JP4845630B2 - Method for producing knots extract - Google Patents

Method for producing knots extract Download PDF

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JP4845630B2
JP4845630B2 JP2006213099A JP2006213099A JP4845630B2 JP 4845630 B2 JP4845630 B2 JP 4845630B2 JP 2006213099 A JP2006213099 A JP 2006213099A JP 2006213099 A JP2006213099 A JP 2006213099A JP 4845630 B2 JP4845630 B2 JP 4845630B2
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extraction solvent
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潤 山田
秀喜 松田
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Yaizu Suisan Kagaku Kogyo Co Ltd
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Description

本発明は、節類エキスの製造方法に関する。   The present invention relates to a method for producing knotweed extract.

鰹節等の節類や、昆布等の海藻類から得られるだしは、めんつゆや煮物等の和食のベース調味料として広く使用されており、このようなだしを配合した様々な調味料や加工食品が数多く出回っている。   Dashi obtained from bonito and other seaweeds and seaweed such as kelp is widely used as a base seasoning for Japanese foods such as noodle soup and boiled food. Various seasonings and processed foods containing such dashi are available. Many are on the market.

工業スケールで、鰹節等の節類や、昆布等の海藻類から得られるだしの製造を行う方法としては、抽出原料となる節類及び/又は海藻類を抽出溶媒とともにタンクに入れ、これらを適宜撹拌しながらエキスの抽出を行うバッチ式抽出法や、抽出原料を充填したカラムに抽出溶媒を通液してエキスの抽出を行うカラム式抽出法等が知られている。また、アルコール易溶性の香気成分、呈味成分等を効率よく抽出する目的で、抽出溶媒としてアルコール又はアルコール含有水を用いることも行われている。   On the industrial scale, as a method of producing soup stock obtained from bonito and other seaweeds and seaweeds such as kelp, put the moss and / or seaweed used as the extraction raw material in a tank together with the extraction solvent, A batch type extraction method for extracting an extract while stirring, a column type extraction method for extracting an extract by passing an extraction solvent through a column filled with extraction raw materials, and the like are known. In addition, alcohol or alcohol-containing water is also used as an extraction solvent for the purpose of efficiently extracting alcohol-soluble aromatic components, taste components, and the like.

一般に、バッチ式抽出法では、比較的多量の抽出溶媒に抽出原料が長時間浸される状態とされるので、抽出中に風味の劣化が起こり、風味に富んだ抽出エキスを得る方法としては適さなかった。また、得られる抽出エキスの固形分濃度も5%以下と低いものとなり、そのためこれを濃縮する工程によってもエキスの香気成分等が失われ、風味を損ねるという問題があった。   In general, in the batch extraction method, the extraction raw material is immersed in a relatively large amount of extraction solvent for a long period of time, so that flavor deterioration occurs during extraction, which is suitable as a method for obtaining an extract extract rich in flavor. There wasn't. In addition, the solid content concentration of the obtained extract is as low as 5% or less, and therefore, there is a problem that the flavor component of the extract is lost and the flavor is impaired even in the step of concentrating the extract.

一方、カラム式抽出法は、バッチ式抽出法に比べて比較的少量の抽出溶媒で抽出することができるので、香気成分、呈味成分等を高濃度に含む抽出エキスを得ることに適している。   On the other hand, the column-type extraction method can be extracted with a relatively small amount of extraction solvent as compared with the batch-type extraction method, and is therefore suitable for obtaining an extract containing a high concentration of aroma components and taste components. .

例えば、下記特許文献1には、カラム式抽出法を用いたエキスの製造方法として、予め節からアルコール抽出して得られた節のアルコール抽出液を抽出溶媒として用いて、カラムに別途充填した節から抽出を行う工程と、前記工程で得られたカラム抽出液から20〜40℃の温度条件下でアルコールを除去する工程とを含むことを特徴とする節エキスの製造方法が開示されている。また、下記特許文献2には、粗砕した節をカラムに充填し、水又はアルコール溶液を通液してエキスを抽出する工程と、さらに蛋白分解酵素液を通液してエキスを抽出する工程を有することを特徴とする風味だしの製造法が開示されている。
特開2002−281933号公報 特開2000−279124号公報
For example, in Patent Document 1 below, as a method for producing an extract using a column-type extraction method, a knot alcohol that has been separately packed in a column is obtained by using a knot alcohol extract obtained by kneading alcohol from knots in advance as an extraction solvent. And a step of removing alcohol from the column extract obtained in the above step under a temperature condition of 20 to 40 ° C. is disclosed. Patent Document 2 listed below includes a step of filling a column with coarsely crushed nodes, extracting an extract by passing water or an alcohol solution, and further extracting a extract by passing a protease solution. There is disclosed a method for producing a flavor dashi characterized by having
JP 2002-281933 A JP 2000-279124 A

