JPH09315956A - Preparation of granule - Google Patents

Preparation of granule

Info

Publication number
JPH09315956A
JPH09315956A JP8137811A JP13781196A JPH09315956A JP H09315956 A JPH09315956 A JP H09315956A JP 8137811 A JP8137811 A JP 8137811A JP 13781196 A JP13781196 A JP 13781196A JP H09315956 A JPH09315956 A JP H09315956A
Authority
JP
Japan
Prior art keywords
powder
melting point
binder
flavor
raw material
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP8137811A
Other languages
Japanese (ja)
Other versions
JP3111165B2 (en
Inventor
Kazunori Sonobe
一憲 園部
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
House Foods Corp
Original Assignee
House Foods Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by House Foods Corp filed Critical House Foods Corp
Priority to JP08137811A priority Critical patent/JP3111165B2/en
Publication of JPH09315956A publication Critical patent/JPH09315956A/en
Application granted granted Critical
Publication of JP3111165B2 publication Critical patent/JP3111165B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To prepare the granules of a food, a medicine, etc., capable of emphasizing its flavor, fragrance, etc., excellent in texture, capable of being maintained in a good shape from their preparation time to their handling time. SOLUTION: This method for preparing the granules of a food, a medicine, etc., comprises mixing a powdery raw material with the powder of a binder having a melting point of 40-130 deg.C, heating and stirring the mixture at a higher temperature than the melting point of the binder powder or higher, simultaneously spraying the heated and melted products of solid fats containing a solid fat having a melting point of 40-120 deg.C in an amount of >=70% on the heated and stirred mixture, and subsequently cooling the mixture at a lower temperature than the melting point of the binder powder or lower. The powdery raw material includes various kinds of flavor materials and fragrant materials and is used in an amount of 70-95wt.%. The binder powder includes beef tallow and palm oil, and is used in an amount of 4-20wt.%. The solid fats are used in an amount of 1-20wt.%. The solid fats are the extract fats of a flavor raw component and/or a fragrant raw component, or the heated mixture of a raw material solid fat with the flavor raw material and/or the fragrant raw material. The method for preparing the granules is effective for granulating the powder of a single spice such as pepper, the powder of a mixed spice such as curry powder, etc.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【発明の属する技術分野】本発明は、食品、薬品等の造
粒物を製造するための方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing granules such as foods and medicines.

【0002】[0002]

【従来の技術】食品等の造粒物の製造方法として、粉末
素材を高融点のバインダー粉末と混合し、上記融点以上
に加熱した後融点以下に冷却する方法、あるいは、高融
点油脂を溶融状態で粉末素材に噴霧する方法等が提案さ
れている。上記の方法において、造粒のためにバインダ
ーを原料中に4〜20重量%(以下%と略称する)程度
用いる必要があり、通常バインダーとしては高融点油脂
等の特殊で高価な原料が使われる。ところで、先行技術
のように、単に風味材、香気材等の素材とバインダーと
を結合させた形態の粉末では、風味・香気等を十分に引
き立て難く、高融点のバインダーの量が多く造粒物の食
感がザラツキ、原料コストが上がるという問題があっ
た。一方、上記の問題がない程度にまでバインダーの融
点を下げたり、その量を減らすと、造粒物を計量充填す
る際計量升や充填機に溶融付着したり、輸送・保管時及
び取扱い時に造粒物が溶融結着して安定に形状を保持で
きないという問題があった。
2. Description of the Related Art As a method for producing granules such as foods, a powder material is mixed with a binder powder having a high melting point, heated above the melting point and then cooled to below the melting point, or a high melting point oil and fat is melted. Has proposed a method of spraying a powder material. In the above method, it is necessary to use about 4 to 20% by weight (hereinafter abbreviated as “%”) of binder in the raw material for granulation, and a special and expensive raw material such as high melting point oil is usually used as the binder. . By the way, as in the prior art, in the case of a powder in which a raw material such as a flavor material and an aroma material is simply combined with a binder, it is difficult to bring out the flavor and aroma sufficiently, and the amount of the high melting point binder is large. There was a problem that the texture was rough and the raw material cost increased. On the other hand, if the melting point of the binder is lowered to the extent that the above problems do not occur, or if the amount is reduced, it will melt and adhere to the weighing box or filling machine when the granulated material is weighed and filled, and it will not be produced during transportation, storage and handling. There is a problem that the particles are melt-bonded and cannot stably maintain their shape.

