JPH047194B2 - - Google Patents

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Publication number
JPH047194B2
JPH047194B2 JP58129688A JP12968883A JPH047194B2 JP H047194 B2 JPH047194 B2 JP H047194B2 JP 58129688 A JP58129688 A JP 58129688A JP 12968883 A JP12968883 A JP 12968883A JP H047194 B2 JPH047194 B2 JP H047194B2
Authority
JP
Japan
Prior art keywords
candida
citric acid
palm oil
palm
genus
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
Application number
JP58129688A
Other languages
Japanese (ja)
Other versions
JPS6024191A (en
Inventor
Takeo Osada
Takao Matsumoto
Yoshuki Ichikawa
Tadayuki Miura
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.)
Showa Shell Sekiyu KK
Original Assignee
Showa Shell Sekiyu KK
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
Application filed by Showa Shell Sekiyu KK filed Critical Showa Shell Sekiyu KK
Priority to JP12968883A priority Critical patent/JPS6024191A/en
Priority to GB08417854A priority patent/GB2143527A/en
Publication of JPS6024191A publication Critical patent/JPS6024191A/en
Publication of JPH047194B2 publication Critical patent/JPH047194B2/ja
Granted legal-status Critical Current

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Classifications

    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12PFERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
    • C12P7/00Preparation of oxygen-containing organic compounds
    • C12P7/40Preparation of oxygen-containing organic compounds containing a carboxyl group including Peroxycarboxylic acids
    • C12P7/44Polycarboxylic acids
    • C12P7/48Tricarboxylic acids, e.g. citric acid

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  • Organic Chemistry (AREA)
  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Zoology (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Wood Science & Technology (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Microbiology (AREA)
  • General Chemical & Material Sciences (AREA)
  • Biotechnology (AREA)
  • Health & Medical Sciences (AREA)
  • Biochemistry (AREA)
  • Bioinformatics & Cheminformatics (AREA)
  • General Engineering & Computer Science (AREA)
  • General Health & Medical Sciences (AREA)
  • Genetics & Genomics (AREA)
  • Preparation Of Compounds By Using Micro-Organisms (AREA)
  • Micro-Organisms Or Cultivation Processes Thereof (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

