JPH0662809A - Method for treating seaweeds - Google Patents

Method for treating seaweeds

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Publication number
JPH0662809A
JPH0662809A JP4220225A JP22022592A JPH0662809A JP H0662809 A JPH0662809 A JP H0662809A JP 4220225 A JP4220225 A JP 4220225A JP 22022592 A JP22022592 A JP 22022592A JP H0662809 A JPH0662809 A JP H0662809A
Authority
JP
Japan
Prior art keywords
oil
seaweeds
seaweed
mmhg
reduced pressure
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP4220225A
Other languages
Japanese (ja)
Other versions
JP3179198B2 (en
Inventor
Shuzo Nakazono
修三 中園
Moriyuki Tsutsumi
守幸 堤
Eiji Nakazono
英司 中園
Toshihiko Kusuda
俊彦 楠田
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Individual
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Individual
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Priority to JP22022592A priority Critical patent/JP3179198B2/en
Publication of JPH0662809A publication Critical patent/JPH0662809A/en
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Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

PURPOSE:To provide a seaweed theating method effective for long-term preservation of seaweeds such as wakame seaweeds (Undaria pinnatifida), Hizikia fusiforme or laver. CONSTITUTION:A hot animal oil, fish oil or plant oil in a closed vessel is charged with seaweeds such as wakame seaweeds, Hizikia fusiforme or laver, and the contents are agitated under heating while reducing the pressure in the vessel and adjusting the oil temperature. Thus, the thermal decomposition of the active ingredients in the seaweeds (e.g. sodium L-glutamate) can be prevented, and the treatment is made under a three-step pressure-decreasing situation made up of earlier stage pressure reduction process, middle stage pressure reduction process and later stage pressure reduction process. Thereby, the saline component on the surface of the seaweeds migrates into the hot oil along with penetration of the oil into the texture of the seaweeds, resulting in dehydrating the water contained in the seaweeds. The oil thus absorbed is then removed from the seaweeds.

Description

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

【0001】[0001]

【産業上の利用分野】本発明はわかめ、ひじき、のり等
の海草類の長期保存に有効な処理方法に関するものであ
る。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a treatment method effective for long-term storage of seaweeds such as seaweed, hijiki seaweed and seaweed.

【0002】[0002]

【従来の技術】わかめ、ひじき、のり等の海草類は、呈
味成分としてのL−グルタミン酸ソーダおよびミネラ
ル、各種ビタミン類等、体に有用な栄養素を豊富に含
み、保存食として一般家庭などで広く食されている。
Seaweeds such as seaweed, hijiki seaweed and seaweed contain abundant nutrients useful for the body such as sodium L-glutamate and minerals as taste components, various vitamins, etc. It is eaten.

【0003】これらの海草類は、採取後、海水を洗い流
した後、乾燥を行って保存に供するものである。
After collecting these seaweeds, the seawater is washed away and then dried for storage.

【0004】[0004]

【発明が解決しようとする課題】しかし、かかる乾燥方
法は、天日または乾燥機等によりおこなわれるものであ
るために、海草類中の水分が充分に脱水されず、また海
草類中に含まれる水溶性蛋白質等が安定化されず、腐敗
の恐れがあった。
However, since such a drying method is carried out in the sun or a dryer, the water content in the seaweeds is not sufficiently dehydrated, and the water-solubility contained in the seaweeds is not sufficient. There was a risk of spoilage due to unstabilized proteins and the like.

【0005】また、乾燥機等による高温加熱によって呈
味成分であるL−グルタミン酸ソーダが熱分解し、調理
に際して、調味効果が少なくなることが多く、また、そ
の他の有効成分であるビタミン等が分解されてしまうと
いう問題があった。
[0005] Further, when heated at a high temperature by a dryer or the like, the taste component sodium L-glutamate is thermally decomposed and the seasoning effect is often reduced during cooking, and other effective ingredients such as vitamins are decomposed. There was a problem that it would be done.

【0006】本発明は、上記の問題点を解決する海草類
の処理方法を提供することを目的とするものである。
An object of the present invention is to provide a method for treating seaweeds which solves the above problems.

