Ibota. Because of the tendency of discoloration from damaged or strained or stressed parts, the glucosidase, polyphenol oxidase and other enzymes contained in the organelles dissipate out of the endoplasmic reticulum for some reason. It is possible that the iridoid glycosides contained in the leaf act as a protein cross-linking agent and bind to the protein to produce a pigment.
 これらの自己消化作用は、含水条件下で生じるものと考えられるため、杜仲生葉の変色及びイリドイド類等の減少を防ぐためには、できるだけ葉にストレスをかけることなく、酵素反応及び自己消化作用に要する葉中の水分を速やかに除去することによって、酵素反応及び自己消化作用を生じないようにすることが重要であると考えられる。
 これらのことから、本発明者は、できるだけ葉にストレスをかけることなく、酵素反応及び自己消化作用に要する葉中の水分を速やかに除去することに着目して検討を行った結果、適採後の社仲生葉を、葉同士が互いに接触しないようにほぼ均等な間隔に並べ、並べた葉の状態を維持しつつ遠赤外線を照射して、葉中水分が乾燥前水分量の30%以下になるまで乾燥することを見いだし、既に提案している(上記特許文献4)。
Since these self-digestion effects are thought to occur under water-containing conditions, in order to prevent discoloration of 杜 nakasei leaves and reduction of iridoids, etc., it is necessary for enzyme reaction and self-digestion without stressing the leaves as much as possible. It is considered important to prevent the enzymatic reaction and autolysis from occurring by quickly removing moisture in the leaves.
From these results, the present inventor conducted an examination focusing on the rapid removal of water in the leaves necessary for the enzymatic reaction and autolysis action without stressing the leaves as much as possible. The leaves are arranged at almost equal intervals so that the leaves do not touch each other, and far-infrared rays are irradiated while maintaining the state of the arranged leaves, so that the moisture in the leaves is 30% or less of the moisture content before drying. It has been found that it is dried until it has become, and has already been proposed (Patent Document 4).
 本発明者は、さらに検討を重ねた結果、杜仲生葉の遠赤外線照射によって、葉中水分が乾燥前水分量の3%以下になるまで乾燥を行う場合、熱の吸収を速やかに行うためには、葉の表面温度を60℃以下、好ましくは50℃以下にしておくことが必要であり、そのために0~60℃、好ましくは0~40℃、さらに好ましくは5~15℃の送風を行いつつ遠赤外線を照射することで、葉中水分量を、加熱開始後30分以内に乾燥前水分量の3%以下にすることができることを見いだした。そして、この方法によれば、葉にほとんどストレスをかけることなく、短時間で速やかに酵素反応及び自己消化作用に要する葉中の水分を除去することができる結果、鮮やかな緑色を保持し、且つ、ゲニポシド酸、イリドイド類、ポリフェノール等の高機能性成分の減少が低く抑えられ、これらの高機能性成分を高濃度で含有する社仲葉緑色乾燥品が得られるものである。 As a result of further investigations, the present inventor, in order to quickly absorb heat when performing drying until the moisture in the leaves becomes 3% or less of the moisture content before drying by irradiation with far-infrared rays of the green leaves The leaf surface temperature must be 60 ° C. or lower, preferably 50 ° C. or lower, and for that purpose, while blowing air at 0 to 60 ° C., preferably 0 to 40 ° C., more preferably 5 to 15 ° C. It has been found that by irradiating far infrared rays, the water content in the leaf can be reduced to 3% or less of the water content before drying within 30 minutes after the start of heating. And according to this method, as a result of being able to remove the moisture in the leaves necessary for the enzymatic reaction and the self-digesting action quickly and in a short time with almost no stress on the leaves, the vivid green color is maintained, and , Geniposide acid, iridoids, polyphenols, and other high-functional components can be kept from decreasing, and a dried green product of the company Nakaba can be obtained containing these high-functional components in high concentrations.
 本発明は、これらの知見に基づいて完成するに至ったものであり、以下の発明を提供するものである。
[1]杜仲生葉を遠赤外線照射により加熱乾燥する方法において、加熱乾燥処理の開始から終了まで、杜仲生葉に0~60℃の送風を行いつつ遠赤外線を照射することにより、加熱開始後30分以内に葉中水分量が乾燥前水分量の3%以下になるまで加熱乾燥することを特徴とする杜仲葉緑色乾燥品の製造方法。
[2]前記送風に、液体窒素を用いることを特徴とする[1]の杜仲葉緑色乾燥品の製造方法。
[3]前記加熱処理の開始から終了まで、遠赤外線加熱乾燥装置の設定温度を200~600℃で加熱乾燥することを特徴とする[1]又は[2]の杜仲葉緑色乾燥品の製造方法。
[4]加熱乾燥処理の開始から終了まで、赤外線非接触温度計により測定した葉の表面温度が60℃以下となる範囲で加熱乾燥することを特徴とする[1]~[3]のいずれかの杜仲葉緑色乾燥品の製造方法。
[5]加熱乾燥処理の開始から終了まで、湿度30%以下の雰囲気下にて加熱乾燥することを特徴とする[1]~[4]のいずれかの杜仲葉緑色乾燥品の製造方法。
[6]杜仲生葉を、葉同士が互いに接触しないように略均等の間隔に並べ、並べた葉の状態を維持しつつ加熱乾燥することを特徴とする[1]~[5]のいずれかの杜仲葉緑色乾燥品の製造方法。
[7]前記杜仲葉は、予め裁断することなく適採したそのままの形状の社仲生葉である、[1]~[6]のいずれかの杜仲葉緑色乾燥品の製造方法。
[8]前記杜仲葉は、摘採後、葉脈とその両側の部分との三片に裁断した状態である、[1]~[6]のいずれかの杜仲葉緑色乾燥品の製造方法。
[9][1]~[8]のいずれかの方法で得られた杜仲葉緑色乾燥品を、温度を0~70℃以下で粉砕して粉末にする工程を含むことを特徴とする緑色の杜仲の粉末飲料の製造方法。
[10]前記粉砕工程において、0~70℃の送風を行うことを特徴とする[9]の緑色の杜仲の粉末飲料の製造方法。
[11]前記送風に、液体窒素を用いることを特徴とする[10]の緑色の杜仲の粉末飲料の製造方法。
The present invention has been completed based on these findings, and provides the following inventions.
[1] In the method of heating and drying cocoon leaves by far-infrared irradiation, 30 minutes after the start of heating by irradiating far-infrared rays while blowing air at 0 to 60 ° C. from the start to the end of the heat drying treatment A method for producing a dried green leaf green product, characterized in that heat drying is performed until the water content in the leaf becomes 3% or less of the water content before drying.
[2] The method for producing a dried dried green product of [1], wherein liquid nitrogen is used for the blowing.
