JP6170331B2 - Production method of fine bran - Google Patents
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Description
本発明は、小麦ふすまの粉砕物である微粉ふすまの製造方法に関し、詳細には、機能性素材として近年注目されているアルキルレゾルシノールを高含有する微粉ふすまの製造方法に関する。 The present invention relates to a method for producing fine powdered bran, which is a pulverized product of wheat bran, and in particular, relates to a method for producing finely powdered bran containing a high amount of alkylresorcinol which has recently attracted attention as a functional material.
近年、健康意識の高まりから、食物繊維、ビタミン、ミネラル等の栄養素に富む小麦ふすまの需要が増してきており、それに伴い、小麦ふすまの有効利用に関する技術が種々提案されている。例えば特許文献1には、小麦ふすまから各種栄養素に富む特定画分(糊粉細胞粒子及び果皮−種皮粒子の画分)を採取する方法として、小麦ふすまの粉砕物から、粒径が約40μmより小さい粒子の画分を除去し、残りの画分(粒径約40μm超の画分)を静電的に荷電し、その電荷の差によって前記特定画分を採取する方法が記載されている。また特許文献2には、小麦ふすまを粒径500μm以下に粉砕し、その粉砕物から粒径30μm以下の微粒子を除いた後、残りの画分(粒径30μm超の画分)から空気分級により不要な画分を分級して取り除き、更に、その残りの画分を高蛋白画分(粒度が95±25μm以下の画分)と高食物繊維画分(粒度が95±25μmより大きい画分)とに分離する方法が記載されている。 In recent years, the demand for wheat bran rich in nutrients such as dietary fiber, vitamins, and minerals has increased due to an increase in health consciousness, and various techniques relating to the effective use of wheat bran have been proposed accordingly. For example, in Patent Document 1, as a method for collecting a specific fraction rich in various nutrients (a fraction of paste cell particles and pericarp-seed coat particles) from wheat bran, a particle size of about 40 μm is obtained from a pulverized product of wheat bran. A method is described in which a fraction of small particles is removed, the remaining fraction (a fraction having a particle size of more than about 40 μm) is electrostatically charged, and the specific fraction is collected by the difference in charge. In Patent Document 2, wheat bran is pulverized to a particle size of 500 μm or less, fine particles having a particle size of 30 μm or less are removed from the pulverized product, and the remaining fraction (fraction having a particle size of more than 30 μm) is subjected to air classification. Unnecessary fractions are classified and removed, and the remaining fractions are divided into a high protein fraction (a fraction with a particle size of 95 ± 25 μm or less) and a high dietary fiber fraction (a fraction with a particle size greater than 95 ± 25 μm). And a method for separating them.
また、アルキルレゾルシノールが抗肥満作用、抗酸化作用、抗免疫作用等を有することは周知である。非特許文献1には、アルキルレゾルシノールが、天然の非イソテルぺノイド系フェノール性両親媒性化合物であるレゾルシノール脂質として広く植物に含まれることが記載されており、また、レゾルシノール脂質の給源となる植物として、小麦等のイネ科植物が記載されている。また、非特許文献2には、アルキルレゾルシノールが植物の中でも特に小麦やライ麦に特に多く含まれている旨が記載されている。尚、特許文献1及び2には、アルキルレゾルシノールについては記載されていない。 In addition, it is well known that alkylresorcinol has an anti-obesity action, an antioxidant action, an anti-immunity action and the like. Non-Patent Document 1 describes that alkylresorcinol is widely contained in plants as a resorcinol lipid that is a natural non-isoterpenoid phenolic amphiphilic compound, and a plant that is a source of resorcinol lipid. As mentioned above, gramineous plants such as wheat are described. Non-Patent Document 2 describes that a large amount of alkylresorcinol is particularly contained in wheat and rye among plants. Patent Documents 1 and 2 do not describe alkylresorcinol.
本発明は、アルキルレゾルシノールを高含有し、食品素材として有用な微粉ふすまの製造方法に関する。 The present invention relates to a method for producing finely powdered bran, which contains a high content of alkylresorcinol and is useful as a food material.
本発明者等は、鋭意検討した結果、下記工程1〜5を経て得られた小麦ふすまの粉砕物(中位径200μm以下の微粉ふすま画分)から中位径50μm以上の粒子画分を分級して除いた、中位径50μm未満の微粒子画分に、アルキルレゾルシノールが高含有されていることを知見した。
・工程1:原料小麦をロール粉砕して粗粉砕物を得る工程。
・工程2:前記粗粉砕物から小麦ふすまを採取する工程。
・工程3:前記小麦ふすまを湿熱処理する工程。
・工程4:前記湿熱処理で得られた湿熱処理小麦ふすまを粉砕して微粉砕物を得る工程。
・工程5:前記微粉砕物を、中位径200μm以下の微粉ふすま画分とそれ以外の他の画分とに分級し、該微粉ふすま画分を採取する工程。
As a result of intensive studies, the present inventors classified a particle fraction having a median diameter of 50 μm or more from a pulverized product of wheat bran (fine powder bran fraction having a median diameter of 200 μm or less) obtained through the following steps 1 to 5. It was found that alkylresorcinol was highly contained in the fine particle fraction having a median diameter of less than 50 μm.
Step 1: Rolling the raw material wheat to obtain a coarsely pulverized product.
Step 2: A step of collecting wheat bran from the coarsely pulverized product.
-Process 3: The process of wet-heat-treating the said wheat bran.
