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JPH0638760B2 - Method for producing sugar-dense product for fermentation - Google Patents
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JPH0638760B2 - Method for producing sugar-dense product for fermentation - Google Patents

Method for producing sugar-dense product for fermentation

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Publication number
JPH0638760B2
JPH0638760B2 JP58082124A JP8212483A JPH0638760B2 JP H0638760 B2 JPH0638760 B2 JP H0638760B2 JP 58082124 A JP58082124 A JP 58082124A JP 8212483 A JP8212483 A JP 8212483A JP H0638760 B2 JPH0638760 B2 JP H0638760B2
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Japan
Prior art keywords
molasses
fermentation
treated
electrodialysis
raw material
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
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JP58082124A
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Japanese (ja)
Other versions
JPS59205950A (en
Inventor
良介 遠山
俊了 竹崎
和也 藤沢
Original Assignee
台糖株式会社
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Priority to JP58082124A priority Critical patent/JPH0638760B2/en
Publication of JPS59205950A publication Critical patent/JPS59205950A/en
Publication of JPH0638760B2 publication Critical patent/JPH0638760B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Description

【発明の詳細な説明】 本発明は発酵原料として利用される醗酵用糖蜜製品の製
造方法に関するものである。更に詳しくは糖蜜を中性膜
と陽イオン交換膜とを組み合せた電気透析装置で処理す
る事により糖蜜中に含まれている陽イオン及び陰イオン
等の発酵阻害物質を除去した後に該糖蜜を発酵原料とし
て使用する糖蜜の利用に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing a molasses product for fermentation used as a fermentation raw material. More specifically, molasses is treated with an electrodialysis device that combines a neutral membrane and a cation exchange membrane to remove fermentation inhibitors such as cations and anions contained in molasses and then ferment the molasses. It relates to the use of molasses used as a raw material.

一般的に糖蜜は発酵原料として最も多量に使用されてい
る。しかし乍ら従来から糖蜜中の発酵阻害物質が原因と
なり発酵生産能が低下する事に関して、多くの知見がが
得られている。其の為、糖蜜を種々の方法で処理した後
に発酵原料として使用する事が行われて来たが、歩留及
びコスト面等より適当な法が発明されていなかった。其
処で従来法と異つた方法で処理した糖蜜を発酵原料とし
て使用する事により発酵生産能を向上し、発酵生産物精
製時のトラブルを軽減する事が望まれていた。
Molasses is generally used in the largest amount as a fermentation raw material. However, much knowledge has been obtained from the past regarding the fact that fermentation inhibitory substances in molasses cause the decrease in fermentation productivity. Therefore, it has been practiced to use molasses as a raw material for fermentation after treating it with various methods, but an appropriate method has not been invented in terms of yield and cost. Therefore, it has been desired that the molasses treated by a method different from the conventional method is used as a fermentation raw material to improve the fermentation productivity and reduce troubles during the purification of the fermentation product.

本発明者等は既に糖液の脱塩に関して「ポリビニールア
ルコール系隔膜を用いた電気透析による糖液の脱塩精製
法」(特許第835862号、特公昭51−9016号
公報)及び「糖液精製法」(特許第1014134号、
特公昭54−31050号公報)の発明を完成している
が今度其れ等の一利用分野として本発明を完成したもの
である。即ち本発明者等は、陽イオン交換膜と中性膜を
交互に複数組合わせた多室構造の電気透析装置を用いて
原料糖蜜を電気透析し、K、Ca、Na、Mg等の陽イ
オンやClやSO等の陰イオンを糖蜜より除去して原
料糖蜜中の全灰分量を約1/2〜約1/4の範囲内に低下させ
た後、該糖蜜を主に炭素源としてアルコール醗酵及びア
ミノ醗酵を行うと、発酵生産能の向上、発酵生産物精製
時の操作の容易さ、加熱時のスケールの減少等の利点を
見出し本発明を完成したものである。
The inventors of the present invention have already referred to a desalting and refining method of a sugar solution by electrodialysis using a polyvinyl alcohol-based diaphragm (Patent No. 835862, Japanese Patent Publication No. 51-9016) and "Sugar solution". Purification method "(Patent No. 1014134,
The invention of Japanese Examined Patent Publication No. 54-31050) has been completed, but the present invention has now been completed as one field of application. That is, the present inventors electrodialyze raw molasses by using an electrodialyzer having a multi-chamber structure in which a plurality of cation exchange membranes and neutral membranes are alternately combined, and cations such as K, Ca, Na, and Mg. After removing the anions such as Cl, SO 4 and the like from the molasses to reduce the total ash content in the raw molasses to within the range of about 1/2 to about 1/4, the molasses is mainly used as a carbon source for alcohol. When fermentation and amino fermentation are carried out, the present invention has been completed by finding advantages such as improvement of fermentation productivity, ease of operation during purification of fermentation products, and reduction of scale during heating.

