JP3962585B2 - Stevia extract manufacturing method - Google Patents

Stevia extract manufacturing method Download PDF

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JP3962585B2
JP3962585B2 JP2001396281A JP2001396281A JP3962585B2 JP 3962585 B2 JP3962585 B2 JP 3962585B2 JP 2001396281 A JP2001396281 A JP 2001396281A JP 2001396281 A JP2001396281 A JP 2001396281A JP 3962585 B2 JP3962585 B2 JP 3962585B2
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extract
stevia
pressure
fermentation
atmospheric pressure
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JP2003192479A (en
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俊彦 山名
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ダイエーワーク株式会社
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Description

【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。
【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。
【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。
【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。
【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より高い圧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、該抽出液を大気圧より低い圧に減圧した状態で加熱して網によりあく又は不純物をすくい取りながら濃縮する工程と、濃縮された抽出液を発酵機により圧力0.2±0.02MPaに加圧された状態で1次発酵させる工程と、1次発酵させた濃縮液を25℃〜40℃の温度で発酵・熟成する工程とを有することを特徴としている。
【0006】
また、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。
【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10cm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。
【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。
【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。
【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30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。
【0011】
その後、圧力釜で大気圧より高い約0.15±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。
【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。
【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。
【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。
【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。
【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。
【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。
【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。
【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。
【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2577105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。
【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。
【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、1500〜2000倍に希釈したもので、同等の効果が確認できた。
【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。
【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より高い圧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、該抽出液を大気圧より低い圧に減圧した状態で加熱して網によりあく又は不純物をすくい取りながら濃縮する工程と、濃縮された抽出液を発酵機により大気圧の約2倍に加圧された状態で1次発酵させる工程と、1次発酵させた濃縮液を25℃〜40℃の温度で発酵・熟成する工程とを有するので、あくや不純物をすくい取ることによって、雑菌が少なくなり、従来より高温の25℃〜40℃での熟成が可能となります。さらに、大気圧より高い圧に加圧された状態で1次発酵させることで、雑菌を死滅させたり、増殖を抑えたりし易くなり、品質のよいステビアエキスを、安価に得ることができる。
[0001]
[Technical field to which the invention belongs]
The present invention relates to a method for producing stevia extract.
[0002]
[Prior art]
Stevia extract is widely used as a growth material for growth of useful microorganisms in soil in the agricultural field, as a growth-promoting activator, as a nutritional supplement feed additive in the livestock field, and as an active ingredient in health foods and various cosmetics. Has been done. As a method for producing this stevia extract, a method proposed in Japanese Patent No. 2577105 is known. In this method, the dried stevia leaves and stems are pulverized and powdered, put into water and boiled to obtain a stevia extract, and the extract is concentrated, fermented and matured.
[0003]
[Problems to be solved by the invention]
However, the above method requires a lot of labor for the boiling and concentration steps, and has a high production cost such as low energy efficiency when concentrating. In addition, many boilings occur in the boiling and concentrating steps, which have problems such as inhibiting fermentation and remaining as impurities to lower the quality.
The present invention has been conceived from such a fact, and an object of the present invention is to provide a method for producing a stevia extract with improved quality, simple production, and reduced production costs.
[0005]
[Means for Solving the Problems]
In order to achieve the above object, the method for producing a stevia extract according to the present invention comprises boiling stevia stem powder under a pressure higher than atmospheric pressure, and then removing solids to obtain an extract; The extract is heated while being decompressed to a pressure lower than atmospheric pressure, and concentrated while scooping or scooping out impurities, and the concentrated extract is applied to a pressure of 0.2 ± 0.02 MPa by a fermenter. It is characterized by having a step of primary fermentation in a pressed state and a step of fermenting and aging the concentrated solution subjected to primary fermentation at a temperature of 25 ° C to 40 ° C.
[0006]
Moreover, the process which dries the liquid stevia extract in any one of the above to a powder form can also be added.
[0007]
DETAILED DESCRIPTION OF THE INVENTION
Hereinafter, the present invention will be specifically described based on examples. Stevia used as a raw material is grown by pesticide-free organic cultivation in any of plant seedlings, cutting seedlings, or seeded seedlings, and a matured one is harvested once a year (early October). The mowing is performed by removing the stevia leaf by hand picking and then cutting the stevia stem at a location about 10 cm from the root. Since stevia leaves generate a lot of boiling when boiled, and this drilling has been found to cause fermentation inhibition and purity reduction, stevia leaves are not used in the present invention.
[0008]
The stevia stalks after cutting in this way are naturally dried or dried with a drier to bring the moisture content to 5% to 10%. Stevia stems dried in this way are pulverized to about 20 mesh to obtain Stevia stem powder.
[0009]
This stevia stem powder is boiled with water and extracted. Conventionally, this extraction process has been carried out at atmospheric pressure using an atmospheric kettle. However, hot water extraction and heat concentration with an atmospheric pressure kettle took time and effort for the amount of heat. Therefore, in the present invention, the extraction process is performed as follows.
[0010]
First, 100 liters of water is added to 20 kg of the above stevia stem powder, and the mixture is left to stand for about 30 minutes at room temperature. As a result, the dried stevia stem powder absorbs moisture and becomes soft, and the active ingredients can be easily taken out.
[0011]
Then, it is boiled by heating at a temperature of 125 ± 10 ° C. under a pressure of about 0.15 ± 0.02 MPa, which is higher than atmospheric pressure, in a pressure cooker. Since it is pressurized to atmospheric pressure or higher with a pressure cooker, the boiling point rises to 125 ± 10 ° C., which promotes the elution of active ingredients contained in stevia stem and can be efficiently extracted into hot water. The extraction time varies depending on the state of stevia stem powder, but is about 30 minutes to 1 hour.