本発明は発酵法による各種パーム油よりクエン
酸を製造する方法に関するものである。 従来、各種パーム油を発酵し、培地中にクエン
酸を高濃度で蓄積させ、これを採取する方法は見
当らない。 パーム油類は東南アジア地域に多量に産出して
おり(450万トン/年、1980年現在)、これら資源
の高付加価値化を図ることは資源の有効利用上重
要であると考える。この見地から、本発明者ら
は、パーム油類を容易に資化する酵母を見出し、
発酵培地中にクエン酸を高濃度で生成、蓄積し、
これを採取する方法を完成した。 すなわち、本発明は、炭素源としてパーム油を
含む培地中にキヤンデイダ属およびデバリオミセ
ス属のうち特定の酵母を好気的に培養し、該培地
中にクエン酸を蓄積させ、これを採取することを
特徴とするクエン酸の製法に関するものである。 本発明に用いる微生物は各種パーム油を資化し
てクエン酸を培地中に蓄積する能力を有するキヤ
ンデイダ・トロピカリス(Candida tropicalis)、
キヤンデイダ・インターメデイア(Candida
intermedia)、キヤンデイダ・ブルムプテイ
(Candida brumptii)、キヤンデイダ・ギヤマン
デイー(Candida guilliermondii)およびデバリ
オミセス・ハンゼニー(Debaryomyces
hansenii)に属する酵母である。 更に、本発明に用いる酵母は栄養要求変異株お
よび変種を含むものである。 本発明で使用する培地は、使用する酵母類の性
質に応じて選択されるが、炭素源は粗パーム油、
精製パーム油、パームオレインおよびパームステ
アリンの単独または混合物である。上記の各種パ
ーム油を適宜単独または混合物で使用することは
培地への分散性を良好ならしめるために必要であ
る。 原料の各種パーム油の培地への添加量は1ない
し20重量%で、好ましくは5ないし15重量%であ
る。窒素源として硝酸塩、硫酸塩のような無機ア
ンモニウム塩、酢酸アンモニウムのような有機ア
ンモニウム塩、アミノ酸類、尿素およびアンモニ
アが使用できる。 上記の各種窒素源は単独で使用してもよくまた
2種以上を混合して使用してもよい。無機塩とし
ては、第1リン酸塩、第2リン酸塩、硫酸塩、塩
酸塩、カリウム塩、ナトリウム塩、マグネシウム
塩、鉄塩、マンガン塩、銅塩、亜鉛塩など通常の
無機塩類が使用できる。 有機微量栄養素としては、ビオチン、チアミン
等のビタミン類を含む酵母エキス、コンステープ
リカーなどの天然物を使用してもよい。 発酵条件は好気的条件がよい。培養温度は25℃
ないし40℃の範囲で、好ましくは35℃が適当であ
る。培養中のPHは3ないし10の範囲でよいが、好
ましくは4ないし7である。培養中のPH調整は炭
酸カルシウム、カセイソーダまたはアンモニアな
どを用いて行なうことができる。 培養は通常50ないし150時間、好ましくは80な
いし100時間行なわれる。 培地中に蓄積されたクエン酸は、通常微生物の
培養によつて得られる有機酸類をその培養物から
分離するのに用いられる手段、たとえば過、遠
心分離等の方法で固体を分離した後、カラムクロ
マト処理、イオン交換樹脂処理あるいは濃縮処理
などによりクエン酸またはその塩として分離採取
することができる。 以下に、実施例を掲げて本発明を説明するが、
これに限定されるものではない。 実施例 1 培地組成 精製パーム油 6.0wt% NH3Cl 3.0(g/) KH2O4 0.5(g/) MgSO4・7H2O 0.5(g/) F4SO4・7H2O 5.0(mg/) MnSO4・7H2O 0.1(mg/) ZnSO4・nH2O 0.1(mg/) CuSO4・5H2O 5(μg/) ビオチン 100(μg/) チアミン・塩酸塩 100(μg/) 酵母抽出物 1.0(g/) PH 5.0 種培養として、内容500mlの坂口フラスコ5個
にそれぞれ上記組成の培養液30mlを分注したの
ち、115℃で10分間殺菌し、約35℃に放冷した後、
キヤンデイダ・トロピカリス(Candida
tropicalis)(IFO−0589)、キヤンデイダ・イン
ターメデイア(Candida intermedia)(IFO−
0761)、キヤンデイダ・ブルムプテイー
(Candida brumptii)(IFO−0744)、キヤンデイ
ダ・ギヤマンデイー(Candida guilliermondii)
(IFO−0838)およびデバリオミセス・ハンゼニ
ー(Debaryomyces hansenii)(IFO−0019)を
それぞれ3白金耳づつ移植した。 培養条件は温度35℃、振盪数120往復/分、振
巾7cmであつた。培養時間は3日間であるが、培
養開始約20時間後に酵母の成育を確認した後PH調
整のため、別に殺菌したCaCO3を培養液に対し
て5wt/vol%を添加してから培養を続け、これ
を種培養液とした。 生産培養とに種培地と同じ組成の培地30mlを
500mlの坂口フラスコ5個に入れ、115℃で10分間
加熱滅菌し、35℃まで放冷後、上記の種培養液
1.5ml(5vol%)をそれぞれ接種した。これを120
往復/分、振巾7cm、35℃の条件下で7日間培養
した。なお、培養開始後15時間目にPH調整のため
別に殺菌したCaCO3を培養液に対して5wt%を添
加した。 培養終了後、この培養物を塩酸でPH2.5とした
後ケイソウ土を過助剤として吸引過し、酵母
を主とする固型物はこれを少量の水で洗滌した。
次に液と洗滌液とを合せ、合併液を苛性ソーダ
で中和したのち加熱して沈澱を折出させ、これを
冷却後吸引過してクエン酸カルシウムを得た。 このクエン酸カルシウムを約10倍量の水に懸濁
し、これに、その液が塩化バリウム溶液によつ
て硫酸根の存在をわずかに示すに至るまで、撹拌
下50%硫酸水溶液を滴下したのち沸騰水中で約30
分間加熱する。これを必要によつては脱色操作を
施した後熱時過して液を50〜60℃の下で減圧
濃縮し、途中石膏の沈澱が析出した場合はこれを
別し、更に濃縮を続け、ややうすいシラツプ状
にまで至らしめる。 このシラツプ状濃縮物を氷点下に放置するとク
エン酸の結晶が析出する。それぞれ発酵液当りの
クエン酸の生成量(g/)は次のようである。 キヤンデイダ・トロピカリス(Candida
tropicalis) 52.1 キヤンデイダ・インターメデイア(Candida
intermedia) 30.4 キヤンデイダ・ブルムプテイ(Candida
brumptii) 34.5 キヤンデイダ・ギヤマンデイー(Candida
guilliermondii) 18.9 デバリオミセス・ハンゼニー(Debaryomyces
hansenii) 15.0 実施例 2 実施例1と同様な方法を用いたが、炭素源は各
種パーム油で、使用した菌種はキヤンデイダ・ト
ロピカリス(Candida tropicalis)(IFO−0589)
であつた。その結果は第1表に示した。
The present invention relates to a method for producing citric acid from various palm oils using a fermentation method. Until now, no method has been found to ferment various palm oils, accumulate citric acid in a medium at a high concentration, and then collect the citric acid. Palm oil is produced in large quantities in Southeast Asia (4.5 million tons/year, as of 1980), and we believe that increasing the added value of these resources is important for effective resource utilization. From this point of view, the present inventors discovered a yeast that can easily assimilate palm oil,
Produces and accumulates citric acid in high concentration in the fermentation medium,
I have perfected the method to collect this. That is, the present invention involves aerobically cultivating specific yeasts of the genus Candeida and Debaryomyces in a medium containing palm oil as a carbon source, accumulating citric acid in the medium, and collecting the citric acid. This article relates to the characteristic method for producing citric acid. The microorganism used in the present invention is Candida tropicalis, which has the ability to assimilate various palm oils and accumulate citric acid in the medium.
Candida Intermedia
intermedia), Candida brumptii, Candida guilliermondii and Debaryomyces
hansenii). Furthermore, the yeast used in the present invention includes auxotrophic mutants and variants. The medium used in the present invention is selected depending on the properties of the yeast used, and the carbon source is crude palm oil,
