JP2000053993A - Production of fat-and-oil-containing granule - Google Patents

Production of fat-and-oil-containing granule

Info

Publication number
JP2000053993A
JP2000053993A JP10260822A JP26082298A JP2000053993A JP 2000053993 A JP2000053993 A JP 2000053993A JP 10260822 A JP10260822 A JP 10260822A JP 26082298 A JP26082298 A JP 26082298A JP 2000053993 A JP2000053993 A JP 2000053993A
Authority
JP
Japan
Prior art keywords
fat
oil
granules
water
spraying
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.)
Pending
Application number
JP10260822A
Other languages
Japanese (ja)
Inventor
Toshiji Sugiura
利治 杉浦
Koji Tabata
浩治 田畑
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.)
Okawara Mfg Co Ltd
Original Assignee
Okawara Mfg Co Ltd
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 Okawara Mfg Co Ltd filed Critical Okawara Mfg Co Ltd
Priority to JP10260822A priority Critical patent/JP2000053993A/en
Publication of JP2000053993A publication Critical patent/JP2000053993A/en
Pending legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To obtain, using compact apparatuses, granules containing fat-and-oil in high concentrations, excellent in dissolvability and causing no blocking by adding fat-and-oil to a powder stock such as for food using an agitation granulator to conduct a primary granulation, followed by spraying the resultant granules with water or the like using a fluidized bed granulator to effect surface modification of the granules. SOLUTION: The objective granules are obtained by the following process: fat-and-oil is added to a powder stock such as for food or feed using an agitation granulator 1 to conduct a primary granulation, and the resulting granules are then sprayed with pref. fat-and-oil followed by water or hot water using a fluidized bed granulator 2 to effect surface modification of the granules, wherein it is preferable that the fat-and-oil spraying operation using the fluidized bed granulator is conducted under feeding of cooling air, while the (hot) water spraying is performed under feeding hot air.

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、食品や飼料の原料
粉体に油脂を添加して造粒する方法に関し、特に高濃度
に油脂を添加して造粒する油脂含有顆粒の製造方法に関
する。尚、本発明において高濃度油脂添加とは、原料粉
体100重量部に対して15重量部以上の油脂を添加す
ることをいう。また乳化油脂とは、油脂と水又は温水を
攪拌混合して、水又は温水中に油脂を分散させたものを
いう。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for granulating a raw material powder of food or feed by adding fats and oils, and more particularly to a method for producing fat-containing granules by adding fats and oils at a high concentration to granulate. In the present invention, adding high-concentration fats and oils means adding 15 parts by weight or more of fats and oils to 100 parts by weight of raw material powder. The emulsified fats and oils are those obtained by stirring and mixing the fats and oils with water or warm water to disperse the fats and oils in water or warm water.

【0002】[0002]

【従来の技術】家畜用の人工乳、代用乳などの飼料や調
味料、粉末ミルク、粉末スープなどの食品のように油脂
を添加した造粒物を得るのには、攪拌造粒方法や流動層
造粒方法が行われている。攪拌造粒方法では、油脂を高
速度で添加できる、大量処理が可能であるという特徴が
あるが、製品への油脂添加率上限が低い、油脂添加率を
高くすると製品を袋詰めしたとき圧密されてブロッキン
グする(粒子が塊状化すること)、溶解性が悪化すると
いう欠点があり、流動層造粒方法では、製品への油脂添
加率は比較的高く取れるものの、処理能力が流動層の形
成可能な油脂噴霧速度に依存するため(急速に噴霧する
と流動不良・流動不能になる)、大量処理ができず装置
が大型化するという欠点がある。
2. Description of the Related Art In order to obtain granules to which fats and oils are added, such as feeds such as artificial milk and milk substitutes for livestock and foods such as seasonings, powdered milks and powdered soups, a stirring granulation method and a fluidizing method are required. A layer granulation method has been performed. The agitation granulation method has the feature that fats and oils can be added at a high speed, and large-scale processing is possible.However, the upper limit of the fats and oils addition rate to the product is low, and when the fats and oils addition rate is high, the product is compacted when packed in a bag. Has the disadvantage that the solubility deteriorates. In the fluidized-bed granulation method, the addition rate of fats and oils to the product can be relatively high, but the processing capacity can form a fluidized bed. However, there is a disadvantage that the apparatus cannot be processed in a large amount and the apparatus becomes large in size because it depends on the oil spraying speed.

