JPH05192666A - Production of high-concentration mineral liquid - Google Patents

Production of high-concentration mineral liquid

Info

Publication number
JPH05192666A
JPH05192666A JP947292A JP947292A JPH05192666A JP H05192666 A JPH05192666 A JP H05192666A JP 947292 A JP947292 A JP 947292A JP 947292 A JP947292 A JP 947292A JP H05192666 A JPH05192666 A JP H05192666A
Authority
JP
Japan
Prior art keywords
producing
mineral liquid
liquid according
days
concentration mineral
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
JP947292A
Other languages
Japanese (ja)
Other versions
JPH074594B2 (en
Inventor
Yuji Tsuchida
優二 土田
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.)
HEALTH KOSAN KK
Original Assignee
HEALTH KOSAN 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 HEALTH KOSAN KK filed Critical HEALTH KOSAN KK
Priority to JP947292A priority Critical patent/JPH074594B2/en
Publication of JPH05192666A publication Critical patent/JPH05192666A/en
Publication of JPH074594B2 publication Critical patent/JPH074594B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Abstract

PURPOSE:To enable the production of the high-concn. mineral liquid by adding concd. sulfuric acid, ethyl alcohol and water to a mixture composed of coal, bringing the mixture into reaction, effecting the maturation of 1st, 2nd and 3rd maturation periods, heating and sterilizing the supernatant liquid and adding the ethyl alcohol thereto. CONSTITUTION:The concd. sulfuric acid is added at 0.5 to 5%, the ethyl alcohol at 1 to 3% and the water at 8 to 15% to the mixture composed of 10 to 90% humus and the balance the coal of a low rank of coalification, such as peat. This mixture is heated to 60 to 90 deg.C and is agitated to effect the reaction. The mixture is then rested for the 1st maturation period of 4 to 10 days to cause fermentation and maturation. The water of 30 to 100 times weight is thereafter added to the mixture and while the mixture is aerated, the mixture is matured for the 2nd maturation period of 7 to 15 days. Further, the solids are filtered and the resultant filtrate is rested for the 3rd maturation period of 5 to 10 days to effect precipitation and maturation; thereafter, the supernatant liquid thereof is drawn and is subjected to precision filtration then to sterilization by heating. Finally, the ethyl alcohol is added at 0.1 to 1% by weight to the filtrate.

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、高濃度ミネラル液製造
方法に関する。
FIELD OF THE INVENTION The present invention relates to a method for producing a high-concentration mineral liquid.

【0002】[0002]

【従来の技術】従来、ミネラル含有水としては、ミネラ
ルを豊富に含有する天然水が使用されていた。又、特殊
な岩石からミネラルを抽出して使用する技術も公知であ
る。然しながら、これら公知の方法で得られるミネラル
水は、飲用水としては有効量のミネラルを含むとして
も、ミネラルの含有量が低く、又、有効な有機質を含ま
ないので、飲用水以外の用途に供されることがなかっ
た。
2. Description of the Related Art Conventionally, natural water rich in minerals has been used as mineral-containing water. Further, a technique of extracting and using minerals from a special rock is also known. However, the mineral water obtained by these known methods has a low content of minerals even if it contains an effective amount of minerals as drinking water and does not contain effective organic matter, so it is used for applications other than drinking water. It was never done.

【0003】カルシウム、ナトリウム、マグネシウム、
カリウム、亜鉛、鉄、マンガン等のミネラルの外、アミ
ノ酸、フミン酸、ビタミン類、糖類等の有機質を含み、
希釈して飲用でき、土壌改良剤、食品用水添加剤、殺菌
防臭剤、水質保全剤などとして広く利用できる高濃度ミ
ネラル液を製造する方法は知られていない。
Calcium, sodium, magnesium,
In addition to minerals such as potassium, zinc, iron and manganese, it contains organic substances such as amino acids, humic acid, vitamins and sugars.
There is no known method for producing a high-concentration mineral liquid that can be diluted and drunk and widely used as a soil conditioner, a water additive for foods, a germicidal deodorant, a water quality preservation agent, and the like.

【0004】[0004]

【発明が解決しようとする課題】本発明の目的とすると
ころは、叙上の高濃度ミネラル液製造方法を提供するこ
とにある。
SUMMARY OF THE INVENTION An object of the present invention is to provide a method for producing a high concentration mineral liquid as described above.

