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JP2842645B2 - Agar granulation method - Google Patents
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JP2842645B2 - Agar granulation method - Google Patents

Agar granulation method

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Publication number
JP2842645B2
JP2842645B2 JP1336897A JP33689789A JP2842645B2 JP 2842645 B2 JP2842645 B2 JP 2842645B2 JP 1336897 A JP1336897 A JP 1336897A JP 33689789 A JP33689789 A JP 33689789A JP 2842645 B2 JP2842645 B2 JP 2842645B2
Authority
JP
Japan
Prior art keywords
agar
powdered
aqueous
granulating
aqueous solution
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 - Lifetime
Application number
JP1336897A
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Japanese (ja)
Other versions
JPH03195480A (en
Inventor
真一 春日
正明 小島
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.)
INA SHOKUHIN KOGYO KK
Original Assignee
INA SHOKUHIN KOGYO KK
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Application filed by INA SHOKUHIN KOGYO KK filed Critical INA SHOKUHIN KOGYO KK
Priority to JP1336897A priority Critical patent/JP2842645B2/en
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Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は寒天の造粒方法に関する。The present invention relates to a method for granulating agar.

〔従来の技術〕[Conventional technology]

従来、工業的に製造される寒天は、粉末状である場合
がほとんどである。この粉末状寒天は、保管、運搬上便
利であるばかりか、実際に使用する際溶解も比較的容易
である。しかし、粉末状寒天は、粒径が小さいため(60
〜400メッシュ)、例えば、ユーザーが釜に粉末状寒天
を投入する際、飛散してほこりとなり易く、ユーザーは
粉末状寒天が飛散しないように充分注意をしながら釜に
粉末状寒天を投入していた。また、粉末状寒天は、加熱
撹拌して溶解する際、粉末状寒天が水をだき込み、いわ
ゆるままこ現象が生じるから、このままこ現象が生じな
いように、充分注意をしながら溶解して使用されてい
た。
Conventionally, most industrially manufactured agars are in powder form. This powdery agar is not only convenient for storage and transportation, but also relatively easy to dissolve when actually used. However, powdered agar has a small particle size (60
For example, when a user puts powdered agar into a pot, the powdered agar tends to be scattered and becomes dusty, and the user puts powdered agar into the pot while paying careful attention so that the powdered agar does not scatter. Was. In addition, when powdered agar is heated and stirred to dissolve, the powdered agar drips in water and causes a so-called mushrooming phenomenon. It had been.

また、本願出願人による易溶性を有する寒天(特願昭
62-155925号)が知られている。この易溶性寒天は、粉
末であり溶解性が良いものの、前述のように溶解させる
際、水を抱き込みままこを作り易いから、充分注意をし
て易溶性寒天を溶解し使用に供していた。
In addition, the present applicant has a readily soluble agar (Japanese Patent Application
No. 62-155925) is known. This easily soluble agar is a powder and has good solubility, but when it is dissolved as described above, it is easy to make water while embracing the water. .

また、上述のように粉末状寒天が飛散し易いことか
ら、近年冷凍法によるフレーク状寒天が一部使用される
ようになった。このフレーク状寒天は、5mm〜15mm位の
大きさの寒天ゲルを冷凍脱水し、乾燥させたものであ
る。このフレーク状寒天は、使用時水に一定時間浸漬
し、そのあと加熱撹拌し溶解して使用に供する。
In addition, since powdery agar is easily scattered as described above, flake-like agar by the freezing method has recently been partially used. The flake agar is obtained by freezing and dehydrating an agar gel having a size of about 5 mm to 15 mm and drying it. The flaked agar is immersed in water for a certain period of time at the time of use, and then heated and stirred to dissolve before use.

