KR100853313B1 - A high efficient method for extracting beta-carotene from persimmon skin - Google Patents
A high efficient method for extracting beta-carotene from persimmon skin Download PDFInfo
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- TUPZEYHYWIEDIH-WAIFQNFQSA-N beta-carotene Natural products CC(=C/C=C/C=C(C)/C=C/C=C(C)/C=C/C1=C(C)CCCC1(C)C)C=CC=C(/C)C=CC2=CCCCC2(C)C TUPZEYHYWIEDIH-WAIFQNFQSA-N 0.000 title claims abstract description 41
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- WQZGKKKJIJFFOK-VFUOTHLCSA-N beta-D-glucose Chemical compound OC[C@H]1O[C@@H](O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-VFUOTHLCSA-N 0.000 description 1
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- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23L—FOODS, 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
- A23L19/00—Products from fruits or vegetables; Preparation or treatment thereof
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23P—SHAPING OR WORKING OF FOODSTUFFS, NOT FULLY COVERED BY A SINGLE OTHER SUBCLASS
- A23P10/00—Shaping or working of foodstuffs characterised by the products
- A23P10/20—Agglomerating; Granulating; Tabletting
- A23P10/25—Agglomeration or granulation by extrusion or by pressing, e.g. through small holes, through sieves or between surfaces
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23V—INDEXING SCHEME RELATING TO FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES AND LACTIC OR PROPIONIC ACID BACTERIA USED IN FOODSTUFFS OR FOOD PREPARATION
- A23V2002/00—Food compositions, function of food ingredients or processes for food or foodstuffs
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23V—INDEXING SCHEME RELATING TO FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES AND LACTIC OR PROPIONIC ACID BACTERIA USED IN FOODSTUFFS OR FOOD PREPARATION
- A23V2250/00—Food ingredients
- A23V2250/20—Natural extracts
- A23V2250/21—Plant extracts
- A23V2250/211—Carotene, carotenoids
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- Life Sciences & Earth Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Food Science & Technology (AREA)
- Polymers & Plastics (AREA)
- Health & Medical Sciences (AREA)
- Nutrition Science (AREA)
- Extraction Or Liquid Replacement (AREA)
- Medicines Containing Plant Substances (AREA)
Abstract
Description
본 발명은 감과피로부터 베타-카로틴의 고효율 추출방법에 관한 것으로, 더욱 상세하게는 감과피를 건조한 후 분말화하고 압출한 다음 5~10중량% NaCl이 함유된 물을 감과피 분말 중량대비 50~100% 혼합하여 분쇄하고 건조하여 전처리하고 상기와 같이 전처리된 감과피를 초임계이산화탄소와 보조용매로서 아세톤을 사용하여 초임계 추출함으로써 감과피로부터 베타-카로틴을 높은 수율로 추출할 수 있는 방법에 관한 것이다.The present invention relates to a high-efficiency extraction method of beta-carotene from persimmon skin, and more particularly, dried persimmon skin, powdered and extruded, and then water containing 5-10 wt% NaCl 50 ~ A method of extracting beta-carotene from persimmon peel in high yield by supercritical extraction using 100% of mixed persimmon pulverized, dried, pretreated and supercritical carbon dioxide and acetone as cosolvent. will be.
감(Persimmon, Diospyros Kaki,L.) 과실은 아열대 및 온대지방의 과실로 한국과 일본, 중국이 주산지로 지중해 지역의 나라에서도 유망한 작물로 각광받고 있다. 감은 포도당, 과당 등의 당류와 비타민 A 및 C가 풍부한 알칼리성 식품이며, 설사와 피를 멈추게 하는 약리작용을 가지는 과실로 알려져 있다. 현재, 국내 감 생산량은 년간 약 239,000M / T이며 그 생산량이 매년 증가하고 있는 추세이며 건시를 비롯해 여러 가지 형태로 소비되고 있다. 곳감 가공시 감과피가 많이 발생하는데, 지용성 색소인 카로테노이드(carotenoid)가 다량 함유되어 있다. Persimmon, Diospyros Kaki , L.) Fruits are subtropical and temperate fruits, and Korea, Japan, and China are the most prominent crops in the Mediterranean region. Persimmon is an alkaline food rich in sugars such as glucose and fructose, vitamins A and C, and is known as fruit having pharmacological action to stop diarrhea and blood. At present, domestic persimmon production is about 239,000M / T per year, and its production is increasing every year, and is being consumed in various forms, including Kunxi. Persimmon skin is generated a lot during persimmon processing, and it contains a large amount of carotenoids, which are fat-soluble pigments.