【0005】[0005]

【課題を解決するための手段】上述の課題は、10%以
上90%以下の腐植土と残部が泥炭など石炭化度の低い
石炭から成る混合物に、0.5%以上5%以下の濃硫
酸、1%以上3%以下のエチルアルコール及び8%以上
15%以下の水を添加し、60°C以上90°C以下の
温度に加熱、攪拌し反応を行わせ、次いで、これを4日
以上10日以下の第一熟成期間放置して醗酵、熟成させ
た後、これに重量で30倍以上100倍以下の水を加
え、曝気しながら、7日以上15日以下の第二熟成期間
熟成させ、更に、固形物を濾過して得た濾液を5日以上
10日以下の第三熟成期間放置して沈澱及び熟成を行わ
せた後、その上澄液を採取し、精密濾過した後、加熱殺
菌し、、最後に重量比で0.1%以上1%%以下のエチ
ルアルコールを添加することにより達成される。
[Means for Solving the Problems] The above-mentioned problems are caused by adding 0.5% or more and 5% or less concentrated sulfuric acid to a mixture of 10% or more and 90% or less humus and the balance of coal having a low degree of coalification such as peat. Add 1% or more and 3% or less of ethyl alcohol and 8% or more and 15% or less of water, heat to a temperature of 60 ° C or more and 90 ° C or less to stir the reaction, and then allow it to react for 4 days or more. After fermentation and aging for 10 days or less in the first aging period, add 30 times or more and 100 times or less by weight of water to this, and aerate for a second aging period of 7 days or more and 15 days or less. Furthermore, the filtrate obtained by filtering the solid matter is left to stand for a third aging period of 5 days or more and 10 days or less for precipitation and aging, and the supernatant is collected, microfiltered, and heated. Sterilize, and finally add 0.1% or more and 1% or less by weight of ethyl alcohol. It is achieved by

【0006】[0006]

【実施例】以下、実施例により本発明方法について説明
する。 〔実施例1〕腐植土50Kgと粉砕した泥炭50Kgを
混合し、これに96%濃硫酸1Kg、エチルアルコール
1Kg及び塩素等の有害不純物を含まない水10リット
ルを添加し、80°Cで2時間攪拌し、これをタンクに
密封して、5日間放置し(第一熟成期間)、醗酵及び熟
成をさせた。この第一熟成期間終了後、タンクの弁を開
き水5キロリットルを注入し、攪拌し、曝気しながら1
0日間(第二熟成期間)熟成させた。この第二熟成期間
に二価鉄を含むゲル状物質が液面に浮上するので、これ
を他の固形物と共に濾過し、濾液を得、この濾液を更に
10日間(最終熟成期間)タンク内に静置して沈澱及び
熟成を行わせた。最終熟成期間終了後、タンク内の上澄
液を1ミクロンフィルターで濾過精製し、これに活性剤
としてエチルアルコール1%を添加して清澄な高濃度ミ
ネラル液を得た。
EXAMPLES The method of the present invention will be described below with reference to examples. [Example 1] 50 kg of humus soil and 50 kg of crushed peat were mixed, and to this was added 1 kg of 96% concentrated sulfuric acid, 1 kg of ethyl alcohol and 10 liters of water containing no harmful impurities such as chlorine, and the mixture was kept at 80 ° C for 2 hours. The mixture was stirred, sealed in a tank, and allowed to stand for 5 days (first aging period) for fermentation and aging. After the first aging period, open the valve of the tank and inject 5 kiloliters of water, stir and aerate 1
It was aged for 0 days (second aging period). During this second aging period, a gel-like substance containing ferric iron floats on the liquid surface, so this is filtered together with other solid matter to obtain a filtrate, and this filtrate is further stored in a tank for 10 days (final aging period). It was left to stand for precipitation and aging. After the completion of the final ripening period, the supernatant in the tank was filtered and purified with a 1-micron filter, and 1% of ethyl alcohol was added as an activator to this to obtain a clear high-concentration mineral liquid.

【0007】この高濃度ミネラル液の性質及び成分は次
の通りであった。
The properties and components of this highly concentrated mineral liquid were as follows.

