JP2003192479A - Method for manufacturing stevia extract - Google Patents
Method for manufacturing stevia extractInfo
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- JP2003192479A JP2003192479A JP2001396281A JP2001396281A JP2003192479A JP 2003192479 A JP2003192479 A JP 2003192479A JP 2001396281 A JP2001396281 A JP 2001396281A JP 2001396281 A JP2001396281 A JP 2001396281A JP 2003192479 A JP2003192479 A JP 2003192479A
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- extract
- stevia
- fermentation
- atmospheric pressure
- pressure
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- 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.)
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- Coloring Foods And Improving Nutritive Qualities (AREA)
- Agricultural Chemicals And Associated Chemicals (AREA)
- Fertilizers (AREA)
Abstract
Description
【0001】[0001]
【発明が属する技術分野】本発明は、ステビアエキスの
製造方法に関する。TECHNICAL FIELD The present invention relates to a method for producing stevia extract.
【0002】[0002]
【従来の技術】農業分野における土壌中の有用微生物の
増殖資材、成長促進活性剤などとして、また畜産分野で
の栄養補助飼料添加物として、また、健康食品、各種化
粧品の有効成分等々としてステビアエキスの利用は、広
く行われている。このステビアエキスの製法としては、
特許第2577105号に提案された方法が知られてい
る。これは、乾燥させたステビアの葉と茎を粉砕して粉
末化し、これを水に入れて煮沸してステビア抽出液を
得、この抽出液を濃縮し、発酵・熟成させるものであ
る。BACKGROUND OF THE INVENTION Stevia extract is used as a material for growing useful microorganisms in soil in the agricultural field, as a growth promoting activator, as a nutritional supplement feed additive in the field of livestock, and as an active ingredient in health foods and various cosmetics. Is widely used. As a manufacturing method of this Stevia extract,
The method proposed in Japanese Patent No. 2577105 is known. In this method, dried stevia leaves and stems are crushed into powder, put in water and boiled to obtain a stevia extract, and the extract is concentrated, fermented and aged.
【0003】[0003]
【発明が解決しようとする課題】しかし、上記の方法
は、煮沸、濃縮工程に非常に手間が掛かり、また、濃縮
する際のエネルギー効率が悪いなど、製造コストが嵩ん
でいた。また、煮沸、濃縮工程においてあくが多く生
じ、これが、発酵を抑制したり、不純物として残留し品
質を低下させるなどの問題もあった。However, in the above-mentioned method, the boiling and concentrating steps are very troublesome and the energy efficiency in concentrating is poor, resulting in high manufacturing cost. In addition, there is a problem in that a lot of holes are generated in the boiling and concentration steps, which suppresses fermentation and remains as an impurity to deteriorate the quality.
【0004】本発明は、このような事実から考えられた
もので、品質が向上し、製造が簡単で、製造コストの引
き下げが可能なステビアエキスの製造方法を提供するこ
とを目的としている。The present invention has been conceived from such a fact, and an object of the present invention is to provide a method for producing stevia extract, which has improved quality, is easy to produce, and can reduce the production cost.
【0005】[0005]
【課題を解決するための手段】上記の目的を達成するた
めに本発明のステビアエキスの製造方法は、ステビア茎
粉末を大気圧以上に加圧された状態で煮沸した後、固形
物を取り除いて抽出液を得る工程と、該抽出液を減圧し
た状態で加熱して濃縮する工程と、濃縮された抽出液を
発酵機により1次発酵させる工程と、1次発酵させた濃
縮液を発酵・熟成する工程とを有することを特徴として
いる。発酵機による1次発酵時に、発酵機内を0.2M
Pa程度に加圧して行ってもよい。Means for Solving the Problems In order to achieve the above object, a method for producing a stevia extract according to the present invention is as follows: Stevia stalk powder is boiled under a pressure higher than atmospheric pressure, and then solid matter is removed. A step of obtaining an extract, a step of heating and concentrating the extract under a reduced pressure, a step of subjecting the concentrated extract to a primary fermentation by a fermenter, and a step of fermenting and aging the concentrated concentrate subjected to the primary fermentation And a step of performing. 0.2M inside the fermenter during the primary fermentation by the fermenter
The pressure may be increased to about Pa.
