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JPH0255021B2 - - Google Patents
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JPH0255021B2 - - Google Patents

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Publication number
JPH0255021B2
JPH0255021B2 JP58060965A JP6096583A JPH0255021B2 JP H0255021 B2 JPH0255021 B2 JP H0255021B2 JP 58060965 A JP58060965 A JP 58060965A JP 6096583 A JP6096583 A JP 6096583A JP H0255021 B2 JPH0255021 B2 JP H0255021B2
Authority
JP
Japan
Prior art keywords
water
particles
alginate
particle size
bait
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
JP58060965A
Other languages
Japanese (ja)
Other versions
JPS59187744A (en
Inventor
Ryuzo Ueno
Toshio Matsuda
Koichi Tago
Juji Kunimi
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.)
Ueno Seiyaku Oyo Kenkyujo KK
Original Assignee
Ueno Seiyaku Oyo Kenkyujo KK
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 Ueno Seiyaku Oyo Kenkyujo KK filed Critical Ueno Seiyaku Oyo Kenkyujo KK
Priority to JP58060965A priority Critical patent/JPS59187744A/en
Publication of JPS59187744A publication Critical patent/JPS59187744A/en
Publication of JPH0255021B2 publication Critical patent/JPH0255021B2/ja
Granted legal-status Critical Current

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Description

【発明の詳細な説明】[Detailed description of the invention]

