JP4131689B2 - Method for producing algal salt - Google Patents

Method for producing algal salt Download PDF

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JP4131689B2
JP4131689B2 JP2003292796A JP2003292796A JP4131689B2 JP 4131689 B2 JP4131689 B2 JP 4131689B2 JP 2003292796 A JP2003292796 A JP 2003292796A JP 2003292796 A JP2003292796 A JP 2003292796A JP 4131689 B2 JP4131689 B2 JP 4131689B2
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康人 細谷
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天野実業株式会社
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本発明は、海藻に含まれる成分のいわゆる海藻エキスを食塩に取り込んだ藻塩の製造方法に関し、さらに詳しくは、海藻エキスを効率良く抽出して取り込み、ミネラルバランスが良く品質の安定した藻塩の製造方法に関する。 The present invention is a so-called seaweed extract components contained in seaweed relates to a process for the preparation of algae salt taken into brine, more particularly, it captures the seaweed extract and efficiently extracted, well quality mineral balance stable algae salt It relates to a manufacturing method.

海藻エキスを食塩に含有せさたいわゆる藻塩は、古くは、海藻に海水をかけて塩分を付着させ、焼いて水に溶かし、上澄み液を煮詰めることにより得られる。従来、この藻塩の製造方法として、海水と海藻とを繰り返し接触させて前記海水中の水分を蒸発させることにより塩分が濃縮した鹹水を製造する鹹水製造工程と、得られた鹹水を濃縮する鹹水の濃縮工程と、濃縮した鹹水に海藻を焼却した藻灰を添加して溶解させる藻灰の溶解工程と、藻灰溶解鹹水を濾過して海藻エキス含有鹹水とする濾過工程と、得られた海藻エキス含有鹹水を煮詰める煮詰め工程と、該煮詰め工程で得られた混合物から水分を分離する脱水工程と、該脱水工程で得られた脱水塩を加熱して藻塩として回収する焼塩工程とを有するものがある(例えば、特許文献1参照。)。   In the past, so-called algal salt containing seaweed extract in salt is obtained by applying seawater to seaweed to deposit salt, baking it, dissolving it in water, and simmering the supernatant. Conventionally, as a method for producing the algae salt, a brine production process for producing saltwater-enriched brine by repeatedly contacting seawater and seaweed to evaporate water in the seawater, and brine obtained by concentrating the obtained brine A concentration step, a step of dissolving algae ash in which algae ash incinerated with seaweed is added to the concentrated brine, and a step of filtering the algae ash-dissolved brine to obtain a seaweed extract-containing brine, and the obtained seaweed extract Some have a simmering step for simmering the contained brine, a dehydration step for separating water from the mixture obtained in the simmering step, and a calcination salt step for heating and recovering the dehydrated salt obtained in the dehydration step as algal salt (For example, see Patent Document 1).

上記の特許文献1に記載のものでは、次のような問題点があった。
(1)海水を原料としているため、海水に含まれるマグネシウムなどのニガリ成分が残存しており、得られた藻塩は苦味を呈する。そこで、海藻エキスを抽出したのち上記のニガリ成分を脱水にて除去すると、ニガリとともに抽出成分の一部が失われるので、結果として海藻からの抽出効率が低下する。
The one described in Patent Document 1 has the following problems.
(1) Since seawater is used as a raw material, bittern components such as magnesium remaining in seawater remain, and the obtained algal salt exhibits a bitter taste. Therefore, if the above-mentioned bittern component is removed by dehydration after extracting the seaweed extract, a part of the extract component is lost together with the bittern, resulting in a decrease in extraction efficiency from the seaweed.

(2)鹹水に藻灰を溶解したのち濾過して不溶解物を除去しているが、藻灰は微細であるため、上記の濾過に例えばセライト濾過や目の細かなフィルターを用いる必要がある。しかしコンブやモズクから抽出されるアルギン酸などの有機成分は粘度が高いため、目の細かなフィルターでの濾過が容易でないうえ、これらの有機成分も濾過の際に除去されるので、結果として海藻からの抽出効率が低下する。   (2) Algae ash is dissolved in brine and then filtered to remove insoluble matter. However, since alga ash is fine, it is necessary to use, for example, Celite filtration or a fine filter for the above filtration. . However, organic components such as alginic acid extracted from kombu and mozuku have a high viscosity, so it is not easy to filter with fine filters, and these organic components are also removed during filtration, resulting in seaweed. The extraction efficiency of is reduced.

(3)海水を藻枝条架に循環注水する場合は、海水が徐々に濃縮されながら海藻と接触するが、塩分濃度が異なると浸透圧の関係から海藻エキスの抽出量が異なる。このため海藻エキスの抽出量が一定せず、得られた藻塩の品質にバラツキを生じ易い。   (3) When seawater is circulated and poured into the algae branch, the seawater comes into contact with the seaweed while being gradually concentrated. However, when the salinity concentration is different, the amount of seaweed extract extracted varies depending on the osmotic pressure. For this reason, the extraction amount of the seaweed extract is not constant, and the quality of the obtained algal salt tends to vary.

特開平11−253126号公報JP 11-253126 A

本発明は上記の問題点を解消し、海藻エキスを効率良く抽出して取り込み、ミネラルバランスが良く品質の安定した藻塩の製造方法を提供することを技術的課題とする。 The present invention is to solve the above takes the seaweed extract and efficiently extracted, and technical object to provide a method for producing mineral balance is good quality stable algae salt.

本発明は、上記の課題を解決するため、例えば本発明の実施の形態を示す図1から図3に基づいて説明すると、次のように構成したものである。
即ち、請求項1に記載の発明は藻塩の製造方法に関し、精製塩100重量部を水に溶解して所定濃度に調製した塩水へ5〜60重量部の海藻を投入し、所定時間浸漬する抽出工程(1)と、上記の浸漬後の海藻混合液を濾過して海藻エキス抽出塩水と抽出残渣とに分離する分離工程(2)と、上記の抽出残渣を焼却して炭化させ、得られた藻灰に水を加えてこの藻灰に含まれるミネラルを溶解したのち、不溶解物を除去してミネラル溶解液を得るミネラル回収工程(3)と、上記のミネラル溶解液を、前記の分離工程で得た海藻エキス抽出塩水に混合する混合工程(4)と、上記の混合工程(4)で得られた混合液から水分を蒸発させて固形分を回収する乾燥工程(6)と、を備えることを特徴とする。
In order to solve the above problems, the present invention is configured as follows, for example, based on FIGS. 1 to 3 showing an embodiment of the present invention.
That is, the invention according to claim 1 relates to a method for producing algae salt, an extraction in which 5 to 60 parts by weight of seaweed is poured into salt water prepared by dissolving 100 parts by weight of purified salt in water and adjusted to a predetermined concentration, and immersed for a predetermined time. The step (1), the separation step (2) in which the seaweed mixed solution after the immersion is filtered and separated into the seaweed extract-extracted brine and the extraction residue, and the extraction residue is incinerated to be carbonized and obtained. Mineral recovery step (3), in which water is added to alga ash to dissolve minerals contained in the alga ash, and then insoluble matter is removed to obtain a mineral solution, and the above mineral solution is separated from the above-described separation step. A mixing step (4) for mixing with the seaweed extract-extracted salt water obtained in step 1 and a drying step (6) for recovering solids by evaporating water from the mixed solution obtained in the mixing step (4). It is characterized by that.

