JPH0751042B2 - Method for producing lactic acid bacteria beverage - Google Patents
Method for producing lactic acid bacteria beverageInfo
- Publication number
- JPH0751042B2 JPH0751042B2 JP61053683A JP5368386A JPH0751042B2 JP H0751042 B2 JPH0751042 B2 JP H0751042B2 JP 61053683 A JP61053683 A JP 61053683A JP 5368386 A JP5368386 A JP 5368386A JP H0751042 B2 JPH0751042 B2 JP H0751042B2
- Authority
- JP
- Japan
- Prior art keywords
- lactic acid
- acid bacteria
- plate
- stock solution
- glass tube
- 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.)
- Expired - Lifetime
Links
- JVTAAEKCZFNVCJ-UHFFFAOYSA-N lactic acid Chemical compound CC(O)C(O)=O JVTAAEKCZFNVCJ-UHFFFAOYSA-N 0.000 title claims description 152
- 239000004310 lactic acid Substances 0.000 title claims description 76
- 235000014655 lactic acid Nutrition 0.000 title claims description 76
- 241000894006 Bacteria Species 0.000 title claims description 67
- 235000013361 beverage Nutrition 0.000 title claims description 23
- 238000004519 manufacturing process Methods 0.000 title claims description 10
- 239000011521 glass Substances 0.000 claims description 32
- 238000000855 fermentation Methods 0.000 claims description 22
- 230000004151 fermentation Effects 0.000 claims description 22
- 239000000499 gel Substances 0.000 claims description 20
- 235000015203 fruit juice Nutrition 0.000 claims description 19
- 239000011550 stock solution Substances 0.000 claims description 15
- 230000002093 peripheral effect Effects 0.000 claims description 11
- 229940041514 candida albicans extract Drugs 0.000 claims description 8
- 239000012138 yeast extract Substances 0.000 claims description 8
- 239000011259 mixed solution Substances 0.000 claims description 7
- 235000011389 fruit/vegetable juice Nutrition 0.000 claims description 6
- 239000000284 extract Substances 0.000 claims description 5
- 235000012149 noodles Nutrition 0.000 claims description 4
- 240000007594 Oryza sativa Species 0.000 claims 2
- 235000007164 Oryza sativa Nutrition 0.000 claims 2
- 235000009566 rice Nutrition 0.000 claims 2
- 239000000243 solution Substances 0.000 description 13
- 239000011324 bead Substances 0.000 description 6
- 239000000047 product Substances 0.000 description 6
- 210000004027 cell Anatomy 0.000 description 5
- 238000002474 experimental method Methods 0.000 description 5
- 239000007789 gas Substances 0.000 description 5
- 238000000034 method Methods 0.000 description 5
- 235000015197 apple juice Nutrition 0.000 description 4
- 235000019640 taste Nutrition 0.000 description 4
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 3
- 239000001301 oxygen Substances 0.000 description 3
- 229910052760 oxygen Inorganic materials 0.000 description 3
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- 235000020244 animal milk Nutrition 0.000 description 2
- 238000012258 culturing Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 235000016709 nutrition Nutrition 0.000 description 2
- 239000002504 physiological saline solution Substances 0.000 description 2
- 150000008442 polyphenolic compounds Chemical class 0.000 description 2
- 235000013824 polyphenols Nutrition 0.000 description 2
- 230000000630 rising effect Effects 0.000 description 2
- IXPNQXFRVYWDDI-UHFFFAOYSA-N 1-methyl-2,4-dioxo-1,3-diazinane-5-carboximidamide Chemical compound CN1CC(C(N)=N)C(=O)NC1=O IXPNQXFRVYWDDI-UHFFFAOYSA-N 0.000 description 1
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 1
- UXVMQQNJUSDDNG-UHFFFAOYSA-L Calcium chloride Chemical compound [Cl-].[Cl-].[Ca+2] UXVMQQNJUSDDNG-UHFFFAOYSA-L 0.000 description 1
- 241000675108 Citrus tangerina Species 0.000 description 1
- 244000199866 Lactobacillus casei Species 0.000 description 1
- 235000013958 Lactobacillus casei Nutrition 0.000 description 1
- GUBGYTABKSRVRQ-QKKXKWKRSA-N Lactose Natural products OC[C@H]1O[C@@H](O[C@H]2[C@H](O)[C@@H](O)C(O)O[C@@H]2CO)[C@H](O)[C@@H](O)[C@H]1O GUBGYTABKSRVRQ-QKKXKWKRSA-N 0.000 description 1
- 241000220225 Malus Species 0.000 description 1
- 239000001888 Peptone Substances 0.000 description 1
- 108010080698 Peptones Proteins 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 235000021016 apples Nutrition 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- 238000009954 braiding Methods 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- 230000001808 coupling effect Effects 0.000 description 1
- 235000013399 edible fruits Nutrition 0.000 description 1
- 238000011156 evaluation Methods 0.000 description 1
- 239000000796 flavoring agent Substances 0.000 description 1
- 235000019634 flavors Nutrition 0.000 description 1
- 235000019674 grape juice Nutrition 0.000 description 1
- 230000036541 health Effects 0.000 description 1
- 210000001822 immobilized cell Anatomy 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 229940017800 lactobacillus casei Drugs 0.000 description 1
- 239000008101 lactose Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 235000015097 nutrients Nutrition 0.000 description 1
- 230000035764 nutrition Effects 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 230000000149 penetrating effect Effects 0.000 description 1
- 235000019319 peptone Nutrition 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 235000010413 sodium alginate Nutrition 0.000 description 1
- 239000000661 sodium alginate Substances 0.000 description 1
- 229940005550 sodium alginate Drugs 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- 241001148471 unidentified anaerobic bacterium Species 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Landscapes
- Dairy Products (AREA)
- Non-Alcoholic Beverages (AREA)
Description
【発明の詳細な説明】 a.発明の目的 (産業上の利用分野) この考案は嗜好品としての乳酸菌飲料を製造する方法の
改良に関し、特に林檎果汁等の果物果汁を含む乳酸菌飲
料を製造する場合に適用して有効な発明である。DETAILED DESCRIPTION OF THE INVENTION a. Object of the invention (field of industrial application) The present invention relates to improvement of a method for producing a lactic acid bacterium beverage as a favorite product, and particularly to produce a lactic acid bacterium beverage containing fruit juice such as apple juice. The invention is effective when applied to cases.
