KR20150115254A - Method for preparing concentration powder of Cervi Cornus colla - Google Patents

Method for preparing concentration powder of Cervi Cornus colla Download PDF

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KR20150115254A
KR20150115254A KR1020140039966A KR20140039966A KR20150115254A KR 20150115254 A KR20150115254 A KR 20150115254A KR 1020140039966 A KR1020140039966 A KR 1020140039966A KR 20140039966 A KR20140039966 A KR 20140039966A KR 20150115254 A KR20150115254 A KR 20150115254A
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water
concentrate
antler
hours
active ingredient
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KR1020140039966A
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Korean (ko)
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조진숙
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농업회사법인 우성제약 주식회사
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Publication of KR20150115254A publication Critical patent/KR20150115254A/en

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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
    • 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
    • A23L13/00Meat products; Meat meal; Preparation or treatment thereof
    • A23L13/20Meat products; Meat meal; Preparation or treatment thereof from offal, e.g. rinds, skins, marrow, tripes, feet, ears or snouts
    • 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
    • A23L2/38Other non-alcoholic beverages
    • 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
    • A23L3/00Preservation of foods or foodstuffs, in general, e.g. pasteurising, sterilising, specially adapted for foods or foodstuffs
    • A23L3/40Preservation of foods or foodstuffs, in general, e.g. pasteurising, sterilising, specially adapted for foods or foodstuffs by drying or kilning; Subsequent reconstitution
    • A23L3/44Freeze-drying
    • 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
    • A23L33/00Modifying nutritive qualities of foods; Dietetic products; Preparation or treatment thereof
    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23VINDEXING SCHEME RELATING TO FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES AND LACTIC OR PROPIONIC ACID BACTERIA USED IN FOODSTUFFS OR FOOD PREPARATION
    • A23V2002/00Food compositions, function of food ingredients or processes for food or foodstuffs
    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23VINDEXING SCHEME RELATING TO FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES AND LACTIC OR PROPIONIC ACID BACTERIA USED IN FOODSTUFFS OR FOOD PREPARATION
    • A23V2250/00Food ingredients
    • A23V2250/20Natural extracts
    • A23V2250/204Animal extracts
    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23VINDEXING SCHEME RELATING TO FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES AND LACTIC OR PROPIONIC ACID BACTERIA USED IN FOODSTUFFS OR FOOD PREPARATION
    • A23V2300/00Processes
    • A23V2300/10Drying, dehydrating
    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23VINDEXING SCHEME RELATING TO FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES AND LACTIC OR PROPIONIC ACID BACTERIA USED IN FOODSTUFFS OR FOOD PREPARATION
    • A23V2300/00Processes
    • A23V2300/14Extraction
    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23VINDEXING SCHEME RELATING TO FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES AND LACTIC OR PROPIONIC ACID BACTERIA USED IN FOODSTUFFS OR FOOD PREPARATION
    • A23V2300/00Processes
    • A23V2300/50Concentrating, enriching or enhancing in functional factors

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  • Life Sciences & Earth Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Nutrition Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Food Science & Technology (AREA)
  • Polymers & Plastics (AREA)
  • Mycology (AREA)
  • Medicines Containing Plant Substances (AREA)

Abstract

The present invention relates to a method for manufacturing concentration powder of gelatin of an antler which is made by cutting an antler, boiling the same in water, and concentrating the same. The method comprises the steps of: (1) cutting the antler, putting the same in water, and removing blood or an impurity; (2) putting the antler, gained through the step (1), in water at 80 to 90 °C for 44 to 52 hours, and firstly extracting an active ingredient of the antler; (3) completely removing existing water from the remaining antler after being extracted by the step (2), filling the same with new water, putting the remaining antler at 85 to 90°C for 22 to 26 hours in the new water, and secondly extracting an active ingredient of the antler; (4) completely removing existing water from the remaining antler after being extracted by the step (3), filling the same with new water, putting the remaining antler at 85 to 90°C for 22 to 26 hours in the new water, and thirdly extracting an active ingredient of the antler; (5) filtering a concentrate, gained through the steps (2), (3), and (4), through a filter where particles only lower than or equal to a certain particle size can pass through; (6) vacuum-concentrating the concentrate, gained through the step (5), at 60 to 70°C; (7) cooling the concentrate, gained through the step (6), at room temperature; (8) freezing and drying the concentrate cooled through the step (7); and (9) grinding the concentrate frozen and dried through the step (8).

