JP4147620B2 - Method for producing coated granular composition and coated granular composition - Google Patents
Method for producing coated granular composition and coated granular composition Download PDFInfo
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- JP4147620B2 JP4147620B2 JP11814998A JP11814998A JP4147620B2 JP 4147620 B2 JP4147620 B2 JP 4147620B2 JP 11814998 A JP11814998 A JP 11814998A JP 11814998 A JP11814998 A JP 11814998A JP 4147620 B2 JP4147620 B2 JP 4147620B2
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Description
【0001】
【発明の属する技術分野】
本発明は、特に、食品、飼料、医薬品、医薬部外品、化粧品等の原材料となりうる直径50μm以下という微粉末を含む芯材を、有効に、且つ生産効率良く油脂により被覆しうる被覆粒状組成物の製造方法及びこの製造方法により得られた被覆粒状組成物に関する。
【0002】
【従来の技術】
従来、食品、飼料、医薬品、医薬部外品、化粧品等の各分野における各種原材料となる粒状物を油脂により被覆することによって、粒状物が外気や水分と接触すること、並びに粒状物同士が接触すること等に起因する粒状物の劣化防止が行われている。このような油脂による被覆方法としては、粒状物に液状の油脂を噴霧して被覆する方法や、芯材と、特定融点以上の硬化油粉末とを一緒に高速で撹拌し、接触・衝突させることによって芯材の全周囲表面に油脂を固着させる方法等が知られている。特に、前記接触・衝突させる方法は、芯材に対して均一な被覆が可能であるため有効な手段である。
しかし、直径50μm以下の芯材を含む場合、十分な被覆性能を保持しうる状態で芯材を被覆することが困難であり、被覆した油脂の隙間から水等が侵入して芯材を溶解するなど、溶出防止性に問題が生じる恐れが高い。
【0003】
一方、特開平7−87950号公報には、芯物質に、溶融状態にある脂質を噴霧又は滴下して一次被覆膜を形成し、得られた一次被覆粒子に融点40℃以上の脂質粉状体を接触、衝突させ、二次被覆膜を形成する二重被覆粒子の製造方法が提案されている。しかし、この方法は、芯物質として直径数百μmのものが意図されているに過ぎず、直径50μm以下の芯物質には適用が困難である。
【0004】
【発明が解決しようとする課題】
従って、本発明の目的は、芯材として50μm以下の微粉末を有する場合であっても、溶出防止性等に優れた被覆性能を容易に付与することができ、しかも生産効率に優れる被覆粒状組成物の製造方法を提供することにある。
本発明の別の目的は、芯材として50μm以下の微粉末を含み、各々の被覆粒状物が、溶出防止性等に優れた被覆性能を有する被覆粒状組成物を提供することにある。
【0005】
【課題を解決するための手段】
すなわち、本発明によれば、直径50μm以下の微粉末を含む芯材を、ツェイン、グルテン、プルラン、ゼラチン、キサンタンガム、寒天、ジェランタンガム又はカラギーナンからなる常温において水難溶性を示す物質により被覆、造粒する工程(A)と、得られた造粒物を油脂により被覆する工程(B)とを含むことを特徴とする被覆粒状組成物の製造方法が提供される。
また本発明によれば、前記製造方法により得た被覆粒状組成物であって、直径50μm以下の微粉末を含む芯材の全周囲表面が、ツェイン、グルテン、プルラン、ゼラチン、キサンタンガム、寒天、ジェランタンガム又はカラギーナンからなる常温において水難溶性を示す物質層と、その外側に油脂層とを備えていることを特徴とする被覆粒状組成物が提供される。
【0006】
【発明の実施の形態】
以下本発明を更に詳細に説明する。
本発明の製造方法では、まず、直径50μm以下の微粉末を含む芯材を、特定の常温において水難溶性を示す物質により被覆、造粒する工程(A)を行う。工程(A)に用いる芯材は、通常、直径50μm以下の微粉末を5〜100重量%含有しており、この直径50μm以下の微粉末が被覆性能を低下させるので、工程(A)を経ることによりその大部分が直径50μmを超える粒子になる。
【0007】
芯材を構成する材料としては、通常、外気や水分との接触、並びに芯材同士の接触により劣化が生じたり、溶出により辛味や苦味等の強い成分であり、被覆によりこのような劣化や溶出が防止若しくは抑制されうる直径50μm以下のものを含む材料であれば特に限定されず、各種の食品、飼料、医薬品、医薬部外品、化粧品等の材料が挙げられる。具体的には、カテキン、イーストエキス、イチョウ葉、ギムネマ、プロポリス、カプサイシン、ビタミンB群等のエキスや粉末等が挙げられる。常温で液状のエキス類等は、凍結乾燥、スプレー乾燥等により微粉末としたものを用いることができる。
【0008】
工程(A)に用いる前記芯材を造粒するため常温において水難溶性を示す物質は、ツェイン、グルテン、プルラン、ゼラチン、キサンタンガム、寒天、ジェランタンガム又はカラギーナンからなる。
【0009】
