[go: up one dir, main page]

JP2019050731A - Method for promoting growth of organisms performing oxygen-generating photosynthesis - Google Patents

Method for promoting growth of organisms performing oxygen-generating photosynthesis Download PDF

Info

Publication number
JP2019050731A
JP2019050731A JP2016006440A JP2016006440A JP2019050731A JP 2019050731 A JP2019050731 A JP 2019050731A JP 2016006440 A JP2016006440 A JP 2016006440A JP 2016006440 A JP2016006440 A JP 2016006440A JP 2019050731 A JP2019050731 A JP 2019050731A
Authority
JP
Japan
Prior art keywords
medium
culture
growth
photosynthesis
microalgae
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
JP2016006440A
Other languages
Japanese (ja)
Inventor
啓二 木寺
Keiji Kidera
啓二 木寺
史樹 谷口
Fumiki Taniguchi
史樹 谷口
敦弘 東島
Atsuhiro Tojima
敦弘 東島
利明 中
Toshiaki Naka
利明 中
裕文 福留
Hirofumi Fukudome
裕文 福留
港 脇坂
Minato Wakizaka
港 脇坂
礼次郎 野上
Reijiro NOGAMI
礼次郎 野上
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.)
SIXONPOWER CO Ltd
Kyushu Institute of Technology NUC
Mishima Kosan Co Ltd
Original Assignee
SIXONPOWER CO Ltd
Kyushu Institute of Technology NUC
Mishima Kosan Co Ltd
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 SIXONPOWER CO Ltd, Kyushu Institute of Technology NUC, Mishima Kosan Co Ltd filed Critical SIXONPOWER CO Ltd
Priority to JP2016006440A priority Critical patent/JP2019050731A/en
Priority to PCT/JP2016/058004 priority patent/WO2017122368A1/en
Publication of JP2019050731A publication Critical patent/JP2019050731A/en
Pending legal-status Critical Current

Links

Images

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
    • C12N1/00Microorganisms, e.g. protozoa; Compositions thereof; Processes of propagating, maintaining or preserving microorganisms or compositions thereof; Processes of preparing or isolating a composition containing a microorganism; Culture media therefor
    • C12N1/12Unicellular algae; Culture media therefor

Landscapes

  • Engineering & Computer Science (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Biotechnology (AREA)
  • Chemical & Material Sciences (AREA)
  • Bioinformatics & Cheminformatics (AREA)
  • Zoology (AREA)
  • Organic Chemistry (AREA)
  • Wood Science & Technology (AREA)
  • Genetics & Genomics (AREA)
  • Botany (AREA)
  • Biomedical Technology (AREA)
  • Virology (AREA)
  • Microbiology (AREA)
  • Tropical Medicine & Parasitology (AREA)
  • Cell Biology (AREA)
  • Biochemistry (AREA)
  • General Engineering & Computer Science (AREA)
  • General Health & Medical Sciences (AREA)
  • Medicinal Chemistry (AREA)
  • Micro-Organisms Or Cultivation Processes Thereof (AREA)

Abstract

To provide a method for promoting growth of organisms performing oxygen-generating photosynthesis, by an inexpensive, safe and easy process.SOLUTION: A culture promoter containing a pyrrole compound is added to a culture medium where organisms performing oxygen-generating photosynthesis are grown, and the culture medium is held in organism growth conditions. Here, the pyrrole compound preferably contains a tetrapyrrole compound, and as the organisms performing oxygen-generating photosynthesis, algae can be used.SELECTED DRAWING: None

Description

本発明は、酸素発生型光合成を行う生物の増殖促進方法に関する。 The present invention relates to a method for promoting the growth of an organism that performs oxygen-generating photosynthesis.

酸素発生型光合成を行う生物から、コケ植物、シダ植物、及び種子植物を除いたもの(従って、水中に存在する酸素発生型光合成を行う生物)を藻類といい、その中で顕微鏡サイズ(ミクロン単位の大きさ)の藻類は微細藻類と呼ばれ、約10万種が多様な環境中に生息している。近年、微細藻類は、光合成による二酸化炭素固定能力が高いこと、食品、医薬品、更にバイオ燃料等の原料となる有用物質(例えば、脂質)の生産能力が高いこと、通年での収穫が可能であること等の理由から、バイオマス資源として注目されている。 An organism that performs oxygen-generating photosynthesis excluding moss, fern, and seed plants (thus, an organism that performs oxygen-generating photosynthesis that exists in water) is called an algae, and it has a microscopic size (micron unit). Algae are called microalgae, and about 100,000 species live in diverse environments. In recent years, microalgae have a high ability to fix carbon dioxide by photosynthesis, a high ability to produce useful substances (eg, lipids) as raw materials for foods, pharmaceuticals, and biofuels, and can be harvested throughout the year. For these reasons, it is attracting attention as a biomass resource.

ここで、微細藻類による有用物質の生産量は、個々の微細藻類に含まれる有用物質の含有量と微細藻類の個体数との積に比例する。しかしながら、自然条件下では微細藻類の増殖速度は遅く、有用物質の生産効率も低いという問題がある。このため、微細藻類による有用物質生産の実用化(商業ベースで利用)に向けては、微細藻類による有用物質の生産効率向上と微細藻類の増殖速度向上(大量培養)を人工的に図る必要があり、特に微細藻類の大量培養の効率化(即ち、培養工程の経済性改善)が大きな課題となっている。 Here, the production amount of useful substances by microalgae is proportional to the product of the content of useful substances contained in each microalgae and the number of individuals of microalgae. However, there are problems that the growth rate of microalgae is slow under natural conditions and the production efficiency of useful substances is low. For this reason, it is necessary to artificially improve the production efficiency of useful substances using microalgae and the growth rate of microalgae (mass culture) for the practical use (use on a commercial basis) of the production of useful substances using microalgae. In particular, increasing the efficiency of mass culture of microalgae (that is, improving the economic efficiency of the culture process) is a major issue.