Description

녹각교 농축분말 제조방법{Method for preparing concentration powder of Cervi Cornus colla}BACKGROUND OF THE INVENTION 1. Field of the Invention [0001] The present invention relates to a method for preparing a cervical colostrum,

본 발명은 녹각교 제조방법에 관한 것으로, 더욱 상세하게는 골질화 되지 않은 어린 뿔이 시간이 지나면서 점차 무기질 성분이 증가 되어 골질화 된 녹각을 절단하여 물에 끓여서 농축하여 만든 녹각교 농축분말 제조방법에 관한 것이다.
More particularly, the present invention relates to a method for manufacturing a raspberry glaze, and more particularly, to a method for manufacturing a raspberry glaze which does not become ossified, ≪ / RTI >

녹각이란 사슴의 뿔이 뼈처럼 단단히 굳어진 것을 말한다. 사슴은 뿔이 나기 시작하면 매년 새로 나오며, 그 뿔이 60 ~ 70일이 지나면 각질화가 시작되고 가을에서 겨울에 걸쳐 뿔에 있는 털이 빠지게 되며, 4 ~ 5월이면 구각이 탈락하고 새로이 뿔이 나서 성장하는데, 이때 골질화 되지 않은 어린뿔을 녹용이라 하며 그냥 두어 점차 무기질 성분이 골질화 된 부분을 녹각이라 하고, 이 녹각을 절단하여 물로 끓여서 농축하여 만든 아교질 덩어리를 녹각교라 한다.It is said that the horn of a deer is hardened like a bone. When the horns begin to appear, the deer grows every year. When the horns are 60 to 70 days old, keratinization starts and the hairs on the horns fall off from autumn to winter. In April ~ May, the corners fall off and new horns grow At this time, the unbroken unglazed young horn is called "antler" and the part where the mineral component is gradually made into a bone is called a "wakagaku". The kneaded mass made by boiling and concentrating the wakagaku is cut into a wakagaku.

녹각교는 뼈와 치아의 생성을 도와주고, 조혈과 저혈압 및 강압작용을 하며, 소아 발육을 촉진하고, 부인 산전, 산후 일체 호로에 응용되며, 신체의 저항력을 증시키고, 상처 및 궤양의 유압을 촉진시키며, 생체 활동력을 증강시키고, 체내의 콜레스테롤을 감소시켜 동맥경화를 방지하는 등 다양한 효과가 입증되어 있다.It can be used in hematopoietic, hypotensive and cooperative tasks, promoting pediatric development, in maternal and postnatal fertility, increasing body resistance, and reducing the pressure of wounds and ulcers Accelerating, promoting bioactivity, reducing cholesterol in the body, and preventing arteriosclerosis.

녹각은 뼈와 같이 단단한 물질이기 때문에 잘게 자르거나 가루를 낸다 해도 식용이나 약용으로 이용하는데 매우 불편하므로, 최근에는 녹각을 절단하여 물로 끓여서 농축하여 만든 녹각교로 이용하는 것이 일반적이다.Since it is a hard material like bones, it is very uncomfortable to use it for edible or medicinal purposes even if it is cut or crushed finely. In recent years, it is common to use a raspberry made by cutting a waxy oven and boiling it with water and concentrating it.

일반적인 녹각교의 제조는 녹각을 잘게 잘라 물속에 넣어 하루에 1 ~ 2번 물을 갈아주어 맑은 물에 반복하였다가 꺼내어 용기에 넣고 각질이 유동될 정도로 끓여서 교액을 얻은 후 약한 불로 농축한다. 이렇게 농축된 교액을 냉각시켜 작은 쪽편으로 만들어 건조시켜 이루어진다. 이러한 녹각교는 녹각을 이용하는 것 보다는 식용이나 약용으로 이용하기도 편리하고 다른 식재나 약재로 혼합하여 사용하기도 편리하였지만 농축하여 덩어리 형태로 만들어 지기 때문에 제조기간도 많이 걸리고 유효성분의 농축효율도 떨어지며 이용하기에도 여전히 불편하였다.Generally, the preparation of the scallops is done by cutting the scallops and putting them into the water, changing the water one or two times a day, repeating them in clear water, taking them out, putting them in the container, boiling them until the dead skin flows and concentrate them. The thickened liquor is cooled and made into small pieces and dried. This type of earthenware is convenient to be used for edible or medicinal purposes rather than using a dagger, and it is convenient to use it by mixing with other food materials or medicinal materials, but since it is made into a lump form by concentration, it takes a lot of preparation period, It was still uncomfortable.

따라서 최근에는 유효성분의 농축효율도 높고 식재나 약재로 직접이용하거나 첨가하여 사용하는데에 더 효율적인 녹각교를 농축하여 분말상태로 만드는 방법이 개발되어 있다. 이는 노각을 80 ~ 90의 물속에 넣고 유효성분만 추출하여 진공 농축한 후 동결건조시키고, 동결건조된 농축액을 분쇄하여 분말상태로 만드는 방법이다.Recently, there has been developed a method of concentrating and more effectively forming a powdery state of a grapefruit bridge, which is more efficient in concentrating the active ingredient and using the same directly as a plant material or a pharmaceutical material. This is a method in which the lobes are placed in a water of 80 to 90, extracted with an effective component, concentrated in vacuo, lyophilized, and lyophilized into a powder.