【0007】[0007]

【課題を解決するための手段】本発明は、密閉容器内の
加熱された動物油、魚油または植物油に、わかめ、ひじ
き、のり等の海草類を投入し、密閉容器内を減圧しなが
ら加熱された動物油、魚油または植物油を熱媒体として
油温を加減しつつ加熱攪拌することにより海草類中のL
−グルタミン酸ソーダ等の有効成分の熱分解を防止し、
しかも、初期減圧過程においては、常圧より100 〜300m
mHg の減圧条件下で処理し、次いで中期減圧過程におい
ては、常圧より500 〜700mmHg の減圧条件下で処理し、
最後に後期減圧過程においては、常圧より700 〜750mmH
g の減圧条件下で処理を行うことにより、海草類の表面
の塩分を加熱油中に移行せしめると共に、この油が組織
中に浸透し、海草類に含まれる水分を脱水せしめ、その
後、密閉容器から取り出した海草類を圧縮または遠心分
離により油を脱油することに特徴を有する海草類の処理
方法を提供するものである。
DISCLOSURE OF THE INVENTION The present invention is to heat animal oil, fish oil or vegetable oil in a closed container into which seaweeds such as seaweed, hijiki, and seaweed are put, and the animal oil is heated under reduced pressure in the closed container. , Fish oil or vegetable oil as a heat medium, by heating and stirring while adjusting the oil temperature, L in seaweed
-Prevents thermal decomposition of active ingredients such as sodium glutamate,
Moreover, in the initial depressurization process, 100 to 300 m above normal pressure.
Treated under reduced pressure of mHg, then in the medium-term reduced pressure process, treated under reduced pressure of 500-700 mmHg from normal pressure,
Finally, in the late depressurization process, 700 to 750 mmH
By carrying out the treatment under a reduced pressure condition of g, the salt content on the surface of the seaweed is transferred to the heating oil, and this oil penetrates into the tissue to dehydrate the water contained in the seaweed, and then remove it from the closed container. The present invention provides a method for treating seaweeds characterized by deoiling oils from the seaweeds by compression or centrifugation.

【0008】[0008]

【実施例】【Example】

(実施例1)以下、実施例に基づいて、本発明を具体的
に説明すると、まず、密閉が可能な内容積4.5 m3 のク
ッカーの中に、魚油、鶏油等の各種動物油、あるいは各
種植物油等の単一油または混合油を収納し、クッカーの
ジャケット部に圧入した蒸気により油を加熱する。
(Example 1) Hereinafter, the present invention will be described in detail with reference to Examples. First, various animal oils such as fish oil and chicken oil, or various animal oils in a cooker having an internal volume of 4.5 m 3 which can be sealed are used. A single oil such as vegetable oil or a mixed oil is stored, and the oil is heated by steam injected into the jacket of the cooker.

【0009】油の温度が70〜80℃になったところで、加
熱油中に、あらかじめ乾燥を行っているわかめ、ひじ
き、のり等の海草類または採取後の海水を含んだ前記海
草類1000kgを投入し、浸漬せしめて、クッカーを閉蓋す
る。
When the temperature of the oil reaches 70 to 80 ° C., 1000 kg of the seaweeds such as seaweed, hijiki, and seaweed that have been dried in advance or the seaweeds containing seawater after sampling are put into heating oil, Let it soak and close the cooker.

【0010】次に、クッカー内の加熱油の油温を60℃前
後に保持しながらクッカー内の原料を攪拌しつつ、クッ
カー内を減圧する。
Next, while maintaining the oil temperature of the heating oil in the cooker at around 60 ° C., the raw materials in the cooker are stirred and the inside of the cooker is depressurized.

【0011】かかる減圧処理は、原料投入後から5〜10
分程度の初期減圧過程においては、常圧より250mmHg の
小さい減圧条件下で油温が55〜62℃前後で減圧処理を行
い、原料中に含まれる水溶性蛋白質等が組織中から流出
しないように短時間で組織中に凝固安定化させるもので
ある。
The depressurizing treatment is carried out 5 to 10 times after the raw materials are charged.
In the initial depressurization process of about 10 minutes, under the depressurization condition of 250 mmHg, which is smaller than normal pressure, the depressurization process is performed at an oil temperature of 55 to 62 ° C to prevent water-soluble proteins contained in the raw material from flowing out from the tissue. It stabilizes solidification in the tissue in a short time.