카로테노이드(Carotenoid) 화합물 중에서 비타민(vitamin) A로서의 역가가 가장 높은 베타-카로틴(β-carotene)은 식품, 의약품 및 화장품 등의 착색제 및 첨가제로서 오래전부터 사용되고 있으며 현재는 강력한 항암 효과, 대사과정에서 retinol의 주공급원으로 보고되어 건강식품으로서 그 중요성이 크게 인식되고 있다. Beta-carotene, which has the highest titer as vitamin A among carotenoid compounds, has been used for a long time as colorants and additives in foods, medicines, and cosmetics. It is reported as a major source of health, and its importance as a health food is greatly recognized.
그러나, 현재 산업적으로 이용되고 있는 대부분의 β-carotene은 화학합성품으로 최근 인간의 건강에 대한 관심의 증대로 인하여 천연물에 대한 욕구가 증대하고 있기 때문에 천연산 β-carotene을 얻을 수 있다면 시장에서 상품으로서의 가치가 매우 높을 것이다. However, most of the β-carotene that is currently used industrially is a chemical synthetic product, and as the desire for natural products is increasing due to the recent increase in interest in human health, if a natural β-carotene can be obtained as a commodity on the market, It will be very high value.
그런데, 천연물로부터 β-carotene을 생산하는데 가장 필수적인 요인은 추출과정 중 β-carotene의 변성을 최소화할 수 있는 새로운 추출방법의 개발이다. 초임계유체 추출공정과 마이크로웨이브 추출장치를 이용한 천연물의 추출은 최근 많은 관심의 대상이 되고 있다. However, the most essential factor in producing β-carotene from natural products is the development of a new extraction method that can minimize the denaturation of β-carotene during the extraction process. Supercritical fluid extraction process and the extraction of natural products using a microwave extraction device has recently been the subject of much interest.
종래 많이 이용되었던 용매추출법은 적절한 용매의 선택, 유기용매의 잔존, 용매의 제거 및 낮은 분리효과 등의 어려움이 있다. Solvent extraction, which has been widely used in the related art, has difficulty in selecting an appropriate solvent, remaining of an organic solvent, removing a solvent, and low separation effect.
이에 비하여 초임계유체 추출은 단순히 압력과 온도의 조절에 의하여 용질로부터 용매를 쉽게 제거할 수 있으며, 용매추출법이나 마이크로웨이브법보다 열에너지 비용이 적게 소요되는 장점이 있다.On the other hand, supercritical fluid extraction can easily remove the solvent from the solute by simply adjusting the pressure and temperature, and it has the advantage that the thermal energy cost is less than that of the solvent extraction method or the microwave method.
마이크로웨이브 추출공정은 마이크로웨이브(Microwave) 발생장치를 에너지원으로 사용하여 생체 물질로부터 천연물을 추출하는 방법으로 기존의 용매추출방법 보다 더 선택적이고 빠르게 천연물을 추출할 수 있다.The microwave extraction process is a method of extracting natural products from biological materials using a microwave generator as an energy source, which is more selective and faster than conventional solvent extraction methods.
본 발명자들은 상기와 같은 점을 감안하여 감과피를 40~50℃에서 24~48시간 건조한 후 50~100 메쉬로 분말화하고 분말화된 감과피를 압출한 다음 압출된 감과피 분말에 5~10중량% NaCl이 함유된 물을 감과피 분말 중량대비 50~100% 혼합하여 분쇄하고 40~50℃에서 24~48시간 건조하여 전처리하고 상기와 같이 전처리된 감과피를 초임계 이산화탄소 85~90중량%와 보조용매로서 아세톤 10~15중량%를 사용하여 초임계 추출함으로써 본 발명을 완성하였다.In view of the above, the present inventors dried persimmon peel at 40-50 ° C. for 24 to 48 hours, and then powdered persimmon skin into 50-100 mesh, extruded powdered persimmon peel, and then 5-10 to the extruded persimmon peel powder. 50% by weight of water containing NaCl containing 50% by weight of persimmon skin powder is mixed and pulverized, dried at 40-50 ° C for 24 to 48 hours, and pretreated as described above. 85-90% by weight of supercritical carbon dioxide The present invention was completed by supercritical extraction using 10-15% by weight of acetone as a cosolvent.