しかしながら、従来のカラム式抽出法は、香気成分、呈味成分等を高濃度に含む抽出エキスを得ることができるものの、原料に由来する臭み、苦味等の成分も一緒に抽出されるので、これらの成分によって抽出エキスの風味、呈味のバランスを損ねるという問題があった。また、節類の粉砕物等でカラム状に形成された抽出原料の充填層は、物理的に不均一であるので、その充填層から抽出される香気成分、呈味成分等の均質性を保つことが難しかった。   However, although the conventional column extraction method can obtain an extract extract containing aroma components, taste components, etc. at high concentrations, components such as odor and bitterness derived from the raw materials are also extracted together. There was a problem that the balance of the flavor and taste of the extracted extract was impaired by the components. In addition, the packed bed of extraction raw material formed in a column shape with pulverized pulverized material etc. is physically non-uniform, so the aroma components and taste components extracted from the packed layer are kept homogeneous. It was difficult.

したがって、本発明の目的は、カラム式抽出法による節類エキスの製造方法おいて、節類のもつ香気成分及び呈味成分を充分、かつ効率よく抽出する新たな方法を提供し、風味に富んだ節類エキスを安定に供給できる節類エキスの製造方法を提供することにある。   Accordingly, an object of the present invention is to provide a new method for extracting aroma components and taste components of nodules sufficiently and efficiently in a method for producing nodules extract by column-type extraction method, which is rich in flavor. An object of the present invention is to provide a method for producing a nodular extract that can stably supply the nodular extract.

上記目的を達成するため、本発明の節類エキスの製造方法は、受け面にフィルターを備えた容器に節類を充填し、前記容器内に形成された節類の充填層のカラムベッド面にシャワー状、噴霧状、及び/又は液滴状にした抽出溶媒を滴下して、前記充填層のカラムベッド面に前記抽出溶媒が液溜めされない状態で、前記充填層に前記抽出溶媒を通液することを特徴とする。 In order to achieve the above object, the method for producing a nodular extract of the present invention includes filling a nodule into a container having a filter on the receiving surface, and applying the nodule packed bed formed in the container to the column bed surface. The extraction solvent in the form of shower, spray, and / or droplets is dropped , and the extraction solvent is passed through the packed bed in a state where the extraction solvent is not stored on the column bed surface of the packed bed. It is characterized by that.

本発明によれば、原料節類で形成された充填層のカラムベッド面に抽出溶媒が液溜めされない状態で通液するので、前記充填層が余分な抽出溶媒を含み膨潤して、物理的及び/又は化学的に劣化することを防ぐことができる。これにより、抽出過程中、前記充填層を形成する原料節類からの良好な抽出状態を保つことができ、風味、呈味のバランスを損ねる成分が抽出されることを抑制することができる。また、余分な抽出溶媒の圧力によって、前記充填層に不均一な移動相の通り道が形成されることを防ぎ、抽出溶媒を均一に分散させつつ通液させることができるので、節類のもつ香気成分及び呈味成分を充分、かつ効率よく抽出することができる。
また、シャワー状、噴霧状、及び/又は液滴状にした前記抽出溶媒を前記充填層のカラムベッド面に滴下するので、前記充填層のカラムベッド面の全面に行き渡るように抽出溶媒を均一に滴下することができる。
According to the present invention, since the extraction solvent passes through the column bed surface of the packed bed formed of the raw material paste without being pooled, the packed bed swells containing excess extraction solvent, It is possible to prevent chemical degradation. Thereby, it is possible to maintain a good extraction state from the raw material knot forming the packed bed during the extraction process, and to suppress the extraction of components that impair the balance between flavor and taste. In addition, it is possible to prevent the formation of a non-uniform path for the mobile phase in the packed bed due to the pressure of the excess extraction solvent, and to allow the extraction solvent to pass through while being uniformly dispersed. Ingredients and taste ingredients can be extracted sufficiently and efficiently.
Further, since the extraction solvent in the form of shower, spray, and / or droplets is dropped on the column bed surface of the packed bed, the extraction solvent is uniformly distributed so as to reach the entire surface of the packed bed. Can be dripped.

本発明においては、前記節類の粒度が、3〜32メッシュパスであることが好ましい。これによれば、節類の表面から香気成分及び呈味成分等が抽出されるので、抽出効率がよい。また、滴下された抽出溶媒が前記充填層に浸透する速度を一定範囲の速度に保つことができるので、作業性がよい。   In the present invention, the particle size of the nodules is preferably 3 to 32 mesh passes. According to this, since an aroma component, a taste component, etc. are extracted from the surface of knots, extraction efficiency is good. Moreover, since the speed | rate which the dripped extraction solvent osmose | permeates the said packed bed can be kept in the speed of a fixed range, workability | operativity is good.

本発明においては、前記抽出溶媒をノズルから滴下し該ノズルが回転するようにしてシャワー状、噴霧状、及び/又は液滴状に滴下することが好ましい。 In the present invention, a shower shape as the nozzle is dropped the extraction solvent from the nozzle is rotated, aerosolized, and / or it is preferable to lower drops Ekishizukujo.