Step 4: A step of pulverizing the wet heat-treated wheat bran obtained by the wet heat treatment to obtain a finely pulverized product.
Step 5: A step of classifying the finely pulverized product into a fine powder bran fraction having a median diameter of 200 μm or less and other fractions, and collecting the fine powder bran fraction.
本発明は、前記知見に基づきなされたもので、小麦ふすまの粉砕物を、中位径50μm未満の微粒子画分とそれ以外の他の画分とに分級し、該微粒子画分を採取する工程を有する、微粉ふすまの製造方法を提供するものである。 The present invention has been made on the basis of the above-mentioned knowledge, and classifies the wheat bran pulverized product into a fine particle fraction having a median diameter of less than 50 μm and other fractions, and collects the fine particle fraction. The manufacturing method of the fine powder bran which has this.
本発明によれば、アルキルレゾルシノールを高含有し、食品素材として有用な微粉ふすまを効率良く製造することができる。この微粉ふすまは、従来の小麦ふすまに比してアルキルレゾルシノールの含有率が高いため、人体に有用なアルキルレゾルシノールを効率的に摂取可能な食品素材として有用である。 ADVANTAGE OF THE INVENTION According to this invention, the fine powder bran which contains alkyl resorcinol highly and is useful as a foodstuff material can be manufactured efficiently. Since this fine powder bran has a higher content of alkylresorcinol than conventional wheat bran, it is useful as a food material that can efficiently ingest alkylresorcinol useful for the human body.
本発明の微粉ふすまの製造方法は、小麦ふすまの粉砕物を出発物質として用い、該粉砕物を粒径に基づき複数の画分に分級し、そのうちの特定画分(相対的に粒径の小さい画分)を採取する工程を有する。以下、先ず、本発明の製造方法の出発物質である、小麦ふすまの粉砕物について説明する。 The method for producing fine powder bran of the present invention uses a pulverized product of wheat bran as a starting material, classifies the pulverized product into a plurality of fractions based on the particle size, and a specific fraction (of which the particle size is relatively small). A step of collecting a fraction). Hereinafter, first, wheat bran pulverized material, which is a starting material of the production method of the present invention, will be described.
小麦ふすまの粉砕物の原料となる小麦ふすまは、小麦粒の外皮部を主体とするものである。小麦ふすまとしては、一般的な小麦粉の製造過程で生じる、小麦粒から胚乳を除去した残部、あるいはこの残部からさらに胚芽を除去したもの等を用いることができ、組成や製造過程を問わない。また、小麦ふすまの原料となる小麦の種類は特に制限されない。 Wheat bran, which is a raw material for pulverized wheat bran, is mainly composed of the outer skin of wheat grains. As wheat bran, the remainder obtained by removing the endosperm from the wheat grains, which is produced during the production process of general wheat flour, or the one obtained by further removing the germ from the remainder can be used, regardless of the composition or the production process. Moreover, the kind of wheat used as the raw material of wheat bran is not particularly limited.
小麦ふすまは、原料小麦を粉砕して得られた粗粉砕物から採取することができる。小麦の粉砕方法は特に制限されず、公知の粉砕方法を適宜用いることができ、例えば、ロール式粉砕、衝撃式粉砕、気流式粉砕等が挙げられる。本発明ではこれらの1つを単独で又は2つ以上を組み合わせて用いることができ、例えば、ロール式粉砕と衝撃式粉砕とを組み合わせ、両者をこの順で実施することができる。また、ロール式粉砕等による小麦の粉砕は、1回でも良く、多段階で複数回行っても良い。また、衝撃式粉砕に用いる粉砕機としては、衝撃板と回転ローター間で機械的衝撃により粉砕を行うものであれば特に限定されるものではなく、例えばターボミル、ブレードミル等を用いることができる。 Wheat bran can be collected from a coarsely pulverized product obtained by pulverizing raw wheat. The method for pulverizing wheat is not particularly limited, and a known pulverization method can be appropriately used. Examples thereof include roll pulverization, impact pulverization, and airflow pulverization. In the present invention, one of these can be used alone or in combination of two or more. For example, roll pulverization and impact pulverization can be combined, and both can be carried out in this order. Moreover, the wheat pulverization by roll-type pulverization or the like may be performed once or multiple times in multiple stages. The pulverizer used for impact pulverization is not particularly limited as long as pulverization is performed between the impact plate and the rotating rotor by mechanical impact, and for example, a turbo mill, a blade mill, or the like can be used.
小麦ふすまの製造において、小麦を粉砕する前に、該小麦に加水して調湿しても良いが、通常は、加水・調湿せずに小麦を粉砕する。また、小麦を粉砕して得られた粗粉砕物から小麦ふすまを採取する方法は特に制限されず、例えば篩分け等の公知の分級方法により、粗粉砕物を小麦ふすまとそれ以外の成分とに分離し、該小麦ふすまを採取する方法を利用できる。 In the production of wheat bran, before pulverizing wheat, the wheat may be hydrated and conditioned, but the wheat is usually pulverized without hydration / humidification. The method for collecting wheat bran from the coarsely pulverized product obtained by pulverizing wheat is not particularly limited. For example, the coarsely pulverized product is classified into wheat bran and other components by a known classification method such as sieving. A method of separating and collecting the wheat bran can be used.