微細藻類の大量培養による有用物質生産の実用化に向けては、微細藻類のスクリーニングや微細藻類の遺伝子組換え等の様々な取り組みが国内外において報告されている。しかしながら、スクリーニングにより増殖速度の大きな微細藻類の有望種を選抜するには長い時間と多くの費用を要するという問題がある。一方、遺伝子組換え株を屋外で培養する場合は種々の制約が伴うと共に、遺伝子組換え株が培養地外に飛散した際の環境に及ぼす影響には不明な点が多いという問題がある。
そこで、有用物質の生産効率が高いと期待されている微細藻類を用いて、その培地に増殖を促進する化学物質を添加して微細藻類を大量培養して、有用物質生産の実用化を図ることが提案されている(例えば、非特許文献1〜3参照)。
Various approaches such as screening of microalgae and genetic recombination of microalgae have been reported in Japan and overseas for the practical application of the production of useful substances by mass culture of microalgae. However, there is a problem that it takes a long time and a lot of money to select promising species of microalgae having a high growth rate by screening. On the other hand, when a genetically modified strain is cultured outdoors, there are various limitations, and there are many unclear points regarding the influence on the environment when the genetically modified strain is scattered outside the culture site.
Therefore, using microalgae that are expected to have high production efficiency of useful substances, add chemical substances that promote growth to the culture medium, and cultivate microalgae in large quantities to achieve practical production of useful substances. Has been proposed (see, for example, Non-Patent Documents 1 to 3).

野上礼次郎、脇坂港、「アルギン酸オリゴマーの添加によるスピルリナの増殖促進」、第17回マリンバイオテクノロジー学会大会講演要旨集、2015年5月30日、p.109Reijiro Nogami, Minato Wakisaka, “Promotion of Spirulina Growth by Addition of Alginate Oligomer”, 17th Annual Meeting of the Marine Biotechnology Society, May 30, 2015, p. 109 野上礼次郎、脇坂港、「アルギン酸オリゴマーの添加によるユーグレナの増殖促進」、第16回マリンバイオテクノロジー学会大会講演要旨集、2014年5月31日、p.61Reijiro Nogami, Minato Wakisaka, “Promoting Euglena Growth by Addition of Alginate Oligomers”, Abstracts of the 16th Annual Meeting of the Marine Biotechnology Society, May 31, 2014, p. 61 野上礼次郎、脇坂港、CHE MAAIL Che Mohd Hakiman「アルギン酸オリゴマーの添加によるボトリオコッカスの増殖促進」、2014年生態工学会年次大会発表論文集、p.83−84Reijiro Nogami, Minato Wakisaka, CHE MAAIL Che Mohd Hakiman “Promoting Botryococcus Growth by Addition of Alginate Oligomers”, Proceedings of Annual Conference of Ecological Engineering Society 2014, p. 83-84

微細藻類の大量培養により有用物質生産の実用化を図るには、微細藻類の増殖率を、現状の増殖率に対して少なくとも2〜3倍に向上させる必要があるとされており、非特許文献1〜3に記載された方法では、微細藻類の増殖を更に向上させるには至っていない。このため、微細藻類の増殖速度を高位に維持し安定して培養できる培養条件が見出された際に、微細藻類の増殖速度を更に促進する作用を示す安価で安全(環境に及ぶす影響がなく)、かつ使用方法が簡便となる新たな化学物質が求められている。 In order to commercialize useful substances by mass cultivation of microalgae, it is said that the growth rate of microalgae needs to be improved at least 2 to 3 times the current growth rate. The methods described in 1 to 3 have not led to further improvement of the growth of microalgae. For this reason, when culture conditions that can maintain a high growth rate of microalgae and can be stably cultured have been found, an inexpensive and safe effect that further promotes the growth rate of microalgae (impact on the environment is affected). There is a need for new chemical substances that are easy to use.

本発明はかかる事情に鑑みてなされたもので、安価、安全かつ簡便な手法により達成することが可能な酸素発生型光合成を行う生物の増殖促進方法を提供することを目的とする。 The present invention has been made in view of such circumstances, and an object of the present invention is to provide a method for promoting the growth of a living body that performs oxygen-generating photosynthesis that can be achieved by an inexpensive, safe and simple technique.