工程(A)において、前記複数の芯材を、前記常温で水難溶性を示す物質で造粒するには、例えば、食品分野において通常使用される流動層造粒機、流動層造粒機に撹拌羽根を取り付けた撹拌型流動層造粒機、転動板を備えた転動型流動層造粒機、ワースター型流動層コーティング機等の流動型造粒機、粉末を撹拌し、その中にバインダーを添加して顆粒状にする撹拌型造粒機、粉末をバインダーと共に高圧で押し出す押出し造粒機等を用いて行うことができる。
造粒条件は特に限定されず、例えば、流動層造粒機を用いて行う場合、公知の条件で行うことができる。好ましくは、芯材を常温で水難溶性を示す物質で被覆した後の粒径がほとんど50μmを超えるように、特に好ましくは造粒物のほとんどが粒径75〜500μmとなるような条件で、且つ芯材と、常温で水難溶性を示す物質との配合割合を前記粒径となるように適宜決定して行うのが望ましい。
造粒に際しては、必要に応じてバインダーを添加することもできる。バインダーとしては、デキストリン、乳糖、コーンスターチ、粉糖等の糖類;脱脂粉乳、大豆蛋白等の蛋白質;セルロース粉等が挙げられ、その使用量は、公知の方法に基づいて適宜決定することができる。
【0010】
本発明の被覆粒状組成物の製造方法では、前記工程(A)で得られた造粒物を油脂により被覆する工程(B)を行うことによって、目的の被覆性能に優れた被覆粒状組成物が得られる。
【0011】
工程(B)に用いる油脂としては、牛脂、豚脂、魚油等の動物性油脂;ナタネ油、大豆油、パーム油、ヤシ油、エゴマ油、ゴマ油、アマニ油等の植物性油脂が挙げられる。これらの油脂は、硬化、分別、エステル交換等の油脂加工を行った精製脱臭油であっても良い。また、油脂の形態は後述する被覆方法により選択することができ、液状、半固形状、固体状のいずれであっても良い。
【0012】
工程(B)において、工程(A)により得られた造粒物を油脂により被覆する方法としては、特に限定されないが、工程(A)により得られた造粒物に、融点40℃以上の硬化油粉末を接触・衝突させて造粒物の全周囲表面に油脂を固着させて被覆する方法▲1▼;工程(A)により得られた造粒物に、流動層内で油脂を液状噴霧し、造粒物の全周囲表面を油脂で被覆する方法▲2▼等が挙げられ、特に均一な被覆層が得られる点から方法▲1▼が好ましい。
【0013】
前記方法▲1▼に用いる融点40℃以上の硬化油粉末としては、牛脂硬化油粉末、豚脂硬化油粉末、魚油硬化油粉末等の融点40℃以上の動物性硬化油粉末;ナタネ硬化油粉末、大豆硬化油粉末、パーム硬化油粉末、ヤシ硬化油粉末、エゴマ硬化油粉末、ゴマ硬化油粉末、アマニ硬化油粉末等の融点40℃以上の植物性硬化油粉末が挙げられる。これら硬化油粉末の粒径は、0.1〜50μm程度、特に1〜10μmが好ましい。
方法▲1▼において、工程(A)により得られた造粒物に、融点40℃以上の硬化油粉末を接触・衝突させる際の造粒物と硬化油粉末との混合比は、前記造粒物の粒径と前記硬化油粉末の粒径との粒径比を考慮して適宜決定することができ、例えば、造粒物:硬化油粉末が重量比で1:0.01〜5、特に1:0.05〜1の範囲から選択するのが好ましい。
方法▲1▼において、造粒物と硬化油粉末との接触・衝突は、例えば、高能率粉体混合装置等の公知の粉体を接触させる装置を用いて行うことができる。接触・衝突の条件は、融点40℃以上の硬化油粉末が溶融しない40℃未満の温度において、接触・衝突により硬化油粉末の表面が溶け、造粒物外表面に溶着し固着する条件であれば特に限定されない。
【0014】
前記方法▲2▼に用いる油脂としては、前述の動物性油脂、植物性油脂等が挙げられ、油脂が半固形状若しくは固形状の場合には、液状にして使用することができる。
方法▲2▼において、工程(A)により得られた造粒物に、流動層内で油脂を液状噴霧するには、例えば、撹拌機等により造粒物を撹拌させておき、液状の油脂をノズル、アトマイザー等を使用して噴霧する公知の方法等で行うことができる。
【0015】
本発明の被覆粒状組成物は、前記製造方法により得られる被覆粒状物であり、該被覆粒状物は、直径50μm以下の微粉末の芯材の全周囲表面に、水難溶性を示す物質層と、その外側に油脂層とを備えているものを含む。
得られる被覆粒状物の粒径は、優れた被覆性能を有するために、75〜500μmが好ましい。
【0016】
【発明の効果】
本発明の被覆粒状組成物の製造方法では、常温で水難溶性を示す物質による造粒の後に、油脂による被覆を行うので、直径50μm以下の複数の微粉末を含む芯材に対して、生産効率良く溶出防止性等に優れた被覆性能を容易に付与することができ、食品、飼料、医薬品、医薬部外品、化粧品等のあらゆる原材料の劣化防止等に利用できる。また得られる被覆粒状組成物は、芯材が50μm以下という微粉末であるにもかかわらず、溶出防止性等に優れた被覆性能を示す。
【0017】
【実施例】
以下、実施例及び比較例により更に詳細に説明するが本発明はこれらに限定されるものではない。
【0018】
実施例1
苦味の強い、50μm以下の粒子を55%含むカテキン粉末(商品名「ポリフェノン100」、太陽化学(株)製)250gを、デキストリン225gと共に流動層造粒機(商品名「フローコーターミニ」、フロイント産業(株)製)に仕込み、10%ゼラチン溶液250g(商品名「ゼラチンR」、新田ゼラチン社製)を用いて造粒した。造粒条件は、吸気温度60℃、排気温度35℃になるように、吸気量、給液量を調整した。30分間造粒後、直径50μm以下の粒子は2.5%に減少していた。
次いで得られた造粒物300gを用い、平均粒径3μmのナタネ極度硬化油微粉末100gを添加し、撹拌型造粒機(商品名「OMD−3型」、奈良機械(株)製)にて、機内温度20℃、窒素ガス封入下で主軸回転数500rpm、副軸回転数500rpmの条件で10分間撹拌して多数の油脂被膜カテキン粒状物を得た。得られた粒状物の平均粒径は200μmであった。これら多数の粒状物は、苦味が非常に良くマスキングされており、十分な油脂被覆効果が得られた。
