JPS5810059B2 - Method for producing granular potato starch - Google Patents

Method for producing granular potato starch

Info

Publication number
JPS5810059B2
JPS5810059B2 JP56028606A JP2860681A JPS5810059B2 JP S5810059 B2 JPS5810059 B2 JP S5810059B2 JP 56028606 A JP56028606 A JP 56028606A JP 2860681 A JP2860681 A JP 2860681A JP S5810059 B2 JPS5810059 B2 JP S5810059B2
Authority
JP
Japan
Prior art keywords
potato starch
solution
fluidized
temperature
granulated
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.)
Expired
Application number
JP56028606A
Other languages
Japanese (ja)
Other versions
JPS57144952A (en
Inventor
三浦▲あきら▼梧
山谷治
西田浩男
長屋幸一
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.)
HOKUREN NOGYO KYODO KUMIAI RENGOKAI
Original Assignee
HOKUREN NOGYO KYODO KUMIAI RENGOKAI
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 HOKUREN NOGYO KYODO KUMIAI RENGOKAI filed Critical HOKUREN NOGYO KYODO KUMIAI RENGOKAI
Priority to JP56028606A priority Critical patent/JPS5810059B2/en
Publication of JPS57144952A publication Critical patent/JPS57144952A/en
Publication of JPS5810059B2 publication Critical patent/JPS5810059B2/en
Expired legal-status Critical Current

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Description

【発明の詳細な説明】 この発明は浮遊懸濁状態の馬鈴薯澱粉を噴霧した馬鈴薯
澱粉の糊化溶液の粒子に凝集して微顆粒状の馬鈴薯澱粉
を造る方法に係るものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing finely granulated potato starch by agglomerating potato starch in a floating suspension state into particles of a sprayed potato starch gelatinization solution.

従来より馬鈴薯澱粉は糊化温度が低いことや粘度が高い
ことなどから食品業界や化学業界などで広く利用されて
いる。
Potato starch has been widely used in the food and chemical industries due to its low gelatinization temperature and high viscosity.

しかしながら、馬鈴薯澱粉はそのままでは粉末であるた
めに飛散性があるとともにそのまま水に溶解したり、ま
たは馬鈴薯澱粉とかまぼこ、ハンペンなどの水分を含ん
だ状態の原料と混合したりなどすると、馬鈴薯澱粉がい
わゆる「だま」になりやすい欠点があり、馬鈴薯澱粉の
「だま」になったのをこねたり、つぶしたりなどして「
だま」をなくするには人手などとその作業時間を必要と
し、かつその作業などをすることにより最終製品である
食品などの品質劣化の原因にもなる場合があるので馬鈴
薯澱粉を水を溶解する時などに「だま」にならないよう
な馬鈴薯澱粉の出現が強(望まれている。
However, since potato starch is a powder as it is, it is easily dispersed, and if it is dissolved in water as it is, or mixed with raw materials containing water such as kamaboko or hanpen, potato starch becomes Potato starch has the disadvantage that it tends to form lumps, so if you knead or crush the lumps of potato starch,
Eliminating lumps requires labor and time, and doing so may cause quality deterioration of the final product, such as food, so potato starch is dissolved in water. It is hoped that the potato starch will be strong enough to not become lumpy during cooking.

そして従来より粉体の顆粒化について種々の製造方法が
公表されており、例えばコンスターチ、ワキンコーンス
ターチ、小麦澱粉の顆粒は馬鈴薯澱粉に較べてきわめて
造りやすい条件で容易に顆粒化することができるが、馬
鈴薯澱粉の顆粒は困難な問題があるために今まで実現さ
れていない。
Various manufacturing methods have been published for granulating powders. For example, granules of cornstarch, waxed cornstarch, and wheat starch can be easily granulated under conditions that are much easier to produce than potato starch. Potato starch granules have not been realized until now due to difficult problems.

その実現されていない理由としては馬鈴薯澱粉は水分を
よくすい込みすぎるので造粒することができないし、ま
た他の結合剤、例えば乳糖、アルギン酸ソーダ、ゼラチ
ンを使用して顆粒化すると、馬鈴薯澱粉が有する固有の
特性である高粘度が低下してしまうので顆粒化した馬鈴
薯澱粉の製品価値が著しく低下してしまうためである。
The reason why this has not been achieved is that potato starch absorbs too much water and cannot be granulated, and that granulation using other binders, such as lactose, sodium alginate, and gelatin, makes potato starch This is because the high viscosity, which is an inherent property of the granulated potato starch, is reduced, and the product value of the granulated potato starch is significantly reduced.

この発明はこのような現状に鑑みて、溶解性がよくて分
散性にすぐれていて「だま」にならないことや飛散性を
防止すること、比較的低い糊化温度、高粘度などの良い
性状をほとんど変えないことなどを目的としたものであ
る。
In view of the current situation, this invention has good properties such as good solubility and dispersibility, does not form lumps and prevents scattering, relatively low gelatinization temperature, and high viscosity. The purpose is to make almost no changes.