本発明で用いる小麦ふすまの粉砕物は、小麦ふすまを粉砕することによって得られる。小麦ふすまの粉砕方法は特に制限されず、公知の粉砕方法を適宜用いることができ、例えば、ロール式粉砕、衝撃式粉砕、気流式粉砕等が挙げられ、本発明ではこれらの1つを単独で又は2つ以上を組み合わせて用いることができる。 The pulverized wheat bran used in the present invention is obtained by pulverizing wheat bran. A method for pulverizing wheat bran is not particularly limited, and a known pulverization method can be used as appropriate. Examples thereof include roll-type pulverization, impact-type pulverization, and air-flow-type pulverization. In the present invention, one of these can be used alone. Or two or more can be used in combination.
小麦ふすまの粉砕物の製造において、小麦ふすまを粉砕する前に、該小麦ふすまを加熱処理することが好ましい。小麦ふすまを加熱処理することにより、次工程で小麦ふすまが粉砕されやすくなる。小麦ふすまの加熱処理は、乾熱処理でも良く、湿熱処理でも良いが、特に湿熱処理が好ましい。乾熱加熱は、容器中に原料(小麦粉ふすま)を入れ、水分を加えずに、該容器の外から加熱する熱処理である。湿熱加熱は、原料(小麦粉ふすま)中の水分を維持しながら、又は水分を加えながら行う熱処理であり、より具体的には、水蒸気又は水の存在下で原料を加熱する方法が挙げられ、その際、水蒸気又は水自体で原料を加熱しても良い。 In the production of pulverized wheat bran, it is preferable to heat-treat the wheat bran before pulverizing the wheat bran. By heat-treating the wheat bran, the wheat bran is easily pulverized in the next step. The heat treatment of wheat bran may be dry heat treatment or wet heat treatment, but wet heat treatment is particularly preferable. Dry heat heating is a heat treatment in which a raw material (wheat flour bran) is placed in a container and heated from outside the container without adding moisture. Wet heat heating is a heat treatment performed while maintaining or adding moisture in the raw material (wheat flour bran), more specifically, a method of heating the raw material in the presence of water vapor or water, At this time, the raw material may be heated with water vapor or water itself.
本発明で用いる小麦ふすまの粉砕物の粒径は特に制限されないが、該粉砕物の中位径(D50)が200μm以下であると、その後の該粉砕物の分級工程において、アルキルレゾルシノールを高含有する画分をより確実に採取できるようになる。本発明で用いる小麦ふすまの粉砕物の中位径は、好ましくは150μm以下〜180μm以下、更に好ましくは150μm未満である。小麦ふすまの粉砕物の粒径の調整は、篩、空気分級機等を用いて常法に従って行うことができる。 The particle size of the pulverized product of wheat bran used in the present invention is not particularly limited, but if the median diameter (D50) of the pulverized product is 200 μm or less, a high content of alkylresorcinol is contained in the subsequent classification step of the pulverized product. The fraction to be collected can be collected more reliably. The median diameter of the pulverized wheat bran used in the present invention is preferably 150 μm or less to 180 μm or less, and more preferably less than 150 μm. Adjustment of the particle size of the wheat bran pulverized product can be performed according to a conventional method using a sieve, an air classifier or the like.
本発明において、中位径(D50)とは、体積分率で計算した累積体積頻度が粒径の小さい方から計算して50%になる粒径(体積中位径)を意味する。例えば、中位径200μm以下とは、粒子(小麦ふすまの粉砕物)の累積頻度が50%に達したときの粒径が200μm以下になることを意味する。中位径は、レーザー回折/散乱式粒度分布計(商品名「マイクロトラック」、日機装社製)で測定した体積基準のメジアン径として得られる。 In the present invention, the median diameter (D50) means a particle diameter (volume median diameter) at which the cumulative volume frequency calculated by the volume fraction is 50% calculated from the smaller particle diameter. For example, the median diameter of 200 μm or less means that the particle diameter when the cumulative frequency of particles (wheat bran pulverized product) reaches 50% is 200 μm or less. The median diameter is obtained as a volume-based median diameter measured with a laser diffraction / scattering particle size distribution meter (trade name “Microtrack”, manufactured by Nikkiso Co., Ltd.).
本発明で用いる小麦ふすまの粉砕物の製造方法の一例として、前記工程1〜5を有する製造方法が挙げられる。前記工程1及び2については、前述した小麦ふすまの製造に関する説明の通りであるので、以下では、他の工程について説明を補足する。 The manufacturing method which has the said process 1-5 is mentioned as an example of the manufacturing method of the pulverized material of wheat bran used by this invention. Since Steps 1 and 2 are as described above for the production of wheat bran, the following description supplements the other steps.
前記工程3において、小麦ふすまの湿熱処理は、小麦ふすまに含まれるアミラーゼやプロテアーゼ等の各種酵素の活性を失活又は低減させるように行うことが好ましい。小麦ふすまにおける酵素の活性を失活又は低減させておくと、小麦ふすまの二次加工性が向上すると共に、これを用いた二次加工品の風味、食感が向上する。好ましい小麦ふすまの湿熱処理の一例として、水蒸気を導入する密閉系容器内において、加熱温度80〜110℃、加熱時間(小麦ふすまの容器内滞留時間)1〜60秒間で小麦ふすまを湿熱処理する方法が挙げられる。斯かる湿熱処理方法において、加熱温度は好ましくは85〜98℃、更に好ましくは90〜95℃であり、加熱時間は好ましくは5〜30秒間である。斯かる湿熱処理方法は、特許第2784505号公報に記載の装置を用いて実施することができる。 In the step 3, the wet heat treatment of the wheat bran is preferably performed so as to deactivate or reduce the activity of various enzymes such as amylase and protease contained in the wheat bran. When the activity of the enzyme in wheat bran is deactivated or reduced, the secondary processability of wheat bran is improved, and the flavor and texture of the secondary processed product using the wheat bran are improved. As an example of a wet heat treatment of wheat bran, a method of performing a wet heat treatment of wheat bran for 1 to 60 seconds at a heating temperature of 80 to 110 ° C. and a heating time (wheat bran residence time) in a closed container into which water vapor is introduced. Is mentioned. In such a wet heat treatment method, the heating temperature is preferably 85 to 98 ° C, more preferably 90 to 95 ° C, and the heating time is preferably 5 to 30 seconds. Such a wet heat treatment method can be carried out using an apparatus described in Japanese Patent No. 2784505.