更に、上述のほこりになり易い点を解決したものとし
て、顆粒状寒天の製造法(特開昭56-121464号公報)が
知られている。この顆粒状寒天の製造法によれば、メッ
シュ80以上、含水率6%以下に調整した粉末状寒天を回
転する混合機内に徐々に投入しながら、噴霧機により寒
天の最終製品の含水率が約15〜20%になる如く設定して
霧状に万遍なく加水し、加水、混合が完了後一定時間静
止して寒天を粒状に固定させた後、粒状寒天を振動ふる
いにかけて20メッシュ〜24メッシュに粒度を揃えた顆粒
状寒天を作ることができる。
Further, as a method for solving the above-mentioned point of easily becoming dusty, there is known a method for producing granular agar (JP-A-56-121464). According to this method for producing granular agar, the powder agar adjusted to a mesh of 80 or more and a water content of 6% or less is gradually introduced into a rotating mixer while the water content of the final product of the agar is reduced by a sprayer. Set to 15-20%, add water evenly in the form of a mist, and after the addition and mixing are completed, stop for a certain period of time and fix the agar in granular form. Granular agar with a uniform particle size can be produced.

〔発明が解決しようとする課題〕[Problems to be solved by the invention]

しかしながら、上述の粉末状寒天(易溶性寒天を含
む)は、粒径が小さいため、取扱い時飛散してほこりと
なり易く、作業環境が悪くなり、また、相当量の寒天が
容器等に残留して不経済となり、更に、粒径が小さいか
ら溶解し易い反面、水をだき込んでままこになり易く、
この傾向は特に易溶性寒天により大きく現われる。
However, the above-mentioned powdered agar (including easily soluble agar) has a small particle size, so it is liable to be scattered during handling and becomes dusty, the working environment is deteriorated, and a considerable amount of agar remains in a container or the like. It is uneconomical, and it is easy to dissolve because the particle size is small, but it is easy to get water and soak,
This tendency is particularly pronounced with readily soluble agar.

また、フレーク状寒天は、溶解する際、水に一定時間
浸漬しなければならない。その分時間がかかり時間を節
約しようとすると、未溶解の寒天が残るという不都合が
ある。
Further, when the flake agar is dissolved, it must be immersed in water for a certain period of time. If it takes time to save the time, there is a disadvantage that unmelted agar remains.

更に、上述の顆粒状寒天の製造法では、水をバインダ
ーとしているため、顆粒状寒天の顆粒強度が得られず、
わずかな力により顆粒状寒天は崩壊してしまう欠点があ
る。従って、この製造法では、顆粒強度を高めるため、
押出造粒の圧力を高めることが試みられた。しかし、過
度の圧力により粉末状寒天の1部が水で溶解し、顆粒強
度は上昇した反面溶解性が低下し、加えて多くの水が必
要となり、この結果再乾燥の必要性が生じ、経済性が著
しく低下した。
Furthermore, in the above-mentioned method for producing granular agar, since water is used as a binder, the granular strength of granular agar cannot be obtained,
There is a disadvantage that granular agar is disintegrated by a slight force. Therefore, in this production method, in order to increase the granule strength,
Attempts have been made to increase the extrusion granulation pressure. However, due to excessive pressure, a part of the powdered agar is dissolved in water, and the granule strength is increased, but the solubility is reduced, and in addition, more water is required, which results in the necessity of re-drying, and the economy is reduced. The properties were significantly reduced.

そして、従来寒天の造粒されなかった理由は以下のと
おりである。
The reason why agar is not conventionally granulated is as follows.

寒天水溶液は、寒天の凝固性のため凝固温度以下で造
粒することが難しい。寒天を水によって造粒する場合
は、粒子が部分溶解して結着し造粒するが、寒天は融点
が高い(一般に85℃以上)ため所定の接着力を得るのが
難しく、造粒しても所定の造粒強度が得られないと考え
られていた。また、寒天水溶液により造粒しても、寒
天水溶液の水は94%以上あるから、乾燥効率はメリット
がないと考えられていた。
It is difficult to granulate the aqueous agar solution at or below the coagulation temperature due to the coagulability of agar. When agar is granulated with water, the particles are partially melted to bind and granulate, but agar has a high melting point (generally 85 ° C or higher), making it difficult to obtain the prescribed adhesive strength. Also, it was considered that a predetermined granulation strength could not be obtained. Also, even if granulation was carried out with an agar aqueous solution, it was thought that there was no merit in drying efficiency because the water of the agar aqueous solution was 94% or more.