【0003】[0003]

【発明が解決しようとする課題】したがって、本発明の
解決しようとする課題は、油脂添加率が高く取れ、大量
処理が可能で、製品がブロッキングすることのない、溶
解性に優れた油脂含有顆粒の造粒方法を提供することで
ある。
SUMMARY OF THE INVENTION Accordingly, an object of the present invention is to provide a fat and oil-containing granule which has a high fat addition ratio, can be processed in a large amount, does not block products, and has excellent solubility. Is to provide a granulation method.

【0004】[0004]

【課題を解決するための手段】本発明者は、攪拌造粒
機、流動層造粒機を使用して粉体に高濃度に油脂を添加
する方法を種々検討した結果、攪拌造粒機と流動層造粒
機を組合わせて使用することによって、攪拌造粒のみで
は製品がブロッキングする油脂濃度であっても、これを
流動層造粒機で水または温水を噴霧して表面改質すれ
ば、ブロッキングを防止できること、また、攪拌造粒機
で油脂を添加し、さらに流動層造粒機で油脂を噴霧した
のち水または温水を噴霧し、あるいは乳化油脂を噴霧し
て表面改質すれば、ブロッキングを生じることなくさら
に高濃度に油脂を添加できることを見出して本発明を完
成させたものである。
The inventor of the present invention has studied various methods for adding fats and oils to powder at a high concentration using a stirring granulator and a fluidized bed granulator. By using a fluidized bed granulator in combination, even if the concentration of fats and oils is such that the product blocks only with stirring granulation, it can be sprayed with water or hot water with a fluidized bed granulator to modify the surface. , That blocking can be prevented, and if the surface is modified by adding fats and oils with a stirring granulator, spraying water or hot water after further spraying fats and oils with a fluidized bed granulator, or spraying emulsified fats and oils, The inventors have found that fats and oils can be added at a higher concentration without causing blocking, thereby completing the present invention.

【0005】すなわち、上記課題を解決するための請求
項1記載の方法は、食品や飼料などの粉体原料に、油脂
を高濃度に含有させた顆粒を造粒する油脂含有顆粒の製
造方法において、攪拌造粒機で油脂を添加して一次造粒
したのち、流動層造粒機で水又は温水を噴霧して表面改
質をすることを特徴とするものである。これによって、
攪拌造粒ではブロッキングしてしまう濃度まで油脂を添
加することが可能となる。
[0005] That is, a method according to the first aspect of the present invention for solving the above-mentioned problems is directed to a method for producing oil-and-fat-containing granules in which granules containing a high concentration of fats and oils in a powdery raw material such as food and feed are granulated. After adding oil and fat with a stirring granulator and performing primary granulation, water or hot water is sprayed with a fluidized bed granulator to perform surface modification. by this,
In stirring granulation, it is possible to add fats and oils to a concentration at which blocking occurs.

【0006】上記課題を解決するための請求項2記載の
方法は、食品や飼料などの粉体原料に、油脂を高濃度に
含有させた顆粒を造粒する油脂含有顆粒の製造方法にお
いて、攪拌造粒機で油脂を添加して一次造粒したのち、
流動層造粒機で油脂を噴霧し、さらに水または温水を噴
霧して表面改質をすることを特徴とする。これによっ
て、さらに高濃度まで油脂を添加することができる。
According to a second aspect of the present invention, there is provided a method for producing oil-and-fat-containing granules, comprising granulating granules containing a high concentration of fats and oils in a powder material such as food or feed. After the primary granulation by adding fats and oils with a granulator,
It is characterized by spraying oils and fats with a fluidized bed granulator and further spraying water or hot water to perform surface modification. Thereby, fats and oils can be added to a higher concentration.

【0007】上記課題を解決するための請求項3記載の
方法は、請求項2記載の要件に加えて、流動層造粒機に
おける油脂の噴霧が冷風供給下に行われ、水または温水
の噴霧が熱風供給下に行われることを特徴とする。これ
によって、油脂は冷風下に噴霧されるのですばやく粒子
表面で固化し、水または温水は熱風下に噴霧されるので
粒子の表面改質が速やかに行なうことができる。
According to a third aspect of the present invention, in addition to the requirements of the second aspect, the spraying of the fat or oil in the fluidized bed granulator is performed under a supply of cold air, and the spraying of water or hot water is performed. Is performed under hot air supply. As a result, the oils and fats are sprayed under cold air, so that they are quickly solidified on the particle surface, and water or hot water is sprayed under hot air, so that the surface modification of the particles can be performed quickly.

