KR20110021409A - Manufacturing method of low salt concentrated liquid of marine products and natural source using the low salt concentrated liquid - Google Patents
Manufacturing method of low salt concentrated liquid of marine products and natural source using the low salt concentrated liquid Download PDFInfo
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- 239000012528 membrane Substances 0.000 claims abstract description 31
- 238000000034 method Methods 0.000 claims abstract description 25
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- 238000001914 filtration Methods 0.000 claims abstract description 18
- 238000001728 nano-filtration Methods 0.000 claims abstract description 11
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- 102000035195 Peptidases Human genes 0.000 claims abstract description 7
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Classifications
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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
- A23L17/00—Food-from-the-sea products; Fish products; Fish meal; Fish-egg substitutes; Preparation or treatment thereof
- A23L17/20—Fish extracts
-
- 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
- A23L23/00—Soups; Sauces; Preparation or treatment thereof
-
- 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
- A23L5/00—Preparation or treatment of foods or foodstuffs, in general; Food or foodstuffs obtained thereby; Materials therefor
- A23L5/20—Removal of unwanted matter, e.g. deodorisation or detoxification
-
- 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
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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)
- Marine Sciences & Fisheries (AREA)
- Zoology (AREA)
- Seasonings (AREA)
Abstract
Description
본 발명은 수산계 자숙액을 이용하여 농축액의 제조 시 염도를 낮추고 유용성분 및 정미 성분의 손실을 방지할 수 있는 저염도 농축액의 제조방법 및 이를 이용하여 제조된 저염도 농축액과 천연 요리장에 관한 것이다.The present invention relates to a method for preparing a low salinity concentrate that can lower the salinity and prevent the loss of useful and polished ingredients in the preparation of the concentrate using a fish-based cooked liquid, and a low salt concentrate and a natural cooker prepared using the same.
한국인의 사망원인 중 대부분은 고혈압을 비롯한 순환기계 질환이 차지하고 있으며, 나트륨의 과잉 섭취는 고혈압과 같은 질환의 주요 원인이 되는 것으로 알려져 있다. 시판 간장이나 혼합간장, 산분해간장 등과 같은 조미료와 이를 이용한 조미식품은 식염 농도가 높아 기호도가 낮으며 고혈압, 심장질환과 같은 각종 성인병의 원인이 되기도 한다. 이에 각종 식품들의 저염화 연구가 활발하게 진행되고 있다. 이러한 저염화 방법 중에서 최근에는 전기적으로 하전된 막을 이용한 전기투석법의 이용 가능성과 역삼투장치를 이용한 연구 및 산업화가 진행되어 왔다.Most of the causes of death in Korea are due to circulatory diseases, including hypertension, and excessive intake of sodium is known to be a major cause of diseases such as hypertension. Commercial seasonings such as soy sauce, mixed soy sauce, and acid-decomposed soy sauce and seasoning foods using the same have high salt concentrations and are low in palatability and may cause various adult diseases such as high blood pressure and heart disease. Accordingly, research on low salts of various foods is being actively conducted. Among these low salting methods, the possibility of using an electrodialysis method using an electrically charged membrane and the research and industrialization using a reverse osmosis apparatus have been in progress.
전기투석법은 이온성분을 용액으로부터 분리하는 공정으로, 용액에 전압을 인가하여 전기장을 걸어주면 용액 속의 이온성분이 전기장에 의해 양이온 교환수지 막과 음이온 교환수지막을 선택적으로 통과하여 발생하는 물질전달 원리에 이론적 기초를 두고 있는 방법이다. 그리고 전기투석법은 역삼투압, 한외여과와 함께 가장 많이 사용하는 막공정 중의 하나로, 전기적으로 하전된 막을 사용하여 탈염을 목적으로 주로 사용되고 있다.Electrodialysis is a process that separates ions from a solution. When a voltage is applied to a solution and an electric field is applied, ionic components in the solution are selectively passed through a cation exchange resin membrane and an anion exchange resin membrane by an electric field. This is a method based on a theoretical basis. Electrodialysis is one of the most commonly used membrane processes with reverse osmosis and ultrafiltration, and is mainly used for the purpose of desalination using electrically charged membranes.