[0012]
The extract thus obtained is dehydrated to obtain an extract containing no solids. The dehydration method is not particularly limited, but in this embodiment, it is put 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 solids.
[0013]
Conventionally, the step of obtaining this extract was performed under atmospheric pressure. For this reason, it has been very troublesome to extract active ingredients. Briefly, stevia leaves and stem powder are boiled for about 1 hour in a boiled state, squeezed with a squeezing machine to obtain the first extract, and the squeezed residue is again simmered for about 1 hour and The extract was obtained twice, and the first and second extracts were mixed to obtain an extract. On the other hand, in the method of the present invention, the pressure is increased to the atmospheric pressure or higher by the pressure cooker, so that the active ingredient can be extracted in a short time due to high temperature.
[0014]
Next, about 80 liters of the extract from which the solid content has been removed is put into a vacuum concentrator, and the pressure is reduced to less than atmospheric pressure at a temperature of 80 ± 5 ° C. and a pressure of 0.06 ± 0.01 MPa. Concentrate for a time to obtain about 60 liters of concentrated liquid having a concentrated specific gravity of 1.3.
[0015]
Conventionally, this step has been performed by a method in which the mixed extract is boiled and concentrated under atmospheric pressure. Therefore, the concentration did not proceed unless the temperature was raised to 100 ° C., which is the normal boiling point of water.
[0016]
However, in the present invention, the heat concentration is performed under a reduced pressure lower than the atmospheric pressure, so that the boiling point of the extract is lowered and the latent heat of vaporization is reduced, so that both the time required for concentration and the amount of heat can be saved.
[0017]
During the concentration process, a crack occurs on the surface of the extract. It has been found that this crack is a cause of inhibiting fermentation and inhibiting active ingredients. Therefore, in the present invention, the net is scooped by rotating a net of about 50 mesh. When the concentration has progressed, the sugar content of the concentrate is measured, and when it reaches 8 to 25 degrees, the concentration is stopped.
[0018]
The concentrated solution thus obtained is put into a fermenter and subjected to primary fermentation over 24 hours in a state of being pressurized to about twice the atmospheric pressure at a temperature of 30 ° C. and a pressure of 0.2 ± 0.02 MPa. Stevia fermentation is basically natural fermentation in which stevia is fermented in a natural state without adding yeast from outside. Conventionally, the above concentrated liquid is directly fermented in an aging tank. However, in this method, the amount of yeast contained in stevia is small and easily contaminated with bacteria. Therefore, only the contaminated bacteria grow and the concentrated solution may rot, and the stability of fermentation is lacking. On the other hand, in this invention, since a concentrate is put into a fermenter and it ferments under predetermined temperature and predetermined pressure, it can prevent rot and can ferment stably. That is, many of the miscellaneous bacteria do not have pressure resistance, and thus are easy to kill or suppress proliferation. On the other hand, yeast required for fermentation has pressure resistance, and can be preferentially grown. As a result, it has become possible to suppress the propagation of various bacteria and allow stable fermentation.
[0019]
When a fermenter is used, the fermentation period can be shortened from about 1/2 to about 1/3 of the normal time, but a large number of fermenters are required. Therefore, only the primary fermentation, that is, the stage in which the yeast is proliferated preferentially is performed in the fermenter, and the subsequent fermentation and aging are performed in the aging tank.
[0020]
After the completion of primary fermentation, the concentrate is transferred to an aging tank and aged at 25 to 40 ° C. for 30 to 360 days. The reason for the aging period is that the longer the aging time, the higher the sugar content. In the above-mentioned Patent No. 2577105, the ripening temperature was 20 ° C. to 25 ° C., but in the present invention, there are few varieties, there is no miscellaneous bacteria after primary ripening, and the yeast is increasing. For this reason, ripening can be performed at a temperature of 25 ° C. or higher, and the ripening period shown in the above-mentioned Japanese Patent No. 2577105 can be shortened to about half of the ripening period. Impurities such as dead bodies and crystals of yeast are generated during the fermentation and ripening, so a net of about 70 mesh was rotated into the liquid so that these could be removed.
[0021]
As described above, the fermentation of stevia is natural fermentation without adding yeast, but when promoting the fermentation, the yeast previously cultured is added to the concentrate, and then the primary fermentation process or the fermentation / ripening process is performed. It may be done.
[0022]
The fermented ripening liquid thus obtained is stevia extract. This stevia extract is used as it is or diluted with water or the like. Since the stevia extract manufactured by the method of the present invention has high purity, the dilution ratio can be made larger than the conventional one. For example, foliar spraying is carried out on various fruit trees for agricultural use or soil irrigation is used, but conventional stevia extract has been diluted about 700 to 1000 times. On the other hand, the stevia extract by the manufacturing method of this invention was diluted 1500 to 2000 times, and the equivalent effect has been confirmed.
[0023]
The above stevia extract is a liquid, but this liquid may be dried to form a powder. By making the extract into a dry powder form, it is possible to simplify storage and use. The powdered stevia extract may be used as it is, or may be used by dissolving 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]
【The invention's effect】
As described above, according to the present invention, the stevia stem powder is boiled in a state of being pressurized to a pressure higher than atmospheric pressure, and then the solid is removed to obtain an extract, and the extract is subjected to atmospheric pressure. Heating at a lower pressure and concentrating while scooping or scooping out impurities with a net, and primary fermentation in a state where the concentrated extract is pressurized to about twice the atmospheric pressure by a fermenter And the step of fermenting and aging the concentrated fermented liquid at a temperature of 25 ° C. to 40 ° C. By scooping out impurities and impurities, the number of miscellaneous bacteria is reduced, which is higher than conventional 25 ° C. Aging at ~ 40 ° C is possible. Furthermore, by performing primary fermentation in a state where the pressure is higher than atmospheric pressure, it becomes easy to kill germs and suppress growth, and a high quality stevia extract can be obtained at low cost.