前記工程4において、湿熱処理小麦ふすまの粉砕方法としては、衝撃式粉砕が好ましい。湿熱処理小麦ふすまの粉砕の程度は、次工程(前記工程5)の分級において、中位径150μm未満〜200μm未満の微粉ふすま画分の割合が80〜100質量%、特に90〜100質量%となるように行うことが好ましい。尚、前記工程4において衝撃式粉砕を行い且つ次工程の前記工程5における分級を空気分級機により行う場合、空気分級機内蔵の衝撃式微粉砕機を用いることにより、前記工程4と前記工程5とを略同時に行うことが可能となり、設備やコストの面で有利である。空気分級機内蔵の衝撃式微粉砕機としては、例えばホソカワミクロン社製のACMパルベライザー(商品名)を挙げることができる。 In the step 4, impact pulverization is preferred as a method for pulverizing the wet heat-treated wheat bran. The degree of pulverization of the wet heat-treated wheat bran is 80 to 100% by mass, particularly 90 to 100% by mass, in the classification of the next step (said step 5), the proportion of the fine powder bran fraction having a median diameter of less than 150 μm to less than 200 μm. It is preferable to do so. In addition, when impact type pulverization is performed in the step 4 and classification in the next step 5 is performed by an air classifier, by using an impact type fine pulverizer with a built-in air classifier, the steps 4 and 5 can be performed. Can be performed almost simultaneously, which is advantageous in terms of equipment and cost. Examples of the impact type fine pulverizer with built-in air classifier include ACM pulverizer (trade name) manufactured by Hosokawa Micron.
前記工程5において、前記工程4で得られた湿熱処理小麦ふすまの微粉砕物を、篩による分級又は空気分級機による分級により、中位径200μm以下の微粉ふすま画分とそれ以外の他の画分(粗ふすま画分)とに分級する(第1の分級工程)。本発明で用いるのは、前者の微粉ふすま画分であり、この微粉ふすま画分を採取して、後述する更なる分級工程(第2の分級工程)に用いる。後者の粗ふすま画分(中位径200μm超の粒子の画分)は基本的に不要であり廃棄しても良いが、前記工程4に戻して再度粉砕することもできる。 In the step 5, the finely pulverized product of the wet heat-treated wheat bran obtained in the step 4 is classified into a fine powder bran fraction having a median diameter of 200 μm or less and other fractions by classification with a sieve or classification with an air classifier. Classification into a fraction (crude bran fraction) (first classification step). The former fine powder bran fraction is used in the present invention, and this fine powder bran fraction is collected and used in a further classification step (second classification step) described later. The latter coarse bran fraction (the fraction of particles having a median diameter of more than 200 μm) is basically unnecessary and may be discarded, but can be returned to the step 4 and pulverized again.
本発明の製造方法の主たる特徴の1つとして、以上のようにして製造された小麦ふすまの粉砕物を、「中位径(D50)50μm未満の微粒子画分」と「それ以外の他の画分」(中位径50μm以上の粒子の画分)とに分級し、該微粒子画分を採取する工程を有している点が挙げられる。小麦ふすまの粉砕物として前記「中位径(D50)200μm以下の微粉ふすま画分」を用いる場合、該微粉ふすま画分を得るのに利用した分級工程(第1の分級工程)と、該微粉ふすま画分を中位径50μm未満の微粒子画分とそれ以外の他の画分とに分級する工程(第2の分級工程)との2種類の分級工程を実施することになる。中位径(D50)については前述した通りである。 As one of the main characteristics of the production method of the present invention, the wheat bran pulverized product produced as described above is divided into “fine particle fraction with a median diameter (D50) of less than 50 μm” and “other fractions”. And a fraction of particles having a median diameter of 50 μm or more and collecting the fine particle fraction. When using the above-mentioned “fine powder bran fraction having a median diameter (D50) of 200 μm or less” as a pulverized product of wheat bran, a classification step (first classification step) used to obtain the fine powder bran fraction, and the fine powder Two types of classification steps, ie, a step of classifying the bran fraction into a fine particle fraction having a median diameter of less than 50 μm and another fraction (second classification step) are performed. The median diameter (D50) is as described above.