여기서, 전기투석법은 탈염하고자 하는 물질에 함유되어 있는 저분자 무기염은 제거가 가능하지만 분자량이 큰 이온성 물질은 막을 투과할 수 없는 특성을 가지고 있다. 이러한 특성을 이용하여 초산회수에 관한 연구와 회분식 발효에서의 젖산의 분리, 금속이온의 회수, 무기용액의 제거 특성과 침출수 처리, 김치공장 폐수에서 염 회수, 해수의 담수화 및 액젓의 탈염, 참치 및 굴 자숙액의 탈염, 그리고 간장의 탈염 등에 활용에 대한 연구가 진행되고 있다.In the electrodialysis, the low molecular weight inorganic salt contained in the material to be desalted can be removed, but the ionic material having a high molecular weight cannot penetrate the membrane. Using these characteristics, research on acetic acid recovery, separation of lactic acid in batch fermentation, recovery of metal ions, removal of inorganic solutions and leachate treatment, recovery of salt from Kimchi factory wastewater, desalination of seawater and desalination of fish sauce, tuna and Research is being conducted on the desalination of oyster cooked liquid and the desalination of liver.
그러나 전기투석법은 식품산업에서의 탈염으로 목적으로 사용하기에는 설비 구축에 따른 투자비용과 에너지 소비가 크고, 운전관리 비용의 부담 또한 크며, 전기투석막 주요 장치 외에 부가적으로 폐수처리, 회수 염수 저장시설 등의 대규모 부대시설이 요구되는 한계점을 가지고 있다. 또한, 전기투석법은 탈염 과정에서 조미식품의 품질을 좌우하는 중요한 정미 성분들이 염과 함께 대량 제거되므로 조미소재의 가치를 떨어뜨리는 문제점이 있어 식품산업에서의 이용이 확대되지 못하고 있다.However, the electrodialysis method has a large investment cost and energy consumption for the purpose of desalination in the food industry, a large burden of operation and management costs, and wastewater treatment and recovery brine storage facilities in addition to the main equipment of the electrodialysis membrane. There are limitations that large facilities such as In addition, the electrodialysis method has a problem of degrading the value of the seasoning material because the important seasoning ingredients that determine the quality of seasoning foods in the desalting process together with the salt is not expanded, so the use in the food industry has not been expanded.
역삼투법은 물은 자유로이 통과하나 용질(염류 등)은 통과시키지 않는 반투막(semi-impermeable membrane)을 이용하는 방법으로, 반투막을 통과하여 물의 일부가 수용액 중으로 삼투함에 따라 수두차가 발생하고, 이러한 물의 삼투로 인한 압력보다 높은 압력(해수의 경우 50~100㎏f/㎠)을 반대편 수용액에 가하면 수용액 중의 물이 순수한 물 쪽으로 이동하게 되는 원리에 기초한 방법이다.Reverse osmosis is a method using a semi-impermeable membrane that allows water to pass freely but does not allow solutes (salts, etc.) to pass through the membrane. When a pressure higher than the pressure (50-100 kgf / cm 2 in the case of seawater) is added to the opposite aqueous solution, the water in the aqueous solution moves to pure water.
종래의 일반적인 역삼투법의 제거 대상물질로 용해성 염류, 이온성 물질 및 분자량 350 이하의 물질을 대상으로 하므로 주로 해수 담수화, 펄프 폐액 정화, 도금폐수 처리 등에 이용되고 있다. 그러나 식품 공정과 같은 부패되기 쉬운 액상 물질을 처리하는 경우에 열수 또는 약품으로 살균이 충분이 이뤄지지 않은 물질 여과 시 반투막의 오염이 불가피하여 사용이 제한적이며, 사용 수명이 비교적 짧을 뿐만 아니라, 운전 시4~10㎫의 높은 압력을 필요로 하므로 에너지 효율이 낮다. 또한 역삼투법 역시 탈염 과정에서 염분뿐만 아니라 식품의 주요 영양성분인 유리아미노산 및 맛을 좌우하는 정미성분 등이 함께 제거되므로 염분만을 선택적으로 제거하고자 하는 용도로는 적합하지 않다.It is mainly used for seawater desalination, pulp waste liquid purification, plating wastewater treatment, etc. because the target materials of the conventional reverse osmosis method are soluble salts, ionic substances and substances having a molecular weight of 350 or less. However, when handling perishable liquid substances such as food processes, semi-permeable membranes are inevitable when filtering substances that are not sufficiently sterilized by hot water or chemicals, and thus use is limited, and their service life is relatively short. Energy efficiency is low because it requires a high pressure of ˜10 MPa. In addition, the reverse osmosis method is not suitable for the purpose of selectively removing only the salinity, since not only salts but also free amino acids, which are the main nutrients of foods, and taste-determining taste-determining ingredients are removed in the desalting process.
