JPH01157395A - Method for culturing microorganism - Google Patents
Method for culturing microorganismInfo
- Publication number
- JPH01157395A JPH01157395A JP31344487A JP31344487A JPH01157395A JP H01157395 A JPH01157395 A JP H01157395A JP 31344487 A JP31344487 A JP 31344487A JP 31344487 A JP31344487 A JP 31344487A JP H01157395 A JPH01157395 A JP H01157395A
- Authority
- JP
- Japan
- Prior art keywords
- medium
- culture medium
- natural rubber
- fermentation
- added
- 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.)
- Granted
Links
- 238000000034 method Methods 0.000 title claims abstract description 5
- 244000005700 microbiome Species 0.000 title claims description 8
- 238000012258 culturing Methods 0.000 title 1
- 238000000855 fermentation Methods 0.000 claims abstract description 17
- 230000004151 fermentation Effects 0.000 claims abstract description 17
- 244000043261 Hevea brasiliensis Species 0.000 claims abstract description 9
- 229920003052 natural elastomer Polymers 0.000 claims abstract description 9
- 229920001194 natural rubber Polymers 0.000 claims abstract description 9
- 241000894006 Bacteria Species 0.000 claims abstract description 7
- 239000004816 latex Substances 0.000 claims abstract description 5
- 229920000126 latex Polymers 0.000 claims abstract description 5
- 239000012141 concentrate Substances 0.000 claims abstract description 3
- 239000012452 mother liquor Substances 0.000 claims abstract description 3
- 241000233866 Fungi Species 0.000 claims abstract 6
- 240000004808 Saccharomyces cerevisiae Species 0.000 claims abstract 2
- 238000001694 spray drying Methods 0.000 claims abstract 2
- 230000001580 bacterial effect Effects 0.000 claims description 19
- 239000002609 medium Substances 0.000 abstract description 37
- 239000001963 growth medium Substances 0.000 abstract description 9
- 239000007788 liquid Substances 0.000 abstract description 7
- 239000000843 powder Substances 0.000 abstract description 6
- 239000002994 raw material Substances 0.000 abstract description 5
- 210000002966 serum Anatomy 0.000 abstract 3
- 239000008267 milk Substances 0.000 abstract 2
- 210000004080 milk Anatomy 0.000 abstract 2
- 235000013336 milk Nutrition 0.000 abstract 2
- 241000186046 Actinomyces Species 0.000 abstract 1
- 241000196324 Embryophyta Species 0.000 abstract 1
- 230000000813 microbial effect Effects 0.000 abstract 1
- 230000000644 propagated effect Effects 0.000 abstract 1
- 230000001902 propagating effect Effects 0.000 abstract 1
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 20
- 235000000346 sugar Nutrition 0.000 description 13
- 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 12
- 229940041514 candida albicans extract Drugs 0.000 description 12
- 239000008103 glucose Substances 0.000 description 12
- 239000012138 yeast extract Substances 0.000 description 12
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 9
- 239000001888 Peptone Substances 0.000 description 8
- 108010080698 Peptones Proteins 0.000 description 8
- 235000019319 peptone Nutrition 0.000 description 8
- 230000000694 effects Effects 0.000 description 6
- JVTAAEKCZFNVCJ-UHFFFAOYSA-N lactic acid Chemical compound CC(O)C(O)=O JVTAAEKCZFNVCJ-UHFFFAOYSA-N 0.000 description 6
- 229920002472 Starch Polymers 0.000 description 5
- 238000004519 manufacturing process Methods 0.000 description 5
- 235000019698 starch Nutrition 0.000 description 5
- 239000008107 starch Substances 0.000 description 5
- 244000068988 Glycine max Species 0.000 description 4
- 235000010469 Glycine max Nutrition 0.000 description 4
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 4
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 4
- 235000018102 proteins Nutrition 0.000 description 4
- 102000004169 proteins and genes Human genes 0.000 description 4
- 108090000623 proteins and genes Proteins 0.000 description 4
- 102000004190 Enzymes Human genes 0.000 description 3
- 108090000790 Enzymes Proteins 0.000 description 3
- 108091005804 Peptidases Proteins 0.000 description 3