녹각교를 분말상태로 제조하였기 때문에 요리를 하거나 약용으로 사용할 때 식재료에 간단히 뿌려서 먹어도 되고 요리중에 간단히 첨가할 수 있으며 약용으로 사용할 때도 환으로 만들거나 다른 약재에 혼합시키거나 첨가하기도 편리하다.It can be easily sprinkled on the ingredients when it is cooked or used for medicinal purposes because it is made in powder form and it can be easily added in cooking.

이러한 편리성 때문에 최근에는 녹각교를 분말상태로 제조하여 이용하지만, 제조과정에서 수추출하는 과정이 필수적인데, 수추출시간이 많이 걸리고, 수추출 효율성이 떨어져 녹각의 유효성분이 많이 낭비되고 있으며, 수추출 과정에서 단백질 성분이 석회질화 되는 문제점이 있었다.
Because of this convenience, it is necessary to make the process of extracting water in the manufacturing process. However, it takes a lot of water extraction time, the water extraction efficiency is low, and the effective amount of the extract is wasted. There is a problem that the protein component is calcified in the extraction process.

대한민국 등록특허 10-1286849 호Korean Patent No. 10-1286849

본 발명은 전술한 바와 같은 문제점을 해결하기 위한 것으로, 녹각교 제조공정중에서 수추출 단계를 세분화시켜 추출시간을 단축하고, 녹각의 유효성분 추출률도 높이고, 특히 수추출 과정에서 단백질 성분이 석회질화 되는 것도 감소시킬 수 있는 녹각교 농축분말 제조방법을 제공하고자 한다.
Disclosure of Invention Technical Problem [8] Accordingly, the present invention has been made in order to solve the above-mentioned problems, and it is an object of the present invention to provide a process for producing a starch- And a method for producing the same.

본 발명은 상기의 목적을 달성하기 위하여 녹각을 절단하여 물에 끓여서 농축하여 만든 녹각교 농축분말 제조방법에 있어서, (1) 녹각을 편절하여 수침한 후 핏물이나 이물질을 제거하는 단계; (2) 단계(1)에 의해 얻어진 녹각을 80 ~ 90℃의 물속에 44 ~ 52시간 동안 담가 녹각의 유효성분을 1차적으로 추출하는 단계; (3) 단계(2)에 의해서 추출되고 남은 녹각에 기존에 있던 물은 완전히 제거하고 새로운 물을 채워 85 ~ 90℃에서 22 ~ 26시간 동안 담가 녹각의 유효성분을 2차적으로 추출하는 단계; (4) 단계(3)에 의해서 추출되고 남은 녹각에 기존에 있던 물을 완전히 제거하고 새로운 물을 채워 85 ~ 90℃에서 22 ~ 26시간 동안 담가 녹각의 유효성분을 3차적으로 추출하는 단계; (5) 단계(2)(3)(4)를 통해 얻어진 농축물을 특정 입자 크기 이하만 통과하는 거름망에 여과시키는 단계: (6) 단계(5)를 통해 얻어진 농축물을 60 ~ 70℃에서 진공 농축시키는 단계; (7) 단계(6)를 통해 얻어진 농축물을 상온에서 냉각시키는 단계: (8) 단계(7)에 의해 냉각된 농축물을 동결시켜 건조시키는 단계; (9) 단계(8)를 통해 동결건조된 농축물을 분쇄하는 단계;를 포함하여 이루어진 것을 특징으로 하는 녹각교 농축분말 제조방법을 제공한다.In order to accomplish the above object, the present invention provides a method for preparing a grapefruit concentrate powder by cutting a green leaf, boiling it in water and concentrating it, the method comprising the steps of: (1) decanting the green leaf to remove blood and foreign matter; (2) first extracting the active ingredient of the green bean by immersing the green angle obtained in the step (1) in water at 80 to 90 ° C for 44 to 52 hours; (3) extracting the active ingredient of the wax glaze at 85 to 90 ° C for 22 to 26 hours by completely removing the water existing in the wax glaze extracted by step (2) and filling with fresh water; (4) extracting the active ingredient of the wax glaze by immersion for 22 to 26 hours at 85 to 90 ° C by completely removing the existing water from the wax glaze extracted by step (3) and filling with fresh water; (5) filtering the concentrate obtained through steps (2), (3) and (4) into a sieve net that passes only below a specific particle size: (6) concentrating the concentrate obtained from step (5) Vacuum concentrating; (7) cooling the concentrate obtained at step (6) at room temperature; (8) freezing and drying the concentrate cooled by step (7); And (9) pulverizing the lyophilized concentrate through step (8).