本発明は養魚用の水に速溶性のアルギン酸塩の
顆粒製剤に関する。 ハマチ、タイなどの養殖魚は、イワシ、サン
マ、サバなどの比較的大量に漁獲され、経済的に
安価に入手できるものを生餌として飼育される。
これら生餌は養殖魚の生長時期にあわせ、稚魚期
にはミンチの形で、ある程度成育すると丸餌やブ
ツ切りの形で投餌される。生餌は栄養的にバラン
スのとれた餌ではあるが、これのみでは不十分
で、発育促進、疾病予防、治療等の目的で各種ビ
タミン類、ミネラル類、抗菌剤等の添加が行われ
る。これらの添加物をミンチに添加する場合は、
例えば鮮魚、解凍魚、凍結魚等に均一に振りかけ
て破砕機を通し、ミンチ中に均一に添加物が混合
されるようにするが、生餌に添加する添加物の量
は非常に少ないので、適当な賦形剤で希釈して混
合のバラツキが少なくなるよう配慮されている。
ミンチはそれ自体である程度の粘結性を有してお
り、投餌されると海水中で直ちに分散することは
なく一定の形状を保つているので、その大部分は
養殖魚に摂食されるが、それでもかなりな程度散
逸し、添加物の損失と養殖魚場の汚染を招く。そ
こで賦形剤としては小麦粉、殿粉、グルテン、天
然糊料等の粘着性を有する物質が用いられること
が多い。このような粘着性の賦形剤を用いれば、
ミンチが散逸することが少なく、添加物も有効に
摂取される。しかし丸餌やブツ切り餌に添加物を
添加する場合は単に表面に振りかけるのみであ
る。丸餌やブツ切り餌が鮮魚や解凍魚の場合は餌
体表面が濡れており、粘着性の賦形剤を用いると
一応餌体表面に付着するが、これを投餌すると海
水中ですぐに餌体表面よりはがれてしまい、添加
物がほとんど無駄になることが多く、養殖魚場を
汚染する。さらに丸餌やブツ切り餌が凍結魚のま
まである場合は、粘着性の賦形剤でも全く付着し
ないので、添加物を使用することができない。 丸餌やブツ切り餌を凍結魚のまま投餌する方法
は、解凍の手間が省けること、赤水等で養殖魚場
を汚染しないこと、餌料効率が良いこと等の理由
で最近増え始めている。しかし前記のように、丸
餌やブツ切り餌の場合、鮮魚、解凍魚、凍結魚に
かかわらず、添加物を全く添加できないか、添加
してもほとんど無駄になることが多い。そこで丸
餌やブツ切り餌を摂食するある程度生育した養殖
魚においても、ビタミン類や抗菌剤等を投与する
必要がある場合は、わざわざ生餌をミンチにし、
これに添加混合して投与している。 アルギン酸は褐藻類より得られる親水性の高分
子物質であるが、そのナトリウム塩、カリウム塩
などのアルカリ金属塩又はアンモニウム塩を適当
な濃度になるよう水に溶解すると、水糊状の粘稠
な溶液となる。この溶液は海水中のカルシウムイ
オンと接触するとアルギン酸カルシウムが生成し
てゲル化する。丸餌やブツ切り餌への添加物の添
加に、このようなアルギン酸塩の性状を利用する
ことが試みられている。すなわちアルギン酸ナト
リウムの水溶液に添加物を混合し、この溶液を丸
餌やブツ切り餌の表面にふりかけて付着させ投餌
すると、アルギン酸ナトリウムがカルシウムと反
応してゲル化し、ゼリー膜を形成するので、添加
物が海水中に散逸することがなく養殖魚に有効に
摂取される。 ところがアルギン酸のアルカリ金属塩やアンモ
ニウム塩は水和が強い親水性高分子物質であるの
で、均一な水溶液を調製するのに手数がかかる。
例えばアルギン酸ナトリウムは、水溶液を調製す
るために水に加えると直ちにままこ状態になつて
しまい、溶解に多くの時間がかかる。これを防ぐ
ためには、強力な撹拌機を用いる方法、アルギン
酸ナトリウムをごく少量ずつ加える方法、撹拌機
で撹拌しながら温水に少量ずつ加える方法、アル
ギン酸ナトリウムをエタノールやプロピレングリ
コールで湿潤させてから水に加える方法などが一
般に用いられている。しかしこれらの方法は特別
な機械を必要とし、あるいは溶剤を用いる煩雑さ
があつて、いずれも養殖場における餌の調製の実
情からして実施困難である。投餌は生餌を魚船に
積込み、生けすまで運んで行うが、一回一船当り
の積込み量は数トンから十数トンになる。生餌の
処理や調製は魚船への積込みを考えて、急港の岸
壁や船上で行われる。投餌に要する時間は、生け
すの広さや数により異なるが、通常数時間は要す
るので、早朝より生餌を準備する作業が行われ
る。このような状態では手間のかかる方法で大量
のアルギン酸塩の水溶液を調製するのはきわめて
不便である。 本発明者らはこのような問題を解決すべく鋭意
研究した結果、アルギン酸塩を水易溶性の糖類を
用いて適当な大きさの顆粒にすることにより、冷
水に速溶で簡単に均一な溶液を調製できるアルギ
ン酸塩製剤が得られることを見い出して本発明を
完成した。 本発明は、アルギン酸のアルカリ金属塩及び/
又はアンモニウム塩(以下アルギン酸塩と呼ぶ)
10〜95重量%及び糖、糖アルコール、デキストリ
ン及び/又はα殿粉5〜90重量%から成り、180
〜1000μの粒径を有することを特徴とする、冷水
に速溶性の養魚用アルギン酸塩顆粒製剤である。 本発明におけるアルギン酸のアルカリ金属塩と
しては、アルギン酸のナトリウム塩、カリウム塩
が用いられる。糖としては例えば乳糖、蔗糖、ぶ
どう糖、麦芽糖、オリゴ糖など、またた糖アルコ
ールとしては例えばD―ソルビツト、マンニツ
ト、マルチトールなどがあげられる。デキストリ
ンは冷水で可溶の殿粉分解物を指す。これらは単
独で又は2種以上を混合して用いてもよい。アル
ギン酸塩としては入手が容易な点からアルギン酸
ナトリウムが有利である。市販のアルギン酸塩は
粒径が小さく、180μ以下のものが50%以上存在
する。このようなアルギン酸塩を水に添加する
と、非常に注意深く少量ずつ添加しても、水と接
触した部分が吸水して糊状となり凝集するので、
ままこ状態となつて溶解するのに非常に時間がか
かる。通常は溶解速度を上げるために、粒子径を
小さくし、表面積を広くして水との接触面積を増
やすことが好ましいが、アルギン酸塩ではこの方
法は逆効果である。微粉のアルギン酸塩は水に添
加しても分散しにくく、水と接触する表面の微粉
の部分は直ちに溶解するが、これが強力な糊の役
目を果たして粉全体が大きな塊となり、表面を粘
度の高い糊状の膜が覆つているような状態になる
ので、激しく撹拌しても個々の粒子に分散するこ
とはなく、塊の表面から少しずつ溶解するだけで
ある。 本発明の製剤は粒径が180〜1000μと比較的大
きいので、製剤の状態において流動性が良い。こ
れを水に添加すると微粉の場合と同様に水と接触
した部分より吸水するが、粒径が大きく表面積が
小さいので、ごく短時間では粒子全体が溶解して
しまうことはなく、ゆるやかな撹拌で個々の粒子
が分散し、ままこ状態になることはなく、短時間
で容易に均一な溶液が得られる。 本発明の製剤の粒径は180〜1000μであるが、
180μ以下の粒子が含まれていても10%以内であ
ればあまり効果に影響はない。しかしこれ以上含
まれると、ゆるやかな撹拌ではままこ状態にな
る。粒径が1000μ以上の粒子は分散には良い影響
を与えるが、粒子自体の溶解に時間がかかるので
好ましくない。 本発明の製剤はアルギン酸塩及び糖、糖アルコ
ール、デキストリン及び/又はα殿粉の混合物を
造粒することにより得られる。造粒物は通常の湿
式の造粒方法によつて調製することができるが、
粉末を空気中に浮遊流動させて液を散布し造粒す
る流動層造粒法、粉末を高速で撹拌しながら液を
散布して造粒する撹拌造粒法、粉末を転動させな
がら液を散布して造粒する転動造粒法などの方法
を用いることが好ましい。糖、糖アルコール、デ
キストリン又はα殿粉はアルギン酸塩の造粒の際
の結合剤として作用する。アルギン酸塩は水和力
が強く、造粒に際して加水すると、水をかけた部
分のみが吸水し、水を強く捕えて離さないので他
の部分に均一に分散しないため、アルギン酸塩の
みでは造粒に必要な結合力が生じない。また、全
体に結合力が生じるように過剰に加水すると大き
な塊になつてしまう。糖、糖アルコール、デキス
トリン又はα殿粉は加水によりその表面が溶解し
て粘着力が生じるので、これらのものとアルギン
酸塩の混合物は前記の造粒法により容易に造粒物
にすることができる。 糖、糖アルコール、デキストリン及び/又はα
殿粉の添加量は5〜90重量%である。添加量がこ
れより少ないと十分に造粒効果を発揮せず、また
添加量が増加すると造粒性は良くなるが、アルギ
ン酸塩の含有量が少なくなるので90重量%以上で
は経済的でない。糖、糖アルコール、デキストリ
ン又はα殿粉は、造粒効果以外にアルギン酸塩の
粒子同士が接触するのを防ぎ、水に添加した時に
ままこ状態になるのを防ぐ効果がある。 本発明の製剤は通常水に溶解し、粘稠なアルギ
ン酸塩水溶液にしたのち、ビタミン類、ミネラル
類、抗菌剤等の添加物を加えて均一な溶液又は懸
濁液を調製して用いられる。また本発明の製剤に
添加物を混合し、これを水に加えて均一な溶液又
は懸濁液を調製する方法も採用される。本発明の
製剤の水溶液の濃度は、本発明の製剤中のアルギ
ン酸塩の含有量及びアルギン酸塩の重合度により
異なるが、アルギン酸塩水溶液の粘度が200〜
10000センチポイズ位を示すところ、すなわちア
ルギン酸塩として0.6〜3%程度が好ましい。水
溶液の使用濃度はこの範囲に限定されるものでは
なく、更に高い濃度の液も容易に調製できる。調
製された溶液又は懸濁液は丸餌やブツ切り餌に振
りかけられて投餌され、養殖魚に有効に摂取され
る。この液をミンチに混ぜ込んで投餌しても有効
である。 実施例 1 アルギン酸ナトリウム2.5Kg、乳糖1.25Kg及び
D―ソルビツト1.25Kgを流動槽容量20の流動層
造粒機に仕込み、2分間混合したのち粉末を浮遊
流動させながら水を結合液として噴霧し造粒す
る。造粒物が適当な大きさになつたところで噴霧
を止めて乾燥する。水の噴霧量は1290mlである。
乾燥後、放冷した造粒物を1000μの篩網で篩つた
ところ、粒径1000μ以上の粒子は2.6%であつた。
通過した部分について粒度を測定すると、180〜
1000μの粒子が97.2%、180μ以下の粒子が2.8%で
あつた(本発明品1)。 実施例 2 アルギン酸ナトリウム0.5Kg及びデキストリン
(商品名パインデツクス#3、松谷化学社製)4.5
Kgを流動層造粒機に仕込み、実施例1と同様にし
て造粒する。水の噴霧量は720mlである。造粒物
を1000μの篩網で篩つたところ、粒径1000μ以上
の粒子は0.4%であつた。通過した部分について
粒度を測定すると、180〜1000μの粒子が99.5%、
180μ以下の粒子が0.5%であつた(本発明品2)。 実施例 3 アルギン酸ナトリウム4.75Kg及びα殿粉0.2Kg
を流動層造粒機に仕込み、5%α殿粉水溶液を結