- 239000004365 Protease Substances 0.000 description 3
- 102100037486 Reverse transcriptase/ribonuclease H Human genes 0.000 description 3
- 230000037396 body weight Effects 0.000 description 3
- 150000001875 compounds Chemical class 0.000 description 3
- 238000000354 decomposition reaction Methods 0.000 description 3
- 229940088598 enzyme Drugs 0.000 description 3
- 239000004310 lactic acid Substances 0.000 description 3
- 235000014655 lactic acid Nutrition 0.000 description 3
- 235000003170 nutritional factors Nutrition 0.000 description 3
- 125000001477 organic nitrogen group Chemical group 0.000 description 3
- YBJHBAHKTGYVGT-ZKWXMUAHSA-N (+)-Biotin Chemical compound N1C(=O)N[C@@H]2[C@H](CCCCC(=O)O)SC[C@@H]21 YBJHBAHKTGYVGT-ZKWXMUAHSA-N 0.000 description 2
- WHUUTDBJXJRKMK-UHFFFAOYSA-N Glutamic acid Natural products OC(=O)C(N)CCC(O)=O WHUUTDBJXJRKMK-UHFFFAOYSA-N 0.000 description 2
- 235000001014 amino acid Nutrition 0.000 description 2
- 150000001413 amino acids Chemical class 0.000 description 2
- 235000013922 glutamic acid Nutrition 0.000 description 2
- 239000004220 glutamic acid Substances 0.000 description 2
- 238000011081 inoculation Methods 0.000 description 2
- 235000012054 meals Nutrition 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 235000016709 nutrition Nutrition 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- 239000011780 sodium chloride Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 150000008163 sugars Chemical class 0.000 description 2
- PHIQHXFUZVPYII-ZCFIWIBFSA-N (R)-carnitine Chemical compound C[N+](C)(C)C[C@H](O)CC([O-])=O PHIQHXFUZVPYII-ZCFIWIBFSA-N 0.000 description 1
- XSHGVIPHMOTDCS-UHFFFAOYSA-N 1-(5-fluoropentyl)-n-(2-phenylpropan-2-yl)indazole-3-carboxamide Chemical compound N=1N(CCCCCF)C2=CC=CC=C2C=1C(=O)NC(C)(C)C1=CC=CC=C1 XSHGVIPHMOTDCS-UHFFFAOYSA-N 0.000 description 1
- -1 1.0% polypeptone Substances 0.000 description 1
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 description 1
- 235000017060 Arachis glabrata Nutrition 0.000 description 1
- 244000105624 Arachis hypogaea Species 0.000 description 1
- 235000010777 Arachis hypogaea Nutrition 0.000 description 1
- 235000018262 Arachis monticola Nutrition 0.000 description 1
- 239000002028 Biomass Substances 0.000 description 1
- 241000736839 Chara Species 0.000 description 1
- 235000011511 Diospyros Nutrition 0.000 description 1
- 244000236655 Diospyros kaki Species 0.000 description 1
- 108010073178 Glucan 1,4-alpha-Glucosidase Proteins 0.000 description 1
- 102100022624 Glucoamylase Human genes 0.000 description 1
- 241000108056 Monas Species 0.000 description 1
- 108010059712 Pronase Proteins 0.000 description 1
- 241000269821 Scombridae Species 0.000 description 1
- 240000008042 Zea mays Species 0.000 description 1
- 235000005824 Zea mays ssp. parviglumis Nutrition 0.000 description 1
- 235000002017 Zea mays subsp mays Nutrition 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 241001148470 aerobic bacillus Species 0.000 description 1
- 102000004139 alpha-Amylases Human genes 0.000 description 1
- 108090000637 alpha-Amylases Proteins 0.000 description 1
- 229940024171 alpha-amylase Drugs 0.000 description 1
- 235000011114 ammonium hydroxide Nutrition 0.000 description 1
- BFNBIHQBYMNNAN-UHFFFAOYSA-N ammonium sulfate Chemical compound N.N.OS(O)(=O)=O BFNBIHQBYMNNAN-UHFFFAOYSA-N 0.000 description 1
- 229910052921 ammonium sulfate Inorganic materials 0.000 description 1
- 235000011130 ammonium sulphate Nutrition 0.000 description 1
- 229960002685 biotin Drugs 0.000 description 1
- 235000020958 biotin Nutrition 0.000 description 1
- 239000011616 biotin Substances 0.000 description 1
- 239000008280 blood Substances 0.000 description 1
- 210000004369 blood Anatomy 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 239000005018 casein Substances 0.000 description 1
- BECPQYXYKAMYBN-UHFFFAOYSA-N casein, tech. Chemical compound NCCCCC(C(O)=O)N=C(O)C(CC(O)=O)N=C(O)C(CCC(O)=N)N=C(O)C(CC(C)C)N=C(O)C(CCC(O)=O)N=C(O)C(CC(O)=O)N=C(O)C(CCC(O)=O)N=C(O)C(C(C)O)N=C(O)C(CCC(O)=N)N=C(O)C(CCC(O)=N)N=C(O)C(CCC(O)=N)N=C(O)C(CCC(O)=O)N=C(O)C(CCC(O)=O)N=C(O)C(COP(O)(O)=O)N=C(O)C(CCC(O)=N)N=C(O)C(N)CC1=CC=CC=C1 BECPQYXYKAMYBN-UHFFFAOYSA-N 0.000 description 1