【0008】上記課題を解決するための請求項4記載の
方法は、食品や飼料などの粉体原料に、油脂を高濃度に
含有させた顆粒を造粒する油脂含有顆粒の製造方法にお
いて、攪拌造粒機で油脂を添加して一次造粒したのち、
流動層造粒機で乳化油脂を噴霧して表面改質をすること
を特徴とする。これによって、油脂と水または温水を別
々に噴霧する工程を簡略化することができる。
According to a fourth aspect of the present invention, there is provided a method for producing oil-and-fat-containing granules which comprises granulating granules containing a high concentration of fats and oils in a powder material such as food or feed. After the primary granulation by adding fats and oils with a granulator,
It is characterized in that the surface is modified by spraying emulsified fats and oils with a fluidized bed granulator. Thereby, the step of separately spraying the fat and oil and water or hot water can be simplified.

【0009】上記目的を達成するための請求項5記載の
方法は、請求項4記載の要件に加えて、乳化油脂の噴霧
が、熱風供給下で行われることを特徴とする。これによ
って、粒子の表面改質を速やかに行なうことができる。
A method according to a fifth aspect of the present invention for achieving the above object is characterized in that, in addition to the requirements described in the fourth aspect, the emulsified fat or oil is sprayed under a hot air supply. Thereby, the surface modification of the particles can be performed promptly.

【0010】[0010]

【発明の実施の形態】次に本発明の実施の形態を、図面
に基づいて説明する。図1は、特許請求の範囲の請求項
1記載の発明(第1の実施の形態)、または請求項4,
5記載の発明(第3の実施の形態)を実施する装置の模
式図であり、図2は、請求項2,3記載の発明(第2の
実施の形態)を実施する装置の模式図である。符号1は
攪拌造粒機であって、特にその形状は限定されないが特
開平6−182178号、特開平7−112124号に
示される攪拌造粒機、あるいは特公昭57−7769号
に示されるいわゆるシュギ式造粒機のような大量処理の
できる高速攪拌造粒機が望ましい。符号2は、流動層造
粒機であって、多孔板6下部には流動化気体を供給する
熱風吹込み室3および冷風吹込み室4が設けられ、多孔
板6上部には噴霧ノズル5が設けられた装置である。噴
霧ノズル5は、一流体ノズルであっても、二流体ノズル
であっても良く、噴霧するものに応じて使い分けること
ができる。
Embodiments of the present invention will now be described with reference to the drawings. FIG. 1 shows the invention according to claim 1 (first embodiment) or claim 4,
FIG. 2 is a schematic view of an apparatus for implementing the invention (third embodiment) according to the fifth aspect, and FIG. 2 is a schematic view of an apparatus for implementing the invention (second embodiment) according to the second and third aspects. is there. Reference numeral 1 denotes a stirring granulator, the shape of which is not particularly limited. However, the stirring granulator described in JP-A-6-182178 and JP-A-7-112124 or the so-called so-called JP-B-57-7770 is disclosed. A high-speed agitation granulator capable of mass processing, such as a Sugi-type granulator, is desirable. Reference numeral 2 denotes a fluidized bed granulator, in which a hot air blowing chamber 3 and a cold air blowing chamber 4 for supplying fluidized gas are provided below the perforated plate 6, and a spray nozzle 5 is provided above the perforated plate 6. It is a device provided. The spray nozzle 5 may be a one-fluid nozzle or a two-fluid nozzle, and can be used properly depending on what is sprayed.

【0011】図1に基づいて第1の実施の形態を説明す
る。飼料あるいは食品の粉体原料と油脂は、攪拌造粒機
1に投入されて造粒され、造粒物は流動層造粒機2に投
入される。流動層造粒機2の一端に投入された造粒物
は、他端に向かって流動移送される間に、熱風吹込み室
3の上部に設けた噴霧ノズルから水または温水を噴霧さ
れ、冷風吹込み室4上部で仕上げ冷却されて製品となり
流動層造粒機2から排出される。この間に、噴霧される
水または温水と冷却空気によって、粒子の表面が硬化す
るなどの表面改質作用を受ける。これによって、攪拌造
粒機による油脂添加では、ブロッキングが生じる物であ
っても、これを防止することができる。なお、熱風吹込
み室3に吹込まれる熱風は60〜100℃程度が望まし
く、冷風吹き込み室4に吹込まれる冷風は−5〜20℃
程度が望ましい。
A first embodiment will be described with reference to FIG. The feed or food powder raw material and the fats and oils are charged into the stirring granulator 1 and granulated, and the granulated material is charged into the fluidized bed granulator 2. The granulated material put into one end of the fluidized bed granulator 2 is sprayed with water or hot water from a spray nozzle provided at an upper part of the hot air blowing chamber 3 while being flow-transferred toward the other end, and cooled. The product is finished and cooled in the upper part of the air blowing chamber 4 to be a product, and is discharged from the fluidized bed granulator 2. During this time, the surface of the particles undergoes a surface modification action such as hardening by sprayed water or hot water and cooling air. Thereby, even if the blocking is caused by the addition of the fat or oil by the stirring granulator, this can be prevented. The hot air blown into the hot air blowing chamber 3 is desirably about 60 to 100 ° C., and the cool air blown into the cold air blowing chamber 4 is −5 to 20 ° C.
A degree is desirable.