この発明の顆粒馬鈴薯澱粉の製造方法において、馬鈴薯
澱粉は市販のものを用い、結合剤としての馬鈴薯澱粉の
糊化溶液は市販の馬鈴薯澱粉に多量の水を加えて液温8
0℃位になるまで数分間加熱攪拌して糊化し、濃度約1
〜5%位にしたものを用いる。
In the method for producing granular potato starch of the present invention, commercially available potato starch is used, and a gelatinized solution of potato starch as a binder is prepared by adding a large amount of water to commercially available potato starch at a liquid temperature of 8.
Heat and stir for several minutes until the temperature reaches about 0°C to gelatinize and reduce the concentration to about 1.
~5% is used.

馬鈴薯澱粉を流動造粒装置に入れ、下から50℃から6
0℃に加熱した圧縮空気を入れると、馬鈴薯澱粉は流動
造粒装置の室内で吹き上げる空気中で浮遊懸濁している
状態、いわゆる流動化状態になる。
Put the potato starch into a fluidized granulator and heat it from 50℃ to 6℃ from the bottom.
When compressed air heated to 0° C. is introduced, the potato starch becomes suspended in the air blown up inside the chamber of the fluidized granulator, a so-called fluidized state.

このように流動化状態の馬鈴薯澱粉が存在している室内
に結合剤である馬鈴薯澱粉の糊化溶液を毎分100〜2
50m1の割合で噴霧することにより糊化溶液の粒子を
結合核として流動化状態の馬鈴薯澱粉が結合核の周囲に
凝集して成長し、微顆粒状の馬鈴薯澱粉となる。
In this way, a gelatinizing solution of potato starch, which is a binder, is poured into the chamber where potato starch in a fluidized state is present at a rate of 100 to 20% per minute.
By spraying at a rate of 50 ml, potato starch in a fluidized state aggregates and grows around the binding nuclei using particles of the gelatinizing solution as binding nuclei, resulting in finely granular potato starch.

流動化状態の馬鈴薯澱粉の温度(品温)は高い方が望し
いが、糊化開始温度が低いことなどから、約50℃以下
に保持する必要がある。
Although it is desirable that the temperature (product temperature) of potato starch in a fluidized state be high, it is necessary to maintain it at about 50° C. or lower because the gelatinization start temperature is low.

このようにして造った顆粒馬鈴薯澱粉を乾燥してから篩
分機で篩分けしてほぼ一定の大きさの顆粒馬鈴薯澱粉を
造って、製品として販売する方が望しいこの発明の製造
方法で造った顆粒馬鈴薯澱粉は馬鈴薯澱粉本来の糊化温
度および高粘度などの性状をほとんど変えることなく、
従来の馬鈴薯澱粉と同様に使用することができるし、ま
た溶解性が良(て水に直ちに溶けるとともに分散性が優
れていて水に溶かしてから使用することなくそのまま他
の原料に加えても「だま」になることなく、他の原料と
ほぼ均一に混合することができる。
The granular potato starch thus produced is dried and then sieved by a sieving machine to produce granular potato starch of approximately constant size, which is preferably produced by the production method of the present invention and sold as a product. Granular potato starch has almost no change in the original properties of potato starch, such as its gelatinization temperature and high viscosity.
It can be used in the same way as conventional potato starch, and it has good solubility (it immediately dissolves in water and has excellent dispersibility), so it can be added to other raw materials without having to be dissolved in water before use. It can be mixed almost uniformly with other ingredients without forming lumps.

この発明の製造方法で造った顆粒馬鈴薯澱粉は顆粒であ
るので袋より出して使用する際に飛散することがないた
めに1度に大量に加えることができるし、1度に大量に
加えて水に溶解したりなどして作業性がよいとともに作
業する人が従来の馬鈴薯澱粉のように飛散した粉を吸込
むことがないために衛生上も良い。
Since the granular potato starch produced by the production method of this invention is in the form of granules, it does not scatter when taken out of the bag and used, so it can be added in large quantities at one time, and it can be added in large quantities at one time and watered with water. It is easy to work with, as it can be dissolved in water, and it is also hygienic because workers do not have to inhale scattered powder like they would with conventional potato starch.

この発明の製造方法で造った顆粒馬鈴薯澱粉をから揚げ
月初として使用すると粉がほぼ均一に付着し、かつ油切
れが良(てから揚げしたものはソフトな仕上りにするこ
とができる。
When the granulated potato starch produced by the production method of this invention is used as a fried chicken, the flour will adhere almost uniformly and the oil will drain well (the fried food will have a soft finish).