【0019】
比較例1
実施例1と同様なカテキン粉末250g、デキストリン250gを良く粉体混合した。得られた粉体中における50μm以下の粒子の含有割合は45%であった。次いで、粉体混合した粉末300gを、実施例1と同様なナタネ極度硬化油微粉末100gと共に撹拌型造粒機(商品名「OMD−3型」、奈良機械(株)製)にて、機内温度20℃、窒素ガス封入下で主軸回転数500rpm、副軸回転数500rpmの条件で10分間撹拌して油脂被膜カテキン粒状物を調製した。得られた油脂被覆カテキン粒状物は、油脂被膜が均一になっておらず、苦味が強く、飲食に適さず、この方法では十分な油脂被覆効果が得られなかった。
【0020】
実施例2
臭いの強い市販のイーストエキス粉末350g(直径50μm以下の粒子50%含有)をデキストリン137.5gと共に、流動層造粒機(商品名「フローコーターミニ」、フロイント産業(株)製)に仕込み、5%プルラン溶液250g(商品名「プルランPF−10」、(株)林原生物化学研究所製)を用いて造粒した。造粒条件は、吸気温度60℃、排気温度35℃になるように、吸排気量、給液量を調整した。45分間造粒後、直径50μm以下の粒子は1.2%に減少していた。
次いで、得られた造粒物350gを再び流動層造粒機内に仕込み、ナタネ硬化油(融点36℃、日本油脂(株)製)50gを溶融、噴霧して、多数の油脂被覆イーストエキス粒状物を得た。この際、造粒機の運転条件は、吸気温度を室温とし、吸排気量、給液状態は流動状態により調整した。得られた粒状物の平均粒径は185μmであった。これら多数の粒状物は、臭いが非常に良くマスキングされており、十分な油脂被覆効果が得られた。
【0021】
比較例2
実施例2と同様なイーストエキス末350g及びデキストリン150gを粉体混合し、そのうち350gを流動層造粒機内に仕込み、ナタネ硬化油(融点36℃、日本油脂(株)製)50gを溶融、噴霧して多数の油脂被覆イーストエキス粒状物を得た。得られた粒状物は、油脂被膜が均一でなく、臭いが強く、飲食に適していなかった。従って、この方法では十分な油脂被覆効果が得られなかった。[0001]
BACKGROUND OF THE INVENTION
In particular, the present invention provides a coated granular composition capable of effectively and efficiently coating a core material containing fine powder having a diameter of 50 μm or less, which can be a raw material for foods, feeds, pharmaceuticals, quasi drugs, cosmetics, etc. The present invention relates to a method for producing a product and a coated granular composition obtained by the production method.
[0002]
[Prior art]
Conventionally, by covering granular materials, which are various raw materials in each field of food, feed, pharmaceuticals, quasi drugs, cosmetics, etc., with fats and oils, the granular materials come into contact with the outside air and moisture, and the granular materials are in contact with each other. Preventing the deterioration of the granular material due to such as. As a coating method with such fats and oils, a method of coating granular materials by spraying liquid fats and oils, stirring a core material and a hardened oil powder having a specific melting point or more together at high speed, and bringing them into contact with each other. A method of fixing oils and fats to the entire peripheral surface of the core material is known. In particular, the contact / collision method is an effective means because the core material can be uniformly coated.
However, when a core material having a diameter of 50 μm or less is included, it is difficult to coat the core material in a state where sufficient covering performance can be maintained, and water or the like enters from the gap between the coated oils and fats to dissolve the core material. There is a high risk of problems in elution prevention.