そこで、本発明は、上記事情に鑑みてなされたもの
で、取扱い及び溶解が容易で且つ製造も容易で経済性の
富んだ寒天の造粒方法を提供することを目的とする。
The present invention has been made in view of the above circumstances, and an object of the present invention is to provide an economical agar granulation method that is easy to handle and dissolve, easy to manufacture, and highly economical.

〔課題を解決するための手段〕[Means for solving the problem]

本発明者は、寒天及びその製造方法について研究を続
けてきた。また、寒天の用途についても鋭意研究を続け
てきた。その結果、寒天水溶液をバインダーとすれば、
粉末状寒天を容易に造粒することができることを知見
し、本発明を完成するに至った。すなわち、本発明は、
寒天水溶液をバインダーとして粉末状寒天を造粒するこ
とを特徴とする寒天の造粒方法である。
The inventor has continued research on agar and its production method. We have also been studying the use of agar. As a result, if the agar aqueous solution is used as the binder,
We have found that powdered agar can be easily granulated, and have completed the present invention. That is, the present invention
This is a method for granulating agar, which comprises granulating powdered agar using an agar aqueous solution as a binder.

本発明の最大の特徴は、粉末状寒天の各粒子を付着さ
せて大きな粒子とする造粒に際して、寒天水溶液をバイ
ンダーとして使用することにある。前記した特開昭56-1
21464号明細書で示されているように、バインダーとし
て水を使用して粉末状寒天を大きくして顆粒状寒天を得
ることができる。
The greatest feature of the present invention resides in that an aqueous agar solution is used as a binder when granulating powdered agar particles to form large particles. JP-A-56-1 mentioned above
As indicated in US Pat. No. 21464, powdered agar can be enlarged using water as a binder to obtain granular agar.

本発明においてバインダーとして用いられる寒天水溶
液の濃度及び粉末状寒天に対する比率は、寒天の種類、
粒度分布により若干異なるから、設定された寒天の種
類、粒度分布に応じてあらかじめ設定すれば良い。一般
には、0.1〜6.0重量%及び10〜100重量%、好ましくは
1.0〜2.0重量%及び20〜40重量%の範囲から選べば良
い。上記濃度が0.1重量%より少ないと、バインダーと
しての機能が低くなりすぎ、所定の造粒強度を得ること
ができない。逆に濃度が6.0重量%より多いと、寒天水
溶液の濃度が高くなりすぎ噴霧することが困難になる。
また、粉末状寒天に対する寒天水溶液の比率が10重量%
より少ないと、粉末状寒天に寒天水溶液が充分行き渡ら
ず造粒の収率が低下しすぎる。逆に比率が100重量%よ
り多いと、水分が多くなりすぎ、再乾燥の場合かなりの
エネルギーロスを伴う。
The concentration of the aqueous agar solution used as a binder in the present invention and the ratio to the powdery agar, the type of agar,
Since it differs slightly depending on the particle size distribution, it may be set in advance according to the type of agar and the particle size distribution that have been set. Generally, 0.1-6.0% and 10-100% by weight, preferably
It may be selected from the range of 1.0 to 2.0% by weight and 20 to 40% by weight. If the above concentration is less than 0.1% by weight, the function as a binder becomes too low, and a predetermined granulation strength cannot be obtained. Conversely, if the concentration is more than 6.0% by weight, the concentration of the aqueous agar solution becomes too high and it becomes difficult to spray.
The ratio of aqueous agar to powdered agar is 10% by weight.
If the amount is smaller, the agar aqueous solution does not sufficiently spread to the powdery agar, and the yield of granulation is too low. Conversely, if the proportion is more than 100% by weight, the water content becomes too large, and re-drying involves considerable energy loss.