次にこの発明の実施例について説明する。Next, embodiments of the invention will be described.

実施例 1 馬鈴薯澱粉(水分18%、アミログラフィー特性値粘度
1300Bu、糊化開始温度61.5℃)5kgを流動
造粒装置10室内2に入れて完全密閉する。
Example 1 5 kg of potato starch (moisture 18%, amyographic characteristic value viscosity 1300 Bu, gelatinization start temperature 61.5° C.) is placed in chamber 2 of fluidized granulation device 10 and completely sealed.

2%馬鈴薯澱粉水溶液21を液温80℃位になるまで1
0分間程度加熱攪拌して糊化溶液を造る。
2% potato starch aqueous solution 21 until the temperature of the solution reaches 80℃
Heat and stir for about 0 minutes to prepare a gelatinized solution.

この糊化溶液を流動造粒装置1の溶液タンク3にに入れ
て溶液タンク3を70℃位に加温状態にして糊化溶液を
糊化状態に維持する。
This gelatinized solution is put into the solution tank 3 of the fluidized granulator 1, and the solution tank 3 is heated to about 70° C. to maintain the gelatinized solution in a gelatinized state.

流動造粒装置10室内2の下方に位置する圧縮空気入口
4より50℃から60℃位に加熱した圧縮空気を毎秒1
.65mの速さで噴出することにより室内2の馬鈴薯澱
粉は流動造粒装置10室内2で次ぎ上がる空気中で浮遊
懸濁している状態、いわゆる流動化状態になり、馬鈴薯
澱粉の品温は50℃以下に調節する。
Compressed air heated to about 50°C to 60°C is supplied from the compressed air inlet 4 located below the chamber 2 of the fluidized granulation device 10 at a rate of 1 per second.
.. By ejecting at a speed of 65 m, the potato starch in room 2 becomes suspended in the air that rises next in room 2 of the fluidized granulator 10, a so-called fluidized state, and the temperature of the potato starch is 50°C. Adjust as below.

この流動造粒装置10室内2に溶液タンク3より糊化溶
液を噴霧ノズル口径(直径)1.8mm噴霧量毎分14
0m/噴霧空気圧3Kg/cm2の条件で噴霧すること
により室内2に噴霧した糊化溶液の粒子を結合核にして
室内2に流動化状態の馬鈴薯澱粉の粉末が次第に凝集し
て顆粒に成長する。
The gelatinizing solution is sprayed from the solution tank 3 into the chamber 2 of this fluidized granulation device 10 with a nozzle diameter (diameter) of 1.8 mm and a spray rate of 14 mm per minute.
By spraying under the conditions of 0 m/spraying air pressure of 3 Kg/cm2, the particles of the gelatinizing solution sprayed into the chamber 2 serve as binding nuclei, and the potato starch powder in a fluidized state in the chamber 2 gradually aggregates and grows into granules.

顆粒に成長したものは重(なって室内2の底に沈下し、
流動化状態の馬鈴薯澱粉は室内2で依然として浮遊して
噴霧した糊化溶液の粒子に次第に凝集していく。
Those that have grown into granules become heavy (and sink to the bottom of room 2,
The potato starch in a fluidized state remains suspended in the chamber 2 and gradually aggregates into particles of the sprayed gelatinization solution.

この流動造粒装置1を約67分間作動して造粒工程を終
了し、そのまま加熱空気だけを流動造粒装置1に送り込
んで造粒した顆粒馬鈴薯澱粉を乾燥する。
This fluidized granulator 1 is operated for about 67 minutes to complete the granulation process, and then only heated air is sent into the fluidized granulator 1 to dry the granulated potato starch.

この実施例1の製造方法で造った顆粒馬鈴薯澱粉と原料
の馬鈴薯澱粉との性状を測定した結果は次の通りである
The results of measuring the properties of the granulated potato starch produced by the production method of Example 1 and the raw material potato starch are as follows.

実施例 2 馬鈴薯澱粉(水分18%、粘度1300Bu、糊化開始
温度61.5℃)5kgを流動造粒装置の室内に入れて
完全密閉する。
Example 2 5 kg of potato starch (moisture 18%, viscosity 1300 Bu, gelatinization start temperature 61.5° C.) is placed in the chamber of a fluidized granulation device and completely sealed.

3%馬鈴薯澱粉水溶液を糊化状態になるまで加熱攪拌し
て糊化溶液を造る。
A gelatinized solution is prepared by heating and stirring a 3% potato starch aqueous solution until it becomes gelatinized.

この糊化溶液を流動造粒装置の溶液タンクに入れて下記
の条件で造粒を行う。
This gelatinized solution is placed in a solution tank of a fluidized granulator and granulated under the following conditions.