【0012】次の中期減圧過程においては、常圧より60
0mmHg の大きい減圧条件下で、油温が53〜55℃程度で減
圧処理を行い、約15分間この状態を保持する。同減圧条
件は、水の沸点に近い状態であるので、海草類の組織中
に含まれる水分が蒸散して脱水されると共に、海草類の
表面または海草類の表面の海水中の塩分が加熱油中に混
入し、同塩分含有の加熱油が組織中に浸透していく。
[0012] In the next medium-term depressurization process, the normal pressure is 60
Under a large decompression condition of 0 mmHg, the decompression treatment is performed at an oil temperature of about 53 to 55 ° C, and this state is maintained for about 15 minutes. Under the same depressurized condition, since the water is close to the boiling point of water, the water contained in the tissues of seagrass evaporates and is dehydrated, and the salt content of the seagrass surface or the seawater on the surface of the seagrass is mixed in the heating oil. Then, the heating oil containing the same salt penetrates into the tissue.

【0013】そして、最後の後期減圧過程においては、
常圧より700mmHg 前後の減圧条件下において、油温は63
℃前後で減圧処理を行う。この段階では、中期減圧過程
より開始した脱水処理が引き続き行われ、最終的には、
原料の含水量は、4〜6%という状態にまで脱水され
る。反応時間は、原料の種類および量によっても異なる
が、約30〜60分程度である。上記3段階減圧過程におけ
る減圧量と減圧時間との関係を図1のグラフに示す。
Then, in the final late decompression process,
Under the reduced pressure condition of around 700 mmHg from normal pressure, the oil temperature is 63
Depressurize at around ℃. At this stage, the dehydration process started from the medium-term decompression process is continued, and finally,
The water content of the raw material is dehydrated to a state of 4 to 6%. The reaction time is about 30 to 60 minutes, although it varies depending on the kind and amount of the raw materials. The graph of FIG. 1 shows the relationship between the pressure reduction amount and the pressure reduction time in the above three-stage pressure reduction process.

【0014】以上のようにして、3段階の減圧処理を行
うことによって、まず初期減圧過程において水溶性蛋白
質等の有用な栄養素は、原料の組織中に凝固安定化し、
中期減圧過程において、組織中の水分の脱水処理を迅速
におこなうと共に、後期減圧過程において、同脱水処理
を完全なものとするものである。
By performing the three-stage depressurization treatment as described above, first, useful nutrients such as water-soluble proteins are coagulated and stabilized in the tissue of the raw material in the initial depressurization process.
In the middle-stage decompression process, water in the tissue is dehydrated rapidly, and in the latter-stage decompression process, the dehydration process is completed.

【0015】そして、海草類から移行した塩分を含み、
加熱された植物油、魚油または動物油は前記海草類に含
まれる水分と置換されて組織中に含有されると共に、塩
分の浸透圧作用によって、含水分は海草類の組織の細胞
外に完全に滲出していき飛躍的な脱水処理が行える。ま
た、塩分が組織中に深く浸透して、いわゆる塩漬けと同
機能を果たし、かつ、殺菌効果をも得ることができる。
[0015] And, including the salt transferred from seaweed,
The heated vegetable oil, fish oil, or animal oil is contained in the tissue by replacing the water contained in the seaweed, and the water content is completely exuded to the extracellular part of the tissue of the seaweed by the osmotic action of salt. A dramatic dehydration process can be performed. Further, salt penetrates deeply into the tissue, performs the same function as so-called salting, and can also have a bactericidal effect.

【0016】さらに、全減圧過程において、油温は50〜
60℃前後という低温でほぼ完全な脱水を行うことができ
るため、高温によって分解してしまうビタミン等の有用
な栄養素を失うことなく、海草類中に保持可能である。
Further, the oil temperature is 50 to
Since almost complete dehydration can be performed at a low temperature of around 60 ° C, it can be retained in seaweeds without losing useful nutrients such as vitamins that are decomposed by high temperatures.

【0017】次に、前記減圧加熱処理した原料を、クッ
カーから取り出し、これを圧搾装置たとえばスクリュー
プレス機等により物理的に圧搾した後、遠心分離機によ
り遠心分離して原料中の油分を分離除去する。遠心分離
時には、単位あたり4500〜5000ポンド程度の圧力をかけ
る。また、必要に応じてノルマルヘキサン等の脱油剤で
脱油するものである。
Next, the reduced pressure heat-treated raw material is taken out from the cooker, physically squeezed by a squeezing device such as a screw press, and then centrifugally separated by a centrifuge to separate and remove the oil component in the raw material. To do. When centrifuging, apply pressure of about 4500 to 5000 pounds per unit. Further, it is deoiled with a deoiling agent such as normal hexane if necessary.