【表1】 [Table 1]

【表2】 [Table 2]

【表3】 [Table 3]

【表4】 [Table 4]

【0008】上記には示されていないが、この高濃度ミ
ネラル液は6.5%のフミン酸を含有する。この高濃度
ミネラル液は上表に示した分析値から知られるように、
各種の有用なミネラル成分を含み、然も有害な物質を含
まないので、例えばこれを1000倍に希釈して清涼飲
料水としたり、又食品製造用水としたりすることができ
る。又、このような希釈水は、強い殺菌作用があること
が証明されている。表5には、上記の1000倍希釈水
と滅菌精製水に表5に示した試験菌を添加し、4時間放
置後の残存細菌数を対比して示してある。
Although not shown above, this highly concentrated mineral fluid contains 6.5% humic acid. This high-concentration mineral liquid, as known from the analysis values shown in the table above,
Since it contains various useful mineral components and does not contain harmful substances, it can be diluted 1000 times to prepare soft drinks or food manufacturing water. Further, such dilution water has been proved to have a strong bactericidal action. Table 5 shows the number of remaining bacteria after the test bacteria shown in Table 5 were added to the 1000-fold diluted water and the sterilized purified water, and left standing for 4 hours.

【0009】[0009]

【表5】 [Table 5]

【0010】このときの試験方法は次の通りである。 (1)試験者 財団法人日本食品センター (2)試験菌種 大腸菌 :Escherichia coil IFO 3301 緑膿菌 :Pseudomonas aerug
inosa IFO 13275 黄色ブドウ球菌:Staphylococcus au
reus IFO 12732 腸炎ビブリオ ;Vibrio parahaemol
yticus IFO 12711
The test method at this time is as follows. (1) Tester Japan Food Center (2) Test strain Escherichia coli: Escherichia coil IFO 3301 Pseudomonas aeruginosa: Pseudomonas aerug
Inosa IFO 13275 Staphylococcus aureus: Staphylococcus au
reus IFO 12732 Vibrio parahaemolyticus; Vibrio parahaemol
yticus IFO 12711

【0011】(3)菌液の調製 普通ブイヨン培地(但し、腸炎ビブリオについては3%
食塩添加普通プイヨン培地)で35°C、16〜29時
間震盪培養した試験菌の培養液を、滅菌生理食塩水で1
ミリリットル当たりの菌数が厄10,000,000個
となるように希釈し、菌液とした。
(3) Preparation of bacterial solution Ordinary broth medium (3% for Vibrio parahaemolyticus)
A culture solution of a test bacterium, which had been shake-cultured at 35 ° C for 16 to 29 hours in a normal broth medium containing salt, was sterilized with saline for 1 hour.
The bacterial solution was diluted so that the number of bacteria per milliliter became a troublesome 10,000,000.

【0012】(4)菌数測定用培地 腸炎ビブリオ以外の試験菌:SCDLP寒天培養地(日
本製薬) 腸炎ビブリオ :3%食塩添加SCDLP寒天培
養地(日本製薬)(5)試験操作 メンブランフィルター(0.45ミクロン)にて除菌後の
試供品10ミリリットルに菌液1ミリリットルを加えて
混合した後、4時間後に試供品中の生菌数を菌数測定用
培地を用いた混釈平板培養法(35°C、2日間培養)
により測定した。また、対照として滅菌精製水または滅
菌3%食塩水について同様に試験した。 (4)試供品 実施例1で得た高濃度ミネラル液を水で1000倍に希
釈し、試供品とした。
(4) Medium for measuring the number of bacteria Test bacteria other than Vibrio parahaemolyticus: SCDLP agar culture medium (Nippon Pharmaceutical Co., Ltd.) Vibrio parahaemolyticus: SCDLP agar culture medium with 3% sodium chloride (Nippon Pharmaceutical Co., Ltd.) (5) Test operation Membrane filter (0) (0.45 micron) 1 ml of the bacterial solution was added to 10 ml of the sample after sterilization, and after 4 hours, the pour plate culture method using the culture medium for measuring the viable cell count in the sample was performed. (35 ° C, 2 days culture)
It was measured by. As a control, sterilized purified water or sterilized 3% saline was similarly tested. (4) Free sample The highly concentrated mineral liquid obtained in Example 1 was diluted 1000 times with water to give a free sample.