本発明者らは、酸素発生型光合成を担う葉緑素クロロフィルは、分子式CNの五員環構造(ピロール環構造)4個が炭素原子を1個ずつ挟んで結合したテトラピロール環構造の一つであるクロリン環を有する化合物であるため、葉緑素クロロフィルの原料となるピロール化合物を含む培地で微細藻類を培養すれば、光合成が促進されることによって微細藻類の増殖も促進されるとの仮設に基づき種々研究を重ねた結果、WO2009/069806号公報に記載の大腸菌によるバイオ生産で得られたテトラピロール化合物を含むピロール化合物を微細藻類の培地に加えることにより、微細藻類の増殖の促進を安価、安全かつ簡便な手法により達成できることを見出し、本発明を完成するに至った。
即ち、本発明に係る酸素発生型光合成を行う生物の増殖促進方法は、ピロール化合物を含む培養促進剤を、酸素発生型光合成を行う生物が生育する培地に添加し、該培地を前記生物の増殖条件に保持することにより行っている。
The present inventors have found that chlorophyll chlorophyll responsible for oxygen-generating photosynthesis has a tetrapyrrole ring structure in which four five-membered ring structures (pyrrole ring structures) of the molecular formula C 4 H 5 N are bonded with one carbon atom in between. Since it is a compound having one chlorin ring, it is hypothesized that if microalgae are cultured in a medium containing a pyrrole compound as a raw material for chlorophyll chlorophyll, photosynthesis is promoted to promote microalgae growth. As a result of various studies based on the above, as a result of adding a pyrrole compound containing a tetrapyrrole compound obtained by bioproduction by Escherichia coli described in WO2009 / 069806 to a microalgae culture medium, the promotion of microalgae growth is inexpensive. The inventors have found that this can be achieved by a safe and simple technique and have completed the present invention.
That is, in the method for promoting the growth of a living organism that performs oxygen-generating photosynthesis according to the present invention, a culture promoter containing a pyrrole compound is added to a medium in which a living organism that performs oxygen-generating photosynthesis grows, and the medium is propagated. This is done by maintaining the conditions.

本発明に係る酸素発生型光合成を行う生物の増殖促進方法においては、培養促進剤に含まれるピロール化合物は、葉緑素クロロフィルのクロリン環の構造の一部であるため安全である(自然界に存在している物質であるため、環境に与える影響はない)。そして、培養促進剤を酸素発生型光合成を行う生物の培地に添加し、培養促進剤が添加された培地を酸素発生型光合成を行う生物の増殖条件下に保持するだけなので、簡便な手法により酸素発生型光合成を行う生物の増殖を行うことができる。その結果、酸素発生型光合成を行う生物の大量増殖を、安価、安全かつ簡便な方法で行うことが可能になる。 In the method for promoting the growth of an organism that performs oxygen-generating photosynthesis according to the present invention, the pyrrole compound contained in the culture promoter is safe because it is part of the structure of the chlorolin ring of chlorophyll chlorophyll (it exists in nature). This has no impact on the environment. Then, the culture promoter is simply added to the culture medium of the organism that performs oxygen-generating photosynthesis, and the culture medium to which the culture promoter is added is kept under the growth conditions of the organism that performs oxygen-generated photosynthesis. Growth of organisms that perform developmental photosynthesis can be performed. As a result, it is possible to carry out mass growth of organisms that perform oxygen-generating photosynthesis by an inexpensive, safe and simple method.

実施例1におけるユーグレナの培養結果の説明図である。It is explanatory drawing of the culture result of Euglena in Example 1. 実施例2におけるボトリオコッカスの培養結果の説明図である。It is explanatory drawing of the culture result of Botryococcus in Example 2. 実施例3におけるスピルリナの培養結果の説明図である。It is explanatory drawing of the culture result of Spirulina in Example 3.

本発明の一実施の形態に係る酸素発生型光合成を行う生物の増殖促進方法は、例えば、遺伝子ypjD(b2611)が変異により発現できなくなった大腸菌によるバイオ生産で得られたピロール化合物を、酸素発生型光合成を行う生物の一例である微細藻類が生育する培地に添加し、培地を微細藻類の増殖条件に保持する。
なお、大腸菌によるバイオ生産ではピロール化合物が安価かつ大量に得られるので、培養促進剤を安価に製造することが可能になる。
The method for promoting the growth of a living organism that performs oxygen-generating photosynthesis according to an embodiment of the present invention includes, for example, using a pyrrole compound obtained by bioproduction using Escherichia coli in which the gene ypjD (b2611) cannot be expressed due to a mutation, It is added to a medium in which microalgae, which are examples of organisms that perform type photosynthesis, grow, and the medium is maintained under the microalgae growth conditions.
In addition, since the pyrrole compound can be obtained in a large amount at a low cost in the bioproduction using Escherichia coli, the culture promoter can be produced at a low cost.

本発明の方法で培養される微細藻類は、酸素発生型光合成を行い、主要な光合成色素としてクロロフィルを含有するものが好ましく、例えば、原核生物であるラン藻類、真核生物のスーパーグループにおける灰色植物、緑色植物、クリプト藻類、不等毛植物、ハプト藻類、渦鞭毛藻類、ユーグレナ藻類、クロララクニオン藻類、クロメラ藻類等が挙げられる。
また、微細藻類の増殖条件とは、微細藻類毎に従来から推奨されている一般的な増殖条件(増殖速度を高位に維持し安定して培養できる条件)であればよい。
The microalgae cultured by the method of the present invention preferably carry out oxygen-generating photosynthesis and preferably contain chlorophyll as a main photosynthesis pigment. For example, prokaryotic cyanobacteria, gray plants in eukaryotic supergroups , Green plants, crypto algae, unequal hairy plants, hapto algae, dinoflagellates, euglena algae, chloracarnion algae, chromella algae and the like.
The growth conditions for microalgae may be general growth conditions that have been conventionally recommended for each microalgae (conditions that allow stable growth while maintaining a high growth rate).