(従来の技術及びこの問題点) 近年嗜好の多様化と、乳酸菌が健康の増進に役立つこと
から、各種の乳酸菌飲料が造られる様になって来た。(Prior art and this problem) In recent years, various lactic acid bacterium beverages have come to be produced because of diversification of taste and lactic acid bacteria are useful for promoting health.
ところが、乳酸菌を飲料中で醗酵させる為の条件が厳し
い為、乳酸菌飲料の種類は現在の所限られたものしか無
く、例えば果汁中の乳酸菌で醗酵させた乳酸菌飲料は未
だ市販されていないのが実状である。However, since the conditions for fermenting lactic acid bacteria in beverages are severe, the types of lactic acid bacteria beverages are currently limited, for example, lactic acid bacteria beverages fermented with lactic acid bacteria in fruit juice have not yet been marketed. It is the actual situation.
これは、林檎等の果汁のPH値が低く(酸性)、更に果汁
中に含まれるポリフェノール類が乳酸菌の発育を阻害す
るので、単に果汁に乳酸菌を加えただけではこの乳酸菌
が死滅してしまう為と考えられている。This is because the PH value of fruit juices such as apples is low (acidic), and the polyphenols contained in the fruit juices inhibit the growth of lactic acid bacteria, so simply adding lactic acid bacteria to the fruit juice kills the lactic acid bacteria. It is believed that.
又、乳酸菌の栄養要求特性が複雑であり、成育も遅い
為、果汁中での乳酸菌の成育を人為的に可能としても、
醗酵時間を長くしなければならず、製造コスト的に採算
が合わない事も市販されていない一因と考えられる。Also, because the nutritional requirements of lactic acid bacteria are complicated and the growth is slow, even if artificial growth of lactic acid bacteria in fruit juice is possible,
Fermentation time must be lengthened, and the fact that it is not profitable in terms of manufacturing cost is considered to be one reason why it is not commercially available.
天然果汁を主成分とする乳酸菌飲料を製造する方法とし
ては、別途獣乳中で増殖させた乳酸菌を果汁に添加する
方法や、果汁のPH値を大きくする方法、或いは処理材を
用いてポリフェノール類を除去する方法が知られている
が、獣乳中で増殖させた乳酸菌を用いるのでは、純粋に
果汁のみの乳酸菌飲料を得る事が出来ず、残りの2通り
の方法も、本発明者が行なった実験では、上記何れの方
法でも果汁を主成分とする乳酸菌飲料を造る事は出来な
かった。As a method for producing a lactic acid bacterium beverage containing natural fruit juice as a main component, a method of separately adding lactic acid bacteria grown in animal milk to the fruit juice, a method of increasing the PH value of the fruit juice, or a polyphenol using a treatment material Although a method for removing lactic acid bacteria is known, it is not possible to obtain a lactic acid bacterium beverage purely composed of fruit juice by using lactic acid bacteria grown in animal milk. In the experiment conducted, it was not possible to produce a lactic acid bacterium beverage containing fruit juice as a main component by any of the above methods.
本発明の乳酸菌飲料の製造方法は、PH値の低い果汁を含
む乳酸菌飲料の製造を効率的に行なって、近年印の嗜好
の多様化に対応出来る様にする事を目的としている。The method for producing a lactic acid bacterium beverage of the present invention is intended to efficiently produce a lactic acid bacterium beverage containing a juice having a low PH value, so that it is possible to cope with the diversification of tastes in recent years.
b.発明の構成 (問題を解決するための手段) 本発明の乳酸菌飲料の製造方法に於いては、まず酵母エ
キスと、麺汁と、穀物種子胚芽エキス等の栄養エキスの
1種又は2種以上を、果汁中に、乳酸菌の発育に必要な
最小限度の量をやや上回る量で、製品としての果汁入り
乳酸菌飲料の風味、外観(色合い)に悪影響を及ぼさな
い量として、0.05〜1.0%添加混合して、PH値が3.0〜4.