請求項2に記載の発明は藻塩の製造方法に関し、精製塩100重量部を水に溶解して所定濃度に調製した塩水へ5〜60重量部の海藻を投入し、所定時間浸漬する抽出工程(1)と、上記の浸漬後の海藻混合液を濾過して海藻エキス抽出塩水と抽出残渣とに分離する分離工程(2)と、上記の抽出残渣を焼却して炭化させ、得られた藻灰に水を加えてこの藻灰に含まれるミネラルを溶解したのち、不溶解物を除去してミネラル溶解液を得るミネラル回収工程(3)と、上記の分離工程(2)で得られた海藻エキス抽出塩水から水分を蒸発させて固形分を回収する乾燥工程(6)と、を備え、前の製造サイクルのミネラル回収工程(3)で回収されたミネラル溶解液を、上記の抽出工程(1)で塩水に混合することを特徴とする。   The invention according to claim 2 relates to a method for producing algal salt, an extraction step in which 100 parts by weight of purified salt is dissolved in water and 5 to 60 parts by weight of seaweed is poured into the salt water prepared to a predetermined concentration and immersed for a predetermined time ( 1), a separation step (2) in which the seaweed mixed solution after immersion is filtered and separated into seaweed extract-extracted brine and extraction residue, and the extraction residue is incinerated and carbonized, and the resulting algal ash Seawater extract obtained by the mineral recovery step (3) obtained by adding water to the alga ash to dissolve minerals contained in the alga ash and then removing the insoluble matter to obtain a mineral solution, and the separation step (2) above. A drying step (6) for recovering solids by evaporating water from the extracted salt water, and extracting the mineral solution recovered in the mineral recovery step (3) of the previous production cycle with the extraction step (1) And mixed with salt water.

本発明によれば、海藻に含まれる成分を食塩に取り込んだ藻塩であって、含有するカルシウム成分が0.4重量%以下、カリウム成分が10.0重量%以下、マグネシウム成分が0.5重量%以下の藻塩を得ることができる。 According to the present invention, it is an algal salt in which a component contained in seaweed is incorporated in salt, and the calcium component contained is 0.4% by weight or less, the potassium component is 10.0% by weight or less, and the magnesium component is 0.5% by weight. % Or less algal salt can be obtained.

上記の抽出工程では、塩水が所定濃度に調製され、これに所定量の海藻が所定時間浸漬されるので、海藻に含まれるグルタミン酸やアルギン酸などの海藻エキスの、塩水中への抽出量が安定する。そして、この抽出工程で抽出しきれなかった海藻中のミネラル等は、ミネラル回収工程で抽出残渣から回収され、塩水に取り込まれる。従って、この塩水を乾燥して得られた藻塩には、海藻に含まれる有機成分やミネラルなど、海藻から取り出すことができるエキスの全てがバランスよく取り込まれる。   In the above extraction step, salt water is prepared at a predetermined concentration, and a predetermined amount of seaweed is immersed in the predetermined time, so that the extraction amount of seaweed extracts such as glutamic acid and alginic acid contained in the seaweed into the salt water is stabilized. . And the mineral etc. in the seaweed which could not be extracted by this extraction process are collect | recovered from an extraction residue by a mineral collection | recovery process, and are taken in into salt water. Therefore, all the extracts that can be extracted from the seaweed, such as organic components and minerals contained in the seaweed, are taken into the algal salt obtained by drying the salt water in a balanced manner.

上記の抽出工程で、精製塩の所定濃度は、高濃度ほど浸透圧の関係から海藻エキスが容易に抽出され、また、乾燥工程で蒸発させる水分量が少なくエネルギーコストを低減できる。しかし塩分濃度が高すぎると過飽和状態となって溶解しきれない塩分が析出し、一方、塩分濃度が低すぎると海藻浸漬中に腐敗を生じる惧れがある。そこで、上記の塩水の塩分濃度は、15〜35重量%に設定するのが好ましく、15〜25重量%に設定するとさらに好ましい。   In the extraction step, the higher the concentration of the purified salt, the easier the seaweed extract is extracted from the relationship of osmotic pressure, and the less the amount of water evaporated in the drying step, the lower the energy cost. However, if the salinity is too high, it becomes supersaturated and a salt that cannot be dissolved is deposited. On the other hand, if the salinity is too low, there is a risk of spoilage during immersion in seaweed. Therefore, the salt concentration of the above-mentioned salt water is preferably set to 15 to 35% by weight, and more preferably set to 15 to 25% by weight.

上記の抽出工程は、上記の分離工程ののちに、追加抽出工程として繰り返すことができる。即ち、本発明は、上記の分離工程で分離した海藻エキス抽出塩水に、新しい海藻を投入して所定時間浸漬する、1または複数の追加抽出工程をさらに備え、この追加抽出工程による浸漬後の海藻混合液に、前記の分離工程を再度施してもよい。これにより海藻エキス抽出液に含まれる海藻エキス成分の含有量を大幅に高めることができる。   The extraction process can be repeated as an additional extraction process after the separation process. That is, the present invention further includes one or a plurality of additional extraction steps in which fresh seaweed is introduced into the seaweed extract-extracted salt water separated in the separation step and immersed for a predetermined time, and the seaweed after immersion in the additional extraction step You may perform the said isolation | separation process again to a liquid mixture. Thereby, content of the seaweed extract component contained in a seaweed extract extract can be raised significantly.