【0006】前記濃縮する工程及び/又は発酵・熟成す
る工程で、網によりあく又は不純物をすくい取ることが
望ましい。前記のいずれかに記載の液状ステビアエキス
を乾燥して粉末状にする工程を付加することもできる。[0006] In the step of concentrating and / or the step of fermenting and aging, it is desirable to scrape off impurities or scoop out impurities. It is also possible to add a step of drying the liquid stevia extract described in any of the above into a powder form.
【0007】[0007]
【発明の実施の形態】以下、本発明を実施例に基づき具
体的に説明する。原料となるステビアは、株苗又は挿し
木苗或いは播種苗いずれにおいても、栽培は無農薬有機
栽培により行われ、成熟したものを年に1度(10月上
旬)刈りとったものを用いる。刈り取りは、ステビア葉
を手摘みにより除去した後、ステビア茎を根本から10
cm程度の所で刈り取ることにより行われる。ステビア
葉は、煮沸時にあくを多く生じ、このあくが発酵抑制や
純度低下の原因となることが分かったので、本発明では
ステビア葉は用いないこととしている。BEST MODE FOR CARRYING OUT THE INVENTION The present invention will be specifically described below based on Examples. Stevia, which is a raw material, is cultivated by pesticide-free organic cultivation in any of seedlings, cuttings, and seedlings, and mature ones are trimmed once a year (early October). For mowing, after removing the Stevia leaf by hand, remove the Stevia stem from the root.
It is done by cutting at about cm. Stevia leaves were found to produce a large amount of arbor during boiling, and it was found that this arbor causes fermentation inhibition and deterioration of purity. Therefore, the present invention does not use stevia leaves.
【0008】こうして刈り取った後のステビア茎を自然
乾燥又は乾燥機により乾燥し、水分含有率を5%ないし
10%にする。こうして乾燥したステビアの茎を20メ
ッシュ程度に粉砕し、ステビア茎粉末とする。The Stevia stalks thus cut off are dried naturally or by a drier to have a water content of 5% to 10%. The dried Stevia stalks are pulverized to about 20 mesh to obtain Stevia stalk powder.
【0009】このステビア茎粉末を水で煮沸して抽出処
理する。従来この抽出工程は、常圧釜により大気圧下で
行われていた。しかし、常圧釜による熱水抽出および加
熱濃縮では、熱量の割に時間と手間がかかっていた。そ
こで本発明では、以下のようにして抽出処理している。This Stevia stalk powder is boiled in water for extraction treatment. Conventionally, this extraction step has been carried out under atmospheric pressure by means of an atmospheric pressure pot. However, the hot water extraction and the heating concentration in the atmospheric pressure pot takes time and effort for the amount of heat. Therefore, in the present invention, the extraction processing is performed as follows.
【0010】まず、上記のステビア茎粉末20kgに対
して水100リットルを加えかき混ぜた上、常温で約3
0分間放置する。これにより乾燥したステビア茎の粉末
が水分を吸収して柔らかくなり、有効成分を取り出し易
くなる。First, 100 liters of water was added to 20 kg of the above-mentioned Stevia stalk powder, and the mixture was agitated.
Leave for 0 minutes. As a result, the dried powder of Stevia stalk absorbs water and becomes soft, making it easy to take out the active ingredient.
【0011】その後、圧力釜で大気圧より高い約0.1
5±0.02MPaの圧力下、温度125±10℃で加
熱して沸騰させる。圧力釜で大気圧以上に加圧した状態
なので、沸点が125±10℃と上昇し、ステビア茎に
含まれる有効成分の溶出を促し、効率的に熱水中に抽出
することができる。この抽出時間はステビア茎粉末の状
態によって異なるが30分ないし1時間程度である。After that, in the pressure cooker, the pressure is higher than the atmospheric pressure by about 0.1.
