JPS6255080A - Production of pectinase preparation - Google Patents

Production of pectinase preparation

Info

Publication number
JPS6255080A
JPS6255080A JP60193999A JP19399985A JPS6255080A JP S6255080 A JPS6255080 A JP S6255080A JP 60193999 A JP60193999 A JP 60193999A JP 19399985 A JP19399985 A JP 19399985A JP S6255080 A JPS6255080 A JP S6255080A
Authority
JP
Japan
Prior art keywords
black mold
activity
black
producing
production
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.)
Pending
Application number
JP60193999A
Other languages
Japanese (ja)
Inventor
シメオン・グリゴリエビツチ・チヤガ
ツベタナ・セムコワ・ドスチノワ
デシミラ・コレワ・カラコマコワ
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
ISUSUREDO TSUENTORU BIOTEKUNOR
ISUSUREDO TSUENTORU PO BIOTEKUNOROGIA
Original Assignee
ISUSUREDO TSUENTORU BIOTEKUNOR
ISUSUREDO TSUENTORU PO BIOTEKUNOROGIA
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Priority to DE19853529221 priority Critical patent/DE3529221A1/en
Priority to CH3576/85A priority patent/CH666283A5/en
Application filed by ISUSUREDO TSUENTORU BIOTEKUNOR, ISUSUREDO TSUENTORU PO BIOTEKUNOROGIA filed Critical ISUSUREDO TSUENTORU BIOTEKUNOR
Priority to JP60193999A priority patent/JPS6255080A/en
Publication of JPS6255080A publication Critical patent/JPS6255080A/en
Pending legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12NMICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
    • C12N9/00Enzymes; Proenzymes; Compositions thereof; Processes for preparing, activating, inhibiting, separating or purifying enzymes
    • C12N9/14Hydrolases (3)

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  • Life Sciences & Earth Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Genetics & Genomics (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Bioinformatics & Cheminformatics (AREA)
  • Zoology (AREA)
  • Wood Science & Technology (AREA)
  • Molecular Biology (AREA)
  • Microbiology (AREA)
  • Biotechnology (AREA)
  • Biomedical Technology (AREA)
  • Biochemistry (AREA)
  • General Engineering & Computer Science (AREA)
  • General Health & Medical Sciences (AREA)
  • Medicinal Chemistry (AREA)
  • Enzymes And Modification Thereof (AREA)
  • Micro-Organisms Or Cultivation Processes Thereof (AREA)

Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 この発明は、黒カビの突然変異体金側りたペクチン分解
酵素製剤の製造方法に関する。この製剤は、果実や野菜
の果肉からの抽出物に用いられ、それらのジュースを清
澄にする。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Field of Application] The present invention relates to a method for producing a pectin-degrading enzyme preparation derived from a mutant of black mold. This preparation is used for extracts from the pulp of fruits and vegetables and to clarify their juices.

〔従来技術とその問題点〕[Prior art and its problems]

黒かびの一菌株ファンティーグンを培養して得られるペ
クチン分解酵素製剤の製造法はよく知られておシ、活性
1500 U/♂の培養液を得ることができる(ブルガ
リア国特許証16862)。
The method for producing a pectin-degrading enzyme preparation obtained by culturing the black mold fungus Fantegun is well known, and a culture solution with an activity of 1500 U/male can be obtained (Bulgarian Patent No. 16862).

ところが、この方法には、培養液の活性レベルが不十分
でアリ、反応の至適温度が45℃と高すぎるという欠点
がある。そして後者の理由から、前記製剤を製造し、使
用する上で費用が嵩むという好ましくない結果が生まれ
てくる。
However, this method has the disadvantages that the activity level of the culture solution is insufficient and the optimum temperature for the reaction is too high at 45°C. The latter reason has the undesirable result of increased costs in manufacturing and using the formulation.

〔問題点を解決するための手段〕[Means for solving problems]

この発明の目的は、熱に安定なペクチン分解酵素の製造
法を提供することである。この方法によれば大量培養が
可能で、酵素活性の高い産物が得られる。この目的は、
黒かび8MX−41(薬剤管理のための国立機関Kl 
984年2月28日付で8番として寄託)を培養して発
酵させるととKよシ違せられる。この黒かびMX−4I
は、黒かび8Mの分生胞子を自然選択し、紫外線を照射
したあと、実験室条件下で弗酸させ、既存の酵素活性測
定法によシ篩い分けられたものである。
An object of this invention is to provide a method for producing a heat-stable pectinolytic enzyme. According to this method, large-scale cultivation is possible and products with high enzyme activity can be obtained. This purpose is
Black mold 8MX-41 (National Institute for Drug Control Kl)
K. (deposited as No. 8 on February 28, 1984) was cultured and fermented. This black mold MX-4I
Conidia of Mold 8M were naturally selected, irradiated with ultraviolet rays, hydrofluoric acidized under laboratory conditions, and sieved using existing enzyme activity measurement methods.