大腸菌は貧栄養培地中で培養する。このとき、大腸菌を貧栄養培地以外の適当な培地、例えば、LB培地等の培地中で前培養し(15〜40℃の温度で6〜24時間培養した後)、得られた前培養物を貧栄養培地に接種して本培養(20℃〜40℃の温度で12時間〜96時間かけて培養)することが好ましい。大腸菌の培養条件は、大腸菌に対する一般的な条件であればよい。
なお、貧栄養培地として、例えば、脱イオン水1リットル中に、KHPOを9g、KHPOを21g、(NHSOを2g、クエン酸二水和物を1g、グルコースを3.6g、及びMgSOを100mg溶解させた水溶液を使用することができる。
E. coli is cultured in an oligotrophic medium. At this time, Escherichia coli is precultured in a suitable medium other than the oligotrophic medium, for example, a medium such as LB medium (after culturing at a temperature of 15 to 40 ° C. for 6 to 24 hours), and the obtained preculture is obtained. It is preferable to inoculate an oligotrophic medium and perform main culture (culture at a temperature of 20 ° C. to 40 ° C. for 12 hours to 96 hours). The culture conditions for E. coli may be general conditions for E. coli.
Incidentally, as a poor nutrient medium, e.g., deionized water in 1 liter, a KH 2 PO 4 9g, K 2 HPO 4 to 21g, 2 g of (NH 4) 2 SO 4, citric acid dihydrate 1g, An aqueous solution in which 3.6 g of glucose and 100 mg of MgSO 4 are dissolved can be used.

大腸菌の培養中に、大腸菌からはテトラピロール化合物、テトラピロール化合物前駆体等のピロール化合物(培養物)が菌体外に排出され、排出されたピロール化合物は貧栄養培地中に混入する。このため、大腸菌の培養が終了した貧栄養培地を遠心分離機にかけて懸濁物(大腸菌細胞の凝集体)を沈殿させ、得られた上澄液をフィルター(ポアサイズ0.22μm)で濾過することにより、大腸菌が除去された状態のピロール化合物を含む培養促進剤を得ることができる。
なお、培養促進剤中の水分量を調整することにより、培養促進剤中のピロール化合物の濃度を任意の値に調整することができる。これにより、培地に培養促進剤を添加した際における培地中のピロール化合物の含有量(より詳細には、ピロール化合物を含む窒素化合物の含有量)の調整が容易にできる。
During the cultivation of E. coli, pyrrole compounds (cultured products) such as tetrapyrrole compounds and tetrapyrrole compound precursors are discharged out of the cells from the E. coli, and the discharged pyrrole compounds are mixed in the poor nutrient medium. For this reason, the oligotrophic medium after the cultivation of E. coli is centrifuged to precipitate the suspension (aggregates of E. coli cells), and the resulting supernatant is filtered through a filter (pore size 0.22 μm). A culture promoter containing a pyrrole compound from which E. coli has been removed can be obtained.
In addition, the density | concentration of the pyrrole compound in a culture promotion agent can be adjusted to arbitrary values by adjusting the moisture content in a culture promotion agent. Thereby, the content of the pyrrole compound in the culture medium (more specifically, the content of the nitrogen compound containing the pyrrole compound) when the culture promoter is added to the culture medium can be easily adjusted.

(実施例1)
ユーグレナ(NIES−48株)の培養を行った。培養は、30ミリリットルのスクリューキャップ試験管内に注入した10ミリリットルの培地に一定重量のユーグレナを加え、スクリューキャップ試験管をインキュベーター庫内に静置し、空気を通気しながら温度を22〜26℃、白色蛍光灯を用いて照度を6000〜6500Lux、白色蛍光灯の点灯時間と消灯時間をそれぞれ12時間とする明暗サイクルの条件下で、35日間行った。なお、スクリューキャップ試験管は、1日おきに振盪させた。
Example 1
Euglena (NIES-48 strain) was cultured. For cultivation, add Euglena with a constant weight to 10 ml of medium injected into a 30 ml screw cap test tube, leave the screw cap test tube in an incubator, and adjust the temperature to 22 to 26 ° C. while ventilating air. The test was carried out for 35 days under conditions of a light-dark cycle using a white fluorescent lamp with an illuminance of 6000 to 6500 Lux, and a white fluorescent lamp having a turn-on time and a turn-off time of 12 hours, respectively. The screw cap test tube was shaken every other day.