【0003】[0003]

【発明が解決しようとする課題】上記の事情に鑑み、本
発明者は、先行技術の造粒方法によるよりも、更に風味
・香気等が引き立ち、食感に優れ、かつ製造から取扱い
時を通して、良好に形状を保持し得る造粒物を製造する
ための新しい技術を開発することを目的として鋭意研究
を積み重ねた。その結果、粉末素材及びバインダー粉末
を粉体混合した後、該バインダーの融点以上に加熱混合
し、これに特定の融点とSFCを有する固体脂を加熱溶
融して噴霧し、冷却することによって、所期の目的を達
成し得ることを見出し、本発明を完成するに至った。ま
た、上記固体脂を風味・香気成分を含んだものとすれば
造粒物の風味・香気を更に引き立て得る。
In view of the above-mentioned circumstances, the present inventor has found that the flavor and aroma are more prominent, the texture is excellent, and the product is handled from the production to the handling, as compared with the granulation method of the prior art. Accurate research has been conducted for the purpose of developing a new technique for producing a granulated product capable of maintaining good shape. As a result, after the powder material and the binder powder are powder-mixed, they are heated and mixed at a temperature higher than the melting point of the binder, and solid fat having a specific melting point and SFC is heated and melted and sprayed, and then cooled. The present invention has been completed by finding that the objectives of the term can be achieved. Further, if the solid fat contains a flavor / aroma component, the flavor / aroma of the granulated product can be further enhanced.

【0004】[0004]

【課題を解決するための手段】上記課題を解決するため
の本発明は、粉末素材を融点40〜130°Cのバイン
ダー粉末と粉体混合した後、該混合物を該バインダー粉
末の融点以上で加熱混合すると共に、上記加熱混合中の
混合物に、融点40°C以上でかつ20°C以下のSF
Cが70以上の固体脂を加熱溶融して噴霧し、その後混
合物を該バインダー粉末の融点以下に冷却することを特
徴とする造粒物の製造方法、である。
According to the present invention for solving the above problems, a powder material is powder-mixed with a binder powder having a melting point of 40 to 130 ° C., and then the mixture is heated at a temperature equal to or higher than the melting point of the binder powder. While mixing, the mixture being heated and mixed with SF having a melting point of 40 ° C or higher and 20 ° C or lower.
A method for producing a granulated product, which comprises melting and spraying a solid fat having a C of 70 or more, and then cooling the mixture to a temperature not higher than the melting point of the binder powder.

【0005】[0005]

【発明の実施の形態】以下、本発明について詳細に説明
する。本発明で用いる主原料は、粉末素材、バインダー
粉末及び特定の固体脂である。粉末素材としては、原料
がバインダー粉末の融点以上に加熱された場合にも溶融
しない性質のものであればよく、各種風味材、香気材等
の粉末を単品乃至任意の組み合せで用いればよい。具体
的には、カレーパウダー、各種香辛料、動植物・魚介類
由来の粉末、食塩(焼成塩を含む)、糖質が例示され
る。粉末素材の粒度を500μm以下程度とすること
で、本発明の方法による造粒を好適になし得る。粉末素
材は全原料に対して70〜95%、好ましくは80〜9
0%用いるのがよい。これにより、得られる造粒物に風
味、香気等を好適に付与することができ、一方上記範囲
に満たないとこの効果が十分でなく、上記範囲を超える
と造粒し難い傾向がある。
BEST MODE FOR CARRYING OUT THE INVENTION The present invention will be described in detail below. The main raw materials used in the present invention are powder materials, binder powders and specific solid fats. Any powder material may be used as long as it does not melt even when the raw material is heated above the melting point of the binder powder, and powders such as various flavors and aroma materials may be used individually or in any combination. Specific examples thereof include curry powder, various spices, powder derived from animals and plants / seafood, salt (including baked salt), and sugar. By setting the particle size of the powder material to about 500 μm or less, granulation by the method of the present invention can be suitably performed. 70% to 95%, preferably 80% to 9%, of the powder material
It is recommended to use 0%. This makes it possible to suitably impart flavor, aroma and the like to the obtained granulated product. On the other hand, if the amount is less than the above range, this effect is not sufficient, and if it exceeds the above range, granulation tends to be difficult.