【0013】このように、本発明方法により製造された
高濃度ミネラル液は、強力な滅菌作用があるので、これ
を希釈して清涼飲料水や食品製造用水として使用しても
極めて安全であり、又、動植物の成長に有用な各種のミ
ネラル及び有用な有機物を含むので、これを畑や、植木
鉢などの土壌に施せば、土壌中の有用生物の繁殖を増進
するので、顕著な土壌の性質が顕著に改良される効果が
ある。この土壌改良効果は、この高濃度ミネラル液に含
まれるアミノ酸、ビタミン類、フミン酸などの所謂土壌
有機とミネラルの相乗効果によるもので、これらはそれ
自体生物の栄養素である上、互いに結合して金属を含む
金属酵素として土壌微生物などの生理機能を高める効果
がある。
As described above, since the high-concentration mineral liquid produced by the method of the present invention has a strong sterilizing action, it is extremely safe to dilute it and use it as soft drink water or water for food production. Also, since it contains various minerals and useful organic substances that are useful for the growth of plants and animals, applying this to soil such as fields and flowerpots promotes the reproduction of useful organisms in the soil, so that the outstanding soil properties are There is a remarkable improvement effect. This soil improvement effect is due to the synergistic effect of so-called soil organic matter and minerals such as amino acids, vitamins, humic acid, etc. contained in this high-concentration mineral liquid. As a metal enzyme containing metal, it has an effect of enhancing physiological functions such as soil microorganisms.

【0014】同様の理由により、この高濃度ミネラル液
を養魚池、水槽、生簀などに使用すると、有害な細菌の
増殖を制限し、余った餌や魚の排泄物を食べるプランク
トンや微小生物の繁殖を促すので、養魚場の水質が良好
な水準に保持され、このため海水の汚染が防止されるの
みでなく、養殖魚そのものにもミネラル及び有用な有機
物が供給されるようになるので、養殖の効率が高められ
るものである。
For the same reason, when this high-concentration mineral liquid is used in a fish pond, an aquarium, a cage, etc., the growth of harmful bacteria is restricted, and the proliferation of plankton and microscopic organisms that eat excess food and fish excrement. As a result, the quality of water in the fish farm is maintained at a good level, which not only prevents pollution of seawater but also supplies minerals and useful organic substances to the cultured fish itself. Is enhanced.

【0015】又更に、本発明方法により製造された高濃
度ミネラル液は、公知のミネラル抽出液と同等以上の消
臭作用を有し、家庭から排出される生ごみなどに振り掛
けて使用することが推奨される。
Furthermore, the high-concentration mineral liquid produced by the method of the present invention has a deodorizing action equal to or higher than that of a known mineral extraction liquid, and it can be sprinkled and used on food waste discharged from home. Recommended.

【0016】尚、本発明方法は、叙上の実施例に限定さ
れるものでなく、多くの変更例を包含するものである。
以下、幾つかの変更例に就いて述べる。例えば、原料と
して使用する石炭は、石炭化度が低くミネラル及び有機
質を多く含むものであれば、泥炭に限らず、褐炭、亜炭
なども使用でき、又、腐植土との混合比も、原料炭の成
分にもよるが、10%以上90%以下の範囲で自由に変
更できるものである。
It should be noted that the method of the present invention is not limited to the above-mentioned embodiments, but includes many modifications.
Hereinafter, some modified examples will be described. For example, the coal used as a raw material is not limited to peat, as long as it has a low degree of coalification and contains a large amount of minerals and organic matter, lignite, lignite, etc. can also be used, and the mixing ratio with humus is It can be freely changed within the range of 10% or more and 90% or less, depending on the component.

【0017】腐植土としては、成分等に特別な制約はな
く、人工の培養土などでも良いが、一般的には、寒冷地
で湿潤な針葉樹林地帯で天然に産するものが望ましい。
而して、この原料炭と腐植土の組成にもよるが、それら
のうち何れか一方の配合比を10%以下とすると、抽出
されるミネラル及び/又は有機質の量が偏ったり、不十
分となったりする。この原料炭と腐植土の配合比は50
%宛とすることが望ましい。
The humus soil is not particularly limited in its components and the like, and artificial culture soil or the like may be used, but generally, humus soil naturally produced in a coniferous forest area which is humid in a cold region is preferable.
Thus, depending on the composition of the raw coal and the humus, if the mixing ratio of any one of them is 10% or less, the amount of extracted minerals and / or organic matter may be unbalanced or insufficient. To become. The mixing ratio of this raw coal and humus is 50
It is desirable to address to.