【0018】このようにして得られる海草類は、油分が
十分に除去されるため、海草類中に残留した油脂が分解
することによる悪臭、および味覚、消化障害等が防止で
きる。
Since the oil content of the seaweed thus obtained is sufficiently removed, it is possible to prevent the malodor, taste and digestive disorders due to the decomposition of the oil and fat remaining in the seaweed.

【0019】そして、得られた海草類は、低温条件下で
ほぼ完全な脱水を行うことが出来ることで、高温によっ
て分解してしまうL−グルタミン酸ソーダ等の呈味成分
や、ビタミン等の有用な栄養素を失うことなく、飼料中
に保持しつつ、長期間、安定な品質を保ちながら保存す
ることが可能である。また、低温加熱で良いので、簡単
な装置で反応を行え、本発明の海草類を得ることができ
る。
Since the obtained seaweeds can be dehydrated almost completely under low temperature conditions, they are used as taste components such as L-sodium glutamate, which are decomposed by high temperature, and useful nutrients such as vitamins. It is possible to preserve the stable quality for a long period of time while maintaining it in the feed without losing the product. Further, since low-temperature heating is sufficient, the reaction can be carried out with a simple device and the seaweed of the present invention can be obtained.

【0020】(実施例2)装置、原料等基本的な構成は
実施例1と同じであるが、3段階減圧過程における減圧
量を変えて減圧処理をおこなった。すなわち、図2に示
すように、初期減圧過程においては、常圧より100mmHg
の減圧条件下で、油温は60〜63℃で約10分間処理を行っ
た。次の中期減圧過程においては、常圧より500mmHg の
減圧条件下で、油温は54〜58℃の状態を約15分間保ち、
処理を行った。最後の後期減圧過程においては、徐々に
減圧して最終的には、常圧より700mmHg 程度まで減圧
し、油温は65℃前後に保って約40分間反応を行った。減
圧処理の後、搾油処理等は、実施例1と同様の処理を行
った。
(Embodiment 2) The apparatus, raw materials and the like are basically the same in construction as Embodiment 1, but decompression treatment was carried out by changing the decompression amount in the three-stage decompression process. That is, as shown in FIG. 2, in the initial depressurization process, 100 mmHg
The oil temperature was 60-63 ° C. under the reduced pressure condition of 10 minutes for about 10 minutes. In the next medium-term depressurization process, the oil temperature was kept at 54-58 ° C for about 15 minutes under a depressurized condition of 500 mmHg from normal pressure.
Processed. In the final depressurization process in the last stage, the pressure was gradually reduced, and finally the pressure was reduced to about 700 mmHg from normal pressure, and the oil temperature was kept at around 65 ° C to carry out the reaction for about 40 minutes. After the depressurization treatment, the oil treatment and the like were the same as those in Example 1.

【0021】以上の反応条件における減圧処理によって
も、含水量が4〜6%で、豊富な栄養素を有し、長期保
存可能な海草類を得ることができた。
Even under reduced pressure treatment under the above reaction conditions, it was possible to obtain seaweeds having a water content of 4 to 6%, rich nutrients, and long-term storage.

【0022】(実施例3)装置、原料等基本的な構成は
実施例1と同じであるが、3段階減圧過程における減圧
量を変えて減圧処理をおこなった。すなわち、図3に示
すように、初期減圧過程においては、常圧より300mmHg
の減圧条件下で、油温は55〜60℃で約5分間処理を行っ
た。次の中期減圧過程においては、常圧より700mmHg の
減圧条件下で、油温は53〜56℃の状態を約15分間保ち約
40分間反応を行った。最後の後期減圧過程においては、
常圧より750mmHg 程度まで減圧し、油温は62℃前後に保
った。減圧処理の後、搾油処理等は、実施例1と同様の
処理を行った。
(Embodiment 3) The apparatus, raw materials and the like are basically the same in construction as in Embodiment 1, but the pressure reduction process was performed by changing the pressure reduction amount in the three-stage pressure reduction process. That is, as shown in FIG. 3, in the initial depressurization process, 300 mmHg
The oil temperature was 55 to 60 ° C. for about 5 minutes under the reduced pressure condition. In the next medium-term depressurization process, the oil temperature should be kept at 53 to 56 ° C for about 15 minutes under the depressurized condition of 700 mmHg from normal pressure.
The reaction was carried out for 40 minutes. In the final late decompression process,
The pressure was reduced from atmospheric pressure to about 750 mmHg, and the oil temperature was kept around 62 ° C. After the depressurization treatment, the oil treatment and the like were the same as those in Example 1.