本発明においては、前記抽出溶媒を前記充填層の断面積に対して410リットル/h・m以下の流量速度で滴下することが好ましい。これによれば、抽出溶媒が滴下される前記充填層のカラムベッド面に前記抽出溶媒が液溜めされない状態で、抽出溶媒の通液を行うことができる。 In the present invention, the extraction solvent is preferably added dropwise at a flow rate of 410 liters / h · m 2 or less with respect to the cross-sectional area of the packed bed. According to this, the extraction solvent can be passed in a state where the extraction solvent is not stored on the column bed surface of the packed bed onto which the extraction solvent is dropped.

本発明においては、前記充填層の高さが、30〜60cmであることが好ましい。これによれば、滴下された抽出溶媒が前記充填層に浸透する速度を一定範囲の速度に保つことができるので、作業性がよい。   In the present invention, the height of the packed bed is preferably 30 to 60 cm. According to this, since the speed | rate which the dripped extraction solvent osmose | permeates the said packed bed can be maintained to the speed | rate of a fixed range, workability | operativity is good.

本発明においては、前記抽出溶媒がエタノール含有水であることが好ましい。これによれば、アルコール溶解性の香気成分、呈味成分等を効率よく抽出することができる。また、抽出後に抽出エキスからのアルコール除去が容易である。   In the present invention, the extraction solvent is preferably ethanol-containing water. According to this, alcohol-soluble aroma components, taste components, and the like can be efficiently extracted. Moreover, alcohol removal from an extract is easy after extraction.

本発明においては、前記節類が、鰹節、鯖節、メジ節、いわし節、煮干、アゴ節、及びそれらの節削り、節類生産過程で生じる副産物、又はこれらの混合物から選ばれた少なくとも一種であることが好ましい。   In the present invention, the nodules are at least one selected from bonito, bonito, medusa, sardine, sardines, jaws, and their savings, by-products produced in the production of nodules, or mixtures thereof. It is preferable that

本発明の節類エキスの製造方法によれば、原料節類で形成された充填層のカラムベッド面に抽出溶媒が液溜めされない状態で通液するので、前記充填層が余分な抽出溶媒を含み膨潤して、物理的及び/又は化学的に劣化することを防ぐことができる。これにより、抽出過程中、前記充填層を形成する原料節類からの良好な抽出状態を保つことができ、風味、呈味のバランスを損ねる成分が抽出されることを抑制することができる。また、余分な抽出溶媒の圧力によって、前記充填層に不均一な移動相の通り道が形成されることを防ぎ、抽出溶媒を均一に分散させつつ通液させることができるので、節類のもつ香気成分及び呈味成分を充分、かつ効率よく抽出することができる。   According to the method for producing a nodule extract of the present invention, since the extraction solvent passes through the column bed surface of the packed bed formed of the raw material nodule, the packed bed contains an extra extraction solvent. It can swell and prevent physical and / or chemical degradation. Thereby, it is possible to maintain a good extraction state from the raw material knot forming the packed bed during the extraction process, and to suppress the extraction of components that impair the balance between flavor and taste. In addition, it is possible to prevent the formation of a non-uniform path for the mobile phase in the packed bed due to the pressure of the excess extraction solvent, and to allow the extraction solvent to pass through while being uniformly dispersed. Ingredients and taste ingredients can be extracted sufficiently and efficiently.

本発明の節エキスの製造方法おいては、受け面にフィルターを備えた容器に節類を充填し、その容器内に形成された節類の充填層のカラムベッド面にシャワー状、噴霧状、及び/又は液滴状にした抽出溶媒を滴下する。そして、前記充填層のカラムベッド面に滴下した抽出溶媒が液溜めされない状態で、節類の充填層に抽出溶媒を通液して、節類エキスを得る。
In the method for producing a knot extract of the present invention, a vessel having a filter on the receiving surface is filled with knot, and the column bed surface of the knot packed bed formed in the vessel is showered, sprayed, And / or the extraction solvent made into the droplet form is dripped. Then, in a state where the extraction solvent dripped onto the column bed surface of the packed bed is not pooled, the extracted solvent is passed through the packed bed of nodes to obtain a node extract.

本発明において抽出原料として用いる節類は、一般的に入手可能な節類であれば特に制限はない。具体的には、鰹節、鯖節、メジ節、いわし節、煮干、アゴ節、及びそれらの節削り、節類生産過程で生じる副産物、又はこれらの混合物から選ばれた少なくとも一種を用いることが好ましい。   The nodule used as an extraction raw material in the present invention is not particularly limited as long as it is a generally available nodule. Specifically, it is preferable to use at least one selected from bonito, bonito, medusa, sardine, boiled and dried chin, and their shavings, by-products generated in the process of producing nodules, or a mixture thereof. .