【0018】濃硫酸の添加量が0.5%以下となると、
有効成分の抽出率が著しく低下するが、逆にこの添加量
を5%以上とすると、製品のPHが低くなり過ぎる上、
装置の腐植が著しくなるので、添加量は0.5%以上5
%以下とする。なおこの硫酸添加量は、製品のPHが3
ないし3.8となるように調節することが望ましい。腐
植土や原料炭の酸性度にもよるが、通常この添加量は1
%前後である。
When the amount of concentrated sulfuric acid added becomes 0.5% or less,
Although the extraction rate of the active ingredient is remarkably reduced, if the addition amount is 5% or more, the pH of the product becomes too low and
Since the humus of the equipment becomes significant, the addition amount should be 0.5% or more 5
% Or less. The amount of sulfuric acid added is 3 when the PH of the product is 3
It is desirable to adjust the value so that it is from 3.8 to 3.8. Depending on the acidity of humus and coking coal, this amount is usually 1
It is around%.

【0019】エチルアルコールの添加量を、1%以下と
すると有効成分の抽出率が著しく低下するが、これを3
%以上としても抽出率が向上しないので、3%以上の添
加は無益である。望ましいアルコール添加量は、通常2
%前後である。水の添加量についても同様で、これを8
%以下又は15%以上とすると、第一熟成期間中に十分
な熟成が出来なくなり、抽出率が減退する。水の添加量
は通常10%前後とすることが推奨される。
When the amount of ethyl alcohol added is 1% or less, the extraction rate of the active ingredient is remarkably lowered.
Even if it is more than 3%, the extraction rate does not improve, so the addition of more than 3% is useless. The desirable amount of alcohol is usually 2
It is around%. The same applies to the amount of water added.
If it is less than 15% or more than 15%, sufficient aging cannot be performed during the first aging period and the extraction rate decreases. It is generally recommended that the amount of water added be around 10%.

【0020】而してこれらの原料を混合するに当たって
は、60°C以上、90°C以下の温度、望ましくは8
0°Cで約2時間攪拌することが推奨される。この温度
が60°C以下であると十分な抽出ができなくなり、逆
に90°C以上とすると有効成分が失われる。
When mixing these raw materials, the temperature is not lower than 60 ° C and not higher than 90 ° C, preferably 8 ° C.
It is recommended to stir at 0 ° C for about 2 hours. When the temperature is 60 ° C or lower, sufficient extraction cannot be performed, and when the temperature is 90 ° C or higher, the active ingredient is lost.

【0021】第一熟成期間は、抽出反応と、抽出成分の
熟成を行わせるものである。この期間を4日未満とする
と十分な熟成ができないが、10以上としても無益であ
る。通常、この第一熟成期間は5〜6日間とすることが
推奨される。第一熟成期間終了後の水の注入量が、熟成
生成物の重量の30倍以下であると有効成分を完全に抽
出できない。又、この水量が100倍以上となると、抽
出液が薄くなり過ぎて不都合を生じる。通常、推奨され
る水の注入量は50倍前後である。
The first aging period is for allowing the extraction reaction and the aging of the extracted components. If this period is less than 4 days, sufficient ripening cannot be achieved, but if it is 10 or more, it is useless. Usually, it is recommended that this first ripening period be 5 to 6 days. If the amount of water injected after the end of the first aging period is 30 times or less the weight of the aging product, the active ingredient cannot be completely extracted. If the amount of water is 100 times or more, the extract liquid becomes too thin, which causes a problem. Usually, the recommended water injection amount is around 50 times.

【0022】第二熟成期間は、曝気によりゲル状成分を
浮上分離させ、更に有効成分の抽出と熟成を行うもので
あり、少なくとも7日以上、望ましくは10日前後の期
間が必要である。但し、この期間を15日以上として無
益である。
In the second aging period, the gel-like component is floated and separated by aeration, and the active ingredient is further extracted and aged, and a period of at least 7 days or more, preferably about 10 days is required. However, this period is 15 days or more and is useless.