상술한 문제점을 해결하기 위한 본 발명의 실시예들은 염도를 낮추되, 탈염 과정에서 수산계 자숙액의 주요 유용성분 및 정미성분을 손실을 방지할 수 있는 저염도 농축액의 제조방법 및 이를 이용하여 제조된 저염도 농축액과 천연 요리장을 제공하기 위한 것이다.Embodiments of the present invention for solving the above problems are low salinity, a method for preparing a low salinity concentrate that can prevent the loss of the main useful components and taste components of the fish-based cooked liquid in the desalting process and prepared using the same To provide a low salt concentrate and a natural cook.
또한, 기존 농축액 생산시설에 도입이 용이할 뿐만 아니라 설치 및 운영이 용이한 저염도 농축액의 제조방법 및 이를 이용하여 제조된 저염도 농축액과 천연 요리장을 제공하기 위한 것이다.In addition, the present invention provides a method for preparing a low salinity concentrate, which is easy to be introduced into an existing concentrate production facility and easy to install and operate, and a low salinity concentrate prepared using the same and a natural cookery.
상술한 본 발명의 목적을 달성하기 위한 본 발명의 실시예들에 따르면, 수산계 자숙액의 저염도 농축액 제조방법은, 수산계 자숙액에서 불순물을 제거하는 전처리 단계, 상기 전처리가 완료된 자숙액에 내알칼리성 단백질 분해 효소를 1종이상 투입하여 가수분해 하는 단계, 상기 가수분해가 완료된 자숙액에서 이취 성분, 분자량10,000 이상의 성분, 염분을 선택적으로 제거하는 3단 여과 처리 단계 및 상기 여과 처리가 완료된 자숙액을 농축시키는 단계를 포함하여 이루어질 수 있다.According to the embodiments of the present invention for achieving the above object of the present invention, a method for producing a low salinity concentrate of the fish-based cooked liquid, pre-treatment step to remove impurities from the fish-based cooked liquid, alkali resistance to the pre-processed cooked liquid Hydrolyzing by adding one or more proteolytic enzymes, three-stage filtration treatment step of selectively removing the off-flavor components, molecular weight of 10,000 or more components, salts from the hydrolysis-completed ripening solution and the cooked complete solution Concentration can be achieved.
여기서, 상기 3단 여과 처리 단계는, 활성탄을 이용하여 상기 자숙액에서 이취 성분을 제거하는 탈취 단계, 상기 이취 성분이 제거된 자숙액에서 한외여과막을 이용하여 분자량10,000 이상의 성분을 제거하는 단계 및 상기 분자량10,000 이상의 성분이 제거된 자숙액을 나노여과막을 통과시킴으로써 염분을 선택적으로 제거하는 단계로 이루어질 수 있다. 그리고 상기 탈취 단계는, 상기 가수분해된 자숙액에 상기 활성탄을 투입하는 단계, 상기 활성탄이 투입된 자숙액을 기설정된 시간 동안 교반시키는 단계 및 상기 교반된 자숙액을 백토층을 가압 통과시키는 단계로 이루어질 수 있다. 예를 들어, 상기 탈취 단계는 가수분해된 자숙액 내의 고형분 함량 대비 활성탄을 0.5 내지 10% w/w 투입하여 일정 시간 교반함에 따라 상기 자숙액에서 이취 성분을 제거할 수 있다. 또한, 상기 나노여과막은 스파이럴 타입의 염 저지율이 40 내지 70%인 나노여과막을 사용할 수 있다.Here, the three-stage filtration treatment step, the deodorizing step of removing the off-flavor components from the boiling water using activated carbon, the step of removing components of molecular weight 10,000 or more by using an ultrafiltration membrane from the cooked liquid from which the off-flavor component is removed and the Selective removal of the salt may be performed by passing the self-permeating liquid from which the molecular weight 10,000 or more components are removed through the nanofiltration membrane. The deodorizing step includes the step of injecting the activated carbon into the hydrolyzed porcelain solution, stirring the porcelain solution into which the activated carbon is added for a predetermined time, and pressurizing the stirred porcelain solution through the clay layer. Can be. For example, in the deodorizing step, 0.5 to 10% w / w of activated carbon relative to the solid content in the hydrolyzed self-producing solution may be added to remove the off-flavor component from the self-producing solution by stirring for a predetermined time. In addition, the nanofiltration membrane may use a nanofiltration membrane having a spiral blocking rate of 40 to 70%.