5の混合液を造り、この混合液を乳酸醗酵用原液として
使用する。b. Structure of the Invention (Means for Solving the Problem) In the method for producing a lactic acid bacteria beverage of the present invention, first, one or two kinds of nutrition extracts such as yeast extract, noodle juice, and grain seed germ extract. The above is added to the fruit juice in an amount that is slightly above the minimum amount required for the growth of lactic acid bacteria and that does not adversely affect the flavor and appearance (color) of the lactic acid bacteria beverage containing fruit juice as a product. When mixed, PH value is 3.0-4.
Make a mixed solution of 5 and use this mixed solution as a stock solution for lactic acid fermentation.
この様にして調整された醗酵用原液は、乳酸菌に接触さ
せる事で醗酵させて、乳酸菌飲料とするが、醗酵を効率
的に行なう場合は乳酸菌を108〜109個/mlの割合で包括
固定化したゲルに連続的に接触させる事で、乳酸菌を固
定化しない状態で醗酵させる場合よりも迅速に混合液中
に乳酸菌を混入させると共に、この乳酸菌を醗酵させ、
果汁を含む乳酸菌飲料とする。The fermentation stock solution thus prepared is fermented by contact with lactic acid bacteria to give a lactic acid bacterium beverage, but if the fermentation is carried out efficiently, the lactic acid bacteria are included at a rate of 10 8 to 10 9 cells / ml. By continuously contacting the immobilized gel, the lactic acid bacterium is mixed into the mixed solution more quickly than the case where the lactic acid bacterium is fermented in a non-immobilized state, and the lactic acid bacterium is fermented,
A lactic acid bacterium beverage containing fruit juice.
醗酵用原液とゲルとの接触を良好にして、乳酸の育成を
迅速に行なわせるには、この醗酵用原液を、乳酸菌を10
8〜109個/mlの割合で包括固定化したゲルと共に、下端
開口を底板によって塞がれ、上端開口部に開閉自在な蓋
板を設けたガラス筒と、ガラス筒の内側にこのガラス筒
とほぼ同心に設けられた水平方向の円輪板の内周縁に、
この内周縁から上方に立ち上る円筒を設けた整流板と、
この整流板の円筒に下端部を嵌合させて固定した多数の
小孔を有する支持枠と、上記底板の上側に設けれモータ
により竪軸を中心として上記整流板を構成する円輪板の
下側に於いて回転駆動される遠心翼とから成る培養装置
に投入し、上記遠心翼を回転させて、支持枠の外周面に
付着したゲルの間に乳酸醗酵用原液を流す様にして醗酵
を行なう。In order to make good contact between the fermentation stock solution and the gel and to accelerate the growth of lactic acid, this fermentation stock solution should be mixed with 10% lactic acid bacteria.
A glass tube with a bottom plate that closes the bottom opening and a lid plate that can be opened and closed at the top opening together with the gel that is comprehensively immobilized at a rate of 8 to 10 9 pieces / ml, and this glass tube inside the glass tube. On the inner peripheral edge of the horizontal circular plate provided concentrically with
A straightening plate provided with a cylinder that rises upward from the inner peripheral edge,
A support frame having a large number of small holes fixed by fitting the lower end portion to the cylinder of this straightening plate, and the lower part of the circular plate that constitutes the above straightening plate around the vertical axis by a motor provided above the bottom plate. Put into a culture device consisting of a centrifugal blade that is rotationally driven on the side, rotate the centrifugal blade, and make the stock solution for lactic acid fermentation flow between the gels attached to the outer peripheral surface of the support frame to perform fermentation. To do.
(実施例) 次に、本発明者が行なった実験に就いて説明する。Example Next, an experiment conducted by the present inventor will be described.
イ.ゲルビーズ作成 まず乳酸菌として、Lactobacillus casei IAM 1045を保
存培地より取り出して10mlのLPY培地に植え継いだ。こ
のLPY培地は、水に乳糖を1%と、ペプトンを0.7%と、
酵母エキスを0.5%とを加えたものである。I. Preparation of gel beads First, as lactic acid bacteria, Lactobacillus casei IAM 1045 was taken out from the storage medium and subcultured in 10 ml of LPY medium. This LPY medium contains 1% lactose and 0.7% peptone in water,
Yeast extract is added with 0.5%.
この様なLPY培地上に植え継がれた乳酸菌は、30℃で24
時間培養後、更に250m1のLPY培地に植菌して更に30℃で
24時間培養し、この培地中の乳酸菌の数を(3〜10)×
107個/mlに増殖した。Lactic acid bacteria subcultured on such LPY medium were
After culturing for an additional time, inoculate into 250m1 of LPY medium and further at 30 ℃
After culturing for 24 hours, the number of lactic acid bacteria in this medium is (3-10) ×
Proliferated to 10 7 cells / ml.
乳酸菌の数が(3〜10)×107個/mlに達した上記LPY培
地は、遠心分離器を用いて、3000rpmの速度で5分間遠
心分離作業を行ない、乳酸菌を捕集した。The above LPY medium in which the number of lactic acid bacteria reached (3 to 10) × 10 7 cells / ml was subjected to centrifugal separation at a speed of 3000 rpm for 5 minutes using a centrifuge to collect lactic acid bacteria.
捕集された乳酸菌は、更に滅菌処理済の生理的食塩水に
よって洗浄し、洗浄乳酸菌を得た。The collected lactic acid bacteria were further washed with physiological saline that had been sterilized to obtain washed lactic acid bacteria.