合液として噴霧し造粒する。結合液の噴霧量を
1000mlで止めて乾燥する。造粒物を1000μの篩網
で篩つたところ粒径1000μ以上の粒子は5.2%であ
つた。通過した部分について粒度を測定すると、
180〜1000μの粒子が87.7%、180μ以下の粒子が
12.3%であつた。180μ以下の粒子を除いて製剤と
した(本発明品3)。 実施例 4 アルギン酸ナトリウム2.4Kg、乳糖1.0Kg及びD
―ソルビツト0.6Kgを撹拌槽容量24の撹拌造粒
機に仕込み、5分間混合したのち撹拌下に水を結
合液として噴霧し造粒する。水の噴霧量は600ml
である。造粒物は流動乾燥したのち1000μの篩網
で篩つたところ、粒径1000μ以上の粒子は6.7%で
あつた。通過した部分について粒度を測定する
と、180〜1000μの粒子が92.1%、180μ以下の粒子
が7.9%であつた。180μ以下の粒子を除いて製剤
とした(本発明品4)。 実施例 5 アルギン酸カリウム2.5Kg、乳糖1.0Kg、D―ソ
ルビツト1.0Kg及びα殿粉0.5Kgを流動層造粒機に
仕込み、実施例1と同様にして造粒する。水の噴
霧量は1200mlである。造粒物を1000μの篩網で篩
つたところ、粒径1000μ以上の粒子は4.3%であつ
た。通過した部分について粒度を測定すると、
180〜1000μの粒子が96.7%、180μ以下の粒子が
3.3%であつた(本発明品5)。 比較例 1 アルギン酸ナトリウム5.0Kgを流動層造粒機に
仕込み、粉末を浮遊流動させながら水を結合液と
して噴霧する。水の噴霧量が2000mlに達してもほ
とんど粒子径は大きくならなかつたので、2500ml
になつたところで噴霧を止めて乾燥する。造粒物
を1000μの篩網で篩つたところ、粒径1000μ以上
の粒子は7.2%であつた。通過した部分について
粒度を測定すると180〜1000μの粒子が62.3%、
180μ以下の粒子が37.7%であつた。180μ以下の粒
子を除いて製剤とした(比較品1)。 比較例 2 アルギン酸ナトリウム4.0Kgを撹拌造粒機に仕
込み、撹拌下5%D―ソルビツト水溶液を噴霧し
て造粒する。噴霧液を1800mlで止め、造粒物を流
動乾燥したのち1000μの篩網で篩つたところ、粒
径1000μ以上の粒子は21.5%であつた。通過した
部分について粒度を測定すると180〜1000μの粒
子が70.9%、180μ以下の粒子が29.1%であつた。
そこで180μ以下の粒子を除いて製剤とした(比
較品2)。 実験例 1 実施例1〜5並びに比較例1及び2で得た顆粒
製剤を60メツシユ(250μ)の篩網で篩い、網上
に残つた顆粒製剤各10gを500ml容のポリエチレ
ン袋に詰め、空気を入れて十分膨らませたのちヒ
ートシールし、これを激しく100回振盪して衝撃
を与えた。次いでこのように処理した顆粒製剤の
60メツシユの篩網の通過量を求めて粉化率とし
た。実験は2回くり返した。結果を下記表に示
す。アルギン酸塩のみであるいはアルギン酸塩に
5%以下の結合剤を加えて造粒し顆粒は衝撃で壊
れ易い。これに対し本発明品は衝撃にも壊れない
強い顆粒になつていることが知られる。
The present invention relates to a granular formulation of alginate which is rapidly soluble in water for fish farming. Farmed fish such as yellowtail and sea bream are raised in relatively large quantities using raw food such as sardines, saury, and mackerel, which can be obtained economically and inexpensively.
These live baits are fed according to the growth period of the farmed fish, in the form of minced meat when the fish are young, and once they have grown to a certain extent, they are fed in the form of whole baits or pieces. Raw feed is a nutritionally balanced feed, but it is not sufficient on its own, and various vitamins, minerals, antibacterial agents, etc. are added for the purpose of promoting growth, disease prevention, treatment, etc. When adding these additives to minced meat,
For example, the additives are sprinkled evenly on fresh fish, thawed fish, frozen fish, etc. and passed through a crusher to ensure that the additives are evenly mixed into the minced fish, but the amount of additives added to live bait is very small. Care is taken to reduce variation in mixing by diluting with appropriate excipients.
Mince itself has a certain degree of cohesiveness, and when fed, it does not immediately disperse in seawater and maintains a certain shape, so most of it is eaten by farmed fish. However, it still dissipates to a considerable extent, resulting in loss of additives and contamination of fish farms. Therefore, sticky substances such as wheat flour, starch, gluten, and natural thickening agents are often used as excipients. If such a sticky excipient is used,
The minced meat is less likely to dissipate, and the additives are effectively ingested. However, when adding additives to whole or cut baits, they are simply sprinkled on the surface. When whole bait or piece bait is fresh or thawed fish, the surface of the bait is wet, and if a sticky excipient is used, it will adhere to the surface of the bait, but if you cast it, the bait will quickly disappear in the seawater. The additives often come off from the body surface, wasting most of the additives, and contaminating fish farms. Furthermore, if the whole bait or cut bait is frozen fish, even sticky excipients will not stick to the bait at all, so additives cannot be used. The method of feeding frozen fish with whole bait or cut bait has started to increase recently because it saves the trouble of thawing, does not contaminate fish farms with red water, etc., and is highly efficient as a feed source. However, as mentioned above, in the case of whole bait or cut bait, regardless of whether it is fresh fish, thawed fish, or frozen fish, additives cannot be added at all, or even if they are added, it is often a waste. Therefore, even for farmed fish that have grown to a certain extent and feed on whole or chopped bait, if it is necessary to administer vitamins or antibacterial agents, the raw bait must be minced.