Refined palm oil, palm olein and palm stearin alone or in mixture. It is necessary to appropriately use the above-mentioned various palm oils alone or in a mixture in order to improve the dispersibility in the medium. The amount of each type of palm oil as a raw material added to the medium is 1 to 20% by weight, preferably 5 to 15% by weight. Inorganic ammonium salts such as nitrates, sulfates, organic ammonium salts such as ammonium acetate, amino acids, urea and ammonia can be used as nitrogen sources. The various nitrogen sources mentioned above may be used alone or in combination of two or more. Common inorganic salts used include primary phosphates, secondary phosphates, sulfates, hydrochlorides, potassium salts, sodium salts, magnesium salts, iron salts, manganese salts, copper salts, zinc salts, etc. can. As organic micronutrients, natural products such as yeast extract containing vitamins such as biotin and thiamine, and constabilized liquor may be used. Aerobic conditions are preferable for fermentation. Culture temperature is 25℃
The temperature range is from 40°C to 40°C, preferably 35°C. The pH during culturing may range from 3 to 10, preferably from 4 to 7. PH adjustment during culture can be performed using calcium carbonate, caustic soda, ammonia, or the like. Cultivation is usually carried out for 50 to 150 hours, preferably 80 to 100 hours. The citric acid accumulated in the medium is separated from the solids by means normally used to separate organic acids obtained by culturing microorganisms from the culture, such as filtration or centrifugation, and then passed through a column. It can be separated and collected as citric acid or its salt by chromatography, ion exchange resin treatment, concentration treatment, etc. The present invention will be explained below with reference to Examples.
It is not limited to this. Example 1 Medium composition Refined palm oil 6.0wt% NH 3 Cl 3.0 (g/) KH 2 O 4 0.5 (g/) MgSO 4・7H 2 O 0.5 (g/) F 4 SO 4・7H 2 O 5.0 (mg /) MnSO 4・7H 2 O 0.1 (mg/) ZnSO 4・nH 2 O 0.1 (mg/) CuSO 4・5H 2 O 5 (μg/) Biotin 100 (μg/) Thiamin/hydrochloride 100 (μg/) Yeast extract 1.0 (g/) PH 5.0 As a seed culture, 30 ml of the culture solution with the above composition was dispensed into each of five 500 ml Sakaguchi flasks, then sterilized at 115°C for 10 minutes and allowed to cool to about 35°C. rear,
Candida tropicalis
tropicalis) (IFO−0589), Candida intermedia (IFO−
0761), Candida brumptii (IFO−0744), Candida guilliermondii
(IFO-0838) and Debaryomyces hansenii (IFO-0019) were transplanted in three platinum loops each. The culture conditions were a temperature of 35° C., a shaking frequency of 120 cycles/min, and a shaking width of 7 cm. The culture time is 3 days, but after confirming the growth of yeast approximately 20 hours after the start of culture, to adjust the pH, separately sterilized CaCO 3 was added to the culture solution at 5 wt/vol%, and culture was continued. This was used as a seed culture solution. Add 30 ml of a medium with the same composition as the seed medium to the production culture.
Pour into five 500ml Sakaguchi flasks, heat sterilize at 115℃ for 10 minutes, cool to 35℃, and add the above seed culture solution.
1.5 ml (5 vol%) was inoculated each. This is 120
The cells were cultured for 7 days under the conditions of reciprocation/min, shaking width of 7 cm, and 35°C. Note that 5 wt% of separately sterilized CaCO 3 was added to the culture solution for PH adjustment 15 hours after the start of culture. After the cultivation was completed, the culture was adjusted to pH 2.5 with hydrochloric acid, and diatomaceous earth was used as a support agent to suction it, and solid materials, mainly yeast, were washed away with a small amount of water.
Next, the liquid and the washing liquid were combined, and the combined liquid was neutralized with caustic soda and then heated to precipitate out, which was cooled and filtered by suction to obtain calcium citrate. This calcium citrate was suspended in about 10 times the amount of water, and a 50% aqueous sulfuric acid solution was added dropwise with stirring until the solution showed a slight presence of sulfate groups due to the barium chloride solution, and then boiled. About 30 underwater
Heat for a minute. If necessary, this is subjected to a decoloring operation, and then heated, and the liquid is concentrated under reduced pressure at 50 to 60°C. If gypsum precipitates are deposited during the process, they are separated, and the concentration is continued. It will turn into a slightly thin syrup. When this syrupy concentrate is left at sub-zero temperatures, citric acid crystals will precipitate. The amount of citric acid produced per fermentation liquid (g/) is as follows. Candida tropicalis
tropicalis) 52.1 Candida intermedia (Candida
intermedia) 30.4 Candida Burumptei (Candida
brumptii) 34.5 Candida gear Monday (Candida
guilliermondii) 18.9 Debaryomyces hanzenii (Debaryomyces
hansenii) 15.0 Example 2 The same method as in Example 1 was used, but the carbon source was various palm oils, and the bacterial species used was Candida tropicalis (IFO-0589).
It was hot. The results are shown in Table 1.