【0006】バインダー粉末は融点40〜130°C、
好ましくは60〜80°Cのもので、上記融点により得
られる造粒物が常温で適正に形状を保持し、かつ風味・
香気等の優れたものになる。融点が上記範囲に満たない
と計量充填時や取扱い時に造粒物が溶融結着しやすく、
これを超えると、当該融点以上での加熱により粉末素
材、固体脂の品質(風味・香気等)を損なうことがあ
る。バインダー粉末は、上記性能のものであれば何れで
もよく、牛脂、豚脂、ヤシ油、パーム油、大豆油、なた
ね油、綿実油、魚油等を硬化した固体脂粉末、鯨ロウ、
パームロウ、みつロウ等のロウ類粉末、マルトース等の
糖質粉末、グリセリンモノパルミチン酸エステル、グリ
セリンモノステアリン酸エステル等の乳化剤粉末等が挙
げられる。これらは、その融点、粉末素材・後記固体脂
の性質、造粒物の用途等を考慮して適宜選択して用い得
る。バインダー粉末の粒度を500μm以下程度とする
ことで、本発明の方法による造粒を好適になし得る。バ
インダー粉末は全原料に対して4〜20%、好ましくは
5〜10%用いるのがよい。これにより、造粒と形状保
持、風味・香気等の付与及び食感の改善を好適に達成し
得る。バインダーの添加量が上記範囲に満たないと造粒
と形状保持がし難く、一方これを超えると造粒物の風味
等が不十分となり、食感がザラザラし易い傾向がある。
The binder powder has a melting point of 40 to 130 ° C.
Preferably, the temperature is 60 to 80 ° C., and the granulated product obtained by the above melting point properly retains the shape at room temperature and has a flavor /
It becomes excellent in fragrance. If the melting point is less than the above range, the granulated material easily melts and binds during metering and filling,
If it exceeds this, heating above the melting point may impair the quality (flavor, aroma, etc.) of the powder material and solid fat. The binder powder may be any as long as it has the above performance, solid fat powder obtained by hardening beef tallow, lard, coconut oil, palm oil, soybean oil, rapeseed oil, cottonseed oil, fish oil, whale wax,
Examples thereof include wax powders such as palm wax and beeswax, sugar powders such as maltose, and emulsifier powders such as glycerin monopalmitate and glycerin monostearate. These may be appropriately selected and used in consideration of the melting point, powder material / property of solid fat described later, use of granulated product and the like. By setting the particle size of the binder powder to about 500 μm or less, the granulation by the method of the present invention can be suitably performed. The binder powder is used in an amount of 4 to 20%, preferably 5 to 10%, based on all raw materials. Thereby, granulation and shape retention, addition of flavor and aroma, and improvement of texture can be suitably achieved. If the added amount of the binder is less than the above range, it is difficult to granulate and maintain the shape. On the other hand, if it exceeds this range, the flavor and the like of the granulated product become insufficient and the texture tends to be rough.