[3] The method for producing a green dried green product of [1] or [2], wherein the far infrared heating and drying apparatus is heated and dried at a set temperature of 200 to 600 ° C. from the start to the end of the heat treatment. .
[4] Any one of [1] to [3], wherein the leaf surface temperature measured with an infrared non-contact thermometer is 60 ° C. or less from the start to the end of the heat drying treatment. Method for producing dried green leaves.
[5] The method for producing a dried dried green product of [1] to [4], wherein the drying is performed in an atmosphere of 30% or less from the start to the end of the heat drying treatment.
[6] Any one of [1] to [5], wherein the leaves are arranged at substantially equal intervals so that the leaves do not contact each other and are heated and dried while maintaining the state of the arranged leaves A method for producing dried green leaves.
[7] The method for producing a green dried green product of any one of [1] to [6], wherein the green leaf is a straight green leaf that has been appropriately cut without being cut in advance.
[8] The method for producing a green dried green product of any one of [1] to [6], wherein the pruned leaves are cut into three pieces of a vein and portions on both sides thereof after plucking.
[9] A green product characterized in that it comprises a step of pulverizing the green dried green leaf product obtained by any one of the methods [1] to [8] to a powder at a temperature of 0 to 70 ° C. or lower. A method for producing Tochu's powdered beverage.
[10] The method for producing a green Bunchu powdered drink according to [9], wherein the air is blown at 0 to 70 ° C. in the pulverizing step.
[11] The method for producing a green Tochu powder drink according to [10], wherein liquid nitrogen is used for the blowing.
 本発明の製造方法によれば、葉にほとんどストレスをかけることなく、短時間で速やかに酵素反応及び自己消化作用に要する葉中の水分を除去することができる結果、鮮やかな緑色を保持し、且つ、ゲニポシド酸、イリドイド類、ポリフェノール等の高機能性成分の減少が低く抑えられ、これらの高機能性成分を高濃度で含有する社仲葉緑色乾燥品が得られる。 According to the production method of the present invention, it is possible to quickly remove the water in the leaf required for the enzymatic reaction and autolysis action in a short time, with almost no stress on the leaf, thus maintaining a bright green color, In addition, a decrease in high-functional components such as geniposide acid, iridoids, and polyphenols is suppressed to a low level, and a dried Nakanaka green product containing these high-functional components at a high concentration is obtained.
本発明の方法を実施するのに用いる装置の一例を模式的に示す概略図。Schematic which shows typically an example of the apparatus used in implementing the method of this invention.
 本発明にかかる杜仲葉緑色乾燥品の製造方法は、杜仲生葉を遠赤外線照射により加熱乾燥する方法において、加熱乾燥処理の開始から終了まで、杜仲生葉に0~60℃、好ましくは0~40℃、さらに好ましくは5~15℃の送風を行いつつ遠赤外線を照射して加熱し、加熱開始後30分以内に葉中水分量が乾燥前水分量の3%以下になるまで加熱乾燥することを特徴とするものである。 The method for producing a dried dried green leaf product according to the present invention is a method in which dried dried leaves are irradiated with far-infrared rays, and the dried dried leaves are heated to 0 to 60 ° C, preferably 0 to 40 ° C. More preferably, heating is performed by irradiating far infrared rays while blowing air at 5 to 15 ° C., and heating and drying until the moisture content in the leaf becomes 3% or less of the moisture content before drying within 30 minutes after the start of heating. It is a feature.
 本発明の製造方法において、原料として使用する杜仲生葉は、収獲後、加熱乾燥処理に供される前の社仲葉を意味するものであり、栽培により生産されたものであっても、天然より生産されたものであってもよい。例えば、当年葉で落葉前の生葉、神奈川県内においては、例えば、4~10月、好ましくは5~8月、より好ましくは7~8月に採取した生葉を用いることができる。 In the production method of the present invention, the bamboo leaves used as a raw material mean the company leaves before being subjected to heat drying treatment after harvesting, and even if they are produced by cultivation, It may be produced. For example, fresh leaves collected before the fall of the current year, in Kanagawa Prefecture, for example, fresh leaves collected from April to October, preferably from May to August, more preferably from July to August can be used.
 杜仲葉は、自己破壊をおこしやすく劣化が早い。さらに裁断された杜仲葉は、裁断と同時に劣化が急速に進む。その為速やかに発酵を阻止するために乾燥しなければならない。速やかに乾燥する方法として、遠赤外線の乾燥方法が望ましい。
 そして、遠赤外線加熱における乾燥時間を短くするためには、遠赤外線と葉の表面温度の差を出来るだけ大きくしなければならない。しかし、葉を凍結させてしまうと温度を掛けた際に、ストレスによる劣化が起こり紫色に変色を起こすため、凍結させることはできない。
 そこで、本発明では、杜仲生葉に0~60℃、好ましくは0~40℃、より好ましくは5~15℃の送風をしつつ遠赤外線を照射して加熱することにより、加熱乾燥処理の開始から終了まで、葉の表面温度を60℃以下、好ましくは50℃以下、さらに好ましくは40℃以下に保ち、熱の吸収を速やかに行わせるものである。
 また、上記の所定温度の送風を行う方法については、特に限定されないが、たとえば、単に外気を送風しても良く、あるいは、電気装置を用いて冷風を作って送風しても良く、好ましくは、送風に、液体窒素を用いることで、0~40℃、好ましくは0~20℃の送風を効率良くおこなうことができる。
Tochu Nakaba is easily self-destructing and deteriorates quickly. Further, the cut Nakaba leaves rapidly deteriorated simultaneously with the cutting. Therefore, it must be dried quickly to prevent fermentation. A far-infrared drying method is desirable as a method for rapid drying.
And in order to shorten the drying time in far-infrared heating, the difference between the far-infrared and the leaf surface temperature must be made as large as possible. However, if the leaves are frozen, when they are heated, they are deteriorated by stress and discolored to purple, so they cannot be frozen.
Therefore, in the present invention, the heat-drying treatment is started by irradiating far-infrared rays with the far-infrared rays while heating them at 0-60 ° C, preferably 0-40 ° C, more preferably 5-15 ° C. Until completion, the leaf surface temperature is kept at 60 ° C. or lower, preferably 50 ° C. or lower, more preferably 40 ° C. or lower, and heat is absorbed quickly.
In addition, the method for blowing air at the predetermined temperature is not particularly limited. For example, the outside air may be simply blown, or the air may be blown by using an electric device. Preferably, By using liquid nitrogen for air blowing, air blowing at 0 to 40 ° C., preferably 0 to 20 ° C., can be performed efficiently.