Claims (2)

ステビア茎粉末を大気圧より高い圧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、該抽出液を大気圧より低い圧に減圧した状態で加熱して網によりあく又は不純物をすくい取りながら濃縮する工程と、濃縮された抽出液を発酵機により圧力0.2±0.02MPaに加圧された状態で1次発酵させる工程と、1次発酵させた濃縮液を25℃〜40℃の温度で発酵・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。After boiling Stevia stalk powder under a pressure higher than atmospheric pressure, the solid is removed to obtain an extract, and the extract is heated to a pressure lower than atmospheric pressure and heated to a net. The step of concentrating while scooping out impurities or impurities, the step of primary fermentation of the concentrated extract under a pressure of 0.2 ± 0.02 MPa by a fermenter, and the concentration subjected to primary fermentation And a step of fermenting and aging the liquid at a temperature of 25 ° C to 40 ° C. 請求項1記載のステビアエキスを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。  A method for producing a stevia extract, comprising a step of drying the stevia extract according to claim 1 into a powder form.
JP2001396281A 2001-12-27 2001-12-27 Stevia extract manufacturing method Expired - Fee Related JP3962585B2 (en)

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Cited By (1)

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Publication number Priority date Publication date Assignee Title
CN103156057A (en) * 2011-12-16 2013-06-19 邝素明 Microbial fermented feed and production process thereof

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KR20010111560A (en) * 2001-11-22 2001-12-19 김신영 manufacture methode of stevia concentrated liquor
KR100620854B1 (en) * 2004-05-24 2006-09-14 박수상 The manufacturing method of the stevia-extracts
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

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103156057A (en) * 2011-12-16 2013-06-19 邝素明 Microbial fermented feed and production process thereof

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