또한, 상기 단계(3)과 단계(4)에서 새로운 물을 채워 넣을 때, 단계(2) 물 양의 40 ~ 60wt% 인 것을 특징으로 하고, 상기 단계(5)의 농축물을 여과시키는 단계에서, 농축물의 온도는 85 ~ 90℃를 유지하여 농축물의 유동성이 저하되지 않도록 하는 것을 특징으로 한다.
The method according to any one of the above items (1) to (4), wherein the fresh water is filled in the step (3) and the step (4) , And the temperature of the concentrate is maintained at 85 to 90 캜 so that the fluidity of the concentrate is not lowered.

본 발명에 따르면, 녹각을 물속에 넣고 가열하여 녹각교를 수추출할 때 1차,2차,3차로 단계가 나누어 이루어지므로, 단계 없이 연속되는 한번으로 수추출이 이루어질 때 농축물의 농도가 높아지면서 수추출시간이 길어지는 것이 방지되어 전체적인 수추출시간이 단축되고, 80℃ 이상에서 장시간 수추출 할때 미량이지만 농축물의 일부가 석회질화되는데 수추출시간이 단축되면서 이러한 석회질화도 상대적으로 감소시킬 수 있다.According to the present invention, since the steps are divided into first, second and third stages when the green bean is put in water and heated to extract the green bean ganoderma, the concentration of the concentrate is increased The water extraction time is prevented from being lengthened, and the total water extraction time is shortened. When the water is extracted at a temperature of 80 ° C or more for a long time, a trace amount of the concentrate is calcified, but the water extraction time is shortened and the calcification can be relatively reduced .

또한 수추출 후속 공정에서 물을 전부 제거해야 하므로 녹각의 양에 비해 물의 양이 적을수록 좋지만, 물의 양이 적어지면 수추출 하는 동안 농축물의 농도가 높아지면서 수추출 시간이 길어지므로 이러한 점을 고려하여 보통 녹각의 양에 비해 물의 양을 3 ~ 5배수로 하지만, 본 발명에서는 수추출단계를 3차로 나누고 각 단계를 넘어갈 때 마다 농축물을 따로 분리한 후 새로운 물을 채워 수추출하므로 농축물의 농도가 상대적으로 낮으며, 이로 인해 녹각의 양에 비해 물의 양을 기존 보다 상대적으로 적게 하여도 수추출이 잘되므로 후속되는 공정에서 물을 제거하는 시간도 단축시킬 수 있다.
In addition, since the water must be completely removed in the subsequent process of water extraction, the smaller the amount of water compared to the amount of the antler, the better. However, as the amount of water decreases, the concentration of concentrate increases during water extraction, In the present invention, the water extraction step is divided into three stages, and the concentrate is separately separated each time it is passed through each step, and the water is extracted by filling with fresh water. Therefore, the concentration of the concentrate is relatively Therefore, even if the amount of water is relatively smaller than the amount of water, the water extraction is performed well, so that the time for removing water in the subsequent process can be shortened.

도 1은 본 발명에 따른 녹각교 농축분말 제조 공정도이다.FIG. 1 is a view illustrating a process for producing a granulated green tea product according to the present invention.

첨부된 도면을 참조하여 본 발명은 상세히 설명하면 다음과 같다. 도 1은 본 발명에 따른 녹각교 농축분말 제조 공정도이다.The present invention will be described in detail with reference to the accompanying drawings. FIG. 1 is a view illustrating a process for producing a granulated green tea product according to the present invention.

도 1에 도시된 바와 같이, 매년 새로나는 사슴의 어린뿔이 점차 무기질 성분이 증가되어 골질화된 부분을 자른 녹각을 구비한다.As shown in Fig. 1, a new deer's horn of the deer gradually increases the mineral component every year and has a perforated section cut by the osseed part.

녹각을 다루기 쉽게 몇 토막으로 잘라 맑은 물에 24 ~ 48시간 동안 담가두어 녹각속의 핏물이나 녹각에 붙어 있는 이물질을 제거한다. 핏물과 이물질을 제거되는 동안 1 ~ 3번 물을 갈아주어 핏물과 이물질 등 불순물을 완전히 제거한다.(S10)Cut the dough into several pieces easily to remove the dough and soak it in clear water for 24 ~ 48 hours to remove foreign substances from the blood or the wax in the wax. During the removal of blood and foreign matter, the water is changed one to three times to completely remove impurities such as blood and foreign matter (S10).