培地は、A1(AF−6培地が10ミリリットル)、A2(AF−6培地9ミリリットルと培養促進剤1ミリリットルの混合物)、A3(AF−6培地5ミリリットルと培養促進剤5ミリリットルの混合物)、及びA4(培養促進剤10ミリリットル)の4種類である。なお、AF−6培地1リットル当たりの組成は、NaNOが140mg、NHNOが22mg、MgSO・7HOが30mg、KHPOが10mg、KHPOが5mg、CaCl・2HOが10mg、Fe−citrateが2mg、Citric acidが2mg、Biotinが2μg、Thiamine HClが2μg、VitaminBが10μg、VitaminB12が1μg、NaEDTA・2HOが5mg、FeCl・6HOが0.98mg、MnCl・4HOが180μg、ZnClが52μg、CoCl・6HOが20μg、NaMoO・2HOが12.5μg、Distilled Waterが1リットルである。また、培養促進剤中のピロール化合物を含む窒素化合物の含有量は560mg/リットルであり、その中にはポルフィリン環構造を持つピロール化合物16mg/リットルも含まれる。 Medium is A1 (10 ml of AF-6 medium), A2 (mixture of 9 ml of AF-6 medium and 1 ml of culture accelerator), A3 (mixture of 5 ml of AF-6 medium and 5 ml of culture accelerator), And A4 (10 ml of culture accelerator). The composition per liter of AF-6 medium is as follows: NaNO 3 is 140 mg, NH 4 NO 3 is 22 mg, MgSO 4 .7H 2 O is 30 mg, KH 2 PO 4 is 10 mg, K 2 HPO 4 is 5 mg, CaCl 2 2H 2 O 10 mg, Fe-citrate 2 mg, Citric acid 2 mg, Biotin 2 μg, Thiamine HCl 2 μg, Vitamin B 6 10 μg, Vitamin B 12 1 μg, Na 2 EDTA · 2H 2 O 5 mg, FeCl 6 0.98 mg 6H 2 O, 180 μg MnCl 2 .4H 2 O, 52 μg ZnCl 2 , 20 μg CoCl 2 .6H 2 O, 12.5 μg Na 2 MoO 4 .2H 2 O, 1 liter Distilled Water is there. In addition, the content of the nitrogen compound including the pyrrole compound in the culture promoter is 560 mg / liter, which includes pyrrole compound having a porphyrin ring structure of 16 mg / liter.

培養が終了したA1〜A4からそれぞれ5ミリリットルの細胞懸濁液をスウィネスフィルターホルダーに挿入したφ25のGF/Cフィルターを用いて濾過し、濾過後にGF/Cフィルターから取り出した使用済み濾紙をシャーレ内に入れて、105℃の乾燥庫で5時間乾燥させた。乾燥後、使用済み濾紙を収容したシャーレをデシケータ内に移して冷却し、冷却後に使用済み濾紙を収容したシャーレの重量を測定した。そして、使用済み濾紙を収容したシャーレの重量から、予め求めておいた濾紙乾燥重量とシャーレ乾燥重量を差し引くことにより、5ミリリットルの細胞懸濁液中に存在していたユーグレナの乾燥重量を算出した。図1に、A1〜A4より採取した5ミリリットルの細胞懸濁液中にそれぞれ含まれていたユーグレナの乾燥重量を示す。 5 ml of each cell suspension from A1 to A4 after culturing was filtered using a φ25 GF / C filter inserted in a Sweeness filter holder, and the used filter paper taken out from the GF / C filter after filtration was removed from the petri dish. It was put in and it was made to dry for 5 hours with a 105 degreeC drying cabinet. After drying, the petri dish containing the used filter paper was transferred into a desiccator and cooled, and the weight of the petri dish containing the used filter paper after cooling was measured. Then, the dry weight of Euglena present in the 5 ml cell suspension was calculated by subtracting the dry weight of the filter paper and the dry weight of the petri dish previously obtained from the weight of the petri dish containing the used filter paper. . FIG. 1 shows the dry weight of Euglena contained in each 5 ml cell suspension collected from A1 to A4.

図1に示すように、A1(AF−6培地のみ)で増殖させる場合の増殖速度に対して、培養促進剤を添加したすべての培地A2〜A4では大きな増殖速度を示すことが確認でき、培養促進剤を10倍希釈した培地(A2)では2倍、培養促進剤を2倍希釈した培地(A3)では7.7倍、培養促進剤のみの培地(A4)では6.7倍となった。
また、図1は、ユーグレナの増殖速度を増大させる培地中に含まれる培養促進剤の希釈率(ピロール化合物を含む窒素化合物の含有量)には最適値が存在することを示しており、ピロール化合物を含む窒素化合物を過剰に添加することは、培養促進剤のコスト増加につながり好ましくない。
As shown in FIG. 1, it can be confirmed that all the media A2 to A4 to which a culture accelerator is added show a large growth rate compared to the growth rate when growing on A1 (AF-6 medium only). In the medium (A2) diluted 10-fold with the promoter, it was doubled, in the medium (A3) diluted twice with the culture promoter, it was 7.7 times, and in the medium (A4) with only the culture promoter, it was 6.7 times. .
In addition, FIG. 1 shows that there is an optimum value for the dilution rate of the culture promoter contained in the medium that increases the growth rate of Euglena (content of nitrogen compound including pyrrole compound). It is not preferable to add an excessive amount of the nitrogen compound containing, which leads to an increase in the cost of the culture promoter.

(実施例2)
ボトリオコッカス(NIES−2199株)の培養を行った。培養は、30ミリリットルのスクリューキャップ試験管内に注入した10ミリリットルの培地に一定重量のボトリオコッカスを加え、スクリューキャップ試験管をインキュベーター庫内に静置し、空気を通気しながら温度を22〜26℃、白色蛍光灯を用いて照度を6000〜6500Lux、白色蛍光灯の点灯時間と消灯時間をそれぞれ12時間とする明暗サイクルの条件下で、65日間行った。なお、スクリューキャップ試験管は、1日おきに振盪させた。
(Example 2)
Botryococcus (NIES-2199 strain) was cultured. For cultivation, a certain weight of Botryococcus was added to 10 ml of medium injected into a 30 ml screw cap test tube, the screw cap test tube was left still in an incubator, and the temperature was adjusted to 22 to 26 while ventilating air. It was performed for 65 days under the conditions of a light-dark cycle in which the illuminance was 6000 to 6500 Lux using a white fluorescent lamp and the lighting time and extinguishing time of the white fluorescent lamp were 12 hours each. The screw cap test tube was shaken every other day.