 杜仲生葉は、カットしてから葉中水分量が乾燥前水分量の3%以下になるまで加熱乾燥してもよいし、あるいは、予め裁断することなく適採したそのままの形状の社仲生葉を葉中水分量が乾燥前水分量の3%以下になるまで乾燥してからカットしても良い。
 杜仲生葉をカットする際には、葉にストレスを与えないように鋭利に裁断し、葉脈を2cm以下の四角形さらに1cmの四角形又は葉脈に直角方向に2cm以下さらに1cm以下の短冊形に切断しなければならない。
杜 Nakasei leaves may be heat-dried after cutting until the moisture content in the leaves is 3% or less of the moisture content before drying. It may be cut after drying until the moisture content in the leaf is 3% or less of the moisture content before drying.
カ ッ ト When cutting Nakasei leaves, they must be cut sharply so as not to stress the leaves, and the veins should be cut into squares of 2 cm or less, 1 cm squares, or rectangular shapes of 2 cm or less and 1 cm or less in a direction perpendicular to the veins. I must.
 本発明における上記加熱乾燥は、送風装置及び空調設備のついている遠赤外線加熱機を用いて行われるが、乾燥を早めるために、設定温度を200~600℃、好ましくは0~500℃、さらに好ましくは300~400℃で、乾燥する。
 また、本発明において、遠赤外線加熱機は、コンベア式のものでも、或いは多段式のものでもよく、照射される遠赤外線の波長は、例えば、1~1000μm、好ましくは2.5~50μmの範囲から適宜選択することができる。
The heat drying in the present invention is performed using a far infrared heater equipped with a blower and an air conditioner. In order to accelerate the drying, the set temperature is 200 to 600 ° C., preferably 0 to 500 ° C., more preferably. Is dried at 300-400 ° C.
In the present invention, the far-infrared heater may be a conveyor type or a multi-stage type, and the wavelength of the far infrared ray to be irradiated is, for example, in the range of 1 to 1000 μm, preferably 2.5 to 50 μm. Can be appropriately selected.
 また、本発明の製造方法においては、遠赤外線による加熱乾燥処理を行なう際、杜仲生葉の葉同士が互いに接触しないように略均等に並べ、並べた葉の状態を維持した状態で、遠赤外線を照射することが好ましい。例えば、杜仲生葉をロータリー式乾燥炉の回転ドラム等に入れ、葉を回転させた状態で加熱乾燥すると、杜仲葉とドラムあるいは葉同士の接触により歪みや圧力を生じてしまうため、自己消化作用により杜仲葉の変色が生じ易くなる。また、遠赤外線照射部と葉との距離が一定でないため、加熱ムラが生じたり、あるいは葉から蒸散した水蒸気によって葉周辺の湿度が上昇し、蒸気による有用成分の溶出を生じてしまう場合がある。これに対して、杜仲生葉の葉同士が互いに接触しないように略均等に並へ、並べた葉の状態を維持した状態で、遠赤外線を照射することによって、葉同士あるいは葉と装置の接触等によるストレスを生じず、ほとんどストレスのない状態で、速やかに葉中の水分を除去することができるため、鮮やかな緑色を有しつつ、有用成分を高濃度で含有する杜仲葉緑色乾燥品が得られる。また、葉同士が互いに接触しない状態であれば、例えば、上下三段の乾燥棚に並べた状態で、遠赤外線を照射しても構わない。 In addition, in the production method of the present invention, when performing the heat drying treatment with far infrared rays, the leaves are arranged substantially evenly so that the leaves are not in contact with each other, and the far infrared rays are maintained in a state where the arranged leaves are maintained. Irradiation is preferred. For example, if you put a cocoon leaf in a rotary drum of a rotary drying furnace and heat and dry it with the leaf rotated, distortion or pressure will occur due to contact between the nakanaka leaf and the drum or between the leaves. Discoloration of 杜 中葉 tends to occur. In addition, since the distance between the far-infrared irradiation part and the leaf is not constant, uneven heating may occur, or the moisture around the leaf may increase due to water vapor evaporated from the leaf, and elution of useful components due to the vapor may occur. . On the other hand, the leaves or the leaves and the device contact each other by irradiating far-infrared rays while maintaining the state of the arranged leaves in a substantially uniform manner so that the leaves do not touch each other. The water in the leaves can be quickly removed in a state where there is almost no stress due to the occurrence of stress due to, and a green dried green product that contains vivid green and contains useful components at a high concentration is obtained. It is done. Moreover, as long as the leaves are not in contact with each other, for example, far infrared rays may be irradiated in a state where the leaves are arranged on three upper and lower drying shelves.
 また、本発明の製造方法において、遠赤外線による加熱乾燥処理は、少なくとも杜仲葉の水分量が乾燥前水分量の3%以下になるまで行なう。ここで、乾燥前水分量とは、遠赤外線による加熱乾燥処理に供する直前の杜仲葉に含まれる水分量を意味する。すなわち、本発明の製造方法においては、例えば、加熱乾燥処理に供する前の杜仲葉に含まれる水分量が100gであった場合に、葉中に残存する水分量が3g以下になるまで、遠赤外線による加熱乾燥処理を行なう。
 本発明の製造方法においては、速やかに葉中の水分量を乾燥前水分量の3%以下まで減少させることによって、酵素反応及び自己消化作用の進行が顕著に妨げられる。
In the production method of the present invention, the heat drying treatment with far-infrared rays is performed until at least the moisture content of the Tochu Naka leaf is 3% or less of the moisture content before drying. Here, the moisture content before drying means the moisture content contained in the Tochu-nakaba immediately before being subjected to the heat drying treatment by far infrared rays. That is, in the production method of the present invention, for example, when the amount of water contained in the bamboo leaf before being subjected to the heat-drying treatment is 100 g, the far-infrared rays until the amount of water remaining in the leaves becomes 3 g or less. The heat drying process by is performed.
In the production method of the present invention, the progress of the enzymatic reaction and the self-digestion action is significantly hindered by quickly reducing the water content in the leaves to 3% or less of the water content before drying.
 なお、加熱乾燥処理工程において、葉中の水分の除去速度が遅くなると、水分除去に要する時間に応じて自己消化反応が徐々に進行し、杜仲葉の変色及びイリドイド類の減少を招くことになる。このため、例えば、葉中水分量を乾燥前水分量の3%以下まで減少するのに30分を超える時間を要すると、杜仲葉が変色を生じたり、有用成分が著しく減少してしまう場合がある。したがって、酵素反応及び自己消化作用をより確実に停止するためには、より速やかに葉中水分を除去することが望ましく、好ましくは20分以内、より好ましくは10分以内に、葉中水分量を乾燥前水分量の3%以下まで乾燥することが望ましい。 In addition, in the heat drying treatment process, when the water removal rate in the leaves is slow, the self-digestion reaction gradually proceeds according to the time required for the water removal, leading to discoloration of chunaka leaves and reduction of iridoids. . For this reason, for example, if it takes more than 30 minutes to reduce the moisture content in the leaf to 3% or less of the moisture content before drying, the color of the Nakanaka leaf may change or the useful components may be significantly reduced. is there. Therefore, in order to stop the enzyme reaction and autolysis more reliably, it is desirable to remove the moisture in the leaf more quickly, preferably within 20 minutes, more preferably within 10 minutes. It is desirable to dry to 3% or less of the moisture content before drying.