따라서, 본 발명의 목적은 감과피로부터 베타-카로틴의 고효율 추출방법을 제공하는 것이다.Accordingly, it is an object of the present invention to provide a high efficiency extraction method of beta-carotene from persimmon skin.
본 발명의 상기 목적은 감과피를 40~50℃에서 24~48시간 건조한 후 50~100 메쉬로 분말화하고 분말화된 감과피를 압출한 다음 압출된 감과피 분말에 5~10중량% NaCl이 함유된 물을 감과피 분말 중량대비 50~100% 혼합하여 분쇄하고 40~50℃에서 24~48시간 건조하여 전처리하고 상기와 같이 전처리된 감과피를 초임계이산화탄소 85~90중량%와 보조용매로서 아세톤 10~15중량%를 사용하여 초임계 추출함으로써 달성하였다.The object of the present invention is to dry persimmon peel at 40 ~ 50 ℃ 24 ~ 48 hours and then powdered into 50 ~ 100 mesh and extruding the powdered persimmon peel 5 to 10% by weight of NaCl in the extruded persimmon peel powder 50 ~ 100% of the contained water is mixed with the persimmon skin powder, pulverized, dried for 24 ~ 48 hours at 40 ~ 50 ℃ and pretreated. The pretreated persimmon skin is prepared as 85 ~ 90% by weight of supercritical carbon dioxide and cosolvent. Achieved by supercritical extraction using 10-15% by weight of acetone.
이하, 발명의 구성을 구체적으로 설명한다.EMBODIMENT OF THE INVENTION Hereinafter, the structure of this invention is demonstrated concretely.
본 발명은 감과피로부터 베타-카로틴의 고효율 추출방법을 제공한다.The present invention provides a high efficiency extraction method of beta-carotene from persimmon skin.
본 발명에서 감과피로부터 β-carotene을 고효율 추출하기 위해서는 하기 단계를 포함하는 전처리를 수행한 후 추출하는 것이 요구된다:In order to efficiently extract β-carotene from persimmon skin in the present invention, it is required to perform extraction after performing a pretreatment including the following steps:
감과피를 40~50℃에서 24~48시간 건조하는 단계;Drying persimmon skin at 40-50 ° C. for 24-48 hours;
건조된 감과피를 50~100 메쉬로 분말화하는 단계;Powdering dried persimmon skin into 50-100 mesh;
분말화된 감과피를 압출하는 단계;Extruding the powdered persimmon skin;
압출된 감과피 분말에 5~10중량% NaCl이 함유된 물을 감과피 분말 중량대비 50~100% 혼합하여 분쇄하는 단계; 및Mixing 5 to 10% by weight of water containing NaCl in the extruded persimmon skin powder by mixing 50 to 100% by weight of the persimmon skin powder; And
분쇄된 압출 감과피 분말을 40~50℃에서 24~48시간 건조하는 단계.Drying the milled extruded persimmon skin powder at 40 ~ 50 ℃ 24 ~ 48 hours.
본 발명의 감과피로부터 베타-카로틴을 고효율로 추출하는 방법은 하기 단계를 포함한다:A method of efficiently extracting beta-carotene from persimmon skin of the present invention comprises the following steps:
감과피를 40~50℃에서 24~48시간 건조하는 단계;Drying persimmon skin at 40-50 ° C. for 24-48 hours;
건조된 감과피를 50~100 메쉬로 분말화하는 단계;Powdering dried persimmon skin into 50-100 mesh;
분말화된 감과피를 압출하는 단계;Extruding the powdered persimmon skin;
압출된 감과피 분말에 5~10중량% NaCl이 함유된 물을 감과피 분말 중량대비 50~100% 혼합하여 분쇄하는 단계;Mixing 5 to 10% by weight of water containing NaCl in the extruded persimmon skin powder by mixing 50 to 100% by weight of the persimmon skin powder;
분쇄된 압출 감과피 분말을 40~50℃에서 24~48시간 건조함으로써 감과피를 전처리하는 단계; 및Pretreating the persimmon skin by drying the pulverized extruded persimmon powder at 40 to 50 ° C. for 24 to 48 hours; And
초임계이산화탄소 85~90중량%와 보조용매로서 아세톤 10~15중량%를 사용하여 상기 전처리된 감과피를 초임계 추출하는 단계.Supercritical extraction of the pretreated persimmon skin using 85 to 90% by weight of supercritical carbon dioxide and 10 to 15% by weight of acetone as a cosolvent.