한편, 상술한 본 발명의 목적을 달성하기 위한 본 발명의 실시예들에 따르면, 수산계 자숙액을 이용하여 제조된 저염도 농축액은, 수산계 자숙액에서 이취 성분, 분자량 10,000 이상의 성분 및 염분을 선택적으로 제거하는 3단 여과 처리 및 3단 여과 처리된 자숙액을 저온 농축하여 제조될 수 있으며, 여기서, 제조된 농축액은 brix 50~55%, 염도 7% 이하로 형성될 수 있다.On the other hand, according to the embodiments of the present invention for achieving the above object of the present invention, the low salinity concentrate prepared by using a fish-based cooked liquid, selectively removes the odor component, a molecular weight of 10,000 or more components and salt in the fish-based cooked liquid The three-stage filtration process and three-stage filtration process to remove can be prepared by low-temperature concentration, wherein the prepared concentrate can be formed of brix 50 ~ 55%, salinity 7% or less.
한편, 상술한 본 발명의 목적을 달성하기 위한 본 발명의 실시예들에 따르면, 수산계 자숙액의 저염도 농축액을 이용한 천연 요리장은, 수산계 자숙액을 이용하여 제조된 저염도 농축액에 조미재료를 혼합하여 형성되며, 상기 수산계 자숙액의 저염도 농축액은 상기 수산계 자숙액에서 이취 성분, 분자량 10,000 이상의 성분 및 염분을 선택적으로 제거하는 3단 여과 처리 및 3단 여과 처리된 자숙액을 저온 농축하여 제조될 수 있다.On the other hand, according to the embodiments of the present invention for achieving the above object of the present invention, a natural cook using a low salt concentrate of the fish-based cooked liquid, mixed the seasoning material to a low salt concentrate prepared using the fish-based cooked liquid The low salinity concentrate of the fish-based cooked liquid is prepared by low-temperature concentration of a three-stage filtration treatment and a three-stage filtered cooked liquid to selectively remove the off-flavor component, the molecular weight of 10,000 or more, and salt from the fish-based cooked liquid. Can be.
이상에서 본 바와 같이, 본 발명의 실시예들에 따르면, 탈염 과정에서 자숙 액에 함유되어 있는 다량의 아미노산과 저분자 펩타이드류를 포함하는 유용성분 및 정미성분이 그대로 함유되어 있는 저염도 농축액을 제조할 수 있다.As described above, according to embodiments of the present invention, during the desalting process to prepare a low-salt concentrate containing a large amount of amino acids and low-molecular peptides contained in the cooked liquid and the essential ingredients as it is Can be.
또한, 유용성분과 정미성분들이 그대로 포함되어 있으면서 염도가 낮아 다른 조미재료와의 배합이 용이하며, 관능적 특성이 개선되어 다양한 수산계 천연 요리장의 원료로 이용 가능하다.In addition, the useful ingredients and tasteful ingredients are included as it is, the salinity is low, it is easy to mix with other seasoning ingredients, and the sensory properties are improved, it can be used as a raw material of various fishery-based natural cookery.
이하 첨부된 도면들을 참조하여 본 발명의 실시예들을 상세하게 설명하지만, 본 발명이 실시예에 의해 제한되거나 한정되는 것은 아니다. 본 발명을 설명함에 있어서, 공지된 기능 혹은 구성에 대해 구체적인 설명은 본 발명의 요지를 명료하게 하기 위하여 생략될 수 있다.DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Hereinafter, embodiments of the present invention will be described in detail with reference to the accompanying drawings, but the present invention is not limited to or limited by the embodiments. In describing the present invention, a detailed description of well-known functions or constructions may be omitted for clarity of the present invention.