[0003]
On the other hand, in JP-A-7-87950, a lipid in a molten state is sprayed or dropped on a core material to form a primary coating film, and the resulting primary coated particles are in the form of lipid powder having a melting point of 40 ° C. or higher. A method for producing double-coated particles in which a body is brought into contact with and collided to form a secondary coating film has been proposed. However, this method is only intended for a core material having a diameter of several hundred μm, and is difficult to apply to a core material having a diameter of 50 μm or less.
[0004]
[Problems to be solved by the invention]
Accordingly, an object of the present invention is to provide a coated granular composition that can easily provide coating performance excellent in elution prevention and the like, and has excellent production efficiency even when it has a fine powder of 50 μm or less as a core material. It is in providing the manufacturing method of a thing.
Another object of the present invention is to provide a coated granular composition containing a fine powder of 50 μm or less as a core material and each coated granular product having a coating performance excellent in elution prevention and the like.
[0005]
[Means for Solving the Problems]
That is, according to the present invention, a core material containing fine powder having a diameter of 50 μm or less is coated with a substance having poor water solubility at room temperature consisting of zein, gluten, pullulan, gelatin, xanthan gum, agar, gellantan gum, or carrageenan. There is provided a method for producing a coated granular composition comprising the step (A) of granulating and the step (B) of coating the obtained granulated product with fats and oils.
According to the present invention, the coated granule composition obtained by the above production method, wherein the entire peripheral surface of the core material containing fine powder having a diameter of 50 μm or less has zein, gluten, pullulan, gelatin, xanthan gum, agar, gel There is provided a coated granular composition comprising a substance layer composed of lanthanum gum or carrageenan and having poor water solubility at room temperature and an oil layer on the outside thereof.
[0006]
DETAILED DESCRIPTION OF THE INVENTION
The present invention will be described in detail below.