It is added and mixed with this and administered. Alginic acid is a hydrophilic polymeric substance obtained from brown algae, but when its alkali metal salts such as sodium salts and potassium salts or ammonium salts are dissolved in water to an appropriate concentration, it becomes a viscous water paste-like substance. It becomes a solution. When this solution comes into contact with calcium ions in seawater, calcium alginate is produced and gelled. Attempts have been made to utilize the properties of alginates to add additives to whole baits and chopped baits. In other words, when an additive is mixed with an aqueous solution of sodium alginate, and this solution is sprinkled on the surface of whole bait or cut bait to make it adhere, the sodium alginate reacts with calcium and gels, forming a jelly film. The additives are effectively ingested by farmed fish without being dissipated into seawater. However, since alkali metal salts and ammonium salts of alginic acid are hydrophilic polymeric substances that are highly hydrated, it takes time and effort to prepare a uniform aqueous solution.
For example, when sodium alginate is added to water to prepare an aqueous solution, it immediately becomes lumpy and takes a long time to dissolve. To prevent this, you can use a strong stirrer, add the sodium alginate in very small portions, add the sodium alginate little by little to warm water while stirring with a stirrer, or moisten the sodium alginate with ethanol or propylene glycol before adding it to the water. Addition methods are commonly used. However, these methods require special machines or are complicated to use solvents, and are difficult to implement due to the actual situation of feed preparation in aquaculture farms. Bait casting is carried out by loading live bait onto a fish boat and transporting it to the fish tank, and the amount loaded per boat can range from several tons to more than a dozen tons at a time. The processing and preparation of live bait is carried out on the quayside of the port or on board the ship, with the intention of loading it onto a fishing boat. The time required to cast bait varies depending on the size and number of cages, but it usually takes several hours, so the work to prepare live bait begins early in the morning. Under such conditions, it is extremely inconvenient to prepare a large amount of alginate aqueous solution by a laborious method. The inventors of the present invention conducted extensive research to solve these problems, and found that by forming alginate into granules of an appropriate size using easily water-soluble saccharides, it was possible to quickly dissolve and easily form a uniform solution in cold water. The present invention was completed by discovering that alginate preparations that can be prepared can be obtained. The present invention provides an alkali metal salt of alginic acid and/or
or ammonium salt (hereinafter referred to as alginate)
10-95% by weight and 5-90% by weight of sugar, sugar alcohol, dextrin and/or alpha starch, 180
This is an alginate granule formulation for fish farming that is rapidly soluble in cold water and is characterized by having a particle size of ~1000μ. As the alkali metal salt of alginic acid in the present invention, sodium salt and potassium salt of alginic acid are used. Examples of sugars include lactose, sucrose, glucose, maltose, and oligosaccharides; examples of sugar alcohols include D-sorbitol, mannitol, and maltitol. Dextrin refers to starch decomposition products that are soluble in cold water. These may be used alone or in combination of two or more. As the alginate, sodium alginate is advantageous because it is easily available. Commercially available alginate has a small particle size, with more than 50% having a particle size of 180μ or less. When such alginates are added to water, even if they are added very carefully and in small quantities, the parts that come into contact with the water absorb water, become glue-like, and clump together.
It takes a very long time to get into a sticky state and dissolve. Normally, in order to increase the dissolution rate, it is preferable to reduce the particle size and increase the surface area to increase the contact area with water, but this method has the opposite effect with alginates. Even when finely powdered alginate is added to water, it is difficult to disperse, and the part of the fine powder on the surface that comes into contact with water dissolves immediately, but this acts as a strong glue and the whole powder forms a large lump, creating a highly viscous surface. Since the mixture is covered with a glue-like film, even if it is vigorously stirred, it will not be dispersed into individual particles, but will only dissolve little by little from the surface of the lump. Since the formulation of the present invention has a relatively large particle size of 180 to 1000μ, it has good fluidity in the formulation state. When added to water, it absorbs water from the parts that come into contact with water, just like fine powder, but since the particle size is large and the surface area is small, the entire particle will not dissolve in a very short time, and it can be stirred slowly. Individual particles are dispersed and do not remain in a lumpy state, and a homogeneous solution can be easily obtained in a short time. The particle size of the formulation of the present invention is 180-1000μ,