녹각이 담가지는 물은 온도가 너무 높은면 지방과 단백질이 주성분인 녹각의 유효성분이 빠져나올 수 있으므로 25℃ 이하를 유지하는 것이 바람직하다.If the temperature of the water is too high, the active ingredient of the main component of the oil is removed.

핏물과 이물질을 제거한 녹각은 1차수추출 단계로서 80 ~ 90℃의 물에 44 ~ 52시간 동안 담가 두어 녹각 속에 함유된 지방과 단백질(이하, 유효성분이라 통칭함)을 주성분으로 하는 유효성분을 추출한다.(S20)In the first stage extraction step, the green algae which have removed the blood and foreign matter is immersed in water at 80 ~ 90 ℃ for 44 ~ 52 hours to extract the active ingredient containing the fat and protein (hereinafter referred to as active ingredient) (S20)

물의 온도가 높을수록 추출시간은 빠르지만 90℃ 이상에서는 녹각의 유효성분이 석회질화가 빠르게 진행되므로 온도를 높이는 것은 한정될 수 밖에 없다. 1차수추출단계에서는 녹각속의 유효성분이 70wt%정도 추출되는데, 52시간이 넘어가면 먼저 추출된 유효성분의 물속 농도가 높아져 추출효율이 떨어지므로 52시간이 넘기지 않도록 하는 것이 바람직하다.The higher the temperature of the water, the faster the extraction time, but at 90 ° C or higher, the effective content of the wax glaze accelerates the calcification, so raising the temperature is limited. In the first order extraction step, the effective component of the green wing is extracted by about 70 wt%. When the time exceeds 52 hours, the extraction efficiency becomes lower due to the higher water concentration of the extracted active component.

1차수추출이 끝나면 2차수출 단계로서, 녹각만 남겨두고 농축물(추출되어 물과 혼합된 녹각의 유효성분)을 완전히 분리한 후, 남겨진 녹각에 새로운 맑은물을 채워 넣고 80 ~ 90℃에서 22 ~ 26시간 동안 담가 두어 녹각 속에 함유된 유효성분을 추출한다.(S30)After the extraction of the first order, the second step of exporting is to completely separate the concentrate (the active ingredient of the extract from the green bean curd mixed with water) leaving only the leaves of the green bean, then filling the fresh green leaves with fresh clear water, For 26 hours to extract the active ingredient contained in the green wok (S30).

2차수추출 단계에서는 1차수추출 단계에서 추출되고 남은 30wt%의 유효성분중 20wt% 정도가 추출된다.In the second order extraction step, 20wt% of the remaining 30wt% active ingredient extracted in the first order extraction step is extracted.

2차수출이 끝나면 3차수출 단계로서, 녹각만 남겨두고 농축물을 완전히 분리 한 후, 남겨진 녹각에 새로운 맑은물을 부어 넣고 80 ~ 90℃에서 22 ~ 26시간 동안 담가 두어 논각 속에 함유된 유효성분을 추출한다.(S40)When the second export is completed, the third stage of exporting is to leave only the green leaves and completely separate the concentrate, then pour fresh clear water into the remaining green leaves and immerse at 80 ~ 90 ℃ for 22 ~ 26 hours to remove the active ingredient (S40)

2,3차수추출 단계에서 새로 채워 넣는 물은 1차수추출단계에서 유효성분의 상당부분이 빠져 나갔으므로 1차수추출단계의 물 양의 40 ~ 60wt% 이다.The water to be newly filled in the 2nd and 3rd extraction stages is 40 ~ 60wt% of the amount of water in the 1st extraction stage because a significant part of the active ingredient has escaped in the 1st extraction stage.

3차수추출 단계에서는 2차수추출 단계에서 추출되고 남은 10wt%의 유효성분이 추출된다.In the third order extraction step, the remaining 10 wt% effective components extracted from the second order extraction step are extracted.

수추출단계를 1,2,3차로 구분하지 않고 100시간 이상 담가두어 한번에 녹각속의 유효성분을 추출해 낼수도 있지만, 위에서도 언급한 바와 같이, 추출된 유효성분의 농도가 높아지면서 추출효율이 크게 떨어지고, 더욱 문제가 되는 것은 연속되는 추출시간이 길어질수록 유효성분의 일부가 석회질화 된다. 석회질화된 유효성분은 농축물 속에 미량으로 존재하더라도 녹각교의 품질을 저하시키는 주요인 이었고, 별도의 공정을 통해 유효성분과 분리하는 것도 알려진 바가 없었다.The extracting step may be carried out for at least 100 hours without dividing the extracting step into the first, second and third stages. However, as mentioned above, since the concentration of the extracted active ingredient is increased and the extraction efficiency is greatly decreased, What is more problematic is that as the continuous extraction time becomes longer, a part of the active ingredient becomes calcified. The calcined active ingredient was the main cause of deterioration of the quality of the edible brass even when present in trace amounts in the concentrate and there was no known separation from the active ingredient through a separate process.