【0023】最終熟成期間は、主として固形成分の沈澱
を行わせるためのもので、この期間は最低5日、望まし
くは10日間とする。15日以上の熟成は無益である。
最終熟成期間終了後の濾過は、精密濾過器によることが
要求される。又、加熱殺菌は、ミネラル液の使用目的に
応じて適宜の方法が採用されるものであるが、飲料用な
どの場合、80°Cで30分加熱することが望ましい。
The final ripening period is mainly for the precipitation of the solid components, and this period is at least 5 days, preferably 10 days. Aging for more than 15 days is useless.
Filtration after the final ripening period is required to be performed by a microfilter. Further, the heat sterilization is carried out by adopting an appropriate method depending on the purpose of use of the mineral liquid, but in the case of beverage use, it is desirable to heat at 80 ° C. for 30 minutes.

【0024】製品にエチルアルコールを添加する目的
は、ミネラル水の活性を高めるためであり、最低0.1
%、望ましくは1%ヲ添加する。添加量が0.1%以下
では見るべき効果がなく、又、3%以上添加してもコス
トが嵩むのみで活性を高める効果が見られない。
The purpose of adding ethyl alcohol to the product is to enhance the activity of mineral water, and the minimum amount is 0.1.
%, Preferably 1%. If the addition amount is 0.1% or less, there is no effect to be observed, and even if it is added in an amount of 3% or more, the cost is increased and the effect of enhancing the activity is not observed.

【0025】[0025]

【発明の効果】本発明方法により得られる高濃度ミネラ
ル液は、叙上の如き成分を有するので、これを希釈して
清涼飲料水、ミネラルウォーターとして飲用に供するこ
とができ、これを長期に渡り飲用すれば健康の増進に有
益である。この高濃度ミネラル液は、食品製造用水とし
て利用でき、更に、養魚場、鑑賞魚用などの水槽、活魚
用の生簀、池水、ゴルフ場等の排水などの浄化、水質保
全に有効である。又、この高濃度ミネラル液は、土壌改
良作用を有し、更に消臭剤としても利用し得るものであ
る。
Since the high-concentration mineral liquid obtained by the method of the present invention has the above-mentioned components, it can be diluted and used as soft drink or mineral water for a long period of time. Drinking it is beneficial for improving health. This high-concentration mineral liquid can be used as water for food production, and is also effective for purification and water quality conservation of fish tanks, fish tanks for appreciation fish, cages for live fish, pond water, drainage water of golf courses, and the like. In addition, this high-concentration mineral liquid has a soil improving action and can be used as a deodorant.

Claims (14)