It is heated to a temperature of 125 ± 10 ° C. and boiled under a pressure of 5 ± 0.02 MPa. Since the pressure is higher than atmospheric pressure in the pressure cooker, the boiling point rises to 125 ± 10 ° C., which promotes the elution of the active ingredient contained in the Stevia stalk and enables efficient extraction into hot water. The extraction time varies depending on the state of the Stevia stem powder, but is about 30 minutes to 1 hour.
【0012】こうして得た抽出液を脱水し、固形分を含
まない抽出液にする。脱水方法は、特に限定しないが、
この実施例では、綿の袋に入れ、回転式脱水機又はスク
リュウ式脱水機により脱水し、固形分を含まない完全な
抽出液約80リットルを得ている。The extract thus obtained is dehydrated to obtain an extract containing no solid content. The dehydration method is not particularly limited,
In this example, the product was placed in a cotton bag and dehydrated by a rotary dehydrator or a screw dehydrator to obtain about 80 liters of a complete extract containing no solid content.
【0013】従来は、この抽出液を得る工程は、大気圧
下で行っていた。そのため、有効成分の抽出に非常に手
間が掛かっていた。概要を説明すると、ステビアの葉と
茎の粉末を沸騰状態で1時間程度煮詰め、搾り機で絞っ
て第1回抽出液を得、搾りカスを再度1時間程度かけて
煮詰めて、搾り機で第2回抽出液を得、第1回と第2回
の抽出液を混合して抽出液を得ていた。これに対し、本
発明の方法では、圧力釜で大気圧以上に加圧するので、
高温になり短時間で有効成分を抽出できる。Conventionally, the step of obtaining this extract has been carried out under atmospheric pressure. Therefore, it takes a lot of time to extract the active ingredient. The outline is as follows: Stevia leaf and stem powder is boiled in the boiling state for about 1 hour, squeezed with a squeezing machine to obtain the 1st extraction liquid, squeezed waste is boiled again for about 1 hour, and squeezed with a squeezing machine. The extract was obtained twice and the extract was obtained by mixing the first and second extracts. On the other hand, in the method of the present invention, since the pressure in the pressure cooker is increased to the atmospheric pressure or higher,
The temperature becomes high and the active ingredient can be extracted in a short time.
【0014】次に、上記の固形分の取り除かれた抽出液
約80リットルを真空濃縮機に入れ、温度80±5℃、
圧力0.06±0.01MPaの大気圧未満に減圧され
た条件下で約2時間濃縮し、濃縮比重1.3の濃縮液を
約60リットル得る。Next, about 80 liters of the extract from which the above solid content was removed was placed in a vacuum concentrator, and the temperature was adjusted to 80 ± 5 ° C.
Concentrate for about 2 hours under the pressure reduced to less than the atmospheric pressure of 0.06 ± 0.01 MPa to obtain about 60 liters of a concentrated liquid having a specific gravity of 1.3.
【0015】この工程は、従来は、上記の混合した抽出
液を大気圧下で煮詰めて濃縮する方法で行っていた。そ
のため、通常の水の沸点である100℃まで温度を上げ
なければ、濃縮が進まなかった。This step has conventionally been carried out by a method in which the above-mentioned mixed extract is boiled down under atmospheric pressure and concentrated. Therefore, the concentration did not proceed unless the temperature was raised to 100 ° C., which is the normal boiling point of water.
【0016】しかし、本発明では、大気圧より低い減圧
下で加熱濃縮するので、抽出液の沸点が下がり、蒸発潜
熱も下がるので、濃縮に要する時間と熱量の双方が節約
できることになった。However, in the present invention, since the heat concentration is carried out under reduced pressure lower than the atmospheric pressure, the boiling point of the extract is lowered and the latent heat of vaporization is also reduced, so that both the time and the amount of heat required for concentration can be saved.