この洗浄乳酸菌は、予め滅菌処理をしておいた20mlの生
理的食塩水中に入れて鹸濁し、更にこの鹸濁液に予め調
整しておいた5%のアルギン酸ナトリウム液30mlを加え
て、雑菌が混入しない様にして混合した。The washed lactic acid bacteria were suspended in 20 ml of physiological saline that had been sterilized in advance and suspended, and 30 ml of a 5% sodium alginate solution prepared in advance was added to the suspension to prevent any bacteria. It mixed so that it might not mix.
この様にして得られた混合液は、3%の塩化カルシウム
溶液中に滴下してこの溶液中で固化させ、直径が3〜5m
mのゲルビーズとした。The mixed solution thus obtained was dropped into a 3% calcium chloride solution and solidified in this solution, and the diameter was 3 to 5 m.
m gel beads were used.
ロ.固定化された菌体の増殖 上記ゲルビーズ中に含まれる乳酸菌を増殖する為、この
ゲルビーズを図面に示す様な醗酵槽内に、予め滅菌処理
した醗酵用原液950mlと共に投入し、30℃で48時間培養
作業を行なった。B. In order to grow the lactic acid bacteria contained in the above-mentioned gel beads, the gel beads are put in a fermentation tank as shown in the drawing together with 950 ml of a stock solution for fermentation which has been sterilized in advance, and 48 hours at 30 ° C. Culture work was performed.
ここで言う醗酵用原液とは、PH3.9の林檎果汁に、酵母
エキスを0.25%混合した混合液の事の言う。The undiluted solution for fermentation here is a mixed solution of PH3.9 apple juice and 0.25% of yeast extract.
又、実験に使用した醗酵槽は、円筒状のガラス筒1の下
端部には、このガラス筒1の外径よりも少し大きな外径
を有する円板状の底板2を固定する事によって、ガラス
筒1の下端開口を塞いでいる。この底板2の外周寄り部
分で、ガラス筒1の外周面よりも外側に突出した部分に
は、複数本のスタッド3、3の下端部をそれぞれ螺着し
固定している。各スタッド3、3の上端部はそれぞれガ
ラス筒1の上端縁よりも少し上方に迄突出しており、こ
の上端部を上記ガラス筒1の外径よりも少し大きな外径
を有する円板状の蓋板4の外周寄り部分に穿設した円孔
5、5にそれぞれ挿通している。円孔5、5を挿通し、
蓋板4の上面から突出した各スタッド3、3の上端部に
はナット(図示省略)を螺合自在として、上端蓋板4を
ガラス筒1の上端開口部に開閉自在に装着している。In the fermenter used in the experiment, a glass bottom plate 2 having a slightly larger outer diameter than the outer diameter of the glass tube 1 is fixed to the lower end portion of the cylindrical glass tube 1 so that the glass The lower end opening of the cylinder 1 is closed. Lower end portions of a plurality of studs 3 and 3 are respectively screwed and fixed to portions of the bottom plate 2 near the outer periphery of the bottom plate 2 that project outward from the outer peripheral surface of the glass tube 1. The upper ends of the studs 3 and 3 respectively project slightly above the upper edge of the glass tube 1, and the upper ends of the studs 3 and 3 are disc-shaped lids having an outer diameter slightly larger than the outer diameter of the glass tube 1. The plate 4 is inserted into circular holes 5 and 5 formed near the outer periphery of the plate 4, respectively. Insert the circular holes 5 and 5,
Nuts (not shown) can be screwed onto the upper ends of the studs 3 and 3 protruding from the upper surface of the cover plate 4, and the upper end cover plate 4 is openably and closably attached to the upper end opening of the glass tube 1.
又、ガラス筒1の内側には、このガラス筒とほぼ同心に
設けられた水平方向の円輪板23の内周縁に、この内周縁
から上方に立ち上る円筒24を設けた整流板25を、ステー
7、7によって固定している。Further, inside the glass tube 1, a straightening plate 25 having a cylinder 24 rising upward from the inner peripheral edge of a horizontal circular disk 23 provided substantially concentric with the glass tube is installed. It is fixed by 7, 7.
この整流板25の下端部には、ステンレスのフィラメント
を編組して成る金網を円筒状に形成した支持枠6の下端
部を外嵌する事によって、この支持枠6を上記ガラス筒
1の内側に、このガラス筒1とほぼ同心に固定してい
る。At the lower end of the straightening plate 25, a lower end of a supporting frame 6 formed by cylindrically forming a metal mesh made by braiding stainless steel filaments is fitted onto the inner side of the glass tube 1. The glass tube 1 is fixed substantially concentrically.
一方、前記底板2の上面中心部には垂直軸8を植設して
おり、この垂直軸8に、回転ブロック9の中心部に固定
した倒立円筒状のキャップ10を回転自在に被着してい
る。上記回転ブロック9の周囲には環状の磁石11を嵌合
固定しており、この磁石11と、前記底板2を固定した基
板12の下方にブラケット13を介して固定したモータ14の
出力軸15に固定した環状の磁石16とを、底板2を介して
対向させている。On the other hand, a vertical shaft 8 is planted in the center of the upper surface of the bottom plate 2, and an inverted cylindrical cap 10 fixed to the center of a rotary block 9 is rotatably attached to the vertical shaft 8. There is. An annular magnet 11 is fitted and fixed around the rotary block 9, and the magnet 11 and an output shaft 15 of a motor 14 fixed via a bracket 13 below a base plate 12 to which the bottom plate 2 is fixed. The fixed annular magnet 16 is opposed to the bottom plate 2 via the bottom plate 2.