上記2種類以上の原料の混合物を使用する場合には、それらをブレンドして上記容器に充填してもよく、また、原料を多層状に充填してもよく、得たい節類エキスの風味等により適宜方法を選ぶことができる。   When using a mixture of the above two or more kinds of raw materials, they may be blended and filled into the container, or the raw materials may be filled in multiple layers, such as the flavor of the knot extract to be obtained, etc. The method can be selected as appropriate.

以下、図1に示す模式図に沿って、本発明の技術的特徴を具体的に説明する。   Hereinafter, the technical features of the present invention will be specifically described with reference to the schematic diagram shown in FIG.

容器10は、その受け面にフィルター20を備えている。フィルター20は、抽出溶媒の通過を許容しつつ、容器10に充填される節類の流出を防ぐ。なお、フィルター20の上部には、フィルター20の目詰まりを防止するために、補助フィルター21を備えている。   The container 10 includes a filter 20 on its receiving surface. The filter 20 prevents the nodule from filling the container 10 from flowing out while allowing the extraction solvent to pass therethrough. Note that an auxiliary filter 21 is provided above the filter 20 in order to prevent the filter 20 from being clogged.

容器10には、粉砕された節類が充填され、容器10の円柱形状に沿ってカラム状の充填層30を形成している。   The container 10 is filled with pulverized nodes, and a column-shaped packed layer 30 is formed along the cylindrical shape of the container 10.

上記充填層30に抽出溶媒を通液するために、容器10の上方に備えられた図示しない滴下装置の抽出溶媒滴下口50から、抽出溶媒40を滴下する。滴下された抽出溶媒40は、充填層のカラムベッド面31に到達する。   In order to pass the extraction solvent through the packed bed 30, the extraction solvent 40 is dropped from an extraction solvent dropping port 50 of a dropping device (not shown) provided above the container 10. The extracted extraction solvent 40 reaches the column bed surface 31 of the packed bed.

ここで、本発明において「滴下した抽出溶媒が液溜めされない状態」とは、滴下した抽出溶媒が容器内に形成された節類の充填層に浸透して、充填層のカラムベット面において液溜されない状態を保ちながら通液することを意味する。   Here, in the present invention, “the state in which the dropped extraction solvent is not pooled” means that the dropped extraction solvent permeates the packed bed of nodules formed in the container and collects the liquid on the column bed surface of the packed bed. It means that the liquid is passed while keeping the state that is not done.

したがって、例えば、上記カラムベッド面31に到達した抽出溶媒40が充填層30内に速やかに浸透してカラムベッド面31の表面に滞ることがないように、抽出溶媒が滴下される。   Therefore, for example, the extraction solvent is dropped so that the extraction solvent 40 that has reached the column bed surface 31 does not rapidly permeate into the packed bed 30 and stay on the surface of the column bed surface 31.

上記抽出溶媒の滴下手段としては、複数のノズルを有するシャワーノズル、又はスプレイノズル等から、シャワー状、噴霧状、液滴状に滴下することが好ましい。また、ノズルを回転させながら滴下することが好ましい。これによれば、抽出溶媒を上記魚節充填層の上部表面に均一に滴下することができる。   The extraction solvent is preferably dropped from a shower nozzle having a plurality of nozzles or a spray nozzle in a shower form, a spray form, or a drop form. Moreover, it is preferable to drop while rotating the nozzle. According to this, an extraction solvent can be dripped uniformly at the upper surface of the said fish clause packed bed.

本願発明において、上記充填層のカラムベット面において抽出溶媒が液溜されない状態を保つためには、抽出溶媒の滴下速度を魚節充填層の断面積に対して410リットル/h・m以下で滴下することが好ましく、効率、作業性を考慮すると300〜410リットル/h・mで滴下することがより好ましい。 In the present invention, in order to keep the extraction solvent from collecting on the column bed surface of the packed bed, the dropping speed of the extraction solvent is 410 liters / h · m 2 or less with respect to the cross-sectional area of the fish-section packed bed. It is preferable to drop, and considering efficiency and workability, it is more preferable to drop at 300 to 410 liter / h · m 2 .

