JPH0662879A - Production of lysine - Google Patents
Production of lysineInfo
- Publication number
- JPH0662879A JPH0662879A JP21490492A JP21490492A JPH0662879A JP H0662879 A JPH0662879 A JP H0662879A JP 21490492 A JP21490492 A JP 21490492A JP 21490492 A JP21490492 A JP 21490492A JP H0662879 A JPH0662879 A JP H0662879A
- Authority
- JP
- Japan
- Prior art keywords
- lysine
- juice
- fermentation
- raw material
- liquid
- 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.)
- Withdrawn
Links
- KDXKERNSBIXSRK-UHFFFAOYSA-N Lysine Natural products NCCCCC(N)C(O)=O KDXKERNSBIXSRK-UHFFFAOYSA-N 0.000 title claims abstract description 22
- 239000004472 Lysine Substances 0.000 title claims abstract description 22
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 12
- 238000000855 fermentation Methods 0.000 claims abstract description 25
- 230000004151 fermentation Effects 0.000 claims abstract description 25
- 239000007788 liquid Substances 0.000 claims abstract description 13
- 238000000034 method Methods 0.000 claims abstract description 10
- 238000000926 separation method Methods 0.000 claims abstract description 8
- 238000000108 ultra-filtration Methods 0.000 claims abstract description 7
- 239000007787 solid Substances 0.000 claims abstract description 6
- 235000015203 fruit juice Nutrition 0.000 claims description 4
- 239000000356 contaminant Substances 0.000 claims 1
- 235000011389 fruit/vegetable juice Nutrition 0.000 abstract description 17
- 239000002994 raw material Substances 0.000 abstract description 9
- 235000013399 edible fruits Nutrition 0.000 abstract description 8
- 244000052616 bacterial pathogen Species 0.000 abstract 1
- 239000000725 suspension Substances 0.000 abstract 1
- 241000220225 Malus Species 0.000 description 9
- 235000015197 apple juice Nutrition 0.000 description 6
- 241000894006 Bacteria Species 0.000 description 4
- 238000001035 drying Methods 0.000 description 4
- 238000003825 pressing Methods 0.000 description 4
- 230000001954 sterilising effect Effects 0.000 description 4
- WQZGKKKJIJFFOK-GASJEMHNSA-N Glucose Natural products OC[C@H]1OC(O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-GASJEMHNSA-N 0.000 description 3
- 239000008103 glucose Substances 0.000 description 3
- 239000002054 inoculum Substances 0.000 description 3
- 238000004659 sterilization and disinfection Methods 0.000 description 3
- 235000000346 sugar Nutrition 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 235000021016 apples Nutrition 0.000 description 2
- 238000004925 denaturation Methods 0.000 description 2
- 230000036425 denaturation Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 235000012054 meals Nutrition 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 241001672694 Citrus reticulata Species 0.000 description 1
- 241000219094 Vitaceae Species 0.000 description 1
- 150000001413 amino acids Chemical class 0.000 description 1
- 239000002518 antifoaming agent Substances 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 238000005119 centrifugation Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000005187 foaming Methods 0.000 description 1
- 235000021021 grapes Nutrition 0.000 description 1
- 244000144972 livestock Species 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 235000015097 nutrients Nutrition 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 238000010025 steaming Methods 0.000 description 1
- 150000008163 sugars Chemical class 0.000 description 1
- 238000009423 ventilation Methods 0.000 description 1
Landscapes
- Preparation Of Compounds By Using Micro-Organisms (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は糖分を含む果物、例えば
リンゴ、ミカン、ブドウなど各種の果物の果汁液を搾汁
した搾汁粕の2次搾汁液を原料として、発酵法によって
リジンを製造する方法に関する。BACKGROUND OF THE INVENTION The present invention uses a secondary squeezing liquid of a squeezed lees obtained by squeezing juices of fruits containing sugar, such as apples, mandarins, and grapes, to produce lysine by fermentation. On how to do.
