JP2006320320A5 - - Google Patents
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- JP2006320320A5 JP2006320320A5 JP2006119090A JP2006119090A JP2006320320A5 JP 2006320320 A5 JP2006320320 A5 JP 2006320320A5 JP 2006119090 A JP2006119090 A JP 2006119090A JP 2006119090 A JP2006119090 A JP 2006119090A JP 2006320320 A5 JP2006320320 A5 JP 2006320320A5
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本発明の他の目的は、海藻類を原料として、廃棄物の少ない海藻熱処理組成物の製造方法を提供することである。本発明の製造方法により得られた海藻熱処理組成物を使用した、調味料、食品、健康食品を提供することを目的とする。 Another object of the present invention is to provide a method for producing a seaweed heat-treating composition with less waste using seaweed as a raw material. It aims at providing a seasoning, a foodstuff, and a health food using the seaweed heat-treatment composition obtained by the manufacturing method of the present invention.
また、105〜200℃で加熱処理を行う前に、海藻類を、pH1〜13の水性媒体中で30〜100℃にて加熱すること(以下、「可溶化処理」ともいう。)も好ましい実施態様である。可溶化処理を行うことにより、海藻類が膨潤及び/又は可溶化されるので、このような可溶化処理を加圧加熱処理前に行うことにより、加熱処理溶液が均一化され、再現性の良い海藻高温抽出組成物が得られ、さらに可溶性成分の収率が向上するので好ましい。以下、可溶化処理を行った後、加圧加熱処理を行う実施態様を「二段階加熱処理」ともいうこととする。
海藻類は室温で水性媒体中に溶解しようとしても、完全に溶解しない。加圧加熱処理前に微粉末状にした海藻類を可溶化することにより、加熱処理溶液が均一化され、品質にばらつきの少ない海藻高温抽出組成物を製造することができるので更に好ましい。
In addition, heating the seaweed at 30 to 100 ° C. in an aqueous medium having a pH of 1 to 13 (hereinafter, also referred to as “solubilization treatment”) before performing the heat treatment at 105 to 200 ° C. is also preferable. It is an aspect. Since the seaweed swells and / or is solubilized by performing the solubilization treatment, by performing such a solubilization treatment before the pressure heat treatment, the heat treatment solution is made uniform and reproducible. A seaweed high temperature extraction composition is obtained, and the yield of soluble components is further improved, which is preferable. Hereinafter, the embodiment in which the pressure heat treatment is performed after the solubilization treatment is referred to as “two-stage heat treatment”.
Seaweeds do not dissolve completely when trying to dissolve in an aqueous medium at room temperature. By solubilizing the microalgae seaweeds prior to the pressure heat treatment, the heat treatment solution can be made uniform, and a seaweed high-temperature extract composition with little variation in quality can be produced.
海藻類の高温抽出組成物はその機能が注目されている。特に、本発明の製造方法では、海藻類を加水分解反応を伴う加熱処理をするため、海藻類に含まれる多糖類が少糖化及び/又はオリゴ糖化し、さらにタンパク質をオリゴペプチド化、またはオリゴペプチドからさらにアミノ酸まで加水分解すると考えられる。本発明により得られた海藻高温抽出組成物は、抗ガン作用、免疫力増強作用、または血圧降下作用を含む各種の生理機能(生理活性)を有していると期待され、また、増粘性、保湿性やゲル化性等のような物理化学的機能の向上に寄与するものである。本発明により得られた海藻高温抽出組成物は、上述の用途には限られず、食品、化粧品、医薬品、繊維加工品等の幅広い製品への用途を有するものである。さらに、原料である海藻類から、高温抽出組成物を得た後の固形分(残渣)は、食物繊維、ペプチド、多糖類等を多く含むことから、家畜飼料及び園芸肥料等に応用して効果的に使用することが可能である。
尚、本発明において、多糖とは多くの単糖から構成される平均分子量が100,000を超える糖類を指す。少糖とは、オリゴ糖と同義であって、単糖が複数個結合したものであり、分子量が100,000を超えないものを指す。
The high temperature extraction composition of seaweed has attracted attention for its function. In particular, in the production method of the present invention, the seaweed is subjected to a heat treatment accompanied by a hydrolysis reaction. To further amino acids. The seaweed high-temperature extract composition obtained by the present invention is expected to have various physiological functions (physiological activities) including an anti-cancer action, an immunity enhancing action, or a blood pressure lowering action. It contributes to the improvement of physicochemical functions such as moisture retention and gelation. The seaweed high-temperature extract composition obtained according to the present invention is not limited to the above-described uses, and has a wide range of uses such as foods, cosmetics, pharmaceuticals, and processed textiles. Furthermore, the solid content (residue) after obtaining the high-temperature extraction composition from the raw seaweed contains a lot of dietary fiber, peptides, polysaccharides, etc., so it is effective when applied to livestock feed and horticultural fertilizers. Can be used.
In the present invention, the polysaccharide refers to a saccharide having an average molecular weight exceeding 100,000, which is composed of many monosaccharides. The oligosaccharide is synonymous with an oligosaccharide, and is a combination of a plurality of monosaccharides and a molecular weight not exceeding 100,000.