【0007】次に、固体脂は、融点40°C以上(好ま
しくは40〜50°C)、20°C以下のSFC(固体
脂含量)が70以上の固体脂である。上記性能により、
造粒、形状保持及び食感の改善等の効果が好適に達成さ
れ、一方融点又はSFCが上記範囲に満たないと、造粒
及び形状保持が達成し難い。上記固体脂は風味成分及び
/又は香気成分を含むものであることが望ましく、これ
により造粒物により好適に風味・香気が付与される。上
記固体脂の原料油脂としては、前記性能を有する油脂を
任意に用い得、特にパーム油、牛脂、豚脂等の硬化油脂
を用いるのがよく、これにより造粒と形状保持、風味・
食感等の改善、原料コスト等の面で好適に所望の効果が
得られる。
Next, the solid fat is a solid fat having a melting point of 40 ° C. or higher (preferably 40 to 50 ° C.) and an SFC (solid fat content) of 20 ° C. or lower of 70 or higher. Due to the above performance,
The effects such as granulation, shape retention and texture improvement are suitably achieved, while if the melting point or SFC is less than the above range, granulation and shape retention are difficult to achieve. It is desirable that the solid fat contains a flavor component and / or an aroma component, and thereby the granules can suitably impart the flavor and aroma. As the raw material fats and oils of the above solid fats, fats and oils having the above-mentioned properties can be arbitrarily used, and it is particularly preferable to use hardened fats and oils such as palm oil, beef tallow, and lard, whereby granulation and shape retention, flavor and
Desired effects can be suitably obtained in terms of improving texture and cost of raw materials.

【0008】また、原料油脂に風味成分及び/又は香気
成分を含む場合の態様は任意であるが、以下の態様が好
適に例示される。即ち、固体脂を風味成分及び/又は香
気成分の抽出油とする。具体的には、原料油脂60〜9
0%と、任意の香辛料、調味料等、例えばカレーパウダ
ー、牛・豚・鶏の肉骨、オニオン、ガーリック、ジンジ
ャー等の香辛野菜等から選ばれた1乃至それ以上10〜
40%とを、60〜140°Cで加熱処理した後残渣を
除いて得た香味油とすればよい。他に、原料油脂70〜
80%と風味原料及び/又は香気原料(ガーリック、ジ
ンジャー等)20〜30%とを加熱混合したものとする
こともできる。上記固体脂は全原料に対して1〜20
%、好ましくは5〜15%用いるのがよい。これによ
り、造粒と形状保持、風味・香気等の付与、食感の改善
を好適に達成し得、上記範囲を外れるとこれらの効果が
不十分となることがある。尚、本発明の主旨を逸脱しな
い範囲で、以上の主原料とは別の原料を用い得ることは
勿論である。
[0008] Further, the case where the raw material fat contains a flavor component and / or an aroma component is arbitrary, but the following modes are preferably exemplified. That is, the solid fat is used as the extracted oil of the flavor component and / or the aroma component. Specifically, the raw material fat 60 to 9
0% and 1 or more selected from spices and seasonings, such as curry powder, beef / pork / chicken meat and bones, onion, garlic, spicy vegetables such as ginger.
40% may be used as a flavor oil obtained by removing the residue after heat treatment at 60 to 140 ° C. In addition, the raw material oil 70
It is also possible to heat-mix 80% and 20 to 30% of a flavor raw material and / or an aroma raw material (garlic, ginger, etc.). The above solid fat is 1 to 20 with respect to all raw materials.
%, Preferably 5 to 15%. As a result, granulation and shape retention, addition of flavor and aroma, and improvement of texture can be suitably achieved, and if these values are out of the above ranges, these effects may be insufficient. Needless to say, a raw material different from the above main raw materials can be used without departing from the scope of the present invention.