【0012】次に図2に基づいて第2の実施の形態を説
明する。第2の実施の形態に使用される装置は、流動層
造粒機2の流動化気体の供給室が、造粒物投入側から製
品排出側に向って、冷風吹込み室4−1、熱風吹込み室
3、冷風吹き込み室4−2と区分されていて、冷風吹込
み室4−1の上部に油脂を噴霧する噴霧ノズル5−1
が、熱風吹込み室3の上部に水または温水を噴霧する噴
霧ノズル5−2が設けられていることを特徴とするが、
その他の点は第1の実施の形態で使用される装置と同じ
である。飼料あるいは食品の粉体原料と油脂は、攪拌造
粒機1に投入されて造粒され、造粒物は流動層造粒機2
に投入される。流動層造粒機2に投入された造粒物は、
冷風吹込み室4−1の上部で噴霧ノズル5−1からさら
に油脂(固形油脂を溶融したもの)を添加され、熱風吹
込み室3の上部で噴霧ノズル5−2から水または温水を
噴霧され、冷風吹込み室4−2で仕上げ冷却されて製品
として排出される。この間、油脂は冷風供給下に噴霧さ
れるので素早く固化し、熱風供給下に水または温水を噴
霧したのち仕上げ冷却されるので、粒子の表面が硬化す
るなどの表面改質作用が速やかに行われる。したがっ
て、より高濃度に油脂を添加してもブロッキングを生じ
ない溶解性に優れた顆粒を得ることができる。なお、冷
風吹込み室4−1に吹込まれる冷風は、常温程度が望ま
しいが、その他の温度は第1の実施の形態と同じで良
い。
Next, a second embodiment will be described with reference to FIG. In the apparatus used in the second embodiment, the fluidized-gas supply chamber of the fluidized-bed granulator 2 is configured such that the cold-air blowing chamber 4-1 moves from the granulated material input side to the product discharge side. A spray nozzle 5-1 which is divided into a wind blowing chamber 3 and a cold wind blowing chamber 4-2, and sprays oil and fat on an upper portion of the cold wind blowing chamber 4-1.
However, a spray nozzle 5-2 for spraying water or hot water is provided above the hot air blowing chamber 3,
Other points are the same as those of the device used in the first embodiment. Feed or food powder raw materials and fats and oils are put into a stirring granulator 1 and granulated, and the granulated material is fluidized bed granulator 2
It is thrown into. The granulated material charged into the fluidized bed granulator 2 is
Oil and fat (melted solid fat) is further added from the spray nozzle 5-1 at the upper part of the cold air blowing chamber 4-1 and water or hot water is sprayed from the spray nozzle 5-2 at the upper part of the hot air blowing chamber 3. Then, it is finished and cooled in the cold air blowing chamber 4-2 and discharged as a product. During this time, the fats and oils are sprayed under the supply of cold air, so that they quickly solidify, and are sprayed with water or hot water under the supply of hot air, and then subjected to finish cooling, so that the surface modification action such as hardening of the surface of the particles is quickly performed. . Therefore, it is possible to obtain granules excellent in solubility that do not cause blocking even when oils and fats are added at a higher concentration. The temperature of the cool air blown into the cool air blowing chamber 4-1 is preferably about room temperature, but other temperatures may be the same as those in the first embodiment.

【0013】次に図1に基づいて第3の実施の形態を説
明する。第3の実施の形態と第1の実施の形態の相違点
は、噴霧ノズル5から噴霧されるものが、第1の実施の
形態では水または温水であるの対し、第3の実施の形態
では乳化油脂であり、その他の点は共通である。これに
よれば、噴霧ノズル5から乳化油脂を噴霧するので油脂
の添加と造粒物の表面改質を同時に行なえるという効果
がある。
Next, a third embodiment will be described with reference to FIG. The difference between the third embodiment and the first embodiment is that what is sprayed from the spray nozzle 5 is water or hot water in the first embodiment, whereas it is water or hot water in the third embodiment. It is an emulsified fat, and the other points are common. According to this, since the emulsified fat is sprayed from the spray nozzle 5, there is an effect that the addition of the fat and oil and the surface modification of the granulated material can be performed at the same time.