Even if particles with a size of 180 μ or less are included, as long as they are within 10%, they will not affect the effectiveness much. However, if more than this is included, even gentle stirring will result in a lumpy state. Particles having a particle size of 1000 μm or more have a positive effect on dispersion, but are not preferable because it takes time for the particles themselves to dissolve. The formulation of the invention is obtained by granulating a mixture of alginate and sugar, sugar alcohol, dextrin and/or alpha starch. Granules can be prepared by normal wet granulation methods,
Fluidized bed granulation method, in which powder is suspended and fluidized in the air and then granulated by scattering a liquid; agitation granulation method, in which powder is dispersed and granulated while stirring at high speed; and liquid is granulated by rolling the powder. It is preferable to use a method such as a rolling granulation method in which particles are dispersed and granulated. Sugars, sugar alcohols, dextrins or alpha starch act as binders during the granulation of alginates. Alginate has a strong hydration power, and when water is added during granulation, only the area on which water is applied will absorb water, and because it strongly captures water and does not let it go, it will not disperse uniformly to other areas, so alginate alone cannot be used for granulation. The necessary binding force does not occur. Also, if excessive water is added to create a cohesive force throughout the product, it will become a large lump. The surface of sugar, sugar alcohol, dextrin, or alpha starch dissolves when water is added, creating adhesive strength, so a mixture of these and alginate can be easily made into granules by the above-mentioned granulation method. . sugar, sugar alcohol, dextrin and/or alpha
The amount of starch added is 5 to 90% by weight. If the amount added is less than this, the granulation effect will not be sufficiently exerted, and if the amount added is increased, the granulation property will improve, but since the content of alginate will decrease, it is not economical if it exceeds 90% by weight. In addition to the granulation effect, sugar, sugar alcohol, dextrin, or alpha starch has the effect of preventing alginate particles from coming into contact with each other, and preventing a lumpy state when added to water. The preparation of the present invention is usually used by dissolving it in water to form a viscous alginate aqueous solution, and then adding additives such as vitamins, minerals, antibacterial agents, etc. to prepare a uniform solution or suspension. Alternatively, a method may be adopted in which additives are mixed with the formulation of the present invention and added to water to prepare a uniform solution or suspension. The concentration of the aqueous solution of the formulation of the present invention varies depending on the content of alginate in the formulation of the present invention and the degree of polymerization of the alginate, but the viscosity of the aqueous alginate solution is 200 to
It is preferable that it exhibits a value of about 10,000 centipoise, that is, about 0.6 to 3% as an alginate. The concentration of the aqueous solution used is not limited to this range, and solutions with even higher concentrations can be easily prepared. The prepared solution or suspension is sprinkled on whole bait or chopped bait and cast, and is effectively ingested by farmed fish. It is also effective to mix this liquid with mince and feed it. Example 1 2.5 kg of sodium alginate, 1.25 kg of lactose, and 1.25 kg of D-sorbit were charged into a fluidized bed granulator with a fluidized tank capacity of 20, mixed for 2 minutes, and then water was sprayed as a binding liquid while the powder was suspended and fluidized. Grainy. When the granules reach an appropriate size, stop spraying and dry. The amount of water sprayed is 1290ml.
After drying, the granulated product was allowed to cool and was sieved through a 1000μ sieve, and 2.6% of the particles were found to have a particle size of 1000μ or more.
When we measure the particle size of the part that has passed through, it is 180~