培地は、B1(BG11培地が10ミリリットル)、B3(BG11培5ミリリットルと培養促進剤5ミリリットルの混合物)、及びB4(培養促進剤10ミリリットル)の4種類である。なお、BG11培地1リットル当たりの組成は、NaNOが1500mg、KHPO・3HOが40mg、MgSO・7HOが75mg、CaCl・2HOが36mg、Ferric ammonium citrateが6mg、Citric acidが6mg、NaEDTA−Mgが1mg、NaCOが20mg、HBOが2.86mg、MnCl・4HOが1.81mg、ZnSO・7HOが0.222mg、NaMoO・2HOが0.39mg、CuSO・5HOが79μg、Co(NO)・6HOが49μg、Distilled Waterが1リットルである。また、培養促進剤中のピロール化合物を含む窒素化合物の含有量は560mg/リットルであり、その中にはポルフィリン環構造を持つピロール化合物16mg/リットルも含まれる。 There are four types of culture media: B1 (BG11 medium is 10 ml), B3 (5 ml of BG11 medium and 5 ml culture accelerator), and B4 (10 ml culture accelerator). The composition per liter of BG11 medium is 1500 mg NaNO 3 , 40 mg KH 2 PO 4 .3H 2 O, 75 mg MgSO 4 .7H 2 O, 36 mg CaCl 2 .2H 2 O, and 6 mg Ferric ammonium citrate. , Citric acid 6 mg, Na 2 EDTA-Mg 1 mg, Na 2 CO 3 20 mg, H 3 BO 3 2.86 mg, MnCl 2 .4H 2 O 1.81 mg, ZnSO 4 .7H 2 O 0. 222 mg, Na 2 MoO 4 .2H 2 O is 0.39 mg, CuSO 4 .5H 2 O is 79 μg, Co (NO 3 ) 2 .6H 2 O is 49 μg, and Distilled Water is 1 liter. In addition, the content of the nitrogen compound including the pyrrole compound in the culture promoter is 560 mg / liter, which includes pyrrole compound having a porphyrin ring structure of 16 mg / liter.

培養が終了したB1、B3、B4からそれぞれ5ミリリットルの細胞懸濁液をスウィネスフィルターホルダーに挿入したφ25のGF/Cフィルターを用いて濾過し、実施例1と同様の方法で、5ミリリットルの細胞懸濁液中に存在していたボトリオコッカスの乾燥重量を算出した。図2に、B1、B3、B4より採取した5ミリリットルの細胞懸濁液中にそれぞれ含まれていたボトリオコッカスの乾燥重量を示す。 5 ml cell suspensions from each of B1, B3, and B4 after culturing were filtered using a φ25 GF / C filter inserted into a Sweeness filter holder, and 5 ml of cell suspension was filtered in the same manner as in Example 1. The dry weight of Botryococcus present in the cell suspension was calculated. FIG. 2 shows the dry weight of Botryococcus contained in 5 ml of cell suspension collected from B1, B3, and B4.

図2に示すように、B1(BG11培地のみ)で増殖させる場合の増殖速度に対して、培養促進剤を添加した培地B3、B4では大きな増殖速度を示すことが確認でき、培養促進剤を2倍希釈した培地(B3)では23倍、培養促進剤のみの培地(B4)では5倍となった。
また、図2は、ボトリオコッカスの増殖速度を増大させる培養促進剤の希釈率(ピロール化合物を含む窒素化合物の含有量)には最適値が存在することを示しており、ピロール化合物を含む窒素化合物を過剰に添加することは、培養促進剤のコスト増加につながり好ましくない。
As shown in FIG. 2, it can be confirmed that the mediums B3 and B4 to which the culture promoter is added have a large growth rate compared to the growth rate in the case of growing on B1 (BG11 medium only). It was 23 times in the medium (B3) diluted twice, and 5 times in the medium (B4) containing only the culture accelerator.
FIG. 2 also shows that there is an optimum value for the dilution ratio of the culture promoter that increases the growth rate of Botryococcus (content of nitrogen compound including pyrrole compound). Adding an excessive amount of the compound is not preferable because it leads to an increase in the cost of the culture promoter.

(実施例3)
スピルリナ(NIES−39株)の培養を行った。培養は、30ミリリットルのスクリューキャップ試験管内に注入した10ミリリットルの培地に一定重量のスピルリナを加え、スクリューキャップ試験管をインキュベーター庫内に静置し、空気を通気しながら温度を22〜26℃、白色蛍光灯を用いて照度を6000〜6500Lux、白色蛍光灯の点灯時間と消灯時間をそれぞれ12時間とする明暗サイクルの条件下で行った。なお、スクリューキャップ試験管は、1日おきに振盪させた。
(Example 3)
Spirulina (NIES-39 strain) was cultured. The culture is performed by adding a constant weight of Spirulina to 10 ml of medium injected into a 30 ml screw cap test tube, leaving the screw cap test tube still in the incubator, and keeping the temperature at 22-26 ° C. while ventilating air. Using a white fluorescent lamp, the illuminance was 6000 to 6500 Lux, and the white fluorescent lamp was turned on and off for 12 hours. The screw cap test tube was shaken every other day.