 また、赤外線による加熱乾燥処理において、加熱処理の開始から終了まで、湿度30%以下、より好ましくは10%以下の雰囲気下にて乾燥処理を行なうことが望ましい。なお、通常の場合、加熱乾燥処理においては、葉表面からの水分の蒸発が起こるため、乾燥の進行とともに雰囲気湿度が上昇する。しかしながら、遠赤外線による加熱乾燥処理中に雰囲気湿度が10%を超えると、葉表面からの水分の気化が進みにくくなり、短時間で葉中の水分を除去することが難しくなる。例えば、密閉式の乾燥機を用いた場合、葉中水分の気化によって、雰囲気湿度が著しく上昇する。また、さらに湿度が上昇して水蒸気が飽和すると、気化熱が生じなくなって不必要に葉温が上昇してしまったり、あるいは蒸気中への有用成分の流失が生じる恐れもある。なお、加熱乾燥処理工程中の湿度を30%以下に維持するためには、送風手段によって適宜調整すればよい。 Further, in the heat drying process using infrared rays, it is desirable to perform the drying process in an atmosphere with a humidity of 30% or less, more preferably 10% or less, from the start to the end of the heat treatment. In a normal case, in the heat drying process, moisture evaporates from the leaf surface, so that the atmospheric humidity increases with the progress of drying. However, if the atmospheric humidity exceeds 10% during the heat-drying process using far infrared rays, it is difficult to evaporate moisture from the leaf surface, and it becomes difficult to remove moisture in the leaf in a short time. For example, when a hermetic dryer is used, the atmospheric humidity significantly increases due to the evaporation of moisture in the leaves. Further, when the humidity is further increased and the water vapor is saturated, the heat of vaporization is not generated and the leaf temperature is unnecessarily increased, or the useful component may be lost to the steam. In addition, what is necessary is just to adjust suitably with a ventilation means, in order to maintain the humidity in a heat drying process process at 30% or less.
 また、遠赤外線による加熱乾燥処理において、赤外線非接触温度計により計測した葉の最高温度が60℃以下、より好ましくは50以下の範囲となるように、送風手段を適宜制御することが望ましい。 Further, in the heat drying treatment with far infrared rays, it is desirable to appropriately control the blowing means so that the maximum leaf temperature measured by the infrared non-contact thermometer is 60 ° C. or less, more preferably 50 or less.
 図1に、本発明の製造方法における遠赤外線による加熱乾燥処理工程の一実施例を示すが、本発明はこれに限定されるものではない。
 コンベア式の遠赤外線加熱乾燥装置10は、乾燥室12の内部に、遠赤外線照射部14及び送風部16が設けられている。また、コンベア18は、一方から乾燥室12を通過して他方全と連続して移動可能なように設けられている。
Although one Example of the heat drying process process by the far infrared rays in the manufacturing method of this invention is shown in FIG. 1, this invention is not limited to this.
The conveyor-type far-infrared heating and drying apparatus 10 is provided with a far-infrared irradiation unit 14 and a blower 16 inside a drying chamber 12. Moreover, the conveyor 18 is provided so that it can move from the one side through the drying chamber 12 and continuously with the other side.
 遠赤外線による加熱乾燥処理工程に供する杜仲生葉20は、コンベア18上に葉同士が互いに接触しないように略均等の間隔に並べられる。そして、コンベア18上に並べられた杜仲生葉20は、並べられた葉の状態を維持しつつ乾燥室12内部へと送られる。乾燥室12内部では、遠赤外線照射部14により、上下方向から、杜仲生葉20へと遠赤外線が照射される。そして、遠赤外線が照射された杜仲生葉20は、葉温が上昇して水分が気化し、水分量が減少する。ここで、乾燥室12内は、送風部16により送風されることによって、室内の雰囲気湿度及び雰囲気温度がほぼ一定に保たれる。すなわち、通常の場合、加熱により葉中の水分が気化して水蒸気になることで、乾燥室12内の湿度及び温度は上昇するが、送風部16により送風することで水蒸気が外部へと排出され、乾燥室12内の湿度及び温度がほぼ一定に保たれる。乾燥室12内で乾燥された杜仲生葉20は、コンベア18により、乾燥室12の外部へと送られる。なお、本発明の製造方法においては、杜仲生葉20は、遠赤外線の照射開始後30分以内に葉の水分量が乾燥前水分量の3%以下まで減少している。 杜 Nakasei leaves 20 to be subjected to a heat drying process using far infrared rays are arranged on the conveyor 18 at substantially equal intervals so that the leaves do not contact each other. Then, the green leaves 20 arranged on the conveyor 18 are sent into the drying chamber 12 while maintaining the state of the arranged leaves. Inside the drying chamber 12, far-infrared rays are radiated from the up-and-down direction to the cocoon leaves 20 by the far-infrared ray irradiation unit 14. Then, the foliage leaves 20 irradiated with far-infrared rays have a leaf temperature that rises, moisture is vaporized, and the amount of moisture decreases. Here, the inside of the drying chamber 12 is blown by the blower 16 so that the atmospheric humidity and the atmospheric temperature in the room are kept almost constant. That is, in normal cases, the moisture in the leaves is vaporized by heating to become water vapor, so that the humidity and temperature in the drying chamber 12 are increased. However, the water is exhausted to the outside by being blown by the blower unit 16. The humidity and temperature in the drying chamber 12 are kept almost constant. The dried green leaves 20 dried in the drying chamber 12 are sent to the outside of the drying chamber 12 by the conveyor 18. In addition, in the manufacturing method of this invention, the water | moisture content of the foliage leaf 20 has decreased to 3% or less of the water content before drying within 30 minutes after the start of far-infrared irradiation.