本発明に用いる寒天水溶液の温度は、すくなくとも粉
末状寒天に寒天水溶液が噴霧されてほぼ行き渡るまで
は、寒天水溶液が凝固しないように保温されていなけれ
ばならない。従って、寒天水溶液の温度は60〜80℃の範
囲にあることが望ましい。この保温は、装置全体を保温
することによって行なっても良く、寒天水溶液を80℃近
くに加温し、寒天水溶液の熱含量によって結果的に装置
全体を保温し、少なくとも粉末状寒天に寒天水溶液がほ
ぼ行き渡るまで保温するようなものであっても良い。
The temperature of the aqueous solution of agar used in the present invention must be kept at least until the aqueous solution of agar is solidified until the aqueous solution of agar is sprayed onto powdered agar and almost completely spreads. Therefore, the temperature of the aqueous agar solution is preferably in the range of 60 to 80 ° C. This heat retention may be carried out by keeping the entire apparatus warm.The agar aqueous solution is heated to about 80 ° C., and as a result, the entire apparatus is kept warm by the heat content of the agar aqueous solution. It may be one that keeps warm until it is almost all over.

本発明に用いられる寒天は、テングサ属(Gelidiu
m)、オバクサ属(Ptevocladia)、オゴノリ属(Gracil
aria)、ユイキリ属(Acanthopeltis)等を原料とし
て、従来方法によって製造されたものであれば、その化
学的構成または平均分子量に関係なく、いずれも使用し
得る。
The agar used in the present invention is of the genus Aspergillus (Gelidiu).
m), genus Ptevocladia, and genus Gracil (Gracil
aria), Acanthopeltis or the like can be used as long as it is produced by a conventional method, irrespective of its chemical constitution or average molecular weight.

すなわち、本発明の寒天は、1、3で結合したβ−D
−ガラクトピラノース基と3、6−アンヒドロ−α−L
−ガラクトピラノース基とが交互に繰り返してなるアガ
ローズ及び該アガロース以外のアガロペクチンより主と
してなる複合物質である。また、本発明方法は、寒天以
外にカラギナン、キサンタンガム、ジェランガムにも適
用することができるものである。
That is, the agar of the present invention comprises β-D
-Galactopyranose group and 3,6-anhydro-α-L
-A complex substance mainly composed of agarose having alternating galactopyranose groups and agaropectin other than the agarose. Further, the method of the present invention can be applied to carrageenan, xanthan gum, and gellan gum in addition to agar.

次に、図面に基づいて寒天の造粒方法について述べ
る。
Next, a method for granulating agar will be described with reference to the drawings.

第1図は、流動層造粒の工程を示すもので、寒天溶解
タンク1に、所定量の水及び寒天供給装置2から所定量
の粉末状寒天をそれぞれ供給し、撹拌機3を撹拌させな
がら粉末寒天を加熱溶解して、濃度1.5重量%、温度70
℃程度の寒天水溶液を調整する。同時に粉末状寒天を寒
天供給装置4から流動槽5に送る。流動槽5には多孔板
(焼結板、金網でも良い)6を介して送風ブロワー7に
てエアーが送られているから、流動槽5内に入った粉末
状寒天は流動層8を形成する。この粉末状寒天の流動層
8に、定量ポンプ9を介して噴霧機10から前述の寒天水
溶液を、粉末状寒天10に対して3の割合で噴霧して、粉
末状寒天を粒状にする。粒状にならなかった粉末状寒天
は、飛散してサイクロン(図示せず)を介して寒天供給
装置4に戻り、造粒された寒天は、ロータリーバルブ11
を介して製品ホッパー12に送られる。この製品ホッパー
12に貯留された造粒された寒天は、製品とされる。
FIG. 1 shows a process of fluidized-bed granulation, in which a predetermined amount of water and a predetermined amount of powdered agar are supplied from an agar supply device 2 to an agar dissolution tank 1 while stirring a stirrer 3. Heat and melt powder agar, 1.5% by weight, temperature 70
Prepare an aqueous agar solution at about ° C. At the same time, the powdered agar is sent from the agar supply device 4 to the fluidized tank 5. Since air is sent to the fluidizing tank 5 by a blower blower 7 through a perforated plate (a sintered plate or a wire mesh) 6, the powdered agar entering the fluidizing tank 5 forms a fluidized bed 8. . The above-mentioned aqueous solution of agar is sprayed onto the fluidized bed 8 of powdered agar from a sprayer 10 via a metering pump 9 at a ratio of 3 to the powdered agar 10 to make the powdered agar into granules. The powdered agar that has not been granulated scatters and returns to the agar supply device 4 via a cyclone (not shown), and the granulated agar is supplied to the rotary valve 11.
Through the product hopper 12. This product hopper
The granulated agar stored in 12 is a product.