【0017】濃縮行程中、抽出液の表面にあくが発生す
るが、このあくが、発酵を抑制したり、有効成分を阻害
する原因となっていることが分かった。そこで、本発明
では、50メッシュ程度の網を回転させてあくをすくい
取ることとしている。濃縮が進んできたら、濃縮液の糖
度を測定し、8度ないし25度になったところで、濃縮
を止める。It was found that the surface of the extract was tainted during the concentration process, and this awning was the cause of inhibiting fermentation or inhibiting the active ingredient. Therefore, in the present invention, a net of about 50 mesh is rotated to scoop out the perforation. Once the concentration has proceeded, measure the sugar content of the concentrate and stop the concentration when it reaches 8 to 25 degrees.
【0018】こうして得られた濃縮液を、発酵機に入
れ、温度30℃、圧力0.2±0.02MPaの大気圧
の約2倍に加圧された状態で24時間かけて1次発酵さ
せる。ステビアの発酵は、基本的には、外部から酵母菌
を加えずに、ステビアが自然状態で有する酵母菌で発酵
させる自然発酵である。従来は、上記の濃縮液を直接熟
成タンクに入れて発酵させていた。しかし、この方法で
は、ステビアが有する酵母菌の量は少なく、雑菌が混入
し易い状態なので、混入した雑菌ばかりが増殖して濃縮
液が腐敗することもあり、発酵の安定性に欠けていた。
これに対し本発明では、濃縮液を発酵機に入れて所定温
度、所定圧の下で発酵させるので、腐敗を防止して安定
して発酵させることができる。すなわち、雑菌の多くの
ものは耐圧性がないので死滅させたり増殖を抑えたりし
易い。一方、発酵に必要な酵母菌は耐圧性があるので、
優先的に増殖させることができる。その結果、雑菌の繁
殖を抑えて安定した発酵をさせることができるようにな
った。The concentrate thus obtained is put into a fermenter and subjected to primary fermentation for 24 hours under the condition that the temperature is 30 ° C. and the pressure is about twice the atmospheric pressure of 0.2 ± 0.02 MPa. . The fermentation of Stevia is basically a natural fermentation in which Stevia is fermented with a yeast that naturally exists without adding yeast from the outside. Conventionally, the above concentrated solution was directly put into an aging tank for fermentation. However, according to this method, the amount of yeast contained in Stevia is small and various bacteria are easily mixed in. Therefore, only the mixed bacteria may grow and the concentrated solution may be spoiled, resulting in lack of stability of fermentation.
On the other hand, in the present invention, since the concentrated liquid is put into the fermenter and fermented at a predetermined temperature and a predetermined pressure, spoilage can be prevented and stable fermentation can be performed. That is, since many of the various bacteria do not have pressure resistance, it is easy to kill them or suppress their growth. On the other hand, the yeast required for fermentation has pressure resistance,
It can grow preferentially. As a result, it became possible to suppress the propagation of various bacteria and to perform stable fermentation.
【0019】発酵機を使用すると、発酵期間が通常の1
/2から1/3程度に短縮できるのであるが、多数の発
酵機が必要になる。そこで、1次発酵、すなわち、上記
の酵母菌を優先的に増殖させる段階だけを発酵機で行
い、その後の発酵と熟成とは熟成タンクで行うこととし
ている。When a fermenter is used, the fermentation period is 1
Although it can be shortened from / 2 to 1/3, a large number of fermenters are required. Therefore, the primary fermentation, that is, only the step of preferentially growing the above-mentioned yeast is performed in the fermenter, and the subsequent fermentation and aging are performed in the aging tank.