さて糖蜜中に含有されている塩類濃度が高くなると発酵
阻害作用が有る事は多数の報告に有るが、糖蜜中の塩類
等を除去した後に発酵原料として使用すると工業的には
コスト面に於て採算の合うものではなかつた。例えば陽
イオン及び陰イオン交換樹脂又は陽イオン及び陰イオン
交換膜による電気透析等の採用には何れも欠点、特に経
済上の欠点があり発酵原料に供されるための糖蜜製微の
実用化は困難であつた。
It has been reported in many reports that when the concentration of salts contained in molasses is high, it has a fermentation inhibitory effect.However, if the salt is removed from molasses and then used as a fermentation raw material, it is industrially costly. It wasn't profitable. For example, the adoption of electrodialysis or the like using a cation and anion exchange resin or a cation and anion exchange membrane has drawbacks, especially economical disadvantages, and practical application of molasses for use as a fermentation raw material is not possible. It was difficult.

本発明者等が用いた中性膜及び陽イオン交換膜による電
気透析で、沖蝿産糖蜜は70%強の灰分が除去され、該
糖蜜を主に炭素源として使用したエタノール発酵に於い
ては処理前糖蜜に較べて発酵収率が60%強にまで上昇
した。又、糖蜜を発酵原料とするアミノ酸発酵の代表例
であるL−リジン発酵に於いては沖蝿産糖蜜、フイリピ
ン産糖窒の何れの場合に於いても、処理前糖蜜に較べて
最終L−リジン濃度各々50%強及び60%強にまで生
産能が上昇した。此の様に、中性膜と陽イオン交換膜と
を使用する電気透析により処理した糖蜜を、主に炭素源
として使用する事により発酵生産能を向上する事が出来
た。更に処理糖蜜は多くの陽イオン、陰イオンが除去さ
れる為、一般的に行われている様に、同じ全糖濃度で糖
蜜を仕込んだ場合、処理前糖蜜に比して処理糖蜜を使用
した方が灰分が少くブリツクス度も低くなる。従つて培
養液の粘度、比重、浸透圧等も低下し発酵時及び発酵生
産物精製時の操作が容易になり更に灰分が原因となる滅
菌等の加熱時のスケール発生が軽減する利点が見出され
たものである。
By electrodialysis using a neutral membrane and a cation exchange membrane used by the present inventors, 70% or more of ash content in Oki fly molasses was removed, and in ethanol fermentation using the molasses mainly as a carbon source, The fermentation yield increased to more than 60% as compared with the untreated molasses. In addition, in the case of L-lysine fermentation, which is a typical example of amino acid fermentation using molasses as a fermentation raw material, in both cases of molasses produced from Oki fly and molasses produced from filipin, the final L- The productivity increased to lysine concentrations of over 50% and over 60%, respectively. As described above, the fermentation productivity could be improved by mainly using the molasses treated by electrodialysis using the neutral membrane and the cation exchange membrane as the carbon source. Furthermore, since many cations and anions are removed from the treated molasses, when molasses was charged at the same total sugar concentration, treated molasses was used as compared to the untreated molasses, as is generally done. The lower the ash content, the lower the brixiness. Consequently, the viscosity, specific gravity, osmotic pressure, etc. of the culture broth are reduced, facilitating the operation during fermentation and refining the fermentation products, and finding the advantage that scale generation during heating such as sterilization due to ash content is reduced. It was done.

実施例1 沖蝿産原糖蜜を電気透析する事により得られた糖蜜をエ
タノール発酵の原料として使用した例を以下に示す。
Example 1 An example in which molasses obtained by electrodialyzing raw molasses produced in Oki fly was used as a raw material for ethanol fermentation is shown below.