 ここで、乾燥室12内において、室内の雰囲気湿度、雰囲気温度、及び葉表面の温度が以上に示した好適な数値範囲内となるように、遠赤外線照射部14による遠赤外線の照射強度、及び送風部16による送風温度及び送風量を調節することが望ましい。すなわち、図1の遠赤外線加熱乾燥装置10を使用して、遠赤外線照射部14及び送風部16の運転条件を調整し、乾燥室12内の雰囲気温度、雰囲気湿度、及び葉表面の温度等を適切に制御することによって、加熱開始後30分以内に葉の水分量が乾燥前水分量の3%以下になるまで乾燥される。さらに、杜仲生葉20同士が互いに接触しないように略均等の間隔に並べられている場合には、遠赤外線の照射によって葉が均一に効率よく加熱されるとともに、乾燥工程中に葉同士あるいは葉と装置の接触による歪みや圧力も生じず、葉にほとんどストレスがかからないため、乾燥工程中での変色も生じにくい。なお、酵素反応及び自己消化作用が進行するためには、葉中の水分として自由水が含まれている必要があると考えられ、葉中水分量が乾燥前水分量の3%以下になるまで乾燥した杜仲葉においては、葉中に含まれる自由水のほぼ全量が除去されているため、変色あるいは有用成分の減少はほとんど生じない。 Here, in the drying chamber 12, the far-infrared irradiation intensity by the far-infrared irradiation unit 14 so that the indoor atmospheric humidity, the atmospheric temperature, and the leaf surface temperature are within the preferable numerical ranges shown above, and It is desirable to adjust the blowing temperature and the blowing amount by the blowing unit 16. That is, using the far-infrared heating and drying apparatus 10 of FIG. 1, the operating conditions of the far-infrared irradiation unit 14 and the blower unit 16 are adjusted, and the atmospheric temperature, atmospheric humidity, leaf surface temperature, etc. in the drying chamber 12 are adjusted. By appropriate control, the leaves are dried until the moisture content of the leaves becomes 3% or less of the moisture content before drying within 30 minutes after the start of heating. Furthermore, when the leaves are arranged at substantially equal intervals so as not to contact each other, the leaves are heated uniformly and efficiently by irradiation with far infrared rays, and the leaves or leaves There is no distortion or pressure due to the contact of the apparatus, and the leaves are hardly stressed, so discoloration is unlikely to occur during the drying process. In order for the enzymatic reaction and self-digestion to proceed, it is considered that free water must be included as the moisture in the leaves, and until the moisture content in the leaves becomes 3% or less of the moisture content before drying. In dried Tochu leaves, almost all of the free water contained in the leaves has been removed, so there is almost no discoloration or decrease in useful components.
 また、本発明の製造方法においては、摘採後の杜仲生葉を製品とするまでの間、杜仲葉を湿度50%以下、より好ましくは湿度30%以下の条件下に保持することが望ましい。社仲葉が、湿度50%を超える高湿度下に置かれることで、イリドイド類、ポリフェノール類等の高機能成分の減少を生じる場合があり、加えて、葉が紫色に変色して、緑色の製品が得られない場合がある。 Also, in the production method of the present invention, it is desirable to keep the chunaka leaf under the condition of humidity of 50% or less, more preferably 30% or less, until the pickled chunaka leaf is made into a product. If Nakanakayo is placed under high humidity exceeding 50% humidity, it may cause a decrease in high-functional components such as iridoids and polyphenols. In addition, the leaves turn purple and green The product may not be obtained.
 また、上記乾燥処理工程においては、予め細かく裁断した杜仲生葉を用いることによって、急速に乾燥を進めることができるものの、裁断箇所から自己消化作用が進行し、イリドイド類の有用成分が分解してしまうとともに、変色により鮮やかな緑色が得られなくなる場合がある。このため、本発明の製造方法においては、適採した杜仲生葉を、できるだけそのままの形状で乾燥させることが望ましい。一方で、細かく裁断せずに杜仲生葉そのままの形状で乾燥すると、従来の乾燥方法では、特に葉脈を完全に乾燥させるために非常に長時間を要するものの、本発明の製造方法では、杜仲生葉そのままの形状であっても、速やかに葉脈中の水分を除去することができる。 Moreover, in the said drying process, although it can accelerate | stimulate rapidly by using the pre-cut finely-leaved green leaves, a self-digestion action advances from a cutting location and the useful component of iridoids will decompose | disassemble. At the same time, a vivid green color may not be obtained due to discoloration. For this reason, in the production method of the present invention, it is desirable to dry the appropriately picked potato leaves in the shape as possible. On the other hand, when dried in the shape as it is without chopping finely, it takes a very long time to completely dry the veins with the conventional drying method. Even if it is the shape of this, the water | moisture content in a leaf vein can be removed rapidly.
 なお、杜仲の葉は30cm以上にも成長し、葉脈は5mm以上の太さにまでなる。このように大きな杜仲生葉の場合、乾燥工程において葉脈部分と葉脈以外の部分との間で水分の蒸発に差が生じ、自己消化作用による葉脈の紫色化が進行する。これは、葉脈周辺では構造にストレスがかかり、葉脈の細胞が十分に水分を含有した状態で破壊されることによるものと考えられる。これにより、イリドイド等の有用成分が分解して含有量が減少し、加えて変色により緑色の精彩さも失われてしまう。また、特に葉脈には高機能性成分が多く含まれているため、葉脈の乾燥は極めて重要である。しかしながら、従来の乾燥方法では、5mm以上の太さになる葉脈部分を速やかに乾燥することは非常に困難である。このため、本発明の製造方法においては、杜仲葉を葉脈とその両側の部分との三片に裁断し、それぞれの片について乾燥処理することが望ましい。すなわち、杜仲葉の葉脈部分とその他の部分とに分けて、加熱温度や処理時間を変える等、それぞれに応じた乾燥処理を行なうことで、自己消化作用による変色や過度の加熱により生じる熱分解等、高機能成分の損失を低く抑えることができる。また、葉脈部分とその他の部分とでは含まれる成分の種類及び量が異なつており、例えば、葉脈部分にはゲニポシド酸が多く含まれ、他の部分にはクロロゲン酸が多く含まれている。したがつて、所望とする有効成分の種類に応じて、葉脈部分に由来する製品と他の部分に由来する製品とを分けることも可能である。 In addition, the leaves of Tochu are grown to 30 cm or more, and the veins are 5 mm or more in thickness. In the case of such a large cocoon leaf, a difference in water evaporation occurs between the vein portion and the portion other than the leaf vein in the drying process, and the leaf vein becomes purple due to self-digestion. This is considered to be due to the structure being stressed around the veins and the cells of the veins being destroyed in a state sufficiently containing water. As a result, useful components such as iridoids are decomposed to reduce the content, and in addition, the green color is lost due to discoloration. In particular, since the veins contain a lot of highly functional components, the drying of the veins is extremely important. However, with the conventional drying method, it is very difficult to quickly dry a vein portion having a thickness of 5 mm or more. For this reason, in the production method of the present invention, it is desirable to cut the bamboo leaf into three pieces of the vein and the portions on both sides thereof, and dry each piece. In other words, it is divided into the leaf vein part and other parts of Tochu Naka leaf, changing the heating temperature and treatment time, etc., and performing the drying treatment according to each, discoloration due to self-digestion action, thermal decomposition caused by excessive heating, etc. The loss of high-functional components can be kept low. In addition, the types and amounts of components contained in the vein portion and other portions are different. For example, the vein portion contains a large amount of geniposide acid and the other portions contain a large amount of chlorogenic acid. Therefore, it is possible to separate a product derived from the vein portion and a product derived from another portion according to the desired type of active ingredient.