キャップ10を介して垂直軸8に回転自在に支持された回
転ブロック9の外周には、複数枚の平板状の翼板17、17
を放射方向に固定する事で、シロッコファン状の遠心翼
18の構成している。A plurality of flat blades 17, 17 are provided on the outer periphery of the rotary block 9 rotatably supported by the vertical shaft 8 via the cap 10.
By fixing the radial direction, the sirocco fan-shaped centrifugal blade
It has 18 components.
更に、この遠心翼18の上方で、前記整流板25を構成する
円筒24の内側部分には、ガラス筒1の内側に貯溜された
液体中に酸素を含まない気体を吹き込む為の気泡ノズル
19を設けている。この気泡ノズル19は、ガラス筒1の上
端開口を開閉する蓋板4の中心にこの蓋板4を貫通した
状態で固定した送気管20の下端部に、複数の小孔21、21
を有するノズル部22を固定したもので、送気管20を通じ
て送り込む圧縮気体を前記遠心翼18の直上位置に噴出す
る様に構成している。Further, above the centrifugal blade 18, an air bubble nozzle for blowing a gas containing no oxygen into the liquid stored inside the glass tube 1 is provided inside the cylinder 24 constituting the flow straightening plate 25.
19 are provided. This bubble nozzle 19 has a plurality of small holes 21, 21 at a lower end portion of an air supply pipe 20 fixed in a state of penetrating the lid plate 4 which opens and closes an upper end opening of the glass tube 1.
The nozzle portion 22 having the above is fixed, and the compressed gas fed through the air feeding pipe 20 is configured to be ejected to a position directly above the centrifugal blade 18.
尚、図示及び詳しい説明は省略するが、蓋板4には送気
管20の他、ガラス容器1内の培養液の状態を検出する為
のセンサや、培養液中に栄養分を送る為の管等が設けら
れている。Although illustration and detailed description are omitted, in addition to the air supply pipe 20, a sensor for detecting the state of the culture solution in the glass container 1, a tube for feeding nutrients into the culture solution, etc. Is provided.
以上に述べた通り構成される培養装置によって乳酸菌を
醗酵させて果汁を主成分とする乳酸菌飲料を造る場合、
まずガラス筒1の内側に乳酸醗酵用原液と共に乳酸菌を
固定した粒状ゲルを投入する。When fermenting lactic acid bacteria by the culture device configured as described above to make a lactic acid bacterium beverage mainly composed of fruit juice,
First, a granular gel in which lactic acid bacteria are fixed is put into the inside of the glass tube 1 together with the stock solution for lactic acid fermentation.
投入を完了したならば、送気管20を通じて気泡ノズル19
を構成するノズル部22内に窒素(N2)、二酸化炭素(CO
2)等、乳酸菌の醗酵に不適な酸素(O2)を含まない圧
縮気体を送り込み、このノズル部22の小孔21、21からガ
ラス筒1内に貯溜された培養液中に気体を吹き込みつ
つ、モータ14に通電する事によって遠心翼18を回転させ
る。Once charging is complete, bubble nozzle 19 through air line 20
Nitrogen (N 2 ) and carbon dioxide (CO
2 ) A compressed gas that does not contain oxygen (O 2 ) that is unsuitable for fermentation of lactic acid bacteria, such as 2 ), is sent, and the gas is blown into the culture solution stored in the glass tube 1 through the small holes 21, 21 of the nozzle portion 22. The centrifugal blade 18 is rotated by energizing the motor 14.
即ち、モータ14への通電によりこのモータ14の出力軸15
に固定された磁石16を回転させると、マグネットカップ
リング作用によって、この磁石16と底板2を介して対向
した磁石11が回転し、この磁石11と共に回転ブロック9
に固定された複数枚の翼板17により構成された遠心翼18
が、整流板25を構成する円輪板23の下側に於いて、垂直
軸8を中心として回転する。That is, by energizing the motor 14, the output shaft 15 of the motor 14
When the magnet 16 fixed to the rotor is rotated, the magnet 11 opposed to the magnet 16 via the bottom plate 2 is rotated by the magnet coupling action, and the magnet 11 and the rotation block 9 are rotated together.
Centrifugal blade 18 composed of multiple blades 17 fixed to the
On the lower side of the circular plate 23 that constitutes the flow regulating plate 25, it rotates about the vertical axis 8.
モータ14への通電に伴なう遠心翼18の回転により、培養
液を貯溜したガラス容器1の底部に、上記円輪板23の下
面に沿ってガラス筒1の中心寄り部分から外側に向う流
れが惹起され、これに伴なって整流板25を構成する円筒
24の内側に通じる支持枠6の内側の圧力が外側の圧力よ
りも低くなる。Due to the rotation of the centrifugal blades 18 accompanying the energization of the motor 14, the flow toward the outside from the portion near the center of the glass tube 1 along the lower surface of the circular plate 23 to the bottom of the glass container 1 storing the culture solution. And the cylinder that forms the current plate 25 accordingly.