- 235000021240 caseins Nutrition 0.000 description 1
- 230000002301 combined effect Effects 0.000 description 1
- 230000003750 conditioning effect Effects 0.000 description 1
- 235000005822 corn Nutrition 0.000 description 1
- 235000012343 cottonseed oil Nutrition 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000000921 elemental analysis Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 230000002255 enzymatic effect Effects 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 239000000284 extract Substances 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 229940005740 hexametaphosphate Drugs 0.000 description 1
- 230000007062 hydrolysis Effects 0.000 description 1
- 238000006460 hydrolysis reaction Methods 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 239000002440 industrial waste Substances 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 230000003993 interaction Effects 0.000 description 1
- 244000144972 livestock Species 0.000 description 1
- 235000020640 mackerel Nutrition 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 235000010755 mineral Nutrition 0.000 description 1
- 238000010090 natural rubber production Methods 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 229910017464 nitrogen compound Inorganic materials 0.000 description 1
- 150000002830 nitrogen compounds Chemical class 0.000 description 1
- 235000015097 nutrients Nutrition 0.000 description 1
- 230000035764 nutrition Effects 0.000 description 1
- 150000007524 organic acids Chemical class 0.000 description 1
- 235000005985 organic acids Nutrition 0.000 description 1
- 150000002897 organic nitrogen compounds Chemical class 0.000 description 1
- 235000020232 peanut Nutrition 0.000 description 1
- 239000008363 phosphate buffer Substances 0.000 description 1
- 238000003307 slaughter Methods 0.000 description 1
- 230000001954 sterilising effect Effects 0.000 description 1
- 238000004659 sterilization and disinfection Methods 0.000 description 1
- 241001148471 unidentified anaerobic bacterium Species 0.000 description 1
- 235000013343 vitamin Nutrition 0.000 description 1
- 229940088594 vitamin Drugs 0.000 description 1
- 229930003231 vitamin Natural products 0.000 description 1
- 239000011782 vitamin Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Landscapes
- Preparation Of Compounds By Using Micro-Organisms (AREA)
- Micro-Organisms Or Cultivation Processes Thereof (AREA)
Abstract
Description
【発明の詳細な説明】
天然ゴムの樹液からラテックスを分離した残りの母液(
以下Natural Rubber 5erun 略
してNR8と呼ぶ)は、いわば天然ゴム生産における産
業廃棄物であり、天然ゴム生産国におけるこれの放置は
環境保全上看過できなくなりつつある。まして、NR3
は、多量のタンパク質を含み、有機酸、糖類、及びその
誘導体をふくんでいるので、微生物にとっては富栄養価
をもつものと考えられ、放置すれば、大きな環境汚染を
引き起こすことになりかねないが、反面、資源化できれ
ば新しい大きなバイオマスとなりうる可能性もひめでい
る。[Detailed Description of the Invention] The remaining mother liquor after separating latex from natural rubber sap (
Natural Rubber 5erun (hereinafter referred to as NR8 for short) is, so to speak, industrial waste from natural rubber production, and the neglect of this in natural rubber producing countries is becoming impossible to ignore in terms of environmental conservation. Moreover, NR3
Because it contains large amounts of protein, organic acids, sugars, and their derivatives, it is thought to have a rich nutritional value for microorganisms, and if left untreated, it could cause major environmental pollution. On the other hand, if it can be recycled, it has the potential to become a new and large biomass.
本発明者は、東甫アジアのラテックス工場で排出するN
R3を原料としてこれを濃縮し、あるいは粉末のNR3
としたものを用いて実験し、このような液状あるいは粉
末のNR3には色々な微生物に対する生育促進効果や、
生育必須因子を含んでいることを見いだした。The inventor has investigated the N emissions from Toho Asia's latex factory.
Use R3 as a raw material and concentrate it, or make powdered NR3.
Experiments using liquid or powdered NR3 revealed that it has a growth-promoting effect on various microorganisms,
It was found that it contains essential factors for growth.