第2図は破解造粒の工程を示すもので、第1図の流動
層造粒と同一部分については図面に同一符号を付して説
明を省略する。寒天供給装置4から切り出された粉末状
寒天は混合機13に供給され、この粉末状寒天に噴霧機14
から前述の寒天水溶液を噴霧して、混合機13内にて粉末
状寒天を凝集状態にする。凝集状態の寒天を破解造粒機
15の破解部16で破解し、更にスクリーン17にて粒径をそ
ろえる。このスクリーン17を通過して造粒された寒天
は、製品ホッパー18に送られ製品となる。
FIG. 2 shows the process of pulverization granulation, and the same parts as those in the fluidized bed granulation of FIG. The powdered agar cut out from the agar supply device 4 is supplied to a mixer 13, and the powdered agar is sprayed with a sprayer 14.
Then, the above-mentioned aqueous solution of agar is sprayed to make the powdered agar into a coagulated state in the mixer 13. Agglomerated agar for pulverizing granulation
Disintegrated in 15 disintegration part 16, and the particle size is further adjusted on screen 17. The agar granulated after passing through the screen 17 is sent to a product hopper 18 to be a product.

第3図は、押出し造粒の工程を示すもので、第1図、
第2図と同一部分については、図面に同一符号を付して
説明を省略する。寒天供給装置4から切り出された粉末
状寒天は混合機13に供給され、この粉末状寒天に噴霧機
14から前述の寒天水溶液を噴霧して、混合機13にて粉末
状寒天に寒天水溶液を均一に混合して、押出し造粒機19
に送る。この押出し造粒機19に供給された粉末状寒天
は、所定圧力にて押出し成型部20に送られ、ここで粒径
をそろえられ、製品ホッパー21に送られて製品となる。
FIG. 3 shows the process of extrusion granulation, and FIG.
The same parts as those in FIG. 2 are denoted by the same reference numerals in the drawings, and description thereof will be omitted. The powdered agar cut out from the agar supply device 4 is supplied to a mixer 13, and the powdered agar is sprayed with a sprayer.
The agar aqueous solution described above is sprayed from 14 and the agar aqueous solution is uniformly mixed with the powdered agar in the mixer 13, and the mixture is extruded into a granulator 19.
Send to The powdered agar supplied to the extruder-granulator 19 is sent to an extruder 20 at a predetermined pressure, where the particle size is uniformed, and sent to a product hopper 21 to be a product.

〔作用〕[Action]

粉末状寒天の各粒子の粘着性のある寒天水溶液をバイ
ンダーとするから、得られた粒状寒天の造粒強度が高
く、造粒するに際し圧力をほとんどかけないから、粉末
状寒天はポーラスな状態の粒状寒天となる。
Since the adhesive agar aqueous solution of each particle of the powdered agar is used as a binder, the granulated agar obtained has a high granulation strength and hardly applies pressure during granulation, so that the powdered agar is in a porous state. It becomes granular agar.