モルト入シの寒天上で72時間培養後、黒かびJMX−
41は丸いコロニーを形成する。そのコo=−のヘリは
滑かで、中心は窪んでおシ、はりきシとした放射状のひ
だがある。そして黄褐色の中心部は直径1.73であシ
、周辺の白い部分の幅は1.2備である。7日の後には
コロニーの直径は9 cst K達する。色は黒である
。中心は窪みつづけ、放射状のひだがさらにはりきシと
表われる。培養物はその培地に色素を分泌しない。コロ
ニーの反対側は明るいクリーム色である。
After culturing on agar containing malt for 72 hours, black mold JMX-
41 forms round colonies. The edge of the o=- is smooth, with a concave center and sharp radial folds. The diameter of the yellow-brown center is 1.73mm, and the width of the white part around it is 1.2mm. After 7 days the colony diameter reaches 9 cst K. The color is black. The center continues to be depressed, and the radial folds become more pronounced. The culture does not secrete pigment into its medium. The other side of the colony is a light cream color.

ジャガイ七入シの寒天上で72時間培養後、黒かび8P
/DC−41は球状コロニーを形成する。その中心部分
は直径0.5 cmで淡い黄色を帯び、その次の層は幅
2.2 asで黒色、表面は3關の白色層をなしている
。はぼ7口径コロニーの直径は7傭に達する。淡い色の
中心部分は同じ大きさのままであるが、黒色層が2.5
 cmに成長し、表面の白色層は0.53となる。
After culturing for 72 hours on potato agar, 8P black mold
/DC-41 forms spherical colonies. The central part is 0.5 cm in diameter and pale yellow, the next layer is 2.2 as wide and black, and the surface has three white layers. The diameter of the Habo7 caliber colony reaches 7 mm. The light colored center remains the same size, but the black layer increases by 2.5
The white layer on the surface becomes 0.53 cm.

カベクードックス(Chap*k −Dox )の寒天
上では72時間培養後、直径1.1 cmの球状コロニ
ーを形成する。中心は白色で、表面は薄く色素が沈着し
て、淡いクリーム色をしている。7口径コロニーの直径
は3ないし411mに達し、中心は白色で、その周囲は
黄緑色の幅0.7備の層が取シ巻いている。その後、2
cI!Lの黒色層、2ないし3mの周辺白色層が成長す
る。
On Chap*k-Dox agar, spherical colonies with a diameter of 1.1 cm are formed after culturing for 72 hours. The center is white, and the surface is lightly pigmented, giving it a pale cream color. The diameter of the 7-caliber colony reaches 3 to 411 m, with a white center surrounded by a 0.7 mm wide layer of yellow-green color. After that, 2
cI! A black layer of L and a peripheral white layer of 2 to 3 m grow.

培IIIKよシ、長さ250ないし500ミクロン、厚
さ2ないし3.5ミクロンの分生胞子を形成する。その
末端は直径1.5ないし2.2ミクロンの球状となって
おり、色は暗褐色ないし黒である。
In medium IIIK, conidia are formed 250 to 500 microns long and 2 to 3.5 microns thick. Its end is spherical, 1.5 to 2.2 microns in diameter, and dark brown to black in color.

固形培地上で、8MX−41は、よく泡立った空−気の
ミセルと、−腐敗性菌糸でできたミセルを有するコロニ
ーを形成する。
On solid media, 8MX-41 forms colonies with well-bubbly air micelles and micelles made of putrid mycelia.

培養物を、乾燥重量6−のモルト抽出物を含む傾斜寒天
培地上でも培養し得る。
Cultures may also be grown on slanted agar plates containing 6-dry weight malt extract.

黒かび1MX−4Iの培養産物を従来の黒かび8Mのそ
れと比較すると、前者の酵素活性が数倍高いという違い
がある。最良組成の培地で培養を開始してから144時
間たつと、発酵液ld中に前者では、ポリガラクッロデ
ーゼ活性4000±300Uおよびペクチンエステラー
ゼ活性20±4Uの培養物が蓄積するが、後者ではそれ
らがそれぞれ1500±20Uおよび4±0.5Uであ
る。
Comparing the culture product of Black Mold 1MX-4I with that of the conventional Black Mold 8M, there is a difference in that the enzyme activity of the former is several times higher. After 144 hours from the start of culture in the medium with the best composition, a culture with polygalacrodase activity of 4000 ± 300 U and pectin esterase activity of 20 ± 4 U accumulates in the fermentation solution ld in the former, but in the latter. Then they are 1500±20U and 4±0.5U, respectively.