圧縮空気温度 60℃→10分間→70℃(5分間)→
10分間→60℃(15分間)→10分間→55℃ と
順次変化させる。
Compressed air temperature 60℃ → 10 minutes → 70℃ (5 minutes) →
The temperature is changed in this order: 10 minutes → 60°C (15 minutes) → 10 minutes → 55°C.

(流動造粒装置の馬鈴薯澱粉の品温は約50℃) 噴霧量(毎分) 100me→140m1→100m
1と順次変化させる。
(The temperature of potato starch in the fluidized granulator is approximately 50℃) Spray amount (per minute) 100me → 140ml → 100m
1 and change sequentially.

噴霧ノズル口径(直径) 1.8mm 噴霧空気圧 3kg/cm2 馬鈴薯澱粉が糊化溶液の粒子に凝集状況を見ながら造粒
条件を変化操作することにより実施例1より造粒時間を
短縮化して約50分間で造粒物を造る。
Spray nozzle caliber (diameter) 1.8 mm Spray air pressure 3 kg/cm2 The granulation time was shortened from Example 1 by changing the granulation conditions while monitoring the agglomeration of potato starch into the particles of the gelatinization solution, resulting in approximately 50% of the granulation time. Makes granules in minutes.

次に加熱した空気を流動造粒装置の室内に送り込んで造
粒物を乾燥する。
Next, heated air is sent into the chamber of the fluidized granulator to dry the granules.

この実施例2の製造方法で造った顆粒馬鈴薯澱粉と原料
の馬鈴薯澱粉との性状を測定した結果は次の通りである
The results of measuring the properties of the granulated potato starch produced by the production method of Example 2 and the raw material potato starch are as follows.

【図面の簡単な説明】[Brief explanation of the drawing]

図面は1部切断した正面図である。 1は流動造粒装置、2は室内、3は溶液タンク、4は圧
縮空気入口。
The drawing is a partially cutaway front view. 1 is a fluidized granulation device, 2 is an indoor room, 3 is a solution tank, and 4 is a compressed air inlet.

Claims (1)

【特許請求の範囲】[Claims] 1 密閉した室内に馬鈴薯澱粉を吹き上げる空包により
浮遊懸濁した状態にし、かつ馬鈴薯澱粉の温度を約50
℃以下に保持して室内に濃度約1〜5%馬鈴薯澱粉の糊
化溶液を噴霧し、該噴霧した糊化溶液の粒子を結合核と
して浮遊懸濁している馬鈴薯澱粉を凝集して微顆粒状に
することを特部とする顆粒馬鈴薯澱粉の製造方法。
1. Potato starch is made into a suspended state by blowing up the potato starch in a sealed room, and the temperature of the potato starch is kept at about 50°C.
A gelatinized solution of potato starch with a concentration of about 1 to 5% is sprayed into the room while maintaining the temperature below ℃, and the particles of the sprayed gelatinized solution are used as binding nuclei to aggregate the suspended potato starch into fine granules. A method for producing granulated potato starch, the special feature of which is to produce granulated potato starch.
JP56028606A 1981-02-28 1981-02-28 Method for producing granular potato starch Expired JPS5810059B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP56028606A JPS5810059B2 (en) 1981-02-28 1981-02-28 Method for producing granular potato starch

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP56028606A JPS5810059B2 (en) 1981-02-28 1981-02-28 Method for producing granular potato starch

Publications (2)

Publication Number Publication Date
JPS57144952A JPS57144952A (en) 1982-09-07
JPS5810059B2 true JPS5810059B2 (en) 1983-02-24

Family

ID=12253230

Family Applications (1)

Application Number Title Priority Date Filing Date
JP56028606A Expired JPS5810059B2 (en) 1981-02-28 1981-02-28 Method for producing granular potato starch

Country Status (1)

Country Link
JP (1) JPS5810059B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS604956U (en) * 1983-06-22 1985-01-14 東京理化器械株式会社 Sample injection tube

Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB9917339D0 (en) 1999-07-24 1999-09-22 Cerestar Holding Bv Starch granulation
DK1715758T3 (en) * 2004-02-19 2007-07-02 Tate & Lyle Europe Nv Spray-dried starch hydrolyzate agglomerate product and process for preparing a spray-dried starch hydrolyzate agglomerate product
JP4503494B2 (en) * 2005-06-15 2010-07-14 日清フーズ株式会社 Fried powder
JP7258780B2 (en) * 2018-02-06 2023-04-17 株式会社日清製粉ウェルナ potato starch
CN111669978A (en) * 2018-02-06 2020-09-15 日清富滋株式会社 Potato starch and potato starch compositions
JP7323461B2 (en) * 2018-02-06 2023-08-08 株式会社日清製粉ウェルナ potato starch

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS604956U (en) * 1983-06-22 1985-01-14 東京理化器械株式会社 Sample injection tube

Also Published As

Publication number Publication date
JPS57144952A (en) 1982-09-07

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