The pressure inside the support frame 6 communicating inside 24 becomes lower than the pressure outside.
この様に遠心翼18の回転に伴なって支持枠6の内外に圧
力差が生じると、この支持枠6の外側に存在する培養液
が支持枠6の内側に流れ込もうとする流れが惹起され、
ガラス筒1内の培養液は支持枠6の内側を流下し、支持
枠6の外周面とガラス筒1の内周面との間の筒状の空間
を上昇しつつガラス筒1内を循環して流れるが、この流
れの途中に存在する支持枠6に形成された多数の小孔
(網目)は、培養液と共にガラス容器1内に投入された
多数の粒状ゲルの粒径(3〜5mm)よりも小さく、培養
液と共に流れようとする各粒状ゲルはこの小孔を通過す
る事は出来ず、支持枠6の外周面に付着したままとな
り、培養液のみが支持枠6を通過しつつ流れる。When a pressure difference is generated between the inside and the outside of the support frame 6 as the centrifugal blade 18 rotates in this way, the culture solution existing outside the support frame 6 is caused to flow into the inside of the support frame 6. Is
The culture solution in the glass tube 1 flows down inside the support frame 6 and circulates in the glass tube 1 while rising in a tubular space between the outer peripheral surface of the support frame 6 and the inner peripheral surface of the glass tube 1. The large number of small holes (mesh) formed in the support frame 6 existing in the middle of this flow, the particle size (3 to 5 mm) of the large number of granular gel put into the glass container 1 together with the culture solution. Each of the granular gels, which are smaller than the above, and cannot flow through the small holes, cannot pass through the small holes, remain attached to the outer peripheral surface of the support frame 6, and only the culture liquid flows while passing through the support frame 6. .
この様に外周面に粒状ゲルが付着した支持枠6を通過し
て流れる培養液中には、前記遠心翼18の直上で整流板を
構成する円筒24の内側位置に設けた気泡ノズル19から酸
素を含まない気体が送り込まれており、この培養液中を
常に嫌気性菌である乳酸菌の醗酵に最適な状態に保って
いる為、上記支持枠6に付着した粒状ゲルに固定された
乳酸菌は、大きな反応速度によって連続的な培養が行な
われて、培養液中の乳酸菌の数が次第に増加する。As described above, in the culture solution flowing through the support frame 6 having the granular gel adhered to the outer peripheral surface, oxygen is supplied from the bubble nozzle 19 provided inside the cylinder 24 constituting the flow straightening plate immediately above the centrifugal blade 18. Since a gas containing no is sent and the culture solution is always kept in an optimum state for fermentation of lactic acid bacteria which are anaerobic bacteria, the lactic acid bacteria fixed to the granular gel attached to the support frame 6 are: Continuous culture is performed with a large reaction rate, and the number of lactic acid bacteria in the culture solution gradually increases.
又、この様な培養装置を使用する事により、乳酸菌を固
定化した粒状ゲルの表面に常に醗酵用原液が流通する
為、醗酵に伴なう反応生成物である乳酸が局部的に濃縮
される事が防止され、乳酸の濃度増加に伴なう乳酸菌の
活性低下を防止出来る。Further, by using such a culture device, since the stock solution for fermentation always flows on the surface of the granular gel on which lactic acid bacteria are immobilized, lactic acid, which is a reaction product associated with fermentation, is locally concentrated. This can prevent the decrease in the activity of lactic acid bacteria due to the increase in the concentration of lactic acid.
更に、支持枠6の外周面に付着する粒状ゲルは、培養装
置の運転時に翼板17によって叩かれる事がない為、培養
装置の運転に伴なって粒状ゲルが破壊される事はない。Further, since the granular gel attached to the outer peripheral surface of the support frame 6 is not hit by the vanes 17 during the operation of the culture device, the granular gel is not destroyed by the operation of the culture device.
この様な固定化された菌体の増殖は、30℃で48時間行な
い、ゲルビーズ中に含まれる乳酸菌の数を108〜109個/m
l迄増やした。The growth of such immobilized cells was carried out at 30 ° C for 48 hours, and the number of lactic acid bacteria contained in the gel beads was 10 8 to 10 9 cells / m 2.
I increased to l.
ハ.製品取り出し 上述の様にしてゲルビーズ中に含まれる乳酸菌の数を10
8〜109個/ml迄増やしたならば、醗酵用原液を30ml/時の
割合で醗酵槽のガラス容器中に送り込みつつ、このガラ
ス容器中から同量の醗酵済の製品取り出しを行なった。C. Product removal As described above, reduce the number of lactic acid bacteria contained in gel beads to 10
When the concentration was increased to 8 to 10 9 cells / ml, the fermented stock solution was fed into the glass container of the fermenter at a rate of 30 ml / hour, and the same amount of fermented product was taken out from the glass container.
この製品取り出しは30日間連続して行ない、取り出した
製品を20代、30代、40代の男女5名ずつ、合計30名に試
飲させた所、各年代に於いて男女の区別なく合格点を得
られた。乳酸菌を加えない単なる林檎果汁との評価に就
いて明確な差異は生じなかったが、乳酸菌を加えたもの
の方が加えないものよりも良いとする者が、逆の者とほ
ぼ同数居り、本発明の方法により造られた乳酸菌飲料が
嗜好の多様化に対応出来るものである事が解った。This product was taken out for 30 consecutive days, and the taken out product was tasted by 5 men and women in their 20s, 30s and 40s, for a total of 30 people. Was obtained. Although there was no clear difference in the evaluation with mere apple juice without addition of lactic acid bacteria, there were almost the same number of those who added lactic acid bacteria as those better than those without added lactic acid bacteria, It was found that the lactic acid bacterium drink produced by the method described above can cope with diversified taste.