【0023】以上の反応条件における減圧処理によって
も、含水量が4〜6%で、豊富な栄養素を有し、長期保
存可能な海草類が得られた。
Even under reduced pressure treatment under the above reaction conditions, seaweeds having a water content of 4 to 6%, abundant nutrients and long-term storability were obtained.

【0024】[0024]

【発明の効果】以上説明してきたように、本発明では、
わかめ、ひじき、のり等の海草類を、3段階の減圧過程
において、植物油、魚油または動物油を熱媒体として一
定条件で加熱処理したことによって、加熱油が前記海草
類に含まれる水分と置換されて脱水処理が円滑に行わ
れ、保存食として安定な品質で長期間の保存が可能であ
る。
As described above, according to the present invention,
Seaweeds such as seaweed, hijiki, and seaweed were heat-treated under a certain condition with vegetable oil, fish oil, or animal oil as a heat medium in a three-stage depressurization process, so that the heating oil was replaced with water contained in the seaweeds and dehydrated. Is carried out smoothly and can be stored for a long time with stable quality as a preserved food.

【0025】また、加熱油中に、海草類の表面の塩分が
混入し、同加熱油が海草類の組織中に浸透することによ
って、同塩分の浸透圧効果により、脱水処理をより迅速
に完全に行うことができる。
Further, the salt content of the surface of the seaweed is mixed into the heated oil, and the heated oil permeates into the tissues of the seaweed, whereby the osmotic effect of the salt causes the dehydration treatment to be completed more quickly and completely. be able to.

【0026】さらに、海草類中に含まれている蛋白質そ
の他の栄養素を初期減圧段階において組織中で凝固させ
たことによって、中期および後期減圧過程においても流
出することなく保持されるので、栄養価の高い海草類を
得ることが出来る。
Furthermore, since proteins and other nutrients contained in seaweed are coagulated in the tissue in the initial decompression stage, they are retained without flowing out in the middle and late decompression processes, and thus have high nutritional value. You can obtain seaweeds.

【0027】そして、減圧処理は、低温で行うことが出
来るので、従来の高温脱水によって分解してしまってい
たL−グルタミン酸ソーダ等の呈味成分や、ビタミン等
の有用な栄養素も、原料中に保持させることができ、調
理の際の調味効果および健康食としての品質も充分に保
持しうるという効果を奏する。
Since the reduced pressure treatment can be carried out at a low temperature, taste components such as L-sodium glutamate, which have been decomposed by conventional high temperature dehydration, and useful nutrients such as vitamins are also contained in the raw materials. It can be retained, and the effect of seasoning at the time of cooking and the quality of healthy food can be sufficiently retained.

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

【図1】3段階減圧による減圧過程を示す図であり、縦
軸に常圧からの減圧量を、横軸に減圧時間を示してい
る。
FIG. 1 is a diagram showing a depressurization process by three-stage depressurization, in which the vertical axis represents the amount of depressurization from normal pressure and the horizontal axis represents the depressurization time.

【図2】3段階減圧による減圧過程を示す図であり、縦
軸に常圧からの減圧量を、横軸に減圧時間を示してい
る。
FIG. 2 is a diagram showing a depressurization process by three-stage depressurization, in which the vertical axis represents the amount of depressurization from normal pressure and the horizontal axis represents the depressurization time.

【図3】3段階減圧による減圧過程を示す図であり、縦
軸に常圧からの減圧量を、横軸に減圧時間を示してい
る。
FIG. 3 is a diagram showing a depressurization process by three-stage depressurization, in which the vertical axis represents the amount of decompression from normal pressure and the horizontal axis represents the decompression time.