이하, 도 1을 참조하여 본 발명의 일 실시예에 따른 저염도 농축액 제조방법에 대해서 상세하게 설명한다.Hereinafter, with reference to Figure 1 will be described in detail a low salt concentrate manufacturing method according to an embodiment of the present invention.
수산계 자숙액을 이용한 저염도 농축액 제조방법은, 우선, 어류나 패류 등의 수산계 재료를 일정 시간 동안 소정 온도에서 자숙(煮熟)하여 자숙액을 제조한다(S1).In the method for producing a low salinity concentrate using a fish-based cooked liquid, first, fish-based ingredients such as fish and shellfish are cooked at a predetermined temperature for a predetermined time to prepare a cooked liquid (S1).
그리고 제조된 자숙액에서 비수용성 불순물을 제거하는 전처리를 수행한다(S2).And pretreatment is performed to remove the water-insoluble impurities from the prepared cooking liquid (S2).
여기서, 자숙액은 재료가 되는 수산계 재료 자체에서 유래된 껍질, 뼈, 머리, 내장 등의 비수용성 불순물이 포함되어 있는데, 이러한 비수용성 불순물을 제 거하기 위해서 자숙액을 5~10㎛의 마이크로 필터로 여과한다.Here, the cooking solution contains water-insoluble impurities such as shells, bones, heads, and intestines derived from the fishery-based material itself, which is a material. Filter with.
다음으로, 전처리된 자숙액에 내알칼리성 단백질 분해 효소를 1종 이상 투입하여 가수분해시킨다(S3).Next, at least one alkali proteolytic enzyme is added to the pretreated cooked liquor and hydrolyzed (S3).
예를 들어, 가수 분해 단계에서는 혼합된 효소를 자숙액에 0.005 내지 0.5% w/w 투입한 후 40~60℃에서 1 내지 24 시간 동안 가수분해 시킨다. 그리고 가수분해가 완료된 자숙액 내의 효소를 실활시키기 위해 자숙액을 80~95℃에서 5~40분 동안 가온 반응시킨다.For example, in the hydrolysis step, the mixed enzyme is added to 0.005 to 0.5% w / w in the self-boiling solution and then hydrolyzed at 40 ~ 60 ℃ for 1 to 24 hours. And in order to deactivate the enzyme in the hydrolyzed complete solution, the warming solution is heated at 80-95 ° C. for 5-40 minutes.
다음으로, 가수분해가 완료된 자숙액을 3단 여과 시스템을 이용하여 이취 성분 및 분자량 10,000 이상의 성분 그리고 염분을 단계적으로 제거하여 고단백?저염도 수산계 자숙액을 형성할 수 있다.Next, a high-protein-low salted fish-based cooked liquid may be formed by gradually removing the hydrolyzed cooked liquid by using a three-stage filtration system, in which a odor component, a molecular weight of 10,000 or more, and salts are gradually removed.
여기서, 3단 여과 처리는 이취 성분을 제거하기 위한 탈취 단계(S41)와 분자량 10,000 이상의 성분의 제거 단계(S42), 그리고 염분 제거 단계(S43)로 이루어진다.Here, the three-stage filtration treatment consists of a deodorization step (S41) for removing off-flavor components, a removal step (S42) of components having a molecular weight of 10,000 or more, and a salt removal step (S43).
상세하게는, 탈취 단계(S41)는 활성탄을 이용하여 자숙액에서 이취 성분을 제거할 수 있으며, 내알칼리성 단백질 분해 효소에 의해 가수분해가 완료된 자숙액을 55~65℃로 냉각시킨 후 활성탄에 여과한다. 또한, 탈취 단계에서는 자숙액에 가수분해된 고형분 함량 대비 활성탄을 0.5~10% w/w 투입하여 10~100RPM의 속도로 5분 내지 2시간 동안 교반 반응시킨 후 백토층을 가압 통과시키는 방식으로 수행된다.In detail, the deodorizing step (S41) may remove the off-flavor components from the cooked liquor using activated charcoal, and cools the cooked liquor that has been hydrolyzed by alkaline proteolytic enzymes at 55 to 65 ° C. and then filter the activated charcoal. do. In addition, in the deodorizing step, 0.5 ~ 10% w / w of activated carbon compared to the content of the hydrolyzed solid content in the cooked liquid was stirred for 5 minutes to 2 hours at a rate of 10 ~ 100RPM and then carried out by pressing through the clay layer do.