小麦ふすまの粉砕物から「中位径50μm未満の微粒子画分」を選別するための分級(第2の分級工程)は、篩、空気分級機等の公知の分級手段を用いて行うことができるが、特に分級効率の点から空気分級機を用いて行うのが好ましい。空気分級機とは、粉体を気体の流れの中におき、気流と遠心力を利用して粉末粒子の粒径と真比重の差を利用して行う分級手段である。具体的には、特開59−4477号に記載されているような回転式空気分級機を用いて前記分級(第2の分級工程)を行うのが好ましい。この回転式空気分級機を用いて「中位径50μm未満の微粒子画分」を分級する場合、2,500〜6,000回転/分で分級ローターを回転させ、風量0.5〜3.0m3/分の条件で行うことが好ましい。 Classification (second classification step) for selecting “a fine particle fraction having a median diameter of less than 50 μm” from pulverized wheat bran can be performed using a known classification means such as a sieve or an air classifier. However, it is preferable to use an air classifier from the viewpoint of classification efficiency. The air classifier is a classifying means for placing powder in a gas flow and making use of the difference between the particle size and true specific gravity of the powder particles using airflow and centrifugal force. Specifically, the classification (second classification step) is preferably performed using a rotary air classifier as described in JP-A-59-4477. When classifying a “fine particle fraction with a median diameter of less than 50 μm” using this rotary air classifier, the classification rotor is rotated at 2,500 to 6,000 rpm, and the air volume is 0.5 to 3.0 m. It is preferable to carry out under the condition of 3 / min.
また、小麦ふすまの粉砕物から「中位径50μm未満の微粒子画分」を選別するための分級(第2の分級工程)において、分級は1回でも良く、多段階で複数回行っても良い。また、本発明で最終的に採取するのは、中位径50μm未満の微粒子画分であり、それ以外の他の画分(中位径50μm以上の粒子の画分)は基本的に不要であり廃棄しても良いが、前記工程4に戻して再度粉砕することもできる。 In the classification (second classification step) for selecting “fine particle fraction having a median diameter of less than 50 μm” from the pulverized wheat bran, the classification may be performed once or multiple times in multiple stages. . The final collection in the present invention is a fine particle fraction having a median diameter of less than 50 μm, and other fractions (fractions of particles having a median diameter of 50 μm or more) are basically unnecessary. Yes, it may be discarded, but it can be returned to the step 4 and pulverized again.
小麦ふすまの粉砕物から選別された中位径50μm未満の微粒子画分は、人体に有用なアルキルレゾルシノールを高含有しており、食品素材として有用である。本発明者らの知見によれば、この中位径50μm未満の微粒子画分の中でも、特に中位径30μm以下の微粒子画分、とりわけ中位径15μm以下の微粒子画分は、アルキルレゾルシノールの含有率が高いので、これらの画分と他の画分とを分離しておく意義はある。即ち本発明においては、小麦ふすまの粉砕物を、「中位径30μm以下の微粒子画分」と「それ以外の他の画分」(中位径30μm超の粒子の画分)とに分級することもできるし、あるいは、「中位径15μm以下の微粒子画分」と「それ以外の他の画分」(中位径15μm超の粒子の画分)とに分級することもできる。また本発明においては、小麦ふすまの粉砕物から選別された「中位径50μm未満の微粒子画分」を2つ以上の画分に分級し、それぞれ分取することもでき、例えば、「中位径15μm以下の微粒子画分」と「中位径15μm超且つ50μm未満の微粒子画分」とに分級・分取することもできる。このように、本発明では小麦ふすまに含まれる「中位径30μm以下の微粒子画分」を重要成分と認識しているのに対し、特許文献1及び2に記載の発明では該微粒子画分を不要成分として除去しており、この点からも両発明の技術思想の違いは明確である。 The fine particle fraction with a median diameter of less than 50 μm selected from the pulverized wheat bran contains a high content of alkylresorcinol useful for the human body and is useful as a food material. According to the knowledge of the present inventors, among the fine particle fractions having a median diameter of less than 50 μm, the fine particle fraction having a median diameter of 30 μm or less, in particular, the fine particle fraction having a median diameter of 15 μm or less contains alkylresorcinol. Since the rate is high, it is meaningful to separate these fractions from other fractions. That is, in the present invention, the pulverized wheat bran is classified into “a fine particle fraction having a median diameter of 30 μm or less” and “other fraction” (a fraction of particles having a median diameter of more than 30 μm). Alternatively, it can be classified into “a fine particle fraction having a median diameter of 15 μm or less” and “another fraction” (a fraction of particles having a median diameter of more than 15 μm). In the present invention, the “fine particle fraction having a median diameter of less than 50 μm” selected from the pulverized wheat bran can be classified into two or more fractions, each of which can be collected. The fine particle fraction having a diameter of 15 μm or less ”and the“ fine particle fraction having a median diameter of more than 15 μm and less than 50 μm ”can be classified and sorted. Thus, in the present invention, the “fine particle fraction having a median diameter of 30 μm or less” contained in wheat bran is recognized as an important component, whereas in the inventions described in Patent Documents 1 and 2, the fine particle fraction is It is removed as an unnecessary component, and the difference between the technical ideas of both inventions is clear from this point.