【特許請求の範囲】[Claims] 【請求項1】下記(1)ないし(8)の工程から成るこ
とを特徴とする高濃度ミネラル液製造方法。 (1)重量比(以下同様)で、10%以上90%以下の
腐植土と、残部が石炭化度の低い石炭から成る混合物を
原料とし、これに0.5%以上5%以下の濃硫酸、1%
以上3%以下のエチルアルコール及び8%以上15%以
下の水を添加し、60°C以上90°C以下の温度に加
熱、攪拌する工程。 (2)前工程により製造した原料を、4日以上10日以
下の期間(以下、第一熟成期間という)放置して醗酵、
熟成させる工程。 (3)第一熟成期間中熟成させた原料に、重量で30倍
以上100倍以下の水を加え、曝気しながら、7日以上
15日以下の期間(以下、第二熟成期間という)熟成さ
せる工程。 (4)第二熟成期間中熟成させた原料から固形物を濾過
し、濾液を採取する工程。 (5)前工程により採取した濾液を、5日以上15日以
下の期間(以下、第三熟成期間という)放置して沈澱及
び熟成させる工程。 (6)第三熟成期間中熟成させた濾液の上澄液を採取
し、精密濾過する工程。 (7)前工程により得られた濾液を加熱殺菌する工程。 (8)前工程で得られた液に0.1%以上3%以下のエ
チルアルコールを添加する工程。
1. A method for producing a high-concentration mineral liquid, comprising the following steps (1) to (8): (1) A mixture of humus of 10% to 90% by weight (the same applies below) and the balance of coal having a low degree of coalification is used as a raw material, and 0.5% to 5% of concentrated sulfuric acid is added to the mixture. 1%
A step of adding 3% or less of ethyl alcohol and 8% or more and 15% or less of water, and heating to a temperature of 60 ° C. or more and 90 ° C. or less and stirring. (2) Fermentation by leaving the raw material produced in the previous step for 4 to 10 days (hereinafter referred to as the first aging period).
Aging process. (3) Add 30 to 100 times by weight of water to the raw material that has been aged during the first aging period, and allow it to age for 7 to 15 days (hereinafter referred to as the second aging period) while aerating. Process. (4) A step of filtering the solid matter from the raw material aged during the second aging period and collecting the filtrate. (5) A step of allowing the filtrate collected in the preceding step to stand for 5 days to 15 days (hereinafter referred to as the third aging period) to be precipitated and aged. (6) A step of collecting the supernatant of the filtrate aged during the third aging period and performing microfiltration. (7) A step of heat sterilizing the filtrate obtained in the previous step. (8) A step of adding 0.1% or more and 3% or less of ethyl alcohol to the liquid obtained in the previous step.
【請求項2】泥炭を原料として使用する請求項1に記載
の高濃度ミネラル液製造方法。
2. The method for producing a high-concentration mineral liquid according to claim 1, wherein peat is used as a raw material.
【請求項3】原料として、腐植土50%と泥炭50%と
から成る混合物を用いることを特徴とする請求項1又は
2にに記載の高濃度ミネラル液製造方法。
3. The method for producing a high-concentration mineral liquid according to claim 1, wherein a mixture of 50% humus and 50% peat is used as a raw material.
【請求項4】原料に対する濃硫酸の添加量が、1%であ
る請求項1ないし3の何れか一に記載の高濃度ミネラル
液製造方法。
4. The method for producing a high-concentration mineral liquid according to claim 1, wherein the amount of concentrated sulfuric acid added to the raw material is 1%.
【請求項5】原材料に対するエチルアルコールの添加量
が、2%である請求項1ないし4の何れか一に記載の高
濃度ミネラル液製造方法。
5. The method for producing a high-concentration mineral liquid according to claim 1, wherein the amount of ethyl alcohol added to the raw material is 2%.
【請求項6】原材料に対する水の添加量が、10%であ
る請求項1ないし5の何れか一に記載の高濃度ミネラル
液製造方法。
6. The method for producing a high-concentration mineral liquid according to claim 1, wherein the amount of water added to the raw material is 10%.
【請求項7】原材料に対するエチルアルコールの添加量
が、2%である請求項1ないし6の何れか一に記載の高
濃度ミネラル液製造方法。
7. The method for producing a high-concentration mineral liquid according to claim 1, wherein the amount of ethyl alcohol added to the raw material is 2%.
【請求項8】第一熟成期間が5日間である請求項1ない
し7の何れか一に記載の高濃度ミネラル液製造方法。
8. The method for producing a high-concentration mineral liquid according to claim 1, wherein the first aging period is 5 days.
【請求項9】第一熟成期間終了後の希釈率が、50倍で
ある請求項1ないし8の何れか一に記載の高濃度ミネラ
ル液製造方法。
9. The method for producing a high-concentration mineral liquid according to claim 1, wherein the dilution ratio after the first aging period is 50 times.
【請求項10】第二熟成期間が10日間である請求項1
ないし9の何れか一に記載の高濃度ミネラル液製造方
法。
10. The second ripening period is 10 days.
10. The method for producing a high-concentration mineral liquid according to any one of 1 to 9.
【請求項11】最終熟成期間が10日間である請求項1
ないし10の何れか一に記載の高濃度ミネラル液製造方
法。
11. The final ripening period is 10 days.
11. The method for producing a high-concentration mineral liquid according to any one of 1 to 10.
【請求項12】加熱殺菌が80°Cで30分間行われる
請求項1ないし11の何れか一に記載の高濃度ミネラル
液製造方法。
12. The method for producing a high-concentration mineral liquid according to claim 1, wherein heat sterilization is performed at 80 ° C. for 30 minutes.
【請求項13】最終工程で添加するエチルアルコールの
添加量が1%である請求項1ないし12の何れか一に記
載の高濃度ミネラル液製造方法。
13. The method for producing a high-concentration mineral liquid according to claim 1, wherein the amount of ethyl alcohol added in the final step is 1%.
【請求項14】最終工程で得られた製品のPHが3ない
し3.8である請求項1ないし13の何れか一に記載の
高濃度ミネラル液製造方法。
14. The method for producing a high-concentration mineral liquid according to claim 1, wherein the pH of the product obtained in the final step is 3 to 3.8.
JP947292A 1992-01-22 1992-01-22 High-concentration mineral liquid manufacturing method Expired - Lifetime JPH074594B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP947292A JPH074594B2 (en) 1992-01-22 1992-01-22 High-concentration mineral liquid manufacturing method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP947292A JPH074594B2 (en) 1992-01-22 1992-01-22 High-concentration mineral liquid manufacturing method