処理糖蜜の調整 ブリツクス50に調整した沖蝿産糖蜜8.0を有効膜
面積0.775dm2の中性膜(台糖株式会社製品,商標
名:台糖N−4膜)と陽イオン交換膜(旭化成株式会社
製品,商標名:アシプレツクスCK−1)とを交互に2
0枚ずつ0.75mm間隔で支持枠にセツトされた電気透
析装置で回分式により処理した。運転条件はセル電圧
2.0V、平均電流密度43Amp/dm2、流量70/h
r、電気透析時間は6時間である。電気透析後の糖蜜を
濃縮し処理糖蜜とした。
Preparation of treated molasses Molasses 8.0 produced in Okibae adjusted to Brix 50 is an effective membrane area of 0.775 dm 2 neutral membrane (product of Taito Corporation, trade name: Taito N-4 membrane) and cation exchange membrane (Asahi Kasei). Co., Ltd., trade name: Aciplex CK-1) and 2 alternately
It was treated batchwise with an electrodialyzer set on a support frame at intervals of 0.75 mm, 0 sheet each. Operating conditions are cell voltage 2.0V, average current density 43Amp / dm 2 , flow rate 70 / h
r, electrodialysis time is 6 hours. The molasses after electrodialysis was concentrated to obtain treated molasses.

沖蝿産処理糖蜜と処理前糖蜜の分析値を第1表に一括表
示示した。但し百分率及びppmは重量基準で示される。
Table 1 shows the analytical values of the molasses produced by Oki fly and the molasses before treatment. However, percentages and ppm are shown on a weight basis.

発酵試験 使用菌株はサツカロミセス セレビジエ(Saccharomyce
s cerevisiae)協会7号 64C〔醸造協会提供〕で
ある。使用した培地は次の通りである。
Fermentation test The strain used is Saccharomyces cerevisiae.
cerevisiae) Association No. 7 64C (provided by the Brewing Society). The medium used is as follows.

保存スラント(酵母エキス1%,ポリペプトン(和光純
薬株式会社製品)2%,寒天1.5%)、前培養培地
(酵母エキス1%,ポリペプトン2%,グルコース5
%)、及び本培養培地〔糖蜜(28%全糖、即ちこの培
地中に全糖分として28%を含有する糖蜜)、硫安2
%〕。
Preserved slant (1% yeast extract, 2% polypeptone (product of Wako Pure Chemical Industries, Ltd.), 1.5% agar), preculture medium (1% yeast extract, 2% polypeptone, 5 glucose)
%), And the main culture medium [molasses (28% total sugar, that is, molasses containing 28% as total sugar in this medium), ammonium sulfate 2
%].

前培養は500ml三角フラスコに250mlの前培養培地
を入れ殺菌後に保存スラントから1白金耳植菌し回転振
盪機(ロータリーシエーカー)で30℃に20時間培養
した。本培養は10容の壜培養器(ジヤーフアメン
タ)に本培養培地を4.5仕込み前培養液50mlを植
菌し30℃、200ppmの条件で6日間培養した。発酵
試験は(a)処理糖蜜のみ;(b)処理糖蜜9部及び処理前糖
蜜1部の混合糖蜜;(c)処理糖蜜8部及び処理前糖蜜2
部の混合糖蜜;及び(d)処理前糖蜜のみの以上4種類の
糖蜜を用いた。
For pre-culturing, 250 ml of pre-culture medium was put into a 500-ml Erlenmeyer flask, and after sterilization, 1 platinum loop was inoculated from the preserved slant and cultured at 30 ° C. for 20 hours on a rotary shaker (rotary shaker). For the main culture, 4.5 volumes of the main culture medium was charged into a 10-volume bottle incubator (Jahuamenta), 50 ml of the preculture medium was inoculated, and the cells were cultured at 30 ° C. and 200 ppm for 6 days. Fermentation test is (a) treated molasses only; (b) mixed molasses containing 9 parts treated molasses and 1 part untreated molasses; (c) 8 parts treated molasses and 2 molasses before treatment
The above-mentioned four types of molasses were used.

発酵試験の結果を第2表に一括表示した。The results of the fermentation test are collectively shown in Table 2.

実施例2 沖蝿産原糖蜜を電気透析する事により得られた糖蜜をL
−リジン発酵の原料として使用した例を以下に示す。
Example 2 L molasses obtained by electrodialyzing raw molasses produced in Oki fly
-The example used as a raw material of lysine fermentation is shown below.