一般に、微生物はその生育に色々な栄養因子を要求する
ことが多く、それらは、アミノ酸、ビタミン、ミネラル
など多様であり、また、必ずしも人だけでなく、複数の
栄養因子を要求することも多い。従って、発酵用の培地
には、複数の栄養因子を供給する目的で、有機窒素源な
どの天然の有機栄養が用いられる。これらには、脱脂大
豆加水分解液(IIVP) 、Corn 5teep
Liquor(C3L)、綿実ミ−ル、ビーナツツミー
ル、pharlan+cdia 、 distille
rs 5oluble、家畜血液、屠殺廃液、カゼイン
氷解物など多種多様である。しかも、これらを工業生産
の発酵原料とする場合には、コストか安価なこと、季節
的、突発的ではなく安定的に供給できること、品質が安
定していることなどが必須である上に、色々な微生物に
広く効果のある、普遍的なものでることが望ましい。こ
のような条件を満足するのは、上記の多数の天然有機栄
養源のなかでも、)iVP、C3L、酵母エキスなどに
限られるが、MVPやC3Lはそれぞれ食品工業の副産
物として製造されている為に、最近では製法の転換とと
もにコスト高になったり、供給量が減少しており、酵母
エキスはコスト高で工業原料としては難点が多い。In general, microorganisms often require a variety of nutritional factors for their growth, including a variety of amino acids, vitamins, and minerals, and often require multiple nutritional factors, not just humans. Therefore, fermentation media use natural organic nutrients, such as organic nitrogen sources, to provide multiple nutritional factors. These include defatted soybean hydrolyzate (IIVP), Corn 5teep
Liquor (C3L), cottonseed meal, peanut meal, pharlan+cdia, distille
There are a wide variety of sources, including RS 5olable, livestock blood, slaughter waste fluid, and casein thawed product. Moreover, when using these as fermentation raw materials for industrial production, it is essential that they be inexpensive, that they can be supplied stably rather than seasonally or suddenly, and that their quality is stable. It would be desirable to have a universal product that is widely effective against various microorganisms. Of the many natural organic nutritional sources mentioned above, only iVP, C3L, yeast extract, etc. satisfy these conditions, but MVP and C3L are each manufactured as by-products of the food industry. However, recently, due to changes in production methods, costs have increased and supplies have decreased, and yeast extract is expensive and has many disadvantages as an industrial raw material.
粉末NR3の一般的性状は、元素分析値ではC22%
H5,5%
N 9,5%
^sh 18.5%
であるか、この内、有11INのバランスをみると、不
溶性窒素化合物が6%、不溶性無窒素化合物が1.5χ
、可溶性有機窒素化合物が16.5%、可溶性無窒素化
合物が28%その他、硫酸アンモニウム28%、灰分1
8%、水分2% となっている。The general properties of powder NR3 are: C22% H5.5% N 9.5% ^sh 18.5% according to the elemental analysis values, and looking at the balance of 11 IN, insoluble nitrogen compounds account for 6%. , the insoluble nitrogen-free compound is 1.5χ
, 16.5% soluble organic nitrogen compounds, 28% soluble nitrogen-free compounds, 28% ammonium sulfate, ash 1
8%, moisture 2%.
可溶性無窒素化合!l−!IJ 28%中発酵原料とな
りそうな有R酸や還元糖の含量は小量であり、NR3は
発酵のC源とはなりにくいと考られるが、単純な有機窒
素源であるとも言えない。Soluble nitrogen-free compound! l-! The content of R acids and reducing sugars that are likely to be fermentation raw materials in IJ 28% is small, and NR3 is unlikely to be a C source for fermentation, but it cannot be said to be a simple organic nitrogen source.
実験結果によれば、NR3は、その形態が液体であれ、
粉末であれ、細菌、酵禄において広く生育促進効果を示
し、培地有機窒素源に酵母エキス、1−IVP、C3L
等を用いる発酵ではこれらをNR8に置き換えて十分発
酵生産の目的を達することが明らかとなった。また、そ
の効果は、細菌の場合は、好気性菌でも、嫌気性菌でも
同様であった。According to the experimental results, NR3, regardless of its liquid form,
Even as a powder, it has a wide range of growth-promoting effects on bacteria and fermentation, and contains yeast extract, 1-IVP, and C3L as organic nitrogen sources for the medium.
It has become clear that the purpose of fermentation production can be sufficiently achieved by replacing these with NR8 in fermentation using NR8 and the like. Moreover, in the case of bacteria, the effect was similar for both aerobic and anaerobic bacteria.
さらに、一部の微生物では、NR3を培地に添加する前
に、予めプロテアーゼ処理によって加水分解しておいて
も、加水分解せずにそのまま培地に添加しても同様の効
果が見られた。Furthermore, in some microorganisms, similar effects were observed even when NR3 was hydrolyzed by protease treatment before being added to the medium, or when it was added to the medium as it was without hydrolysis.
このような実験事実を考えると、NR3の微生物に対す
る効果は、含まれるタンパク質やそれが分解して生ずる
アミノ酸の効果だけによるものではなく、NR3の中に
含まれる未同定の物質や、それとタンパクとの複合効果
によるものと考えられる。Considering these experimental facts, the effect of NR3 on microorganisms is not only due to the effects of the proteins it contains and the amino acids produced by its decomposition, but also to unidentified substances contained in NR3 and its interaction with proteins. This is thought to be due to the combined effect of
以下実施例をもって、本発明を説明する。The present invention will be explained below with reference to Examples.
実施例の1
グルコース10(1、HQSOa + 7112034
+ag、 Na1l 2PO4・12H20771+1
(1、にC110mg に、NR3の117テア一セ
分解液(NR320gをH/30リン酸バッファーpH
7,01Nに添加し、不溶性物質はそのままにして、こ
れにプロナーゼ20011gを添加し、30℃12hr
反応させたもの。タンパク質の分解率は約94%である
)をNR3換算で2g相当量を添加し、pHを7.0に
調整したのち、純水でIIに希釈する。Example 1 Glucose 10 (1, HQSOa + 7112034
+ag, Na1l 2PO4・12H20771+1
(1. Add 110 mg of C to 117 tera Ice decomposition solution of NR3 (320 g of NR) to H/30 phosphate buffer pH.