따라서 녹각교의 품질을 높이기 위해서 위에서와 같이 녹각을 3단계로 나누어 수추출하고, 수추출하는 단계마다 특정한 시간을 정해서 녹각속의 유효성분은 최대한 취하고 유효성분이 석회질화 되는 량은 최소화시켜 궁극적으로 녹각교의 생산성을 높이고 품질은 높일 수 있도록 한 것이다.Therefore, in order to improve the quality of the scaffolding, the scaffolding is divided into three stages, and the number of the active ingredients in the scaffold is maximized and the amount of the active ingredient is minimized by ultimately determining the productivity of the scaffolding So that the quality can be increased.

1,2,3수추출단계를 거쳐 얻어진 농축물 중에는 녹각의 일부가 깨지거나 완전히 제거되지 않은 이물질이 농축물 속에 혼입되어 있으므로 불순물을 제거하고 유효성분만을 걸려내기 위해서 마이크로그물망을 통해 필터링 한다. 마이크로그물망은 필요에 따라 격자의 크기를 선택할 수 있지만 바람직한 실험치로서 입자가 0.25㎛ 이하만 통과할 수 있도록 한다.(S50)1,2,3 Water In the concentrate obtained through the extraction step, a part of the antler is broken or the foreign matter which is not completely removed is mixed in the concentrate. Therefore, it is filtered through the micro mesh to remove the impurities and to take the effective delivering. The micro mesh can select the size of the lattice according to need, but it is a preferable experimental value so that the particles can pass through only 0.25 탆 or less (S50)

여과방식은 용기의 하부에 마이크로그물망을 설치하고 그 용기 안에 농축물을 부어 넣고 2 ~ 3시간 동안 자연유하 방식으로 필터링 하는데, 여과가 이루어지는 동안 용기를 가열하여 농축물이 85 ~ 90℃를 유지하도록 한다. 여과 과정에서 농축물의 온도가 내려가면 유동성이 떨어지면서 서로 엉겨 붙거나 마이크로그물망에 달라붙어 여과 시간이 오래 걸리게 된다.In the filtration method, a micro mesh is installed in the lower part of the vessel. Concentrate is poured into the vessel and the vessel is filtered by natural submergence for 2 to 3 hours. During the filtration, the vessel is heated to maintain the concentrate at 85 to 90 ° C do. When the temperature of the concentrate is lowered during the filtration process, the fluidity is lowered, and the filtration time becomes longer due to clinging to each other or sticking to the micro mesh.

마이크로그물망을 통과시킨 농축물은 공기와의 지속적인 접촉으로 발생되는 성분 변화를 방지하기 위하여 진공상태에서 농축시킨다.(S60)The concentrate having passed through the micro-network is concentrated in a vacuum state to prevent a component change caused by continuous contact with air. (S60)

진공농축은 24시간 정도 진행되는데 그 과정에서 농축물에 혼합된 물의 70% 정도가 증발하고, 농축물간에 엉겨 붙어 결정화될 수 있을 정도인 30% 정도의 물만 남게 된다. 진공농축 과정에서 농축물의 온도가 높을수록 수분의 증발은 빠르지만 80℃ 이상에서는 농축물이 성분변화를 일으킬 수 있으므로 60 ~ 70℃에서 농축하는 것이 바람직하다.Vacuum concentration lasts about 24 hours, during which about 70% of the water mixed with the concentrate evaporates and only about 30% of the water remains so that the concentrate can be clumped and crystallized. The higher the temperature of the concentrate in vacuum concentration is, the faster the evaporation of water is. However, it is preferable to concentrate at 60 to 70 ° C because the concentrate may cause component change at 80 ° C or higher.

진공농축 과정에서 70wt% 정도의 물이 증발되어도 30wt% 정도의 물은 남게 되는데, 이 정도의 수분을 함유한 농축물은 일정량씩 계량하여 배출시킬 수 있는 계량탱크에 담아서 3 ~ 4시간 동안 자연냉각시켜 겔상태로 결정화 시킨다.(S70)Even if 70 wt% of water is evaporated in the vacuum concentration process, about 30 wt% of water remains. The concentrate containing this amount of water is put into a weighing tank which can be weighed and discharged for a predetermined amount, And crystallized in a gel state. (S70)

계량탱크를 통해 냉각시켜 겔상태로 결정화된 농축물은 접시형태의 트레이에 일정량씩 분배하여 24 ~ 48시간 동안 -85℃ 정도로 냉각시켜 건조시킨다.(S80)The gelatinized concentrate is cooled to -85 ° C. for 24 to 48 hours and then dried (S 80).