본 발명에서 초임계유체 추출조건으로 온도는 40-60℃, 압력은 150-250bar, 시간은 50-70분인 것이 바람직하다.In the present invention, the supercritical fluid extraction conditions are preferably 40-60 ° C., pressure 150-250 bar, and time 50-70 minutes.
본 발명에서 카로테노이드(Carotenoid)계 색소 추출은 Curl의 방법을 응용하여 50% MeOH을 사용하여 가용성 당을 제거하고 상온에서 각각의 용매에 의해 추출된 상층부를 40℃ 이하에서 농축 후 ethyl ether와 포화 NaCl 용액(1:1, v/v)에 현탁시켜 진탕하고, 분리된 상층액에 10% KOH/ethanol 용액을 첨가하여 질소가스로 충진하고 24시간동안 방치한 다음, 분리된 상층액을 취하여 무수황산나트륨으로 탈 수한 후 회전증발농축기로 감압 농축하여 질소가스로 건조함으로써 수행한다.In the present invention, carotenoid pigment extraction is applied by Curl method to remove soluble sugars using 50% MeOH, and the upper layer extracted by each solvent at room temperature is concentrated below 40 ℃ ethyl ether and saturated NaCl The solution was suspended in solution (1: 1, v / v) and shaken. The 10% KOH / ethanol solution was added to the separated supernatant, filled with nitrogen gas, left for 24 hours, and the separated supernatant was taken up with anhydrous sodium sulfate. After dehydration, the mixture was concentrated under reduced pressure with a rotary evaporator and dried with nitrogen gas.
본 발명에서 시료의 β-카로틴 함량은 건고물에 0.01% BHT가 함유된 클로로포름 1mL에 용해하여 HPLC법에 의하여 분석한다. HPLC 시스템은 sykam510 model, C18 column(waters, 4.6mm x 250mm), UV-VIS detector로 구성되어 있는 것을 사용한다. 검출파장은 410nm이며 이동상은 클로로포름:메탄올(4:96)이며 유속은 1mL/min이다. 검량선은 시그마(sigma)(C-4646) 표준품 β-카로틴을 구입하여 0.01% BHT가 함유된 클로로포름에 용해시켜 HPLC로 분석하여 피크 면적을 작성하여 수행한다.Β-carotene content of the sample in the present invention is dissolved in 1mL chloroform containing 0.01% BHT in the dried material and analyzed by HPLC method. The HPLC system uses a sykam510 model, a C18 column (waters, 4.6mm x 250mm) and a UV-VIS detector. The detection wavelength is 410 nm, the mobile phase is chloroform: methanol (4:96), and the flow rate is 1 mL / min. The calibration curve is performed by purchasing a sigma (C-4646) standard β-carotene, dissolving it in chloroform containing 0.01% BHT, analyzing it by HPLC, and preparing a peak area.
이하, 본 발명의 구체적인 방법을 실시예를 들어 상세히 설명하고자 하지만 본 발명의 권리범위는 이들 실시예에만 한정되는 것은 아니다.Hereinafter, the specific method of the present invention will be described in detail with reference to Examples, but the scope of the present invention is not limited only to these Examples.
본 발명은 감과피를 40~50℃에서 24~48시간 건조한 후 50~100 메쉬로 분말화하고 분말화된 감과피를 압출한 다음 압출된 감과피 분말에 5~10중량% NaCl이 함유된 물을 감과피 분말 중량대비 50~100% 혼합하여 분쇄하고 40~50℃에서 24~48시간 건조하여 전처리하고 상기와 같이 전처리된 감과피를 초임계이산화탄소 85~90중량%와 보조용매로서 아세톤 10~15중량%를 사용하여 초임계 추출함으로써 비타민 A로서 역가가 가장 높은 베타-카로틴을 감과피로부터 높은 수율로 추출할 수 있는 방법을 제공할 수 있는 매우 뛰어난 효과가 있다.The present invention is dried persimmon peel at 40 ~ 50 ℃ for 24 to 48 hours and then powdered into 50 ~ 100 mesh and extruded powdered persimmon peel and water containing 5 to 10% by weight NaCl in the extruded persimmon skin 50 to 100% of the persimmon skin powder was mixed and pulverized, dried at 40 to 50 ° C for 24 to 48 hours, and pretreated. The pretreated persimmon skin was 85 to 90% by weight of supercritical carbon dioxide and
실시예Example 1: One: 감과피Persimmon 전처리 Pretreatment
본 발명에 사용한 감 껍질 즉, 감과피는 경상북도 상주 지방에서 곶감을 만들기 위해 박피한 것을 사용하였다.The persimmon peel used in the present invention, namely persimmon peel, was used for peeling to make dried persimmon in Sangju, Gyeongsangbuk-do.