7,01N, and while leaving the insoluble substances as is, add 20011 g of pronase to this, and incubate at 30°C for 12 hours.
Something that reacted. (Protein decomposition rate is approximately 94%) was added in an amount equivalent to 2 g in terms of NR3, the pH was adjusted to 7.0, and then diluted to II with pure water.
一方、グルコース10g 、H(]SO4・71120
34mg、Na1l 2 PO4−12112077+
ng、KCI 10+ng に、酵母エキス(オリエ
ンタル酵母社製)5(lとポリペプトン(大五栄養製)
5(Jを加えpH調整後純水によってI!Jとしたもの
を対照とした。On the other hand, 10g of glucose, H(]SO4・71120
34mg, Na1l2PO4-12112077+
ng, KCI 10+ng, yeast extract (manufactured by Oriental Yeast Co., Ltd.) 5 (l) and polypeptone (manufactured by Daigo Nutrition Co., Ltd.)
5 (J) was added, the pH was adjusted, and then I!J was prepared with pure water as a control.
これら両培地に、’I’ G C−液体培地に30’C
で−・夜培養した5treptococcus 1ac
tis(ATCC19435)を2011接種し、30
℃で静置培養した。培養12時間後の菌体側を乾燥菌体
重量法により、生成した乳酸量をIIPLcによって定
着した。NR8を含む培地においては、乾燥菌体重1.
2h/、Q 、乳酸生成量9、2g#であった。一方、
酵母エキス、ポリペプトンを含む対照培地では、乾燥菌
体重j1M 1.25g/l、乳酸生成M 9.h/J
か得られた。In both these media, 'I' G C-liquid medium at 30'C.
- 5treptococcus 1ac cultured at night
tis (ATCC19435) was inoculated in 2011, and 30
The cells were incubated statically at ℃. After 12 hours of culture, the bacterial cell side was determined by the dry bacterial weight method, and the amount of lactic acid produced was determined by IIPLc. In the medium containing NR8, the dry bacterial weight was 1.
2h/, Q, lactic acid production amount was 9.2g#. on the other hand,
In the control medium containing yeast extract and polypeptone, dry bacterial weight J1M 1.25 g/l, lactic acid production M9. h/J
or obtained.
実施例2
キャラサバ澱粉の酵素糖化液(キャラサバ澱粉100(
]を5001の純水に溶解の後、α−アミラーゼ600
uを添加して70℃に加温して30分間保持し、液化を
行う。しかるのち、40℃に冷却し、グルコアミラーゼ
を添加して、ゆっくり振とうしながら24時間反応させ
た糖化液をグルコース109相当址J1ユし、これに酵
母エキス0.3g、ベプI−ン0,5gを添加し、pH
6,2に調整の後純粋で100+alに稀釈しものを基
準培地とした。Example 2 Enzyme saccharification solution of Charasaba starch (Charasaba starch 100 (
] in 5001 pure water, α-amylase 600
Add u and heat to 70°C and hold for 30 minutes to liquefy. Thereafter, the saccharified solution was cooled to 40°C, glucoamylase was added, and reacted for 24 hours with slow shaking. Add 0.5g and adjust the pH
After adjusting to 6.2, the pure medium was diluted to 100+al and used as a standard medium.
一方、キャラサバ澱粉の酵素糖化液をタル二7−ス10
g相当量計算し、これにNR3粉末(プロテアーゼ処理
しないもの) 0.3(lとペプトン0.5qを添加し
、pH6,2に調整の後、純水で10On+lに希釈し
たものを検討培地とした。Meanwhile, the enzymatic saccharification solution of Charasaba starch was added to Tarnis 7-10
Calculate the equivalent amount of 0.3 g of NR3 powder (not treated with protease) and 0.5 q of peptone, adjust the pH to 6.2, dilute to 10 On+l with pure water, and use it as the study medium. did.
また、キャラサバ澱粉の酵素糖化液をグルコース10g
相当量計算し、ペプトンO,sgを添加し、pH6,2
に′A整の後純水で10011に希釈したもの、および
、キャラサバ澱粉の酵素糖化液をグルコース10(l相
当量計算し、あとは何も加えない培地を比較培地とした
。In addition, 10g of glucose is added to the enzyme saccharification solution of Charasaba starch.
Calculate the equivalent amount, add peptone O, sg, and adjust the pH to 6.2.
The comparison medium was one diluted to 10011 with pure water after conditioning, and the enzyme saccharification solution of charas mackerel starch calculated to be equivalent to 10 liters of glucose, and a medium to which nothing else was added.