〔発明の効果〕〔The invention's effect〕

以上詳述したように、本発明の寒天の造粒方法は、寒
天水溶液をバインダーとして使用するから、造粒強度の
高い粒径の大きい粒状寒天ができ、飛散してほこりとな
ったり、容器等に残留して使用できず、不経済となった
りすることがない。更に、水をバインダーとせず、少量
の寒天水溶液をバインダーとするから、造粒時、寒天水
溶液が凝固しないように保温するだけで良く、再乾燥す
る必要がないため、燃費が低く経済性が高い。
As described in detail above, the agar granulation method of the present invention uses an aqueous agar solution as a binder, so that a granulated agar having a high granulation strength and a large particle size can be formed and scattered into dust or a container or the like. It can not be used and remains uneconomical. Furthermore, since water is not used as a binder and a small amount of agar aqueous solution is used as a binder, during granulation, it is only necessary to keep the temperature so that the agar aqueous solution does not coagulate, and there is no need to re-dry, so fuel efficiency is low and economic efficiency is high. .

また、本発明方法によって得られた粒状寒天は粒径が
大きく、ポーラスな状態であるから、水をだき込んでま
まこになりにくく、特に易溶性寒天に本発明方法を採用
すると、ままことなる可能性が大きく低下し容易に溶解
し、ユーザーの溶解作業が容易かつ短時間になり、まま
こになった分の寒天が無駄にならない。
In addition, since the granular agar obtained by the method of the present invention has a large particle size and is in a porous state, it is difficult for water to penetrate into the agar, and particularly when the method of the present invention is applied to easily soluble agar, it remains. The possibility of dissolution is greatly reduced and dissolution is easy, and the dissolving work of the user is easy and short, and the agar which remains is not wasted.

〔実施例〕〔Example〕

以下実施例について説明する。 Hereinafter, embodiments will be described.

実施例1 濃度1.5重量%、温度70℃の寒天水溶液を200ml(≒0.
2Kg)調製する。流動槽の中に従来製法による粉末状寒
天を1.0Kg入れ、流動槽も略70℃に保温し、この流動槽
内に風速1.0m/sec、圧力800mmaqの70℃のエアーを送
り、流動槽内で粉末状寒天の流動層を形成し、この流動
層に対して上記寒天水溶液を100ml/min、0.2Kg/cm2の条
件で約2分間、200ml噴霧機から噴霧して、流動槽内か
ら粒状寒天約1.2Kgを取り出す。そして、この粒状寒天
の粒度分布及び見掛密度をそれぞれ調べる。
Example 1 200 ml of an aqueous agar solution having a concentration of 1.5% by weight and a temperature of 70 ° C. (≒ 0.
2 kg). 1.0 kg of powdered agar by the conventional method is put in the fluidized tank, the temperature of the fluidized tank is also kept at approximately 70 ° C, and air at 1.0 ° C / sec and a pressure of 800 mmaq at 70 ° C is sent into the fluidized tank. in forming a fluidized layer of powdery agar, about 2 minutes the aqueous agar solution to this fluidized bed 100 ml / min, under conditions of 0.2 Kg / cm 2, and spray from 200ml sprayer, particulate from the fluid tank Take out about 1.2kg of agar. Then, the particle size distribution and apparent density of the granular agar are examined.

実施例2、3 寒天水溶液の濃度を1.0、2.0重量%に調製して、実施
例1と同様な方法にて粒状寒天を作り、それらの粒度分
布及び見掛密度をそれぞれ調べる。
Examples 2 and 3 The agar aqueous solutions were adjusted to a concentration of 1.0 and 2.0% by weight, and granular agar was prepared in the same manner as in Example 1, and their particle size distribution and apparent density were examined.

実施例4 濃度1.5重量%、温度70℃の寒天水溶液を300ml調製す
る。混合機にて粉末状寒天1.0Kgに対して上記寒天水溶
液300mlの割合にて寒天水溶液を噴霧して、凝集状態の
寒天を得る。この凝集状態の寒天を破解造粒機にかけて
破解し、一定時間乾燥し40メッシュのスクリーンにて粒
径をそろえて、粒状寒天約1.2Kgを得る。そして、この
粒状寒天の粒度分布及び見掛密度をそれぞれ調べる。
Example 4 300 ml of an aqueous agar solution having a concentration of 1.5% by weight and a temperature of 70 ° C. is prepared. The agar aqueous solution is sprayed at a ratio of 300 kg of the above aqueous agar solution to 1.0 kg of powdery agar with a mixer to obtain agar in an aggregated state. The coagulated agar is pulverized in a pulverizer / granulator, dried for a certain period of time, and the particle size is adjusted with a 40-mesh screen to obtain about 1.2 kg of granular agar. Then, the particle size distribution and apparent density of the granular agar are examined.