通常の市販の小麦ふすまのアルキルレゾルシノールの含有率は、原料小麦の種類等によって異なるが、概ね0.3質量%程度である。これに対し、本発明の製造方法によって得られる、「中位径50μm未満の微粒子画分」のアルキルレゾルシノールの含有率は、好ましくは0.35質量%以上、更に好ましくは0.5質量%以上を期待できる。また、本発明の製造方法によって得られる、「中位径30μm以下の微粒子画分」のアルキルレゾルシノールの含有率は、好ましくは0.4質量%以上、更に好ましくは0.5質量%以上を期待できる。また、本発明の製造方法によって得られる、「中位径15μm以下の微粒子画分」のアルキルレゾルシノールの含有率は、好ましくは0.5質量%以上、更に好ましくは0.52質量%以上を期待できる。尚、ここでいう「アルキルレゾルシノールの含有率」は、小麦ふすま(微粒子画分)が複数種のアルキルレゾルシノールを含んでいる場合は、それら複数種それぞれの含有率の合計値を意味する。 The content of alkylresorcinol in ordinary commercially available wheat bran is about 0.3% by mass, although it varies depending on the type of raw wheat. On the other hand, the content of alkylresorcinol in the “fine particle fraction having a median diameter of less than 50 μm” obtained by the production method of the present invention is preferably 0.35% by mass or more, more preferably 0.5% by mass or more. Can be expected. The alkylresorcinol content of the “fine particle fraction with a median diameter of 30 μm or less” obtained by the production method of the present invention is preferably 0.4% by mass or more, more preferably 0.5% by mass or more. it can. The alkylresorcinol content of the “fine particle fraction having a median diameter of 15 μm or less” obtained by the production method of the present invention is preferably 0.5% by mass or more, more preferably 0.52% by mass or more. it can. Here, the “content ratio of alkylresorcinol” means the total value of the contents of each of the plurality of types when the wheat bran (fine particle fraction) contains a plurality of types of alkylresorcinol.
本発明の製造方法の実施によって得られる製造結果物(中位径50μm未満の微粒子画分)に含まれるアルキルレゾルシノールについて説明すると、該製造結果物は、好ましくは、下記一般式(I)で表されるアルキルレゾルシノールを1種以上含む。 The alkylresorcinol contained in the product obtained by carrying out the production method of the present invention (fine particle fraction having a median diameter of less than 50 μm) will be described. The product is preferably represented by the following general formula (I). One or more alkylresorcinols.
前記一般式(I)におけるR1に関し、炭素原子数15〜25の飽和アルキル基としては、代表例として、n−ペンタデシル、n−ヘプタデシル、n−ノナデシル、n−ヘンイコシル、n−トリコシル、n−ペンタコシル、n−ヘプタコシル等の直鎖状のものが挙げられ、これらの他に、分岐状又は環状のものでも良い。これらの中でも、炭素原子数15〜23の飽和アルキル基が好ましい。 Regarding R 1 in the general formula (I), examples of the saturated alkyl group having 15 to 25 carbon atoms include n-pentadecyl, n-heptadecyl, n-nonadecyl, n-henicosyl, n-tricosyl, n- Examples include linear ones such as pentacosyl and n-heptacosyl, and besides these, branched or cyclic ones may be used. Among these, a saturated alkyl group having 15 to 23 carbon atoms is preferable.
また、前記一般式(I)におけるR1に関し、炭素原子数15〜25の不飽和アルキル基としては、上記の炭素原子数15〜25の飽和アルキル基に対応するものが挙げられる。不飽和アルキル基に含まれる不飽和結合の数及び位置に特に制限はない。 Moreover, regarding R 1 in the general formula (I), examples of the unsaturated alkyl group having 15 to 25 carbon atoms include those corresponding to the saturated alkyl group having 15 to 25 carbon atoms. There is no restriction | limiting in particular in the number and position of the unsaturated bond contained in an unsaturated alkyl group.
また、前記一般式(I)におけるR2は水素原子であることが好ましく、また、R1はR2に対してパラ位に結合していることが好ましい。 In the general formula (I), R 2 is preferably a hydrogen atom, and R 1 is preferably bonded to R 2 at the para position.
本発明の製造結果物(中位径50μm未満の微粒子画分)に含まれ得るアルキルレゾルシノールの具体例としては、以下のものが挙げられる。
1,3−ジヒドロキシ−5−n−ペンタデシルベンゼン(C15:0)
1,3−ジヒドロキシ−5−n−ヘプタデシルベンゼン(C17:0)
1,3−ジヒドロキシ−5−n−ノナデシルベンゼン(C19:0)
1,3−ジヒドロキシ−5−n−ヘンイコシルベンゼン(C21:0)
1,3−ジヒドロキシ−5−n−トリコシルベンゼン(C23:0)
1,3−ジヒドロキシ−5−n−ペンタコシルベンゼン(C25:0)
Specific examples of the alkyl resorcinol that can be contained in the resulting product of the present invention (fine particle fraction having a median diameter of less than 50 μm) include the following.
1,3-dihydroxy-5-n-pentadecylbenzene (C15: 0)
1,3-dihydroxy-5-n-heptadecylbenzene (C17: 0)
1,3-dihydroxy-5-n-nonadecylbenzene (C19: 0)
1,3-dihydroxy-5-n-henicosylbenzene (C21: 0)
1,3-dihydroxy-5-n-tricosylbenzene (C23: 0)
1,3-dihydroxy-5-n-pentacosylbenzene (C25: 0)
本発明の製造結果物(中位径50μm未満の微粒子画分)は、通常の市販の小麦ふすまと同様に食品素材として用いることができる。この食品素材には、人用の飲食品のみならず、動物用飼料も含まれる。 The resulting product of the present invention (fine particle fraction having a median diameter of less than 50 μm) can be used as a food material in the same manner as ordinary commercially available wheat bran. This food material includes not only food and drink for humans but also animal feed.
以下、実施製造例を挙げて、本発明を更に詳細に説明するが、本発明はこの実施製造例により制限されるものではない。 EXAMPLES Hereinafter, although an Example manufacture example is given and this invention is demonstrated further in detail, this invention is not restrict | limited by this Example manufacture example.