<加熱処理後の操作>
加熱処理後は直ちに圧力容器内の冷却水循環用配管バルブを開け、水道水を通じることで冷却を行った。室温まで冷却後、処理装置の圧力を開放した。
加熱処理を行った処理溶液は遠心器((株)コクサン社製、H−103Fn)で3000rpmの条件下で30分間回転させることで固・液分離を行った。
<Operation after heat treatment>
Immediately after the heat treatment, the cooling water circulation piping valve in the pressure vessel was opened and cooling was performed by passing tap water. After cooling to room temperature, the processing apparatus pressure was released.
The heat-treated treatment solution was subjected to solid / liquid separation by rotating for 30 minutes at 3000 rpm in a centrifuge (manufactured by Kokusan Co., Ltd., H-103Fn).
(実施例6)
(血圧降圧剤としての効果の評価)
<錠剤化処理>
昆布の高温抽出組成物を含む昆布熱処理組成物(以後、まるごと昆布と略す)は、日常的に簡単に摂取することが必要であるため、昆布の高温抽出組成物を含む加熱処理物に対し、錠剤化処理を行った。また、加熱処理を行っていない昆布粉末に対しても錠剤化処理を行った。
錠剤の製造方法を以下に記載する。昆布の原材料は北海道日浦産乾コンブ(利尻系エナガオニコンブ)を用いた。まるごと昆布錠剤および昆布粉末錠剤の製造では、初めに昆布原料を50℃で15時間乾燥し、マキノ式ピンミルで2回粉砕し、粉末試料を作製した。
昆布粉末の二酸化炭素を使用した加水分解を伴う熱処理は、容量10Lのテフロン(登録商標)ライニングのオートクレーブ装置を用いて行った。一回の反応での仕込量は、昆布粉末を600gに水6,000gとした。仕込み後、反応容器はスティーム加熱により30℃まで昇温させ、0.30MPaになるまで二酸化炭素を反応容器内に圧入した。オートクレーブの内圧が0.30MPaで平衡であることを確認後、80℃まで昇温し1時間保温した。つづけて、反応温度を120℃とし、2時間加温を行った。反応終了後直ちに冷却水を循環させオートクレーブ内の温度が30℃以下になるまで冷却を行った。加熱処理物を、コロイドミルを用いて湿式粉砕し、さらに乾燥させることで、粉末の昆布加熱処理物とした。
粉末の昆布熱処理組成物(まるごと昆布)および昆布粉末を用いた造粒行程では、各粉末2100gにマルチトール(アマルティMR−50)を2058g加え、混合攪拌後70%エタノールを1055ml添加し乾燥後、乾燥混合造粒粉末試料を作製した。打錠工程では、上記乾燥混合造粒粉末試料が99%に対し、潤沢剤としてシュガーエステル(DSKF20W)が1%となるように添加し、十分に混合した後、8mmφ、210mgの打錠型を用いて打錠し、試験用錠剤とした。
(Example 6)
(Evaluation of the effect of the blood pressure antihypertensive agent)
<Tablet processing>
The kelp heat treatment composition containing the kelp high-temperature extract composition (hereinafter abbreviated as whole kelp) needs to be easily ingested on a daily basis. Tableting process was performed. Moreover, the tableting process was performed also to the kelp powder which has not been heat-processed.
The manufacturing method of a tablet is described below. The raw material for the kelp used was Hipu from Hokkaido (Rishiri-type Enagaoni Kombu). In the manufacture of whole kelp tablets and kelp powder tablets, the kelp raw material was first dried at 50 ° C. for 15 hours, and pulverized twice with a Makino pin mill to prepare powder samples.
The heat treatment with hydrolysis of the kelp powder using carbon dioxide was performed using an autoclave apparatus of Teflon (registered trademark) lining having a capacity of 10 L. The amount charged in one reaction was 600 g of kelp powder and 6,000 g of water. After charging, the reaction vessel was warmed to 30 ° C. by Steam heating was injected carbon dioxide to the reaction vessel until 0.30 MPa. After confirming that the internal pressure of the autoclave was 0.30 MPa and being in equilibrium, the temperature was raised to 80 ° C. and kept for 1 hour. Subsequently, the reaction temperature was 120 ° C. and heating was performed for 2 hours. Immediately after the completion of the reaction, cooling water was circulated to cool the autoclave until the temperature in the autoclave reached 30 ° C or lower. The heat-treated product was wet pulverized using a colloid mill and further dried to obtain a powdered kelp heat-treated product.
In the granulation process using the powder kelp heat treatment composition (whole kelp) and kelp powder, 2058 g of maltitol (Amalty MR-50) was added to 2100 g of each powder, and after mixing and stirring, 1055 ml of 70% ethanol was added and dried. A dry mixed granulated powder sample was prepared. In the tableting process, the dry mixed granulated powder sample was added to 99% of sugar ester (DSKF20W) as a lubricant, and mixed sufficiently. Then, a tableting mold of 8 mmφ, 210 mg was prepared. Tablets were used for testing.