これら4種類の培地をIDeissclに入れて殺菌し
、Y M (Difco)液体培地で30℃、20培養
した7y+aononas n+obilis NRR
L B14023を51 接種後2日培養し、乾燥菌体
重量と生成したエタノールを測定した。These four types of media were sterilized in IDeisscl, and 7y + aononas n + obilis NRR was cultured at 30°C for 20 days in a YM (Difco) liquid medium.
LB14023 was cultured for 2 days after inoculation, and the dry bacterial weight and produced ethanol were measured.
糖液に酵母エキス、ペプトンを加えた培地では、乾燥菌
体重量2.05u/nlとエタノール5.22+ulが
えられ、NR3を用いた培地では、菌体型i1.611
1g/111 とエタノール5.01nlかえられた。In the medium containing yeast extract and peptone added to the sugar solution, dry bacterial weight 2.05 u/nl and ethanol 5.22+ul were obtained, and in the medium using NR3, the bacterial type i1.611 was obtained.
1 g/111 and 5.01 nl of ethanol were changed.
一方、i液にペプトンだけ加えた培地では、菌体型MO
,84n+q/ll とエタノール3.85m lかえ
られたが、糖液だけの培地では菌の生育、エタノールの
生成共全く認められなかった。On the other hand, in a medium containing only peptone in liquid i, the bacterial type MO
, 84 n+q/ll and 3.85 ml of ethanol, but neither bacterial growth nor ethanol production was observed in the medium containing only sugar solution.
実施例の3
実施例の2で用いたと全く同じ糖液を、クルコース10
(l相当量計景し、これに酵母エキス0.3g、マルト
エキス0.3g、ペグトン0.5すを添加し、pH6゜
2に調整の後純水で10On+lに希釈したものを基準
培地とした。Example 3 The same sugar solution used in Example 2 was mixed with 10 g
(Measure the amount equivalent to 1 liter, add 0.3 g of yeast extract, 0.3 g of malt extract, and 0.5 liter of pegtone, adjust the pH to 6°2, and dilute it to 10 On + liter with pure water, and use it as the standard medium. did.
一方、糖液をグルコース109相当延計算し、これにN
R8粉末(プロテアーゼ処理しないもの)0.3gとペ
プトンO,!o+を添加し、ptl6.2に調整の後、
純水で100nlに希釈したものを検討培地とした。On the other hand, the sugar solution was calculated to be equivalent to 109 glucose, and this was added to N
0.3g of R8 powder (not treated with protease) and peptone O,! After adding o+ and adjusting to ptl6.2,
A medium diluted to 100 nl with pure water was used as the test medium.
また、糖液をグルコース10g相当量計算し、ベグ1〜
ン0.5gを添加し、pH6,2に調整の後純水で10
0+nlに希釈したもの、および、糖液をグルコ−ス1
09相当延計算し、あとは何も加えない培地を比較培地
とした。In addition, calculate the amount of sugar solution equivalent to 10 g of glucose,
After adding 0.5g of water and adjusting the pH to 6.2, dilute with pure water for 10 minutes.
Glucose diluted to 0+nl and sugar solution
09 equivalent extension was calculated, and a medium to which nothing was added was used as a comparison medium.
これら4種類の培地をn+eisselに入れて殺菌し
、クルコース10g/!酵朋エキス3g/l、マルトエ
キス3g/l、ペプトン5(1/ l (pH6、2)
からなる前培養地で30℃、2日培養したSaccha
romyces uraurn IFO0565を5n
l接柿後2[1培養し、乾燥菌体重量と生成したエタノ
ールを測定した。Put these four types of culture medium into n+eissel, sterilize it, and use 10g of crucose/! Yeast extract 3g/l, malt extract 3g/l, peptone 5 (1/l (pH 6, 2)
Saccha cultured at 30°C for 2 days in a preculture medium consisting of
romyces uraurn IFO0565 5n
After persimmon inoculation, the cells were cultured for 2 days, and the dry bacterial weight and the produced ethanol were measured.
糖液に酵母エキス、フル1〜エキス、ペプトンを加えた
培地では、乾燥菌体重量4.901′mg/ml とエ
タノール4.891111が得られ、NR3を用いた培
地では、菌体型i 4.041B!II/1m l と
エタノール4.581111かえられた。一方、糖液に
ペプトンだけを加えた培地では、菌体重量0.64+n
g#a I とエタノール1 、99n+ lがえられ
た。また、糖液だけの培地でも菌体重量0.33+aq
/11 とエタノール0.84n lかえられた。In the medium containing yeast extract, Full 1-extract, and peptone added to the sugar solution, a dry bacterial weight of 4.901'mg/ml and ethanol of 4.891111 were obtained, and in the medium using NR3, the bacterial type i4. 041B! II/1ml and ethanol 4.581111 were changed. On the other hand, in a medium containing only peptone in a sugar solution, the bacterial weight was 0.64+n.
g#a I and ethanol 1,99n+l were obtained. In addition, even in a medium containing only sugar solution, the bacterial weight is 0.33 + aq
/11 and 0.84 nl of ethanol was changed.