【0002】[0002]
【従来の技術】従来、リジン発酵原料としてはグルコー
スを含む合成培地が用いられており、果物の2次搾汁液
を原料としてリジン発酵を実施した例はない。図3に、
従来のリンゴ果汁の製造工程を示す。図3において、1
はリンゴ、2は搾汁工程、3は固液分離工程、4はリン
ゴ果汁、5はリンゴ搾汁粕、6は2次圧搾工程、7は乾
燥工程、8は飼料、9は2次搾汁液を示す。図3に示す
ように、固液分離工程3で分離されたリンゴ果汁4と、
リンゴ搾汁粕5を2次圧搾工程6で得られた2次圧搾粕
を乾燥工程7で乾燥した飼料8は製品となっていたが、
2次圧搾汁液9は廃棄されていた。2. Description of the Related Art Conventionally, a synthetic medium containing glucose has been used as a raw material for lysine fermentation, and there is no example in which lysine fermentation was carried out using a secondary juice of fruit as a raw material. In Figure 3,
The manufacturing process of the conventional apple juice is shown. In FIG. 3, 1
Is an apple, 2 is a squeezing process, 3 is a solid-liquid separation process, 4 is an apple juice, 5 is an apple squeezing lees, 6 is a secondary pressing process, 7 is a drying process, 8 is a feed, 9 is a secondary squeezing liquid. Indicates. As shown in FIG. 3, the apple juice 4 separated in the solid-liquid separation step 3,
The feed 8 obtained by drying the secondary pressed meal obtained from the apple pressed meal 5 in the secondary pressing step 6 in the drying step 7 was a product,
The secondary pressed juice 9 was discarded.
【0003】[0003]
【発明が解決しようとする課題】リジン発酵において、
グルコースを含む合成培地を用いることはコストが高く
実用的ではない。また、従来例えばリンゴ果汁製造工程
ではリンゴ2次搾汁液は廃棄されていたが、この2次搾
汁液中には糖分、窒素分などの栄養源が含まれており、
十分利用価値がある。しかしパルプなどの浮遊固形物を
含むことから従来の図4に示す発酵工程において殺菌の
際に、こげつくなどの不都合が生じるし、殺菌の熱によ
り2次搾汁液中のアミノ酸、糖分がメイラード反応によ
って分解するといった問題点がある。図4において、2
1は培地調整槽、24は主発酵槽、25は種菌培養槽、
26はpHコントローラ、27は消泡コントローラ、2
8は除去フィルタ、29はブロワ、30は殺菌装置を示
す。[Problems to be Solved by the Invention] In lysine fermentation,
The use of synthetic medium containing glucose is costly and impractical. Further, conventionally, for example, apple secondary juice is discarded in the apple juice manufacturing process, but this secondary juice contains nutrients such as sugar and nitrogen.
It is well worth using. However, since suspended solids such as pulp are included, inconvenience such as sticking occurs during sterilization in the conventional fermentation process shown in Fig. 4, and the heat of sterilization causes the amino acids and sugars in the secondary juice to react with the Maillard reaction. There is a problem that it is decomposed by. In FIG. 4, 2
1 is a medium adjusting tank, 24 is a main fermentation tank, 25 is an inoculum culture tank,
26 is a pH controller, 27 is a defoaming controller, 2
8 is a removal filter, 29 is a blower, and 30 is a sterilizer.
【0004】本発明は上記技術水準に鑑み、上述したよ
うな不具合のない果物の二次圧搾汁を原料として発酵法
によってリジンを製造し得る方法を提供しようとするも
のである。In view of the above-mentioned state of the art, the present invention aims to provide a method for producing lysine by a fermentation method using the secondary squeezed juice of fruit free from the above-mentioned problems.
【0005】[0005]
【課題を解決するための手段】本発明は果物の果汁製造
工程で発生する2次搾汁液を遠心分離操作によりパル
プ、固形浮遊物を除去し、さらに限外ろ過操作により雑
菌を除去した後、得られる液を原料としてリジン発酵法
にかけることを特徴とするリジンの製造方法である。[Means for Solving the Problems] According to the present invention, pulp and solid suspended matter are removed from a secondary squeezed liquid generated in a fruit juice production process of a fruit by centrifugal separation operation, and then bacteria are removed by an ultrafiltration operation. A method for producing lysine, which comprises subjecting the obtained liquid to a lysine fermentation method as a raw material.