処理糖蜜の調整 ブリツクス50に調整した沖蝿産糖蜜9.5を実施例
1に使用したものと同じ透析装置で処理した。運転条件
はセル電圧2.0V、平均電流密度4.39Amp/dm2
流量70/hr、電気透析時間は7時間である。電気透
析後に濃縮して処理糖蜜とした。
Preparation of Treated Molasses Molasses 9.5 produced in Okibae adjusted to Brix 50 was treated with the same dialyzer as that used in Example 1. Operating conditions are cell voltage 2.0V, average current density 4.39Amp / dm 2 ,
The flow rate is 70 / hr and the electrodialysis time is 7 hours. After electrodialysis, it was concentrated to give treated molasses.

沖蝿産処理糖蜜及び処理前糖蜜の分析値を第3表に一括
表示した。
Table 3 collectively shows the analytical values of the molasses produced by Oki fly and the molasses before treatment.

発酵試験 使用菌株はコリネバクテリウム グルタミクム(Coryne
bacterium glutamicum)ATCC13280である。使用した培
地は次の通りである。保存スラント(肉エキス10g,
ポリペプトン10g、NaCl5g、寒天1.5%、pH7.
0)、前培養培地(グルコース20g、酵母エキス1
g,、NZ−Amine(和光純薬株式会社製品の商標名)6
g、NH4Clの4g、KH2PO4の5g、Na2HPO4・12H2Oの1
5g、MgSO4・7H2Oの0.25g、FeSO4・7H2Oの0.0
1g、MnSO4・4H2Oの0.01g、脱イオン水1、pH
7.0)本培養培地〔糖蜜50g全糖(全糖として50g
を含有する糖蜜)、NZ−Amine 15g、NH4Cl10g、
脱イオン水で1に調整)、及び添加培地(糖蜜500
g全糖、NH4Clの150g、脱イオン水で1.5に調
整)。前培養は500ml坂口フラスコに前培養培地10
0mlを仕込み殺菌後に保スラントから一白金耳植菌し3
0℃で22時間往復振盪(振幅4cm,135回/分)培
養することにより行われた。本培養は10容ジヤーフ
アメンタに本培養培地3.0を仕込み殺菌後に500ml
の前培養液に植菌して行われた。温度は30℃、回転数
を300rpm、通気量を1vvm、pHを5N・NaOHで6.8
〜7.0に制御した。消泡剤としてはアデカノールLG
109(旭電化株式会社製品の商標名)を使用した。培
養開始約8時間の後に定常期手前で全糖濃度10%、Na
4Cl3%となる様に補糖液1.5を加えた。分析方法
としては菌体濃度は湿菌体重量に依り、全糖濃度は塩酸
加水分解後にソモジーネルソン(Somogi−Nelson)法に
依り、L−リジン塩酸塩濃度はバクテリウムカダベリス
(Bacterium cadaveris)からのL−リジン脱炭酸酵素
を用いる検圧法に依つた。最終結果を第4表に一括表示
した。
Fermentation test The strain used is Corynebacterium glutamicum (Coryne
bacterium glutamicum) ATCC 13280. The medium used is as follows. Preserved slant (meat extract 10g,
Polypeptone 10 g, NaCl 5 g, agar 1.5%, pH 7.
0), pre-culture medium (glucose 20 g, yeast extract 1
g ,, NZ-Amine (Wako Pure Chemical Industries, Ltd. product brand name) 6
g, 4 g of NH 4 Cl, 5 g of KH 2 PO 4 , 1 of Na 2 HPO 4 · 12H 2 O
5g, MgSO 4 · 7H 2 O of 0.25g, FeSO 4 · 7H 2 O 0.0
1 g, 0.01 g of MnSO 4 .4H 2 O, deionized water 1, pH
7.0) Main culture medium [molasses 50 g total sugar (total sugar 50 g
Containing molasses), NZ-Amine 15 g, NH 4 Cl 10 g,
Adjusted to 1 with deionized water), and supplemented medium (molasses 500)
g total sugar, 150 g of NH 4 Cl, adjusted to 1.5 with deionized water). For pre-culture, pre-culture medium 10 in 500 ml Sakaguchi flask
After injecting 0 ml and sterilizing, inoculate 1 platinum loop from the slant-preserving slant.
The culture was performed by reciprocal shaking (amplitude 4 cm, 135 times / min) for 22 hours at 0 ° C. For the main culture, charge 3.0 ml of the main culture medium into a 10-volume jar amenta, and after sterilization, 500 ml.
Was inoculated into the preculture liquid of Temperature is 30 ° C, rotation speed is 300 rpm, aeration is 1 vvm, pH is 6.8 with 5N NaOH.
Controlled to ~ 7.0. As a defoamer, ADEKA NOL LG
109 (trade name of a product of Asahi Denka Co., Ltd.) was used. Approximately 8 hours after the start of culturing, before the stationary phase, the total sugar concentration was 10%, Na
Supplemental sugar solution 1.5 was added so that the content of 4 Cl was 3%. As an analytical method, the bacterial cell concentration depends on the wet bacterial cell weight, the total sugar concentration depends on the Somogi-Nelson method after hydrochloric acid hydrolysis, and the L-lysine hydrochloride concentration indicates the bacterial cadaveris (Bacterium cadaveris). From L. lysine decarboxylase from E. coli. The final results are collectively shown in Table 4.