【0009】次に、以上の原料を用いて造粒物を製造す
る方法について述べる。本発明においては、先ず、バイ
ンダー粉末の融点に満たない温度で、粉末素材をバイン
ダー粉末と粉体混合し、両者を均一に分散させる。上記
混合後、得られた混合物をバインダー粉末の融点以上で
加熱混合する。加熱混合は、混合物に下記の溶融固体脂
を均一に付着させて好適に造粒物を得、また造粒物の粒
径を小さなサイズに揃える上で、斜軸型撹拌混合釜、横
型ニーダー等により撹拌下で行うのが望ましい。加熱は
直接加熱、間接加熱を問わないが、乾式加熱であること
を要する。加熱混合は混合物の品温がバインダーの融点
以上に達した時点で、できるだけ速やかに終えるように
して行う(例えば、混合物が上記品温に達した後5〜1
5分間程度同品温で保持する)のが適当である。尚、前
記の粉体混合から加熱混合を連続的に行い得ることはい
うまでもない。本発明では、上記加熱混合中の混合物
に、前記特定の固体脂を加熱溶融して噴霧する。加熱溶
融は当該固体脂の融点以上に加熱して行えばよく、噴霧
は混合物に溶融固体脂を均一に噴霧できるものであれば
任意の手段で行い得る。上記噴霧は混合物の品温をバイ
ンダーの融点以上に保持する間均一に行うことが、所望
の効果を得る上で望ましい。
Next, a method for producing a granulated product using the above raw materials will be described. In the present invention, first, the powder material is powder-mixed with the binder powder at a temperature lower than the melting point of the binder powder, and both are uniformly dispersed. After the above mixing, the obtained mixture is heated and mixed at a temperature not lower than the melting point of the binder powder. The heat-mixing is carried out by uniformly adhering the following molten solid fat to the mixture to obtain a granulated product, and in adjusting the particle size of the granulated product to a small size, a slant shaft type stirring and mixing pot, a horizontal kneader, etc. Therefore, it is desirable to carry out it under stirring. Heating may be direct heating or indirect heating, but dry heating is required. The heat-mixing is performed so as to finish as soon as possible when the product temperature of the mixture reaches the melting point of the binder or higher (for example, 5-1 after the mixture reaches the product temperature).
It is suitable to keep the same temperature for about 5 minutes). It goes without saying that the powder mixing and the heat mixing can be continuously performed. In the present invention, the specific solid fat is heated and melted and sprayed onto the mixture being heated and mixed. The heating and melting may be carried out by heating above the melting point of the solid fat, and the spraying may be performed by any means as long as the molten solid fat can be uniformly sprayed onto the mixture. It is desirable that the spraying is performed uniformly while maintaining the product temperature of the mixture at the melting point of the binder or higher in order to obtain a desired effect.

【0010】上記加熱した混合物をバインダー粉末の融
点以下に冷却し、バインダーを凝固させて求める造粒物
を得る。冷却は静置下、撹拌下の何れでも行い得るが、
流動層等で撹拌下で行うことが粒径の揃った均一な造粒
物を得る上で望ましい。得られた造粒物は、必要に応じ
て、更に整粒、篩別等の適宜工程を施せばよい。得られ
た造粒物は、適宜計量、容器包装等して製品化すればよ
く、この場合、造粒物は形状保持が安定で溶融して装置
等に付着せず、円滑に処理できて優れた加工適性を有す
る。
The heated mixture is cooled below the melting point of the binder powder, and the binder is solidified to obtain the desired granulated product. Cooling can be carried out under standing or stirring,
It is desirable to carry out stirring in a fluidized bed or the like in order to obtain a uniform granulated product having a uniform particle size. The obtained granulated product may be subjected to appropriate steps such as sizing and sieving, if necessary. The obtained granulated product may be appropriately weighed, packaged, and the like to be commercialized. In this case, the granulated product has stable shape retention, does not melt and does not adhere to a device, etc., and is smoothly processed, which is excellent. It has good workability.