24回の継代の後、次以の組成の培地中で発酵させる。After 24 passages, it is fermented in a medium with the following composition:

O乾燥ビート片   4.5ナイシ5.5’no小麦ぬ
か     0.7ないし1.59G0硫酸アンモニウ
ム  0.35ないし0.75%・リン酸二水素ナトリ
ウム 0.125ないし0.250 ’40澱  粉 
    0.5ないし1.5−〇硫酸マグネシウム  
 0.025ないし0.0540塩化カリウム   0
.025ないし0.05%ミセルを除去した後、発酵液
をフィルターにかけ夾雑物を除き、限外濾過にかけ低分
子量の可溶性混合物を除いた。この結果、容積は7ない
し9倍に減少し、乾燥物質は1.2ないし1.5チから
1.75ないし2チに増加した。その後、36℃以下の
温度で真空J縮を8回繰返し、38℃以下の温度で真空
乾燥した。
O Dried beet pieces 4.5 nai 5.5'no wheat bran 0.7 to 1.59 G0 Ammonium sulfate 0.35 to 0.75% Sodium dihydrogen phosphate 0.125 to 0.250 '40 Starch
0.5 to 1.5-0 magnesium sulfate
0.025 to 0.0540 Potassium Chloride 0
.. After removing 0.025 to 0.05% micelles, the fermentation liquid was filtered to remove impurities and ultrafiltrated to remove low molecular weight soluble mixtures. This resulted in a 7 to 9 fold reduction in volume and an increase in dry matter from 1.2 to 1.5 inches to 1.75 to 2 inches. Thereafter, vacuum J compression was repeated eight times at a temperature of 36°C or lower, and vacuum drying was performed at a temperature of 38°C or lower.

現在の方法とこの発明の方法を比較すると、後者には、
製剤の熱安定性が高く(至適温度50℃)、ポリガラク
ツロデーゼ活性が3倍高く、ペクチンエステラーゼ活性
が5倍高いという利点がある。これによると製造工程に
かかる費用が少なくてすみ、浄化活性の高い製剤が出来
る。この結果、製剤の消費量が低くても脱Rデチン化に
要する時間が短縮される。
Comparing the current method and the method of this invention, the latter has
The formulation has the advantages of high thermal stability (optimum temperature 50°C), 3 times higher polygalacturodase activity, and 5 times higher pectin esterase activity. According to this method, the cost required for the manufacturing process is reduced, and a preparation with high purifying activity can be produced. As a result, the time required for R-detinylation is shortened even when the consumption of the formulation is low.

〔実施例〕〔Example〕

組成 ・乾燥ビート片       4.5チ・小麦ぬか  
       0.75チ・硫酸アンモニウム    
 0.35チ・リン酸二水素ナトリウム    0.1
25%・澱   粉             0.5
%・硫酸マグネシウム     0.025%・塩化カ
リウム       0.025%の発酵培地を滅菌し
、27℃に冷却した後、その45ノの中に黒かびljM
X−41の24時時間積物1.5jを加えた。この接種
物は上記の発酵培地組成と同一の培地で調製した。これ
を連続往発酵器中での発酵は、攪拌器の表面速度264
ないし3.2 m/sで攪拌しながら、27.5±0.
5℃で144±8時間行なった。この際1分画シ培地l
!に対して0.8ないし1.1jの滅菌空気を送り込ん
だ。工程の終りには、ポリガラクツロデーゼ活性400
0±300Uおよびペクチンエステラーゼ活性20±4
Uが蓄積した。ミセルおよび培地中の不溶成分を除いた
後、目の細かい濾紙で濾過し九ところ35ないし37J
の発酵液を得た。次にこれを限外濾過によシ8倍に濃縮
し、続いて38℃以下の温度で真空濃縮を8回縁シ返し
、最後に38℃以下の温度で真空乾燥した。こうして、
ポリガラクツロデーゼ比活性400,000 U/II
、 ペクチンエステラーゼ比活性2000 U/lの調
製物300ないし350Iを得た。/臂−ライトまたは
ケイ藻出で製品化した後、4すfラクツロデーゼ比活性
60,000U/7およびペクチンエステラーゼ比活性
3000/7の製品約2階を得た。
Composition: Dried beet pieces 4.5 cm/Wheat bran
0.75tiammonium sulfate
0.35 Sodium dihydrogen phosphate 0.1
25%・Starch 0.5
%・Magnesium sulfate 0.025%・Potassium chloride 0.025% Fermentation medium was sterilized and cooled to 27℃, and black mold ljM
1.5j of the 24 hour load of X-41 was added. This inoculum was prepared in a medium identical to the fermentation medium composition described above. For fermentation in a continuous fermenter, the surface speed of the stirrer is 264
to 27.5±0. while stirring at 3.2 m/s.
The test was carried out at 5°C for 144±8 hours. At this time, 1 fraction of culture medium
! 0.8 to 1.1j of sterile air was pumped into the tank. At the end of the process, polygalactulodase activity 400
0±300U and pectin esterase activity 20±4
U has accumulated. After removing micelles and insoluble components in the medium, filter with fine filter paper and
A fermented liquid was obtained. Next, this was concentrated 8 times by ultrafiltration, then vacuum concentration was repeated 8 times at a temperature below 38°C, and finally vacuum drying was carried out at a temperature below 38°C. thus,
Polygalactulodase specific activity 400,000 U/II
, a preparation 300-350I with a pectin esterase specific activity of 2000 U/l was obtained. After commercialization with 4Sf lactulodase specific activity of 60,000 U/7 and pectin esterase specific activity of 3000/7, approximately 2F products were obtained.