【0006】[0006]
【作用】リンゴなどの果物の2次搾汁液を遠心分離する
ことによって、パルプなどの浮遊固形分を除去し、さら
に限外ろ過を用いることにより雑菌の除去が可能とな
り、蒸煮殺菌する必要がなくなり、熱による変性を防ぐ
ことが可能となる。また、遠心分離により浮遊固形分を
除去することによって、限外ろ過の時間を短縮すること
が可能となる。[Function] By centrifuging the secondary juice of fruits such as apples, suspended solids such as pulp are removed, and by using ultrafiltration, various bacteria can be removed, and it is not necessary to sterilize by steaming. It is possible to prevent denaturation due to heat. Also, by removing the suspended solids by centrifugation, the time for ultrafiltration can be shortened.
【0007】[0007]
【実施例】本発明の一実施例を図1によって説明する。
図1において、リンゴ原料1は搾汁工程2によって搾汁
され、固液分離工程3を経てリンゴ果汁4とリンゴ搾汁
粕5に分けられる。リンゴ搾汁粕5はさらに圧搾工程
6、乾燥工程7を経て飼料8となる。また、圧搾工程6
で得られた2次搾汁液9を発酵原料としてリジン発酵工
程10でリジンを生産し、分離精製工程11で精製した
後、飼料8に添加する。DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of the present invention will be described with reference to FIG.
In FIG. 1, an apple raw material 1 is squeezed in a squeezing step 2, and is separated into an apple juice 4 and an apple squeeze cake 5 through a solid-liquid separation step 3. The apple juice dregs 5 becomes a feed 8 through a pressing process 6 and a drying process 7. Also, the pressing step 6
Lysine is produced in the lysine fermentation step 10 by using the secondary juice 9 obtained in step 1 as a fermentation raw material, purified in the separation and purification step 11, and then added to the feed 8.
【0008】リジン発酵工程10では、図2に示すよう
に、培地調整槽21により前記リンゴ2次搾汁液9のp
Hを7.0に調整し、遠心分離機22によりパルプを、
限外ろ過装置23により雑菌を除去し、主発酵槽24へ
培地として送入する。主発酵槽24に送入された培地を
冷却した後、種菌培養槽25であらかじめ馴養しておい
た種菌を添加し発酵を開始する。発酵中のpHはpHコ
ントローラ26によってpH7.0に調整し、激しく発
泡した場合は消泡コントローラ27によって消泡剤を添
加する。通気はブロワ29から空気を送り、除菌フィル
タ28によって除菌を行う。発酵終了後発酵液は全量引
き抜き分離精製工程へ送る。全量引き抜いた後、主発酵
槽24を洗浄し、次の発酵の準備をする。In the lysine fermentation step 10, as shown in FIG. 2, p of the apple secondary juice 9 is stored in the medium adjusting tank 21.
H was adjusted to 7.0 and pulp was separated by the centrifuge 22.
The bacteria are removed by the ultrafiltration device 23 and fed into the main fermentation tank 24 as a medium. After cooling the medium fed into the main fermentation tank 24, the inoculum preconditioned in the inoculum culture tank 25 is added to start fermentation. The pH during the fermentation is adjusted to pH 7.0 by the pH controller 26, and in the case of vigorous foaming, the defoaming controller 27 adds an antifoaming agent. For ventilation, air is sent from a blower 29, and a sterilization filter 28 sterilizes the bacteria. After the fermentation is completed, the entire fermentation liquid is drawn and sent to the separation and purification process. After withdrawing the entire amount, the main fermenter 24 is washed to prepare for the next fermentation.
【0009】[0009]
【発明の効果】本発明により、従来のグルコースを含む
合成培地を原料としたリジン発酵に比べてリジン生産コ
ストを低減することが可能となり、また従来廃棄されて
いた果物の2次搾汁液を原料とすることにより、果汁製
造工程の副生物である果汁搾汁粕飼料に生産されたリジ
ンを添加することができ、より付加価値の高い家畜飼料
とすることができる。さらに、限外ろ過を用いて除菌す
ることにより、果汁の2次搾汁液の熱変性を防ぐことが
可能となる。Industrial Applicability According to the present invention, it becomes possible to reduce the lysine production cost as compared with the conventional lysine fermentation using a synthetic medium containing glucose as a raw material, and the conventionally used secondary juice of fruit is used as a raw material. By the above, lysine produced can be added to the juice juice-meal feed, which is a by-product of the fruit juice production process, and livestock feed with higher added value can be obtained. Furthermore, by sterilizing using ultrafiltration, it becomes possible to prevent thermal denaturation of the secondary juice of juice.