【0011】本発明により高品質の造粒物が得られるメ
カニズムについては、次のように考えられる。即ち、粉
体混合された粉末素材及びバインダー粉末を、バインダ
ーの融点以上に加熱すると、表面が溶融したバインダー
粉末に周りの粉末素材が結着され、これと同時に、噴霧
された微粒状の溶融固体脂が上記粉末素材及びバインダ
ー粉末の表面に結着する。これにより、バインダーの造
粒機能を損なわず、かつ上記固体脂がこれを促進して、
安定に造粒が達成される。また、上記のようにして得ら
れた造粒物では、バインダー及び固体脂が形状保持に寄
与し、極めて安定な造粒物になると共に、固体脂に含ま
れた風味・香気成分によって風味・香気が補強され、バ
インダーを適当量用い得、よって、風味・香気及び食感
が改善されたものとなるのである。尚、粉末素材、バイ
ンダー粉末及び固体脂を一緒に混合して加熱しても、先
に溶融した固体脂がダマをつくり、バインダーの造粒機
能が達成されず良好に造粒できないが、本発明における
特定の構成により前記所望の作用効果を得ることができ
る。
The mechanism by which high quality granules are obtained by the present invention is considered as follows. That is, when powdered powder material and binder powder are heated above the melting point of the binder, the surrounding powder material is bound to the binder powder whose surface has melted, and at the same time, the finely divided molten solid that is sprayed. The fat binds to the surface of the powder material and the binder powder. Thereby, without impairing the granulation function of the binder, and the solid fat promotes this,
Granulation is achieved stably. Further, in the granulated product obtained as described above, the binder and the solid fat contribute to shape retention and become an extremely stable granulated product, and at the same time, the flavor and aroma components are contained in the solid fat. Are reinforced, and an appropriate amount of binder can be used, so that the flavor / aroma and texture are improved. Even if the powder material, the binder powder, and the solid fat are mixed and heated together, the solid fat that has been melted first forms lumps, and the granulation function of the binder cannot be achieved, resulting in poor granulation. According to the specific configuration of the above, the desired effect can be obtained.

【0012】次に、実施例に基づいて本発明を具体的に
説明するが、本発明は当該実施例によって何ら限定され
るものではない。
Next, the present invention will be specifically described based on examples, but the present invention is not limited to the examples.

【実施例1】カレーパウダー68重量部(以下部と略称
する)、焼成塩10部、可溶性デンプン11部及びバイ
ンダーである融点75℃のなたね硬化粉末油脂6部をジ
ャケット付き撹拌機で均一に撹拌混合した。これとは別
に、融点45℃で下記のSFCを有する硬化パーム油8
0%、ジンジャー10%、ガーリック10%を約110
°Cで約60分間加熱処理した後残渣を除いて得た香味
油を、約60°Cで溶融状態でストックした。前記撹拌
機中の混合物を品温が約80°Cになるまで加熱撹拌混
合し、混合物が上記品温に達した時点で、これに前記溶
融香味油5部を噴霧機で均一にスプレーした。上記処理
後の混合物を流動層で約40°Cに冷却し篩別して、粒
度約1000μm以下で均一な粒度を有する造粒物を得
た。
Example 1 68 parts by weight of curry powder (hereinafter abbreviated as "part"), 10 parts of calcined salt, 11 parts of soluble starch and 6 parts of rape-cured powdered fat and oil having a melting point of 75 ° C as a binder were uniformly mixed with a stirrer with a jacket. Mix with stirring. Separately, hydrogenated palm oil 8 having the following SFC with a melting point of 45 ° C. 8
0%, ginger 10%, garlic 10% about 110
The flavor oil obtained by removing the residue after heat treatment at about 60 ° C for about 60 minutes was stocked at about 60 ° C in a molten state. The mixture in the stirrer was heated and stirred and mixed until the product temperature reached about 80 ° C., and when the mixture reached the product temperature, 5 parts of the molten flavor oil was uniformly sprayed with a sprayer. The mixture after the above treatment was cooled to about 40 ° C. in a fluidized bed and sieved to obtain a granulated product having a uniform particle size of about 1000 μm or less.