그리고 분자량 10,000 이상의 성분의 제거(S42) 단계에서는 활성탄 여과 처 리가 완료된 자숙액을 한외여과막(Ultrafiltration membrane, UF membrane)을 가압 통과시킴으로써 자숙액 내에서 분자량 10,000 이상의 가수분해물을 제거할 수 있다.In the step of removing components having a molecular weight of 10,000 or more (S42), hydrolyzate having a molecular weight of 10,000 or more can be removed from the cooked liquid by pressurizing an ultrafiltration membrane (Ultrafiltration membrane, UF membrane).
그리고 염분 제거(S43) 단계에서는 한외여과막을 통과하여 분자량 10,000 이상의 성분이 제거된 자숙액을 나노여과막을 통과시킴으로써 염분을 선택적으로 제거할 수 있다. 예를 들어, 나노여과막은 스파이럴 타입으로 염 저지율이 40~70%인 여과막을 사용할 수 있다.In the salt removal step (S43), salts may be selectively removed by passing the self-filtration solution through which the molecular weight of 10,000 or more is removed and passed through the nanofiltration membrane through the ultrafiltration membrane. For example, the nanofiltration membrane is a spiral type and may use a filtration membrane having a salt blocking rate of 40 to 70%.
다음으로, 3단 여과 처리가 완료된 자숙액을 저온 농축하여 고단백?저염도 농축액을 제조할 수 있다(S5).Next, a high-protein-low-salt concentrate can be prepared by concentrating the cooked liquid in which the three-stage filtration process is completed at low temperature (S5).
여기서, 상기와 같이 3단 여과 처리가 완료된 자숙액을 ATAGO 굴절계를 이용하여 자숙액의 고형분 함유량과 염도를 측정하여 고형분 함유량 및 염도가 brix 50~65%가 되도록 저온에서 농축시킬 수 있다.Here, the three-stage filtration process as described above can be concentrated at a low temperature so that the solid content and salinity of brix 50 to 65% by measuring the solid content and salinity of the self-adhesive solution using an ATAGO refractometer.
그리고 상술한 바와 같이 제조된 저염도 농축액에 기타 조미재료를 혼합하여(S6) 천연 요리장을 제조할 수 있다.In addition, other seasoning materials may be mixed with the low salt concentrate prepared as described above (S6) to prepare a natural cook.
이하에서는, 상술한 본 발명의 일 실시예에 따른 저염도 농축액 제조방법에 따라 제조된 저염도 농축액 및 이러한 저염도 농축액을 이용하여 제조된 천연 요리장의 예들을 설명한다.Hereinafter, examples of the low salinity concentrate prepared according to the low salinity concentrate preparation method according to the embodiment of the present invention described above and examples of a natural cooker prepared using the low salt concentrate are described.
[실시예 1]Example 1
참치를 이용하여 저염도 농축액을 제조하였다.A low salt concentrate was prepared using tuna.
참치의 저염도 농축액은, 참치를 90℃에서 30분 내지 1시간 자숙하여 얻은 참치 자숙액을 5~10㎛의 마이크로 필터로 여과하여 비수용성 불순물을 제거한 후, 내알칼리성 단백질 분해 효소를 1종 이상 혼합하여 참치 자숙액 대비 0.005~0.2% w/w 투입하고, 45~55℃에서 2 내지 4시간 가수분해시킨다. 그리고 가수분해된 참치 자숙액의 고형분 함량 대비 활성탄을 1~5% w/w 투입하여 반응시키고 백토층을 가압 통과시킨 후 한외 여과막으로 분자량 10,000 이상의 가수분해물을 제거한다. 그리고 가수분해물이 제거된 참치 자숙액을 brix 5% w/w이하로 희석하기 위해 정제수를 2~5배 v/v 투입한 후 탈염율 40% 이상의 스파이럴형 나노여과막을 통과시켜 염도 0.3% 이하의 저염도 참치 자숙액을 제조할 수 있다. 그리고 염분이 0.3% 이하인 저염도 참지 자숙액을 저온 농축하여 brix 50~55%, 염도 7% 이하의 저염도 참치 농축액을 제조하였다.The low salinity concentrate of tuna is one or more kinds of alkaline proteolytic enzymes after filtering the tuna cooked broth obtained by boiling the tuna at 90 ° C. for 30 minutes to 1 hour using a 5-10 μm microfilter to remove water-insoluble impurities. Mix 0.005 ~ 0.2% w / w compared to the tuna cooked liquid, and hydrolyzed for 2 to 4 hours at 45 ~ 55 ℃. In addition, 1 to 5% w / w of activated carbon is added to the solid content of the hydrolyzed tuna cooked liquid and reacted. After passing through the clay layer, the hydrolyzate having a molecular weight of 10,000 or more is removed by an ultrafiltration membrane. In order to dilute the hydrolyzate-treated tuna cooked liquor to brix 5% w / w or less, purified water was added 2-5 times v / v and passed through a spiral nanofiltration membrane with a desalination rate of 40% or more. Low-salt tuna cooked liquid can be prepared. And low salt tuna concentration of less than 0.3% salinity of low-temperature tuna concentrate was prepared by brix 50 ~ 55%, low salt tuna concentration of less than 7% salinity.