【図1】本発明の一実施例のフローの説明図。FIG. 1 is an explanatory diagram of a flow of an embodiment of the present invention.
【図2】図1のフローのうちのリジン発酵法のフローの
説明図。FIG. 2 is an explanatory diagram of a flow of a lysine fermentation method in the flow of FIG.
【図3】従来の果汁の製造工程の一態様のフローの説明
図。FIG. 3 is an explanatory view of a flow of one aspect of a conventional fruit juice manufacturing process.
【図4】図3のフローの2次搾汁液のリジン発酵法のフ
ローの説明図。FIG. 4 is an explanatory view of a flow of the lysine fermentation method of the secondary juice of the flow of FIG.
Claims (1)
液を遠心分離操作によりパルプ、固形浮遊物を除去し、
さらに限外ろ過操作により雑菌を除去した後、得られる
液を原料としてリジン発酵法にかけることを特徴とする
リジンの製造方法。1. A pulp and a solid suspended matter are removed from a secondary squeezed liquid generated in a fruit juice production process by a centrifugal separation operation,
Further, a method for producing lysine, which comprises subjecting the obtained liquid to a lysine fermentation method after removing contaminants by an ultrafiltration operation.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP21490492A JPH0662879A (en) | 1992-08-12 | 1992-08-12 | Production of lysine |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP21490492A JPH0662879A (en) | 1992-08-12 | 1992-08-12 | Production of lysine |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH0662879A true JPH0662879A (en) | 1994-03-08 |
Family
ID=16663492
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP21490492A Withdrawn JPH0662879A (en) | 1992-08-12 | 1992-08-12 | Production of lysine |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0662879A (en) |
-
1992
- 1992-08-12 JP JP21490492A patent/JPH0662879A/en not_active Withdrawn
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US4794013A (en) | Process for extracting of liquid from a residual substance | |
HUT50017A (en) | Method and apparatus for treating fruit and vegetable sorts particularly for producing juices | |
WO2012138625A2 (en) | System and method for preparing a shelf-stable botanical extract | |
CN105062860A (en) | Gooseberry fruit vinegar and brewage method thereof | |
US5014612A (en) | Process for the production of dealcoholized beverages, as well as a unit and device for performing the process | |
JPH0662879A (en) | Production of lysine | |
EP0137671A1 (en) | Production of juice concentrates | |
CN108070497A (en) | A kind of brewing method of blueberry fruit wine | |
US5090306A (en) | Unit for the preparation of fruits, berries and/or vegetables for the extraction of liquid raw products | |
US3968257A (en) | Processes for the production of protein-containing nutriments and fodders | |
US3795521A (en) | Viscosity controlled pectinolytic enzyme addition to fruit and vegetable juice | |
AU634597B2 (en) | Method for production of a fruit or vegetable juice concentrate | |
US2442789A (en) | Conversion of wheat starch | |
US5731018A (en) | Method for production of a fruit or vegetable juice concentrate | |
CN113693183A (en) | Preparation process of alcohol-free pitaya enzyme bubble beverage | |
US5013570A (en) | Method of producing odorless ripe juice of houttuynia cordata | |
RU2080801C1 (en) | Method for clarifying raw juice from grape, berry and other fruits, vegetables or seeds, and installation for its realization | |
HU219989B (en) | Process for preparing pressed, optionally purified fruit and vegetable juices | |
CN110468020A (en) | A kind of fruit vinegar production | |
CN1127611A (en) | Blue spirulina liquid beverage and preparation method thereof | |
CN1191692A (en) | Juice preparing technology | |
RU2039803C1 (en) | Method for production of grape vitamin elixir | |
RU92002607A (en) | METHOD OF MANUFACTURE OF PECTIN-CONTAINING SEMI-FINISHED PRODUCTS | |
CN113862101A (en) | Preparation method of composite biological enzyme fruit wine | |
US863085A (en) | Manufacture of beverages. |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
A300 | Withdrawal of application because of no request for examination |
Free format text: JAPANESE INTERMEDIATE CODE: A300 Effective date: 19991102 |