上記の抽出工程や追加抽出工程で塩水に投入する海藻は、コンブ、ワカメ、ヒジキ、ホンダワラ、モズクなど、食用可能な海藻を任意に用いることができる。これらの海藻は全体をそのまま、あるいは任意の大きさに切断して用いてもよいが、100mm以下の寸法に裁断したものを用いると、塩水との接触面積が増えて効率よく抽出できるうえ、抽出残渣を焼却する場合も短時間で焼却できるので好ましい。なお、この裁断寸法は50mm以下であるとより好ましく、例えば、長さが15mmで幅が3〜5mm程度など、20mm以下の寸法に裁断するとさらに好ましい。   As the seaweed to be added to the salt water in the above extraction step or additional extraction step, edible seaweeds such as kombu, seaweed, cypress, hondawald, mozuku and the like can be arbitrarily used. These seaweeds may be used as they are or after being cut to an arbitrary size, but if they are cut to a size of 100 mm or less, the contact area with salt water will increase and extraction will be efficient. The residue is preferably incinerated because it can be incinerated in a short time. In addition, it is more preferable that this cutting dimension is 50 mm or less. For example, it is more preferable to cut to a dimension of 20 mm or less, such as a length of 15 mm and a width of about 3 to 5 mm.

上記の分離工程では、濾材の目が粗いと海藻の滓が濾液である海藻エキス抽出塩水に混入し、乾燥工程で不良品を生じる惧れがある。一方、海藻エキス抽出塩水は、海藻エキスのヌメリなどに起因して粘度が高くなるため、濾材の目が細かすぎると濾過に長時間を要するうえ、有機成分の一部が濾過しきれず、結果として抽出効率が低下する。そこで、上記の分離工程では、140〜250メッシュの濾材を用いるのが好ましく、200メッシュ(目開き74μm)前後の濾材を用いると一層好ましい。   In the above separation process, if the filter medium is rough, seaweed cocoons are mixed into the seaweed extract-extracted salt water, which is the filtrate, and a defective product may be produced in the drying process. On the other hand, seaweed extract-extracted salty water has a high viscosity due to the seaweed extract's slime, etc., and if the filter medium is too fine, it takes a long time to filter, and part of the organic components cannot be filtered. Extraction efficiency decreases. Therefore, in the separation step, it is preferable to use a 140 to 250 mesh filter medium, and it is more preferable to use a filter medium having a mesh of about 200 mesh (aperture 74 μm).

上記の乾燥工程では、スプレードライ法によると、微粉末状の藻塩を得ることができ、この微粉末状の藻塩は溶解性やスナック菓子への付着性などに優れ、幅広い用途に適用できるのでより好ましい。しかしながら本発明では、上記の乾燥工程で、例えば水分を15%程度まで濃縮して真空凍結乾燥法や熱風乾燥法で乾燥し、これを粉砕して粉末化するなど、他の乾燥法を用いてもよい。
上記の乾燥工程で乾燥される被乾燥液は、予めホモジナイザー等の撹拌装置で均一化しておくと、海藻エキスと塩分とが均一に混合されるうえ被乾燥液の粘度が低下するので、例えばスプレードライ法では液滴が細かくなり、乾燥装置の内面への塩分の付着量が低下して収率が向上するのでより好ましい。
In the above drying step, a fine powdery algal salt can be obtained according to the spray drying method, and this finely powdered algal salt is excellent in solubility, adhesion to snacks, etc., and more preferable because it can be applied to a wide range of applications. . However, in the present invention, in the above drying step, for example, the moisture is concentrated to about 15%, dried by a vacuum freeze drying method or a hot air drying method, pulverized and powdered, and other drying methods are used. Also good.
If the liquid to be dried to be dried in the above drying step is homogenized in advance with a stirrer such as a homogenizer, seaweed extract and salt are uniformly mixed and the viscosity of the liquid to be dried decreases. The dry method is more preferable because the droplets become finer, and the amount of salt attached to the inner surface of the drying device is reduced to improve the yield.

上記の藻塩は、上記の追加抽出工程を繰り返すことで海藻エキス成分の含有量を高めることができるが、逆にこの追加抽出工程を少なくし、或いは省略することで、藻塩に含まれるミネラル成分、即ち、カルシウム成分とカリウム成分とマグネシウム成分の各含有量を低く抑えることができる。
本発明の藻塩に含まれるミネラル成分のうち、カリウム成分は、好ましくは8.0重量%以下に、より好ましくは5.0重量%以下に低く抑えられる。また、マグネシウム成分も、0.4重量%以下に低く抑えるとより好ましい。
The algal salt can increase the content of the seaweed extract component by repeating the additional extraction step, but conversely, by reducing or omitting this additional extraction step, the mineral component contained in the algal salt, That is, each content of a calcium component, a potassium component, and a magnesium component can be suppressed low.
Of the mineral components contained in the algal salt of the present invention, the potassium component is preferably kept at a low level of 8.0% by weight or less, more preferably at a level of 5.0% by weight or less. Further, it is more preferable that the magnesium component is suppressed to 0.4% by weight or less.

本発明は上記のように構成され作用することから、次の効果を奏する。   Since the present invention is configured and operates as described above, the following effects can be obtained.

(イ)所定濃度に調製した塩水に海藻を浸漬することから、海藻から抽出される有機成分などの海藻エキスの抽出量にバラツキが少なく、品質の安定した藻塩を得ることができる。   (A) Since seaweed is immersed in salt water prepared at a predetermined concentration, the extraction amount of seaweed extracts such as organic components extracted from seaweed has little variation, and a stable quality algal salt can be obtained.

(ロ)精製塩に水を加えた塩水を用いるため、前記の従来技術と異なって、得られた藻塩は海水に含まれるニガリ成分に起因した苦味や金属的味を呈することがない。さらに、塩水からニガリ成分を除去する処理が不要であるため、塩水中に取り込んだ海藻エキスをこのニガリ成分除去処理で失うことがない。   (B) Since salt water obtained by adding water to purified salt is used, the obtained algal salt does not exhibit a bitter or metallic taste due to bittern components contained in seawater, unlike the above-described conventional technology. Furthermore, since the process which removes a bittern component from salt water is unnecessary, the seaweed extract taken in salt water is not lost by this bittern component removal process.

(ハ)抽出工程後の抽出残渣を焼却して得た藻灰は、海藻エキスを含んだ塩水へ直接溶解されるのではなく、一旦水に溶解して不溶解物を除去したのち塩水に混合されるので、微細な不溶解物を目の細かなフィルターやセライト濾過などで効率良く除去できる。しかも、この不溶解物を除去する際に塩水中の海藻エキスが取り除かれる惧れがなく、塩水中に取り込まれた海藻エキスの含有量を高く維持することができる。   (C) Algae ash obtained by incineration of the extraction residue after the extraction process is not directly dissolved in salt water containing seaweed extract, but once dissolved in water to remove insoluble matters, mixed with salt water Therefore, fine insoluble matter can be efficiently removed with a fine filter or Celite filtration. Moreover, there is no concern that the seaweed extract in the salt water will be removed when the insoluble matter is removed, and the content of the seaweed extract taken into the salt water can be kept high.