감과피는 45℃ 열풍건조기에서 36시간 건조한 후 75 메쉬로 분말화한 다음 extruder로 압출하고 7중량% NaCl이 함유된 물을 감과피 분말 중량대비 75% 혼합하여 습식분쇄기(LS1, NETZSCH, Germany)로 분쇄한 후 45℃ 열풍건조기에서 36시간 건조하여 전처리하였다.Persimmon peel is dried for 36 hours at 45 ℃ hot air dryer, powdered into 75 mesh, extruded, extruder, water mixed with 7% by weight of NaCl 75% by weight of persimmon peel, and wet mill (LS1, NETZSCH, Germany) After crushing, the resultant was dried for 36 hours at 45 ° C. in a hot air dryer and pretreated.
실험예Experimental Example 1: One: 전처리된Preprocessed 감과피의Persimmon 일반성분 분석 General Ingredient Analysis
상기 실시예 1에서 전처리된 감과피 분말의 일반 성분을 상법(AOAC)에 의하여 분석하였다. 그 결과를 하기 표 1에 나타내었다. Spanos등은 고구마로부터 β-carotene 추출시 추출수율을 증가시키기 위해서는 시료의 수분함량을 줄이고, 오븐건조에 의한 표면의 경화를 줄이고 분쇄에 의하여 표면적을 최대화해야 한다고 보고하고 있다. 본 실험에서는 조섬유가 86.64%로 대부분을 차지하였으며, 총당이 51.82%이었다.General components of the persimmon skin powder pretreated in Example 1 were analyzed by the conventional method (AOAC). The results are shown in Table 1 below. Spanos et al. Reported that in order to increase the extraction yield of β-carotene from sweet potatoes, it is necessary to reduce the moisture content of the sample, reduce the surface hardening by oven drying, and maximize the surface area by grinding. In this experiment, crude fiber was 86.64% and the majority was 51.82%.
실험예Experimental Example 2: 추출용매에 따른 추출 수율 조사 2: investigation of extraction yield according to extraction solvent
감과피에서 색소를 추출하기 위하여 5종류의 용매(acetone, ethanol, ether, ethyl acetate, hexane)를 이용하여 추출온도 25℃, 추출시간 60분, 추출 용매비 1:20의 동일한 조건에서 추출을 행하였다.To extract pigments from persimmon skin, five kinds of solvents (acetone, ethanol, ether, ethyl acetate, hexane) were used under the same conditions of extraction temperature of 25 ℃, extraction time of 60 minutes and extraction solvent ratio of 1:20. It was.
추출용매에 따른 β-carotene함량을 측정한 결과를 도 1에 나타내었다. 비극성도가 높은 hexane이나 ether을 용매로 추출한 경우보다는 극성도가 상대적으로 높은 ethanol을 사용한 경우가 높았으며 ethylacetate로 추출한 실험구가 가장 높게 나타났다. The results of measuring β-carotene content according to the extraction solvent are shown in FIG. 1. Relative ethanol with higher polarity was higher than hexane or ether with high polarity, and ethylacetate was the highest in the experimental group.
Subra등에 의하면 추출 초기단계에서는 입자표면에 존재하는 카로테노이드들이 단순세척과정에 의해 추출되고 입자내부에 남아 있는 대부분의 카로테노이드들은 확산기작에 의하여 서서히 추출되기 때문에 각각의 추출용매의 확산기작의 차이로 인한 결과라고 보고되고 있다.According to Subra et al., In the early stage of extraction, the carotenoids present on the particle surface are extracted by a simple washing process, and most of the carotenoids remaining inside the particles are gradually extracted by the diffusion mechanism. It is reported.