In the production method of the present invention, first, the step (A) of coating and granulating a core material containing a fine powder having a diameter of 50 μm or less with a substance exhibiting poor water solubility at a specific normal temperature is performed. The core material used in the step (A) usually contains 5 to 100% by weight of fine powder having a diameter of 50 μm or less, and the fine powder having a diameter of 50 μm or less deteriorates the covering performance, so that the step (A) is performed. As a result, most of the particles are larger than 50 μm in diameter.
[0007]
The material constituting the core is usually a component that deteriorates due to contact with the outside air or moisture, or contact between the cores, or is a strong component such as pungent or bitter due to elution. The material is not particularly limited as long as it includes materials having a diameter of 50 μm or less that can be prevented or suppressed, and examples thereof include various foods, feeds, pharmaceuticals, quasi drugs, cosmetics, and the like. Specific examples include catechin, yeast extract, ginkgo biloba, gymnema, propolis, capsaicin, vitamin B group extracts and powders. Extracts that are liquid at room temperature can be finely powdered by freeze drying, spray drying, or the like.
[0008]
In order to granulate the core material used in the step (A), a substance that is sparingly soluble in water at room temperature is composed of zein, gluten, pullulan, gelatin, xanthan gum, agar, gellantan gum, or carrageenan.
[0009]
In the step (A), in order to granulate the plurality of core materials with a substance exhibiting poor water solubility at room temperature, for example, a fluidized bed granulator or a fluidized bed granulator usually used in the food field is stirred. Stirring type fluidized bed granulator with blades, rolling type fluidized bed granulator equipped with rolling plates, fluidized type granulator such as Wurster type fluidized bed coating machine, agitating powder and binder in it Can be performed using an agitation type granulator which is made into a granulated form, an extrusion granulator which extrudes powder at a high pressure together with a binder, and the like.
Granulation conditions are not particularly limited. For example, when using a fluidized bed granulator, it can be performed under known conditions. Preferably, the particle diameter after coating the core material with a substance exhibiting poor water solubility at room temperature is more than 50 μm, particularly preferably under the condition that most of the granulated product has a particle diameter of 75 to 500 μm, and It is desirable to appropriately determine the blending ratio of the core material and the substance exhibiting poor water solubility at room temperature so as to have the above particle diameter.
In granulation, a binder can be added as necessary. Examples of the binder include saccharides such as dextrin, lactose, corn starch, and powdered sugar; proteins such as skim milk powder and soy protein; cellulose powder and the like, and the amount used can be appropriately determined based on a known method.
[0010]
In the method for producing a coated granular composition of the present invention, a coated granular composition excellent in target coating performance is obtained by performing the step (B) of coating the granulated product obtained in the step (A) with fats and oils. can get.
[0011]
Examples of the fats and oils used in the step (B) include animal fats and oils such as beef tallow, pork tallow and fish oil; vegetable oils and fats such as rapeseed oil, soybean oil, palm oil, coconut oil, sesame oil, sesame oil and linseed oil. These oils and fats may be refined deodorized oils that have undergone oil and fat processing such as curing, fractionation, and transesterification. Moreover, the form of fats and oils can be selected with the coating method mentioned later, and any of liquid form, semi-solid form, and solid form may be sufficient.
[0012]
In the step (B), the method of coating the granulated product obtained in the step (A) with fats and oils is not particularly limited, but the granulated product obtained in the step (A) has a melting point of 40 ° C. or higher. A method in which oil powder is brought into contact with and collided to fix oil and fat on the entire peripheral surface of the granulated product (1); the granulated product obtained in the step (A) is sprayed with liquid oil in a fluidized bed. Examples include the method (2) for coating the entire peripheral surface of the granulated product with oils and fats, and the method (1) is preferable from the viewpoint of obtaining a uniform coating layer.
[0013]
Examples of the hardened oil powder having a melting point of 40 ° C. or higher used in the method (1) include animal hardened oil powder having a melting point of 40 ° C. or higher, such as beef tallow hardened oil powder, pork tallow hardened oil powder, fish oil hardened oil powder, etc .; , Vegetable hardened oil powder having a melting point of 40 ° C. or higher, such as hardened soybean oil powder, hardened palm oil powder, hardened palm oil powder, hardened sesame powder, hardened sesame oil powder, hardened linseed oil powder, and the like. The particle diameter of these hardened oil powders is preferably about 0.1 to 50 μm, particularly 1 to 10 μm.