그리고 이와 같이 제조된 저염도 참지 농축액을 이용하여 기타 조미재료와 [표 1]에 기재한 바와 같이 혼합하여 천연 참치 요리장을 제조하였다.And using the low salt sesame concentrate prepared as described above and mixed with other seasoning ingredients as described in Table 1 to prepare a natural tuna cook.
(멸치:버섯:다시마=10:1:1)Comprehensive Extract
(Anchovy: mushroom: Tashima = 10: 1: 1)
[실시예 2][Example 2]
상술한 바와 같이 제조된 저염도 참치 농축액의 성분 분석 결과는 아래 [표 2]와 같다. 표 2를 참조하면, 저염도 참지 농축액은 기존의 통상적으로 판매 및 거래되고 있는 참치 농축액 대비 염도가 약 40~50% 낮으며, 조단백이 1.25배 높Component analysis of the low salt tuna concentrate prepared as described above is shown in Table 2 below. Referring to Table 2, the low salinity tuna concentrate is about 40-50% lower in salinity and 1.25 times higher crude protein than conventional tuna concentrates sold and traded.
음을 알 수 있었다. 또한, 유리아미노산을 분석한 결과 단맛 성분(Pro, Ala, Gly, Ser)은 약 2배 증가, 감칠맛과 신맛(asp, glu) 성분은 약 1.8배 증가하였으며, 필수아미노산(10종)은 약 1.3배 증가하였음을 알 수 있었다.I could see that. In addition, as a result of analyzing the free amino acid, sweet components (Pro, Ala, Gly, Ser) increased about 2 times, umami and sour (asp, glu) components increased about 1.8 times, essential amino acids (10 species) about 1.3 It can be seen that the fold increased.
[실시예3]Example 3
상술한 실시예 1과 유사하게, 굴을 이용하여 이용하여 저염도 농축액을 제조하였다.Similar to Example 1 described above, a low salt concentrate was prepared using oysters.
굴을 90℃에서 10 내지 30분간 자숙하여 얻은 굴 자숙액을 5~10㎛의 마이크로 필터로 여과하여 비수용성 불순물을 제거한 후, 내알칼리성 단백질 분해 효소를 1종 이상 혼합하여 굴 자숙액 대비 0.005~0.2% w/w 투입하여 45~55℃ 에서 2 내지 4시간 가수분해시킨다. 그리고 가수분해된 굴 자숙액의 고형분 함량 대비 활성탄을 0.5~1% w/w 투입하여 반응시키고 백토층을 가압 통과시킨 후, 한외여과막으로 분자량 10,000 이상의 가수분해물을 제거한다. 그리고 가수분해물이 제거된 굴 자숙액에 정제수를 2~5배 v/v 투입하여 brix 5% w/w 이하로 희석하고, 탈염율 40% 이상의 스파이럴형 나노여과막을 통과시켜, 염도 0.3% 이하의 저염도 굴 자숙액을 얻는다. 그리고 염분이 0.3% 이하인 굴 자숙액을 저온 농축하여 brix 50~55%, 염도 7% 이하의 저염도 굴 농축액을 제조할 수 있다.The oyster cooked liquor, which had been cooked at 90 ° C. for 10 to 30 minutes, was filtered through a micro filter of 5 to 10 μm to remove non-aqueous impurities, and then mixed with at least one alkaline proteolytic enzyme, 0.005 ~ 0.2% w / w is added and hydrolyzed at 45 to 55 ° C for 2 to 4 hours. Then, 0.5 to 1% w / w of activated carbon relative to the solids content of the hydrolyzed oyster cooked solution was reacted and passed through a white clay layer, followed by removing the hydrolyzate having a molecular weight of 10,000 or more by an ultrafiltration membrane. Purified water was added 2-5 times v / v to the hydrolyzate-removed oyster cooked water, diluted to brix 5% w / w or less, and passed through a spiral nanofiltration membrane with a desalination rate of 40% or more. Get low salt oyster cooked liquid. In addition, low-temperature oyster cooked liquor with less than 0.3% salinity can be prepared at low salt oyster concentrates with brix 50-55% and salinity below 7%.