동결건조단계에서는 농축물에 포함된 수분함량이 2% 이하가 될 때까지 건조시킨다. 건조된 농축물은 밀가루처럼 분쇄시켜 포장하면 농축분말화 녹각교가 완성된다.(S90)In the lyophilization step, the concentrate is dried until the moisture content is less than 2%. The dried concentrate is crushed and packed like wheat flour, and then the concentrated powdered alum cane is completed. (S90)

상기와 같이 이루어지는 본 발명에 따른 일실시예를 설명하면 다음과 같다.An embodiment according to the present invention will be described as follows.

녹각 100kg을 10cm 정도로 잘라서 48시간 동안 맑은 물속에 냉침시켜 핏물과 이물질을 제거한다.Cut 100kg of green bean into about 10cm and cool in clear water for 48 hours to remove blood and foreign matter.

1차수추출 단계로서 수세된 녹각 100kg에 맑은 물 400ℓ를 부어 넣고 85℃에서 48시간 동안 가열하여 200ℓ의 농축물을 얻는다. 여기서 200ℓ의 농축물은 물과 녹각에서 지방과 단백질을 주성분으로 하는 추출물의 합계이다.As a first order extraction step, 400 kg of clear water is poured into 100 kg of washed green beans and heated at 85 ° C for 48 hours to obtain 200 L of concentrate. Here, the 200-L concentrate is the sum of extracts of fat and protein as main components in water and in the oyster.

2차수추출 단계로서 1차수추출 되고 남은 녹각에 다시 맑은 물 200ℓ를 부어 넣고 24시간 동안 가열하여 100ℓ의 농축물을 얻는다.As a second-order extraction step, 200 l of clear water is poured into the remaining algae extracted with the first order, and heated for 24 hours to obtain 100 l of a concentrate.

3차수추출 단계로서 2차수출되고 남은 녹각에 다시 맑은 물 200리터를 부어 넣고 24시간 동안 가열하여 100리터의 농축액을 얻는다.As a third stage extraction step, 200 liters of clear water is poured into the remaining second leaves and heated for 24 hours to obtain 100 liters of concentrated liquid.

1,2,3차수출물을 통해 얻은 400ℓ농축물을 격자크기가 0.25㎛인 마이크로거름망에 2시간에 걸쳐 통과시켜 마이크로거름망의 격자 보다 큰 이물질은 미량이지만 걸려내고 그 격자 보다 작은 농축물을 얻는다. 마이크로거름망을 통과시킬때 농축물의 온도는 85℃를 유지한다.The 400 L concentrate obtained from the 1,2,3-export is passed through a micro-sieve with a mesh size of 0.25 μm for 2 hours to obtain a small amount of foreign matter larger than the micro-sieve lattice but to obtain a concentrate smaller than the lattice . The temperature of the concentrate is maintained at 85 ° C when passing through the micro-sieve.

마이크로거름망을 통해 여과된 400ℓ의 농축물은 진공농축기에 집어넣고 2기압, 65℃를 유지하면서 농축물이 120ℓ가 될 때까지 물을 증발시킨다. 여기서 진공농축 시간을 더 늘리면 물을 더 많이 증발시킬 수 있지만, 진공농축 과정에서 성분변화를 일으킬 수 있으므로 자연냉각시켰을 때 결정화가 이루어질 정도까지만 증발시킨 것이다.400 L of the filtrate filtered through a micro-sieve is poured into a vacuum concentrator and the water is evaporated until the concentrate becomes 120 L while maintaining 2 atm at 65 ° C. Here, when the vacuum concentration time is further increased, it is possible to evaporate water more, but since the vacuum concentration process may cause the component change, it is evaporated to such an extent that crystallization occurs when the product is naturally cooled.

진공농축기를 거친 120ℓ의 농축물은 일정량씩 계량하여 분배할 수 있는 계량탱크에 집어넣고 4시간 동안 자연냉각시킨다. 계량탱크에서 냉각이 되면 겔상태로 결정화된다.The 120-L concentrate passed through a vacuum concentrator is put in a weighing tank which can be dispensed by a certain amount and is naturally cooled for 4 hours. When cooled in the weighing tank, it crystallizes in a gel state.

결정화된 농축물은 접시와 같은 트레이에 5kg 씩 트레이에 충진시켜 -85℃로 급속동결시키고, 이렇게 동결된 농축물을 0.3torr에서 -18℃를 유지하면서 잔존수분이 2%가 될때까지 동결건조시킨다.The crystallized concentrate is packed into a tray on a tray of 5 kg in a tray and rapidly frozen at -85 ° C. and the lyophilized concentrate is lyophilized at 0.3 ° C. to -18 ° C. until the residual moisture becomes 2% .