【表】 実施例 3 内容3のジヤー・フアーメンターを用いて実
験を行なつた。炭素源は精製パーム油で、培地へ
の添加量は10wt%であつた。培地組成は実施例
1と同様であつた。使用した酵母はキヤンデイ
ダ・トロピカリス(Candida tropicalis)(IFO
−0589)であり、あらかじめ実施例1で種培養し
ておいたものを該培地に5vol%加えた。 発酵条件は、培地仕込量1.5、温度35℃、撹
拌数1000r.p.m.、空気供給速度1V/V.min.、発
酵時間96Hrs.であつた。発酵中PHは10N水酸化ナ
トリウム水溶液を自動的に供給することにより
5.0に維持した。得られたクエン酸生成濃度は
78.7g/であつた。なお、種培養は実施例1と
同様に行ない、その培養時間は60時間であつた。
[Table] Example 3 An experiment was conducted using the jar fermenter of Content 3. The carbon source was refined palm oil, and the amount added to the medium was 10 wt%. The medium composition was the same as in Example 1. The yeast used was Candida tropicalis (IFO
-0589), and 5 vol% of the seed cultured in Example 1 was added to the medium. The fermentation conditions were: medium charge amount 1.5, temperature 35° C., stirring number 1000 rpm, air supply rate 1 V/V min., and fermentation time 96 Hrs. During fermentation, pH is controlled by automatically supplying 10N sodium hydroxide aqueous solution.
I kept it at 5.0. The obtained citric acid production concentration is
It was 78.7g/. The seed culture was performed in the same manner as in Example 1, and the culture time was 60 hours.