 このため、本発明の製造方法においては、例えば、予め裁断することなく適採したそのままの形状の杜仲生葉を、葉の水分量を乾燥前水分量の3%以下になるまで遠赤外線によって加熱乾燥するか、あるいは、摘採後の社仲生葉を、葉脈とその両側の部分との二片に裁断した状態で、乾燥前水分量の水分量3%以下になるまで遠赤外線によって加熱乾燥することが可能である。 For this reason, in the production method of the present invention, for example, the freshly-cured Toka Nakasei leaves, which have been appropriately collected without cutting in advance, are heat-dried with far-infrared rays until the water content of the leaves becomes 3% or less of the water content before drying. Or, after the pruned leaves of the shrunken leaves are cut into two pieces, the vein and the parts on both sides of the leaves, they can be heated and dried with far infrared rays until the moisture content is 3% or less of the moisture content before drying. Is possible.
 以上のようにして得られる杜仲葉緑色乾燥品においては、特に乾燥処理工程中におけるゲニポシド酸、イリドイド類、ポリフェノール類といった高機能性分の減少が低く抑えられるため、これらゲニポシド酸、イリドイド類、及びポリフェノール類の含有量が飛躍的に向上している。 In the dried green rice leaf product obtained as described above, since the reduction of highly functional components such as geniposide acid, iridoids, polyphenols during the drying process is suppressed to a low level, these geniposide acids, iridoids, and The content of polyphenols has been dramatically improved.
 杜仲葉中に含まれるイリドイド類及びポリフェノール類の含有量は、杜仲本の個体差、収穫時期等によって異なるが、本発明により得られた杜仲葉緑色乾燥品においては、イリドイド類の含有量が、原料として使用する収穫直後の社仲生葉に含まれているイリドイド類の含有量(乾燥質量換算)の約70質量%以上を維持していると考えられる。 The content of iridoids and polyphenols contained in the Tochu Naka leaf varies depending on individual differences in Tochu Nakamoto, harvest time, etc., but in the dried green product of Tochu Naka leaf obtained by the present invention, the content of the iridoids, It is considered that about 70% by mass or more of the content (in terms of dry mass) of iridoids contained in the company Nakasei leaves immediately after harvest used as a raw material is maintained.
 また、本発明の製造方法により得られる杜仲葉緑色乾燥品は、イリドイド類及びポリフェノール化合物が高濃度で含有しているため、一旦杜仲葉乾燥品として処理した後、これらの高機能成分を抽出する抽出方法としても有用である。 Moreover, since the dried green leaves of the Nakanaka leaf obtained by the production method of the present invention contain high concentrations of iridoids and polyphenol compounds, these highly functional components are extracted after being once treated as a dried Nakanaka leaf product. It is also useful as an extraction method.
 また、乾燥処理後の杜仲葉緑色乾燥品は、平均径3~14μmに微粉砕した粉末とすることが好ましい。微粉砕の方法は、特に制限されないが、例えば、ジェットミル式粉砕機、気流式粉砕機等を用いることができ、この場合においても、粉砕時の温度を0~70℃以下、好ましくは0~40℃以下、さらに好ましくは0~20℃以下で粉砕することが好ましい。さらには、粉砕時に、0~70℃以下の送風を行うことにより、通風を良くして、熱及び湿度をこもらせないことが好ましく、特に、送風に、液体窒素を使用するなどにより、0~40℃、好ましくは0~20℃の冷風を送風しつつ粉砕を行うことが好ましい。
 そして、こうしてできた緑色の杜仲の粉末は、さわやかな緑の美しい強い甘さを持つ、癖のない3~14μm、好ましく平均6μmの微粉末になり、飲用に適するばかりでなく、杜仲特有のゲニポシド酸、クロロゲンサン、アスペルロシドなどや葉酸、ビタミンE、ビタミンAを多く含む健康食品を提供することができる。
Further, the dried dried green leaves of dried Nakanaka leaves are preferably made into a finely pulverized powder having an average diameter of 3 to 14 μm. The pulverization method is not particularly limited, and for example, a jet mill pulverizer, an airflow pulverizer, or the like can be used. In this case, the pulverization temperature is 0 to 70 ° C. or less, preferably 0 to It is preferable to grind at 40 ° C. or lower, more preferably 0 to 20 ° C. or lower. Furthermore, it is preferable to improve ventilation and prevent heat and humidity from being stored by blowing air at 0 to 70 ° C. during pulverization. In particular, by using liquid nitrogen for blowing, It is preferable to perform pulverization while blowing cold air of 40 ° C., preferably 0 to 20 ° C.
And the green powder of green liquor made in this way becomes a fine powder of 3-14μm, preferably 6μm on average, with a refreshing green and beautiful sweetness, which is not only suitable for drinking but also geniposide peculiar to liquor A health food containing a large amount of acid, chlorogenic sun, asperroside, folic acid, vitamin E, and vitamin A can be provided.
 以下、実施例の記載に基づいて、本発明をさらに詳しく説明するが、本発明はこれら実施例に限定されるものではない。
 (実施例1)
 未裁断の杜仲生葉を、送風機付きの遠赤外線コンベア式乾燥機に、葉が互いに接触しないよう均等に並べ、設定温度350℃で、25℃の送風をしながら、12分30秒間乾燥した。
 乾燥処理中の葉表面の最高温度(赤外線非接触温度計により計測)は約46.5℃であり、乾燥後の水分量は、乾燥前の水分量の3%であった。
 得られた乾燥葉を、サイクロンミルを用い、10~20分間粉砕し、平均7μmの緑色乾燥微粉末を得た。
Hereinafter, the present invention will be described in more detail based on the description of Examples, but the present invention is not limited to these Examples.
Example 1
Uncut cocoon leaves were arranged evenly on a far-infrared conveyor dryer equipped with a blower so that the leaves would not touch each other, and dried for 12 minutes and 30 seconds at a set temperature of 350 ° C. while blowing air at 25 ° C.
The maximum temperature of the leaf surface during the drying treatment (measured with an infrared non-contact thermometer) was about 46.5 ° C., and the moisture content after drying was 3% of the moisture content before drying.
The obtained dried leaves were pulverized for 10 to 20 minutes using a cyclone mill to obtain a green dry fine powder having an average of 7 μm.
 (実施例2)
 20℃の送風とした以外は、実施例1と同様にして13分30秒間乾燥した。
 乾燥処理中の葉表面の最高温度は約37.0℃であり、乾燥後の水分量は、乾燥前の水分量の3%であった。
 得られた乾燥葉から、実施例1と同様にして平均7μmの緑色乾燥微粉末を得た。
(Example 2)
It dried for 13 minutes and 30 seconds like Example 1 except having set it as 20 degreeC ventilation.
The maximum temperature of the leaf surface during the drying treatment was about 37.0 ° C., and the moisture content after drying was 3% of the moisture content before drying.