(ニ)海藻に含まれるグルタミン酸やアルギン酸などの有機成分は抽出工程で塩水中に取り込まれ、一方、抽出工程では抽出しきれなかった、抽出残渣に含まれるミネラルは、ミネラル回収工程で回収されて塩水に混合されるので、海藻に含まれる有機成分とミネラルとの全体を効率良く塩水中に取り込むことができ、成分バランスの良い藻塩を得ることができる。   (D) Organic components such as glutamic acid and alginic acid contained in seaweed are taken into salt water in the extraction process, while minerals contained in the extraction residue that could not be extracted in the extraction process are recovered in the mineral recovery process. Since it is mixed with salt water, the whole organic component and mineral contained in seaweed can be efficiently taken into the salt water, and algae salt with a good component balance can be obtained.

以下、本発明の実施の形態を図面に基づき説明する。
図1は本発明の第1実施形態を示す、藻塩の製造方法のフロー図である。
Hereinafter, embodiments of the present invention will be described with reference to the drawings.
FIG. 1 is a flowchart of a method for producing algal salt, showing a first embodiment of the present invention.

図1に示すように、この藻塩の製造方法は、精製塩と水と海藻を原料とし、精製塩を水に溶解して所定濃度の塩水に調製し、この塩水に海藻を所定時間浸漬する抽出工程(1)と、上記の浸漬後の海藻混合液を濾過して海藻エキス抽出塩水と抽出残渣とに分離する分離工程(2)と、上記の抽出残渣を焼却して炭化させ、得られた藻灰に水を加えてこの藻灰に含まれるミネラル等を溶解したのち、不溶解物を除去してミネラル溶解液を得るミネラル回収工程(3)と、上記のミネラル溶解液を前記の分離工程(2)で得た海藻エキス抽出塩水に混合する混合工程(4)と、この混合工程(4)で得られた混合液を殺菌し均一化する乾燥準備工程(5)と、この準備済み混合液をスプレードライ装置で乾燥して微粉末状の固形分を回収する乾燥工程(6)と、得られた微粉末を篩分けして藻塩に仕上げる仕上工程(7)とからなる。   As shown in FIG. 1, this algal salt production method uses purified salt, water, and seaweed as raw materials, dissolves the purified salt in water to prepare a predetermined concentration of salt water, and soaks seaweed in the salt water for a predetermined time. The step (1), the separation step (2) in which the seaweed mixed solution after the immersion is filtered and separated into the seaweed extract-extracted brine and the extraction residue, and the extraction residue is incinerated to be carbonized and obtained. Mineral recovery step (3), in which water is added to alga ash to dissolve minerals contained in the alga ash, and then insoluble matter is removed to obtain a mineral solution, and the above mineral solution is separated into the separation step A mixing step (4) for mixing with the seaweed extract extracted salt water obtained in (2), a drying preparation step (5) for sterilizing and homogenizing the mixed solution obtained in this mixing step (4), and this prepared mixing A drying step (6) in which the liquid was dried with a spray dryer to recover a fine powdery solid, and the obtained And a finishing step (7) in which the fine powder is sieved to finish the algal salt.

次に、海藻としてコンブを用いた場合を例にとり、上記の各製造工程を詳しく説明する。
最初に抽出工程(1)では、精製塩6kgを水18kgに溶解して、塩分濃度25重量%の塩水を調製し、この塩水にコンブ1.2kgを投入して18時間浸漬した。上記のコンブは、予め長さが15mm程度、幅が3〜5mm程度にカットされたものを用いた。ただし本発明では、例えば100mm程度以下のより大きな寸法にカットしたものを用いても良く、さらにはカットしていない海藻を用いてもよい。なお、上記の投入したコンブは塩水を吸収するので、塩水への投入量は全てのコンブが塩水に浸る程度に抑えておくのが好ましい。
Next, taking the case of using kombu as the seaweed, the above-described production steps will be described in detail.
First, in the extraction step (1), 6 kg of purified salt was dissolved in 18 kg of water to prepare a salt water having a salt concentration of 25% by weight, and 1.2 kg of kombu was added to this salt water and immersed for 18 hours. As the above-mentioned comb, a length previously cut to about 15 mm and a width of about 3 to 5 mm was used. However, in this invention, you may use what was cut into the bigger dimension of about 100 mm or less, for example, and also you may use the seaweed which is not cut. In addition, since the above-mentioned added kombu absorbs salt water, it is preferable to suppress the amount of salt input to the extent that all the kombu is immersed in salt water.

次に、上記のコンブが浸漬されている塩水を、分離工程(2)で先ず140メッュのフィルターで粗く濾過したのち、次いで200メッシュ(目開き74μm)のフィルターを用いて濾過し、約21kgの海藻エキス抽出塩水と約4.2kgの抽出残渣とに分離した。上記の塩水にはコンブエキスが抽出されており、粘度が高いので、目の細かなフィルターを用いると濾過作業が困難になるが、フィルターの目が粗いとコンブの滓が濾液に混入する惧れがあり、200メッシュ程度のフィルターを用いるのが好ましい。   Next, the salt water in which the above-mentioned kombu is immersed is first roughly filtered through a 140-mesh filter in the separation step (2), and then filtered using a 200-mesh filter (aperture 74 μm). It was separated into seaweed extract extracted brine and about 4.2 kg of extraction residue. Comb extract is extracted from the above salt water, and the viscosity is high, so if a fine filter is used, it will be difficult to filter, but if the filter is rough, the koji of the kombu may be mixed into the filtrate. It is preferable to use a filter of about 200 mesh.

なおこの抽出工程(1)では、上記の抽出残渣の含水量を少なくして後述の炭化を容易にさせるほか、抽出残渣に含まれる塩分や海藻エキスをできるだけ多く回収するため、この抽出残渣に脱水処理を施すのが好ましい。この脱水処理で回収された水分は、上記のコンブが浸漬された塩水と同様、200メッシュのフィルターで濾過され、濾液が上記の海藻エキス抽出塩水に戻される。
また上記の抽出残渣は、好ましくは水で洗浄され、この洗浄処理で得られた洗浄液がフィルタで濾過されたのち上記の海藻エキス抽出塩水に加えられる。
In this extraction step (1), the water content of the extraction residue is reduced to facilitate carbonization, which will be described later, and the salt and seaweed extract contained in the extraction residue are recovered as much as possible. It is preferable to apply the treatment. The water recovered by the dehydration treatment is filtered through a 200 mesh filter in the same manner as the salt water in which the kombu is immersed, and the filtrate is returned to the seaweed extract-extracted salt water.
The extraction residue is preferably washed with water, and the washing liquid obtained by this washing treatment is filtered through a filter and then added to the seaweed extract-extracted salt water.