実施例の4
グルコース1.0% 、ヘキサメタリン酸ソータ0.1
7 % 、にC10,1% 、 H(ISO4−
7H200,04%からなる培地(ptl 7.0)を
基本とし、■ 他にはなにも加えないもの
■ 脱脂大豆塩酸加水分解物(MVP)を0.5nl/
旧の濃度なるよう添加したもの■ 酵母エキス0.25
%を添加したもの■ NR3粉末0.25%を添加した
ものの4種の培地を作成し、これを500 nl振どう
フラスコに201づつ分注し殺菌の後、グルコース1.
0%、酵母エキス1゜0%、ボリベプl〜ン1.0%、
NaCl 015xからなる前培養培地(pH7,0)
にPseud。Example 4 Glucose 1.0%, hexametaphosphate sorter 0.1
7%, C10,1%, H(ISO4-
Based on a medium (ptl 7.0) consisting of 7H200.04%, ■ Nothing else added ■ Defatted soybean hydrochloric acid hydrolyzate (MVP) 0.5 nl/
Added to maintain the old concentration ■ Yeast extract 0.25
% of glucose was added ■ Four types of media were prepared with 0.25% of NR3 powder added, and after sterilization, 201 of each medium was dispensed into 500 nl shaking flasks, and 1.25% of glucose was added.
0%, yeast extract 1°0%, volibeprine 1.0%,
Preculture medium consisting of NaCl 015x (pH 7,0)
Pseud.
monas aeruginosa KYU−1(FE
RN P 0701)を接種し、30℃−夜振とう培養
したプロスを100μm添加して、30°Cで3日間振
どう培養を行い、生成した乾燥菌体重量を測定した。培
地■では、菌の生育は全く認められなかった。培地■で
は乾燥菌体重量は2.3ig/ifに、培地■では乾燥
菌体体重量は2,919/11に、培地■では乾燥菌体
重量は3.1ng/n+Iは、それぞれ達した。monas aeruginosa KYU-1 (FE
RN P 0701) was inoculated, 100 μm of Pross cultured at 30°C with overnight shaking was added, cultured with shaking at 30°C for 3 days, and the weight of the produced dry bacteria was measured. In medium ■, no bacterial growth was observed. In the medium (■), the dry bacterial body weight reached 2.3 ig/if, in the medium (■), the dry bacterial body weight reached 2,919/11, and in the medium (■), the dry bacterial body weight reached 3.1 ng/n+I.
実施例の5
グルコース 10%、 K112 PO40,1%、H
GSOa ・711200.24 % 、 FeSO
4−711200,01’X、Mn5O4、41+2
Q O,001%、ビタミンBt 100r/l 、
ビオチン3r/Iからなる培地に、液状NR3を1.0
11/旧の濃度で添加し、p Hを7.0に調整の後殺
菌し、全容1!Jのミニジャーファーメンタ−に300
n lを張り込んだ。Example 5 Glucose 10%, K112 PO40.1%, H
GSOa ・711200.24%, FeSO
4-711200,01'X,Mn5O4,41+2
Q O, 001%, vitamin Bt 100r/l,
Add 1.0 liquid NR3 to a medium consisting of biotin 3r/I.
11/Add at the old concentration, adjust the pH to 7.0 and sterilize, total 1! 300 for J's mini jar fermenter
I staked out n l.
一方NR3以外は全く同じ組成の培地に、NR8の替わ
りに、実施例の4で用いた脱脂大豆塩酸加水分解物を0
.75n+l/旧の濃度なるよう添加したのを、先と同
様pl+を7.0に調整の後殺菌し、全容11のミニジ
ャーファーメンタ−に300n I を張り込み対照と
した。この両ジャーに、グルコース1.0%、酵母エキ
ス1.0%、ポリペプトン1.0%、NaCl O,5
%からなる前培養培地(all 7.0)にBrcvi
bacteriun+ flavuIIATCC140
67を接種し、30℃−夜振とう培養したブロスを15
n+I添加して、温度34℃、通気撹ハンLt1/2
VVM 、t200rpn+ 、 pH制御はアモニア
水をフィードしながらpHを7,5に制御する方法で培
養した。30時間培養の後、脱脂大豆塩酸加水分解物を
用いた培養液には対糖46,5%のグルタミン酸が蓄積
し、液状NR3を用いた培養液には対$348.2%の
グルタミン酸が蓄積していた。On the other hand, in a medium having the same composition except for NR3, 0% of the defatted soybean hydrochloride hydrolyzate used in Example 4 was added instead of NR8.
.. The mixture was added to a concentration of 75n+l/old, sterilized after adjusting the pl+ to 7.0 as before, and 300nI was added to a mini-jar fermenter with a total volume of 11 to serve as a control. Both jars contained 1.0% glucose, 1.0% yeast extract, 1.0% polypeptone, and NaCl O,5
Brcvi in preculture medium (all 7.0) consisting of %
bacteriun+ flavuIIATCC140
67 and cultured at 30°C overnight with shaking.