From the obtained dried leaves, a green dry fine powder having an average of 7 μm was obtained in the same manner as in Example 1.
 (実施例3)
 設定温度を400℃にし、送風に、液体窒素を使用して5℃の冷風を送風とした以外は、実施例1と同様にして10分間乾燥した。
 乾燥処理中の葉表面の最高温度は約15.0℃であり、乾燥後の水分量は、乾燥前の水分量の3%であった。
 得られた乾燥葉から、サイクロンミルを用い、液体窒素を用いて5℃とした冷風を送り込みながら粉砕をおこなって平均6μmの緑色乾燥微粉末を得た。
(Example 3)
Drying was carried out for 10 minutes in the same manner as in Example 1 except that the set temperature was 400 ° C. and liquid nitrogen was used for blowing air and 5 ° C. cold air was used for blowing air.
The maximum temperature of the leaf surface during the drying treatment was about 15.0 ° C., and the moisture content after drying was 3% of the moisture content before drying.
The resulting dried leaves were pulverized using a cyclone mill while feeding cold air at 5 ° C. using liquid nitrogen to obtain a green dry fine powder having an average of 6 μm.
 (比較例1)
 実施例1の装置を用い、設定温度を170℃にし、送風をすることなく、10分間乾燥した。
 乾燥処理中の葉表面の最高温度は約70℃であり、乾燥後の水分量は、乾燥前の水分量の47.3%であった。棚乾燥機を60℃に設定し30分間乾燥した。
 得られた乾燥葉から、実施例1と同様にして平均7μmの緑色乾燥微粉末を得た。
(Comparative Example 1)
Using the apparatus of Example 1, the set temperature was set to 170 ° C. and dried for 10 minutes without blowing.
The maximum temperature of the leaf surface during the drying treatment was about 70 ° C., and the moisture content after drying was 47.3% of the moisture content before drying. The shelf dryer was set to 60 ° C. and dried for 30 minutes.
From the obtained dried leaves, a green dry fine powder having an average of 7 μm was obtained in the same manner as in Example 1.
 (比較例2)
 実施例1の装置を用い、設定温度を230℃にし、送風をすることなく、15分間乾燥した。
 乾燥処理中の葉表面の最高温度は約110℃であり、乾燥後の水分量は、乾燥前の水分量の3%であったが一部焦げた。しかし茎は乾燥できなかった。
 得られた乾燥葉から、実施例1と同様にして平均7μmの緑色乾燥微粉末を得た。
(Comparative Example 2)
Using the apparatus of Example 1, the set temperature was set to 230 ° C., and drying was performed for 15 minutes without blowing.
The maximum temperature of the leaf surface during the drying treatment was about 110 ° C., and the moisture content after drying was 3% of the moisture content before drying, but it was partially burnt. However, the stem could not be dried.
From the obtained dried leaves, a green dry fine powder having an average of 7 μm was obtained in the same manner as in Example 1.
 (比較例3)
 設定温度を140℃にし、120℃の送風とした以外は、実施例1と同様にして20分間乾燥した。
 乾燥処理中の葉表面の最高温度は約130℃であり、乾燥後の水分量は、乾燥前の水分量の3%であった。
 得られた乾燥葉から、実施例1と同様にして平均7μmの緑色乾燥微粉末を得た。
(Comparative Example 3)
Drying was carried out for 20 minutes in the same manner as in Example 1 except that the set temperature was 140 ° C. and the ventilation was 120 ° C.
The maximum temperature of the leaf surface during the drying treatment was about 130 ° C., and the moisture content after drying was 3% of the moisture content before drying.
From the obtained dried leaves, a green dry fine powder having an average of 7 μm was obtained in the same manner as in Example 1.
 実施例1~3及び比較例1~3で得られた乾燥粉末について、色、味、及び成分分析の結果を表1に示す。なお、成分分析は、HPLC(高速液体クロマト;メタノール抽出)により測定した。単位は、いずれもμg/g(有効成分量/サンプル質量)である。 Table 1 shows the results of color, taste, and component analysis of the dry powders obtained in Examples 1 to 3 and Comparative Examples 1 to 3. In addition, the component analysis was measured by HPLC (high performance liquid chromatography; methanol extraction). All units are μg / g (active ingredient amount / sample mass).
Figure JPOXMLDOC01-appb-T000001
Figure JPOXMLDOC01-appb-T000001
 上記表に示されるように、加熱乾燥処理の開始から終了まで、杜仲生葉に0~60℃の送風を行いつつ遠赤外線を照射することにより、葉の表面温度を60℃以下に保ち、加熱開始後30分以内に葉中水分量が乾燥前水分量の3%以下になるまで葉中水分を速やかに乾燥除去して得られた実施例1~3の杜仲茶葉緑色乾燥品は、アスペルロシド、ゲニポシド酸といったイリドイド類を非常に多く含有していることがわかる。また、ポリフェノールの一種である、クロロゲン酸についても高い含有量が得られている。
 特に、送風温度を下げるために、液体窒素を用いて5℃の冷風とし、乾燥後の粉砕においても、液体窒素を用いて5℃で行った実施例3の杜仲茶葉緑色乾燥品は、より瑞々しい緑色を示しているうえ、クロロゲン酸、アスペルロシド、及びゲニポシド酸の含有量が実施例1,2で得られた杜仲茶葉緑色乾燥品の場合よりも増加した。
As shown in the above table, the surface temperature of the leaves is kept at 60 ° C. or lower by irradiating far-infrared leaves while blowing air at 0 to 60 ° C. from the start to the end of the heat drying treatment, and heating starts. The green dried products of Tonaka tea leaves of Examples 1 to 3 obtained by quickly drying and removing the moisture in the leaves until the moisture content in the leaves became 3% or less of the moisture content before drying within 30 minutes later were asperoside and geniposide It can be seen that they contain a large amount of iridoids such as acids. Moreover, high content is also obtained about chlorogenic acid which is a kind of polyphenol.
In particular, in order to lower the blast temperature, the green dried product of Example 3 green tea of Example 3 performed at 5 ° C. using liquid nitrogen in the cold air of 5 ° C. using liquid nitrogen and pulverizing after drying is more suitable. In addition to showing a fresh green color, the contents of chlorogenic acid, asperoside and geniposide acid were increased as compared with the green dried green tea leaves obtained in Examples 1 and 2.