実施例3 フイリピン産原糖蜜を電気透析処理する事により得られ
た糖蜜をL−リジン発酵の原料として使用した例を示
す。
Example 3 An example of using molasses obtained by subjecting a raw molasses produced in Filipin to electrodialysis as a raw material for L-lysine fermentation is shown.

処理糖蜜の調整 ブリツクス50に調整したフイリピン産原糖蜜9を実
施例1に使用したものと同じ透析装置で処理した。運転
条件はセル電圧2.0V、平均電流密度2.69Amp/d
m2、流量70/hr、電気透析時間は6時間である。電
気透析後の濃縮された糖蜜を処理糖蜜とした。
Preparation of treated molasses Raw molasses 9 from Filipin adjusted to Brix 50 was treated with the same dialysis machine as used in Example 1. Operating conditions are cell voltage 2.0V, average current density 2.69Amp / d
m 2 , flow rate 70 / hr, electrodialysis time 6 hours. The concentrated molasses after electrodialysis was used as the treated molasses.

フイリピン産処理糖蜜と処理前糖蜜との分析値を第5表
に一括表示した。(但し沖蝿産糖蜜の全糖濃度に合せて
表示した。) 発酵試験 使用菌株、培地、培養法を実施例2と同様な方法で行つ
た。L−リジン塩酸塩濃度、菌体濃度、全糖濃度の経時
変化を第3図に最終結果を第6表に一括表示した。
Table 5 collectively shows the analytical values of the treated molasses produced in Filipin and the untreated molasses. (However, it is displayed according to the total sugar concentration of molasses produced from Okibatsu.) Fermentation test The strains, medium and culture method used were the same as in Example 2. The time-dependent changes in L-lysine hydrochloride concentration, bacterial cell concentration, and total sugar concentration are shown in FIG. 3 and the final results are shown in Table 6 collectively.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】陽イオン交換膜と中性膜を交互に複数組合
わせた多室構造の電気透析装置を用いて原料糖蜜を電気
透析し、原料糖蜜中の全灰分量を約1/2〜約1/4の範囲内
に低下させることを特徴とする醗酵用糖蜜製品の製造方
法。
1. A raw molasses is electrodialyzed using an electrodialyzer having a multi-chamber structure in which a plurality of cation-exchange membranes and neutral membranes are alternately combined, and the total ash content in the raw molasses is about 1/2 to. A method for producing a molasses product for fermentation, which comprises reducing the concentration within a range of about 1/4.
JP58082124A 1983-05-11 1983-05-11 Method for producing sugar-dense product for fermentation Expired - Lifetime JPH0638760B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP58082124A JPH0638760B2 (en) 1983-05-11 1983-05-11 Method for producing sugar-dense product for fermentation

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP58082124A JPH0638760B2 (en) 1983-05-11 1983-05-11 Method for producing sugar-dense product for fermentation

Publications (2)

Publication Number Publication Date
JPS59205950A JPS59205950A (en) 1984-11-21
JPH0638760B2 true JPH0638760B2 (en) 1994-05-25

Family

ID=13765662

Family Applications (1)

Application Number Title Priority Date Filing Date
JP58082124A Expired - Lifetime JPH0638760B2 (en) 1983-05-11 1983-05-11 Method for producing sugar-dense product for fermentation

Country Status (1)

Country Link
JP (1) JPH0638760B2 (en)

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5747497A (en) * 1980-09-02 1982-03-18 Asahi Glass Co Ltd Purification of sugar solution

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
萩原文二(外1名)著「膜による分離法」(講談社)(昭57−10−10)P.18−24

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