〔実施製造例〕
市販の小麦ふすまの粉砕物を、「中位径15μmの画分」(画分1)、「中位径50μmの画分」(画分2)、「中位径117μmの画分」(画分3)及び「中位径220μmの画分」(画分4)の4つの画分に分級し、それぞれ分取した。この市販の小麦ふすまの粉砕物の中位径(D50)は77μmであった。実施製造例における小麦ふすまの粉砕物の分級・各画分の分取は、具体的には次のようにして行った。
[Example of production]
Commercially available wheat bran pulverized products were classified into “fraction with a median diameter of 15 μm” (fraction 1), “fraction with a median diameter of 50 μm” (fraction 2), “fraction with a median diameter of 117 μm” (fraction Fractions were classified into four fractions, ie, fraction 3) and “fraction having a median diameter of 220 μm” (fraction 4). The median diameter (D50) of the pulverized product of this commercially available wheat bran was 77 μm. Specifically, the classification of each pulverized product of wheat bran and the fractionation in the production examples were carried out as follows.
先ず、中位径77μmの小麦ふすまの粉砕物を回転式空気分級機(ターボクラシファイヤーTC−15、日清エンジニアリング株式会社製)に2.0kg/時間の割合で供給し、3100回転/分で分級ローターを回転させ、風量2.5m3/分の条件下で分級を行い、微粉Iと、該微粉Iよりも粒径の大きい粗粉Iとを得た。微粉Iは前記画分1である。次いで、粗粉Iを前記回転式空気分級機に2.4kg/時間の割合で供給し、1600回転/分で分級ローターを回転させ、風量2.5m3/分の条件下で分級を行い、微粉IIと、該微粉IIよりも粒径の大きい粗粉IIとを得た。微粉IIは前記画分2である。こうして得られた微粉I(画分1)と微粉II(画分2)とを混合したものは、「中位径50μm未満の微粒子画分」である。次いで、粗粉IIを分級機(ロータップシェイカー、株式会社テラオカ製、篩の目の間隔を149μmに設定)に供給し、微粉IIIと、該微粉IIIよりも粒径の大きい粗粉IIIとを得た。微粉IIIは前記画分3であり、粗粉IIIは前記画分4である。 First, crushed wheat bran having a median diameter of 77 μm is supplied to a rotary air classifier (Turbo Classifier TC-15, manufactured by Nissin Engineering Co., Ltd.) at a rate of 2.0 kg / hour, and 3100 rpm. The classification rotor was rotated, and classification was performed under the condition of an air volume of 2.5 m 3 / min to obtain fine powder I and coarse powder I having a larger particle diameter than fine powder I. Fine powder I is fraction 1. Next, the coarse powder I is supplied to the rotary air classifier at a rate of 2.4 kg / hour, the classification rotor is rotated at 1600 rpm, and classification is performed under the condition of an air volume of 2.5 m 3 / min. Fine powder II and coarse powder II having a particle size larger than that of fine powder II were obtained. Fine powder II is the fraction 2. A mixture of fine powder I (fraction 1) and fine powder II (fraction 2) obtained in this way is a “fine particle fraction having a median diameter of less than 50 μm”. Next, coarse powder II is supplied to a classifier (low tap shaker, manufactured by Terraoka Co., Ltd., the interval between sieve meshes is set to 149 μm), and fine powder III and coarse powder III having a particle size larger than fine powder III are obtained. Obtained. Fine powder III is the fraction 3 and coarse powder III is the fraction 4.
〔評価試験〕
前記の市販の小麦ふすまの粉砕物及び画分1〜4それぞれについて、前記一般式(I)で表されるアルキルレゾルシノール並びに灰分、タンパク質及び脂質それぞれの含有率を測定した。アルキルレゾルシノールの含有率は下記方法により測定し、灰分の含有率は「5訂 日本食品標準分成分表分析マニュアルの解説 日本食品分析センター/編集」のP86〜89に開示の方法に従って測定し、タンパク質の含有率は同解説のP29〜36に開示の方法に従って測定し、脂質の含有率は同解説のP37〜61に開示の方法に従って測定した。それらの結果を下記表1に示す。
〔Evaluation test〕
About each of the pulverized product and fractions 1 to 4 of the above-mentioned commercially available wheat bran, the alkylresorcinol represented by the general formula (I) and the contents of ash, protein and lipid were measured. The content of alkylresorcinol is measured by the following method, and the content of ash is measured according to the method disclosed in P86-89 of “5th edition, Japan Food Analysis Center / Editing” Was measured according to the method disclosed in P29 to 36 of the same description, and the lipid content was measured according to the method disclosed in P37 to 61 of the same description. The results are shown in Table 1 below.