また、充填する節類は3〜32メッシュパスに粉砕したものであることが好ましく、6〜24メッシュパスに粉砕したものであることがより好ましい。節類の粉砕物の粒度が32メッシュパスよりも小さい場合であると、カラム内における溶媒の流速が低下し、カラムベット面において抽出溶媒が液溜されやすくなるため、好ましくない。また、節類の粉砕物の粒度が3メッシュパスよりも大きい場合には、カラム内における溶媒の流速が高くなりすぎ、原料に溶媒が十分に浸透せず、抽出効率が低下するため、好ましくない。なお、本発明におけるメッシュの開口はJIS規格に準じており、3、6、24、32、42メッシュの開口はそれぞれ6.87、3.35、0.71、0.50、0.355mmである。   Moreover, it is preferable that the nodes to be filled are pulverized to 3 to 32 mesh pass, and more preferably pulverized to 6 to 24 mesh pass. If the particle size of the pulverized product of knot is smaller than 32 mesh pass, the flow rate of the solvent in the column decreases, and the extraction solvent tends to pool on the column bed surface, which is not preferable. In addition, when the particle size of the pulverized product of the nodules is larger than 3 mesh pass, the flow rate of the solvent in the column becomes too high, the solvent does not sufficiently permeate into the raw material, and the extraction efficiency decreases, which is not preferable. . The mesh openings in the present invention are in accordance with JIS standards, and the openings of 3, 6, 24, 32, and 42 meshes are 6.87, 3.35, 0.71, 0.50, and 0.355 mm, respectively. is there.

また、上記魚節充填層の高さは30cm〜60cmであることが好ましく、40cm〜60cmであることがより好ましい。60cm以上であるとカラム内における溶媒の流速が低下し、カラムベット面において抽出溶媒が液溜されやすくなるため、好ましくない。また、上記魚節充填層の高さが30cm以下であると、節類エキスの生産性が悪くなる。   Moreover, it is preferable that the height of the said fish clause packed bed is 30 cm-60 cm, and it is more preferable that it is 40 cm-60 cm. If it is 60 cm or more, the flow rate of the solvent in the column decreases, and the extraction solvent tends to pool on the column bed surface, which is not preferable. In addition, when the height of the above-mentioned fish node filling layer is 30 cm or less, productivity of the node extract is deteriorated.

本願発明においては、上記容器としてカラム又はタンク等を用いることができ、その素材に特に制限はないが、ステンレス、ポリプロピレン、グラスライニング、FRP等を好ましく用いることができる。   In the present invention, a column or tank can be used as the container, and the material is not particularly limited, but stainless steel, polypropylene, glass lining, FRP and the like can be preferably used.

本願発明においては、原料となる節類の充填に際し、粉砕された節類をそのまま充填してもよく、また、原料100に対して25〜40質量部の抽出溶媒で湿潤させた後に充填してもよいが、より抽出効率を上げるためには、予め抽出溶媒を用いて湿潤させた原料を充填することが好ましい。また、原料を3〜5回に分けて、抽出溶媒で湿潤させながら充填してもよい。   In the present invention, when filling the raw materials, the crushed nodes may be filled as they are, or the raw materials 100 are filled after being moistened with 25 to 40 parts by mass of an extraction solvent. However, in order to further increase the extraction efficiency, it is preferable to fill the raw material wetted beforehand with the extraction solvent. Alternatively, the raw material may be divided into 3-5 times and filled while being wetted with the extraction solvent.

本願発明においては、上記フィルターは、容器に充填される魚節類の流出を防ぐことができ、且つ、抽出エキスの通過を許容する特性を有するフィルターであれば特に制限されない。具体的には、ろ紙、ろ布、セラミック、樹脂、ろ過助剤等が挙げられる。また、フィルターの上部には、フィルターの目詰まりを防止するために、目の粗いフィルターを補助フィルター21として備えていてもよい。   In this invention, the said filter will not be restrict | limited especially if it can prevent the outflow of the fish clauses with which a container is filled, and has the characteristic which accept | permits passage of an extract. Specific examples include filter paper, filter cloth, ceramic, resin, filter aid and the like. Further, a coarse filter may be provided as the auxiliary filter 21 on the upper part of the filter in order to prevent the filter from being clogged.

上記フィルター及び/又は補助フィルターは、上記魚節充填層の下部表面の全面に接するように容器の受け面に配され、抽出液エキスの流出を許容する。したがって、魚節充填層の下部表面において抽出液エキスの流出が阻害されることによる抽出溶媒の移動の乱れを引き起こすことがない。   The filter and / or auxiliary filter is disposed on the receiving surface of the container so as to be in contact with the entire lower surface of the fish-section packed bed, and allows the extract extract to flow out. Therefore, the movement of the extraction solvent is not disturbed by the outflow of the extract extract on the lower surface of the fish clause packed bed.

本発明においては、上記抽出溶媒として水又はアルコール溶液を用いることができる。アルコール溶液としては1〜80容量%のアルコール含水を好ましく使用することができ、単一もしくは異なる濃度のアルコール溶液又は水を複数回に分けて滴下してもよい。また、アルコール溶液を滴下後、続けて水を滴下させ所定量まで抽出液を回収してもよい。更にまた、抽出溶媒のアルコール濃度が連続的に変化するように抽出原料に接触させて抽出液を得ることもできる。なお、アルコールの種類は、飲食品の製造に使用可能なエタノールが好ましい。   In the present invention, water or an alcohol solution can be used as the extraction solvent. As the alcohol solution, a water content of 1 to 80% by volume of alcohol can be preferably used, and a single or different concentration alcohol solution or water may be dropped in several portions. Further, after the alcohol solution is dropped, water may be dropped continuously to recover the extract to a predetermined amount. Furthermore, it is also possible to obtain an extract by contacting the extraction raw material so that the alcohol concentration of the extraction solvent changes continuously. In addition, the kind of alcohol has preferable ethanol which can be used for manufacture of food-drinks.