培地は、S1(SOT培地が10ミリリットル)、S2(SOT培地9ミリリットルと培養促進剤1ミリリットルの混合物)、S3(SOT培地5ミリリットルと培養促進剤5ミリリットルの混合物)、及びS4(培養促進剤10ミリリットル)の4種類である。なお、SOT培地1リットル当たりの組成は、NaHCOが16800mg、KHPOが500mg、NaNOが2500mg、KSOが1000mg、NaClが1000mg、MgSO・7HOが200mg、CaCl・2HOが40mg、FeSO・7HOが10mg、NaEDTA・2HOが80mg、HBOが2.86mg、MnSO・5HOが2.5mg、ZnSO・7HOが0.22mg、CuSO・5HOが80μg、NaMoO・2HOが20μg、Distilled Waterが1リットルである。また、培養促進剤中のピロール化合物を含む窒素化合物の含有量は560mg/リットルであり、その中にはポルフィリン環構造を持つピロール化合物16mg/リットルも含まれる。 Medium is S1 (10 ml of SOT medium), S2 (mixture of 9 ml of SOT medium and 1 ml of culture promoter), S3 (mixture of 5 ml of SOT medium and 5 ml of culture promoter), and S4 (culture promoter) 10 milliliters). The composition per liter of the SOT medium is NaHCO 3 16800 mg, K 2 HPO 3 500 mg, NaNO 3 2500 mg, K 2 SO 4 1000 mg, NaCl 1000 mg, MgSO 4 .7H 2 O 200 mg, CaCl 2 2H 2 O 40 mg, FeSO 4 · 7H 2 O 10 mg, Na 2 EDTA · 2H 2 O 80 mg, H 3 BO 3 2.86 mg, MnSO 4 · 5H 2 O 2.5 mg, ZnSO 4 · 7H 2 O is 0.22 mg, CuSO 4 .5H 2 O is 80 μg, Na 2 MoO 4 .2H 2 O is 20 μg, and Distilled Water is 1 liter. In addition, the content of the nitrogen compound including the pyrrole compound in the culture promoter is 560 mg / liter, which includes pyrrole compound having a porphyrin ring structure of 16 mg / liter.

培養を開始してから14日経過したS1〜S4からそれぞれ5ミリリットルの細胞懸濁液をスウィネスフィルターホルダーに挿入したφ25のGF/Cフィルターを用いて濾過し、実施例1と同様の方法で、5ミリリットルの細胞懸濁液中に存在していたスピルリナの乾燥重量を算出した。図3に、S1〜S4より採取した5ミリリットルの細胞懸濁液中にそれぞれ含まれていたスピルリナの乾燥重量を示す。 After 14 days from the start of culturing, 5 ml of each cell suspension from S1 to S4 was filtered using a φ25 GF / C filter inserted into a Sweeness filter holder, and the same method as in Example 1 was used. The dry weight of Spirulina present in 5 ml of cell suspension was calculated. FIG. 3 shows the dry weight of Spirulina contained in each 5 ml cell suspension collected from S1 to S4.

図3に示すように、S1(SOT培地のみ)で増殖させる場合の増殖速度に対して、
培養促進剤を10倍希釈した培地(S2)では1.04倍、培養促進剤を2倍希釈した培地(S3)では1.7倍となったが、培養促進剤のみの培地(S4)では増殖が見られず、個体数の減少が生じた。
このことから、ピロール化合物を培地に加えてスピルリナの増殖速度を増大させる場合、培養促進剤の希釈率(ピロール化合物を含む窒素化合物の含有量)の最適値はかなり狭い範囲に存在することが分かった。
As shown in FIG. 3, with respect to the growth rate when growing in S1 (SOT medium only),
In the medium (S2) in which the culture promoter was diluted 10-fold, the ratio was 1.04 times, and in the medium (S3) in which the culture accelerator was diluted 2-fold, it was 1.7 times. There was no growth and a decrease in population occurred.
This indicates that when adding pyrrole compounds to the medium to increase the growth rate of spirulina, the optimum value of the dilution ratio of the culture promoter (content of nitrogen compounds including pyrrole compounds) is in a fairly narrow range It was.

以上、本発明を、実施の形態を参照して説明してきたが、本発明は何ら上記した実施の形態に記載した構成に限定されるものではなく、特許請求の範囲に記載されている事項の範囲内で考えられるその他の実施の形態や変形例も含むものである。
例えば、本実施の形態では、ピロール化合物を含む培養促進剤は、大腸菌の培地からの抽出物を用いて作製したが、大腸菌の培養が終了した後の培地から大腸菌を除去した後、水分量を調整することにより作製することもできる。
As described above, the present invention has been described with reference to the embodiment. However, the present invention is not limited to the configuration described in the above-described embodiment, and the matters described in the scope of claims. Other embodiments and modifications conceivable within the scope are also included.
For example, in this embodiment, the culture accelerator containing a pyrrole compound was prepared using an extract from an E. coli medium, but after removing E. coli from the medium after the cultivation of E. coli was completed, the water content was increased. It can also be produced by adjusting.