上記の抽出残渣は、次いでミネラル回収工程(3)で500〜800℃に加熱して焼却し、0.96kgの藻灰に炭化させる。この藻灰に水2.4kgを加えて約80℃に加熱し、藻灰に含まれるミネラル成分を溶解させ、濾布で濾過したのち、セライト濾過で細かな不溶解物を除去し、2.6kgのミネラル溶解液を得た。上記の藻灰に加える水は、量が多いと後述の乾燥工程(6)で蒸発させる水分量が多くなり、コスト高になる。このため、上記の加水量は少ないほうが好ましいが、上記のミネラル溶解液には塩分も含まれており、加水量が少な過ぎると塩分やミネラル等の固形分が溶解しきれないことがある。このため、上記の加水量は、ミネラル溶解液に含まれる固形分が25%以下となるように調整される。
なお、この実施形態では上記の不溶解物を、濾布で濾過したのちセライト濾過することで除去したが、本発明のミネラル回収工程は、これに代えて、例えば自然沈降ののちセライト濾過するなど、他の方法で不溶解物を除去してミネラル溶解液を得てもよい。
Next, the above extraction residue is incinerated by heating to 500 to 800 ° C. in the mineral recovery step (3) and carbonized to 0.96 kg of algal ash. 2.4 kg of water is added to this algal ash and heated to about 80 ° C., the mineral components contained in the algal ash are dissolved, filtered through a filter cloth, fine insoluble matters are removed by Celite filtration, and 2. 6 kg of mineral solution was obtained. If the amount of water added to the algal ash is large, the amount of water evaporated in the drying step (6) described later increases, resulting in an increase in cost. For this reason, although it is preferable that said amount of hydration is small, salt content is also contained in said mineral solution, When solid amount is too small, solid content, such as salt and a mineral, may not fully melt | dissolve. For this reason, said amount of hydration is adjusted so that the solid content contained in a mineral solution may be 25% or less.
In this embodiment, the insoluble matter is removed by filtration through a filter cloth and then through celite filtration, but the mineral recovery step of the present invention is replaced by, for example, celite filtration after natural sedimentation. The mineral solution may be obtained by removing the insoluble matter by other methods.

次に、上記のミネラル溶解液を、混合工程(4)において前記の分離工程(2)で得た海藻エキス抽出塩水と混合する。この混合液は、次の乾燥準備工程(5)で80℃に加熱して殺菌するとともに、混合液の粘度を低下させる。次いで、ホモミキサーやホモジナイザーで撹拌・均一化し、コンブエキスと塩分とを均一に混合するとともに、粘度をさらに低下させる。これらの処理は必ずしも必要ではないが、これらの処理を施すことにより、コンブエキスが均一に分散されるので品質が良くなるうえ、次工程の乾燥時に装置内への付着量が低減し、収率が向上する。なお、上記の混合液は、前記の各工程で異物混入の惧れがある場合、さらに100メッシュ(目開き149μm)程度のフィルターで濾過してこれらの異物が除去される。   Next, the mineral solution is mixed with the seaweed extract extracted brine obtained in the separation step (2) in the mixing step (4). This mixed solution is sterilized by heating to 80 ° C. in the next drying preparation step (5), and lowers the viscosity of the mixed solution. Next, the mixture is stirred and homogenized with a homomixer or homogenizer to uniformly mix the kombu extract and the salt, and further reduce the viscosity. These treatments are not always necessary, but by applying these treatments, the kombu extract is uniformly dispersed, so that the quality is improved and the amount of adhesion to the apparatus is reduced during the drying of the next process, yield. Will improve. In addition, when there is a possibility that foreign matter is mixed in each of the above steps, the mixed liquid is further filtered through a filter of about 100 mesh (mesh size: 149 μm) to remove these foreign matters.

次に、上記の準備済み混合液を乾燥工程(6)で、スプレードライ装置により180〜200℃で乾燥し、微粉末状の固形分を回収する。このとき、乾燥温度が高いほうが収率が向上するが、これは乾燥速度が速くなって装置内への付着量が少なく済むためと思われる。なお、上記のスプレードライ装置としては、アトマイザーが回転円盤式のものであってもよいが、加圧ノズル式のものを用いてもよく、特定の形式のものに限定されない。   Next, in the drying step (6), the prepared mixed liquid is dried at 180 to 200 ° C. by a spray drying apparatus, and a solid content in a fine powder form is recovered. At this time, the higher the drying temperature, the higher the yield. This is probably because the drying speed is increased and the amount of adhesion to the apparatus is reduced. In addition, as said spray drying apparatus, although an atomizer may be a rotary disk type thing, a pressure nozzle type thing may be used and it is not limited to a specific type thing.

最後に、上記の微粉末状の固形分は、仕上工程(7)で32メッシュ(目開き500μm)の篩で篩分けして塊状物を取り除き、これにより5.44kgの微粉末状の藻塩を得た。なお、この仕上工程(7)では、必要に応じて造粒装置を用い、上記の微粉末状の藻塩を顆粒状に成形してもよい。   Finally, in the finishing step (7), the fine powdered solid content is sieved with a 32 mesh (aperture 500 μm) sieve to remove clumps, thereby removing 5.44 kg of fine powdered algal salt. Obtained. In the finishing step (7), the above-mentioned finely powdered algal salt may be formed into granules using a granulator as necessary.

得られた上記の藻塩は、ニガリ成分に起因する苦味や金属的な味がなく、コンブ特有の旨味を有していた。この藻塩が含有する成分を分析した結果、カルシウム成分が0.0907重量%、カリウム成分が1.52重量%、マグネシウム成分が0.139重量%であった。また上記の微粉末状の藻塩はきめの細かな微粒子状であり、溶解性に優れるうえスナック菓子などへの付着も良好で、様々な用途に適用できるものであった。   The obtained algal salt had no bitterness or metallic taste due to the bitter melon component and had a umami characteristic of kombu. As a result of analyzing the components contained in the algal salt, the calcium component was 0.0907% by weight, the potassium component was 1.52% by weight, and the magnesium component was 0.139% by weight. Moreover, the fine powdery algal salt is fine and finely particulate, has excellent solubility and adheres well to snacks and the like, and can be applied to various uses.

上記の実施形態では、精製塩100重量部に対し20重量部のコンブを用いて藻塩を製造した。しかし本発明では、精製塩100重量部に対し例えば60重量部のコンブを用いることもでき、この場合、上記と同様に処理して得られた藻塩の成分は、カルシウム成分が0.131重量%、カリウム成分が4.006重量%、マグネシウム成分が0.218重量%であった。   In said embodiment, algal salt was manufactured using 20 weight part kombu with respect to 100 weight part of refined salt. However, in the present invention, for example, 60 parts by weight of the kombu can be used with respect to 100 parts by weight of the purified salt. In this case, the component of the algal salt obtained by the same treatment as described above has a calcium component of 0.131% by weight. The potassium component was 4.006% by weight and the magnesium component was 0.218% by weight.