本発明においては、カラムジャケット等、上記容器を保温する手段等により、抽出温度が20〜80℃であるようにすることが好ましく、20〜60℃であるようにすることがより好ましい。   In the present invention, the extraction temperature is preferably 20 to 80 ° C., more preferably 20 to 60 ° C., by a means such as a column jacket for keeping the container warm.

本発明において、抽出溶媒の通液量は、得られる抽出液の濃度により適宜任意に選択することができるが、上記充填層を形成する節類の乾燥質量に対し50〜250重量%の抽出液を回収するように抽出溶媒を通液することが好ましく、100〜200重量%の抽出液を回収するように抽出溶媒を通液することがより好ましい。すなわち、抽出溶媒の通液量が少なすぎると充分な抽出効率を得ることができないので好ましくなく、通液量が多すぎると得られる抽出液の固形分濃度が低くなり、濃縮等に手間がかかる上、濃縮による風味の劣化が生じるので好ましくない。   In the present invention, the flow rate of the extraction solvent can be arbitrarily selected depending on the concentration of the obtained extract, but it is 50 to 250% by weight of the extract with respect to the dry mass of the nodes forming the packed bed. It is preferable to pass the extraction solvent so as to collect the liquid, and it is more preferable to pass the extraction solvent so as to collect 100 to 200% by weight of the extraction liquid. That is, if the amount of extraction solvent passed is too small, it is not preferable because sufficient extraction efficiency cannot be obtained. If the amount of solution passed is too large, the solid content concentration of the resulting extract will be low, and it will take time to concentrate, etc. In addition, the flavor is deteriorated by concentration, which is not preferable.

本発明においては、上記のように得られた抽出液を、そのまま、又は、公知の方法により適宜濃縮、乾燥することでアルコール除去及び/又は固形分調整して、節類エキスとすることができる。   In the present invention, the extract obtained as described above can be used as it is or by appropriately concentrating and drying by a known method to remove alcohol and / or adjust the solid content to obtain a nodular extract. .

本発明の製造方法によって得られた節類エキスは、非常に優れた風味・呈味を有しているので、醤油、味噌、合わせ酢、ソース類(焼きそば、焼きうどん、お好み焼き、野菜炒め等)、たれ類(焼肉、しゃぶしゃぶ、焼き魚、煮魚、納豆、湯豆腐、冷奴、ユッケ等)、つゆ類(めんつゆ、なべつゆ、天つゆ等)、ドレッシング等の調味料類や、カレー、ソースミックス、中華料理の素、混ぜご飯の素、米飯加工品、卵料理の素(卵豆腐、茶碗蒸し、玉子焼き等)等の調理品類、更には、スープ、味噌汁、吸い物等のスープ類や、缶詰類、麺類、漬物、佃煮、惣菜、のり、海藻サラダ、練り製品、米菓、スナック類等、様々な飲食品への利用が期待できる。   The nodular extract obtained by the production method of the present invention has a very excellent flavor and taste, soy sauce, miso, mixed vinegar, sauces (yakisoba, fried udon, okonomiyaki, fried vegetables, etc.), Sauces (Yakiniku, shabu-shabu, grilled fish, boiled fish, natto, boiled tofu, chilled fish, yukke, etc.), condiments such as noodle soup, nabetsuyu, tempura soup, curry, sauce mix, Chinese food Cooking products such as raw ingredients, mixed rice ingredients, cooked rice products, egg dishes (eg egg tofu, steamed rice bowls, egg roasted eggs), soups such as soup, miso soup, soup, canned foods, noodles, pickles Can be expected to be used for various foods and beverages, such as simmered sardines, side dishes, seaweed, seaweed salad, kneaded products, rice crackers, and snacks.

以下、実施例を挙げて本発明を具体的に説明する。   Hereinafter, the present invention will be specifically described with reference to examples.

<実施例1>
鰹節粗砕品(7mesh:開口2.80mm pass品)300gを、50容量%エタノール溶液75mlと混合して湿潤させた後、直径4cm、長さ50cmのカラムに充填し、定量ポンプによる流量を7ml/min(断面積に対する流量速度:334.4リットル/h・m)に合わせて、50容量%エタノール溶液300mlをカラムベッド面に液滴状に滴下し、続けて水を液滴状に滴下した。そして、カラム下部から回収された抽出液が600mlに達したところで抽出を終了した。なお、抽出開始から終了時まで、カラムのジャケットには60℃の温水を循環させた。
<Example 1>
300 g of crushed bonito crushed product (7 mesh: 2.80 mm pass product) was mixed with 75 ml of 50% ethanol solution and wetted, then packed into a column of 4 cm in diameter and 50 cm in length, and the flow rate with a metering pump was 7 ml. / Min (flow rate with respect to the cross-sectional area: 334.4 liters / h · m 2 ), 300 ml of a 50% by volume ethanol solution is dropped on the column bed surface in the form of droplets, and then water is dropped in the form of droplets. did. The extraction was terminated when the extract recovered from the lower part of the column reached 600 ml. Note that warm water of 60 ° C. was circulated through the column jacket from the start to the end of extraction.