97.2% of the particles were 1000μ, and 2.8% were particles of 180μ or less (Product 1 of the present invention). Example 2 Sodium alginate 0.5Kg and dextrin (trade name Pinedex #3, manufactured by Matsutani Chemical Co., Ltd.) 4.5
Kg is charged into a fluidized bed granulator and granulated in the same manner as in Example 1. The amount of water sprayed is 720ml. When the granulated product was sieved through a 1000μ sieve, 0.4% of the particles were found to have a particle size of 1000μ or more. When measuring the particle size of the part that passed through, 99.5% of the particles were 180-1000μ.
Particles with a size of 180μ or less were 0.5% (product 2 of the present invention). Example 3 Sodium alginate 4.75Kg and alpha starch 0.2Kg
was charged into a fluidized bed granulator, and granulated by spraying a 5% α-starch aqueous solution as a binding liquid. Spray amount of binding liquid
Stop at 1000ml and dry. When the granules were sieved through a 1000μ sieve, 5.2% of the particles were found to have a particle size of 1000μ or more. When measuring the particle size of the part that has passed through,
87.7% of particles are 180-1000μ, particles less than 180μ
It was 12.3%. A formulation was prepared by excluding particles of 180 μm or less (product 3 of the present invention). Example 4 Sodium alginate 2.4Kg, lactose 1.0Kg and D
-Pour 0.6 kg of Sorbit into a stirring granulator with a stirring tank capacity of 24, mix for 5 minutes, and then spray water as a binding liquid while stirring to granulate. Water spray amount is 600ml
It is. The granules were fluidized and dried, and then sieved through a 1000μ sieve, and 6.7% of the particles were found to have a particle size of 1000μ or more. When the particle size of the portion that passed through was measured, 92.1% of the particles were 180 to 1000μ, and 7.9% were particles of 180μ or less. A preparation was prepared by excluding particles of 180 μm or less (invention product 4). Example 5 2.5 kg of potassium alginate, 1.0 kg of lactose, 1.0 kg of D-sorbitol and 0.5 kg of α-starch are charged into a fluidized bed granulator and granulated in the same manner as in Example 1. The amount of water sprayed is 1200ml. When the granules were sieved through a 1000μ sieve, 4.3% of the particles had a particle size of 1000μ or more. When measuring the particle size of the part that has passed through,
96.7% of particles are 180-1000μ, particles less than 180μ
It was 3.3% (product 5 of the present invention). Comparative Example 1 5.0 kg of sodium alginate is charged into a fluidized bed granulator, and water is sprayed as a binding liquid while the powder is suspended and fluidized. Even when the amount of water sprayed reached 2000ml, the particle size hardly increased, so 2500ml
When it becomes dry, stop spraying and let it dry. When the granules were sieved through a 1000μ sieve, 7.2% of the particles had a particle size of 1000μ or more. When measuring the particle size of the part that passed through, 62.3% of the particles were 180-1000μ.
Particles with a size of 180μ or less accounted for 37.7%. A formulation was prepared by excluding particles of 180μ or less (Comparative product 1). Comparative Example 2 4.0 kg of sodium alginate was charged into a stirring granulator, and 5% D-sorbitol aqueous solution was sprayed on the machine while stirring to granulate it. When the spray liquid was stopped at 1800 ml and the granules were fluidized and dried, they were sieved through a 1000 μm sieve, and 21.5% of the particles were found to have a particle size of 1000 μm or more. When the particle size of the portion that passed through was measured, 70.9% of the particles were 180 to 1000μ, and 29.1% were particles smaller than 180μ.
Therefore, a formulation was prepared by excluding particles of 180μ or less (comparative product 2). Experimental Example 1 The granule preparations obtained in Examples 1 to 5 and Comparative Examples 1 and 2 were sieved through a 60-mesh (250 μ) sieve screen, and each 10 g of the granule preparations remaining on the screen was packed into a 500 ml polyethylene bag and air-filled. After filling the tube with enough air to inflate it, it was heat-sealed and shaken vigorously 100 times to give it a shock. Then, the granule preparation treated in this way is
The amount passing through a 60-mesh sieve was determined and used as the pulverization rate. The experiment was repeated twice. The results are shown in the table below. When granulated with alginate alone or with less than 5% binder added to alginate, the granules are easily broken by impact. On the other hand, it is known that the product of the present invention has strong granules that do not break even on impact.