実施例5、6 寒天水溶液の濃度を1.0、2.0重量%に調製して、実施
例4と同様な方法にて粒状寒天を作り、それらの粒度分
布及び見掛密度をそれぞれ調べる。
Examples 5 and 6 The agar aqueous solutions were adjusted to a concentration of 1.0 and 2.0% by weight, and granular agar was prepared in the same manner as in Example 4, and their particle size distribution and apparent density were examined.

実施例7 濃度1.5重量%、温度70℃の寒天水溶液を400ml調製す
る。混合機にて粉末状寒天1.0Kgに対して上記寒天水溶
液400mlの割合にて、寒天水溶液を噴霧して均一に混合
し、50メッシュ以下の粒径の粒状寒天を得るべく、押出
し成型機にかけ、一定時間乾燥し粒状寒天を約1.2Kg得
る。
Example 7 400 ml of an aqueous agar solution having a concentration of 1.5% by weight and a temperature of 70 ° C. is prepared. In a mixer, the agar aqueous solution was sprayed at a ratio of 400 kg of the agar aqueous solution with respect to 1.0 kg of powdery agar, uniformly mixed by spraying, and subjected to an extruder to obtain granular agar having a particle size of 50 mesh or less, After drying for a certain time, about 1.2 kg of granular agar is obtained.

そして、この粒状寒天の粒度分布及び見掛密度をそれ
ぞれ調べる。
Then, the particle size distribution and apparent density of the granular agar are examined.

実施例8、9 寒天水溶液の濃度を1.0、2.0重量%に調製して、実施
例7と同様な方法にて粒状寒天を作り、それらの粒度分
布及び見掛密度をそれぞれ調べる。
Examples 8 and 9 The agar aqueous solutions were adjusted to concentrations of 1.0 and 2.0% by weight, and granular agar was prepared in the same manner as in Example 7, and their particle size distribution and apparent density were examined.

比較例1 比較のため、粉末状寒天の粒度分布をそれぞれ調べ
る。
Comparative Example 1 For comparison, the particle size distribution of powdered agar was examined.

実施例10、11、12 実施例1、4、7にて得られた粒状寒天について、そ
れぞれ6gを温度80℃の湯200mlに入れ、卓上の撹拌機、
プロペラ径20mmφ、60rpmにて2分間撹拌し、崩壊状態
を目視にて調べる。
Examples 10, 11, and 12 With respect to the granular agar obtained in Examples 1, 4, and 7, 6 g of the granular agar was placed in 200 ml of hot water at a temperature of 80 ° C., and a tabletop stirrer was used.
The mixture is stirred for 2 minutes at a propeller diameter of 20 mmφ and 60 rpm, and the state of collapse is visually inspected.

比較例2 粉末状寒天について実施例10と同様な条件で溶解し、
溶解状態を目視にて調べる。
Comparative Example 2 Powdered agar was dissolved under the same conditions as in Example 10,
Check the dissolution state visually.

結果を表−2に示す The results are shown in Table-2

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

第1図は流動層造粒の工程図、第2図は破解造粒の工程
図、第3図は押出し造粒の工程図である。
FIG. 1 is a process diagram of fluidized bed granulation, FIG. 2 is a process diagram of pulverization granulation, and FIG. 3 is a process diagram of extrusion granulation.