Claims (1)

【特許請求の範囲】 1 炭素源としてパーム油を含む培地に、キヤン
デイダ属(Candida)またはデバリオミセス属
(Debaryomyces)のいずれかに属し、パーム油
を資化し得る酵母からえらばれた1種または2種
以上の酵母を好気的に培養し、該培養液中にクエ
ン酸を高濃度で蓄積させ、これを採取することを
特徴とする発酵法によるクエン酸の製法。 2 パーム油が粗パーム油、精製パーム油、パー
ムオレイン、パームステアリンの単独または混合
物である請求項第1項のクエン酸の製法。 3 キヤンデイダ属の酵母がキヤンデイダ・トロ
ピカリス(Candida tropicalis)、キヤンデイ
ダ・インターメデイア(Candida intermedia)、
キヤンデイダ・ブルムプテイ(Candida
brumptii)、キヤンデイダ・ギヤマンデイー
(Candida guilliermondii)であり、デバリオミ
セス属の酵母がデバリオミセス・ハンゼニー
(Debaryomyces hansenii)である請求項第1項
のクエン酸の製法。
[Scope of Claims] 1. In a medium containing palm oil as a carbon source, one or two selected yeasts belonging to the genus Candida or the genus Debaryomyces and capable of assimilating palm oil are added. A method for producing citric acid by a fermentation method, which comprises aerobically cultivating the above yeast, accumulating citric acid at a high concentration in the culture solution, and collecting the citric acid. 2. The method for producing citric acid according to claim 1, wherein the palm oil is one or a mixture of crude palm oil, refined palm oil, palm olein, and palm stearin. 3 Yeasts of the genus Candida are Candida tropicalis, Candida intermedia,
Candida Brumputei
brumptii), Candida guilliermondii, and the yeast belonging to the genus Debaryomyces is Debaryomyces hansenii.
JP12968883A 1983-07-16 1983-07-16 Preparation of citric acid by fermentation Granted JPS6024191A (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
JP12968883A JPS6024191A (en) 1983-07-16 1983-07-16 Preparation of citric acid by fermentation
GB08417854A GB2143527A (en) 1983-07-16 1984-07-13 Process for manufacturing citric acid by fermentation

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP12968883A JPS6024191A (en) 1983-07-16 1983-07-16 Preparation of citric acid by fermentation

Publications (2)

Publication Number Publication Date
JPS6024191A JPS6024191A (en) 1985-02-06
JPH047194B2 true JPH047194B2 (en) 1992-02-10

Family

ID=15015724

Family Applications (1)

Application Number Title Priority Date Filing Date
JP12968883A Granted JPS6024191A (en) 1983-07-16 1983-07-16 Preparation of citric acid by fermentation

Country Status (2)

Country Link
JP (1) JPS6024191A (en)
GB (1) GB2143527A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102249897A (en) * 2011-05-10 2011-11-23 安徽丰原生物化学股份有限公司 Processing method of citric acid mother solution

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5025789A (en) * 1973-07-18 1975-03-18
JPS568595A (en) * 1979-07-03 1981-01-28 Tokyo Shibaura Electric Co Control rod assembly

Also Published As

Publication number Publication date
GB2143527A (en) 1985-02-13
GB8417854D0 (en) 1984-08-15
JPS6024191A (en) 1985-02-06

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