回収された抽出液のアルコール分は33.5容量%であった。また、50容量%エタノール溶液300mlに続けて滴下した水の量は660mlに達し、全体の抽出時間は2時間であった。   The alcohol content of the recovered extract was 33.5% by volume. In addition, the amount of water dripped following 300 ml of 50% by volume ethanol solution reached 660 ml, and the total extraction time was 2 hours.

<比較例1>
バッチ式抽出法により抽出液を調製した。
<Comparative Example 1>
An extract was prepared by a batch extraction method.

すなわち、鰹節粗砕品(7mesh:開口2.80mm pass品)300gと、30容量%エタノール溶液960mlとを混合し、60℃の湯浴中で2時間攪拌した。攪拌終了後、抽出液をろ紙No.2を用いてろ過し、バッチ抽出液600mlを得た。   That is, 300 g of bonito crushed product (7 mesh: 2.80 mm pass product) and 960 ml of 30% ethanol solution were mixed and stirred in a 60 ° C. hot water bath for 2 hours. After the completion of stirring, the extract was filtered with paper No. 2 was used to obtain 600 ml of batch extract.

<比較例2>
抽出原料の充填層の表面に液溜めした状態で抽出液を調製するために、抽出溶媒の滴下速度を早めた以外は上記実施例1と同様にして抽出液を調製した。
<Comparative Example 2>
An extract was prepared in the same manner as in Example 1 above, except that the dropping rate of the extraction solvent was increased in order to prepare the extract in a state where the liquid was stored on the surface of the packed bed of extraction raw materials.

すなわち、鰹節粗砕品(7mesh:開口2.80mm pass品)300gを、50容量%エタノール溶液75mlと混合して湿潤させた後、直径4cm、長さ50cmのカラムに充填し、定量ポンプによる流量を14ml/min(断面積に対する流量速度:668.8リットル/h・m)に合わせて、50容量%エタノール溶液300mlをカラムベッド面に液滴状に滴下し、続けて水を液滴状に滴下した。そして、カラム下部から回収された抽出液が600mlに達したところで抽出を終了した。なお、抽出開始から終了時まで、カラムのジャケットには60℃の温水を循環させた。 That is, 300 g of bonito crushed product (7 mesh: 2.80 mm pass product) was mixed with 75 ml of 50% by volume ethanol solution and wetted, and then packed into a column of 4 cm in diameter and 50 cm in length. Was adjusted to 14 ml / min (flow rate relative to the cross-sectional area: 668.8 liters / h · m 2 ), 300 ml of 50% ethanol solution was dropped onto the column bed surface, and then water was dropped. It was dripped in. The extraction was terminated when the extract recovered from the lower part of the column reached 600 ml. Note that warm water of 60 ° C. was circulated through the column jacket from the start to the end of extraction.

この比較例においては、50容量%エタノールを150ml滴下した時点から、液溜され始め、抽出終了時には節類の充填層のカラムベッド面から5cmの高さに液溜された。   In this comparative example, the liquid began to be collected from the time when 150 ml of 50% by volume ethanol was dropped, and at the end of extraction, the liquid was collected to a height of 5 cm from the column bed surface of the packed bed of nodes.

回収された抽出液のアルコール分は18.5容量%であった。また、50容量%エタノール溶液300mlに続けて滴下した水の量は660mlに達し、全体の抽出時間は1.5時間であった。   The alcohol content of the recovered extract was 18.5% by volume. Further, the amount of water dripped following 300 ml of 50% by volume ethanol solution reached 660 ml, and the total extraction time was 1.5 hours.

<比較例3>
粒度が、42メッシュパスである鰹節粗砕品を用いて抽出液を調製することを試みた。すなわち、鰹節粗砕品(42mesh pass品)300gを、50容量%エタノール溶液75mlと混合して湿潤させた後、直径4cm、長さ50cmのカラムに充填し、定量ポンプによる流量を7ml/min(断面積に対する流量速度:334.4リットル/h・m)に合わせて、50容量%アルコール溶液300mlをカラムベッド面に液滴状に滴下した。その結果、50容量%アルコール溶液を100ml滴下した時点で抽出溶媒が浸透しなくなった。
<Comparative Example 3>
An attempt was made to prepare an extract using a koji koji crushed product having a particle size of 42 mesh pass. That is, 300 g of crushed bonito crushed product (42 mesh pass product) was mixed with 75 ml of a 50% by volume ethanol solution and wetted, and then packed into a column having a diameter of 4 cm and a length of 50 cm. In accordance with the flow rate with respect to the cross-sectional area: 334.4 liter / h · m 2 ), 300 ml of 50% by volume alcohol solution was dropped on the column bed surface in the form of droplets. As a result, the extraction solvent did not penetrate when 100 ml of 50% by volume alcohol solution was dropped.