Claims (6)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】寒天水溶液をバインダーとして粉末状寒天
を造粒することを特徴とする寒天の造粒方法。
1. A method for granulating agar, comprising granulating powdered agar using an aqueous agar solution as a binder.
【請求項2】粉末状寒天に空気を送り流動させて流動層
を形成し、該流動状態にある前記粉末状寒天に凝固しな
い温度に保持した寒天水溶液を所定比率で均一噴霧し
て、前記粉末状寒天を所定範囲内にある粒径に造粒する
ことを特徴とする寒天の造粒方法。
2. A method for forming a fluidized bed by sending air to and flowing into powdered agar, and uniformly spraying an aqueous agar solution maintained at a temperature at which the powdered agar in the fluidized state does not solidify at a predetermined ratio. A granulation method for agar, comprising granulating a dendritic agar to a particle size within a predetermined range.
【請求項3】粉末状寒天に凝固しない温度に保持した寒
天水溶液を所定比率で均一に噴霧して前記粉末状寒天を
凝集し、該凝集状態にある前記粉末状寒天を破解し所定
目開きのスクリーンを通すことにより、前記粉末状寒天
を所定範囲内にある粒径に造粒することを特徴とする寒
天の造粒方法。
3. An agar aqueous solution maintained at a temperature that does not coagulate on powdered agar is sprayed uniformly at a predetermined ratio to agglomerate the powdered agar, and the powdered agar in the agglomerated state is ruptured to form a predetermined opening. A method for granulating agar, wherein the powdered agar is granulated to a particle size within a predetermined range by passing through a screen.
【請求項4】粉末状寒天に凝固しない温度に保持した寒
天水溶液を所定比率で均一に噴霧し、前記寒天水溶液を
噴霧した前記粉末状寒天を所定圧力にて押出し成型する
ことにより、所定範囲内にある粒径に造粒することを特
徴とする寒天の造粒方法。
4. An agar aqueous solution maintained at a temperature that does not solidify on powder agar is sprayed uniformly at a predetermined ratio, and the powder agar sprayed with the agar aqueous solution is extruded at a predetermined pressure to form a powder within a predetermined range. A granulation method for agar, characterized in that the agar is granulated to a particle size as described above.
【請求項5】寒天水溶液の濃度は、0.1〜6.0重量%の範
囲である請求項(1)、(2)、(3)又は(4)記載
の寒天の造粒方法。
5. The method of granulating agar according to claim 1, wherein the concentration of the aqueous agar solution is in the range of 0.1 to 6.0% by weight.
【請求項6】所定量の粉末状寒天に対する寒天水溶液の
比率は、10〜100重量%の範囲である請求項(1)、
(2)、(3)又は(4)記載の寒天の造粒方法。
6. The method according to claim 1, wherein the ratio of the aqueous solution of agar to the predetermined amount of powdered agar is in the range of 10 to 100% by weight.
(2) The method for granulating agar according to (3) or (4).
JP1336897A 1989-12-26 1989-12-26 Agar granulation method Expired - Lifetime JP2842645B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1336897A JP2842645B2 (en) 1989-12-26 1989-12-26 Agar granulation method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1336897A JP2842645B2 (en) 1989-12-26 1989-12-26 Agar granulation method

Publications (2)

Publication Number Publication Date
JPH03195480A JPH03195480A (en) 1991-08-27
JP2842645B2 true JP2842645B2 (en) 1999-01-06

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Application Number Title Priority Date Filing Date
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Country Link
JP (1) JP2842645B2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
MA22243A1 (en) * 1991-07-30 1992-04-01 Etude Et D Expl D Algues Et Pr PROCESS FOR OBTAINING FAST SOLUBILIZING AGAR-AGAR
KR20000073526A (en) * 1999-05-06 2000-12-05 강헌수 Skillfully dissolve agar manufacture a process

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2504776B2 (en) 1987-06-23 1996-06-05 伊那食品工業株式会社 Agar manufacturing method

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2504776B2 (en) 1987-06-23 1996-06-05 伊那食品工業株式会社 Agar manufacturing method

Also Published As

Publication number Publication date
JPH03195480A (en) 1991-08-27

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