In Method (1), the mixing ratio of the granulated product and the hardened oil powder when the hardened oil powder having a melting point of 40 ° C. or higher is brought into contact with and collided with the granulated product obtained in the step (A) Can be appropriately determined in consideration of the particle size ratio between the particle size of the product and the particle size of the hardened oil powder. For example, the weight ratio of granulated product: hardened oil powder is 1: 0.01 to 5, particularly It is preferable to select from a range of 1: 0.05-1.
In the method {circle around (1)}, the contact / collision between the granulated product and the hardened oil powder can be performed by using a known powder contacting device such as a high efficiency powder mixing device. The contact / impact condition is such that the hardened oil powder having a melting point of 40 ° C. or higher melts at a temperature lower than 40 ° C., and the surface of the hardened oil powder is melted by contact / impact and is welded and fixed to the outer surface of the granulated product. If it does not specifically limit.
[0014]
Examples of the fats and oils used in the method (2) include the aforementioned animal fats and oils and vegetable fats and oils. When the fats and oils are semi-solid or solid, they can be used in a liquid state.
In method {circle around (2)}, in order to liquidally spray the fat and oil in the fluidized bed on the granulated product obtained in the step (A), for example, the granulated product is stirred with a stirrer or the like. It can carry out by the well-known method etc. which spray using a nozzle, an atomizer, etc.
[0015]
The coated granular composition of the present invention is a coated granular product obtained by the above-described production method, and the coated granular material has a substance layer exhibiting poor water solubility on the entire peripheral surface of a fine core material having a diameter of 50 μm or less, The thing provided with the fats and oils layer on the outside is included.
The particle diameter of the obtained coated granular material is preferably 75 to 500 μm in order to have excellent coating performance.
[0016]
【The invention's effect】
In the method for producing a coated granular composition according to the present invention, after granulation with a substance exhibiting poor water solubility at room temperature, coating with fats and oils is performed, so that production efficiency is achieved for a core material containing a plurality of fine powders having a diameter of 50 μm or less. It is possible to easily provide a coating performance that is excellent in elution prevention and the like, and can be used to prevent deterioration of all raw materials such as food, feed, pharmaceuticals, quasi drugs, and cosmetics. In addition, the obtained coated granular composition exhibits a coating performance excellent in elution prevention property and the like, although the core material is a fine powder of 50 μm or less.
[0017]
【Example】
Hereinafter, although an Example and a comparative example demonstrate in detail, this invention is not limited to these.
[0018]
Example 1
250 g of catechin powder (trade name “Polyphenone 100”, Taiyo Kagaku Co., Ltd.) having a strong bitterness and containing 55% of particles of 50 μm or less together with 225 g of dextrin, fluidized bed granulator (trade name “Flow Coater Mini”, Freund And granulated using 250 g of a 10% gelatin solution (trade name “Gelatin R”, manufactured by Nitta Gelatin Co., Ltd.). As the granulation conditions, the intake air amount and the liquid supply amount were adjusted so that the intake air temperature was 60 ° C. and the exhaust temperature was 35 ° C. After granulation for 30 minutes, particles having a diameter of 50 μm or less were reduced to 2.5%.
Next, using 300 g of the obtained granulated product, 100 g of rapeseed extremely hardened oil fine powder having an average particle diameter of 3 μm was added, and the mixture was added to a stirring granulator (trade name “OMD-3”, manufactured by Nara Machinery Co., Ltd.). The mixture was stirred for 10 minutes under the conditions of an in-machine temperature of 20 ° C. and nitrogen gas filling under conditions of a main shaft rotation speed of 500 rpm and a sub shaft rotation speed of 500 rpm to obtain a large number of oil-coated catechin granules. The average particle diameter of the obtained granular material was 200 μm. Many of these granular materials were masked with a very good bitter taste, and a sufficient oil-fat coating effect was obtained.