실험예Experimental Example 3: 3: 초임계Supercritical 이산화탄소에 의한 추출 수율 조사 Investigation of Extraction Yield by Carbon Dioxide
본 실험에 사용한 초임계유체 추출장치는 최대압력이 300bar까지 사용가능한 모델로 추출온도는 50℃, 압력은 200bar, 추출시간은 60분이고 추출용매로서 이산화탄소(2 ml/min)와 보조용매(이산화탄소량의 10중량%)로서 아세톤, 에탄올 및 메탄올을 사용하였으며, 시료 추출정도를 온도, 압력 변화 및 보조용매의 종류에 대하여 측정하고 각 추출물들의 β-carotene함량을 비교하였다.The supercritical fluid extraction device used in this experiment is a model that can be used with a maximum pressure of 300bar. The extraction temperature is 50 ℃, the pressure is 200bar, the extraction time is 60 minutes, and the extraction solvent is carbon dioxide (2 ml / min) and cosolvent (carbon dioxide amount). Acetone, ethanol and methanol were used for the extraction, and the degree of sampling was measured for temperature, pressure change, and type of cosolvent, and the β-carotene content of each extract was compared.
추출온도는 카로테노이드의 열에 의한 파괴를 고려하여 60℃이하로 결정하였다. 도 2는 각각의 보조용매에 따른 추출압력의 함수로서 여러 온도에서 얻어진 β-carotene의 함량을 나타내고 있다. 일정온도에서 압력의 증가에 따라, 일정압력에서 온도의 감소에 따라 β-carotene의 추출수율이 증가하는 경향이었다. 이는 압력증가, 온도 감소에 따른 초임계 이산화탄소의 밀도가 증가하기 때문인 것으로 판단된다.Extraction temperature was determined below 60 ℃ in consideration of heat destruction of carotenoids. 2 shows the content of β-carotene obtained at various temperatures as a function of extraction pressure for each cosolvent. The extraction yield of β-carotene tended to increase with increasing pressure at constant temperature and with decreasing temperature at constant pressure. This is because the density of supercritical carbon dioxide increases with increasing pressure and decreasing temperature.
초임계이산화탄소에 대한 β-carotene의 용해도가 작기 때문에 용해도를 증가시키기 위하여 초임계이산화탄소에 보조용매로서 극성이 다른 아세톤, 에탄올, 메탄올을 가하여 감과피 분말로부터 β-carotene을 추출한 결과를 도 2에 나타내었는데, 아세톤을 보조용매로서 사용한 경우가 에탄올, 메탄올 실험구보다 β-carotene 추출 수율이 높음을 알 수 있었다.Since the solubility of β-carotene in supercritical carbon dioxide is small, the results of extracting β-carotene from persimmon skin powder by adding acetone, ethanol and methanol of different polarities as cosolvents to the supercritical carbon dioxide to increase the solubility are shown in FIG. When acetone was used as a co-solvent, β-carotene extraction yield was higher than that of ethanol and methanol experiments.
실험예Experimental Example 4: 마이크로웨이브에 의한 추출 수율 조사 4: Investigation of extraction yield by microwave
마이크로웨이브(Microwave) 추출장치는 2,450MHz 주파수의 상압형 추출장치(Microdigest unit, Prolabo, France)를 사용하였다. 추출장치는 에너지(power, watt, W)와 time control이 가능하며 환류냉각관이 장착되어 있다. 추출에너지는 100-200W, 추출시간은 3분, 추출용매는 아세톤, 에탄올, 헥산으로 1:20의 비율로 추출을 행하였다.Microwave extractors were used at atmospheric pressure type extractors (Microdigest unit, Prolabo, France) of 2,450MHz frequency. The extraction unit provides energy (power, watt, W) and time control and is equipped with a reflux condenser. The extraction energy was 100-200 W, the extraction time was 3 minutes, and the extraction solvent was extracted with acetone, ethanol and hexane in a ratio of 1:20.