【0014】[0014]

【実施例】次に仔牛の代用乳用の顆粒を、本発明による
方法および比較例として攪拌造粒したものを示す。
EXAMPLES Next, granules for milk replacer of calf are agitated and granulated as a method according to the present invention and as a comparative example.

【0015】[0015]

【表1】 [Table 1]

【0016】脱脂粉乳を主原料とする原料粉体100重
量部に対し油脂(タロー油)25重量部を攪拌造粒機1
で造粒した造粒品は、溶解性では満足できるもののブロ
ッキングの点で不満が残るものであった(試験1)。油
脂32重量部添加した造粒品は、溶解性でも満足できる
ものではなく、ブロッキングの点では不可であった(試
験2)。試験1の造粒品を流動層造粒機2に投入して水
を噴霧して表面改質を行ったところ、溶解性、ブロッキ
ングの点ともに満足できるものであった(試験3、第1
の実施の形態)。試験1の造粒品を流動層造粒機2に投
入に、冷風供給下に油脂12重量部を噴霧し、熱風供給
下に水8重量部を噴霧したところ、溶解性、ブロッキン
グの点ともに満足できるものであった(試験4、第2の
実施の形態)。さらに試験1の造粒品を流動層造粒機2
に投入し、熱風供給下で油脂12重量部と水8重量部か
らなる乳化油脂を噴霧したところ、この方法でも溶解
性、ブロッキングの点ともに満足できる造粒品を得るこ
とができた(試験5、第3の実施例)。
Agitating granulator 1 comprises 25 parts by weight of fat (tallow oil) per 100 parts by weight of raw material powder mainly composed of skim milk powder.
The granulated product obtained in the above was satisfactory in solubility, but was unsatisfactory in terms of blocking (Test 1). The granulated product to which 32 parts by weight of fat or oil was added was not satisfactory in terms of solubility, and was not possible in terms of blocking (Test 2). When the granulated product of Test 1 was charged into the fluidized bed granulator 2 and sprayed with water to perform surface modification, both the solubility and the blocking were satisfactory (Test 3, First Test).
Embodiment). Injecting the granulated product of Test 1 into the fluidized bed granulator 2, spraying 12 parts by weight of fats and oils under cold air supply and spraying 8 parts by weight of water under hot air supply. Both the solubility and blocking are satisfactory. It was possible (Test 4, Second Embodiment). Further, the granulated product of Test 1 is added to the fluidized bed granulator 2
And sprayed emulsified fats and oils consisting of 12 parts by weight of fats and oils and 8 parts by weight of water under hot air supply, and it was possible to obtain granules having satisfactory solubility and blocking in this method (Test 5). Third embodiment).

【0017】[0017]

【発明の効果】上述の通り、本発明は、攪拌造粒機と流
動層造粒機を組合わせて使用することによって、流動層
造粒では不可能な高速度の油脂添加を攪拌造粒過程でお
こない、流動層造粒過程で、攪拌造粒では困難な高含有
率までの油脂添加と、水または温水の噴霧による造粒品
の表面改質を行うので、溶解性に優れたブロッキングの
生じない高濃度に油脂を含有した顆粒を、コンパクトな
装置で得ることができる。
As described above, the present invention uses a combination of an agitation granulator and a fluidized bed granulator to reduce the rate of addition of fats and oils that cannot be achieved in a fluidized bed granulation process. In the fluidized bed granulation process, the addition of fats and oils to a high content, which is difficult with stirring granulation, and the surface modification of the granulated product by spraying with water or hot water, results in blocking with excellent solubility. Granules containing fats and oils at a high concentration can be obtained with a compact apparatus.

【0018】[0018]

【図面の簡単な説明】[Brief description of the drawings]

【図1】本発明の第1、第3の実施例に使用される装置
の模式図である。
FIG. 1 is a schematic view of an apparatus used in first and third embodiments of the present invention.

【図2】本発明の第2の実施例に使用される装置の模式
図である。
FIG. 2 is a schematic view of an apparatus used in a second embodiment of the present invention.