【0020】1次発酵終了後、濃縮液を熟成タンクに移
し25℃から40℃にて30日ないし360日熟成す
る。熟成期間に幅があるのは、糖度が高いほど熟成に時
間が掛かるためである。前記の特許第2577105号
では、熟成温度は20℃から25℃であったが、本発明
では、あくが少ないこと、1次熟成をして雑菌が無く、
酵母菌が増加していることなどの理由から、25℃以上
の温度にして熟成することができ、前記の特許第257
7105号に示す熟成期間のほぼ1/2の期間に短縮す
ることができた。この発酵と熟成のときにも酵母菌の死
骸や結晶等の不純物が発生する為、70メッシュ程度の
網を液内に回転させ、これらを除去できるようにした。After the completion of the primary fermentation, the concentrated solution is transferred to an aging tank and aged at 25 to 40 ° C. for 30 to 360 days. The ripening period varies because the higher the sugar content, the longer the aging. In the above-mentioned Japanese Patent No. 2577105, the aging temperature was from 20 ° C to 25 ° C, but in the present invention, there is little darkness, and primary aging eliminates germs,
Due to the fact that the number of yeasts is increasing, it can be aged at a temperature of 25 ° C. or higher.
The ripening period shown in No. 7105 could be shortened to almost half the period. Impurities such as yeast carcasses and crystals are also generated during the fermentation and aging, so a net of about 70 mesh was rotated in the liquid so that these could be removed.
【0021】前記したように、ステビアの発酵は酵母菌
を加えない自然発酵であるが、発酵を促す場合には、予
め培養した酵母菌を濃縮液に加え、次いで前記1次発酵
工程又は発酵・熟成工程を行うこととしてもよい。As described above, the fermentation of stevia is a natural fermentation without adding yeast, but in the case of promoting fermentation, yeast that has been cultured in advance is added to the concentrated liquid, and then the primary fermentation step or fermentation. An aging step may be performed.
【0022】このようにして得られた発酵熟成液がステ
ビアエキスである。このステビアエキスを原液のまま、
あるいは水等により希釈して用いる。本発明の方法によ
り製造されたステビアエキスは、純度が高いので、希釈
する倍率を従来のものより大きくすることができる。た
とえば、農業用として各種の果樹に葉面散布したり、土
壌灌水したりするが、従来のステビアエキスは700〜
1000倍程度に希釈したものを使用していた。これに
対し、本発明の製造方法によるステビアエキスは、15
00〜2000倍に希釈したもので、同等の効果が確認
できた。The fermented and aged liquid thus obtained is stevia extract. This stevia extract is undiluted,
Alternatively, it is diluted with water before use. Since the stevia extract produced by the method of the present invention has high purity, the dilution ratio can be made larger than that of the conventional one. For example, foliar application to various fruit trees for agricultural use or soil watering, but conventional Stevia extract is 700-
The one diluted about 1000 times was used. On the other hand, the stevia extract produced by the production method of the present invention is 15
The same effect could be confirmed with the product diluted to 100 to 2000 times.
【0023】上記のステビアエキスは、液体であるが、
この液体を乾燥して粉末状にしてもよい。エキスを乾燥
粉末状にする事により、保存上あるいは使用上の簡便化
を図る事が出来る。粉末状のステビアエキスはそのまま
使用してもよく、水等に溶解して用いてもよい。乾燥方
法としては、熱風乾燥でもよいが、フリーズドライが品
質の変化を殆ど起こさないことから望ましい。The above stevia extract is a liquid,
The liquid may be dried to give a powder. By making the extract into a dry powder form, it is possible to simplify storage or use. The powdery stevia extract may be used as it is, or may be used by dissolving it in water or the like. As a drying method, hot air drying may be used, but freeze drying is preferable because it hardly causes a change in quality.
【0024】[0024]
【発明の効果】以上に説明したように本発明によれば、
ステビア茎粉末を大気圧以上に加圧された状態で煮沸し
た後、固形物を取り除いて抽出液を得る工程と、該抽出
液を大気圧以下に減圧した状態で加熱して濃縮する工程
と、濃縮された抽出液を発酵機により1次発酵させる工
程と、1次発酵させた濃縮液を発酵・熟成する工程とを
有するので、品質のよいステビアエキスを、安価に得る
ことができる。As described above, according to the present invention,
After boiling Stevia stalk powder under a pressure higher than atmospheric pressure, a step of removing the solid matter to obtain an extract, a step of heating and concentrating the extract under a reduced pressure below atmospheric pressure, and Since it has a step of first fermenting the concentrated extract with a fermenter and a step of fermenting and aging the concentrated concentrate that has been first fermented, a high quality stevia extract can be obtained at low cost.