又、果汁として林檎果汁以外に、蜜柑果汁、葡萄果汁を
使用し、栄養エキスとして酵母エキス以外に麺汁、穀物
種子胚芽エキスを使用して同様の実験を行なった所、酵
母エキスを使用した場合と同じ結果が得られた。In addition to apple juice as fruit juice, tangerine juice and grape juice were used, and noodle juice and grain seed germ extract were used in the same experiment as yeast extract in addition to yeast extract, where yeast extract was used. The same result was obtained.
更に、醗酵用原液のPH値を上下に変化させて同様の実験
を行なった所、PH値が3.0〜4.5の範囲に在る場合は乳酸
菌飲料の製造を効率良く行なう事が出来たが、PH値が3.
0以下になっても、反対に4.5以上になっても乳酸菌の数
が増えず、効率的な乳酸菌飲料の製造を行なう事が出来
なかった。Furthermore, when the same experiment was performed by changing the PH value of the fermentation stock solution up and down, when the PH value was in the range of 3.0 to 4.5, the lactic acid bacterium beverage could be efficiently produced, but PH The value is 3.
Even if it was 0 or less, or conversely, if it was 4.5 or more, the number of lactic acid bacteria did not increase, and it was not possible to efficiently manufacture a lactic acid bacterium beverage.
c.発明の効果 本発明の乳酸菌飲料の製造方法は以上に述べた通り構成
され実施されるので、従来困難とされていた果汁を含む
乳酸菌飲料の製造を効率良く行なう事が出来、嗜好の多
様化に対応出来るだけでなく、嗜好の変化により消費が
低迷している果物の消費拡大を図る事も出来る。c. Effects of the invention Since the method for producing a lactic acid bacterium beverage of the present invention is configured and carried out as described above, it is possible to efficiently produce a lactic acid bacterium beverage containing fruit juice, which has been considered difficult in the past. Not only can it respond to changes in consumption, but it can also increase consumption of fruits, whose consumption is sluggish due to changes in taste.
図面は本発明の実施に使用される醗酵槽の1例を示す縦
断面図である。 1:ガラス筒、2:底板、3:スタッド、4:蓋板、5:円孔、6:
支持枠、7:ステー、8:垂直軸、9:回転ブロック、10:キ
ャップ、11:磁石、12:基板、13:ブラケット、14:モー
タ、15:出力軸、16:磁石、17:翼板、18:遠心翼、19:気
泡ノズル、20:送気管、21:小孔、22:ノズル部、23:円輪
板、24:円筒、25:整流板。The drawing is a longitudinal sectional view showing an example of a fermenter used for carrying out the present invention. 1: Glass tube, 2: Bottom plate, 3: Studs, 4: Lid plate, 5: Circular hole, 6:
Support frame, 7: stay, 8: vertical axis, 9: rotating block, 10: cap, 11: magnet, 12: board, 13: bracket, 14: motor, 15: output shaft, 16: magnet, 17: vane , 18: Centrifugal blade, 19: Bubble nozzle, 20: Air pipe, 21: Small hole, 22: Nozzle part, 23: Ring plate, 24: Cylinder, 25: Rectifier plate.
Claims (2)
キスの1種又は2種以上を0.05〜1.0%混合し、PH値を
3.0〜4.5とした、果汁を主成分とする混合液を乳酸醗酵
用原液として使用し、この乳酸醗酵用原液を、乳酸菌に
接触させる事で醗酵させる乳酸菌飲料の製造方法。1. A PH value is obtained by mixing one or more of yeast extract, noodle juice, rice germ extract, and malt extract in an amount of 0.05 to 1.0%.
A method for producing a lactic acid bacterium beverage, wherein a mixed solution containing fruit juice as a main component, which is 3.0 to 4.5, is used as a stock solution for lactic acid fermentation, and the stock solution for lactic acid fermentation is fermented by contact with lactic acid bacteria.
キスの1種又は2種以上を0.05〜1.0%混合し、PH値を
3.0〜4.5とした、果汁を主成分とする混合液を乳酸醗酵
用原液とし、この醗酵用原液を乳酸菌を108〜109個/ml
の割合で包括固定化したゲルと共に、下端開口を底板に
よって塞がれ、上端開口部に開閉自在な蓋板を設けたガ
ラス筒と、ガラス筒の内側にこのガラス筒とほぼ同心に
設けられた水平方向の円輪板の内周縁に、この内周縁か
ら上方に立ち上る円筒を設けた整流板と、この整流板の
円筒に下端部を嵌合させて固定した多数の小孔を有する
支持枠と、上記底板の上側に設けれモータにより竪軸を
中心として上記整流板を構成する円輪板の下側に於いて
回転駆動される遠心翼とから成る培養装置に投入し、遠
心翼を回転させて、支持枠の外周面に付着したゲルの間
に乳酸醗酵用原液を流す乳酸菌飲料の製造方法。2. A PH value is obtained by mixing one or more of yeast extract, noodle juice, rice germ extract and malt extract in an amount of 0.05 to 1.0%.