Claims (27)
二酸化炭素の共存する水性媒体中で、
温度105〜200℃、圧力0.10〜5MPaにおいて加熱処理する工程を含むことを特徴とする
海藻高温抽出組成物の製造方法。 Seaweed
In an aqueous medium in which carbon dioxide coexists,
The manufacturing method of the seaweed high temperature extraction composition characterized by including the process heat-processed in the temperature of 105-200 degreeC and the pressure of 0.10-5 Mpa .
温度110〜130℃において0.5〜5時間加熱処理する工程を含むことを特徴とする
海藻高温抽出組成物の製造方法。 A step of saturating carbon dioxide in an aqueous medium in which seaweed is dispersed at a temperature of 20 to 40 ° C. and a pressure of 0.1 to 0.5 MPa; and
The manufacturing method of the seaweed high temperature extraction composition characterized by including the process of heat-processing at the temperature of 110-130 degreeC for 0.5 to 5 hours.
二酸化炭素の共存する水性媒体中で、
温度50〜200℃、圧力が常圧〜5MPaにおいて加熱処理する工程を含むことを特徴とする
海藻熱処理組成物の製造方法。 Seaweed
In an aqueous medium in which carbon dioxide coexists,
A method for producing a seaweed heat treatment composition, comprising a step of heat treatment at a temperature of 50 to 200 ° C. and a pressure of normal pressure to 5 MPa .
温度80〜180℃において0.5〜5時間加熱処理する工程を含むことを特徴とする
海藻熱処理組成物の製造方法。 Injecting carbon dioxide into an aqueous medium in which seaweed is dispersed at a temperature of 20 to 40 ° C. and a pressure of 0.1 to 0.5 MPa; and
The manufacturing method of the seaweed heat treatment composition characterized by including the process of heat-processing at the temperature of 80-180 degreeC for 0.5 to 5 hours.
Priority Applications (1)
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JP2006119090A JP4431711B2 (en) | 2005-04-22 | 2006-04-24 | Seaweed high temperature extraction composition, seaweed heat treatment composition and production method thereof, and seasoning, cosmetic, food and health food containing seaweed high temperature extraction composition or seaweed heat treatment composition |
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JP2006119090A JP4431711B2 (en) | 2005-04-22 | 2006-04-24 | Seaweed high temperature extraction composition, seaweed heat treatment composition and production method thereof, and seasoning, cosmetic, food and health food containing seaweed high temperature extraction composition or seaweed heat treatment composition |
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JP2006320320A JP2006320320A (en) | 2006-11-30 |
JP2006320320A5 true JP2006320320A5 (en) | 2009-06-04 |
JP4431711B2 JP4431711B2 (en) | 2010-03-17 |
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JP2008105985A (en) * | 2006-10-25 | 2008-05-08 | Nicca Chemical Co Ltd | Hyaluronic acid production promoter, skin care preparation for external use, bathing agent, and food and drink |
JP2009149734A (en) * | 2007-12-19 | 2009-07-09 | Kao Corp | Production method for alginic acid of low molecular weight or derivative thereof |
JP2009225791A (en) * | 2008-02-29 | 2009-10-08 | Takara Bio Inc | Seaweed extract and method for producing the same |
JP5939605B2 (en) * | 2011-07-12 | 2016-06-22 | 株式会社Mizkan Holdings | Method for producing composition containing kombu extract, composition containing kombu extract produced by the method, and food containing the composition containing kombu extract |
US20140242109A1 (en) | 2011-09-09 | 2014-08-28 | Kaneka Corporation | Method for cultivating alga and method for producing alginic acid-containing composition |
JP2014136678A (en) * | 2013-01-15 | 2014-07-28 | Kaigen Pharma Co Ltd | Moisturizing cosmetic material and production method thereof |
JP6312074B2 (en) * | 2013-08-09 | 2018-04-18 | 学校法人明治大学 | Insulin resistance reducing food and insulin resistance reducing drug |
JP6320553B2 (en) * | 2014-10-23 | 2018-05-09 | 長谷川香料株式会社 | Taste improving agent for food and drink |
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JP7008324B2 (en) * | 2016-10-24 | 2022-02-10 | 奥野製薬工業株式会社 | Bile acid adsorbent and adiponectin secretagogue |
CN107494699B (en) * | 2017-07-05 | 2020-11-27 | 福州大学 | Biological preservative based on alginate oligosaccharides and application of biological preservative in prawn preservation |
JP7217499B2 (en) * | 2018-09-28 | 2023-02-03 | 焼津水産化学工業株式会社 | Kelp extract and method for producing the same, seasoning containing kelp extract, method for improving flavor of food and drink |
CN110714046B (en) * | 2019-11-22 | 2021-06-04 | 浙江丰安生物制药有限公司 | Preparation method of polypeptide for hydrolyzing pork protein of suckling pig |
WO2023112974A1 (en) * | 2021-12-14 | 2023-06-22 | シード医療製薬株式会社 | Hypertension-improving agent containing seaweed extract, and functional food, quasi-drug and drug containing hypertension-improving agent |
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2006
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