【0013】原料の粒度は、各々カレーパウダーが約3
00μm以下、焼成塩が約250μm以下、なたね硬化
粉末油脂が約600μm以下であった。また、硬化パー
ム油のSFCは、10°C:73.5、15°C:7
3.5、20°C:73.5、25°C:69.4、3
0°C:57.5、35°C:39.5、40°C:2
2.9、45°C:7.2、50°C:6.0であっ
た。製造された造粒物は、カレーパウダーとローストし
たジンジャー、ガーリックの風味が融合した特有の風味
を十分に有するものであった。また、上記造粒物は、計
量乃至充填までの間ホッパー式定量供給装置の計量升に
溶融付着せず正確に計量でき、縦ピロー包装機で良好に
充填包装できた。上記の造粒物によれば、夏期において
も溶融結着せず、またカレーを調理する際に風味材とし
て加えて、カレーに前記特有の風味を醸し出し、ザラつ
いた食感のないものであった。
The particle size of the raw material is about 3 for each curry powder.
It was less than 00 μm, the calcined salt was less than about 250 μm, and the rape-hardened powder oil was about 600 μm or less. The SFC of hardened palm oil is 10 ° C: 73.5, 15 ° C: 7.
3.5, 20 ° C: 73.5, 25 ° C: 69.4, 3
0 ° C: 57.5, 35 ° C: 39.5, 40 ° C: 2
The temperatures were 2.9, 45 ° C: 7.2 and 50 ° C: 6.0. The produced granulated product had a sufficient unique flavor in which the flavors of curry powder, roasted ginger, and garlic were fused. In addition, the above granulated product was able to be accurately weighed without being melted and adhered to the weighing box of the hopper type constant-volume feeding device during the period from weighing to filling, and it could be well filled and packed in the vertical pillow packaging machine. According to the above granulated product, it was not melt-bonded even in the summer, and was added as a flavoring material when cooking curry, to produce the above-mentioned unique flavor in curry, and there was no rough texture. .

【0014】[0014]

【発明の効果】以上詳述したように、本発明によれば、
形状維持に優れ、かつ風味・香気が十分に引き立て等
れ、バインダー由来の食感のザラツキがない高品質の造
粒物を製造することが可能となる。よって、本発明は、
胡椒等の単品香辛料粉末やカレーパウダー等の調合香辛
料粉末等の造粒に適する利点を有する。
As described in detail above, according to the present invention,
It is possible to produce a high-quality granulated product which is excellent in shape retention, fully enhances the flavor and aroma, and has no graininess of the texture derived from the binder. Therefore, the present invention
It has an advantage that it is suitable for granulating a single spice powder such as pepper and a mixed spice powder such as curry powder.

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 粉末素材を融点40〜130°Cのバイ
ンダー粉末と粉体混合した後、該混合物を該バインダー
粉末の融点以上で加熱混合すると共に、上記加熱混合中
の混合物に、融点40°C以上でかつ20°C以下のS
FCが70以上の固体脂を加熱溶融して噴霧し、その後
混合物を該バインダー粉末の融点以下に冷却することを
特徴とする造粒物の製造方法。
1. A powder material is powder-mixed with a binder powder having a melting point of 40 to 130 ° C., and then the mixture is heated and mixed at a temperature not lower than the melting point of the binder powder, and the mixture being heated and mixed has a melting point of 40 °. S above C and below 20 ° C
A method for producing a granulated product, characterized in that a solid fat having an FC of 70 or more is melted by heating and sprayed, and then the mixture is cooled to a temperature not higher than the melting point of the binder powder.
【請求項2】 上記固体脂が風味成分及び/又は香気成
分を含むものである請求項1記載の製造方法。
2. The production method according to claim 1, wherein the solid fat contains a flavor component and / or an aroma component.
【請求項3】 上記固体脂が、風味成分及び/又は香気
成分の抽出油であるか、あるいは原料固体脂と風味原料
及び/又は香気原料とを加熱混合したものである請求項
2記載の製造方法。
3. The production according to claim 2, wherein the solid fat is an extracted oil of a flavor component and / or an aroma component, or a raw solid fat and a flavor raw material and / or an aroma raw material are heated and mixed. Method.
【請求項4】 粉末素材70〜95重量%、バインダー
粉末4〜20重量%及び固体脂1〜20重量%を用いる
請求項1〜3何れか1項に記載の製造方法。
4. The production method according to claim 1, wherein 70 to 95% by weight of powder material, 4 to 20% by weight of binder powder and 1 to 20% by weight of solid fat are used.
JP08137811A 1996-05-31 1996-05-31 Method for producing granulated material Expired - Lifetime JP3111165B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP08137811A JP3111165B2 (en) 1996-05-31 1996-05-31 Method for producing granulated material