図2は本発明の第2実施形態を示す、藻塩の製造方法のフロー図である。
上記の第1実施形態では、ミネラル回収工程で回収したミネラル溶解液を、その製造サイクルの混合工程で海藻エキス抽出塩水に混合した。しかし、本発明では上記のミネラル溶解液を、後の製造サイクルにおいて海藻エキス抽出塩水と混合してもよい。
即ち、この第2実施形態では、図2に示すように、分離工程(2)で得られた海藻エキス抽出塩水には、前の製造サイクルのミネラル回収工程(3)で回収されたミネラル溶解液が混合工程(4)で混合され、一方、この製造サイクルのミネラル回収工程(3)で回収されたミネラル溶解液は、次の製造サイクルの混合工程(4)で海藻エキス抽出塩水に混合される。その他の構成は上記の第1実施形態と同様であり、同様に処理されるので説明を省略する。
FIG. 2 is a flowchart of a method for producing algal salt, showing a second embodiment of the present invention.
In said 1st Embodiment, the mineral solution collect | recovered at the mineral collection | recovery process was mixed with the seaweed extract extraction salt water at the mixing process of the manufacturing cycle. However, in the present invention, the above-described mineral solution may be mixed with seaweed extract-extracted brine in a subsequent production cycle.
That is, in the second embodiment, as shown in FIG. 2, the seaweed extract-extracted salt water obtained in the separation step (2) contains the mineral solution recovered in the mineral recovery step (3) of the previous manufacturing cycle. Is mixed in the mixing step (4), while the mineral solution recovered in the mineral recovery step (3) of this manufacturing cycle is mixed with the seaweed extract extracted brine in the mixing step (4) of the next manufacturing cycle. . Other configurations are the same as those in the first embodiment described above, and are processed in the same manner, and thus the description thereof is omitted.

この第2実施形態では、分離工程(2)で分離された海藻エキス抽出塩水を、ミネラル回収工程(3)が終了するまで放置する必要がないことから、各製造サイクル全体の時間を短縮することができ、製造効率を高めることができる。   In this second embodiment, it is not necessary to leave the seaweed extract-extracted salt water separated in the separation step (2) until the mineral recovery step (3) is completed, so that the time of each production cycle can be shortened. Manufacturing efficiency can be increased.

図3は本発明の第3実施形態を示す、藻塩の製造方法のフロー図である。
この第3実施形態では、図3に示すように、前の製造サイクルのミネラル回収工程(3)で回収されたミネラル溶解液が抽出工程(1)で塩水に混合され、一方、この製造サイクルのミネラル回収工程(3)で回収されたミネラル溶解液は、次の製造サイクルの抽出工程(1)で塩水に混合される。このため、分離工程(2)で得られた海藻エキス抽出塩水は、そのまま直ちに乾燥準備工程(5)で処理される。その他の構成は上記の第2実施形態と同様であり、同様に処理されるので説明を省略する。
FIG. 3 is a flowchart of a method for producing algal salt, showing a third embodiment of the present invention.
In this third embodiment, as shown in FIG. 3, the mineral solution recovered in the mineral recovery step (3) of the previous manufacturing cycle is mixed with salt water in the extraction step (1). The mineral solution recovered in the mineral recovery step (3) is mixed with salt water in the extraction step (1) of the next production cycle. For this reason, the seaweed extract-extracted brine obtained in the separation step (2) is immediately treated in the drying preparation step (5) as it is. Other configurations are the same as those in the second embodiment and are processed in the same manner, and thus the description thereof is omitted.

この第3実施形態では、ミネラル溶解液が抽出工程(1)で塩水に混合されることから、分離工程(2)でミネラル等の海藻エキスの一部が抽出残渣に吸着され、塩水に取り込まれる海藻エキス量が減少する惧れがある。しかし、分離工程(2)で分離された海藻エキス抽出塩水が、そのまま直ちに乾燥準備工程(5)で処理されるので、前記の第1実施形態と異なり、ミネラル回収工程(3)が終了するまで海藻エキス抽出塩水を放置する必要がないうえ、混合工程(4)を省略できることから、各製造サイクル全体の時間を一層短縮することができる。   In this 3rd Embodiment, since a mineral solution is mixed with salt water by an extraction process (1), a part of seaweed extracts, such as a mineral, are adsorbed | sucked to an extraction residue at a separation process (2), and are taken in into salt water. There is a possibility that the amount of seaweed extract will decrease. However, since the seaweed extract-extracted salt water separated in the separation step (2) is immediately processed as it is in the drying preparation step (5), unlike the first embodiment, until the mineral recovery step (3) is completed. Since it is not necessary to leave the seaweed extract-extracted salt water and the mixing step (4) can be omitted, the time of each production cycle can be further shortened.

図4は本発明の第4実施形態を示す、藻塩の製造方法のフロー図である。
図4に示すように、この第4実施形態では、前記の第1実施形態の藻塩の製造方法と同様の工程において、分離工程(2)で分離した海藻エキス抽出塩水に、追加抽出工程(11)と分離工程(2)とをさらに2回ずつ繰り返して施したものである。
FIG. 4 is a flowchart of a method for producing algal salt, showing a fourth embodiment of the present invention.
As shown in FIG. 4, in the fourth embodiment, in the same process as the algal salt production method of the first embodiment, the seaweed extract-extracted salt water separated in the separation process (2) is added to the additional extraction process (11 ) And the separation step (2) are repeated twice more.

上記の追加抽出工程(11)では、前記の分離工程(2)で分離した海藻エキス抽出塩水に、新しい海藻が投入されて所定時間浸漬され、これにより、海藻混合液に含まれる海藻エキスの濃度が大幅に高められる。なお、この実施形態では追加抽出工程を2回施したが、本発明においてこの追加抽出工程を施す場合、回数は1回でもよく3回以上でもよい。   In the additional extraction step (11), fresh seaweed is introduced into the seaweed extract-extracted salt water separated in the separation step (2) and immersed for a predetermined time, whereby the concentration of seaweed extract contained in the seaweed mixture is increased. Is greatly increased. In this embodiment, the additional extraction step is performed twice. However, when this additional extraction step is performed in the present invention, the number of times may be one or three or more.