[0019]
Comparative Example 1
250 g of catechin powder and 250 g of dextrin as in Example 1 were well mixed. The content ratio of particles of 50 μm or less in the obtained powder was 45%. Next, 300 g of the powder mixed powder was mixed with 100 g of rapeseed extremely hardened oil fine powder similar to that in Example 1 with a stirring granulator (trade name “OMD-3”, manufactured by Nara Machinery Co., Ltd.). An oil-coated catechin granular material was prepared by stirring for 10 minutes under conditions of a temperature of 20 ° C. and nitrogen gas filling under conditions of a main shaft rotation speed of 500 rpm and a sub shaft rotation speed of 500 rpm. The obtained oil- or fat-coated catechin granular material does not have a uniform oil-and-oil film, has a strong bitterness, and is not suitable for food and drink. In this method, a sufficient oil-and-fat coating effect cannot be obtained.
[0020]
Example 2
350 g of a strong smelly yeast extract powder (containing 50% of particles with a diameter of 50 μm or less) and 137.5 g of dextrin are charged into a fluidized bed granulator (trade name “Flow Coater Mini”, manufactured by Freund Sangyo Co., Ltd.) Granulation was performed using 250 g of a 5% pullulan solution (trade name “Pullan PF-10”, manufactured by Hayashibara Biochemical Laboratories). As the granulation conditions, the intake / exhaust amount and the liquid supply amount were adjusted so that the intake temperature was 60 ° C. and the exhaust temperature was 35 ° C. After granulation for 45 minutes, particles having a diameter of 50 μm or less were reduced to 1.2%.
Next, 350 g of the obtained granulated product is again charged into the fluidized bed granulator, 50 g of rapeseed oil (melting point 36 ° C., manufactured by Nippon Oil & Fats Co., Ltd.) is melted and sprayed, and a large number of oil-coated yeast extract granules Got. At this time, the operating conditions of the granulator were adjusted such that the intake air temperature was room temperature and the intake / exhaust amount and the liquid supply state were in accordance with the flow state. The average particle diameter of the obtained granular material was 185 μm. Many of these granular materials were masked with odor very well, and a sufficient oil and fat coating effect was obtained.
[0021]
Comparative Example 2
350 g of the same yeast extract powder and 150 g of dextrin as in Example 2 were mixed with powder, 350 g of which was charged into a fluidized bed granulator, and 50 g of rapeseed oil (melting point 36 ° C., manufactured by NOF Corporation) was melted and sprayed. As a result, a large number of oil-coated yeast extract granules were obtained. The obtained granular material was not uniform in oil and fat coating, had a strong odor, and was not suitable for eating and drinking. Therefore, this method did not provide a sufficient oil / fat coating effect.
Claims (4)
Priority Applications (1)
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JP11814998A JP4147620B2 (en) | 1998-04-28 | 1998-04-28 | Method for producing coated granular composition and coated granular composition |
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JP11814998A JP4147620B2 (en) | 1998-04-28 | 1998-04-28 | Method for producing coated granular composition and coated granular composition |
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Cited By (1)
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JP2012087064A (en) * | 2010-10-15 | 2012-05-10 | House Foods Corp | Covered granulated matter comprising unpleasant taste component and solid composition for oral ingestion |
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JP2003001091A (en) * | 2001-06-26 | 2003-01-07 | Pauretsuku:Kk | Fluidized bed granulating and coating method |
JP4806969B2 (en) * | 2005-05-30 | 2011-11-02 | 日油株式会社 | Method for producing α-lipoic acid oil-coated powder and product thereof |
JP4602949B2 (en) * | 2006-08-02 | 2010-12-22 | 和光堂株式会社 | Coated particle-containing composition and method for producing the same |
JP5756727B2 (en) * | 2011-09-30 | 2015-07-29 | ハウス食品グループ本社株式会社 | Granule |
JP2015086171A (en) * | 2013-10-31 | 2015-05-07 | 三菱瓦斯化学株式会社 | Coated powder comprising pyrroloquinoline quinones, and production method thereof, as well as composition thereof |
JP6969786B2 (en) * | 2017-09-25 | 2021-11-24 | 株式会社イムダイン | Hydrogen adsorption composition |
JP2021185807A (en) * | 2020-05-28 | 2021-12-13 | オルト株式会社 | High protein food and production method of the same |
CN114271396B (en) * | 2021-12-31 | 2024-01-23 | 上海福贝宠物用品股份有限公司 | Preparation method of pet food capable of preventing unsaturated grease from being oxidized |
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Cited By (1)
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JP2012087064A (en) * | 2010-10-15 | 2012-05-10 | House Foods Corp | Covered granulated matter comprising unpleasant taste component and solid composition for oral ingestion |
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