그리고 이와 같이 제조된 저염도 굴 농축액을 이용하여 기타 조미재료와 아래 [표 3]에 기재한 바와 같이 혼합하여 천연 굴 요리장을 제조하였다.And using the low-salt oyster concentrate prepared as described above and mixed with other seasoning ingredients as described in Table 3 below to prepare a natural oyster cooking.
본 실시예들에 따르면, 수산계 자숙액에서 염분을 제거하여 저염도 농축액을 형성할 수 있는데, 제조 과정에서 자숙액에 함유되어 있는 아미노산과 저분자 펩타이드류를 포함하는 유용성분 그대로 함유되어 있는 고단백 농축액을 제조할 수 있다. 또한, 탈염 과정에서 자숙액의 정미 성분들이 제거되지 않고 그대로 함유되어 있어 관능적으로도 우수함을 알 수 있었다. 또한, 농축액의 염도가 낮아서 다른 조미재료와 배합이 용이하여 다양한 천연 요리장을 제조할 수 있다.According to the present embodiments, the salt can be removed from the fish-based cooked liquid to form a low salt concentrate. A high protein concentrate containing the useful components including amino acids and low-molecular peptides contained in the cooked liquid during the manufacturing process is intact. It can manufacture. In addition, in the desalting process, the taste components of the cooked water were not removed but were found to be excellent sensory. In addition, since the salinity of the concentrate is low, it is easy to mix with other seasonings, and thus various natural cooks can be prepared.
이상과 같이 본 발명에서는 구체적인 구성 요소 등과 같은 특정 사항들과 한정된 실시예 및 도면에 의해 설명되었으나 이는 본 발명의 보다 전반적인 이해를 돕기 위해서 제공된 것일 뿐, 본 발명은 상술한 실시예들에 한정되는 것은 아니며, 본 발명이 속하는 분야에서 통상적인 지식을 가진 자라면 이러한 기재로부터 다양한 수정 및 변형이 가능하다. 따라서, 본 발명의 사상은 상술한 실시예에 국한되어 정해져서는 아니 되며, 후술하는 특허청구범위뿐 아니라 특허청구범위와 균등하거나 등가적 변형이 있는 모든 것들은 본 발명 사상의 범주에 속한다고 할 것이다.As described above, the present invention has been described by specific embodiments such as specific components and the like, but the embodiments and the drawings are provided only to help a more general understanding of the present invention, and the present invention is limited to the above-described embodiments. In other words, various modifications and variations are possible to those skilled in the art to which the present invention pertains. Therefore, the spirit of the present invention should not be limited to the above-described embodiments, and all the things that are equivalent to or equivalent to the scope of the claims as well as the claims to be described later belong to the scope of the present invention.
도 1은 본 발명의 일 실시예에 따른 수산계 자숙액의 저염도 농축액 제조방법 및 천연 요리장의 제조방법을 설명하기 위한 순서도이다.1 is a flow chart illustrating a method for producing a low salinity concentrate of a fish-based cooked liquid and a method of producing a natural cooker according to an embodiment of the present invention.
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KR20180092347A (en) * | 2017-02-09 | 2018-08-20 | 인제대학교 산학협력단 | Manufacturing method of fermented seefood liquified sauce improved flavor and reduced sodium |
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KR20180092347A (en) * | 2017-02-09 | 2018-08-20 | 인제대학교 산학협력단 | Manufacturing method of fermented seefood liquified sauce improved flavor and reduced sodium |
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