잔존수분이 2% 이하까지 동결건조된 농축물은 0.2 ~ 1.0mm로 분쇄하거나, 3 ~ 4cm 정도로 편을 만들어 포장한다.
The lyophilized concentrate with residual water content of 2% or less is crushed to a size of 0.2 to 1.0 mm, or wrapped to a size of 3 to 4 cm.

S10,S20,S30,S40,S50,S50,S60,S70,S80,S90 : 녹각교 농축분말 제조공정의 순차적인 단계S60, S70, S80, S90: Sequential steps of the manufacturing process of the glutinous concentrate powder, S10, S20, S30, S40, S50, S50,

Claims (3)

녹각을 절단하여 물에 끓여서 농축하여 만든 녹각교 농축분말 제조방법에 있어서,
(1) 녹각을 편절하여 수침한 후 핏물이나 이물질을 제거하는 단계;
(2) 단계(1)에 의해 얻어진 녹각을 80 ~ 90℃의 물속에 44 ~ 52시간 동안 담가 녹각의 유효성분을 1차적으로 추출하는 단계;
(3) 단계(2)에 의해서 추출되고 남은 녹각에 기존에 있던 물은 완전히 제거하고 새로운 물을 채워 85 ~ 90℃에서 22 ~ 26시간 동안 담가 녹각의 유효성분을 2차적으로 추출하는 단계;
(4) 단계(3)에 의해서 추출되고 남은 녹각에 기존에 있던 물을 완전히 제거하고 새로운 물을 채워 85 ~ 90℃에서 22 ~ 26시간 동안 담가 녹각의 유효성분을 3차적으로 추출하는 단계;
(5) 단계(2)(3)(4)를 통해 얻어진 농축물을 특정 입자 크기 이하만 통과하는 거름망에 여과시키는 단계:
(6) 단계(5)를 통해 얻어진 농축물을 60 ~ 70℃에서 진공 농축시키는 단계;
(7) 단계(6)를 통해 얻어진 농축물을 상온에서 냉각시키는 단계:
(8) 단계(7)에 의해 냉각된 농축물을 동결시켜 건조시키는 단계;
(9) 단계(8)를 통해 동결건조된 농축물을 분쇄하는 단계;
를 포함하여 이루어진 것을 특징으로 하는 녹각교 농축분말 제조방법.
A method for producing a waxy dense concentrated powder, which comprises cutting a wax glaze, boiling it in water and concentrating it,
(1) a step of chewing and soaking the green cloth to remove blood and foreign matter;
(2) first extracting the active ingredient of the green bean by immersing the green angle obtained in step (1) in water at 80 to 90 ° C for 44 to 52 hours;
(3) extracting the active ingredient of the wax glaze at 85 to 90 ° C for 22 to 26 hours by completely removing the water existing in the wax glaze extracted by step (2) and filling with fresh water;
(4) extracting the active ingredient of the wax glaze by immersion for 22 to 26 hours at 85 to 90 ° C by completely removing the existing water from the wax glaze extracted by step (3) and filling with fresh water;
(5) filtering the concentrate obtained through steps (2), (3) and (4) into a filter which passes only below a specific particle size:
(6) concentrating the concentrate obtained in step (5) in vacuo at 60-70 DEG C;
(7) cooling the concentrate obtained in step (6) at room temperature;
(8) freezing and drying the cooled concentrate by step (7);
(9) pulverizing the lyophilized concentrate through step (8);
The method of claim 1,
제1항에 있어서,
상기 단계(3)과 단계(4)에서 새로운 물을 채워 넣을 때, 단계(2) 물 양의 40 ~ 60wt% 인 것을 특징으로 하는 녹각교 농축분물 제조방법.
The method according to claim 1,
Wherein the fresh water is filled in the step (3) and the step (4) in an amount of 40 to 60 wt% of the amount of water in the step (2).
제1항에 있어서,
상기 단계(5)의 농축물을 여과시키는 단계에서, 농축물의 온도는 85 ~ 90℃를 유지하여 농축물의 유동성이 저하되지 않도록 하는 것을 특징으로 하는 녹각교 농축분말 제조방법.
The method according to claim 1,
Wherein the concentration of the concentrate is maintained at 85 to 90 DEG C in the step of filtering the concentrate of step (5) so that the fluidity of the concentrate is not lowered.
KR1020140039966A 2014-04-03 2014-04-03 Method for preparing concentration powder of Cervi Cornus colla KR20150115254A (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR102635695B1 (en) 2023-08-01 2024-02-13 유한회사 한풍제약 Manufacturing method of enzymatically-treated cervi cornu calcium powder

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR102635695B1 (en) 2023-08-01 2024-02-13 유한회사 한풍제약 Manufacturing method of enzymatically-treated cervi cornu calcium powder

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