Microwave추출장치를 이용하여 β-carotene을 추출한 결과는 도 3에 나타내었다. 추출용매로 아세톤을 사용한 경우가 에탄올과 헥산을 사용한 것보다 추출에너지원인 watt값이 증가함에 따라 β-carotene함량이 높았다. 에탄올을 추출용매로 사용한 실험구에서는 watt값이 증가함에 따라 β-carotene함량이 감소하였고 hexane의 경우는 뚜렷한 차이가 없었다. 이러한 결과는 선정한 용매에 따라 극성도가 다르고, 입자내 물질의 확산속도 차이에 기인된 영향이라고 사료된다. β-carotene 추출수율은 acetone을 용매로 사용하여 마이크로웨이브로 추출한 구간이 가장 높았다.The results of extracting β-carotene using a microwave extractor are shown in FIG. 3. Acetone was used as the extraction solvent, and the β-carotene content was higher as the watt value of extraction energy was increased than that of ethanol and hexane. In the experimental group using ethanol as the extraction solvent, the β-carotene content decreased with increasing watt value, and there was no significant difference in hexane. These results indicate that the polarity varies depending on the solvent selected and is due to the difference in diffusion rate of the particles in the particles. The highest yield of β-carotene extraction was obtained by microwave extraction using acetone as a solvent.
실시예Example 2: 2: 감과피로부터From persimmon 베타-카로틴의 최적 추출 Optimal Extraction of Beta-Carotene
상기 실시예 1 및 실험예들을 통하여 감과피에서 천연의 β-carotene을 추출하고자 새롭게 발견한 전처리 공정 후 기존의 용매추출법과 최근 많은 연구가 진행되고 있는 초임계유체추출, microwave를 이용한 추출법을 비교하였다. 용매추출의 경우 ethylacetate를 사용하였을 때 12.0593mg/100g으로 다른 용매보다 β-carotene추출이 우수하였고, 초임계유체추출을 이용한 경우는 아세톤을 보조용매로 사용하여 40℃정도, 250bar정도에서 추출한 경우가 20.4515mg/100g으로 추출수율이 가장 우수하였다.After the newly discovered pretreatment process to extract natural β-carotene from persimmon skin, the conventional solvent extraction method was compared with the supercritical fluid extraction and microwave extraction method. . In the case of solvent extraction, ethylacetate was used to extract β-carotene from 12.0593mg / 100g than other solvents.In case of supercritical fluid extraction, acetone was used as a co-solvent at about 40 ℃ and 250bar. The extraction yield was the best with 20.4515mg / 100g.
Microwave를 이용한 추출에서는 아세톤을 추출용매로 사용한 경우가 에탄올, 메탄올 및 핵산을 사용한 실험구보다 효과적이었으며, 추출용매에 따른 효과가 추출에너지원(watt)보다 더 많은 영향을 받음을 알 수 있었다. 따라서 전처리 공정후 초임계유체를 이용한 추출방법이 microwave추출이나 용매추출방법보다 효과적이었으며, 천연의 β-carotene 추출공정으로 산업적으로 적용가능할 것으로 사료된다.In the extraction using microwave, acetone was more effective than the experimental group using ethanol, methanol, and nucleic acid, and the effect of the extraction solvent was more affected than the extraction energy source (watt). Therefore, the extraction method using supercritical fluid after the pretreatment process was more effective than the microwave extraction method or the solvent extraction method, and it may be industrially applicable to the natural β-carotene extraction process.
따라서, 상기와 같은 결과들을 토대로 감과피로부터 베타-카로틴을 최적 추출하였다.Therefore, beta-carotene was optimally extracted from persimmon skin based on the above results.
즉, 상기 실시예 1과 같이 전처리된 감과피를 초임계이산화탄소 90중량%와 보조용매로서 아세톤 10중량%를 사용하여 추출온도는 50℃, 압력은 200bar, 추출시간은 60분으로 초임계 추출하였다(도 4 참조).That is, supercritical extraction was carried out using 90% by weight of supercritical carbon dioxide and 10% by weight of acetone as a co-solvent as per Example 1, extraction temperature was 50 ° C., pressure was 200 bar, and extraction time was 60 minutes. (See Figure 4).