フロントページの続き Fターム(参考) 2B150 AB03 BC06 DD42 DD57 4B018 MD61 MF01 MF06 MF07 MF13 4H011 AB04 BA01 BB08 BB22 DD03 DE15 4H061 AA02 CC41 EE61 EE66 GG13 GG18 GG21 GG22 GG48 Continued front page F-term (reference) 2B150 AB03 BC06 DD42 DD57 4B018 MD61 MF01 MF06 MF07 MF13 4H011 AB04 BA01 BB08 BB22 DD03 DE15 4H061 AA02 CC41 EE61 EE66 GG13 GG18 GG21 GG22 GG48
Claims (3)
た状態で煮沸した後、固形物を取り除いて抽出液を得る
工程と、該抽出液を大気圧以下に減圧した状態で加熱し
て濃縮する工程と、濃縮された抽出液を発酵機により1
次発酵させる工程と、1次発酵させた濃縮液を発酵・熟
成する工程とを有することを特徴とするステビアエキス
の製造方法。1. A step of boiling stevia stalk powder in a state of being pressurized to atmospheric pressure or higher, and then removing solid matter to obtain an extract, and heating the extract in a state of being reduced in pressure to atmospheric pressure or less. The process of concentrating and the concentrated extract by fermenter 1
A method for producing a stevia extract, which comprises a step of secondary fermentation and a step of fermenting and aging the concentrated liquid subjected to primary fermentation.
する工程で、網によりあく又は不純物をすくい取ること
を特徴とする請求項1記載のステビアエキスの製造方
法。2. The method for producing a stevia extract according to claim 1, wherein in the step of concentrating and / or the step of fermenting and aging, scraping or impurities are scraped off with a net.
乾燥して粉末状にする工程を付加したことを特徴とする
ステビアエキスの製造方法。3. A method for producing a stevia extract, characterized by comprising the step of drying the stevia extract according to claim 1 or 2 into a powder form.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2001396281A JP3962585B2 (en) | 2001-12-27 | 2001-12-27 | Stevia extract manufacturing method |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2001396281A JP3962585B2 (en) | 2001-12-27 | 2001-12-27 | Stevia extract manufacturing method |
Publications (2)
Publication Number | Publication Date |
---|---|
JP2003192479A true JP2003192479A (en) | 2003-07-09 |
JP3962585B2 JP3962585B2 (en) | 2007-08-22 |
Family
ID=27602415
Family Applications (1)
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Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR20010111560A (en) * | 2001-11-22 | 2001-12-19 | 김신영 | manufacture methode of stevia concentrated liquor |
WO2005112668A1 (en) * | 2004-05-24 | 2005-12-01 | Soo Sang Park | Manufacturing method of the stevia-extracts |
CN110638852A (en) * | 2019-09-16 | 2020-01-03 | 上海维丘康敬生物科技有限公司 | Pure natural plant antioxidant derived from natural stevia rebaudiana and preparation method thereof |
Families Citing this family (1)
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CN103156057A (en) * | 2011-12-16 | 2013-06-19 | 邝素明 | Microbial fermented feed and production process thereof |
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR20010111560A (en) * | 2001-11-22 | 2001-12-19 | 김신영 | manufacture methode of stevia concentrated liquor |
WO2005112668A1 (en) * | 2004-05-24 | 2005-12-01 | Soo Sang Park | Manufacturing method of the stevia-extracts |
CN110638852A (en) * | 2019-09-16 | 2020-01-03 | 上海维丘康敬生物科技有限公司 | Pure natural plant antioxidant derived from natural stevia rebaudiana and preparation method thereof |
CN110638852B (en) * | 2019-09-16 | 2022-05-17 | 上海维丘康敬生物科技有限公司 | Pure natural plant antioxidant derived from natural stevia rebaudiana and preparation method thereof |
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