Claims (4)

ピロール化合物を含む培養促進剤を、酸素発生型光合成を行う生物が生育する培地に添加し、該培地を前記生物の増殖条件に保持することを特徴とする酸素発生型光合成を行う生物の増殖促進方法。 A growth promoter containing a pyrrole compound is added to a medium in which an organism that performs oxygen-generating photosynthesis grows, and the medium is maintained under the growth conditions of the organism, and the growth promotion of an organism that performs oxygen-generating photosynthesis is characterized by Method. 請求項1記載の酸素発生型光合成を行う生物の増殖促進方法において、前記ピロール化合物はテトラピロール化合物を含むことを特徴とする酸素発生型光合成を行う生物の増殖促進方法。 The method for promoting the growth of an organism performing oxygen-generating photosynthesis according to claim 1, wherein the pyrrole compound contains a tetrapyrrole compound. 請求項1又は2記載の酸素発生型光合成を行う生物の増殖促進方法において、前記生物は藻類であることを特徴とする酸素発生型光合成を行う生物の増殖促進方法。 3. The method for promoting the growth of a living organism that performs oxygen-generating photosynthesis according to claim 1, wherein the living organism is an algae. 請求項3記載の酸素発生型光合成を行う生物の増殖促進方法において、前記培地に含まれる前記ピロール化合物を含む窒素化合物の濃度を16〜560ミリグラム/リットルに調整することを特徴とする酸素発生型光合成を行う生物の増殖促進方法。
4. The method for promoting the growth of an organism performing oxygen-generating photosynthesis according to claim 3, wherein the concentration of the nitrogen compound containing the pyrrole compound contained in the medium is adjusted to 16 to 560 milligrams / liter. A method for promoting the growth of organisms that perform photosynthesis.
JP2016006440A 2016-01-15 2016-01-15 Method for promoting growth of organisms performing oxygen-generating photosynthesis Pending JP2019050731A (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
JP2016006440A JP2019050731A (en) 2016-01-15 2016-01-15 Method for promoting growth of organisms performing oxygen-generating photosynthesis
PCT/JP2016/058004 WO2017122368A1 (en) 2016-01-15 2016-03-14 Growth promotion method for oxygen-generating photosynthetic organism

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2016006440A JP2019050731A (en) 2016-01-15 2016-01-15 Method for promoting growth of organisms performing oxygen-generating photosynthesis

Publications (1)

Publication Number Publication Date
JP2019050731A true JP2019050731A (en) 2019-04-04

Family

ID=59311173

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2016006440A Pending JP2019050731A (en) 2016-01-15 2016-01-15 Method for promoting growth of organisms performing oxygen-generating photosynthesis

Country Status (2)

Country Link
JP (1) JP2019050731A (en)
WO (1) WO2017122368A1 (en)

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0556777A (en) * 1991-08-29 1993-03-09 Shiro Nagai Culture of vitamin b12-requiring strain and vitamin b12-requiring strain obtained thereby
DE10046870A1 (en) * 2000-09-20 2002-03-28 Basf Ag Genetic manipulation of corynebacteria, useful for preparing fine chemicals, using a non-replicable vector that is not recognized as foreign
CA2707014A1 (en) * 2007-11-30 2009-06-04 Fukutome, Hirofumi Method for preparing tetrapyrrole compounds
EP2397557A4 (en) * 2009-02-11 2013-09-04 Univ Mie Process for producing a beta-1,3-glucan

Also Published As

Publication number Publication date
WO2017122368A1 (en) 2017-07-20

Similar Documents

Publication Publication Date Title
CN107460215B (en) Method for producing grease by microalgae mixed culture
JPWO2020071444A1 (en) How to cultivate freshwater microalgae
CN101955904B (en) Algicidal bacteria separation method in natural water environment
JP2012239452A5 (en)
CN106754382B (en) A strain of Mutagenic Zhanjiang Isochrysis and its culture method
RU2416634C1 (en) Halobacterium salinarum bacterial strain - bacteriorhodopsin producer
CN104894162B (en) Gene transformation duckweed and the method expressed
CN106916775A (en) Transgenic algae strain of high-yield nano polyphosphoric acids body and preparation method thereof
CN104946536B (en) Culture method of Isochrysis galbana
US20120264195P1 (en) High bio-productivity chlamydomonas strain DG8-108
JP6359314B2 (en) Medium composition for lipid production and method for lipid production for the red alga Cyanidia
KR101797070B1 (en) Culture compositions for promoting growth of spirulina and the method culturing for promoting growth of spirulina by using the same
Sivakumar et al. Influence of carbon-dioxide on the growth of Spirulina sp.(MCRC-A0003) isolated from Muttukadu backwaters, South India
KR101658040B1 (en) Method for microalgae cultivation using nanobubble water
JP2019050731A (en) Method for promoting growth of organisms performing oxygen-generating photosynthesis
CN103881922B (en) A kind of method of utilization microbial flocculant harvesting microalgae
KR20110132368A (en) Mass acquisition and production method of isolated cyanobacterial species producing paralytic algae toxin
CN110305833A (en) A kind of suspension culture method of masson pine embryogenic cell proliferation
Jiang et al. Cultivation of the microalga, Chlorella pyrenoidosa, in biogas wastewater
TW202122570A (en) Novel spirulina platensis strain
CN112358969A (en) Method for promoting bait microalgae propagation
CN104450538B (en) Mould culture medium and cultural method in a kind of Jue Shi plums for circular cone
CN106754381B (en) Mutagenic dinoflagellate Zhanjiang and the like and culture method thereof
RU2829810C1 (en) Planktonic strain of unicellular green algae chlorella vulgaris kd bcf, intended for biomass production
KR20090079026A (en) Cultivation of Microalgae Using Deep Sea Water