Claims (2)

【特許請求の範囲】[Claims] (1)黒かび(Aspergillus niger)
の一菌株ファンティーゲン(Van Tighen)を
用いた大量培養による酵素製剤の製造方法において、薬
剤管理のための国立機関に1984年2月28日付で8
番として寄託された黒かびの突然変異体8MX−4Iを
発酵用培地中で培養し、発酵液から得られたペクチン分
解酵素を30℃ないし38℃の温度で濃縮乾燥すること
を特徴とするペクチン分解酵素の製造方法。
(1) Black mold (Aspergillus niger)
8, dated February 28, 1984, to the National Agency for Pharmaceutical Control, regarding the method for producing enzyme preparations by mass culture using one strain of Van Tighen.
Pectin, which is characterized by culturing the black mold mutant 8MX-4I, deposited as No. A method for producing a degrading enzyme.
(2)上記発酵培地が以下の成分から成る特許請求の範
囲第1項記載の方法。 ・乾燥ビート片 4.5ないし5.5% ・小麦ぬか 0.7ないし1.5% ・硫酸アンモニウム 0.35ないし0.75% ・リン酸二水素ナトリウム 0.125ないし0.25
0% ・澱粉 0.5ないし1.5% ・硫酸マグネシウム 0.025ないし0.05% ・塩化カリウム 0.025ないし0.05%
(2) The method according to claim 1, wherein the fermentation medium comprises the following components:・Dried beet pieces 4.5 to 5.5% ・Wheat bran 0.7 to 1.5% ・Ammonium sulfate 0.35 to 0.75% ・Sodium dihydrogen phosphate 0.125 to 0.25
0% ・Starch 0.5 to 1.5% ・Magnesium sulfate 0.025 to 0.05% ・Potassium chloride 0.025 to 0.05%
JP60193999A 1985-08-20 1985-09-04 Production of pectinase preparation Pending JPS6255080A (en)

Priority Applications (3)

Application Number Priority Date Filing Date Title
DE19853529221 DE3529221A1 (en) 1985-08-20 1985-08-14 Process for obtaining a pectolytic enzyme preparation
CH3576/85A CH666283A5 (en) 1985-08-20 1985-08-20 METHOD FOR OBTAINING A pectolytic ENZYMPRAEPARATS, PURSUANT TO THIS METHOD AND USE THEREOF PRODUCED ENZYMPRAEPARAT.
JP60193999A JPS6255080A (en) 1985-08-20 1985-09-04 Production of pectinase preparation

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
CH3576/85A CH666283A5 (en) 1985-08-20 1985-08-20 METHOD FOR OBTAINING A pectolytic ENZYMPRAEPARATS, PURSUANT TO THIS METHOD AND USE THEREOF PRODUCED ENZYMPRAEPARAT.
JP60193999A JPS6255080A (en) 1985-08-20 1985-09-04 Production of pectinase preparation

Publications (1)

Publication Number Publication Date
JPS6255080A true JPS6255080A (en) 1987-03-10

Family

ID=25693355

Family Applications (1)

Application Number Title Priority Date Filing Date
JP60193999A Pending JPS6255080A (en) 1985-08-20 1985-09-04 Production of pectinase preparation

Country Status (3)

Country Link
JP (1) JPS6255080A (en)
CH (1) CH666283A5 (en)
DE (1) DE3529221A1 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE3539875A1 (en) * 1985-11-11 1987-05-14 Keller & Bohacek Gmbh METHOD AND DEVICE FOR PRODUCING ENZYME-CONTAINING BIOMASS FROM SUGAR BEET CHIPS
EP0498137A1 (en) * 1991-02-06 1992-08-12 Novo Nordisk A/S Novel expression systems
CN104745558A (en) * 2015-04-07 2015-07-01 河南中烟工业有限责任公司 Pectinase produced through mixed bacterium fermentation, and application thereof in tobacco sheet processing

Also Published As

Publication number Publication date
DE3529221A1 (en) 1987-02-26
CH666283A5 (en) 1988-07-15

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