【表】 実験例 2 1容のビーカーに水500mlを入れ、直径4cm
のプロペラ付撹拌機を用い、一定速度で撹拌(回
転速度200rpm)しながら、水温を約20℃に保ち、
本発明品1の顆粒製剤10gを約2〜3秒間で添加
した。製剤はままこ状態になることなく水中に分
散し、撹拌を続けると10分間で完全に溶解し、粘
稠な溶液が得られた。この溶液の粘度は510cpで
あつた。比較のため、市販のアルギン酸ナトリウ
ム粉末(粒径180μ以下の粒子を98%含む)5g
を用いて同様の方法で溶解試験を行つたところ、
粉末を水に添加したとたんままこ状態になり、そ
のまま撹拌を続けたが2時間後もゲル状の塊が残
つていた。 実験例 3 本発明品4の顆粒製剤10gを用い、実験例2と
同様の方法で溶解試験を行つたところ、10分間で
完全に溶解し、粘稠な溶液が得られた。この溶液
の粘度は1250cpであつた。比較品1の顆粒製剤
6gを用いて溶解試験を行つたところ、粒子同士
が水中で付着して小さな塊となり、完全に溶解す
るのに30分間かかつた。また本発明品4の顆粒製
剤85重量部に実施例4で得た粒径180μ以下の粒
子15重量部を混合した製剤10gを用いて溶解試験
を行つたところ、大部分は水中に分散するが、一
部がままこ状態になり、完全に溶解するのに1時
間かかつた。 実施例 6 本発明品1の顆粒製剤440gとビタミンB1を硬
化油で被覆した製剤560gを混合し、製剤1Kgを
得た。20容のステンレスのタンクに水10を入
れ、直径7cmのプロペラ付撹拌機で回転速度
300rpmで撹拌しながら、前記の製剤450gを1分
間で添加した。製剤はままこ状態になることなく
水中に分散し、15分間で完全に溶解し、粘稠な懸
濁液が得られた。この液の粘度は670cpであつ
た。この懸濁液10mlを冷凍マイワシ1Kgの表面に
均一になるよう振りかけた。この時ビタミンB1
の添加量は5mg/Kgになる。ステンレスのタンク
に人工海水20を入れ、このマイワシ1Kgを投入
し1分間ゆつくり撹拌したのちマイワシを引き上
げ、破砕機を通して均一なミンチにして、残存し
ているビタミンB1量を測定したところ41mg/Kg
であり、回収率は82%であつた。以上のように、
本発明品の使用により凍結した生餌にも添加物を
有効に添加し得ることが確認できた。
[Table] Experimental example 2 Put 500ml of water in a 1 volume beaker and make a diameter of 4cm.
Using a stirrer with a propeller, keep the water temperature at about 20℃ while stirring at a constant speed (rotation speed 200 rpm).
10 g of the granule formulation of Inventive Product 1 was added in about 2 to 3 seconds. The formulation was dispersed in water without becoming lumpy, and when stirring was continued, it completely dissolved in 10 minutes to obtain a viscous solution. The viscosity of this solution was 510 cp. For comparison, 5 g of commercially available sodium alginate powder (contains 98% particles with a particle size of 180μ or less)
When a dissolution test was conducted in the same manner using
When the powder was added to water, it immediately turned into a lumpy state, and although stirring was continued, a gel-like mass remained even after 2 hours. Experimental Example 3 A dissolution test was conducted in the same manner as in Experimental Example 2 using 10 g of the granule preparation of Invention Product 4, and it was completely dissolved in 10 minutes to obtain a viscous solution. The viscosity of this solution was 1250 cp. When a dissolution test was conducted using 6 g of the granule formulation of Comparative Product 1, the particles adhered to each other in water and formed small clumps, and it took 30 minutes to completely dissolve. In addition, when a dissolution test was conducted using 10 g of a preparation prepared by mixing 85 parts by weight of the granule preparation of Invention Product 4 with 15 parts by weight of particles with a particle size of 180 μ or less obtained in Example 4, most of the particles were dispersed in water. , a part of it remained in a sticky state, and it took one hour to completely dissolve it. Example 6 440 g of the granule preparation of the product 1 of the present invention and 560 g of a preparation of vitamin B 1 coated with hydrogenated oil were mixed to obtain 1 kg of the preparation. Pour 10 ml of water into a 20-volume stainless steel tank and adjust the rotation speed using a stirrer with a 7 cm diameter propeller.
While stirring at 300 rpm, 450 g of the above formulation was added in 1 minute. The formulation was dispersed in water without becoming lumpy and completely dissolved in 15 minutes, resulting in a viscous suspension. The viscosity of this liquid was 670 cp. 10 ml of this suspension was sprinkled evenly over the surface of 1 kg of frozen sardines. At this time vitamin B 1
The amount added will be 5mg/Kg. Pour 20ml of artificial seawater into a stainless steel tank, add 1 kg of sardines, stir gently for 1 minute, pull out the sardines, pass through a shredder to mince them evenly, and measure the amount of remaining vitamin B1, which is 41mg / Kg
The recovery rate was 82%. As mentioned above,
It was confirmed that additives could be effectively added to frozen live feed by using the product of the present invention.