이상, 상기 실시예를 통하여 설명한 바와 같이 본 발명 감과피로부터 베타-카로틴의 고효율 추출방법은 감과피를 40~50℃에서 24~48시간 건조한 후 50~100 메쉬로 분말화하고 분말화된 감과피를 압출한 다음 압출된 감과피 분말에 5~10중량% NaCl이 함유된 물을 감과피 분말 중량대비 50~100% 혼합하여 분쇄하고 40~50℃에서 24~48시간 건조하여 전처리하고 상기와 같이 전처리된 감과피를 초임계이산화탄소 85~90중량%와 보조용매로서 아세톤 10~15중량%를 사용하여 초임계 추출함으로써 비타민 A로서 역가가 가장 높은 베타-카로틴을 감과피로부터 높은 수율로 추출할 수 있는 방법을 제공할 수 있으므로 식품산업상 매우 유용한 발명인 것이다.As described above, the high-efficiency extraction method of beta-carotene from the persimmon peel of the present invention, as described through the above embodiment, dried persimmon peel at 40-50 ° C. for 24 to 48 hours, and then powdered into 50-100 mesh and powdered persimmon peel After extruding and pulverized by mixing 50 ~ 100% of water containing 5 ~ 10% by weight of NaCl in the extruded persimmon skin powder compared to the persimmon skin weight, and pre-treated by drying for 24 to 48 hours at 40 ~ 50 ℃ Supercritical extraction of pretreated persimmon skin with 85-90% by weight of supercritical carbon dioxide and 10-15% by weight of acetone as cosolvent can be used to extract beta-carotene with the highest titer as vitamin A from persimmon skin It is a very useful invention in the food industry because it can provide a method.
도 1은 전처리 한 시료와 전처리하지 않은 시료의 추출용매별 베타-카로틴 수율을 비교한 그래프이다.1 is a graph comparing beta-carotene yields by extractant of pretreated and unpretreated samples.
도 2는 전처리 한 시료와 전처리하지 않은 시료의 초임계추출에 따른 베타-카로틴 수율을 비교한 그래프이다.2 is a graph comparing beta-carotene yields according to supercritical extraction of pretreated and unpretreated samples.
도 3은 전처리 한 시료와 전처리하지 않은 시료의 마이크로웨이브추출공정(추출용매별)에 따른 베타-카로틴 수율을 비교한 그래프이다.3 is a graph comparing beta-carotene yields according to the microwave extraction process (by extraction solvent) of the pretreated and unpretreated samples.
도 4는 감과피로부터 베타-카로틴을 추출하기 위한 본 발명의 최적 추출공정을 나타낸 흐름도이다.Figure 4 is a flow chart showing the optimal extraction process of the present invention for extracting beta-carotene from persimmon skin.
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KR101268431B1 (en) | 2010-10-15 | 2013-05-28 | 경북대학교 산학협력단 | Method of producing health-benefit fermented persimmon products by persimmon peel |
KR101269545B1 (en) * | 2011-02-18 | 2013-06-04 | 대구보건대학교산학협력단 | Production method of dried persimmon prepared with persimmon-rind treatment |
KR101350245B1 (en) * | 2011-12-21 | 2014-01-16 | 대상 주식회사 | Solvent-free extraction method of omega-3 unsaturated fatty acid |
KR20160024052A (en) | 2014-08-22 | 2016-03-04 | 영남대학교 산학협력단 | Method for extracting carotenoid from fermented persimmon sludge |
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JP2005035073A (en) * | 2003-07-17 | 2005-02-10 | Fuji Photo Film Co Ltd | Method for manufacturing support for lithographic printing plate |
KR20050033036A (en) * | 2003-10-02 | 2005-04-08 | 주식회사 마광 | Animal feed composition comprising an extract of diospyrous kaki |
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JP2005035073A (en) * | 2003-07-17 | 2005-02-10 | Fuji Photo Film Co Ltd | Method for manufacturing support for lithographic printing plate |
KR20050033036A (en) * | 2003-10-02 | 2005-04-08 | 주식회사 마광 | Animal feed composition comprising an extract of diospyrous kaki |
Cited By (4)
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---|---|---|---|---|
KR101268431B1 (en) | 2010-10-15 | 2013-05-28 | 경북대학교 산학협력단 | Method of producing health-benefit fermented persimmon products by persimmon peel |
KR101269545B1 (en) * | 2011-02-18 | 2013-06-04 | 대구보건대학교산학협력단 | Production method of dried persimmon prepared with persimmon-rind treatment |
KR101350245B1 (en) * | 2011-12-21 | 2014-01-16 | 대상 주식회사 | Solvent-free extraction method of omega-3 unsaturated fatty acid |
KR20160024052A (en) | 2014-08-22 | 2016-03-04 | 영남대학교 산학협력단 | Method for extracting carotenoid from fermented persimmon sludge |
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