───────────────────────────────────────────────────── フロントページの続き (71)出願人 592179344 楠田 俊彦 福岡県福岡市中央区地行1丁目2−11 (72)発明者 中園 修三 福岡県福岡市中央区平尾4丁目7番17号 (72)発明者 堤 守幸 福岡県福岡市中央区赤坂1丁目1−7−27 (72)発明者 中園 英司 福岡県福岡市早良区百道浜4−3−2− 207 (72)発明者 楠田 俊彦 福岡県福岡市中央区地行1丁目2−11 ─────────────────────────────────────────────────── ─── Continuation of the front page (71) Applicant 592179344 Toshihiko Kusunita 1-2-11 Jigoku, Chuo-ku, Fukuoka-shi, Fukuoka (72) Inventor Shuzo Nakazono 4-7-17 Hirao, Chuo-ku, Fukuoka-shi, Fukuoka (72) ) Inventor Moriyuki Tsutsumi 1-7-27 Akasaka, Chuo-ku, Fukuoka-shi, Fukuoka (72) Inventor Eiji Nakazono 4-3-2-207 Hyakudohama, Sawara-ku, Fukuoka-shi, Fukuoka (72) Toshihiko Kusuda Fukuoka-ken 1-2-11 Jigoku, Chuo-ku, Fukuoka-shi

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】密閉容器内の加熱された動物油、魚油また
は植物油に、わかめ、ひじき、のり等の海草類を投入
し、密閉容器内を減圧しながら加熱された動物油、魚油
または植物油を熱媒体として油温を加減しつつ加熱攪拌
することにより海草類中のL−グルタミン酸ソーダ等の
有効成分の熱分解を防止し、しかも、初期減圧過程にお
いては、常圧より100 〜300mmHg の減圧条件下で処理
し、次いで中期減圧過程においては、常圧より500 〜70
0mmHg の減圧条件下で処理し、最後に後期減圧過程にお
いては、常圧より700 〜750mmHg の減圧条件下で処理を
行うことにより、海草類の表面の塩分を加熱油中に移行
せしめると共に、この油が原料の組織中に浸透し、海草
類に含まれる水分を脱水せしめ、その後、密閉容器から
取り出した海草類を圧縮または遠心分離により油を脱油
することを特徴とする海草類の処理方法。
1. A heated animal oil, fish oil or vegetable oil in a closed container is charged with seaweeds such as seaweed, hijiki seaweed and seaweed, and the heated animal oil, fish oil or vegetable oil is used as a heat medium while reducing the pressure in the closed container. By heating and stirring while adjusting the oil temperature, thermal decomposition of active ingredients such as L-sodium glutamate in seaweeds is prevented, and in the initial depressurization process, treatment is performed under reduced pressure conditions of 100 to 300 mmHg above atmospheric pressure. Then, in the medium-term depressurization process, 500 to 70
Treated under a reduced pressure condition of 0 mmHg, and finally in the latter stage decompression process, by treating under a reduced pressure condition of 700 to 750 mmHg from normal pressure, the salt content of the seaweed surface is transferred to the heating oil and Permeates into the tissue of the raw material to dehydrate the water contained in the seaweed, and then the seaweed taken out from the closed container is compressed or centrifuged to deoil the oil.
JP22022592A 1992-08-19 1992-08-19 How to treat seaweeds Expired - Fee Related JP3179198B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP22022592A JP3179198B2 (en) 1992-08-19 1992-08-19 How to treat seaweeds

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP22022592A JP3179198B2 (en) 1992-08-19 1992-08-19 How to treat seaweeds

Publications (2)

Publication Number Publication Date
JPH0662809A true JPH0662809A (en) 1994-03-08
JP3179198B2 JP3179198B2 (en) 2001-06-25

Family

ID=16747847

Family Applications (1)

Application Number Title Priority Date Filing Date
JP22022592A Expired - Fee Related JP3179198B2 (en) 1992-08-19 1992-08-19 How to treat seaweeds

Country Status (1)

Country Link
JP (1) JP3179198B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
ITRM20120388A1 (en) * 2012-08-03 2014-02-04 Algea As METHOD AND PLANT FOR THE PRODUCTION OF ALGAE FLOUR.

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
ITRM20120388A1 (en) * 2012-08-03 2014-02-04 Algea As METHOD AND PLANT FOR THE PRODUCTION OF ALGAE FLOUR.
WO2014020423A1 (en) * 2012-08-03 2014-02-06 Algea As Method and installation for making seaweed meal

Also Published As

Publication number Publication date
JP3179198B2 (en) 2001-06-25

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