A mixed solution containing 3.0 to 4.5 as the main component of fruit juice is used as a stock solution for lactic acid fermentation, and the stock solution for fermentation is 10 8 to 10 9 cells / ml of lactic acid bacteria.
With the gel fixed comprehensively at the ratio of, the lower end opening was closed by the bottom plate, the upper end opening was provided with a lid plate that could be opened and closed, and the glass tube was provided inside the glass tube and approximately concentrically with this glass tube. A straightening plate having a cylinder that rises upward from the inner circumferential edge of the horizontal circular plate, and a supporting frame having a large number of small holes fixed by fitting the lower end portion to the cylinder of the straightening plate. , Placed on an upper side of the bottom plate by a motor, and put into a culture device consisting of a centrifugal blade that is driven to rotate on the lower side of a circular plate that constitutes the straightening plate around the vertical axis, and the centrifugal blade is rotated. And a method for producing a lactic acid bacterium beverage in which a stock solution for lactic acid fermentation is caused to flow between gels attached to the outer peripheral surface of a support frame.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP61053683A JPH0751042B2 (en) | 1986-03-13 | 1986-03-13 | Method for producing lactic acid bacteria beverage |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP61053683A JPH0751042B2 (en) | 1986-03-13 | 1986-03-13 | Method for producing lactic acid bacteria beverage |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS62210948A JPS62210948A (en) | 1987-09-17 |
| JPH0751042B2 true JPH0751042B2 (en) | 1995-06-05 |
Family
ID=12949615
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP61053683A Expired - Lifetime JPH0751042B2 (en) | 1986-03-13 | 1986-03-13 | Method for producing lactic acid bacteria beverage |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0751042B2 (en) |
Families Citing this family (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2641142B2 (en) * | 1987-12-30 | 1997-08-13 | カゴメ株式会社 | Lactic acid fermented beverage and method for producing the same |
| JPH02150246A (en) * | 1988-11-30 | 1990-06-08 | Kenji Takeda | Fermented food and preparation thereof |
| JP2761641B2 (en) * | 1988-12-09 | 1998-06-04 | 日本製粉株式会社 | Fermented milk product and method for producing the same |
| KR20020073851A (en) * | 2001-03-16 | 2002-09-28 | 최원균 | rice germ beverage and method for making the same |
| US7674489B2 (en) * | 2005-09-30 | 2010-03-09 | Kraft Foods Global Brands Llc | Fresh cheese products containing biogenerated flavor components and methods for producing |
| CN118044577A (en) * | 2024-03-14 | 2024-05-17 | 保利国氏生态农业开发河北有限公司 | Beverage and its processing method and application as health beverage |
-
1986
- 1986-03-13 JP JP61053683A patent/JPH0751042B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPS62210948A (en) | 1987-09-17 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US4808419A (en) | Automated method for a semi-solid fermentation used in the production of ancient quality rice vinegar and/or rice wine | |
| TWI629354B (en) | Active fermentation process and fermented liquid and drinks made by using the same | |
| CN108841758A (en) | Corynebacterium glutamicum mutant and its application in L-Leu production | |
| JPH0751042B2 (en) | Method for producing lactic acid bacteria beverage | |
| CN101220331A (en) | A kind of preparation method of double-bacteria fermented red raspberry whole juice fruit wine | |
| CN101455355A (en) | Health-care beverage with sobering-up and antialcoholism function and preparation method thereof | |
| CN113100429A (en) | Process for producing high-nucleotide super-fresh soy sauce | |
| CN107549566A (en) | A kind of Kiwi berry solid beverage ferment and preparation method thereof | |
| CN108315230A (en) | Reactor and the method for preparing yeast culture using reactor | |
| CN106538915B (en) | Method for improving related enzyme activity by fermenting fruit and vegetable juice with probiotics | |
| CN119279187A (en) | Blueberry essence and preparation method thereof | |
| NO154349B (en) | PROCEDURE FOR MANUFACTURING NUTRITIONAL PROTEINS BY CULTIVATING A SUSPENSION OF THE TRICHODERMA | |
| CN208883870U (en) | Reactor | |
| CN208200973U (en) | A production equipment for continuous supply of logarithmic growth phase bacterial liquid | |
| CN108913420A (en) | A kind of fragrance high-fidelity type Fragrant fruit wine and its brewing method | |
| KR101059839B1 (en) | Lactic Acid Bacteria Fermented Peach Enzyme Solution | |
| CN109652251A (en) | A kind of wheat beer and preparation method thereof of fragrance style | |
| CN104593217B (en) | A kind of pomegranate fruit vinegar and brewing method thereof | |
| CN1067541C (en) | Lactic acid fermented apple beverage | |
| JP2724151B2 (en) | Culture method of plant cultured cells | |
| CN115316474A (en) | Preparation method of milk-containing cold-extraction coffee | |
| JPS61135540A (en) | Production of fruit kefir | |
| CN108611249A (en) | A method of cucumber vinegar is made using micro-aerobe fermentation technology | |
| JPH0240316B2 (en) | BAIYOSOCHI | |
| CN116616410B (en) | Milk pudding and preparation method thereof |