<試験例1>
実施例1、比較例1、2で得られた各抽出液を用いて、香り、呈味について10人のパネラーにより官能評価(良好:3点、普通:2点、悪い:1点)を行った。各項目の平均点を表1に示す。
<Test Example 1>
Using each extract obtained in Example 1 and Comparative Examples 1 and 2, sensory evaluation (good: 3 points, normal: 2 points, bad: 1 point) was performed by 10 panelists about aroma and taste. It was. Table 1 shows the average score of each item.

Figure 0004845630
Figure 0004845630

以上から、粗砕鰹節で形成された充填層を用いるカラム式抽出法において、そのカラムベッド面に抽出溶媒が液溜めされない状態で抽出溶媒を通液することにより、バッチ式抽出法や、カラムベッド面が抽出溶媒で液溜めされた状態で行ったカラム式抽出法に比べて、風味の富んだかつお節エキスが得られることがわかる。   From the above, in the column-type extraction method using the packed bed formed of coarsely crushed bonito, the batch-type extraction method or the column bed can be obtained by passing the extraction solvent in a state where the extraction solvent is not stored on the column bed surface. It can be seen that a bonito extract rich in flavor can be obtained as compared with the column-type extraction method in which the surface is pooled with the extraction solvent.

本発明の一実施形態を示す模式図である。It is a schematic diagram which shows one Embodiment of this invention.

符号の説明Explanation of symbols

10 容器
20 フィルター
21 補助フィルター
30 充填層
31 充填層カラムベッド面
40 抽出溶媒
50 抽出溶媒滴下口
10 container 20 filter 21 auxiliary filter 30 packed bed 31 packed bed column bed surface 40 extraction solvent 50 extraction solvent dropping port

Claims (7)

受け面にフィルターを備えた容器に節類を充填し、前記容器内に形成された節類の充填層のカラムベッド面にシャワー状、噴霧状、及び/又は液滴状にした抽出溶媒を滴下して、前記充填層のカラムベッド面に前記抽出溶媒が液溜めされない状態で、前記充填層に前記抽出溶媒を通液することを特徴とする節類エキスの製造方法。 A container having a filter on the receiving surface is filled with nodule , and an extraction solvent in the form of a shower, spray, and / or droplet is dropped on the column bed surface of the nodule packed bed formed in the container. A method for producing a nodular extract, wherein the extraction solvent is passed through the packed bed in a state where the extraction solvent is not stored on the column bed surface of the packed bed. 前記節類の粒度が、3〜32メッシュパスである請求項1に記載の節類エキスの製造方法。   The method for producing a nodular extract according to claim 1, wherein the particle size of the nodule is 3 to 32 mesh pass. 前記抽出溶媒をノズルから滴下し該ノズルが回転するようにしてシャワー状、噴霧状、及び/又は液滴状に滴下する請求項1又は2に記載の節類エキスの製造方法。 Manufacturing process sections such extract according to claim 1 or 2 wherein the nozzle is dropped the extraction solvent from the nozzles drops down like a shower, atomized, and / or Ekishizukujo so as to rotate. 前記抽出溶媒を前記充填層の断面積に対して410リットル/h・m以下の流量速度で滴下する請求項1〜3のいずれか1つに記載の節類エキスの製造方法。 The method for producing a nodular extract according to any one of claims 1 to 3, wherein the extraction solvent is dropped at a flow rate of 410 liter / h · m 2 or less with respect to a cross-sectional area of the packed bed. 前記充填層の高さが、30〜60cmである請求項1〜4のいずれか1つに記載の節類エキスの製造方法。   The method for producing a nodular extract according to any one of claims 1 to 4, wherein a height of the packed bed is 30 to 60 cm. 前記抽出溶媒がエタノール含有水である請求項1〜5のいずれか1つに記載の節類エキスの製造方法。   The method for producing a nodular extract according to any one of claims 1 to 5, wherein the extraction solvent is ethanol-containing water. 前記節類が、鰹節、鯖節、メジ節、いわし節、煮干、アゴ節、及びそれらの節削り、節類生産過程で生じる副産物、又はこれらの混合物から選ばれた少なくとも一種である請求項1〜6のいずれか1つに記載の節類エキスの製造方法。   2. The nodules are at least one selected from bonito, bonito, medusa, sardine, sardines, chin, and their by-products, by-products produced during nodules production, or a mixture thereof. The manufacturing method of the nodal extract of any one of -6.
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