Publications (2)

Publication Number Publication Date
JPH05192666A true JPH05192666A (en) 1993-08-03
JPH074594B2 JPH074594B2 (en) 1995-01-25

Family

ID=11721210

Family Applications (1)

Application Number Title Priority Date Filing Date
JP947292A Expired - Lifetime JPH074594B2 (en) 1992-01-22 1992-01-22 High-concentration mineral liquid manufacturing method

Country Status (1)

Country Link
JP (1) JPH074594B2 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006109709A (en) * 2004-10-12 2006-04-27 Marinekkus:Kk Fish feed and method for breeding fish
KR101235144B1 (en) * 2010-09-08 2013-02-21 삼영이노텍주식회사 Manufacturing method of mineral combined a functional water solution on the eco-friendly
KR20230108440A (en) * 2022-01-11 2023-07-18 농업회사법인 남진영농산업 주식회사 Soil restoration agent containing black peat and enzyme, and method for manufacturing the same

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006109709A (en) * 2004-10-12 2006-04-27 Marinekkus:Kk Fish feed and method for breeding fish
KR101235144B1 (en) * 2010-09-08 2013-02-21 삼영이노텍주식회사 Manufacturing method of mineral combined a functional water solution on the eco-friendly
KR20230108440A (en) * 2022-01-11 2023-07-18 농업회사법인 남진영농산업 주식회사 Soil restoration agent containing black peat and enzyme, and method for manufacturing the same

Also Published As

Publication number Publication date
JPH074594B2 (en) 1995-01-25

Similar Documents

Publication Publication Date Title
KR101799780B1 (en) Method for Manufacturing Plant Nutrient Containing Mineral Element
CN107418807A (en) A kind of production method of Organic grape fruit wine
CN107384673A (en) A kind of production method for not adding sulfur dioxide Organic grape fruit wine
CN107964467A (en) A kind of production method for not adding sulfur dioxide Organic grape fruit wine
JPH05192666A (en) Production of high-concentration mineral liquid
CN101082031A (en) Preparation of straw-protecting bacterium and method for restoring aquaculture environment
US4022882A (en) Germicidal solutions and methods for preserving and purifying milk, other beverages, foods, water and sewage effluent
JPH02203726A (en) Method for transporting live fish
JP4504965B2 (en) Method for producing solid fertilizer and solid fertilizer
US5198114A (en) Dolomitic activated carbon filter
JP4199526B2 (en) Concrete, method for growing plants using the same, plant grown by the methods, method for modifying soil using the same, and composition for soil using the same
JP3572281B2 (en) Fermented health food using deep ocean water and method for producing the same
WO2004004465A1 (en) Functional water with deodorization activity and sterilization activity against multi-drug resistent bacteria, and a preparation method thereof
US20220402834A1 (en) Method for treating human or animal urine and uses of the transformed urine obtained in particular as fertiliser
JP4280850B2 (en) Manufacturing method of organic fertilizer
JP4299532B2 (en) Method for producing glass and water treatment method using the same
Suyani et al. Copper, iron and zinc contents in water, pakcoy (Brassica rapa L.) and tilapia (Oreochromis niloticus) in the presence of aquaponics.
KR100278153B1 (en) Alkaline growth promoting and fermentation agent aqueous composition based on potassium and preparation method thereof
JP3581247B2 (en) Soil improving composition containing sulfur oxidizing fungi and method for producing the same
RU2803343C1 (en) New preparation based on hydrolyzate for waste disinfection
JPH05304959A (en) Photosynthetic bacteria-containing beads
WO2017046709A1 (en) Biocides and preparation thereof
KR980001957A (en) Mineral liquid extraction method
JP6539828B2 (en) Water quality improver and water quality improvement filter
KR20230139186A (en) A process for the preparation of fulvic acid in bulk from humus