 これに対し、送風をせずに、実施例1~3より低い設定温度で同じ時間乾燥して得られた比較例1の杜仲茶葉緑色乾燥品は、癖のない味が得られたが、乾燥が充分でなく、色が紫がかった暗い緑色を呈するものであり、クロロゲン酸、アスペルロシド、ゲニポシド酸の含有量がいずれも低かった。
 また、比較例1よりも設定温度を高くし、乾燥時間を1.5倍にして葉中水分量が乾燥前水分量の3%以下になるまで葉中水分を乾燥除去して得られた比較例2の杜仲茶葉緑色乾燥品は、癖のない味がえられ、色も緑色であったものの、アスペルロシド、及びゲニポシド酸の含有量がいずれも比較例1のものよりもさらに低かった。
 さらに、杜仲生葉に120℃の送風を行いつつ遠赤外線を照射することにより、加熱開始後20分で葉中水分量が乾燥前水分量の3%以下になるまで葉中水分を乾燥除去して得られた比較例3の杜仲茶葉緑色乾燥品は、色はさわやかな緑色であったが、苦みを持つ味であり、クロロゲン酸、アスペルロシド、及びゲニポシド酸の含有量がいずれも非常に低かった。
On the other hand, the dried green tea leaves of comparative example 1 obtained by drying for the same time at a set temperature lower than those of Examples 1 to 3 without blowing air gave a taste free of wrinkles, but were dried. However, the color was purple and dark green, and the contents of chlorogenic acid, asperoside and geniposide acid were all low.
In addition, comparison was obtained by setting the temperature higher than that of Comparative Example 1 and drying and removing the moisture in the leaf until the drying time was 1.5 times and the moisture content in the leaf was 3% or less of the moisture content before drying. The dried green tea leaf green product of Example 2 had a savory taste and a green color, but the contents of asperoside and geniposide acid were both lower than those of Comparative Example 1.
Furthermore, by irradiating far-infrared leaves while blowing air at 120 ° C., the moisture in the leaves is removed by drying until the moisture content in the leaves becomes 3% or less of the moisture content before drying 20 minutes after the start of heating. The obtained green dried green tea leaves of Comparative Example 3 had a refreshing green color, but had a bitter taste and had very low contents of chlorogenic acid, asperloside, and geniposide acid.
 10:遠赤外線加熱乾燥装置
 12:乾燥室
 14:遠赤外線照射部
 16:送風部
 18:コンベア
 20:杜仲生葉
10: Far-infrared heating and drying device 12: Drying room 14: Far-infrared irradiation unit 16: Blowing unit 18: Conveyor 20: Tokinakaseiyo

Claims (11)

  1.  杜仲生葉を遠赤外線照射により加熱乾燥する方法において、加熱乾燥処理の開始から終了まで、杜仲生葉に0~60℃の送風を行いつつ遠赤外線を照射することにより、加熱開始後30分以内に葉中水分量が乾燥前水分量の3%以下になるまで加熱乾燥することを特徴とする杜仲葉緑色乾燥品の製造方法。 In the method of heating and drying cocoon leaves by far-infrared irradiation, the leaves are irradiated within 30 minutes after the start of heating by irradiating far-infrared leaves while blowing air at 0 to 60 ° C. from the start to the end of the heat drying process. A method for producing a dried dried green leafy green product, characterized in that the medium moisture content is heated and dried until it reaches 3% or less of the moisture content before drying.
  2.  前記送風に、液体窒素を用いることを特徴とする請求項1に記載の杜仲葉緑色乾燥品の製造方法。 2. The method for producing a green dried green leaf product according to claim 1, wherein liquid nitrogen is used for the blowing.
  3.  前記加熱処理の開始から終了まで、遠赤外線加熱乾燥装置の設定温度を200~600℃で加熱乾燥することを特徴とする請求項1又は2に記載の杜仲葉緑色乾燥品の製造方法。 The method for producing a dried green product of Tonaka green according to claim 1 or 2, wherein the far-infrared heat drying apparatus is heated and dried at a set temperature of 200 to 600 ° C from the start to the end of the heat treatment.
  4.  加熱乾燥処理の開始から終了まで、赤外線非接触温度計により測定した葉の表面温度が60℃以下となる範囲で加熱乾燥することを特徴とする請求項1~3のいずれか1項に記載の杜仲葉緑色乾燥品の製造方法。 4. From the start to the end of the heat drying treatment, heat drying is performed in a range in which the leaf surface temperature measured by an infrared non-contact thermometer is 60 ° C. or less. A method for producing dried green leaves.
  5.  加熱乾燥処理の開始から終了まで、湿度30%以下の雰囲気下にて加熱乾燥することを特徴とする請求項1~4のいずれか1項に記載の杜仲葉緑色乾燥品の製造方法。 The method for producing a dried dried green leaf product according to any one of claims 1 to 4, wherein the drying is performed in an atmosphere having a humidity of 30% or less from the start to the end of the heat drying treatment.
  6.  杜仲生葉を、葉同士が互いに接触しないように略均等の間隔に並べ、並べた葉の状態を維持しつつ加熱乾燥することを特徴とする請求項1~5のいずれか1項に記載の杜仲葉緑色乾燥品の製造方法。 6. The rice cake according to any one of claims 1 to 5, wherein the leaves are arranged at substantially equal intervals so that the leaves do not contact each other and are dried by heating while maintaining the state of the arranged leaves. A method for producing a dry green leaf product.
  7.  前記杜仲葉は、予め裁断することなく適採したそのままの形状の社仲生葉である、請求項1~6のいずれかに記載の杜仲葉緑色乾燥品の製造方法。 The method for producing a dried green product of Tochu Nakaba according to any one of Claims 1 to 6, wherein said Tochu Nakaba is a company Nakasei leaf that has been appropriately shaped without being cut in advance.
  8.  前記杜仲葉は、摘採後、葉脈とその両側の部分との三片に裁断した状態である、請求項1~6のいずれかに記載の杜仲葉緑色乾燥品の製造方法。 The method for producing a green dried green leaf product according to any one of claims 1 to 6, wherein after the plucking, the green leaf is cut into three pieces of a vein and portions on both sides thereof.
  9.  請求項1~8のいずれか1項に記載の方法で得られた杜仲葉緑色乾燥品を、温度を70以下で粉砕して粉末にする工程を含むことを特徴とする緑色の杜仲の粉末飲料の製造方法。 9. A green green liquor powder drink comprising a step of pulverizing the dried green liquor green product obtained by the method according to any one of claims 1 to 8 at a temperature of 70 or less. Manufacturing method.
  10.  前記粉砕工程において、0~70℃の送風を行うことを特徴とする請求項9に記載の緑色の杜仲の粉末飲料の製造方法。 10. The method for producing a green Tochu powdered beverage according to claim 9, wherein air is blown at 0 to 70 ° C. in the crushing step.
  11.  前記送風に、液体窒素を用いることを特徴とする請求項10に記載の緑色の杜仲の粉末飲料の製造方法。 11. The method for producing a green Tochu powder drink according to claim 10, wherein liquid nitrogen is used for the blowing.
PCT/JP2012/072867 2011-09-07 2012-09-07 Method for producing green and dried eucommia leaf product WO2013035832A1 (en)

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