<アルキルレゾルシノールの含有率の測定方法>
測定対象物に5倍量のエタノールを添加して、600rpm、室温の条件で、16時間撹拌抽出し、その抽出物を濾過して不要物を除きエタノール抽出液を回収した後、エタノールを留去してエタノール抽出物を得る。このエタノール抽出物にメタノールを添加して該エタノール抽出物の濃度が200ug/mlのメタノール添加液を調製し、該メタノール添加液を、孔径0.45μmのフィルターを通過させ、その通過分を、高速液体クロマトグラフィー(HPLC)の試料とする。HPLCの条件は下記の通り。溶出開始後31〜36分に出現するピーク成分を回収して溶媒留去し、アルキルレゾルシノールを得る。こうして得られたアルキルレゾルシノールの総質量と、測定対象物の総質量とから、目的とするアルキルレゾルシノール含有率を算出する。
(HPLCの条件)
・カラム:シリカゲル(ODS−80A、5μm、4.6×250mm、ジーエルサイエンス株式会社製)
・ガードカラム:ODS−80A、5μm、4.6×50mm、
・カラム温度:30℃
・移動相:メタノール100%
・検出波長:215nm
<Measurement method of alkylresorcinol content>
Add 5 times the amount of ethanol to the object to be measured, extract under stirring at 600 rpm and room temperature for 16 hours, filter the extract to remove unnecessary substances, collect the ethanol extract, and then evaporate the ethanol. To obtain an ethanol extract. Methanol is added to the ethanol extract to prepare a methanol addition solution having a concentration of the ethanol extract of 200 ug / ml, and the methanol addition solution is passed through a filter having a pore size of 0.45 μm. A sample for liquid chromatography (HPLC) is used. HPLC conditions are as follows. A peak component appearing 31 to 36 minutes after the start of elution is collected and the solvent is distilled off to obtain alkylresorcinol. The target alkylresorcinol content is calculated from the total mass of the alkylresorcinol thus obtained and the total mass of the measurement object.
(HPLC conditions)
Column: silica gel (ODS-80A, 5 μm, 4.6 × 250 mm, manufactured by GL Sciences Inc.)
Guard column: ODS-80A, 5 μm, 4.6 × 50 mm,
-Column temperature: 30 ° C
-Mobile phase: 100% methanol
・ Detection wavelength: 215 nm
表1から明らかなように、画分1(中位径15μmの画分)及び画分2(中位径50μmの画分)は、分級前の小麦ふすまの粉砕物と同等か、それ以上のアルキルレゾルシノール含有率を有している。尚、小麦ふすまの粉砕物並びにこれから分級された画分1〜4は、組成(灰分、タンパク質及び脂質の含有率)が互いに異なっていることから、各画分は、単に該粉砕物が細かく砕かれたもの(組成的には該粉砕物と同一物質)ではなく、組成的にも互いに異なる別物質である。以上のことから、小麦ふすまの粉砕物から分級され採取された、中位径50μm未満の微粒子画分(画分1と画分2との混合物)は、人体に有用なアルキルレゾルシノールを高含有し、食品素材として有用であることがわかる。 As is clear from Table 1, fraction 1 (fraction with a median diameter of 15 μm) and fraction 2 (fraction with a median diameter of 50 μm) are equal to or higher than the ground wheat bran before classification. It has an alkylresorcinol content. Since the wheat bran pulverized product and the fractions 1 to 4 classified from now on have different compositions (contents of ash, protein and lipid), each fraction is simply finely pulverized. It is not the one that has been released (in terms of composition, the same substance as the pulverized product), but is another substance that is also different in composition. From the above, the fine particle fraction (mixture of fraction 1 and fraction 2) with a median diameter of less than 50 μm classified and collected from pulverized wheat bran contains a high content of alkylresorcinol useful for the human body. It turns out that it is useful as a food material.
Claims (3)
・工程1:原料小麦をロール粉砕して粗粉砕物を得る工程。
・工程2:前記粗粉砕物から小麦ふすまを採取する工程。
・工程3:前記小麦ふすまを湿熱処理する工程。
・工程4:前記湿熱処理で得られた湿熱処理小麦ふすまを粉砕して微粉砕物を得る工程。
・工程5:前記微粉砕物を、中位径200μm以下の微粉ふすま画分とそれ以外の他の画分とに分級し、該微粉ふすま画分を採取する工程。 The finely divided bran fraction having a median diameter of 200 μm or less obtained through the following steps 1 to 5 is classified into a fine particle fraction having a median diameter of 15 μm or less and other fractions, and the fine particle fraction is classified into A method for producing fine powder bran, comprising a step of collecting.
Step 1: Rolling the raw material wheat to obtain a coarsely pulverized product.
Step 2: A step of collecting wheat bran from the coarsely pulverized product.
-Process 3: The process of wet-heat-treating the said wheat bran.
Step 4: A step of pulverizing the wet heat-treated wheat bran obtained by the wet heat treatment to obtain a finely pulverized product.
Step 5: A step of classifying the finely pulverized product into a fine powder bran fraction having a median diameter of 200 μm or less and other fractions, and collecting the fine powder bran fraction.
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| JP2015053868A (en) * | 2013-09-10 | 2015-03-23 | 日清製粉株式会社 | Method for producing bran fine powder |
| JP6435167B2 (en) * | 2013-12-20 | 2018-12-05 | 株式会社日清製粉グループ本社 | Flour composition |
| JP6598238B2 (en) * | 2015-07-01 | 2019-10-30 | 日東富士製粉株式会社 | Method for producing finely ground bran, finely ground bran and food |
| JP6749753B2 (en) * | 2015-10-30 | 2020-09-02 | 昭和産業株式会社 | Processed grain hulls, process for producing grain hulls, process for bakery products, bakery products and mixed powder for bakery products |
| JP2017112990A (en) * | 2015-12-22 | 2017-06-29 | 花王株式会社 | Process for producing processed wheat bran |
| JP2023140651A (en) * | 2022-03-23 | 2023-10-05 | 日東富士製粉株式会社 | Composition for improving bowel movements, method for producing a composition for improving bowel movements, and method for improving bowel movements |
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| JP2549411B2 (en) * | 1988-02-16 | 1996-10-30 | 日清製粉株式会社 | A method for separating high protein and high fiber fractions from wheat bran. |
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