【符号の説明】[Explanation of symbols]

1………攪拌造粒機 2………流動層造粒機 3………熱風吹込み室 4………冷風吹込み室 5………噴霧ノズル 6………多孔板 1 stir granulator 2 fluidized bed granulator 3 hot air blowing chamber 4 cold air blowing chamber 5 spray nozzle 6 perforated plate

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】食品や飼料などの粉体原料に、油脂を高濃
度に含有させた顆粒を造粒する油脂含有顆粒の製造方法
において、攪拌造粒機で油脂を添加して一次造粒したの
ち、流動層造粒機で水又は温水を噴霧して表面改質をす
ることを特徴とする油脂含有顆粒の製造方法。
Claims: 1. A method for producing a fat-containing granule in which granules containing a high concentration of fats and oils are granulated into powdery raw materials such as foods and feeds. A method for producing oil-and-fat-containing granules, which comprises spraying water or warm water with a fluidized-bed granulator to perform surface modification.
【請求項2】食品や飼料などの粉体原料に、油脂を高濃
度に含有させた顆粒を造粒する油脂含有顆粒の製造方法
において、攪拌造粒機で油脂を添加して一次造粒したの
ち、流動層造粒機で油脂を噴霧し、さらに水または温水
を噴霧して表面改質をすることを特徴とする油脂含有顆
粒の製造方法。
2. A method for producing oil-and-fat-containing granules in which granules containing a high concentration of oil and fat are granulated into powdery raw materials such as foods and feeds. Thereafter, a method of producing oil-and-fat-containing granules, which comprises spraying oil or fat with a fluidized-bed granulator and further spraying water or hot water to perform surface modification.
【請求項3】流動層造粒機における油脂の噴霧が冷風供
給下に行われ、水または温水の噴霧が熱風供給下に行わ
れることを特徴とする請求項2記載の油脂含有顆粒の製
造方法。
3. The method for producing oil-containing granules according to claim 2, wherein the spraying of the fat or oil in the fluidized bed granulator is performed under a supply of cold air, and the spraying of water or hot water is performed under a supply of hot air. .
【請求項4】食品や飼料などの粉体原料に、油脂を高濃
度に含有させた顆粒を造粒する油脂含有顆粒の製造方法
において、攪拌造粒機で油脂を添加して一次造粒したの
ち、流動層造粒機で乳化油脂を噴霧して表面改質をする
ことを特徴とする油脂含有顆粒の製造方法。
4. A method for producing oil-and-fat-containing granules in which granules containing a high concentration of oil and fat are granulated into a powdery raw material such as food or feed, wherein the oil or fat is added by a stirring granulator to perform primary granulation. A method for producing oil-and-fat-containing granules, which comprises spraying the emulsified oil or fat with a fluidized-bed granulator and modifying the surface.
【請求項5】乳化油脂の噴霧が、熱風供給下で行われる
ことを特徴とする請求項4記載の油脂含有顆粒の製造方
法。
5. The method for producing oil-containing granules according to claim 4, wherein the spraying of the emulsified oil is performed under hot air supply.
JP10260822A 1998-08-11 1998-08-11 Production of fat-and-oil-containing granule Pending JP2000053993A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10260822A JP2000053993A (en) 1998-08-11 1998-08-11 Production of fat-and-oil-containing granule

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10260822A JP2000053993A (en) 1998-08-11 1998-08-11 Production of fat-and-oil-containing granule

Publications (1)

Publication Number Publication Date
JP2000053993A true JP2000053993A (en) 2000-02-22

Family

ID=17353252

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10260822A Pending JP2000053993A (en) 1998-08-11 1998-08-11 Production of fat-and-oil-containing granule

Country Status (1)

Country Link
JP (1) JP2000053993A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005185903A (en) * 2003-12-24 2005-07-14 Naris Cosmetics Co Ltd Oil spray installation for powder
CN104152272A (en) * 2014-07-23 2014-11-19 青岛和合汇途工程技术有限公司 Two-stage efficient soapstock desolventizing system for mixed oil refinement
JP2022515732A (en) * 2018-12-18 2022-02-22 スタミカーボン・ベー・フェー Urea granulator

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005185903A (en) * 2003-12-24 2005-07-14 Naris Cosmetics Co Ltd Oil spray installation for powder
CN104152272A (en) * 2014-07-23 2014-11-19 青岛和合汇途工程技术有限公司 Two-stage efficient soapstock desolventizing system for mixed oil refinement
JP2022515732A (en) * 2018-12-18 2022-02-22 スタミカーボン・ベー・フェー Urea granulator

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