Add n+I, temperature 34℃, ventilated stirrer Lt1/2
VVM, t200rpn+, and pH control were carried out by controlling the pH to 7.5 while feeding ammonia water. After 30 hours of culture, glutamic acid of 46.5% relative to sugar accumulated in the culture medium using defatted soybean hydrochloride hydrolyzate, and glutamic acid of 348.2% relative to sugar accumulated in the culture medium using liquid NR3. Was.
Claims (1)
液を濃縮し、もしくはスプレードライ法によって粉末化
して、それをそのまま発酵培地とし、または発酵培地に
一部添加して、その培地に細菌(放線菌を含む)、真菌
(酵母または糸状菌)を接種して増殖させ、菌体を生産
させ、かつ/また特定の発酵生産物を蓄積させる微生物
の培養法。1) Concentrate the remaining mother liquor after separating the latex from the natural rubber sap or pulverize it by spray drying and use it as a fermentation medium, or add a portion to the fermentation medium and incubate the medium with bacteria (actiradiation). A method of cultivating microorganisms that involves inoculating and multiplying fungi (including bacteria), fungi (yeast or filamentous fungi), producing bacterial cells, and/or accumulating specific fermentation products.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP62313444A JPH0646941B2 (en) | 1987-12-11 | 1987-12-11 | Microbial culture method |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP62313444A JPH0646941B2 (en) | 1987-12-11 | 1987-12-11 | Microbial culture method |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH01157395A true JPH01157395A (en) | 1989-06-20 |
JPH0646941B2 JPH0646941B2 (en) | 1994-06-22 |
Family
ID=18041374
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP62313444A Expired - Lifetime JPH0646941B2 (en) | 1987-12-11 | 1987-12-11 | Microbial culture method |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0646941B2 (en) |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH01199581A (en) * | 1988-02-04 | 1989-08-10 | Yokohama Rubber Co Ltd:The | Decomposition of natural rubber serum and product |
GB2236107A (en) * | 1989-08-10 | 1991-03-27 | Yokohama Rubber Co Ltd | Natural rubber serum concentrate |
EP1012234A4 (en) * | 1997-02-14 | 2002-11-06 | Life Technologies Inc | Dry powder cells and cell culture reagents and methods of production thereof |
US6627426B2 (en) | 1997-02-14 | 2003-09-30 | Invitrogen Corporation | Methods for reducing adventitious agents and toxins and cell culture reagents produced thereby |
CN102120963A (en) * | 2010-12-21 | 2011-07-13 | 湖南城市学院 | Rapid separation method of eurotium cristatum |
WO2013161674A1 (en) * | 2012-04-27 | 2013-10-31 | 花王株式会社 | Method for producing lactic acid |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS55102492A (en) * | 1979-02-01 | 1980-08-05 | Bayer Ag | Microbiological decomposition of acrylonitrile in water dispersion solution |
-
1987
- 1987-12-11 JP JP62313444A patent/JPH0646941B2/en not_active Expired - Lifetime
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS55102492A (en) * | 1979-02-01 | 1980-08-05 | Bayer Ag | Microbiological decomposition of acrylonitrile in water dispersion solution |
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH01199581A (en) * | 1988-02-04 | 1989-08-10 | Yokohama Rubber Co Ltd:The | Decomposition of natural rubber serum and product |
GB2236107A (en) * | 1989-08-10 | 1991-03-27 | Yokohama Rubber Co Ltd | Natural rubber serum concentrate |
GB2236107B (en) * | 1989-08-10 | 1993-06-30 | Yokohama Rubber Co Ltd | Natural rubber serum concentrate and method of making the same |
EP1012234A4 (en) * | 1997-02-14 | 2002-11-06 | Life Technologies Inc | Dry powder cells and cell culture reagents and methods of production thereof |
US6627426B2 (en) | 1997-02-14 | 2003-09-30 | Invitrogen Corporation | Methods for reducing adventitious agents and toxins and cell culture reagents produced thereby |
EP1702978A3 (en) * | 1997-02-14 | 2006-10-04 | Invitrogen Corporation | Dry powder cells and cell culture reagents and methods of production thereof |
US7572632B2 (en) | 1997-02-14 | 2009-08-11 | Life Technologies Corporation | Dry powder cells and cell culture reagents and methods of production thereof |
CN102120963A (en) * | 2010-12-21 | 2011-07-13 | 湖南城市学院 | Rapid separation method of eurotium cristatum |
WO2013161674A1 (en) * | 2012-04-27 | 2013-10-31 | 花王株式会社 | Method for producing lactic acid |
Also Published As
Publication number | Publication date |
---|---|
JPH0646941B2 (en) | 1994-06-22 |
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