上記の各分離工程(2)で分離された抽出残渣は、それぞれ個別に水で洗浄されたのち、上記のミネラル回収工程(3)でまとめて焼却して炭化される。また、上記の洗浄処理により得られた洗浄液は、各分離工程(2)で分離された海藻エキス抽出塩水にそれぞれ加えられる。
ただし、本発明では上記の抽出残渣は、各分離工程(2)の後にそれぞれ個別にミネラル回収工程を施してもよく、また、上記の洗浄処理を省略したり、上記の洗浄液をまとめて最後の分離工程(2)で得られた海藻エキス抽出塩水に加えてもよい。
The extraction residue separated in each of the separation steps (2) is individually washed with water and then incinerated and carbonized in the mineral recovery step (3). Moreover, the washing | cleaning liquid obtained by said washing | cleaning process is added to the seaweed extract extraction salt water isolate | separated at each isolation | separation process (2), respectively.
However, in the present invention, the extraction residue may be subjected to a mineral recovery step after each separation step (2), or the washing treatment may be omitted or the washing solution may be collected at the end. You may add to the seaweed extract extraction salt water obtained at the isolation | separation process (2).

次に、海藻としてコンブを用いた場合を例にとり、図4に基づいてこの第4実施形態の各製造工程を説明する。
最初に、抽出工程(1)で、精製塩1kgを水3kgに溶解して、塩分濃度25重量%の塩水を調製し、この塩水を85℃に加温した状態でコンブ350gを投入し、30分間浸漬した。
Next, taking the case where a kombu is used as seaweed as an example, each manufacturing process of the fourth embodiment will be described based on FIG.
First, in the extraction step (1), 1 kg of purified salt is dissolved in 3 kg of water to prepare a salt water with a salt concentration of 25% by weight, and 350 g of kombu is added while the salt water is heated to 85 ° C. Immerse for a minute.

次に、上記のコンブが浸漬された塩水を、前記の第1実施形態と同様、分離工程(2)で海藻エキス抽出塩水と抽出残渣とに分離し、この抽出残渣に脱水処理と水による洗浄処理とを施した。この洗浄処理で得られた洗浄液は、上記の海藻エキス抽出塩水に加えて混合した。   Next, the salt water in which the above-mentioned kombu is immersed is separated into seaweed extract-extracted salt water and an extraction residue in the separation step (2) as in the first embodiment, and the extraction residue is dehydrated and washed with water. And processed. The washing liquid obtained by this washing treatment was added to the seaweed extract extracted brine and mixed.

次に、上記の海藻エキス抽出塩水を追加抽出工程(11)で、上記の抽出工程(1)と同様、85℃に加温した状態でコンブ350gを投入し、30分間浸漬し、その後、上記と同様の分離工程(2)を施した。そして、この追加抽出工程(11)と分離工程(2)とをさらにもう一度繰り返し施した。
なお、上記の抽出工程(1)と2回の追加抽出工程(11)で使用されたコンブは、いずれも前記の第1実施形態で用いたコンブと同様、所定寸法にカットしたものを用いた。
Next, the seaweed extract-extracted salt water is added in the additional extraction step (11), in the same manner as in the extraction step (1), 350 g of the kombu is put in a state heated to 85 ° C., and immersed for 30 minutes. The same separation step (2) was performed. Then, this additional extraction step (11) and separation step (2) were repeated once more.
Note that the combs used in the extraction process (1) and the two additional extraction processes (11) were both cut into a predetermined size, similar to the comb used in the first embodiment. .

上記の3回の分離工程(2)で分離された抽出残渣は、ミネラル回収工程(3)で一括して焼却した。そして、得られた藻灰570gに水1.7kgを加えて溶解させ、濾過してミネラル溶解液1.47kgを得た。このミネラル溶解液を混合工程(4)で、上記の最後の分離工程(2)により得られた海藻エキス抽出塩水3.47kgに混合した。その後、この混合液に、前記の第1実施形態と同様の、乾燥準備工程(5)と乾燥工程(6)と仕上工程(7)とを施し、微粉末状の藻塩997gを得た。
得られた藻塩に含まれるミネラル成分は、カルシウム成分が0.215重量%、カリウム成分が7.35重量%、マグネシウム成分が0.347重量%であった。
The extraction residue separated in the above three separation steps (2) was incinerated at once in the mineral recovery step (3). Then, 1.7 kg of water was added to 570 g of the obtained algal ash and dissolved, followed by filtration to obtain 1.47 kg of a mineral solution. In the mixing step (4), this mineral solution was mixed with 3.47 kg of the seaweed extract-extracted brine obtained in the last separation step (2). Thereafter, the mixed preparation was subjected to the drying preparation step (5), the drying step (6), and the finishing step (7) as in the first embodiment to obtain 997 g of a fine powdery algal salt.
The mineral component contained in the obtained algal salt was 0.215% by weight of the calcium component, 7.35% by weight of the potassium component, and 0.347% by weight of the magnesium component.

上記の第4実施形態では、前記の第1実施形態に追加抽出工程を加えた。しかし本発明ではこの追加抽出工程を、前記の第2実施形態や第3実施形態に加えてもよい。   In said 4th Embodiment, the additional extraction process was added to said 1st Embodiment. However, in the present invention, this additional extraction step may be added to the second and third embodiments.

本発明により得られる藻塩は、海藻に含まれる成分を取り込み、ミネラルバランスが良く品質が安定しているので、食卓塩のほか、各種の食品に添加される食塩や、他の調味料と混合した複合調味料に用いられる食塩としての用途に好適である。   Algae salt obtained by the present invention incorporates components contained in seaweed and has a good mineral balance and stable quality, so it is mixed with table salt, salt added to various foods, and other seasonings. It is suitable for use as a salt used in a complex seasoning.

本発明の第1実施形態を示す、藻塩の製造方法のフロー図である。It is a flowchart of the manufacturing method of algal salt which shows 1st Embodiment of this invention. 本発明の第2実施形態を示す、藻塩の製造方法のフロー図である。It is a flowchart of the manufacturing method of algal salt which shows 2nd Embodiment of this invention. 本発明の第3実施形態を示す、藻塩の製造方法のフロー図である。It is a flowchart of the manufacturing method of algal salt which shows 3rd Embodiment of this invention. 本発明の第4実施形態を示す、藻塩の製造方法のフロー図である。It is a flowchart of the manufacturing method of algal salt which shows 4th Embodiment of this invention.