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP08137811A JP3111165B2 (en) 1996-05-31 1996-05-31 Method for producing granulated material

Publications (2)

Publication Number Publication Date
JPH09315956A true JPH09315956A (en) 1997-12-09
JP3111165B2 JP3111165B2 (en) 2000-11-20

Family

ID=15207416

Family Applications (1)

Application Number Title Priority Date Filing Date
JP08137811A Expired - Lifetime JP3111165B2 (en) 1996-05-31 1996-05-31 Method for producing granulated material

Country Status (1)

Country Link
JP (1) JP3111165B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008295380A (en) * 2007-05-31 2008-12-11 Ikari Super Market:Kk Foodstuff containing gaba and its preparation method
WO2011121989A1 (en) * 2010-03-29 2011-10-06 株式会社カネカ Coating fat composition and particulate composition using same

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008295380A (en) * 2007-05-31 2008-12-11 Ikari Super Market:Kk Foodstuff containing gaba and its preparation method
WO2011121989A1 (en) * 2010-03-29 2011-10-06 株式会社カネカ Coating fat composition and particulate composition using same

Also Published As

Publication number Publication date
JP3111165B2 (en) 2000-11-20

Similar Documents

Publication Publication Date Title
EP0594152B1 (en) Method for preparing granular foods
JPS60145055A (en) Preparation of food containing granular fats and oils
EA023270B1 (en) Granular savoury food concentrate and process to produce the same
CA2295883C (en) Particulate flavour composition
JPH10503651A (en) Hydrothermally degradable binder based on fat-coated starch particles
JP3111165B2 (en) Method for producing granulated material
KR20130012102A (en) Preparation method of homogeneously mixed spice mixture
JPS60184378A (en) Production of granular food
JP3488851B2 (en) Rou production method
JPS62118846A (en) Granular edible composition
JP2582526B2 (en) Granular flavor seasoning and method for producing the same
JPH0618518B2 (en) Flavored oil and its manufacturing method
JP2000050795A (en) Granular oil and fat, and its production
JPS58116652A (en) Granular seasoning containing fat or oil and preparation thereof
JPH1169962A (en) Coarse particle type cooking auxiliary substance
JP2007006742A (en) Instant food
JP3705346B2 (en) Method for producing pasty roux
JP2018086025A (en) Block-shaped instant food composition and production method therefor
JPH08512206A (en) Method for producing coated food
JPH03183441A (en) Production of solid flavor oil
WO2021241107A1 (en) Coated organic acid for food additives and shelf-life improver for food
JP3574617B2 (en) Method for producing roasted flour
JP4196507B2 (en) Powdered colorant and method for producing the same
JP3265263B2 (en) Method for producing solid roux
CN109982579B (en) Method for preparing food particles

Legal Events

Date Code Title Description
FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20080914

Year of fee payment: 8

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20080914

Year of fee payment: 8

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090914

Year of fee payment: 9

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090914

Year of fee payment: 9

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20100914

Year of fee payment: 10

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20110914

Year of fee payment: 11

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20110914

Year of fee payment: 11

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20120914

Year of fee payment: 12

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20120914

Year of fee payment: 12

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20130914

Year of fee payment: 13

S533 Written request for registration of change of name

Free format text: JAPANESE INTERMEDIATE CODE: R313533

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350

EXPY Cancellation because of completion of term