Claims (1)

【特許請求の範囲】[Claims] 1 アルギン酸のアルカリ金属塩及び/又はアン
モニウム塩10〜95重量%及び糖、糖アルコール、
デキストリン及び/又はα澱粉5〜90重量%から
成り、180〜1000μの粒径を有することを特徴と
する、冷水に速溶性の養魚用アルギン酸塩顆粒製
剤。
1 Alginic acid alkali metal salt and/or ammonium salt 10 to 95% by weight, sugar, sugar alcohol,
An alginate granule preparation for fish farming which is rapidly soluble in cold water and is characterized by comprising 5 to 90% by weight of dextrin and/or alpha starch and having a particle size of 180 to 1000μ.
JP58060965A 1983-04-08 1983-04-08 Granules for feeding fish Granted JPS59187744A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP58060965A JPS59187744A (en) 1983-04-08 1983-04-08 Granules for feeding fish

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP58060965A JPS59187744A (en) 1983-04-08 1983-04-08 Granules for feeding fish

Publications (2)

Publication Number Publication Date
JPS59187744A JPS59187744A (en) 1984-10-24
JPH0255021B2 true JPH0255021B2 (en) 1990-11-26

Family

ID=13157633

Family Applications (1)

Application Number Title Priority Date Filing Date
JP58060965A Granted JPS59187744A (en) 1983-04-08 1983-04-08 Granules for feeding fish

Country Status (1)

Country Link
JP (1) JPS59187744A (en)

Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4818539A (en) * 1985-02-05 1989-04-04 Warner-Lambert Company Ingestible aggregate and delivery system prepared therefrom
US4747881A (en) * 1985-02-05 1988-05-31 Warner-Lambert Company Ingestible aggregate and delivery system prepared therefrom
US4843098A (en) * 1985-02-05 1989-06-27 Warner-Lambert Company Ingestible aggregate and delivery system prepared therefrom
US4790991A (en) * 1985-02-05 1988-12-13 Warner-Lambert Company Ingestible aggregate and delivery system prepared therefrom
US4851392A (en) * 1985-02-05 1989-07-25 Warner-Lambert Company Ingestible aggregate and delivery system prepared therefrom
ES2152322T3 (en) * 1994-06-29 2001-02-01 Meiji Seika Kaisha COMPOSITION OF STAISTED COLISTINE SULPHATE.

Also Published As

Publication number Publication date
JPS59187744A (en) 1984-10-24

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