符号の説明Explanation of symbols

1…抽出工程
2…分離工程
3…ミネラル回収工程
4…混合工程
5…乾燥準備工程
6…乾燥工程
7…仕上工程
11…追加抽出工程

DESCRIPTION OF SYMBOLS 1 ... Extraction process 2 ... Separation process 3 ... Mineral recovery process 4 ... Mixing process 5 ... Drying preparation process 6 ... Drying process 7 ... Finishing process
11 ... Additional extraction process

Claims (8)

精製塩100重量部を水に溶解して所定濃度に調製した塩水へ5〜60重量部の海藻を投入し、所定時間浸漬する抽出工程(1)と、
上記の浸漬後の海藻混合液を濾過して海藻エキス抽出塩水と抽出残渣とに分離する分離工程(2)と、
上記の抽出残渣を焼却して炭化させ、得られた藻灰に水を加えてこの藻灰に含まれるミネラルを溶解したのち、不溶解物を除去してミネラル溶解液を得るミネラル回収工程(3)と、
上記のミネラル溶解液を、前記の分離工程(2)で得た海藻エキス抽出塩水に混合する混合工程(4)と、
上記の混合工程(4)で得られた混合液から水分を蒸発させて固形分を回収する乾燥工程(6)と、
を備えることを特徴とする、藻塩の製造方法。
An extraction step (1) in which 5 to 60 parts by weight of seaweed is poured into salt water prepared by dissolving 100 parts by weight of purified salt in water and adjusted to a predetermined concentration;
A separation step (2) in which the seaweed mixture after the immersion is filtered and separated into a seaweed extract-extracted brine and an extraction residue;
The extraction residue is incinerated and carbonized, water is added to the obtained algal ash to dissolve minerals contained in the algal ash, and then the insoluble matter is removed to obtain a mineral solution (3) )When,
A mixing step (4) in which the mineral solution is mixed with the seaweed extract-extracted brine obtained in the separation step (2);
A drying step (6) for recovering solids by evaporating water from the mixed solution obtained in the mixing step (4);
A method for producing algal salt, comprising:
精製塩100重量部を水に溶解して所定濃度に調製した塩水へ5〜60重量部の海藻を投入し、所定時間浸漬する抽出工程(1)と、
上記の浸漬後の海藻混合液を濾過して海藻エキス抽出塩水と抽出残渣とに分離する分離工程(2)と、
上記の抽出残渣を焼却して炭化させ、得られた藻灰に水を加えてこの藻灰に含まれるミネラルを溶解したのち、不溶解物を除去してミネラル溶解液を得るミネラル回収工程(3)と、
上記の分離工程(2)で得られた海藻エキス抽出塩水から水分を蒸発させて固形分を回収する乾燥工程(6)と、を備え、
前の製造サイクルのミネラル回収工程(3)で回収されたミネラル溶解液を、上記の抽出工程(1)で塩水に混合することを特徴とする、藻塩の製造方法。
An extraction step (1) in which 5 to 60 parts by weight of seaweed is poured into salt water prepared by dissolving 100 parts by weight of purified salt in water and adjusted to a predetermined concentration;
A separation step (2) in which the seaweed mixture after the immersion is filtered and separated into a seaweed extract-extracted brine and an extraction residue;
The extraction residue is incinerated and carbonized, water is added to the obtained algal ash to dissolve minerals contained in the algal ash, and then the insoluble matter is removed to obtain a mineral solution (3) )When,
A drying step (6) for evaporating water from the seaweed extract-extracted salt water obtained in the separation step (2) to recover a solid content,
A method for producing algal salt, wherein the mineral solution recovered in the mineral recovery step (3) of the previous manufacturing cycle is mixed with salt water in the extraction step (1).
上記の抽出工程(1)において、上記の塩水中の精製塩の濃度が15〜35重量%である、請求項1または請求項2に記載の藻塩の製造方法。   The method for producing algal salt according to claim 1 or 2, wherein in the extraction step (1), the concentration of the purified salt in the brine is 15 to 35% by weight. 上記の抽出工程(1)で塩水に投入する海藻として、100mm以下の寸法に裁断したものを用いる、請求項1から3のいずれか1項に記載の藻塩の製造方法。   The method for producing algal salt according to any one of claims 1 to 3, wherein the seaweed introduced into the salt water in the extraction step (1) is cut into a size of 100 mm or less. 上記の分離工程(2)において、140〜250メッシュの濾材を用いて海藻エキス抽出塩水と抽出残渣とに分離する、請求項1から4のいずれか1項に記載の藻塩の製造方法。   The method for producing algae salt according to any one of claims 1 to 4, wherein in the separation step (2), a seaweed extract-extracted salt water and an extraction residue are separated using a 140 to 250 mesh filter medium. 上記の分離工程(2)で分離した海藻エキス抽出塩水に、新しい海藻を投入して所定時間浸漬する、1または複数の追加抽出工程(11)をさらに備え、
この追加抽出工程(11)による浸漬後の海藻混合液に、前記の分離工程(2)を再度施す、請求項1から5のいずれか1項に記載の藻塩の製造方法。
One or more additional extraction steps (11) in which fresh seaweed is introduced into the seaweed extract extracted brine separated in the separation step (2) and immersed for a predetermined time, are further provided.
The method for producing algal salt according to any one of claims 1 to 5, wherein the separation step (2) is performed again on the seaweed mixed solution after immersion in the additional extraction step (11).
上記の追加抽出工程(11)で塩水に投入する海藻として、100mm以下の寸法に裁断したものを用いる、請求項6に記載の藻塩の製造方法。   The method for producing algal salt according to claim 6, wherein the seaweed introduced into the salt water in the additional extraction step (11) is cut into a size of 100 mm or less. 上記の乾燥工程(6)に先立って被乾燥液を撹拌装置で均一化しておき、この均一化した被乾燥液を乾燥工程(6)でスプレードライ法により乾燥して粉末状の固形分を回収する、請求項1から7のいずれか1項に記載の藻塩の製造方法。 Prior to the drying step (6), the liquid to be dried is homogenized with a stirrer, and the uniform liquid to be dried is dried by a spray drying method in the drying step (6) to collect a powdery solid. to manufacture how the Moshio according to any one of claims 1 to 7.
JP2003292796A 2002-10-01 2003-08-13 Method for producing algal salt Expired - Fee Related JP4131689B2 (en)

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Publication number Priority date Publication date Assignee Title
CN104939023A (en) * 2015-07-10 2015-09-30 中盐榆林盐化有限公司 Preparation method of rich-magnesium salt

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JP5062728B2 (en) * 2006-12-25 2012-10-31 室戸海洋深層水株式会社 Seawater treatment method and mineral water obtained by the seawater treatment method
JP5503506B2 (en) * 2010-11-16 2014-05-28 幸雄 武村 Method for producing seaweed extract
BR112017025439A2 (en) * 2015-05-27 2018-08-07 Douxmatok Ltd intensified salt compositions and methods of preparing same

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104939023A (en) * 2015-07-10 2015-09-30 中盐榆林盐化有限公司 Preparation method of rich-magnesium salt

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